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ГОСТ 28656-2019
МКС 75.160.30
Дата введения 2020-01-01
Предисловие
Цели, основные принципы и основной порядок проведения работ по межгосударственной стандартизации установлены в ГОСТ 1.0-2015 "Межгосударственная система стандартизации. Основные положения" и ГОСТ 1.2-2015 "Межгосударственная система стандартизации. Стандарты межгосударственные, правила и рекомендации по межгосударственной стандартизации. Правила разработки, принятия, обновления и отмены"
Сведения о стандарте
1 РАЗРАБОТАН Акционерным обществом "Волжский научно-исследовательский институт углеводородного сырья" (АО "ВНИИУС")
2 ВНЕСЕН Межгосударственным техническим комитетом по стандартизации МТК 52 "Природный и сжиженные газы"
3 ПРИНЯТ Межгосударственным советом по стандартизации, метрологии и сертификации (протокол от 30 января 2019 г. N 115-П)
За принятие проголосовали:
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Краткое наименование страны по МК (ИСО 3166) 004-97
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Код страны по
МК (ИСО 3166) 004-97
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Сокращенное наименование национального органа по стандартизации
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Беларусь
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BY
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Госстандарт Республики Беларусь
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Казахстан
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KZ
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Госстандарт Республики Казахстан
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Киргизия
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KG
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Кыргызстандарт
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Россия
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RU
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Росстандарт
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Украина
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UA
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Минэкономразвития Украины
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4 Приказом Федерального агентства по техническому регулированию и метрологии от 3 апреля 2019 г. N 119-ст межгосударственный стандарт ГОСТ 28656-2019 введен в действие в качестве национального стандарта Российской Федерации с 1 января 2020 г.
5 ВЗАМЕН ГОСТ 28656-90
Информация об изменениях к настоящему стандарту публикуется в ежегодном информационном указателе "Национальные стандарты", а текст изменений и поправок - в ежемесячном информационном указателе "Национальные стандарты". В случае пересмотра (замены) или отмены настоящего стандарта соответствующее уведомление будет опубликовано в ежемесячном информационном указателе "Национальные стандарты". Соответствующая информация, уведомление и тексты размещаются также в информационной системе общего пользования - на официальном сайте Федерального агентства по техническому регулированию и метрологии в сети Интернет (www.gost.ru)
ВНЕСЕНА поправка, опубликованная в ИУС N 10, 2020 год
Поправка внесена изготовителем базы данных
1 Область применения
1.1 Настоящий стандарт распространяется на сжиженные углеводородные газы (далее - СУГ) - пропан, пропен, бутаны, бутены и их смеси, применяемые в качестве моторного топлива для автомобильного транспорта, топлива технологического и коммунально-бытового потребления или сырья для химических процессов, и устанавливает упрощенный метод вычисления плотности и избыточного давления насыщенных паров на основе данных измерения углеводородного состава методом газовой хроматографии.
1.2 Настоящий метод применяют для определения плотности СУГ в диапазоне температур от минус 50°С до плюс 50°С и избыточного давления насыщенных паров СУГ в интервале от 0,06 до 2,0 МПа при температурах минус 35°С, минус 30°С, минус 20°С, плюс 45°С.
1.3 Настоящий стандарт предназначен для вычисления плотности и давления насыщенных паров СУГ, в которых диапазон массовой доли компонентов составляет от 0,005% до 99,80%.
Примечания
1 Расчетный метод определения плотности и давления насыщенных паров может быть применен для широкой фракции легких углеводородов.
2 Значения плотности и давления насыщенных паров СУГ, вычисленные на основе данных компонентного состава, применяют для подтверждения соответствия требованиям документов на продукцию, и используют для проведения учетных (коммерческих) операций.
(Поправка. ИУС N 10-2020).
2 Нормативные ссылки
В настоящем стандарте использованы нормативные ссылки на следующие межгосударственные стандарты:
ГОСТ 10679-2019 Газы углеводородные сжиженные. Метод определения углеводородного состава
ГОСТ 31369-2008 (ИСО 6976:1995) Газ природный. Вычисление теплоты сгорания, плотности, относительной плотности и числа Воббе на основе компонентного состава
ГОСТ 33012-2014 (ISO 7941:1988) Пропан и бутан товарные. Определение углеводородного состава методом газовой хроматографии
Примечание - При пользовании настоящим стандартом целесообразно проверить действие ссылочных стандартов в информационной системе общего пользования - на официальном сайте Федерального агентства по техническому регулированию и метрологии в сети Интернет или по ежегодному информационному указателю "Национальные стандарты", который опубликован по состоянию на 1 января текущего года, и по выпускам ежемесячного информационного указателя "Национальные стандарты" за текущий год. Если ссылочный стандарт заменен (изменен), то при пользовании настоящим стандартом следует руководствоваться заменяющим (измененным) стандартом. Если ссылочный стандарт отменен без замены, то положение, в котором дана ссылка на него, применяется в части, не затрагивающей эту ссылку.
3 Термины и определения
3.1 В настоящем стандарте применены следующие термины с соответствующими определениями:
3.1.1 сжиженные углеводородные газы; СУГ: Смесь углеводородов (пропана, пропилена, бутанов, бутиленов и бутадиенов с присутствием метана, этана, этилена и (или) пентанов и пентенов), преобразованная в жидкое состояние.
3.1.2 плотность сжиженного углеводородного газа: Масса СУГ, заключенная в единице его объема при определенных значениях давления и температуры.
3.1.3 давление насыщенных паров: Давление, при котором жидкость находится в равновесном состоянии со своей газовой фазой; давление насыщенных паров складывается из избыточного давления и атмосферного давления.
3.1.4 абсолютное давление: Истинное давление, отсчитываемое от абсолютного нуля (давление абсолютного вакуума).
3.1.5 избыточное давление: Давление, равное разности между абсолютным и атмосферным давлением.
3.1.6 летучесть (фугитивность): Величина, предназначенная для применения ряда термодинамических соотношений модели идеального газа к поведению реальных смесей в различных фазах, является функцией давления, температуры и концентрации компонентов газовой смеси, выраженная в единицах давления.
3.1.7 идеальный газ: Газ, подчиняющийся законам идеального газа.
3.2 В настоящем стандарте использовано следующее обозначение:
- группа углеводородов с числом атомов углерода от пяти и выше, массовую долю которых рассматривают как один компонент со свойствами н-пентана.
4 Метод определения плотности сжиженных углеводородных газов
4.1 Определение плотности сжиженных углеводородных газов
4.1.1 Значение плотности СУГ , кг/м , вычисляют на основе закона аддитивности по данным измеренного компонентного состава, определенного хроматографическим методом и значениям плотности индивидуальных углеводородов, входящих в состав СУГ, при заданной температуре по формуле
, (1)
где - число компонентов сжиженного газа;
- массовая доля -го компонента, %;
- плотность -го компонента при данной температуре , кг/м .
4.1.2 Если компонентный состав измерен в молярных долях, то плотность вычисляют по формуле
, (2)
где - молярная доля -го компонента, доли единицы.
Компонентный состав определяют по ГОСТ 10679 или ГОСТ 33012.
4.1.3 Плотность индивидуальных углеводородов в жидком состоянии в зависимости от температуры приведена в таблице А.1 (приложение А).
Значения молярных масс индивидуальных компонентов приведены в приложении Б.
4.1.4 Если в таблице А.1 (приложение А) отсутствует значение плотности компонента при конкретной температуре измерений, то ее значение вычисляют интерполированием табличных значений плотностей, соответствующих температурам, ближайшим к данной.
4.1.5 Примеры расчета плотности СУГ приведены в таблицах В.1, В.2 (приложение В).
4.2 Оформление результатов вычисления плотности сжиженных углеводородных газов
4.2.1 За результат вычисления плотности СУГ при данной температуре принимают значение единичного определения.
4.2.2 Результат вычисления плотности СУГ записывают в виде
, (3)
где - расширенная неопределенность результата вычисления плотности для данной температуры , кг/м , при коэффициенте охвата 2, [1]-[3].
вычисляют по таблице 1. Вычисленные значения плотности СУГ и расширенной неопределенности (абсолютной погрешности) округляют до первого десятичного знака.
Таблица 1 - Расширенная неопределенность результатов вычисления плотности сжиженных углеводородных газов
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Диапазон измерений плотности , кг/м
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Расширенная неопределенность , кг/м
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От 480 до 530 включ.
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Св. 530 до 560 включ.
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Св. 560 до 800 включ.
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4.3 Требования к показателям точности метода
Метод обеспечивает получение результатов вычисления плотности СУГ по измеренному компонентному составу со значением расширенной неопределенности , не превышающей значений, приведенных в таблице 1, при доверительной вероятности 0,95.
5 Метод определения давления насыщенных паров
5.1 Давление насыщенных паров СУГ вычисляют по углеводородному составу, определенному методом газовой хроматографии в молярных долях, и значениям летучести углеводородов, входящих в состав СУГ, соответствующим заданной температуре измерений.
Углеводородный состав, определенный в массовых долях, пересчитывают в молярные доли по формуле
, (4)
где - молярная масса -го компонента по таблице Б.1 приложения Б, кг/кмоль.
5.2 Абсолютное давление насыщенных паров СУГ , МПа, вычисляют методом последовательного приближения, задавая произвольные значения двух ближайших значений давления насыщенных паров при данной температуре (приложение Г), по формуле
, (5)
где - меньшее выбранное значение абсолютного давления СУГ, МПа, по таблицам Г.1-Г.8 (приложение Г);
- большее выбранное значение абсолютного давления СУГ, МПа, по таблицам Г.1-Г.8 (приложение Г).
Пример расчета давления насыщенных паров методом последовательного приближения приведен в приложении Д.
Значения и вычисляют по формулам:
; (6)
, (7)
где и - значения абсолютного давления насыщенных паров, МПа, вычисленные по формулам:
; (8)
, (9)
где и - значения летучести (фугитивности) -го компонента СУГ при абсолютных давлениях и , МПа, приведенные в таблицах Г.1-Г.8 (приложение Г).
В результате вычисления должно соблюдаться условие . Если , то расчет прекращают, задают следующую пару значений давления насыщенных паров и повторяют процедуру приближения.
5.3 Избыточное давление насыщенных паров СУГ , МПа, вычисляют по формуле
, (10)
где - абсолютное давление насыщенных паров СУГ, МПа;
- атмосферное давление, МПа; 101,3 кПа (0,1 МПа).
5.4 Примеры расчета давления насыщенных паров СУГ приведены в таблицах Е.1-Е.4 (приложение Е).
5.5 Оформление результатов вычисления давления насыщенных паров СУГ
5.5.1 За результат вычисления значения давления насыщенных паров СУГ при данной температуре принимают значение единичного определения.
5.5.2 Результат вычисления давления насыщенных паров СУГ , МПа, записывают в виде
, (11)
где - расширенная неопределенность результата вычисления давления насыщенных паров для данной температуры , МПа, при коэффициенте охвата 2;
вычисляют по таблице 2.
Таблица 2 - Расширенная неопределенность результатов вычисления давления насыщенных паров СУГ
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Температура измерений, °С
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Диапазон измерений , МПа
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Расширенная неопределенность , МПа
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Минус 35
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От 0,06 до 0,12 включ.
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LM4AoKqq6smTJ0cOH372KiN5R0cHl8s1MDAwMDDQ09OTSMSFhYUPHz48HB3NfpWJur6+jsfj6+np 6ujoMJnMEc7OkyZO/O23344dP56W9rixsYHL5ZaVlV27dm3Pnj1l5eUQBDGZBrt3716zZo3CkgAG gzFp8uSa6urS0tKurq5Hjx5VVFTQaLTOzs6srKx9e/fGxV0dO27cN998M0B2E8Z5NyDAvW9kgfOu AsPwpUuXnjx50tHRgQ5rgGGYTqcvXbrUy8urtbX1xInj1dU13d3dCmUYDMbs2QFBQX8lNBQIBLdu 3bp+/XpeXp5IJJJKJV1d3TQazdTUdNKkSatWrfL19e1tz0Y+n3/jxo1r164WFRXz+XwaTZfJ1CeR SNbW1vPnBy1evEjtPtM4OBqBi7xBCnjvPf1BMAwjP6oo0/P3rq6u2trampoakUgEQZCxsbGVlZW1 tTUWH5xAIKiurq6rqxOLxRQKxdra2tbWto9L03FwlIKLPBwcnEEEHquNg4MziMBFHg4OziACF3k4 ODiDCFzk4eDgDCJwkYeDgzOIwEUeDg7OIAIXeTg4OIMIXOTh4OAMInCRh4ODM4jARR4ODs4gAhd5 ODg4gwhc5OHg4Awi/h/YnI7uPby0TgAAAABJRU5ErkJggg==)
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Св. 0,12 до 0,20 включ.
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Минус 30
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От 0,06 до 0,12 включ.
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LM4AoKqq6smTJ0cOH372KiN5R0cHl8s1MDAwMDDQ09OTSMSFhYUPHz48HB3NfpWJur6+jsfj6+np 6ujoMJnMEc7OkyZO/O23344dP56W9rixsYHL5ZaVlV27dm3Pnj1l5eUQBDGZBrt3716zZo3CkgAG gzFp8uSa6urS0tKurq5Hjx5VVFTQaLTOzs6srKx9e/fGxV0dO27cN998M0B2E8Z5NyDAvW9kgfOu AsPwpUuXnjx50tHRgQ5rgGGYTqcvXbrUy8urtbX1xInj1dU13d3dCmUYDMbs2QFBQX8lNBQIBLdu 3bp+/XpeXp5IJJJKJV1d3TQazdTUdNKkSatWrfL19e1tz0Y+n3/jxo1r164WFRXz+XwaTZfJ1CeR SNbW1vPnBy1evEjtPtM4OBqBi7xBCnjvPf1BMAwjP6oo0/P3rq6u2trampoakUgEQZCxsbGVlZW1 tTUWH5xAIKiurq6rqxOLxRQKxdra2tbWto9L03FwlIKLPBwcnEEEHquNg4MziMBFHg4OziACF3k4 ODiDCFzk4eDgDCJwkYeDgzOIwEUeDg7OIAIXeTg4OIMIXOTh4OAMInCRh4ODM4jARR4ODs4gAhd5 ODg4gwhc5OHg4Awi/h/YnI7uPby0TgAAAABJRU5ErkJggg==)
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Св. 0,12 до 0,20 включ.
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Минус 20
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От 0,06 до 0,12 включ.
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Св. 0,12 до 0,20 включ.
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aTTDMfMdYnFdfX19XZ24o4NIJNrb2/fv79S3L+66hNPz4CIPBwenF4GbSHBwcHoRuMjDwcHpReAi DwcHpxeBizwcHJxeBC7ycHBwehG4yMPBwelF4CIPBwenF4GLPBwcnF4ELvJwcHB6EbjIw8HB6UXg Ig8HB6cXgYs8HBycXsT/Awy7O8cDM6mbAAAAAElFTkSuQmCC)
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Св. 0,20 до 0,50 включ.
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Плюс 45
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От 0,20 до 0,50 включ.
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CGBvNWAwGFe1zGSQxMTEMWPGwAC9wYMHT5s2LTg4GJ7l5u7uvnPnzoaGBt1N19XVzZs3T7czDh67 vmrVqidPnnRzqv7zzz/hQHJxcekpL5BhfkQ6nb5gwYIxY8ZcvXo1OTm5pKSkqKiIyWROmDDhrbfe CgsLIxKtzuVy9+7dGx0dzefzTU1Nx4wZY2Njc/jwYZVKpWNLPIIgoaGhb7zxxrVr15KSkvh8Po/H o9PpgYGBb775Znh4OJH9ntp49uwZh8OxtLQcOnQoiVVggUCwefPmuro6gUAgl8vt7Ozmzp3r6+sb FBTk4uJCIl8siqJDhw7t06cP3BurbVEb5hxkMplEtuV3k7ra2o8++igbtydPA5VKNWrUG10uQDU3 NWOL+C4uLlgaFWGrUKlU3rlzRyqVmpuba3PJOzs7z5kzp2D7dgCAWCw+fOTIhLcmmBDIxUIaFou1 devWxsZGDofzQs/SQxAkPDzc398fjuqnT5/CUR0UFARHNZEdpdbW1rt37/7qq68KCgrgEpmLi8uh Q4ckEonu/HKTJ08eOXLk9evXExMTi4qK+Hw+jUYbMWLE+PHjw8PDBwwYoLdpe3v7w4cPz5gxA3Ye i+6m0Wi2trZmZmZDhw4dPXr00KFDnZ2dux+9z+PxoISZNGkSuY0xXUBadsrl8qamJniqOgmDvKWl pbCwsKysTKFQlJWVOTo6MplMGGqjF4VCAQ+fbmxs7BGbqL29vaGhoaGhobW1lcTXVSpVQ0NDXV1d fX09FILd79LLR4cO2NraumjRQnNzc8zf1FkHzMrK6lJ9lsvly/720pqZmZ2/cAH7aNvWr7Bx6Obm Vl6u1bN5LyMD8wZaW3MePXrU7dv914Ef1SSGkEgkKioqKi0tlcvl9fX1UCG4dOkSke8qlUqBQACb lslkhvcdVavVIpGo4W8aGxslEkmP+yuwJrStspKA/Foyk8ns0vtAECsrKywzokwmUygUHA6H4BYZ BoPRs8c8mpqadmeqp9Fohgb3/Q/R0dERvX37uXPnt2z56tlTfuyvv3ZZDFuL/+d3ZYdiDp2NiwMA 2NrafvbZ56EzZ2KfSiT/H4xmbGxibKJVrevfv7+bm1tefj4AoKWl5VFWFn7H5OtBN0c1m83GtDb4 QsGMWES+S6fTyR0fjIEgCJvNftGJ2l5EE/+Kk5KePHnS3Nw8Y8YM6qSLfxtqtfrnn346ePDg8hUr Pv74o3UffkjkWzKZ7MGD+zwePzk5OTEx0dLSatasWcuXrxg/fhzeJ/DPoEsUaI+0t7K2dnd3hxIQ ALS4uITk/fQO8vPza2trx44da2hupF7Iq5eAIpHoxIkTxsbG+Gh1in8Jp0+dit6xY9qMGdHbo01N TVFiCd0EAsH6j9fn5OYqlUoajTZ69OjQ0NBhw4ZpuEQ7Kc5aHaZ0Oh0uXEKa/pm2kwKPRCL55Zdf EAR57733yOWe6lW8YgkI06WkpqauXr3a0EQGFC+ahISETZ9+Onz4iAPfHeBwDLCS7OzsfjlxoqSk 5NHDh5cvX05OTv7zzz9H+vquXbNm9uzZWLYLe3t7BoMB94SpVGq1Wmu6YARB8GYay5iaKbsGRdGj R49eu3Zt4cKFYWFhr7o7/wv0lEORBO3t7fv27WOz2e+++5IiXSl0gF8JSUhIzH782LN//0GDBufl 52NlsKjpzish2igtLZ07dw78lqmp6c6du5RKJfwoJ+cJ5kq2tbXLy8vXUc/GTzZgg3bXrm+6c6ev KzKZ7ODBg1ZWVmFhYTq2JFDgeTXZOJRK5f379yMjI7/77rvVq1f/+OOP3VlUoehZaDSExytas3aN VNZx6PChwYMGdae2vn377ty5y8OjHwBAIpF89923Dx48hB+5urr1/Xtnu0jUiiXv7BL53/E0DAaT SKBGr0KlUmVnZ7///vvbt29fvHjxoUOHXo/UuS+BVyABCwoKFixYsHjxYoVCcerUqZ07d/bswi5F N1GpVLt37y4s5P3www9jugq1NZR+/fphsX7Nzc3Xr1+Hf1taWgaNDoJ/y+VyfBooDdRqNZbyxM3d zdfvdVsI7g7FxcVLliyJiIhobm4+ceLEt99+i/eZUujmFUhAgUDg5uZ27NixM2fOvPXWW70kK9z/ ECqVSiRq++abb8LCiB5gohsajWZt9f9evOa/kyQiCBIWGoZ562/fvo1lF9egvb29qvK/mUTDQsOc SSUWfl0RCoX29vYHDx6Mi4sLCQnpgXQpvYlX8LDGjBnT/byGFC8OBEHWfbQuMtKABIsKhYJOp2sr j6IoPhe8KS4JTUBAwKSJE+MvXwYAPHz44NatlC7FbnlZWUlpCQDAzc09MjKSmjXx+Pr6wn11FCR4 BSOJxC4xipcAlqeTRqcHBQZ1Pn9LrVa3S3BnjeN+xzNnTm/cuElbbs6KinLsiEgjIyPM8gUAmJia btiwAYbFtLe379mzp7q6unMNFy5caGpsMjY2/vzzz3skU/HrBPVCdQdqLqUAAAC1Wp3/33hjoFIq seOc8IhEomfPnsG/ZVIpXt69+eablRXl77zzzm+//aZxtn1LS8vXO74uLvlvDPP0GTMm/zPsKTAo 6MvNm+Fm4czMe2vWrK2q+ocQTE5OOnL0CEKjr1i5csmSxdT7TtGD0Ldt2/aq+0DxKhEKhVlZWSdP njwZG4vlL6ioqLC0tDQxMbGxsUEQpKqq6uGDBwdjYq5dvQZDopVKJZ/Ht7S0AABwOBwOhxMcHNwi EOzbv//SpUulpaVNTU21tbW3b9+O3r794qVLKIoiCBISMvXHH360t++D7wCCIMNHjDA3N3v8OFsi kfD5vPT0DABQOp1eXl5+/PixL7/cIlcoN27auPmLL/61BwNQ/I+CoN04tp3iNeDx48fHjh2DKSHw WfKZTObIkSOjoqKYTObZs7+npKS2t7fjDS61Ws1isfp5eHy07iMLi//u1rx3717syZOpt2/DfHNy uRwFwMrSytPTc978eREREX20bKBGUfROWtqRo0fT09Pr6urUarWVlZWRkZGZmdmYMWOXLl0SFBRE uf8oehxKAlIA9O8DPLX9s8sCOr5YV1dXVVUFk9obGxs7ODg4OzvDpMS6USqVz58/r6qqgifk2tnZ ubq6crlcytVF8YKgJCAFBUXvhTIrKCgoei+UBKSgoOi9UBKQgoKi90JJQAoKit4LJQEpKCh6L5QE pKCg6L1QEpCCgqL3QklACgqK3gslASkoKHovlASkoKDovVASkIKCovdCSUAKCorey/8BSyqDJ6l0 Na0AAAAASUVORK5CYII=)
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Св. 0,50 до 1,00 включ.
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Св. 1,00 до 2,00 включ.
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Вычисленные значения давления насыщенных паров СУГ и расширенной неопределенности (абсолютной погрешности) округляют до второго десятичного знака.
5.6 Требования к показателям точности метода
Метод обеспечивает получение результатов вычисления избыточного давления насыщенных паров СУГ по измеренному компонентному составу со значением расширенной неопределенности , не превышающей значений, приведенных в таблице 2 при доверительной вероятности 0,95.
Приложение А (обязательное). Значения плотности углеводородов в жидком состоянииПриложение А
(обязательное)
В настоящем приложении приведены значения плотности углеводородов в жидком состоянии (см. таблицу А.1).
Таблица А.1 - Значения плотности углеводородов в жидком состоянии в зависимости от температуры
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Тем-
пера-
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Плотность, кг/м
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тура,
°С
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Метан
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Этан
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Про-
пан
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Про-
пен
|
Изо-
бутан
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н-бу-
тан
|
Бу-
тен-1
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Изо-
бутен
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транс-
бутен-2
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цис-
бутен-
2
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Бута-
диен-
1,3
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2,2-ди-
метил-
про-
пан
|
Изо-
пен-
тан
|
н-пен-
тан
|
3-ме-
тилбу-
тен-1
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Пен-
тен-1
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2-ме-
тилбу-
тен-1
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транс-
пен-
тен-2
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-50
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343,8
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496,1
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590,9
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611,4
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635,2
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651,1
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673,2
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673,3
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681,4
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699,4
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701,4
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661,4
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686,8
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691,5
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694,2
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707,7
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716,5
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714,0
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-45
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338,9
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488,8
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585,2
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605,2
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630,0
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646,4
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668,0
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667,8
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676,0
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694,0
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696,0
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656,7
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682,1
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687,0
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689,7
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703,2
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712,1
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709,6
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-40
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333,9
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481,0
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579,4
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598,9
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624,7
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641,5
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662,7
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662,4
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670,5
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688,5
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690,5
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652,0
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677,4
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682,5
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685,2
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698,8
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707,7
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705,2
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-35
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328,9
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473,1
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573,7
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592,6
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619,5
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636,7
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657,3
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657,0
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665,0
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683,0
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685,0
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647,2
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672,7
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678,0
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680,6
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694,2
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703,2
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700,6
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-30
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323,9
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464,9
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567,7
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586,3
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614,1
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631,7
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651,9
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651,5
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659,6
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677,6
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679,4
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642,4
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668,0
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673,4
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676,0
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689,6
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698,7
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696,0
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-25
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323,9
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456,3
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561,6
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579,9
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608,7
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626,8
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646,4
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646,2
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654,2
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672,2
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673,8
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637,5
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663,2
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668,8
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671,3
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684,9
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694,1
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691,3
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-20
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314,1
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447,3
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555,5
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573,5
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603,3
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621,8
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640,9
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640,5
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648,7
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666,7
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668,3
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632,6
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658,5
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664,3
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666,6
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680,2
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689,4
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686,6
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-15
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309,4
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437,8
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549,3
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566,7
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597,8
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616,6
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635,3
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635,0
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643,2
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661,2
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662,6
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627,7
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653,7
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659,6
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661,9
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675,4
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684,7
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681,8
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-10
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304,7
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427,5
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542,9
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559,9
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592,3
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611,5
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629,7
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629,4
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637,8
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655,8
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656,8
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622,8
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648,9
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655,0
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657,1
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670,6
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679,9
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677,0
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-5
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299,9
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416,6
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536,4
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552,7
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586,7
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606,6
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624,0
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623,7
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632,4
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650,4
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651,0
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617,9
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644,0
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650,2
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652,2
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665,7
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675,1
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672,2
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0
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295,4
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404,8
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529,7
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545,7
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581,0
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601,0
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618,2
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618,0
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626,9
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644,9
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645,2
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613,0
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639,2
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645,5
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647,2
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660,8
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670,2
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667,5
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5
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291,8
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391,8
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522,8
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538,0
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575,3
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595,7
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612,4
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612,2
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621,4
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639,4
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639,2
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608,0
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634,3
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640,8
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642,2
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655,8
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665,3
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662,8
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10
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286,3
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377,5
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515,8
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530,6
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569,4
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590,2
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606,5
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606,5
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616,0
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634,0
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633,3
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603,0
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629,4
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636,0
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637,2
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650,8
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660,3
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658,0
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15
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281,9
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361,1
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508,6
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522,7
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563,4
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584,6
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600,5
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600,6
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610,6
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628,6
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627,2
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598,0
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624,5
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631,1
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632,2
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645,6
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655,3
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653,1
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20
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277,6
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342,1
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501,1
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514,8
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557,3
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578,9
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594,5
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594,7
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605,1
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623,1
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621,1
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592,9
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619,6
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626,2
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627,2
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640,5
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650,3
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648,2
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25
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273,3
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319,7
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493,4
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506,4
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551,1
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573,2
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588,4
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588,6
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599,6
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617,6
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614,8
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587,8
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614,6
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621,3
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622,1
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635,3
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645,0
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643,1
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30
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269,0
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291,9
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485,5
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498,1
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544,8
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567,3
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582,3
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582,6
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594,2
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612,2
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608,4
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582,6
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609,7
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616,3
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617,0
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630,0
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640,0
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638,1
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35
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264,3
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262,3
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477,5
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489,2
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538,5
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561,3
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576,0
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576,4
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588,8
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606,8
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601,8
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577,8
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604,7
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611,2
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611,9
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624,6
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634,9
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632,8
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40
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260,8
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226,3
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468,9
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480,4
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531,8
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555,2
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569,8
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570,3
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583,3
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601,3
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595,3
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573,1
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599,7
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606,2
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606,8
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619,3
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629,8
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627,5
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45
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256,8
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184,1
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460,4
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471,0
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525,2
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549,0
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563,4
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564,0
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577,8
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595,8
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588,5
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567,7
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594,6
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601,0
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601,6
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613,8
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624,6
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621,9
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50
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253,6
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134,5
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451,3
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461,7
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518,2
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542,6
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557,1
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557,8
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572,4
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590,4
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581,7
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562,3
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589,5
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595,9
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596,4
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608,4
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619,4
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616,3
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Продолжение таблицы А.1
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Тем-
пера-
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Плотность, кг/м
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тура, °С
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цис-
пен-
тен-2
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2-ме-
тилбу-
тен-2
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Цик-
лопе-
нтан
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2,2-ди-
метил-
бутан
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2,3-ди-
метил-
бутан
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2-ме-
тил-
пен-
тан
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3-ме-
тил-
пен-
тан
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н-гек-
сан
|
Метил-
цикло-
пентан
|
Цикло-
гексан
|
Бен-
зол
|
2,2-ди-
метил-
пентан
|
2,4-ди-
метил-
пентан
|
2,3-ди-
метил-
пентан
|
2-ме-
тил-
гексан
|
3-ме-
тил-
гексан
|
1,1-ди-
метил-
цикло-
пентан
|
1,3-ди-
метил-
цикло-
пентан-
цис
|
-50
|
722,7
|
728,4
|
813,0
|
709,4
|
721,7
|
713,0
|
724,4
|
719,9
|
813,7
|
843,8
|
951,7
|
733,4
|
732,7
|
753,5
|
736,2
|
744,7
|
817,9
|
807,5
|
-45
|
718,2
|
724,0
|
808,2
|
705,2
|
717,6
|
708,8
|
720,2
|
715,7
|
809,0
|
839,2
|
946,6
|
729,2
|
728,4
|
749,4
|
732,2
|
740,7
|
813,4
|
803,1
|
-40
|
713,8
|
719,6
|
803,4
|
701,1
|
713,4
|
704,7
|
716,1
|
711,5
|
804,4
|
834,5
|
941,4
|
724,9
|
724,2
|
745,2
|
728,2
|
736,7
|
809,0
|
798,7
|
-35
|
709,3
|
715,1
|
798,6
|
697,0
|
709,2
|
700,6
|
712,0
|
707,3
|
799,8
|
829,8
|
936,2
|
720,7
|
720,0
|
741,0
|
724,2
|
732,6
|
804,5
|
794,4
|
-30
|
704,8
|
710,6
|
793,8
|
692,8
|
705,1
|
696,4
|
707,8
|
703,1
|
795,1
|
825,2
|
931,1
|
716,5
|
715,7
|
736,9
|
720,1
|
728,6
|
800,0
|
789,8
|
-25
|
700,2
|
706,0
|
789,0
|
688,6
|
700,9
|
692,2
|
703,6
|
698,8
|
790,4
|
820,5
|
926,0
|
712,2
|
711,4
|
732,8
|
716,0
|
724,5
|
795,4
|
785,3
|
-20
|
695,6
|
701,4
|
784,2
|
684,4
|
696,7
|
688,0
|
699,4
|
694,6
|
785,8
|
815,9
|
920,8
|
707,9
|
707,2
|
728,6
|
711,9
|
720,4
|
790,9
|
780,8
|
-15
|
690,9
|
696,7
|
779,4
|
680,2
|
692,4
|
683,8
|
695,2
|
690,3
|
781,2
|
811,2
|
915,6
|
703,6
|
703,0
|
724,4
|
707,8
|
716,3
|
786,2
|
776,3
|
-10
|
686,2
|
692,0
|
774,5
|
675,9
|
688,2
|
679,5
|
690,9
|
686,0
|
776,5
|
806,6
|
910,4
|
699,4
|
698,7
|
720,3
|
703,7
|
712,2
|
781,8
|
771,8
|
-5
|
681,2
|
687,2
|
769,6
|
672,6
|
683,8
|
675,2
|
686,6
|
681,6
|
771,8
|
802,0
|
905,2
|
695,2
|
694,4
|
716,2
|
699,6
|
708,0
|
777,2
|
767,3
|
0
|
676,3
|
682,3
|
764,8
|
667,2
|
679,5
|
670,9
|
682,2
|
677,2
|
767,2
|
797,3
|
900,0
|
691,0
|
690,2
|
712,0
|
695,4
|
703,9
|
772,7
|
762,8
|
5
|
671,2
|
677,4
|
760,0
|
662,7
|
675,0
|
666,4
|
677,8
|
672,8
|
762,6
|
792,6
|
894,8
|
686,7
|
685,8
|
707,8
|
691,2
|
699,8
|
768,0
|
758,3
|
10
|
666,0
|
672,4
|
755,1
|
658,2
|
670,6
|
662,0
|
673,3
|
668,4
|
757,9
|
788,0
|
889,6
|
682,4
|
681,5
|
703,6
|
687,0
|
695,6
|
763,6
|
753,8
|
15
|
660,8
|
667,4
|
750,2
|
653,7
|
666,1
|
657,6
|
668,8
|
663,9
|
753,4
|
783,3
|
884,3
|
678,1
|
677,1
|
699,4
|
682,8
|
691,4
|
759,0
|
749,3
|
20
|
655,5
|
662,3
|
745,4
|
649,2
|
661,6
|
653,2
|
664,3
|
659,4
|
748,6
|
778,6
|
879,0
|
673,8
|
672,7
|
695,1
|
678,6
|
687,2
|
754,5
|
744,8
|
25
|
650,2
|
657,2
|
740,4
|
644,6
|
657,0
|
648,6
|
659,8
|
654,8
|
743,9
|
773,9
|
873,7
|
669,5
|
668,3
|
690,9
|
674,3
|
682,9
|
749,9
|
740,2
|
30
|
644,8
|
652,0
|
735,6
|
640,0
|
652,5
|
644,1
|
655,2
|
650,2
|
739,3
|
769,2
|
868,4
|
665,2
|
663,9
|
686,6
|
670,0
|
678,6
|
745,3
|
735,7
|
35
|
639,4
|
646,8
|
730,7
|
635,3
|
647,8
|
639,5
|
650,6
|
645,6
|
734,6
|
764,4
|
863,0
|
660,8
|
659,4
|
682,3
|
665,8
|
674,3
|
740,6
|
731,1
|
40
|
634,1
|
641,5
|
725,8
|
630,6
|
643,2
|
634,9
|
645,9
|
640,9
|
730,0
|
759,6
|
857,6
|
656,5
|
655,0
|
678,0
|
661,5
|
670,0
|
736,0
|
726,5
|
45
|
628,8
|
636,2
|
720,9
|
625,8
|
638,5
|
630,2
|
641,2
|
636,2
|
725,4
|
754,4
|
852,2
|
652,2
|
650,5
|
673,6
|
657,0
|
665,6
|
734,3
|
721,8
|
50
|
623,4
|
630,8
|
716,0
|
621,1
|
633,8
|
625,5
|
636,4
|
631,5
|
720,7
|
749,9
|
846,8
|
647,8
|
646,0
|
669,3
|
652,6
|
661,1
|
726,6
|
717,2
|
Продолжение таблицы А.1
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
Тем-
пера-
|
Плотность, кг/м
|
тура,
°С
|
1,3-ди-
метил-
цикло-
пентан-
транс
|
Толу-
ол
|
1,1,2-
три-
метил-
цикло-
пентан
|
2-
метил-
тилгеп-
тан
|
3,4-ди-
метил-
гексан
|
4-ме-
тил-
геп-
тан
|
3-ме-
тил-
гептан
|
3-
этил-
гексан
|
1,1-
ди-
метил-
цикло-
гексан
|
1,1-
ме-
тил-
этил-
цикло-
пен-
тан
|
1,2-ди-
метил-
цикло-
пентан-
транс
|
1,2-ди-
метил-
цикло-
пен-
тан-
цис
|
н-гептан
|
Метил-
цикло-
гексан
|
1,1,3-
триме-
тил-
цикло-
пентан
|
Этил-
циклопентан
|
2,5-ди-
метил-
гексан
|
-50
|
810,8
|
931,8
|
832,2
|
752,6
|
774,2
|
759,2
|
760,5
|
769,1
|
838,0
|
838,7
|
814,1
|
834,6
|
741,5
|
830,1
|
807,4
|
825,7
|
752,0
|
-45
|
806,8
|
927,2
|
828,0
|
748,8
|
770,4
|
755,4
|
756,7
|
765,2
|
834,0
|
834,6
|
809,7
|
830,2
|
737,5
|
825,8
|
803,2
|
821,6
|
747,9
|
-40
|
802,1
|
922,5
|
823,9
|
745,0
|
766,5
|
751,6
|
752,9
|
761,4
|
830,0
|
830,6
|
805,3
|
825,9
|
733,5
|
821,5
|
799,1
|
817,4
|
743,8
|
-35
|
797,8
|
917,8
|
819,7
|
741,2
|
762,6
|
747,8
|
749,0
|
757,5
|
826,0
|
826,5
|
800,8
|
821,5
|
729,4
|
817,2
|
794,9
|
813,2
|
739,6
|
-30
|
793,3
|
913,2
|
815,5
|
737,3
|
758,7
|
743,9
|
745,2
|
753,6
|
821,9
|
822,4
|
796,4
|
817,1
|
725,4
|
812,9
|
790,7
|
809,0
|
735,5
|
-25
|
788,8
|
908,6
|
811,2
|
733,4
|
754,8
|
740,0
|
741,3
|
749,6
|
817,8
|
818,2
|
791,9
|
812,6
|
721,3
|
808,6
|
786,4
|
804,8
|
731,3
|
-20
|
784,4
|
903,9
|
807,0
|
729,5
|
750,8
|
736,1
|
737,4
|
745,7
|
813,7
|
814,1
|
787,4
|
808,2
|
717,2
|
804,2
|
782,2
|
800,5
|
727,1
|
-15
|
780,0
|
899,3
|
802,8
|
725,6
|
746,8
|
732,2
|
733,4
|
741,7
|
809,6
|
810,0
|
782,9
|
803,8
|
713,1
|
799,8
|
778,0
|
796,8
|
722,9
|
-10
|
775,5
|
894,7
|
798,5
|
721,6
|
742,9
|
728,2
|
729,5
|
737,7
|
805,5
|
805,8
|
778,4
|
799,3
|
709,0
|
795,5
|
773,7
|
792,0
|
718,7
|
-5
|
770,0
|
890,1
|
794,5
|
717,7
|
739,0
|
724,3
|
725,6
|
733,8
|
801,4
|
801,6
|
773,9
|
794,8
|
704,8
|
791,2
|
769,4
|
787,8
|
714,5
|
0
|
766,6
|
885,5
|
790,0
|
713,8
|
735,0
|
720,4
|
721,7
|
729,8
|
797,3
|
797,5
|
769,4
|
790,4
|
700,7
|
786,8
|
765,2
|
783,5
|
710,3
|
5
|
762,2
|
880,8
|
785,8
|
709,8
|
731,0
|
716,4
|
717,8
|
725,8
|
793,2
|
793,4
|
764,9
|
786,0
|
696,5
|
782,4
|
761,0
|
779,2
|
706,1
|
10
|
757,7
|
876,2
|
781,0
|
705,9
|
727,1
|
712,5
|
713,8
|
721,7
|
789,1
|
789,2
|
760,4
|
781,5
|
692,3
|
778,1
|
756,7
|
775,0
|
701,9
|
15
|
753,0
|
871,6
|
776,8
|
701,9
|
723,2
|
708,6
|
709,8
|
717,6
|
785,0
|
785,0
|
755,9
|
777,1
|
688,0
|
773,8
|
752,4
|
770,8
|
697,7
|
20
|
748,8
|
866,9
|
772,5
|
697,9
|
719,2
|
704,6
|
705,8
|
713,6
|
780,9
|
780,9
|
751,4
|
772,6
|
683,8
|
769,4
|
748,2
|
766,5
|
693,5
|
25
|
744,3
|
862,3
|
768,2
|
693,9
|
715,2
|
700,6
|
701,8
|
709,5
|
776,8
|
776,7
|
746,9
|
768,1
|
679,5
|
765,0
|
743,9
|
762,2
|
689,3
|
30
|
739,8
|
857,6
|
764,0
|
689,8
|
711,3
|
696,6
|
697,7
|
705,4
|
772,8
|
772,6
|
742,4
|
763,6
|
675,2
|
760,6
|
739,6
|
757,8
|
685,1
|
35
|
735,2
|
853,0
|
759,6
|
685,8
|
707,2
|
692,6
|
693,6
|
701,2
|
768,6
|
768,4
|
737,8
|
759,0
|
670,8
|
756,2
|
735,3
|
753,4
|
680,8
|
40
|
730,7
|
848,3
|
755,3
|
681,7
|
703,2
|
688,5
|
689,6
|
697,1
|
764,4
|
764,1
|
733,1
|
754,5
|
666,4
|
751,8
|
731,0
|
749,1
|
676,6
|
45
|
726,1
|
843,6
|
742,1
|
677,6
|
699,1
|
684,4
|
685,4
|
692,9
|
760,2
|
759,8
|
728,4
|
750,0
|
662,0
|
747,4
|
726,6
|
744,7
|
672,3
|
50
|
721,5
|
838,8
|
737,7
|
673,4
|
695,0
|
680,3
|
681,3
|
688,7
|
755,9
|
755,5
|
723,7
|
745,3
|
657,6
|
743,0
|
722,3
|
740,3
|
668,0
|
Окончание таблицы А.1
|
|
|
|
|
|
|
|
|
Темпе-
ратура,
|
Плотность, кг/м
|
°С
|
1,2,4-три-
метил-
циклопентан-
транс, цис
|
1,2-
метил-
этил-
циклопентан цис
|
н-октан
|
н-пропил-
циклопентан
|
Этил-
бензол
|
1,4-
диметил-
бензол
|
1,3-
диметил-
бензол
|
1,2-
диметил-
бензол
|
-50
|
806,5
|
842,3
|
758,1
|
833,4
|
928,8
|
920,9
|
922,7
|
938,7
|
-45
|
802,4
|
838,3
|
754,2
|
829,4
|
924,6
|
916,6
|
918,5
|
934,6
|
-40
|
798,2
|
834,3
|
750,4
|
825,4
|
920,1
|
912,5
|
914,5
|
930,5
|
-35
|
794,0
|
830,2
|
746,5
|
821,4
|
915,8
|
908,2
|
910,4
|
926,4
|
-30
|
789,8
|
826,2
|
742,6
|
817,3
|
911,3
|
904,0
|
906,2
|
922,2
|
-25
|
785,6
|
822,1
|
738,6
|
813,2
|
906,8
|
899,7
|
902,0
|
918,0
|
-20
|
781,3
|
818,0
|
734,7
|
809,1
|
902,4
|
895,4
|
897,8
|
913,8
|
-15
|
777,0
|
813,9
|
730,7
|
805,0
|
898,0
|
891,1
|
893,6
|
909,6
|
-10
|
772,8
|
809,8
|
726,7
|
800,9
|
893,5
|
886,8
|
889,4
|
905,4
|
-5
|
768,6
|
805,7
|
722,8
|
796,8
|
889,0
|
882,5
|
885,2
|
901,2
|
0
|
764,3
|
801,6
|
718,8
|
792,7
|
884,6
|
878,2
|
881,0
|
897,0
|
5
|
760,0
|
797,5
|
714,8
|
788,6
|
880,2
|
873,9
|
876,8
|
892,8
|
10
|
755,8
|
793,4
|
710,7
|
784,5
|
875,7
|
869,6
|
872,6
|
888,6
|
15
|
751,6
|
789,3
|
706,6
|
780,4
|
871,4
|
865,3
|
868,4
|
884,4
|
20
|
747,3
|
785,2
|
702,6
|
776,3
|
867,0
|
861,0
|
864,2
|
880,2
|
25
|
743,0
|
781,1
|
698,4
|
772,3
|
862,6
|
856,7
|
859,9
|
876,0
|
30
|
738,7
|
777,0
|
694,3
|
768,1
|
858,3
|
852,5
|
855,6
|
871,9
|
35
|
734,4
|
772,6
|
690,2
|
764,0
|
853,8
|
848,0
|
851,3
|
867,6
|
40
|
730,0
|
768,7
|
686,0
|
759,8
|
849,4
|
843,7
|
847,0
|
863,4
|
45
|
725,6
|
764,5
|
681,8
|
755,6
|
844,9
|
839,3
|
842,7
|
859,1
|
50
|
721,2
|
760,3
|
677,6
|
751,4
|
840,4
|
834,9
|
838,4
|
854,8
|
Примечание - Значения получены в соответствии с ГОСТ 31369, ГОСТ 33012, [1].
|
Приложение Б (обязательное). Значения молярных масс индивидуальных компонентовПриложение Б
(обязательное)
В настоящем приложении приведены значения молярных масс индивидуальных компонентов (см. таблицу Б.1)
Таблица Б.1 - Значения молярных масс индивидуальных компонентов
|
|
Компонент
|
Молярная масса, г/моль*
|
Метан ( )
|
16,043
|
Этан ( )
|
30,070
|
Этилен ( )
|
28,054
|
Ацетилен (этин) ( )
|
26,038
|
Пропан ( )
|
44,097
|
Пропилен ( )
|
42,081
|
Пропадиен ( )
|
40,065
|
Метилацетилен ( )
|
40,065
|
Изобутан ( )
|
58,123
|
н-Бутан ( )
|
58,123
|
Бутен-1 ( )
|
56,108
|
Изобутен ( )
|
56,108
|
транс-Бутен-2 (транс )
|
56,108
|
цис-Бутен-2 (цис- )
|
56,108
|
Бутадиен-1,2 ( )
|
54,092
|
Бутадиен-1,3 ( )
|
54,092
|
2,2-Диметилпропан ( )
|
72,150
|
Изопентан ( )
|
72,150
|
н-Пентан ( )
|
72,150
|
Пентен-1 ( )
|
70,134
|
Циклопентан ( )
|
70,134
|
н-Гексан ( )
|
86,177
|
2-Метилпентан ( )
|
86,177
|
3-Метилпентан ( )
|
86,177
|
2,2-Диметилбутан ( )
|
86,177
|
2,3-Диметилбутан ( )
|
86,177
|
Метилциклопентан ( )
|
84,161
|
Циклогексан ( )
|
84,161
|
Бензол ( )
|
78,114
|
н-Гептан ( )
|
100,204
|
Этилциклопентан ( )
|
98,188
|
Толуол ( )
|
92,141
|
н-Октан ( )
|
114,231
|
* Молярные массы приведены по ГОСТ 31369.
|
Приложение В (рекомендуемое). Пример расчета плотностиПриложение В
(рекомендуемое)
В таблицах В.1, В.2 приведены примеры расчета плотности при различных температурах.
Таблица В.1 - Пример расчета плотности СУГ при температуре 20°С через массовые доли
|
|
|
|
|
Компонент
|
Плотность ,
кг/м
|
Массовая доля
, %
|
|
, кг/м
|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAHgAAABSCAIAAAAQMYfVAAALDklEQVR4nO2cf1ATZxrH390kGiBo QIkiEiaoMe1IcByUnuIB/qhk/NHDGUegZ9XRKbb84Zw458wJVipq1FGnM8f0Tp3ioU6lkTLUH+fo tVLbGS0mNQMUhQApRBPUmJAQEgib3ftjpzvrxmw2Iayi+/lvn33f53n3m3fffd93nw2EYRjgGHvg V92AtwVOaJbghGYJTmiW4IRmCU5oluCEZglOaJbghGYJTmiW4IRmCU5oluCEZglOaJbghGYJTmiW 4IRmCX5EvKAo6nA4zGZzb2+vy+XCjQKBICUlRSqVxsXFwTD1F+3u7tZqtevXr+fzI9OG15zRXqTJ ZLp9+/bNmzebm5tNJpPdbvf5fPgpCIJiY2OlUmlmZuayZcuWL18+bdo0oqJGo6mrq1OpVLGxsbhF p9N9/fXXPp8PwzAYhv1/Gxy8AAAgNTW1uLh44sSJ5LMPHz6srq72er30TlAURVEUAJCYmPjpp58S bRg7whe6p6fnwoULNTU1nZ2duLhisVipVMrlcvzifT5fT0+PwWCorq6urq5OS0srKCgoKChITk5+ 8OBBTU0Nn89HEIRwKBaL5XK52Wxua2trbGx89uyZf1AIghQKRXZ29uzZs2Uymb+OIpFo7ty5jx49 evjw4a1bt/r6+l7a+FmzZuXk5KSmps6aNYulWwoLnYGBgS+++EIul0MQBACAYTgjI+Pw4cP37t2z 2WwoihIlXS5XR0fHuXPnVCpVdHQ0AGDOnDkqlWrOnDkAgJSUlJ6eHn//CII0NTUtWbKE0lQYhktK SiwWC5NG+ny+5uZmlUrlf8nbtm17adwxJWSh29vbN27cKBAI8EZLJJLKysq+vj76Wm63W6PRKJVK 8gUnJycbjcZAVa5duyYUCsnl09PTGapMcPfu3bi4OLITmUzW2dkZkpOIEJrQOp1uwYIFRKPlcvmN GzfIXZie9vb2nJwcorpYLNbpdIEKG41GqVRK1mjTpk3MY+FYrda0tDSyk7y8vOHh4ZCcRIQQpnd6 vX7btm2//vorfpiSknLq1KmVK1fiAwgT5HL56dOns7Ky8EMEQUZGRgIVFgqFlAedSCRiHgtnwoQJ UVFRZEtMTMwrmecwFdpkMu3cuVOv1+OHQqHws88+y87ODjXe7Nmzjxw5MmPGDADA8PDwS594gQhV 5bFzEgaMhPZ4PPv27bt9+zZh2bBhQ2FhYXghFy9evGvXLgiCfD7f8PAw84rTp08PLyKZadOmBZrz jSmMQjY0NNTW1hKHYrF4x44dlCdVSBQVFaWnp6Mo+vz5c+a1KINAeETESRgEF9pisRw/ftzj8RCW VatWZWRkjCZqYmLili1bAABOp3M0fsYRwYXWaDQ6nY44FAgEGzZsmDBhwigDf/DBB1Kp1GazjdLP eCGI0Dab7eLFixgp41Qmk2VmZo4+sFQqXbJkidVqHb2rcUGQic5PP/1E7s4AAKVSmZiYOPrAMAxv 2bLFbDaP3tW4IIjQjY2NXq+XbJk/fz6Px4tI7Pfffz8ifsYFdEOH3W7/+eefyRY+n09ZaHEwhE7o np6e7u5usiU6Ojoik9m3EDqhjUajw+EgW0Qi0ZQpU8a4SW8mdGO0wWAgdvFxxGLx5MmTx7hJAUEQ BEVR8hY2PRAEeb1efIP/lUMntP9GBI/HeyXrV5yvvvrq1q1bWChfNyEI0tHRMXZNYs54el9nMBgM BsOrbkWYjCehCwsL165dSxnNaIAgyO12q9VqyiP9lTCehF6wYEGoW4YDAwNnzpx5HYSmG3BfOsEI aYjkIKDr0ZS3bQCA/v7+gYEBboaHIMjjx4+9Xu/kyZMlEgmTKnQ9WiaTUTadnU7n27MNRMO1q1dz c3MXL1588NAhhlXohFYoFJT9o4GBgfH73I8URqOx4vPPjUaj1Wrt7+9nWItOaIlEgidgEKAoSrw2 fDvxer1q9WHiDTVz6IQWCoW5ubkUY1NT0+DgYKhh3hg033xz4fyFMCoGWeatW7du5syZZMv9+/ff 2k794EHbgQMHhoaHeaEvj4NUUCgUK1euJFscDkdDQ0OoYQJx+fLlK1euRMrbmOJyuSr2V3R1dxcU FIr95mNBCSI0DMNbt25NSEggG2tra1taWkKN5I9ery8rKyO/9n2dOVtdfamubs2atZ98sgMOPTkk +C2QlZW1fft2sqW3t/fEiRMhpWT4Y7FYSktL582bt27dOoZVIrJWCs/Jvaamw2p1cnLy/or98XFx YTgJLjQEQSUlJQsXLiQba2trz58/H2owArvdvmfPHovFsnfvXkreFw1PnjwJOyLB06dPQ5XJZrPt r9hvtVrLysvTlUpfWPuujAb1pKSko0ePkp+KHo+nvLy8vr4+jJD9/f2lpaVXr149ePDgu+++y7yi 2+0OI5y/k5CExjDsX19++d9r14uKPvywqCj8wMzzIS9evEhO2QcASCSSY8eOOZ1O5k5MJtOmTZti YmKOHz+O5+4Hore3VyaTkcMVFxczD4Rjs9nmz59PdpKfn48gCHMP/7t5Mz4+Pi0trbOrC7e0tLRM /WMT4qPNmxn6CS1tV6PRUNaKAoFg9erV169fHxoaoq/rdru/++67hQsXRkdHHz16FP/6gYZffvll 0qRJ5FgqlSrUjNu2tjZK51i0aJHD4WBYvc9iWZqVJRKJ6uq+JYxsCI1h2Pfff5+ZmUnJyYyNjV29 enVVVZVer3/27JnH4xn6A6vVqtfrq6qq8vLyhEKhVCqtqakJqjKKomVlZZSbTyKRNDY2Mm8qiqJq tdq/qfX19UyqIwiye3cpAOBvu3aNjIwQdpaExjDMbDaXl5dTFjIAAAiC4uPj582bt2zZshUrVqxY sWL58uVKpRLfBYyKisrPz9dqtYHcOp1O/B3KnTt3du/eTenOODKZTK1W6/V6g8FgMpn889IHBwdx J1qttqysTCwW+ztJTEzct2+fVqs1GAy///57oJGk/ttvY2NFWVlLzS9+ZhCe0BAW1nQHRdH29va6 urqGhoaOjg6aXEUIgqZPn7506dKtW7dmZ2fTJHP+8MMPJ0+eBAC4XC673Q5elsuMoigMwwkJCQKB QKFQVFZWUhzqdLrKykoEQdxut81mwzDspU4gCJo6dapQKExKSjpy5Ij/72E0duf/Jf+x2XLp0qXs 7D+TT7W2tubm5FifPwcAfLR583/Ong10RS/oEJ7QBHa7vaOjQ6vVdnZ2dnV1uVwu/MIwDJsyZco7 77yjUCgyMjJkMhnx2UsgvF4v/o0iBEH06eJ4H+Hz+f69fmRkxOVy4foyccLj8SZNmkQpOTw0VFJS Un327MGDh/bs+TvlbHhChzN0BMLr9XpIhPRwf62oqamZOHHimjVr7f39/mfDGzoi+c5QIBAE7bav P7+1tn5eUTEjKamyslIcPImF6Vp8PL2cZYHBwcEDBw50dnV9/HGx0+n48ccfKQVgGO7q6iK+cXrS 14eXwTBMKk1JTZVRPRJE8I57A/ittTVh6lQAgFAojAoAec+Ax+PhRoFA8I+9e2k8cz36BXwoim9l DA0NMSrv8xG7jyMv5jdT4IR+gZiYmD+9916/wxFoxgJB0KDL1dzSgqcASiQSuVwOAPD5fDJZKo3n 0U7v3jAwDMP3EgIV4PF4Lc3NeXl5z202AEDRh389ferf+Cn6uQDXo18AgqCg38cJo6KI/s7n8/A/ EwgK9w80LMEJzRKc0CzBCc0SnNCjhFuCjxkzZ878Z1UVPgukpMzRwM2jWYIbOliCE5olOKFZghOa JTihWYITmiU4oVmCE5ol/g8GVyCZczhm4QAAAABJRU5ErkJggg==)
|
277,6
|
0,06
|
0,0002
|
-
|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAPZklEQVR4nO2ceVRTVx7HbxZCCBDZ ggJBWSQBA8GitSJo0aEM9KjYwQVoRaEKpwj2CG5wtAcdbW21i9o6rbZjq1iVg5y6QYEqQu0wbKVV URASUrZAgLCTkJD35o9o+hrI8rIAb8znr+Tm3t/95X3fu+vvPhwMw8AEdsBPtwMm0GESDGOYBMMY JsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjEE0iJWh oaH29nYOh9PU1DQ0NCRPJJFI8+fPZzAYbm5uVlZWSkV+++234uLinTt3mpubG8QHJDAMj4+PAwBw OJw2mQEAZmZmE3+SSqWojBCJRG0y6wNOnxABqVRaVVVVUFBQUlLS1NTU09Mjk8mU8tjZ2bFYrJCQ kHXr1rHZbCLx2S2yf//+oqKi0tJSa2tr3d1XAYfDOXLkSH9/v0QigSCIQCBMmk0mk+HxeHNzc0dH x6ysrDlz5iB/7ezszMrKEggEY2NjMpmMQCBMKoZMJsPhcCQSycbG5uDBg56engb/O0h0FEwqlZaX l587d+727dt9fX0AADMzMy8vLz8/P19fX/lDI5PJuFzugwcP6uvrBwYGaDRaREREQkICk8msqalJ SkqaNWtWaWmpg4ODgf8TAMPDww8fPuzs7ORyuTdv3iwtLZ00W1BQ0Nq1a5lMppOTE5vNJpPJyF/F YvGDBw/4fD6Px7t161ZJScnE2xEAsGjRosjISG9vb2dnZ39//4ltiYGB0cPj8ZKSkmxsbOQWLC0t Y2Njb9y4wefzZTKZUuaBgYGKiordu3e7uroCAKhUqpeX16xZswAAc+fO/eOPP3RwABX9/f0ZGRmK J1sOHo9PTk7u7e3V0sjw8PBHH32kpCgAYOvWrV1dXUb1XwnUghUWFi5evFjh8cKFC/Py8sRiscaC v/766xtvvIFsVZydnZuamnRyGx3t7e3z589HXmg6nd7Y2IjKSH9/P/KPAwBsbW2rq6uN5LMq0AmW m5vr5OSk8Dg0NLShoUH74kKh8O2338bjnw1NqVRqVVUVSod1QSwWh4aGIq/1smXLhoeHURmBICg6 OhppxMfHRyAQGMlnVaAY1l+/fj0lJYXP58u/vvLKK1999RWDwdDegq2t7YkTJ2JiYuRfZTKZRCLR vrjO4PF4pUGgmZmZqpGIKuQjC2QKkUhEa0R/tBWssrIyPT29s7NT/tXBweGDDz7w8PBAW5+Njc3h w4cXLlwIABCLxQKBAK0Fg2CQ8TeRSFS0FlOGVvV1d3fv27ePw+HIv+JwuKSkpFdffVW3Kj08PDIy MshkMgRB8onO1DN79mylx0UHaDQahUIxiD/ao1kwGIa/+eabsrIyRQqdTt+8ebM+N9frr7++fPly GIa7urp0NqIPBnnCVM3MjIrmi15XV3fmzBkIghQpUVFRXl5e+tRqZWWVmJhIIpFGR0f1sfMCokEw GIazs7NbW1sVKZaWlpGRkfq33StXrmQwGIohjAkt0XDdeTzetWvXkCne3t7+/v76V2xvb79q1aqR kRH9Tb1QaFj8LSkpUYw15Pj7+yvWOPQkJSVFKBQaxNSLgzrBZDJZSUkJ/NfFxoCAAEP1tHp2hC8m 6prErq6uiooKZIq5uTmqmbIJg6NOsObm5o6ODmSKpaWlo6OjkV0yoQ51gnG5XKVht7W1ta2trZFd mgp0a9WnftY1EXV9mHwpHZlCpVKNvt8zJfT29tbW1upQyhjOoEKdYP/Hs9rCwkJVu5pqEIvFxnAG FYaJ6cAc5ubmDg4OqJo4GIa7u7una/FTwQsqWHh4+MmTJ9GWevfdd3Nzc43hj/aoE2ziZs9M6HUN 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|
342,1
|
1,16
|
0,0034
|
-
|
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501,1
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62,36
|
0,1244
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-
|
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557,3
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13,42
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0,0241
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|
578,9
|
22,39
|
0,0387
|
-
|
нео-![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAKMAAABWCAIAAAAsUbF9AAAP70lEQVR4nO2deVgT197HJyELS9gM m1QUlDVsPlILtdadovS5LFqtG6W1j4oLgqmCCG5Xq6jYWq5e4IL6FutboC0UN9RHEdCCBfV9ZKmK LLIHiJCwZCOZef+Ye3OnSUhmsmBo5vMXc+ac3/lNvrOc5XcOBAiCABwDgPi2HcCZIHClDQVcaUMB V9pQwJU2FHClDQVcaUMBV9pQwJU2FHClDQVcaUMBV9pQwJU2FHClDQVcaUMBV9pQwJU2FEhasTI0 NNTV1dXc3NzU1DQyMgInUigUNzc3Dw+PGTNmmJmZyRT5/fffKysrY2NjSSTt+CBlbGwMAAACgaAy JxxvQyKR5DOLxWIIgjQ0olcQNIkuEolE1dXVJSUl9+/fb25uZrPZIAjK5KHT6b6+vosWLYqMjPT2 9jYyMoLTY2Njnzx5UlpaamxsrL77cvT29h45coTFYgmFQolEYmRkpFAAiURCIBCoVKqVldWBAwdm zpyJPMvhcA4fPtze3i4SicRisXIjZDLZ3Nw8KSnJ29tbixeiddRUWiQSVVZWZmdn37x5k8PhAABA oVDc3d19fX0ZDAaVSgUAQCwWNzc319bWvnjxYnh42MHBITQ09IsvvnB1da2qqoqJiXFycrp3756l paUWr0cgENTV1XV3d7e3t5eUlNy5c0cikchnCwgICA8P9/b2njp1qq+vL41Gk7k62EhHR8eNGzfu 3r0rEonkjfj6+kZGRjIYDEdHRz8/P+1eiPaBsNPS0rJ582bphZmbm0dFRV2/fp3FYkkkEpnMXC63 srIyPj7e0dERAAArKys3Nzdzc3MAANzd3VkslhoOoGR0dDQtLU3+nbFu3bqenh6URvh8fmZmJuww 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|
592,9
|
0,09
|
0,0002
|
-
|
и-![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAKMAAABWCAIAAAAsUbF9AAAP70lEQVR4nO2deVgT197HJyELS9gM m1QUlDVsPlILtdadovS5LFqtG6W1j4oLgqmCCG5Xq6jYWq5e4IL6FutboC0UN9RHEdCCBfV9ZKmK LLIHiJCwZCOZef+Ye3OnSUhmsmBo5vMXc+ac3/lNvrOc5XcOBAiCABwDgPi2HcCZIHClDQVcaUMB V9pQwJU2FHClDQVcaUMBV9pQwJU2FHClDQVcaUMBV9pQwJU2FHClDQVcaUMBV9pQwJU2FEhasTI0 NNTV1dXc3NzU1DQyMgInUigUNzc3Dw+PGTNmmJmZyRT5/fffKysrY2NjSSTt+CBlbGwMAAACgaAy JxxvQyKR5DOLxWIIgjQ0olcQNIkuEolE1dXVJSUl9+/fb25uZrPZIAjK5KHT6b6+vosWLYqMjPT2 9jYyMoLTY2Njnzx5UlpaamxsrL77cvT29h45coTFYgmFQolEYmRkpFAAiURCIBCoVKqVldWBAwdm zpyJPMvhcA4fPtze3i4SicRisXIjZDLZ3Nw8KSnJ29tbixeiddRUWiQSVVZWZmdn37x5k8PhAABA oVDc3d19fX0ZDAaVSgUAQCwWNzc319bWvnjxYnh42MHBITQ09IsvvnB1da2qqoqJiXFycrp3756l paUWr0cgENTV1XV3d7e3t5eUlNy5c0cikchnCwgICA8P9/b2njp1qq+vL41Gk7k62EhHR8eNGzfu 3r0rEonkjfj6+kZGRjIYDEdHRz8/P+1eiPaBsNPS0rJ582bphZmbm0dFRV2/fp3FYkkkEpnMXC63 srIyPj7e0dERAAArKys3Nzdzc3MAANzd3VkslhoOoGR0dDQtLU3+nbFu3bqenh6URvh8fmZmJuww 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BwiC6enptbW1y5Ytkz87PDSUmZlJpRrv3LlDu4sxJx46nS6zumA82P39dbV1TCbTxcVlvDxr1671 9fWB/+bzeG1yrbbxUK20vb19UlIScgkan89PTU1taWlBWYdCCgoK0tPTmUymwuUBt27fevDwIY1m 9uzZs4qKCunHSXMEAoHmgz9CoRDD6hPUjVcJCK5btz7sb39TkoduYxMUGCg9hFAP6aBq9C9fvnzL li3IHkJtbe3+/fsHBgZQViPDr7/+ymQyP/300zVr1sif5fP5ud/nikQiFou1e/fu0NDQpcuW7dy5 s6ysTPM5pTdv3mgeejw4OKiLCDhHR8fklGRbW1vl2aZPnwH/QSKTbehoR7FQKU0mk5OTk6XrqWAK Cgp27dr1+vVrlDVJKSoqiomJ8ff3T0lJUfhaKy8rKysvlx6Ojo7W19WdP38+PDz8888/f/LkKdYa kaB/CHRtRG2IxH+/JaZYT5k1a6byzP8thTKftbV1eno68hGEIOjKlSurVq0qLi5G+ZRwudy0tLTN mzd7eXmdO3dO4c0rEAhyc3MVtviGhoby8vJWroy8cPEiypfn2NiYzNIvPp+P9cUAgiCLxZJx8i2u Sejp+bcz7733nsxuDspA2UaH6e3t3bRpk8yDaGZmFhkZefXq1fGWvYMg2NXVlZ+fHxwcTKFQwsLC 4GgWhQiFwqqqqvz8/IyMDCaTGRISAi+x/1ONNNqxr79G08tqa2uTWW5Co9Hu3buH6aq7u7sZDAbS CJVKLSoqQlm8oqLc1MQELqiyl6USHo+3bOlSAAAoVOqPP2Lo7mJeKT86OpqVleXh4SHz61OpVB8f ny+//DItLS0vL6+goKCgoCA/P//MmTPR0dEeHh5EItHS0vLgwYPjdaAVIhAI/vjjj2/OnPHx8ZER 7NKlS8rLdnd379ixQ34AcsGCBVVVVSh71SwWKzY2Vn6Wc+7cuWVlZQKBQKUF7Sr9f0+f2trYAACw 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Tk5i4r6QkOXnz59TuDUB3OkoLi7eumWrWCxBEyGqX6FYPB4vYe/eXwoLjY2NwyMidsfHz5gxA5mh 8eXL7Tu2P3/x4kRqakRE+NvyExN8Hk/hHuMKEYvFF3JyEvcl8vkCoUiYkpICKZoL53K5LS0tz58/ HxsbO3n6NKplZmoP2eiC169b4fBmGD8/v2+//fbZs2cdHR01NTWnTp3y9PR0dHTMyvoX/N8TJgUZ Gf+UXtFn0dFKcvL5/L8fOYJpCN3Pzx/l1sb6pbRQIIiL2yUzzzhlyhQnJydzc3MajRYREfHo0aO3 7aZqJBJJb2/vy5cvr169Onu2v/Ra4ICO+vr67u5umWlTgUCQkpyMdT1KQmIiCIJoXNLo/3DoAi6X k5X1r6Kiovb2djjyxMzMzMnJKTAwMCws/P33g0z+M4asz/B4vNzc3NevX7PZbB6PJ51tgyCITCbb 2tra2dtHbdyIXCAxMDDw9yNH+tls9LUYGZHi4+OQG+srQe+UhhkaGurr64N3ILSwsLC1tZX//wh6 DtyilJmnBxCfSzU21tEEPVUaR+voXS8LR0fgShsKuNKGAq60oYArbSjgShsKuNKGAq60oYArbSjg ShsKuNKGAq60ofD/n0Dh6/HGH5AAAAAASUVORK5CYII=)
|
619,6
|
0,43
|
0,0007
|
-
|
н-
|
626,2
|
0,09
|
0,0001
|
-
|
|
-
|
100,00
|
0,1918
|
521,4
|
Таблица В.2 - Пример расчета плотности СУГ при температуре 20°С через молярные доли
|
|
|
|
|
Компонент
|
Плотность ,
кг/м
|
Молярная доля
|
|
, кг/м
|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAHgAAABSCAIAAAAQMYfVAAALDklEQVR4nO2cf1ATZxrH390kGiBo QIkiEiaoMe1IcByUnuIB/qhk/NHDGUegZ9XRKbb84Zw458wJVipq1FGnM8f0Tp3ioU6lkTLUH+fo tVLbGS0mNQMUhQApRBPUmJAQEgib3ftjpzvrxmw2Iayi+/lvn33f53n3m3fffd93nw2EYRjgGHvg V92AtwVOaJbghGYJTmiW4IRmCU5oluCEZglOaJbghGYJTmiW4IRmCU5oluCEZglOaJbghGYJTmiW 4IRmCX5EvKAo6nA4zGZzb2+vy+XCjQKBICUlRSqVxsXFwTD1F+3u7tZqtevXr+fzI9OG15zRXqTJ ZLp9+/bNmzebm5tNJpPdbvf5fPgpCIJiY2OlUmlmZuayZcuWL18+bdo0oqJGo6mrq1OpVLGxsbhF p9N9/fXXPp8PwzAYhv1/Gxy8AAAgNTW1uLh44sSJ5LMPHz6srq72er30TlAURVEUAJCYmPjpp58S bRg7whe6p6fnwoULNTU1nZ2duLhisVipVMrlcvzifT5fT0+PwWCorq6urq5OS0srKCgoKChITk5+ 8OBBTU0Nn89HEIRwKBaL5XK52Wxua2trbGx89uyZf1AIghQKRXZ29uzZs2Uymb+OIpFo7ty5jx49 evjw4a1bt/r6+l7a+FmzZuXk5KSmps6aNYulWwoLnYGBgS+++EIul0MQBACAYTgjI+Pw4cP37t2z 2WwoihIlXS5XR0fHuXPnVCpVdHQ0AGDOnDkqlWrOnDkAgJSUlJ6eHn//CII0NTUtWbKE0lQYhktK SiwWC5NG+ny+5uZmlUrlf8nbtm17adwxJWSh29vbN27cKBAI8EZLJJLKysq+vj76Wm63W6PRKJVK 8gUnJycbjcZAVa5duyYUCsnl09PTGapMcPfu3bi4OLITmUzW2dkZkpOIEJrQOp1uwYIFRKPlcvmN GzfIXZie9vb2nJwcorpYLNbpdIEKG41GqVRK1mjTpk3MY+FYrda0tDSyk7y8vOHh4ZCcRIQQpnd6 vX7btm2//vorfpiSknLq1KmVK1fiAwgT5HL56dOns7Ky8EMEQUZGRgIVFgqFlAedSCRiHgtnwoQJ UVFRZEtMTMwrmecwFdpkMu3cuVOv1+OHQqHws88+y87ODjXe7Nmzjxw5MmPGDADA8PDwS594gQhV 5bFzEgaMhPZ4PPv27bt9+zZh2bBhQ2FhYXghFy9evGvXLgiCfD7f8PAw84rTp08PLyKZadOmBZrz jSmMQjY0NNTW1hKHYrF4x44dlCdVSBQVFaWnp6Mo+vz5c+a1KINAeETESRgEF9pisRw/ftzj8RCW VatWZWRkjCZqYmLili1bAABOp3M0fsYRwYXWaDQ6nY44FAgEGzZsmDBhwigDf/DBB1Kp1GazjdLP eCGI0Dab7eLFixgp41Qmk2VmZo4+sFQqXbJkidVqHb2rcUGQic5PP/1E7s4AAKVSmZiYOPrAMAxv 2bLFbDaP3tW4IIjQjY2NXq+XbJk/fz6Px4tI7Pfffz8ifsYFdEOH3W7/+eefyRY+n09ZaHEwhE7o np6e7u5usiU6Ojoik9m3EDqhjUajw+EgW0Qi0ZQpU8a4SW8mdGO0wWAgdvFxxGLx5MmTx7hJAUEQ BEVR8hY2PRAEeb1efIP/lUMntP9GBI/HeyXrV5yvvvrq1q1bWChfNyEI0tHRMXZNYs54el9nMBgM BsOrbkWYjCehCwsL165dSxnNaIAgyO12q9VqyiP9lTCehF6wYEGoW4YDAwNnzpx5HYSmG3BfOsEI aYjkIKDr0ZS3bQCA/v7+gYEBboaHIMjjx4+9Xu/kyZMlEgmTKnQ9WiaTUTadnU7n27MNRMO1q1dz c3MXL1588NAhhlXohFYoFJT9o4GBgfH73I8URqOx4vPPjUaj1Wrt7+9nWItOaIlEgidgEKAoSrw2 fDvxer1q9WHiDTVz6IQWCoW5ubkUY1NT0+DgYKhh3hg033xz4fyFMCoGWeatW7du5syZZMv9+/ff 2k794EHbgQMHhoaHeaEvj4NUUCgUK1euJFscDkdDQ0OoYQJx+fLlK1euRMrbmOJyuSr2V3R1dxcU FIr95mNBCSI0DMNbt25NSEggG2tra1taWkKN5I9ery8rKyO/9n2dOVtdfamubs2atZ98sgMOPTkk +C2QlZW1fft2sqW3t/fEiRMhpWT4Y7FYSktL582bt27dOoZVIrJWCs/Jvaamw2p1cnLy/or98XFx YTgJLjQEQSUlJQsXLiQba2trz58/H2owArvdvmfPHovFsnfvXkreFw1PnjwJOyLB06dPQ5XJZrPt r9hvtVrLysvTlUpfWPuujAb1pKSko0ePkp+KHo+nvLy8vr4+jJD9/f2lpaVXr149ePDgu+++y7yi 2+0OI5y/k5CExjDsX19++d9r14uKPvywqCj8wMzzIS9evEhO2QcASCSSY8eOOZ1O5k5MJtOmTZti YmKOHz+O5+4Hore3VyaTkcMVFxczD4Rjs9nmz59PdpKfn48gCHMP/7t5Mz4+Pi0trbOrC7e0tLRM /WMT4qPNmxn6CS1tV6PRUNaKAoFg9erV169fHxoaoq/rdru/++67hQsXRkdHHz16FP/6gYZffvll 0qRJ5FgqlSrUjNu2tjZK51i0aJHD4WBYvc9iWZqVJRKJ6uq+JYxsCI1h2Pfff5+ZmUnJyYyNjV29 enVVVZVer3/27JnH4xn6A6vVqtfrq6qq8vLyhEKhVCqtqakJqjKKomVlZZSbTyKRNDY2Mm8qiqJq tdq/qfX19UyqIwiye3cpAOBvu3aNjIwQdpaExjDMbDaXl5dTFjIAAAiC4uPj582bt2zZshUrVqxY sWL58uVKpRLfBYyKisrPz9dqtYHcOp1O/B3KnTt3du/eTenOODKZTK1W6/V6g8FgMpn889IHBwdx J1qttqysTCwW+ztJTEzct2+fVqs1GAy///57oJGk/ttvY2NFWVlLzS9+ZhCe0BAW1nQHRdH29va6 urqGhoaOjg6aXEUIgqZPn7506dKtW7dmZ2fTJHP+8MMPJ0+eBAC4XC673Q5elsuMoigMwwkJCQKB QKFQVFZWUhzqdLrKykoEQdxut81mwzDspU4gCJo6dapQKExKSjpy5Ij/72E0duf/Jf+x2XLp0qXs 7D+TT7W2tubm5FifPwcAfLR583/Ong10RS/oEJ7QBHa7vaOjQ6vVdnZ2dnV1uVwu/MIwDJsyZco7 77yjUCgyMjJkMhnx2UsgvF4v/o0iBEH06eJ4H+Hz+f69fmRkxOVy4foyccLj8SZNmkQpOTw0VFJS Un327MGDh/bs+TvlbHhChzN0BMLr9XpIhPRwf62oqamZOHHimjVr7f39/mfDGzoi+c5QIBAE7bav P7+1tn5eUTEjKamyslIcPImF6Vp8PL2cZYHBwcEDBw50dnV9/HGx0+n48ccfKQVgGO7q6iK+cXrS 14eXwTBMKk1JTZVRPRJE8I57A/ittTVh6lQAgFAojAoAec+Ax+PhRoFA8I+9e2k8cz36BXwoim9l DA0NMSrv8xG7jyMv5jdT4IR+gZiYmD+9916/wxFoxgJB0KDL1dzSgqcASiQSuVwOAPD5fDJZKo3n 0U7v3jAwDMP3EgIV4PF4Lc3NeXl5z202AEDRh389ferf+Cn6uQDXo18AgqCg38cJo6KI/s7n8/A/ EwgK9w80LMEJzRKc0CzBCc0SnNCjhFuCjxkzZ878Z1UVPgukpMzRwM2jWYIbOliCE5olOKFZghOa JTihWYITmiU4oVmCE5ol/g8GVyCZczhm4QAAAABJRU5ErkJggg==)
|
277,6
|
0,0011
|
0,3054
|
-
|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAPZklEQVR4nO2ceVRTVx7HbxZCCBDZ ggJBWSQBA8GitSJo0aEM9KjYwQVoRaEKpwj2CG5wtAcdbW21i9o6rbZjq1iVg5y6QYEqQu0wbKVV URASUrZAgLCTkJD35o9o+hrI8rIAb8znr+Tm3t/95X3fu+vvPhwMw8AEdsBPtwMm0GESDGOYBMMY JsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjEE0iJWh oaH29nYOh9PU1DQ0NCRPJJFI8+fPZzAYbm5uVlZWSkV+++234uLinTt3mpubG8QHJDAMj4+PAwBw OJw2mQEAZmZmE3+SSqWojBCJRG0y6wNOnxABqVRaVVVVUFBQUlLS1NTU09Mjk8mU8tjZ2bFYrJCQ kHXr1rHZbCLx2S2yf//+oqKi0tJSa2tr3d1XAYfDOXLkSH9/v0QigSCIQCBMmk0mk+HxeHNzc0dH x6ysrDlz5iB/7ezszMrKEggEY2NjMpmMQCBMKoZMJsPhcCQSycbG5uDBg56engb/O0h0FEwqlZaX l587d+727dt9fX0AADMzMy8vLz8/P19fX/lDI5PJuFzugwcP6uvrBwYGaDRaREREQkICk8msqalJ SkqaNWtWaWmpg4ODgf8TAMPDww8fPuzs7ORyuTdv3iwtLZ00W1BQ0Nq1a5lMppOTE5vNJpPJyF/F YvGDBw/4fD6Px7t161ZJScnE2xEAsGjRosjISG9vb2dnZ39//4ltiYGB0cPj8ZKSkmxsbOQWLC0t Y2Njb9y4wefzZTKZUuaBgYGKiordu3e7uroCAKhUqpeX16xZswAAc+fO/eOPP3RwABX9/f0ZGRmK 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501,1
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325,0135
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|
578,9
|
0,2017
|
116,7641
|
-
|
нео-![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAKMAAABWCAIAAAAsUbF9AAAP70lEQVR4nO2deVgT197HJyELS9gM m1QUlDVsPlILtdadovS5LFqtG6W1j4oLgqmCCG5Xq6jYWq5e4IL6FutboC0UN9RHEdCCBfV9ZKmK LLIHiJCwZCOZef+Ye3OnSUhmsmBo5vMXc+ac3/lNvrOc5XcOBAiCABwDgPi2HcCZIHClDQVcaUMB V9pQwJU2FHClDQVcaUMBV9pQwJU2FHClDQVcaUMBV9pQwJU2FHClDQVcaUMBV9pQwJU2FEhasTI0 NNTV1dXc3NzU1DQyMgInUigUNzc3Dw+PGTNmmJmZyRT5/fffKysrY2NjSSTt+CBlbGwMAAACgaAy JxxvQyKR5DOLxWIIgjQ0olcQNIkuEolE1dXVJSUl9+/fb25uZrPZIAjK5KHT6b6+vosWLYqMjPT2 9jYyMoLTY2Njnzx5UlpaamxsrL77cvT29h45coTFYgmFQolEYmRkpFAAiURCIBCoVKqVldWBAwdm zpyJPMvhcA4fPtze3i4SicRisXIjZDLZ3Nw8KSnJ29tbixeiddRUWiQSVVZWZmdn37x5k8PhAABA oVDc3d19fX0ZDAaVSgUAQCwWNzc319bWvnjxYnh42MHBITQ09IsvvnB1da2qqoqJiXFycrp3756l paUWr0cgENTV1XV3d7e3t5eUlNy5c0cikchnCwgICA8P9/b2njp1qq+vL41Gk7k62EhHR8eNGzfu 3r0rEonkjfj6+kZGRjIYDEdHRz8/P+1eiPaBsNPS0rJ582bphZmbm0dFRV2/fp3FYkkkEpnMXC63 srIyPj7e0dERAAArKys3Nzdzc3MAANzd3VkslhoOoGR0dDQtLU3+nbFu3bqenh6URvh8fmZmJuww 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|
592,9
|
0,0008
|
0,4743
|
-
|
и-![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAKMAAABWCAIAAAAsUbF9AAAP70lEQVR4nO2deVgT197HJyELS9gM m1QUlDVsPlILtdadovS5LFqtG6W1j4oLgqmCCG5Xq6jYWq5e4IL6FutboC0UN9RHEdCCBfV9ZKmK LLIHiJCwZCOZef+Ye3OnSUhmsmBo5vMXc+ac3/lNvrOc5XcOBAiCABwDgPi2HcCZIHClDQVcaUMB V9pQwJU2FHClDQVcaUMBV9pQwJU2FHClDQVcaUMBV9pQwJU2FHClDQVcaUMBV9pQwJU2FEhasTI0 NNTV1dXc3NzU1DQyMgInUigUNzc3Dw+PGTNmmJmZyRT5/fffKysrY2NjSSTt+CBlbGwMAAACgaAy JxxvQyKR5DOLxWIIgjQ0olcQNIkuEolE1dXVJSUl9+/fb25uZrPZIAjK5KHT6b6+vosWLYqMjPT2 9jYyMoLTY2Njnzx5UlpaamxsrL77cvT29h45coTFYgmFQolEYmRkpFAAiURCIBCoVKqVldWBAwdm zpyJPMvhcA4fPtze3i4SicRisXIjZDLZ3Nw8KSnJ29tbixeiddRUWiQSVVZWZmdn37x5k8PhAABA oVDc3d19fX0ZDAaVSgUAQCwWNzc319bWvnjxYnh42MHBITQ09IsvvnB1da2qqoqJiXFycrp3756l paUWr0cgENTV1XV3d7e3t5eUlNy5c0cikchnCwgICA8P9/b2njp1qq+vL41Gk7k62EhHR8eNGzfu 3r0rEonkjfj6+kZGRjIYDEdHRz8/P+1eiPaBsNPS0rJ582bphZmbm0dFRV2/fp3FYkkkEpnMXC63 srIyPj7e0dERAAArKys3Nzdzc3MAANzd3VkslhoOoGR0dDQtLU3+nbFu3bqenh6URvh8fmZmJuww 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Tk5i4r6QkOXnz59TuDUB3OkoLi7eumWrWCxBEyGqX6FYPB4vYe/eXwoLjY2NwyMidsfHz5gxA5mh 8eXL7Tu2P3/x4kRqakRE+NvyExN8Hk/hHuMKEYvFF3JyEvcl8vkCoUiYkpICKZoL53K5LS0tz58/ HxsbO3n6NKplZmoP2eiC169b4fBmGD8/v2+//fbZs2cdHR01NTWnTp3y9PR0dHTMyvoX/N8TJgUZ Gf+UXtFn0dFKcvL5/L8fOYJpCN3Pzx/l1sb6pbRQIIiL2yUzzzhlyhQnJydzc3MajRYREfHo0aO3 7aZqJBJJb2/vy5cvr169Onu2v/Ra4ICO+vr67u5umWlTgUCQkpyMdT1KQmIiCIJoXNLo/3DoAi6X k5X1r6Kiovb2djjyxMzMzMnJKTAwMCws/P33g0z+M4asz/B4vNzc3NevX7PZbB6PJ51tgyCITCbb 2tra2dtHbdyIXCAxMDDw9yNH+tls9LUYGZHi4+OQG+srQe+UhhkaGurr64N3ILSwsLC1tZX//wh6 DtyilJmnBxCfSzU21tEEPVUaR+voXS8LR0fgShsKuNKGAq60oYArbSjgShsKuNKGAq60oYArbSjg ShsKuNKGAq60ofD/n0Dh6/HGH5AAAAAASUVORK5CYII=)
|
619,6
|
0,0036
|
2,2306
|
-
|
н-
|
626,2
|
0,0007
|
0,4383
|
-
|
|
-
|
1,0000
|
521,3252
|
521,3
|
Приложение Г (обязательное). Значения летучести (фугитивности) компонентов сжиженных углеводородных газовПриложение Г
(обязательное)
В таблицах Г.1-Г.8 приведены значения летучести (фугитивности) компонентов СУГ при различных температурах.
Таблица Г.1 - Значения летучести (фугитивности) компонентов СУГ при температуре плюс 45°С
|
|
|
|
|
|
|
|
|
|
|
|
|
Дав-
|
Летучесть углеводородов
|
ление,
МПа
|
|
|
|
|
|
|
|
|
|
|
|
|
0,1
|
13,200
|
4,000
|
5,600
|
1,250
|
1,500
|
0,550
|
0,410
|
0,360
|
0,200
|
0,130
|
0,170
|
0,045
|
0,5
|
14,000
|
4,200
|
5,700
|
1,370
|
1,550
|
0,600
|
0,450
|
0,410
|
0,210
|
0,150
|
0,190
|
0,053
|
1,0
|
15,000
|
4,400
|
6,200
|
1,450
|
1,650
|
0,660
|
0,480
|
0,450
|
0,240
|
0,170
|
0,210
|
0,060
|
1,5
|
15,500
|
4,700
|
6,500
|
1,530
|
1,730
|
0,690
|
0,510
|
0,480
|
0,260
|
0,180
|
0,230
|
0,063
|
2,0
|
16,400
|
5,000
|
7,000
|
1,680
|
1,920
|
0,760
|
0,560
|
0,540
|
0,280
|
0,200
|
0,240
|
0,072
|
Таблица Г.2 - Значения летучести (фугитивности) компонентов СУГ при температуре минус 20°С
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|
|
|
|
Дав-
|
Летучесть углеводородов
|
ление,
МПа
|
|
|
|
|
|
|
|
|
|
|
|
|
0,05
|
15,0
|
1,40
|
2,50
|
0,260
|
0,33
|
0,075
|
0,0450
|
0,060
|
0,0130
|
0,0090
|
0,009
|
0,0010
|
0,10
|
13,0
|
1,15
|
2,10
|
0,235
|
0,28
|
0,068
|
0,0425
|
0,054
|
0,0125
|
0,0089
|
0,011
|
0,0018
|
0,50
|
11,5
|
1,15
|
2,00
|
0,245
|
0,29
|
0,075
|
0,0435
|
0,062
|
0,0150
|
0,0103
|
0,013
|
0,0025
|
1,00
|
9,6
|
1,16
|
1,90
|
0,250
|
0,29
|
0,079
|
0,0500
|
0,064
|
0,0150
|
0,0115
|
0,014
|
0,0026
|
1,50
|
10,5
|
1,26
|
2,10
|
0,277
|
0,32
|
0,090
|
0,0585
|
0,075
|
0,0188
|
0,0140
|
0,018
|
0,0036
|
2,00
|
11,0
|
1,40
|
2,30
|
0,300
|
0,37
|
0,106
|
0,0680
|
0,088
|
0,0220
|
0,0160
|
0,022
|
0,0040
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Таблица Г.3 - Значения летучести (фугитивности) компонентов СУГ при температуре минус 30°С
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Дав-
|
Летучесть углеводородов
|
ление,
МПа
|
|
|
|
|
|
|
|
|
|
|
|
|
0,05
|
13,3
|
1,10
|
1,93
|
0,180
|
0,227
|
0,0500
|
0,0283
|
0,039
|
0,0083
|
0,0053
|
0,0063
|
0,0006
|
0,10
|
11,3
|
0,89
|
1,70
|
0,165
|
0,193
|
0,2490
|
0,0268
|
0,036
|
0,0075
|
0,0052
|
0,0069
|
0,0008
|
0,50
|
9,7
|
0,90
|
1,63
|
0,173
|
0,210
|
0,2767
|
0,0285
|
0,042
|
0,0090
|
0,0066
|
0,0087
|
0,0012
|
1,00
|
8,5
|
0,91
|
1,53
|
0,177
|
0,213
|
0,0540
|
0,0320
|
0,044
|
0,0097
|
0,0070
|
0,0093
|
0,0013
|
1,50
|
9,3
|
1,00
|
1,70
|
0,202
|
0,237
|
0,0620
|
0,0388
|
0,051
|
0,0116
|
0,0087
|
0,0112
|
0,0021
|
2,00
|
9,9
|
1,07
|
1,83
|
0,228
|
0,270
|
0,0740
|
0,0467
|
0,060
|
0,0147
|
0,0104
|
0,0167
|
0,0026
|
Таблица Г.4 - Значения летучести (фугитивности) компонентов СУГ при температуре минус 35°С
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|
|
|
|
|
|
|
|
|
|
|
Дав-
|
Летучесть углеводородов
|
ление,
МПа
|
|
|
|
|
|
|
|
|
|
|
|
0,05
|
12,50
|
0,950
|
1,65
|
0,140
|
0,175
|
0,038
|
0,020
|
0,029
|
0,006
|
0,0035
|
0,0049
|
0,10
|
10,50
|
0,760
|
1,50
|
0,130
|
0,150
|
0,034
|
0,019
|
0,027
|
0,005
|
0,0033
|
0,0048
|
0,50
|
8,75
|
0,775
|
1,45
|
0,137
|
0,170
|
0,040
|
0,021
|
0,032
|
0,006
|
0,0047
|
0,0065
|
1,00
|
8,00
|
0,790
|
1,35
|
0,140
|
0,175
|
0,042
|
0,023
|
0,034
|
0,007
|
0,0048
|
0,0067
|
1,50
|
8,70
|
0,870
|
1,50
|
0,165
|
0,195
|
0,048
|
0,029
|
0,039
|
0,008
|
0,0060
|
0,0078
|
2,00
|
9,40
|
0,900
|
1,60
|
0,192
|
0,220
|
0,058
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0,036
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0,046
|
0,011
|
0,0076
|
0,0102
|
Таблица Г.5 - Значения летучести (фугитивности) непредельных углеводородов СУГ при температуре плюс 45°С
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|
|
|
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Давление,
МПа
|
Этин (ацетилен),
|
Пропадиен (аллен),
|
Пропин (метилацетилен),
|
Бутадиен-1,3 (дивинил),
|
0,1
|
6,000
|
0,980
|
0,760
|
0,430
|
0,5
|
6,250
|
1,100
|
0,850
|
0,490
|
1,0
|
6,900
|
1,150
|
0,900
|
0,540
|
1,5
|
7,050
|
1,230
|
0,930
|
0,570
|
2,0
|
7,380
|
1,340
|
1,040
|
0,620
|
Таблица Г.6 - Значения летучести (фугитивности) непредельных углеводородов СУГ при температуре минус 20°С
|
|
|
|
|
Давление, МПа
|
Этин (ацетилен),
|
Пропадиен (аллен),
|
Пропин (метилацетилен),
|
Бутадиен-1,3 (дивинил),
|
0,05
|
2,500
|
0,190
|
0,120
|
0,059
|
0,10
|
2,200
|
0,165
|
0,104
|
0,049
|
0,50
|
2,300
|
0,175
|
0,115
|
0,058
|
1,00
|
2,100
|
0,170
|
0,125
|
0,060
|
1,50
|
2,400
|
0,200
|
0,143
|
0,068
|
2,00
|
2,640
|
0,230
|
0,168
|
0,080
|
Таблица Г.7 - Значения летучести (фугитивности) непредельных углеводородов СУГ при температуре минус 30°С
|
|
|
|
|
Давление, МПа
|
Этин (ацетилен),
|
Пропадиен (аллен),
|
Пропин (метилацетилен),
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Бутадиен-1,3 (дивинил),
|
0,05
|
2,200
|
0,130
|
0,080
|
0,035
|
0,10
|
1,800
|
0,120
|
0,080
|
0,033
|
0,50
|
2,250
|
0,130
|
0,090
|
0,038
|
1,00
|
1,700
|
0,130
|
0,080
|
0,040
|
1,50
|
1,840
|
0,140
|
0,100
|
0,048
|
2,00
|
2,000
|
0,170
|
0,120
|
0,060
|
Таблица Г.8 - Значения летучести (фугитивности) непредельных углеводородов СУГ при температуре минус 35°С
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|
|
|
|
Давление, МПа
|
Этин (ацетилен),
|
Пропадиен (аллен),
|
Пропин (метилацетилен),
|
Бутадиен-1,3 (дивинил),
|
0,05
|
1,800
|
0,090
|
0,070
|
0,026
|
0,10
|
1,500
|
0,082
|
0,057
|
0,025
|
0,50
|
1,700
|
0,090
|
0,063
|
0,029
|
1,00
|
1,350
|
0,095
|
0,065
|
0,031
|
1,50
|
1,640
|
0,113
|
0,078
|
0,038
|
2,00
|
1,760
|
0,130
|
0,092
|
0,042
|
Приложение Д (рекомендуемое). Пример расчета давления насыщенных паров при температуре плюс 45°С методом последовательного приближенияПриложение Д
(рекомендуемое)
Задают произвольные значения абсолютного давления насыщенных паров и .
Принимают 1,5 МПа и 2,0 МПа.
При выбранных значениях давления насыщенных паров согласно данным таблиц Г.1, Г.5 (приложение Г) выбирают значения летучести и рассчитывают по формуле .
Расчет приведен в таблице Д.1.
Таблица Д.1 - Расчет при 1,5 МПа и 2,0 МПа
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|
|
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Компонент
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Молярная доля
|
при 1,5 МПа
|
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IR49epSYmFheXu7HZudeuzbp+QOpVNra2trQ0NDW1rZx4yam2nZ/GrGzszt06FB9/SY+v7OysuL7 7y8nJ7+jlOfWrVvVNTUEIjE1JTUwcKkGi8a5sXSnrKyU7een/RUhEAjfXbgw3V6rA4Kg7IsX5dHX rq5zi4qKkL+W/+c/TCYDh8NtjY8fGBjUaG1mCVZWWioPBNMeD09PpTXyGQgEQd9fuuTu5gYAcHZ2 fv/99ysqKqqrqt4/epROp8+ysdm3f79SuJ8q9FqtNzjZFy/mFxSgOujw8pIlO1NTp/6tajpQ9+jR +W+/LS4u5vP5FArF3NycTCYHBgZu2hS9YsVyLQMdZpZgLwLC3t7Orq6xsTH5y6HRvvLYJBjGwEBL YgKJSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxj/A21IX6E7EshsAAAA AElFTkSuQmCC)
|
0,0004
|
4,70
|
0,0019
|
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|
0,0265
|
1,53
|
0,0405
|
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|
0,0059
|
1,73
|
0,0102
|
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0,2100
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0,69
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0,1449
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0,3053
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0,51
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|
0,3297
|
0,48
|
0,1583
|
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|
0,0012
|
0,57
|
0,0007
|
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0,0721
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0,26
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0,0187
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RLJ9+zYAAIhE4rVrSANa6gQklUr37NkDX1h8fLwaNQwODsp2O+zs7C5fvqyVeiD4fP7169cjIyPl vt0EI/uehvD09ExLS2Oz2dqeC2JiYuLnmze9vb1lbR764AORSL4lKyoqSkxMPHjwYExMjKpkBBwO 5+npGRcXl5iY+O233yr+AlVVVYmJiYmJievXr1e19BGDwbi4uOzcuTMxMfHChQuKcT8I/QqoqemR ra0NAABvvvXW6CjScC4GVN3vk0qlpaWlcPa7j4+P4jMny7Vr106dOjUxMbFs2bLdu3eryZjWiEAg qK2tLS0tra6uZjAYXC5XNu8Ch8MtWLDA2tra3d09NDTU399f90WobU+f7j9wAE4xsLCwLCoq8vL6 04xNQ0MDvBpJzWoKKIoNAACVSlX8jmJLSwudToe2lSbWyRmxsrIKCgpSOiMkEomio6Nu3foPAABU Kq2iolzNEEc9oFR6+PDh02fO2NrZ3ci74e2N+AO3umhWkYGBAS6Xi2QeACECgYDFYtXX15eUlBS/ 4Ndff2UwGND6Rn2dCATBtra2V7284F/m5Ml/6dH4VKDHFqiGTqdQKAQC8euvL2pVcbZ8I3GWkJ9/ A+4PrYuK0uojjdOPvgQ0PDwcFbUOAIC4uHhtv+85B2Z8ppPQ0LVBgX/Mb7CesbQLCs9NpFLpubS0 goLCdVFRn356VNVCCVWgAvoTBAJhXdQ6qF/C4/GQTAbNdfJ++un0mdPLl/t+kfqFpaWlttVRAcnj 5uY2f74JAADm5uaK2dx/MSorKg4ePLjI0Sk9Pd3BgTYJC6iA5DE1JUOBKCqVqjTX7C9DQ319XHyc kbHxhfMXXFyWTM7IXPqe4/TAGxkRjAswGMyqVavmRFbQ5Ghvb9+7d+/Q8Mi/f/j3P/4hv3APOaiA 5GlqahoeGXF0dApdqy7lfk7T3ta2ffv2p23tFy9e9PNbqaoY9KlkVbOfEH/ZJ2xy8Pn8q1dzQRDc sWMHjUqbaXemhLa2tm3btzU/efL1xa+h0btSxsfHP05Kys+/qcHc5CIHc5Rnz549efJkYED54iGp RHLh/HlDQ8O1YWFcLneafZsEIqEwIjwcuo8I40BPGYzVr79ubW2Tn39TVZnx8XHo44UUCuXBgwfq Df6NXmHlZWV79+17/vy5o6PToUOJkZGRsvkuQqHw26ysj498vHy5b9qXX5qbm8+gqwgRi8X8cS0i Va0tLbt27y4tLXVxWVpQ8HNBwc9Kbfb0dLe0tDKZzMjINzQvktFa9nOW//v0U/iqSSSTTZs2FRbe 6ujoaGtry8+/sWnjxvnz54eHR7S2ts60p0hhs1iLX8xOmi9c2NDQqKYw/f59LWa4AACDwSKZ1vgb Caimhr5o0SLZ38jQ0NDGxoZCoRAIhEWLFp06dWpgYGCm3dQMjzfS1dVFp9MP/vn/acbEvFleXt7R 0aGYTkS/f3/x4sXI1QMAgI3a9GUYdbPxfz3u3bt3/ty53+vqoBlfHA5nbm7u4uISHBwcHh6uy//o mE4qKyru3L3b398PrQSH94MgSCaTFy5cuGLFyrV/HkJeu3o178YNrb474OHhkZiYqPEfd/y9BAQA gFgs5nK5XC5XLBbj8XgLCwtzc/O59f9NQBCUSqWYFyg9NG0RrL+dgFD0CxoHQtEJVEAoOoEKCEUn UAGh6AQqIBSdQAWEohOogFB0AhUQik6gAkLRCVRAKDqBCghFJ1ABoejE/wM9xkv0z4dvbwAAAABJ RU5ErkJggg==)
|
0,0191
|
0,18
|
0,0034
|
|
0,0298
|
0,23
|
0,0069
|
|
1,0000
|
-
|
0,5412
|
Так как при 1,5 МПа получают 0,54 МПа, следовательно, условие не выполняется, расчет прерывают.
Задают следующую пару значений абсолютного давления насыщенных паров и и повторяют процедуру.
Принимают пару значений 1,0 МПа и 1,5 МПа и возобновляют расчет (см. таблицу Д.2).
Таблица Д.2 - Расчет при 1,0 МПа и 1,5 МПа
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Компонент
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Молярная доля
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при 1,0 МПа
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![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAPZklEQVR4nO2ceVRTVx7HbxZCCBDZ ggJBWSQBA8GitSJo0aEM9KjYwQVoRaEKpwj2CG5wtAcdbW21i9o6rbZjq1iVg5y6QYEqQu0wbKVV URASUrZAgLCTkJD35o9o+hrI8rIAb8znr+Tm3t/95X3fu+vvPhwMw8AEdsBPtwMm0GESDGOYBMMY JsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjEE0iJWh oaH29nYOh9PU1DQ0NCRPJJFI8+fPZzAYbm5uVlZWSkV+++234uLinTt3mpubG8QHJDAMj4+PAwBw OJw2mQEAZmZmE3+SSqWojBCJRG0y6wNOnxABqVRaVVVVUFBQUlLS1NTU09Mjk8mU8tjZ2bFYrJCQ kHXr1rHZbCLx2S2yf//+oqKi0tJSa2tr3d1XAYfDOXLkSH9/v0QigSCIQCBMmk0mk+HxeHNzc0dH x6ysrDlz5iB/7ezszMrKEggEY2NjMpmMQCBMKoZMJsPhcCQSycbG5uDBg56engb/O0h0FEwqlZaX l587d+727dt9fX0AADMzMy8vLz8/P19fX/lDI5PJuFzugwcP6uvrBwYGaDRaREREQkICk8msqalJ SkqaNWtWaWmpg4ODgf8TAMPDww8fPuzs7ORyuTdv3iwtLZ00W1BQ0Nq1a5lMppOTE5vNJpPJyF/F YvGDBw/4fD6Px7t161ZJScnE2xEAsGjRosjISG9vb2dnZ39//4ltiYGB0cPj8ZKSkmxsbOQWLC0t Y2Njb9y4wefzZTKZUuaBgYGKiordu3e7uroCAKhUqpeX16xZswAAc+fO/eOPP3RwABX9/f0ZGRmK J1sOHo9PTk7u7e3V0sjw8PBHH32kpCgAYOvWrV1dXUb1XwnUghUWFi5evFjh8cKFC/Py8sRiscaC v/766xtvvIFsVZydnZuamnRyGx3t7e3z589HXmg6nd7Y2IjKSH9/P/KPAwBsbW2rq6uN5LMq0AmW m5vr5OSk8Dg0NLShoUH74kKh8O2338bjnw1NqVRqVVUVSod1QSwWh4aGIq/1smXLhoeHURmBICg6 OhppxMfHRyAQGMlnVaAY1l+/fj0lJYXP58u/vvLKK1999RWDwdDegq2t7YkTJ2JiYuRfZTKZRCLR vrjO4PF4pUGgmZmZqpGIKuQjC2QKkUhEa0R/tBWssrIyPT29s7NT/tXBweGDDz7w8PBAW5+Njc3h w4cXLlwIABCLxQKBAK0Fg2CQ8TeRSFS0FlOGVvV1d3fv27ePw+HIv+JwuKSkpFdffVW3Kj08PDIy MshkMgRB8onO1DN79mylx0UHaDQahUIxiD/ao1kwGIa/+eabsrIyRQqdTt+8ebM+N9frr7++fPly GIa7urp0NqIPBnnCVM3MjIrmi15XV3fmzBkIghQpUVFRXl5e+tRqZWWVmJhIIpFGR0f1sfMCokEw GIazs7NbW1sVKZaWlpGRkfq33StXrmQwGIohjAkt0XDdeTzetWvXkCne3t7+/v76V2xvb79q1aqR kRH9Tb1QaFj8LSkpUYw15Pj7+yvWOPQkJSVFKBQaxNSLgzrBZDJZSUkJ/NfFxoCAAEP1tHp2hC8m 6prErq6uiooKZIq5uTmqmbIJg6NOsObm5o6ODmSKpaWlo6OjkV0yoQ51gnG5XKVht7W1ta2trZFd mgp0a9WnftY1EXV9mHwpHZlCpVKNvt8zJfT29tbW1upQyhjOoEKdYP/Hs9rCwkJVu5pqEIvFxnAG FYaJ6cAc5ubmDg4OqJo4GIa7u7una/FTwQsqWHh4+MmTJ9GWevfdd3Nzc43hj/aoE2ziZs9M6HUN AoVCcXZ21qGUMZxBhbpRInJzWY5EIpGHj5mYLtQ9Yba2tjjcX8Kq+vr6+vr6pnIq1tHRUVdX9/Tp U5FIRCKR3NzcfH193d3d/2+edbFY3NLS0tTY2MThiEQiKyur6Ohoe3t7VfnVCcZisWxsbORRbHIG Bwc7OjqYTKYhXVZBb2/v1+fOXczO5nA4iuEZkWhGp7usXr1mx44d3t5T4YbxaG5uvnnzZn5+fl1d nYWFhY+PD4vFmjNnDpE4SUjrn6iJ9+jp6WGz2Ur5T506ZfRAExjmcjlrVq9W8xh5e/vk5+draU0i kURERCCLx8XF6eBVXFwc0khERIREItHBzsDAwMnPPmMyGAAAJtP71OnTjY2NWppSJ5hMJlNyEQCw detWCIJ08FJ7+vv7o6L+Ia/O2trax8dn6dKlnp6eSpv6rq5z7927p43BGSXY47q6N9atIxAIBAIh Pj4ebbSdhjC33NxcpcvEZDLb2trQeomKk599hsfjqVTqO8nJZWVlXV1dQ0NDra2tOTlXlwcHI51Z vnxFT0+PRoMzR7A7d37y8/UFAFhYUI4cOToyMoLWBw2CCYXCJUuWIL0kEonZ2dloq1HF4OCgUChE pnQLBP7+bCcnp5ycHKlUqpS/tbV1zZo1SGcuX76isZYZIlhxUZG7uzsAwMzM7PA//6lbc6phx9nW 1nbjxo3IgIDx8fFLly4ZZKdYJBLt2bPnwoULyMT/VlRwOc1Zhw5t2LBBKb4aAECn0z/99NMFC3wU zhQVFUEQBl75+PPPZYlJic3NzQCAuC1b0nbtmvS8jEY0h2Zs3rw5MDAQmXL37t28vDwdKkMCw/DZ s2d/+eUXpXv/57KypYGBb8bGqiro6em5JW6LYjjC4/EkkjE9nTE2PB4vbVdaczMPAMD29z944ICl paVupjQL5ujomJmZSaVSFSljY2PHjh1rbGzUrUo5N27cOHbsWGpqKnJHFIZhBoORnp6u/v8ELw9W ZIB1On0jEomQcWC6IRaLtVlGkEjGPvzwWHVNDQCATCbv3bN33rx5uteqTbspkUj27t2rFCkVFRXV 3d2tQysMw3BBQYGrq+u2bdtGR0d1KN7Y2OjyfGEpav368fFx9fkn9mEhISEikQhtvUp9GJvN1ub8 y80bN6ye316vhYUNDQ2hrReJVtFqZmZmGRkZGzZsQCbm5eWlpKRwuVy0t0h+fv727ds9PDwOHz5s YWGBtjiQL2k+bxNZC1g6BLjDU/Wm45GR4TP/OjM8MgIAIBAIMdExem4oartab2Njc/LkSTwef/ny ZXkKDMNXr15taGg4ePBgeHi4NgujQ0ND58+fP3r0qKen55dffjlxrVJL+vqEw0NDAABra2po6N80 5heJREp7j6OjoxKJZOJ5LzVIJBKlOOXR0dGxMQ3d572Se/fuPdt4c3f3eC3sNQiC2tranjY0NPN4 4+PjNBqNxfL18po/cYQ1OaieR4FAsH37dqVTyRQKJTIy8ocffuDz+aoK8vn8a9euRUREkEik8PDw +vp6fZqFb8+fl7fPa9auHdGiUf3999+V1j9pNFptbS2qSpuampT6Hisrqzt37qgpIpPJtm/fpsj/ 5ptvldy9uyUubt68eYrZLYFAcHZ2TkxMevpUqxk06gN9o6OjX3/9tY+Pj5LwJBKJxWLFx8cfP378 ypUrOTk5OTk5V69e/eSTT+Lj4xcsWEAgEKytrfft26fNVFcNUqk0NiYGAGBpaXn79m2N+ZubmxUH nJCsXr26trZWY/8np7W1dcuWLROXylasWFFeXq5qRtXe3sZk/jmk8vDwcHZ2DgoKOnDgwOnTp5OS kuguLopfX3opoLJS82k5XY7MwjDM4XDee+89Fmvy/gP3HEUKlUqNiYm5e/fuxLkwWmpqamY7OgIA 3nprs6qBQ0tLS2ZmZlpaWkJCgre3t6o1SRcXl9jY2LS0tKysrIkDqO7u7qysrLS0tMTERDabrSo6 3dHRcf369WlpaZmZmS0tLUgLRYWFZLK54klaunTplStXBgYG5L9CEFRTUxOMWLtZvHhxM4+n/u/r 9RaB9vb2srKy+/fvV1dX8/l8oVCI3EEnk8mzZ892c3MLDg4OCwsLCAjQ/4SPTCbbuTP1zJl/eXh6 Xr9+3ZfFmjRbT09PUVGR4s0PqkYlEATJB/dkMjk8PBw5dQEADA4O/vjjj/KNAm2MEInEsLAw5Bn7 z0+fTt25U/6ZwWAWFBR4eLgrFa+uroqMXKcIJ9y1K+348eMEgurBoI73+V/p7+/ncrn3798vQlBZ WdnR0aHD6FkNZaWl9vb2FArlu+++M6BZI7E7PU1xnVet+tukJ8EhCNqdnq7I5uJCV9/BG0awqaG3 tzcs7DUAcOm7d4+NjU23O5pJfucdhRLr129Q1V/W1v5Koz17LvF4/IULF9XYxMyri8bHxz8+ceKn n+5s2rQpMyND/9Z1iqHRaKoaVSbTm+33bN8RgqAnT56osYMZwa5cvnzq1KmQkJUff3zCzs5uut1B jZrNWAsLC19fX8VX+exIVWZsCPZTcfGevXv82OyzZ79yQQyFZzjIc1kwUDe4Qx7vV7/IiQHBKisr U1JSHBxon3/+ubHf5GRYvBheigdLIBBM+uYjOXb2f7YZdDpdzeM40wVrqK/fsSN5XAb9+9/nAwIC ptsddLDZ/nbPz45wudzBwSFVOXHgmUI4HJ7BVHega0YLVl9fH5+Q0Nkl+OKLL15+ebGqbFKpVOOa 3rTg7e39UsBL8s9/8Hjy3ctJGR4Zln9wdHRcvGiRGpszV7D6J08S4uNb29rOnT3397+Hqco2PDy8 Oz29sKhoKn3TEgqFEhMdI1/VFQr7SkpKVOVsfPpsczE0NFTDkUmjTED05vHjx8sCA+fOm1dYWKgq j0gkevz48bZtb7u40B8+fDSV7mlPb2/vypUh8ksdFBTc19c3Mc9Af3/QsmUAAAca7f79X9QbnImH IR49epSYmFheXu7HZudeuzbp+QOpVNra2trQ0NDW1rZx4yam2nZ/GrGzszt06FB9/SY+v7OysuL7 7y8nJ7+jlOfWrVvVNTUEIjE1JTUwcKkGi8a5sXSnrKyU7een/RUhEAjfXbgw3V6rA4Kg7IsX5dHX rq5zi4qKkL+W/+c/TCYDh8NtjY8fGBjUaG1mCVZWWioPBNMeD09PpTXyGQgEQd9fuuTu5gYAcHZ2 fv/99ysqKqqrqt4/epROp8+ysdm3f79SuJ8q9FqtNzjZFy/mFxSgOujw8pIlO1NTp/6tajpQ9+jR +W+/LS4u5vP5FArF3NycTCYHBgZu2hS9YsVyLQMdZpZgLwLC3t7Orq6xsTH5y6HRvvLYJBjGwEBL YgKJSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxj/A21IX6E7EshsAAAA AElFTkSuQmCC)
|
0,0004
|
4,40
|
0,0018
|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAQAklEQVR4nO2ce1QT177H94S8TEwI D4NCBEQeYqxwqBVZojwKVVqVauvzHDyiR0GW9mjVot571rEvxaVLpVYUK/aiWIEKVKqgeCiP2lIQ LHINRXmUhyRAQgB5BBJm5v4xNidnAslMCEKu+fw1mez927+Z7zx+e+/fHghFUWDGdKBMtANmyGEW zMQwC2ZimAUzMcyCmRhmwUwMs2AmhlkwE8MsmIlhFszEMAtmYpgFMzHMgpkYZsFMDLNgJoZZMBPD LJiJQTWKld7e3tbW1vr6+rq6ut7eXmwnnU53dXV1d3d3dnaeOnUqrkplZeW9e/c++OADBoNhFB8w YBhGEASCICKFURSlUCgWFha4/QiCwDA8RiPjxJgEU6lUDx48yM3NLSgoqKurk8lkMAzjylhbWwuF wsDAwHfffXf+/PlU6osWU1NT8/LyoqOjjStYamrqzZs3BwcHVSoVBEEUygiPEBRFYRim0WhMJjMo KCgmJgZXICcn5+rVq4ODg0qlUrcRKpXKYDAWLly4f//+l6MZZFhOh0qlKikp+eqrr27fvt3V1QUA oNFobm5ur7322rx58zANYBhuaGioqqqqqanp6emZNm1aWFjY1q1bPTw8KioqoqKiLC0ti4qKbG1t jXg8jY2NDQ0NEomkvLw8KyurqalJuwyXyw0PDw8ICHB0dHR2dnZzc8MVaG1tra2tlUgkv/76a1ZW Vl1dnbYRNpsdFhYWEhIiEAhmzZrl6elJ8I4cKyh5Ghsbo6KieDye2vVNmzZlZ2dLJBIYhnGFe3p6 SktL9+/fP3PmTAAAl8t1c3OztLQEADg6OjY1NRngAEGqqqoWLVqEO14+n5+VlaXt52jU1tYuW7YM 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|
0,0265
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1,45
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0,0384
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|
0,0059
|
1,65
|
0,0097
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0,3053
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0,48
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0,1465
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|
0,3297
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0,45
|
0,1484
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|
0,0012
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0,54
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0,0006
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0,0721
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0,24
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0,0173
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RLJ9+zYAAIhE4rVrSANa6gQklUr37NkDX1h8fLwaNQwODsp2O+zs7C5fvqyVeiD4fP7169cjIyPl vt0EI/uehvD09ExLS2Oz2dqeC2JiYuLnmze9vb1lbR764AORSL4lKyoqSkxMPHjwYExMjKpkBBwO 5+npGRcXl5iY+O233yr+AlVVVYmJiYmJievXr1e19BGDwbi4uOzcuTMxMfHChQuKcT8I/QqoqemR ra0NAABvvvXW6CjScC4GVN3vk0qlpaWlcPa7j4+P4jMny7Vr106dOjUxMbFs2bLdu3eryZjWiEAg qK2tLS0tra6uZjAYXC5XNu8Ch8MtWLDA2tra3d09NDTU399f90WobU+f7j9wAE4xsLCwLCoq8vL6 04xNQ0MDvBpJzWoKKIoNAACVSlX8jmJLSwudToe2lSbWyRmxsrIKCgpSOiMkEomio6Nu3foPAABU Kq2iolzNEEc9oFR6+PDh02fO2NrZ3ci74e2N+AO3umhWkYGBAS6Xi2QeACECgYDFYtXX15eUlBS/ 4Ndff2UwGND6Rn2dCATBtra2V7284F/m5Ml/6dH4VKDHFqiGTqdQKAQC8euvL2pVcbZ8I3GWkJ9/ A+4PrYuK0uojjdOPvgQ0PDwcFbUOAIC4uHhtv+85B2Z8ppPQ0LVBgX/Mb7CesbQLCs9NpFLpubS0 goLCdVFRn356VNVCCVWgAvoTBAJhXdQ6qF/C4/GQTAbNdfJ++un0mdPLl/t+kfqFpaWlttVRAcnj 5uY2f74JAADm5uaK2dx/MSorKg4ePLjI0Sk9Pd3BgTYJC6iA5DE1JUOBKCqVqjTX7C9DQ319XHyc kbHxhfMXXFyWTM7IXPqe4/TAGxkRjAswGMyqVavmRFbQ5Ghvb9+7d+/Q8Mi/f/j3P/4hv3APOaiA 5GlqahoeGXF0dApdqy7lfk7T3ta2ffv2p23tFy9e9PNbqaoY9KlkVbOfEH/ZJ2xy8Pn8q1dzQRDc sWMHjUqbaXemhLa2tm3btzU/efL1xa+h0btSxsfHP05Kys+/qcHc5CIHc5Rnz549efJkYED54iGp RHLh/HlDQ8O1YWFcLneafZsEIqEwIjwcuo8I40BPGYzVr79ubW2Tn39TVZnx8XHo44UUCuXBgwfq Df6NXmHlZWV79+17/vy5o6PToUOJkZGRsvkuQqHw26ysj498vHy5b9qXX5qbm8+gqwgRi8X8cS0i Va0tLbt27y4tLXVxWVpQ8HNBwc9Kbfb0dLe0tDKZzMjINzQvktFa9nOW//v0U/iqSSSTTZs2FRbe 6ujoaGtry8+/sWnjxvnz54eHR7S2ts60p0hhs1iLX8xOmi9c2NDQqKYw/f59LWa4AACDwSKZ1vgb Caimhr5o0SLZ38jQ0NDGxoZCoRAIhEWLFp06dWpgYGCm3dQMjzfS1dVFp9MP/vn/acbEvFleXt7R 0aGYTkS/f3/x4sXI1QMAgI3a9GUYdbPxfz3u3bt3/ty53+vqoBlfHA5nbm7u4uISHBwcHh6uy//o mE4qKyru3L3b398PrQSH94MgSCaTFy5cuGLFyrV/HkJeu3o178YNrb474OHhkZiYqPEfd/y9BAQA gFgs5nK5XC5XLBbj8XgLCwtzc/O59f9NQBCUSqWYFyg9NG0RrL+dgFD0CxoHQtEJVEAoOoEKCEUn UAGh6AQqIBSdQAWEohOogFB0AhUQik6gAkLRCVRAKDqBCghFJ1ABoejE/wM9xkv0z4dvbwAAAABJ RU5ErkJggg==)
|
0,0191
|
0,17
|
0,0032
|
|
0,0298
|
0,21
|
0,0063
|
|
1,0000
|
-
|
0,5109
|
По результатам расчета из таблицы Д.2 получают 0,51 МПа менее 1,0 МПа, следовательно, условие не выполняется, расчет прекращают, задают следующую пару значений абсолютного давления насыщенных паров и и повторяют процедуру.
Принимают пару значений 0,5 МПа и 1,0 МПа и возобновляют расчет (см. таблицу Д.3).
Таблица Д.3 - Расчет при 0,5 МПа и 1,0 МПа
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Компонент
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Молярная доля
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при 0,5 МПа
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|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAPZklEQVR4nO2ceVRTVx7HbxZCCBDZ ggJBWSQBA8GitSJo0aEM9KjYwQVoRaEKpwj2CG5wtAcdbW21i9o6rbZjq1iVg5y6QYEqQu0wbKVV URASUrZAgLCTkJD35o9o+hrI8rIAb8znr+Tm3t/95X3fu+vvPhwMw8AEdsBPtwMm0GESDGOYBMMY JsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjEE0iJWh oaH29nYOh9PU1DQ0NCRPJJFI8+fPZzAYbm5uVlZWSkV+++234uLinTt3mpubG8QHJDAMj4+PAwBw OJw2mQEAZmZmE3+SSqWojBCJRG0y6wNOnxABqVRaVVVVUFBQUlLS1NTU09Mjk8mU8tjZ2bFYrJCQ kHXr1rHZbCLx2S2yf//+oqKi0tJSa2tr3d1XAYfDOXLkSH9/v0QigSCIQCBMmk0mk+HxeHNzc0dH x6ysrDlz5iB/7ezszMrKEggEY2NjMpmMQCBMKoZMJsPhcCQSycbG5uDBg56engb/O0h0FEwqlZaX l587d+727dt9fX0AADMzMy8vLz8/P19fX/lDI5PJuFzugwcP6uvrBwYGaDRaREREQkICk8msqalJ SkqaNWtWaWmpg4ODgf8TAMPDww8fPuzs7ORyuTdv3iwtLZ00W1BQ0Nq1a5lMppOTE5vNJpPJyF/F YvGDBw/4fD6Px7t161ZJScnE2xEAsGjRosjISG9vb2dnZ39//4ltiYGB0cPj8ZKSkmxsbOQWLC0t Y2Njb9y4wefzZTKZUuaBgYGKiordu3e7uroCAKhUqpeX16xZswAAc+fO/eOPP3RwABX9/f0ZGRmK 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AoVCcXZ21qGUMZxBhbpRInJzWY5EIpGHj5mYLtQ9Yba2tjjcX8Kq+vr6+vr6pnIq1tHRUVdX9/Tp U5FIRCKR3NzcfH193d3d/2+edbFY3NLS0tTY2MThiEQiKyur6Ohoe3t7VfnVCcZisWxsbORRbHIG Bwc7OjqYTKYhXVZBb2/v1+fOXczO5nA4iuEZkWhGp7usXr1mx44d3t5T4YbxaG5uvnnzZn5+fl1d nYWFhY+PD4vFmjNnDpE4SUjrn6iJ9+jp6WGz2Ur5T506ZfRAExjmcjlrVq9W8xh5e/vk5+draU0i kURERCCLx8XF6eBVXFwc0khERIREItHBzsDAwMnPPmMyGAAAJtP71OnTjY2NWppSJ5hMJlNyEQCw detWCIJ08FJ7+vv7o6L+Ia/O2trax8dn6dKlnp6eSpv6rq5z7927p43BGSXY47q6N9atIxAIBAIh Pj4ebbSdhjC33NxcpcvEZDLb2trQeomKk599hsfjqVTqO8nJZWVlXV1dQ0NDra2tOTlXlwcHI51Z vnxFT0+PRoMzR7A7d37y8/UFAFhYUI4cOToyMoLWBw2CCYXCJUuWIL0kEonZ2dloq1HF4OCgUChE pnQLBP7+bCcnp5ycHKlUqpS/tbV1zZo1SGcuX76isZYZIlhxUZG7uzsAwMzM7PA//6lbc6phx9nW 1nbjxo3IgIDx8fFLly4ZZKdYJBLt2bPnwoULyMT/VlRwOc1Zhw5t2LBBKb4aAECn0z/99NMFC3wU zhQVFUEQBl75+PPPZYlJic3NzQCAuC1b0nbtmvS8jEY0h2Zs3rw5MDAQmXL37t28vDwdKkMCw/DZ s2d/+eUXpXv/57KypYGBb8bGqiro6em5JW6LYjjC4/EkkjE9nTE2PB4vbVdaczMPAMD29z944ICl paVupjQL5ujomJmZSaVSFSljY2PHjh1rbGzUrUo5N27cOHbsWGpqKnJHFIZhBoORnp6u/v8ELw9W 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IR49epSYmFheXu7HZudeuzbp+QOpVNra2trQ0NDW1rZx4yam2nZ/GrGzszt06FB9/SY+v7OysuL7 7y8nJ7+jlOfWrVvVNTUEIjE1JTUwcKkGi8a5sXSnrKyU7een/RUhEAjfXbgw3V6rA4Kg7IsX5dHX rq5zi4qKkL+W/+c/TCYDh8NtjY8fGBjUaG1mCVZWWioPBNMeD09PpTXyGQgEQd9fuuTu5gYAcHZ2 fv/99ysqKqqrqt4/epROp8+ysdm3f79SuJ8q9FqtNzjZFy/mFxSgOujw8pIlO1NTp/6tajpQ9+jR +W+/LS4u5vP5FArF3NycTCYHBgZu2hS9YsVyLQMdZpZgLwLC3t7Orq6xsTH5y6HRvvLYJBjGwEBL YgKJSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxj/A21IX6E7EshsAAAA AElFTkSuQmCC)
|
0,0004
|
4,20
|
0,0017
|
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|
0,0265
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1,37
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0,0363
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|
0,0059
|
1,55
|
0,0091
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0,3053
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0,45
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|
0,3297
|
0,41
|
0,1352
|
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|
0,0012
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0,49
|
0,0006
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RLJ9+zYAAIhE4rVrSANa6gQklUr37NkDX1h8fLwaNQwODsp2O+zs7C5fvqyVeiD4fP7169cjIyPl vt0EI/uehvD09ExLS2Oz2dqeC2JiYuLnmze9vb1lbR764AORSL4lKyoqSkxMPHjwYExMjKpkBBwO 5+npGRcXl5iY+O233yr+AlVVVYmJiYmJievXr1e19BGDwbi4uOzcuTMxMfHChQuKcT8I/QqoqemR ra0NAABvvvXW6CjScC4GVN3vk0qlpaWlcPa7j4+P4jMny7Vr106dOjUxMbFs2bLdu3eryZjWiEAg qK2tLS0tra6uZjAYXC5XNu8Ch8MtWLDA2tra3d09NDTU399f90WobU+f7j9wAE4xsLCwLCoq8vL6 04xNQ0MDvBpJzWoKKIoNAACVSlX8jmJLSwudToe2lSbWyRmxsrIKCgpSOiMkEomio6Nu3foPAABU Kq2iolzNEEc9oFR6+PDh02fO2NrZ3ci74e2N+AO3umhWkYGBAS6Xi2QeACECgYDFYtXX15eUlBS/ 4Ndff2UwGND6Rn2dCATBtra2V7284F/m5Ml/6dH4VKDHFqiGTqdQKAQC8euvL2pVcbZ8I3GWkJ9/ A+4PrYuK0uojjdOPvgQ0PDwcFbUOAIC4uHhtv+85B2Z8ppPQ0LVBgX/Mb7CesbQLCs9NpFLpubS0 goLCdVFRn356VNVCCVWgAvoTBAJhXdQ6qF/C4/GQTAbNdfJ++un0mdPLl/t+kfqFpaWlttVRAcnj 5uY2f74JAADm5uaK2dx/MSorKg4ePLjI0Sk9Pd3BgTYJC6iA5DE1JUOBKCqVqjTX7C9DQ319XHyc kbHxhfMXXFyWTM7IXPqe4/TAGxkRjAswGMyqVavmRFbQ5Ghvb9+7d+/Q8Mi/f/j3P/4hv3APOaiA 5GlqahoeGXF0dApdqy7lfk7T3ta2ffv2p23tFy9e9PNbqaoY9KlkVbOfEH/ZJ2xy8Pn8q1dzQRDc sWMHjUqbaXemhLa2tm3btzU/efL1xa+h0btSxsfHP05Kys+/qcHc5CIHc5Rnz549efJkYED54iGp RHLh/HlDQ8O1YWFcLneafZsEIqEwIjwcuo8I40BPGYzVr79ubW2Tn39TVZnx8XHo44UUCuXBgwfq Df6NXmHlZWV79+17/vy5o6PToUOJkZGRsvkuQqHw26ysj498vHy5b9qXX5qbm8+gqwgRi8X8cS0i Va0tLbt27y4tLXVxWVpQ8HNBwc9Kbfb0dLe0tDKZzMjINzQvktFa9nOW//v0U/iqSSSTTZs2FRbe 6ujoaGtry8+/sWnjxvnz54eHR7S2ts60p0hhs1iLX8xOmi9c2NDQqKYw/f59LWa4AACDwSKZ1vgb Caimhr5o0SLZ38jQ0NDGxoZCoRAIhEWLFp06dWpgYGCm3dQMjzfS1dVFp9MP/vn/acbEvFleXt7R 0aGYTkS/f3/x4sXI1QMAgI3a9GUYdbPxfz3u3bt3/ty53+vqoBlfHA5nbm7u4uISHBwcHh6uy//o mE4qKyru3L3b398PrQSH94MgSCaTFy5cuGLFyrV/HkJeu3o178YNrb474OHhkZiYqPEfd/y9BAQA gFgs5nK5XC5XLBbj8XgLCwtzc/O59f9NQBCUSqWYFyg9NG0RrL+dgFD0CxoHQtEJVEAoOoEKCEUn UAGh6AQqIBSdQAWEohOogFB0AhUQik6gAkLRCVRAKDqBCghFJ1ABoejE/wM9xkv0z4dvbwAAAABJ RU5ErkJggg==)
|
0,0191
|
0,15
|
0,0029
|
|
0,0298
|
0,19
|
0,0057
|
|
1,0000
|
-
|
0,4700
|
По результатам расчета получают 0,47 МПа менее 0,5 МПа, следовательно, условие не выполняется, расчет прекращают, задают следующую пару значений абсолютного давления насыщенных паров и и повторяют процедуру.
Принимают пару значений 0,1 МПа и 0,5 МПа.
При выбранных значениях и рассчитывают и (см. таблицу Д.4).
Таблица Д.4 - Расчет и при 0,1 МПа и 0,5 МПа
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Компонент
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Молярная доля
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при 0,1 МПа
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при 0,5 МПа
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![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAPZklEQVR4nO2ceVRTVx7HbxZCCBDZ ggJBWSQBA8GitSJo0aEM9KjYwQVoRaEKpwj2CG5wtAcdbW21i9o6rbZjq1iVg5y6QYEqQu0wbKVV URASUrZAgLCTkJD35o9o+hrI8rIAb8znr+Tm3t/95X3fu+vvPhwMw8AEdsBPtwMm0GESDGOYBMMY JsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjEE0iJWh oaH29nYOh9PU1DQ0NCRPJJFI8+fPZzAYbm5uVlZWSkV+++234uLinTt3mpubG8QHJDAMj4+PAwBw OJw2mQEAZmZmE3+SSqWojBCJRG0y6wNOnxABqVRaVVVVUFBQUlLS1NTU09Mjk8mU8tjZ2bFYrJCQ kHXr1rHZbCLx2S2yf//+oqKi0tJSa2tr3d1XAYfDOXLkSH9/v0QigSCIQCBMmk0mk+HxeHNzc0dH x6ysrDlz5iB/7ezszMrKEggEY2NjMpmMQCBMKoZMJsPhcCQSycbG5uDBg56engb/O0h0FEwqlZaX l587d+727dt9fX0AADMzMy8vLz8/P19fX/lDI5PJuFzugwcP6uvrBwYGaDRaREREQkICk8msqalJ SkqaNWtWaWmpg4ODgf8TAMPDww8fPuzs7ORyuTdv3iwtLZ00W1BQ0Nq1a5lMppOTE5vNJpPJyF/F YvGDBw/4fD6Px7t161ZJScnE2xEAsGjRosjISG9vb2dnZ39//4ltiYGB0cPj8ZKSkmxsbOQWLC0t Y2Njb9y4wefzZTKZUuaBgYGKiordu3e7uroCAKhUqpeX16xZswAAc+fO/eOPP3RwABX9/f0ZGRmK J1sOHo9PTk7u7e3V0sjw8PBHH32kpCgAYOvWrV1dXUb1XwnUghUWFi5evFjh8cKFC/Py8sRiscaC v/766xtvvIFsVZydnZuamnRyGx3t7e3z589HXmg6nd7Y2IjKSH9/P/KPAwBsbW2rq6uN5LMq0AmW m5vr5OSk8Dg0NLShoUH74kKh8O2338bjnw1NqVRqVVUVSod1QSwWh4aGIq/1smXLhoeHURmBICg6 OhppxMfHRyAQGMlnVaAY1l+/fj0lJYXP58u/vvLKK1999RWDwdDegq2t7YkTJ2JiYuRfZTKZRCLR vrjO4PF4pUGgmZmZqpGIKuQjC2QKkUhEa0R/tBWssrIyPT29s7NT/tXBweGDDz7w8PBAW5+Njc3h w4cXLlwIABCLxQKBAK0Fg2CQ8TeRSFS0FlOGVvV1d3fv27ePw+HIv+JwuKSkpFdffVW3Kj08PDIy MshkMgRB8onO1DN79mylx0UHaDQahUIxiD/ao1kwGIa/+eabsrIyRQqdTt+8ebM+N9frr7++fPly GIa7urp0NqIPBnnCVM3MjIrmi15XV3fmzBkIghQpUVFRXl5e+tRqZWWVmJhIIpFGR0f1sfMCokEw GIazs7NbW1sVKZaWlpGRkfq33StXrmQwGIohjAkt0XDdeTzetWvXkCne3t7+/v76V2xvb79q1aqR kRH9Tb1QaFj8LSkpUYw15Pj7+yvWOPQkJSVFKBQaxNSLgzrBZDJZSUkJ/NfFxoCAAEP1tHp2hC8m 6prErq6uiooKZIq5uTmqmbIJg6NOsObm5o6ODmSKpaWlo6OjkV0yoQ51gnG5XKVht7W1ta2trZFd mgp0a9WnftY1EXV9mHwpHZlCpVKNvt8zJfT29tbW1upQyhjOoEKdYP/Hs9rCwkJVu5pqEIvFxnAG FYaJ6cAc5ubmDg4OqJo4GIa7u7una/FTwQsqWHh4+MmTJ9GWevfdd3Nzc43hj/aoE2ziZs9M6HUN AoVCcXZ21qGUMZxBhbpRInJzWY5EIpGHj5mYLtQ9Yba2tjjcX8Kq+vr6+vr6pnIq1tHRUVdX9/Tp U5FIRCKR3NzcfH193d3d/2+edbFY3NLS0tTY2MThiEQiKyur6Ohoe3t7VfnVCcZisWxsbORRbHIG Bwc7OjqYTKYhXVZBb2/v1+fOXczO5nA4iuEZkWhGp7usXr1mx44d3t5T4YbxaG5uvnnzZn5+fl1d nYWFhY+PD4vFmjNnDpE4SUjrn6iJ9+jp6WGz2Ur5T506ZfRAExjmcjlrVq9W8xh5e/vk5+draU0i kURERCCLx8XF6eBVXFwc0khERIREItHBzsDAwMnPPmMyGAAAJtP71OnTjY2NWppSJ5hMJlNyEQCw detWCIJ08FJ7+vv7o6L+Ia/O2trax8dn6dKlnp6eSpv6rq5z7927p43BGSXY47q6N9atIxAIBAIh Pj4ebbSdhjC33NxcpcvEZDLb2trQeomKk599hsfjqVTqO8nJZWVlXV1dQ0NDra2tOTlXlwcHI51Z vnxFT0+PRoMzR7A7d37y8/UFAFhYUI4cOToyMoLWBw2CCYXCJUuWIL0kEonZ2dloq1HF4OCgUChE pnQLBP7+bCcnp5ycHKlUqpS/tbV1zZo1SGcuX76isZYZIlhxUZG7uzsAwMzM7PA//6lbc6phx9nW 1nbjxo3IgIDx8fFLly4ZZKdYJBLt2bPnwoULyMT/VlRwOc1Zhw5t2LBBKb4aAECn0z/99NMFC3wU zhQVFUEQBl75+PPPZYlJic3NzQCAuC1b0nbtmvS8jEY0h2Zs3rw5MDAQmXL37t28vDwdKkMCw/DZ s2d/+eUXpXv/57KypYGBb8bGqiro6em5JW6LYjjC4/EkkjE9nTE2PB4vbVdaczMPAMD29z944ICl paVupjQL5ujomJmZSaVSFSljY2PHjh1rbGzUrUo5N27cOHbsWGpqKnJHFIZhBoORnp6u/v8ELw9W 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3dHRcf369WlpaZmZmS0tLUgLRYWFZLK54klaunTplStXBgYG5L9CEFRTUxOMWLtZvHhxM4+n/u/r 9RaB9vb2srKy+/fvV1dX8/l8oVCI3EEnk8mzZ892c3MLDg4OCwsLCAjQ/4SPTCbbuTP1zJl/eXh6 Xr9+3ZfFmjRbT09PUVGR4s0PqkYlEATJB/dkMjk8PBw5dQEADA4O/vjjj/KNAm2MEInEsLAw5Bn7 z0+fTt25U/6ZwWAWFBR4eLgrFa+uroqMXKcIJ9y1K+348eMEgurBoI73+V/p7+/ncrn3798vQlBZ WdnR0aHD6FkNZaWl9vb2FArlu+++M6BZI7E7PU1xnVet+tukJ8EhCNqdnq7I5uJCV9/BG0awqaG3 tzcs7DUAcOm7d4+NjU23O5pJfucdhRLr129Q1V/W1v5Koz17LvF4/IULF9XYxMyri8bHxz8+ceKn n+5s2rQpMyND/9Z1iqHRaKoaVSbTm+33bN8RgqAnT56osYMZwa5cvnzq1KmQkJUff3zCzs5uut1B jZrNWAsLC19fX8VX+exIVWZsCPZTcfGevXv82OyzZ79yQQyFZzjIc1kwUDe4Qx7vV7/IiQHBKisr U1JSHBxon3/+ubHf5GRYvBheigdLIBBM+uYjOXb2f7YZdDpdzeM40wVrqK/fsSN5XAb9+9/nAwIC ptsddLDZ/nbPz45wudzBwSFVOXHgmUI4HJ7BVHega0YLVl9fH5+Q0Nkl+OKLL15+ebGqbFKpVOOa 3rTg7e39UsBL8s9/8Hjy3ctJGR4Zln9wdHRcvGiRGpszV7D6J08S4uNb29rOnT3397+Hqco2PDy8 Oz29sKhoKn3TEgqFEhMdI1/VFQr7SkpKVOVsfPpsczE0NFTDkUmjTED05vHjx8sCA+fOm1dYWKgq j0gkevz48bZtb7u40B8+fDSV7mlPb2/vypUh8ksdFBTc19c3Mc9Af3/QsmUAAAca7f79X9QbnImH IR49epSYmFheXu7HZudeuzbp+QOpVNra2trQ0NDW1rZx4yam2nZ/GrGzszt06FB9/SY+v7OysuL7 7y8nJ7+jlOfWrVvVNTUEIjE1JTUwcKkGi8a5sXSnrKyU7een/RUhEAjfXbgw3V6rA4Kg7IsX5dHX rq5zi4qKkL+W/+c/TCYDh8NtjY8fGBjUaG1mCVZWWioPBNMeD09PpTXyGQgEQd9fuuTu5gYAcHZ2 fv/99ysqKqqrqt4/epROp8+ysdm3f79SuJ8q9FqtNzjZFy/mFxSgOujw8pIlO1NTp/6tajpQ9+jR +W+/LS4u5vP5FArF3NycTCYHBgZu2hS9YsVyLQMdZpZgLwLC3t7Orq6xsTH5y6HRvvLYJBjGwEBL YgKJSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxj/A21IX6E7EshsAAAA AElFTkSuQmCC)
|
0,0004
|
4,00
|
0,0016
|
4,20
|
0,0017
|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAQAklEQVR4nO2ce1QT177H94S8TEwI D4NCBEQeYqxwqBVZojwKVVqVauvzHDyiR0GW9mjVot571rEvxaVLpVYUK/aiWIEKVKqgeCiP2lIQ LHINRXmUhyRAQgB5BBJm5v4xNidnAslMCEKu+fw1mez927+Z7zx+e+/fHghFUWDGdKBMtANmyGEW zMQwC2ZimAUzMcyCmRhmwUwMs2AmhlkwE8MsmIlhFszEMAtmYpgFMzHMgpkYZsFMDLNgJoZZMBPD LJiJQTWKld7e3tbW1vr6+rq6ut7eXmwnnU53dXV1d3d3dnaeOnUqrkplZeW9e/c++OADBoNhFB8w YBhGEASCICKFURSlUCgWFha4/QiCwDA8RiPjxJgEU6lUDx48yM3NLSgoqKurk8lkMAzjylhbWwuF wsDAwHfffXf+/PlU6osWU1NT8/LyoqOjjStYamrqzZs3BwcHVSoVBEEUygiPEBRFYRim0WhMJjMo KCgmJgZXICcn5+rVq4ODg0qlUrcRKpXKYDAWLly4f//+l6MZZFhOh0qlKikp+eqrr27fvt3V1QUA oNFobm5ur7322rx58zANYBhuaGioqqqqqanp6emZNm1aWFjY1q1bPTw8KioqoqKiLC0ti4qKbG1t jXg8jY2NDQ0NEomkvLw8KyurqalJuwyXyw0PDw8ICHB0dHR2dnZzc8MVaG1tra2tlUgkv/76a1ZW Vl1dnbYRNpsdFhYWEhIiEAhmzZrl6elJ8I4cKyh5Ghsbo6KieDye2vVNmzZlZ2dLJBIYhnGFe3p6 SktL9+/fP3PmTAAAl8t1c3OztLQEADg6OjY1NRngAEGqqqoWLVqEO14+n5+VlaXt52jU1tYuW7YM 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|
0,0265
|
1,25
|
0,0331
|
1,37
|
0,0363
|
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|
0,0059
|
1,50
|
0,0089
|
1,55
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0,0091
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0,2100
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0,55
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0,1155
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0,60
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0,1260
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|
0,3297
|
0,36
|
0,1187
|
0,41
|
0,1352
|
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|
0,0012
|
0,43
|
0,0005
|
0,49
|
0,0006
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sWMHjUqbaXemhLa2tm3btzU/efL1xa+h0btSxsfHP05Kys+/qcHc5CIHc5Rnz549efJkYED54iGp RHLh/HlDQ8O1YWFcLneafZsEIqEwIjwcuo8I40BPGYzVr79ubW2Tn39TVZnx8XHo44UUCuXBgwfq Df6NXmHlZWV79+17/vy5o6PToUOJkZGRsvkuQqHw26ysj498vHy5b9qXX5qbm8+gqwgRi8X8cS0i Va0tLbt27y4tLXVxWVpQ8HNBwc9Kbfb0dLe0tDKZzMjINzQvktFa9nOW//v0U/iqSSSTTZs2FRbe 6ujoaGtry8+/sWnjxvnz54eHR7S2ts60p0hhs1iLX8xOmi9c2NDQqKYw/f59LWa4AACDwSKZ1vgb Caimhr5o0SLZ38jQ0NDGxoZCoRAIhEWLFp06dWpgYGCm3dQMjzfS1dVFp9MP/vn/acbEvFleXt7R 0aGYTkS/f3/x4sXI1QMAgI3a9GUYdbPxfz3u3bt3/ty53+vqoBlfHA5nbm7u4uISHBwcHh6uy//o mE4qKyru3L3b398PrQSH94MgSCaTFy5cuGLFyrV/HkJeu3o178YNrb474OHhkZiYqPEfd/y9BAQA gFgs5nK5XC5XLBbj8XgLCwtzc/O59f9NQBCUSqWYFyg9NG0RrL+dgFD0CxoHQtEJVEAoOoEKCEUn UAGh6AQqIBSdQAWEohOogFB0AhUQik6gAkLRCVRAKDqBCghFJ1ABoejE/wM9xkv0z4dvbwAAAABJ RU5ErkJggg==)
|
0,0191
|
0,13
|
0,0025
|
0,15
|
0,0029
|
|
0,0298
|
0,17
|
0,0051
|
0,19
|
0,0057
|
|
1,0000
|
-
|
0,4254
|
-
|
0,4700
|
В результате расчета при 0,1 МПа и 0,5 МПа получают 0,4254 МПа более 0,1 МПа. Так условие выполняется, то продолжают расчет.
При выбранных значениях давления насыщенных паров по таблицам Г.1, Г.5 (приложение Г) выбирают значения летучести , рассчитывают по формуле ![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAASAAAABWCAIAAADg7dy/AAAfdUlEQVR4nO2deVwT1/bAbyZkQxQQ 2QXBqrjgCiIVF9xBqyIiiBREoWqpyxMUf1prtRW1FqXyVFyebdX3cV8roogIKO4omyJEQti3sIWQ kG0yvz9Gp/PCloQsaOf718zNLGcm99y599xzziUhCAIICAg0A6RrAQgIPmcIBSMg0CCEghEQaBBC wQgINAihYAQEGoRQMAICDUIoGAGBBiEUjIBAgxAKRkCgQQgFIyDQIISCERBoEELBCAg0CKFgBAQa RE/XAnSNRCJpbm6mUCh9+vTBlzc1NcEwbGxsDEGfQDORn5//5MkTXd192LBhX375pa7u/onC5XIl EomxsTGZTMYKhUJhS0uLvr6+vr6+QldBejaPHj3y8/MbMWKEm5vbvXv30MKKiootW7aMGzdu5MiR u3fvFgqFuhVSEU6ePKmpiqAA/v7+MAzr+h18MtTV1f30008uLi4jRoyIjIzk8XgIgsAwfPnyZQ8P j+HDh8+bN+/NmzeKXKpHK1hmZubgwYOxWjJ16lQ+n8/j8QICArDC3r17P336VNeSdg2bzXZxcelI ASAIInWbThTM09NTLBbr+h18GgiFwnXr1mGvjkKhxMfHIwhy48YNY2NjrHzNmjUymazLq/XcLiIM w8eOHXv//j1WIpFIIAhKTk6+cuUKViiTyWAY1oWAymFnZxcTExMQEFBcXCz3k76+fnh4+MiRI5Hu Bb+KxeKqqqrm5uasrKzXr19XVVVhPwmFQhiGKRRKd67/6SKTydhsdlZWFofDodFogwYNcnJy6qiP l5GRcebMGWwXQRAYhvl8fkxMTGNjI1YukUgUurfKig7DsERhFNF1Odhstp2dHV7U1atXwzAcFBSE Lxw8eHB5ebnKT6FlLly4YGho2PZfmDt3bl1dnbruIhKJsrOzv/32W6wOjRo1qqGhQV3X/7R4/fp1 aGiovb39wIEDXV1dR4wYYWhouHjx4qysrHaP37RpE/6vsbCwYDKZaWlpeIUkkUj//ve/Fbm7il8w qVQaFRX19OlTAACZTO68fwIAMDIyMjIyIpPJAwYMcHBwGDJkiJ2dXecNKovFqq6uxnb19fW9vb0F AsHbt2/xh3l6elpZWan2FNrHx8enpKRk+/btcu3fnTt3tmzZEhsbq+jQuVOoVOqoUaMOHTo0dOjQ bdu28fl8GIY/ie+8ehEKhb///vsvv/zC4/HWrVsXFBRkbm5eUFDg4eFx9epVDodz+fJlMzMz/Cki kSgnJwdfMm3atIEDByYmJgoEAqzQxsZm9uzZCgmhWquAih4ZGTl//vx2m+ROoFKp1tbWvr6+V65c aWlp6egWclaB2bNnCwSCoqIia2trrLBv374vXrxQ7RF0BZ/PX7VqVdsmiUKh7Nu3T72mCLFY/N13 3wEArKysCgsL1Xjlng+Xy92wYQONRjM2Nr506RLah5LJZAcPHqRSqQAAPT29W7duyZ1VW1s7fPhw 7E/R19e/e/cugiAbNmzA/1kbNmxQ8J/qrpFDLBYnJCTgKz0qlpeX1+bNm48cOXL6I9HR0cuWLbO0 tMQOo9FoS5YsycvLa/fK27dvx+vkf//7XwRBnjx5YmBggJUHBASIRKJuPoL2qampmTNnTtumx8jI 6OLFi+q915s3bywtLU1NTfPz89V75Z4Mn89fu3YtBEFkMnnv3r3YCKWxsXHMmDHo24Yg6ObNm3In vnv3Dv9N8/Dw4PF4UqnUy8sLKzQ1NVW8WVePFfHrr7/GV5TJkyc3Nze3PUwqlWZlZfn7++MnFpyd nbOzs+WOlMlkwcHB2DGurq6NjY0Igly7dg0718DAIDk5WS3ya5+3b9+OGjWqrY4NGDBAvUZRiUTi 6+tLo9EeP36sxsv2ZKRS6d69e9HP1MyZM9Gag9La2rpq1SoajUahUBYtWlRbWyt3Ln6sRaVSL126 hCAIj8dzdXXF/qPly5dLJBIFhVGDgskpAwBg69atnRzf2Njo6+uLP37mzJlyQ3CJRDJ//nz0VzKZ fPToUbT8xIkT2Fnz58/n8/ndl19XJCUlWVhYtNUxFxcXFoulxhsdOXKETqenpqaq8Zo9maSkpL59 +wIAevXqdefOHblfm5qaEhISbt26xeFw2p5748YNPb0Phgk3N7f6+noEQWpqaoYNG4YW9unTR6lm XQ0KxuPx3NzcsPpBpVLbdm3lyMzMxNctMpn822+/4Q9obm6eMGEC+uvo0aOrq6vR8l27dqGFDAbj r7/+6r7wuuXUqVO9evVqq2M+Pj5qNPqlpKQwGAy0Mf7sqa+vd3d3R1/jrFmzOhnkt0tcXBxWJ3// /Xe0kMlkYkMbHx8fpRwb1OBkVFlZyWazsV0bGxusm9sRjo6OkyZNwnZhGL569WpLSwtW0tLS0tDQ AAAgkUj+/v7m5ubYvdCNCRMmTJ06tfvC65bAwMANGzZgTSbGtWvXoqKixGKxWu4yZMiQoKAgOXPZ 58r58+cfPXoEACCTyUuXLm23/eoEbPLQ0dHR09MT3a6vr0crJ4PBCAwMpNFoSlxRKf1ulytXruCr iJ+fnyI91B9++AEvhomJCX5eAmszHBwcSkpK0EIYhn18fAAAVCr13Llz3Ze8J8DlcpctW9b2f9HX 1z9y5IgK84ftoq7r9HBKSkqwvpydnR2bzVb2CmFhYQAACIIOHTqEFSYkJKAjOg8PD2U/iWr4gqWn 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eXl5Q0ODhYWF2ceUo1qmsrKSw+GYm1tYWGi1E9EjFIyA4HPlsw0DISDoCRAKRkCgQQgFIyDQIISC ERBoEELBCAg0CKFgBAQahFAwAgINQigYAYEGIRSMgECDEApGQKBBCAUjINAghIIREGiQ/wd4rwhF Vi4tPwAAAABJRU5ErkJggg==)
;
;
МПа.
В результате методом последовательного приближения получают 0,47 МПа, следовательно
МПа;
МПа.
Приложение Е (рекомендуемое). Примеры расчета давления насыщенных паровПриложение Е
(рекомендуемое)
В таблицах Е.1-Е.4 приведены примеры расчета давления насыщенных паров СУГ при различных температурах.
Таблица Е.1 - Пример расчета давления насыщенных паров при температуре 45°С
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Компо-
нент
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Моляр-
ная масса , г/моль
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Массовая доля , %
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Моля-
рная доля
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при 1,0 МПа
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при 1,5 МПа
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|
30,070
|
2,0020
|
0,0666
|
0,0322
|
4,40
|
0,1417
|
4,70
|
0,1513
|
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|
44,097
|
30,0066
|
0,6805
|
0,3291
|
1,45
|
0,4772
|
1,53
|
0,5035
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42,081
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22,9965
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0,5465
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0,2643
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1,65
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0,4361
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1,73
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0,4572
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kEAgoN8Yl8vlKm0x+B+o2fqlsbHR0dERrQmCIJK8DIJgYmJiU1MTtnJ2djZa08TEZPLkydHR0S9f vtRym5n29vaMjAzlXAhTU9Pg4OB169YdPnz44gcuXLiwd+/exMREZPbDwcHhyJEjQqFQ41V4PN7c uDgjI6PTp3/GlrPZbB9vL+SKM2dGaNxiTCaTVVZWKsfZDQwM0tLStPzUMAw/e/YsPDxcoREQBJcs WVJbW6txfy25XH4w58D7b51IvHz5/9TU3JORgV5icnBwV1eXqpolJddJpPcT21SqdXV1tZpm1U1l ODk5xcbGnjp1CpUal8t1d3dPS0tbvXq1ws8XO4srFArNzc0PHTqEbjqmEWtr6x07dsydO/f06dPX rl17/fo1Ut7T0/P48ePHjx8DH/xbOWaMsLOzW79+/cqVK7VZViaXy3OPHLleUrJ6zZovv/xSy45h +eOPP5DtO1tbW+l0OupyoshksmPHjv3+++9hYWHm5uYuLi4pKSkK6d51dXWnT5+GIKi9vZ1Op2ON BLSf586dYzAYM2fOpFKpNBpt3bp1Cluh9QOsYU4ACZr8N1DFsSLqBEQikTIyMszMzG7fvi2VSu3t 7SMiIhISEvr0AOfNm7d69WoGg2FlZfX5558vW7ZMpxAFQlBQUGBgYHp6ellZ2YMHD6qqqjgcDp/P RyOZIAiamJjY2dl5enpGRERERUX5+flpGTi5c/v2j4cOBQQEbN2yVc0DXA1UKhXJrgwICIiLi1Nl P6HrVWxsbJSz58zMzPz9/ZEK0dHRGhsxNzcfjEQXTbdMW0tOw2Sqvb39wYMHeTweBEGmpqboDpjK 2NjY5ObmdnZ2kslkfX4uIAh6eXl5eXmtWbOGx+NxudyWlhbUEQBBkEajOTg4WFpa6nRb2ezW7Tu2 S6WyvXv3jR3r0r++ubm5qV+Mqw2Ojo5JSUl6NjK46OIGaJ6NB0FQOfrcJyQSqR9PHfXXpVKpuiZJ KSOVSv+R/Y/Hjyu2bds+e3Yfe4CMlpRadeiwlwH4UUMgAQTVpreMpN3U+k1xUVFeXt7MmTPXrl0r k8mUnWSRSAx/MK1gGBaJRMiwSCAQhu8GzTri4PjRQUHsX1U1e4W96N0wNze3VLtoePQLiM/n5+Tk 9AgEzc3Ny5cv6/PGSSSS5ub3nnN19dP4+HjENAkPD9+xY8foyPl3cnIiGxmJxGIAAHh8Xk+PQJWl 8e7dO/Q3RqPRzP/LBSQWiZDktYaGhoaGBo31+Xx+WVkZcmxhaSmXy0eHgMaOHUe1pra0tAIA0NPd oybdhcf/GHjz8vI2/bADc5+MfgGBBJBiTNGY5CsWi5GHE4FAQNNwKWSVTsOIw9HR0cfbBxFQZ1cn u42tKhmtmfUxPDFlSrD6YP3oF5CVFTUv75T6efKOjo6NGza8YbEAAPD398/OzkaCNzQabQRtmKoe Y2Pj6OhZd0pLAQDo7e199aqpz3lAqVT68tX7KSkq1Xr6tGnqmx39AjI0NFReWqQAl9uOzqBZWlEj IiINDUfhnYmOnp2Tc5Db0SGHYWZf/xQDAACfz3/d9D6KGxIa4ttX0hmWUfLz0hOZDProucrlEDQ0 20wPNv/j7x83Nw45Zjxg9Jlm8+LFX0gGM4VCSU5O1jj04wIa6ehg4JNIpLS0dba2NAAAnjGZVU+f Kte5c/tOV3c3AACzZkVHY/6BRBW4gEY2H7eGkWulpeDg4LTUNAKB0N3dfeniJYXMtbdvmy9evAgA gLOz89ZtW03U+l8IuIBGNo2NL5ADuRxmszXvjk0gENI3bPjiiy8AADh//vyNGzfRt3g83u5du6uZ TGsbm31ZWVNVrF5XRGPCwH8DbDYbzSQPCQ0VDv7/1emDWCx++/Ytk8k8ceKEjc3HHNHxvr6Fly83 NDRwOBz1qSBtbewVy5eTSCQXF5fDh488efLk6tWrsbGxRCJxYmDg1atXIQjSsjPD6y8vh4quzs49 mXuQGMl4X9/Nf//7cJ7BYL15c+78+Xfv3nG5XIlEgk3EMzY2ptFobm5uS5dqWN8uFAoLL106e+5c Q0MDgUCAYdjW1vaLxMTFiYudnBzVnKgALqARCQRB4Aew5chTAdB6u8/e3t7W1lYkh8LBwaEfe+Xi AsLRC9yIxtELXEA4eoELCEcvcAHh6AUuIBy9wAWEoxe4gHD0AhcQjl7gAsLRC1xAOHqBCwhHL3AB 4ejF/wNZyRFh/J83xQAAAABJRU5ErkJggg==)
|
58,123
|
19,9977
|
0,3441
|
0,1664
|
0,66
|
0,1098
|
0,69
|
0,1148
|
|
58,123
|
24,9972
|
0,4301
|
0,2080
|
0,48
|
0,0998
|
0,51
|
0,1061
|
|
-
|
100,0000
|
2,0678
|
1,0000
|
-
|
1,2646
|
-
|
1,3329
|
;
;
МПа;
МПа;
МПа.
Таблица Е.2 - Пример расчета давления насыщенных паров при температуре минус 20°С
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Компо-
нент
|
Моляр-
ная масса , г/моль
|
Массовая доля , %
|
|
Моляр-
ная доля
|
при 0,1 МПа
|
|
при 0,5 МПа
|
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![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAPZklEQVR4nO2ceVRTVx7HbxZCCBDZ ggJBWSQBA8GitSJo0aEM9KjYwQVoRaEKpwj2CG5wtAcdbW21i9o6rbZjq1iVg5y6QYEqQu0wbKVV URASUrZAgLCTkJD35o9o+hrI8rIAb8znr+Tm3t/95X3fu+vvPhwMw8AEdsBPtwMm0GESDGOYBMMY JsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjEE0iJWh oaH29nYOh9PU1DQ0NCRPJJFI8+fPZzAYbm5uVlZWSkV+++234uLinTt3mpubG8QHJDAMj4+PAwBw OJw2mQEAZmZmE3+SSqWojBCJRG0y6wNOnxABqVRaVVVVUFBQUlLS1NTU09Mjk8mU8tjZ2bFYrJCQ kHXr1rHZbCLx2S2yf//+oqKi0tJSa2tr3d1XAYfDOXLkSH9/v0QigSCIQCBMmk0mk+HxeHNzc0dH x6ysrDlz5iB/7ezszMrKEggEY2NjMpmMQCBMKoZMJsPhcCQSycbG5uDBg56engb/O0h0FEwqlZaX l587d+727dt9fX0AADMzMy8vLz8/P19fX/lDI5PJuFzugwcP6uvrBwYGaDRaREREQkICk8msqalJ SkqaNWtWaWmpg4ODgf8TAMPDww8fPuzs7ORyuTdv3iwtLZ00W1BQ0Nq1a5lMppOTE5vNJpPJyF/F YvGDBw/4fD6Px7t161ZJScnE2xEAsGjRosjISG9vb2dnZ39//4ltiYGB0cPj8ZKSkmxsbOQWLC0t Y2Njb9y4wefzZTKZUuaBgYGKiordu3e7uroCAKhUqpeX16xZswAAc+fO/eOPP3RwABX9/f0ZGRmK J1sOHo9PTk7u7e3V0sjw8PBHH32kpCgAYOvWrV1dXUb1XwnUghUWFi5evFjh8cKFC/Py8sRiscaC v/766xtvvIFsVZydnZuamnRyGx3t7e3z589HXmg6nd7Y2IjKSH9/P/KPAwBsbW2rq6uN5LMq0AmW m5vr5OSk8Dg0NLShoUH74kKh8O2338bjnw1NqVRqVVUVSod1QSwWh4aGIq/1smXLhoeHURmBICg6 OhppxMfHRyAQGMlnVaAY1l+/fj0lJYXP58u/vvLKK1999RWDwdDegq2t7YkTJ2JiYuRfZTKZRCLR vrjO4PF4pUGgmZmZqpGIKuQjC2QKkUhEa0R/tBWssrIyPT29s7NT/tXBweGDDz7w8PBAW5+Njc3h w4cXLlwIABCLxQKBAK0Fg2CQ8TeRSFS0FlOGVvV1d3fv27ePw+HIv+JwuKSkpFdffVW3Kj08PDIy MshkMgRB8onO1DN79mylx0UHaDQahUIxiD/ao1kwGIa/+eabsrIyRQqdTt+8ebM+N9frr7++fPly GIa7urp0NqIPBnnCVM3MjIrmi15XV3fmzBkIghQpUVFRXl5e+tRqZWWVmJhIIpFGR0f1sfMCokEw GIazs7NbW1sVKZaWlpGRkfq33StXrmQwGIohjAkt0XDdeTzetWvXkCne3t7+/v76V2xvb79q1aqR kRH9Tb1QaFj8LSkpUYw15Pj7+yvWOPQkJSVFKBQaxNSLgzrBZDJZSUkJ/NfFxoCAAEP1tHp2hC8m 6prErq6uiooKZIq5uTmqmbIJg6NOsObm5o6ODmSKpaWlo6OjkV0yoQ51gnG5XKVht7W1ta2trZFd mgp0a9WnftY1EXV9mHwpHZlCpVKNvt8zJfT29tbW1upQyhjOoEKdYP/Hs9rCwkJVu5pqEIvFxnAG FYaJ6cAc5ubmDg4OqJo4GIa7u7una/FTwQsqWHh4+MmTJ9GWevfdd3Nzc43hj/aoE2ziZs9M6HUN AoVCcXZ21qGUMZxBhbpRInJzWY5EIpGHj5mYLtQ9Yba2tjjcX8Kq+vr6+vr6pnIq1tHRUVdX9/Tp U5FIRCKR3NzcfH193d3d/2+edbFY3NLS0tTY2MThiEQiKyur6Ohoe3t7VfnVCcZisWxsbORRbHIG Bwc7OjqYTKYhXVZBb2/v1+fOXczO5nA4iuEZkWhGp7usXr1mx44d3t5T4YbxaG5uvnnzZn5+fl1d nYWFhY+PD4vFmjNnDpE4SUjrn6iJ9+jp6WGz2Ur5T506ZfRAExjmcjlrVq9W8xh5e/vk5+draU0i kURERCCLx8XF6eBVXFwc0khERIREItHBzsDAwMnPPmMyGAAAJtP71OnTjY2NWppSJ5hMJlNyEQCw detWCIJ08FJ7+vv7o6L+Ia/O2trax8dn6dKlnp6eSpv6rq5z7927p43BGSXY47q6N9atIxAIBAIh Pj4ebbSdhjC33NxcpcvEZDLb2trQeomKk599hsfjqVTqO8nJZWVlXV1dQ0NDra2tOTlXlwcHI51Z vnxFT0+PRoMzR7A7d37y8/UFAFhYUI4cOToyMoLWBw2CCYXCJUuWIL0kEonZ2dloq1HF4OCgUChE pnQLBP7+bCcnp5ycHKlUqpS/tbV1zZo1SGcuX76isZYZIlhxUZG7uzsAwMzM7PA//6lbc6phx9nW 1nbjxo3IgIDx8fFLly4ZZKdYJBLt2bPnwoULyMT/VlRwOc1Zhw5t2LBBKb4aAECn0z/99NMFC3wU zhQVFUEQBl75+PPPZYlJic3NzQCAuC1b0nbtmvS8jEY0h2Zs3rw5MDAQmXL37t28vDwdKkMCw/DZ s2d/+eUXpXv/57KypYGBb8bGqiro6em5JW6LYjjC4/EkkjE9nTE2PB4vbVdaczMPAMD29z944ICl paVupjQL5ujomJmZSaVSFSljY2PHjh1rbGzUrUo5N27cOHbsWGpqKnJHFIZhBoORnp6u/v8ELw9W ZIB1On0jEomQcWC6IRaLtVlGkEjGPvzwWHVNDQCATCbv3bN33rx5uteqTbspkUj27t2rFCkVFRXV 3d2tQysMw3BBQYGrq+u2bdtGR0d1KN7Y2OjyfGEpav368fFx9fkn9mEhISEikQhtvUp9GJvN1ub8 y80bN6ye316vhYUNDQ2hrReJVtFqZmZmGRkZGzZsQCbm5eWlpKRwuVy0t0h+fv727ds9PDwOHz5s YWGBtjiQL2k+bxNZC1g6BLjDU/Wm45GR4TP/OjM8MgIAIBAIMdExem4oartab2Njc/LkSTwef/ny ZXkKDMNXr15taGg4ePBgeHi4NgujQ0ND58+fP3r0qKen55dffjlxrVJL+vqEw0NDAABra2po6N80 5heJREp7j6OjoxKJZOJ5LzVIJBKlOOXR0dGxMQ3d572Se/fuPdt4c3f3eC3sNQiC2tranjY0NPN4 4+PjNBqNxfL18po/cYQ1OaieR4FAsH37dqVTyRQKJTIy8ocffuDz+aoK8vn8a9euRUREkEik8PDw +vp6fZqFb8+fl7fPa9auHdGiUf3999+V1j9pNFptbS2qSpuampT6Hisrqzt37qgpIpPJtm/fpsj/ 5ptvldy9uyUubt68eYrZLYFAcHZ2TkxMevpUqxk06gN9o6OjX3/9tY+Pj5LwJBKJxWLFx8cfP378 ypUrOTk5OTk5V69e/eSTT+Lj4xcsWEAgEKytrfft26fNVFcNUqk0NiYGAGBpaXn79m2N+ZubmxUH nJCsXr26trZWY/8np7W1dcuWLROXylasWFFeXq5qRtXe3sZk/jmk8vDwcHZ2DgoKOnDgwOnTp5OS kuguLopfX3opoLJS82k5XY7MwjDM4XDee+89Fmvy/gP3HEUKlUqNiYm5e/fuxLkwWmpqamY7OgIA 3nprs6qBQ0tLS2ZmZlpaWkJCgre3t6o1SRcXl9jY2LS0tKysrIkDqO7u7qysrLS0tMTERDabrSo6 3dHRcf369WlpaZmZmS0tLUgLRYWFZLK54klaunTplStXBgYG5L9CEFRTUxOMWLtZvHhxM4+n/u/r 9RaB9vb2srKy+/fvV1dX8/l8oVCI3EEnk8mzZ892c3MLDg4OCwsLCAjQ/4SPTCbbuTP1zJl/eXh6 Xr9+3ZfFmjRbT09PUVGR4s0PqkYlEATJB/dkMjk8PBw5dQEADA4O/vjjj/KNAm2MEInEsLAw5Bn7 z0+fTt25U/6ZwWAWFBR4eLgrFa+uroqMXKcIJ9y1K+348eMEgurBoI73+V/p7+/ncrn3798vQlBZ WdnR0aHD6FkNZaWl9vb2FArlu+++M6BZI7E7PU1xnVet+tukJ8EhCNqdnq7I5uJCV9/BG0awqaG3 tzcs7DUAcOm7d4+NjU23O5pJfucdhRLr129Q1V/W1v5Koz17LvF4/IULF9XYxMyri8bHxz8+ceKn n+5s2rQpMyND/9Z1iqHRaKoaVSbTm+33bN8RgqAnT56osYMZwa5cvnzq1KmQkJUff3zCzs5uut1B jZrNWAsLC19fX8VX+exIVWZsCPZTcfGevXv82OyzZ79yQQyFZzjIc1kwUDe4Qx7vV7/IiQHBKisr U1JSHBxon3/+ubHf5GRYvBheigdLIBBM+uYjOXb2f7YZdDpdzeM40wVrqK/fsSN5XAb9+9/nAwIC ptsddLDZ/nbPz45wudzBwSFVOXHgmUI4HJ7BVHega0YLVl9fH5+Q0Nkl+OKLL15+ebGqbFKpVOOa 3rTg7e39UsBL8s9/8Hjy3ctJGR4Zln9wdHRcvGiRGpszV7D6J08S4uNb29rOnT3397+Hqco2PDy8 Oz29sKhoKn3TEgqFEhMdI1/VFQr7SkpKVOVsfPpsczE0NFTDkUmjTED05vHjx8sCA+fOm1dYWKgq j0gkevz48bZtb7u40B8+fDSV7mlPb2/vypUh8ksdFBTc19c3Mc9Af3/QsmUAAAca7f79X9QbnImH IR49epSYmFheXu7HZudeuzbp+QOpVNra2trQ0NDW1rZx4yam2nZ/GrGzszt06FB9/SY+v7OysuL7 7y8nJ7+jlOfWrVvVNTUEIjE1JTUwcKkGi8a5sXSnrKyU7een/RUhEAjfXbgw3V6rA4Kg7IsX5dHX rq5zi4qKkL+W/+c/TCYDh8NtjY8fGBjUaG1mCVZWWioPBNMeD09PpTXyGQgEQd9fuuTu5gYAcHZ2 fv/99ysqKqqrqt4/epROp8+ysdm3f79SuJ8q9FqtNzjZFy/mFxSgOujw8pIlO1NTp/6tajpQ9+jR +W+/LS4u5vP5FArF3NycTCYHBgZu2hS9YsVyLQMdZpZgLwLC3t7Orq6xsTH5y6HRvvLYJBjGwEBL YgKJSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxj/A21IX6E7EshsAAAA AElFTkSuQmCC)
|
30,070
|
2,4984
|
0,0831
|
0,0374
|
1,1500
|
0,0430
|
1,1500
|
0,0430
|
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42,081
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38,0016
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0,9031
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0,4065
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0,2800
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0,1138
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0,2900
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0,1179
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58,123
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14,5005
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0,2495
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0,1123
|
0,0680
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0,0076
|
0,0750
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0,0084
|
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2dohCwAfPHiAZChpRbue6uvrkcRcKyurBQsWqLN8+vQp0hm3tbWFNx6pr6//4osv2tvbVV5iamqa lJTk5OSEHAFB8NSpU3l5eRi/gBL9/f3x8fElJSUpKSlaJz3y8/PT09P9/PwSE7+kUCgQ5sGRBuRy OfLGHwtInjS+PHv6tKmpCS4zLZhM5rsqzcwYDDtbO7jc1tbGqa3FWL92PZWVlSF9ZE9PTw0p3n/+ +SeSU+Dj4zN79uyBgYGkpKSOjg4NDTKLxTp58iQ62t7X17dr165Lly7pmhIkEAji4+OzsrIOHToU Ghqq2fhFS8uhg4cMKdSjR4/im/6gX5rAxCQX1HBqkGWuzHeZJibKnScYCoWC7M8hlUqe1D7BWL8W PclkMiTYDQBAUFCQkZGRSksQBJHZYgAA4L3hUlJS6uvrk5OTR0+5oImIiEhPT0ePWjs7O7dv3753 797nz59j+RoAANTU1ERHR2dlZR04cCAmJkZzJ0YqlR47foxTW7t79+4xrlzg8/my1+EfAAAApbx4 LPT09Ci94HAc56JpqG9AylZWVko7wyAoLVtCmjStaIk/vXz58tGjR3BZc6RgcHCwpaUFLpNIpKam pt27d1+/fj0jIwOdOa4SEokUFRVFpVITEhIaGv76wiKRKC0t7fbt29HR0WvWrJk/f77K9BiJRNLY 2JiXl3fhwoXh4eFjx47t3LlT62YSOdnZly9fXhEevut/d40x06GyshKZrISpqKjQdeKosrJSaUO9 qqqq4eFhvefRVAKCI+jd9Oh0uobvTjZ4fYrL5crlcixbdGjRU1VVFTLkdnJy0hApkMvlyBMGQVBG RgadTv/222+VutsaiIiImDdvXkpKSm5uLnJzm5ubDx48eObMGR8fHx8fn/feew9p6sRicX19fXV1 9cOHD3t7e319fZOTk8PCwrQOr2pra//99dcWFlZHjxwxH8OKGnjlz6VLl5SO37p16/vvv//ss8/U DYTRyOVyNpt99uxZpeN//PHH8ePHd+7cqWvqiwakEimSXgsAgOaFkyRUJ18ikYAKBZZQiiY9QRDE ZrORXQAWLlz4zjvvqDM2MjJCn7WxsTly5Ei0jhNAbm5u586di4qKunjxYlFRETLDw+fz7969e/fu XQAAYLmgextubm779+/fuHEjlm7QwMDAgaSkV6860tPTfX19sfuGkJubW1ZWplAonj9/XlZWNnpV e39//759+7KzswMCAqhUamBg4Pr165VsCgoKfvvtNwiC2tvbi4uL0T8zjEQiSU5OvnHjxuLFi42N jV1cXGJiYsbYlEIAoIBej2HHIwVNi57WrVuHxLhZLJaGR59Op8fFxSUnJ4vF4gULFmzbti0wMFAP h2g0WkRERHh4+KNHj4qKisrLyxsaGnp6eoaGhhANkclkc3Nza2trd3f3FStWhIaGYuxQQxD0fz/8 cCs/f/PmzzZv3qSHewAA2NjYeHl5AQDg4+OzceNGlfcEgiB4dzwAAJQ2YoSxtLSEK/H29o6MjFR3 Y+FNOOE/OsFhLexTgWg06YlMJsN7KWEkMjJy6dKlIAgyGIwxpp3QaLTAwMDAwECZTCYQCHg8Hp/P R4JShoaGNjY2lpaWZmZmOt3lsrLSEydOuLq6Hjp0UN3AQisBAQEBAQH6XYvg4eGhYSnsVEBJTRjv Ms5p3bgv8KVSqVZWVvptkaAEj8dL+ipJKpMdOXJU5UoKdI8Be4RwGkEikQwN9PnFsb8Z35ZlAnK5 /NSp70pKS/fs2RsWtkzlHKdUJgP+fqWOjIwgNoaGhm9GcreRkdGsWa+fTM2TEOLh11F+SysrjDPl b4ueODU15zLPkUgkNrsoIiJCpY1QIEASiX795dfHfwdKtm/fsX591AQ5Op6QyWR7e3vko4YQvAIE 0VF+OztbjP2Kt0VPwn7hkEikFHTVQHt7W3t7G1xe+eGH4+nahOLs7EIikeA+fm9vr7o4mVwuHxjo h8tkMtnNVW2cSIm3RU8GBobGxsaa+wEKhQKJdBsaGiJrBqdLUhQWvL29GQwGHIh59eqVSCRSOXUx JBLxeH+1T+bvvAMPRbHwtujJ29v7xo0bmnsMjx8/3peQAL/yotav375tG3x83rx5E+HihODs4uLt 5fWgqAgAgM6uzp7eXpV64vP5yPvOw8PDcZ4jxvrfFj0xGAwNC1BhDAzI5L8bf4c5Dvot8JjimJiY fLjqwyI2G4KgHn5Pc3Ozo6qhbltbm0AoBACARCJHfhRpqmbaeDRv7CJdPUBPw70xCyxH8/G6j+c5 OgIAIJGIS4pLVNo8fFgJD2+dXZwjIz/CXjmhpzeBf0TOtMW1HefN27p1K9yVvHv3rlDYr2QgGhoq uF8AAACZbLBlyxY7OzvsnhB6mvaMjMj/kRGKYWD/eUxMSEgwAAAcTg165RJMYWFhRWUlAADhK8P/ FR2tkzOEnqY9gj4BkgMyODDYj2HXdQsLi9TUEy7OzmKxODU19eXLV8gpDodz+PBhkUjE8vU9kXpC QwaAaibsP1lNfR48KKT8HSOIjYufbHe00N/f39raWl5evmPHDvQP+umGDaWlpa2trf39/ZprKCsr g1c7Ll36wbVr16qrqzPOnp3//vs0Gi0qKqq+vl4Pr/4KbREAAFD/7FlKaiocglqzZg36//FNQQoL C9js4t7eXiSrBwaCIHNzcyaTGRQUHBamJfWUy+WeP38+Pz+/u7ubQqEoFApXV1d4ZZ+6VGDNEHqa rkAQpFAo4G610mQIcgrjJIlQKOzs7JRIJAwGw9raWu/MC4DQEwG+EP1xAjwh9ESAJ4SeCPCE0BMB nhB6IsATQk8EeELoiQBPCD0R4AmhJwI8IfREgCeEngjwhNATAZ78P/HnzMOImFY5AAAAAElFTkSu QmCC)
|
58,123
|
0,9942
|
0,0171
|
0,0077
|
0,0425
|
0,0003
|
0,0435
|
0,0003
|
|
56,108
|
5,9955
|
0,1069
|
0,0481
|
0,0540
|
0,0026
|
0,0620
|
0,0030
|
|
-
|
100,0000
|
2,2217
|
1,0000
|
-
|
0,2585
|
-
|
0,2677
|
;
;
МПа;
МПа;
МПа.
Таблица Е.3 - Пример расчета давления насыщенных паров при температуре минус 30°С
|
|
|
|
|
|
|
|
|
Компо-
нент
|
Моляр-
ная масса , г/моль
|
Массовая доля , %
|
|
Моля-
рная доля
|
при 0,1 МПа
|
|
при 0,5 МПа
|
|
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30,070
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0,8900
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0,0396
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0,9000
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0,0400
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44,097
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1,9731
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0,8710
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0,1650
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0,1437
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0,1730
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0,1507
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42,081
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2,9551
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0,0702
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0,0310
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0,1930
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0,0060
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0,2100
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0,0065
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58,123
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4,0158
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0,0691
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0,0305
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0,2490
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0,0076
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0,2767
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0,0084
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h8tkMtnNVW2cSIm3RU8GBobGxsaa+wEKhQKJdBsaGiJrBqdLUhQWvL29GQwGHIh59eqVSCRSOXUx JBLxeH+1T+bvvAMPRbHwtujJ29v7xo0bmnsMjx8/3peQAL/yotav375tG3x83rx5E+HihODs4uLt 5fWgqAgAgM6uzp7eXpV64vP5yPvOw8PDcZ4jxvrfFj0xGAwNC1BhDAzI5L8bf4c5Dvot8JjimJiY fLjqwyI2G4KgHn5Pc3Ozo6qhbltbm0AoBACARCJHfhRpqmbaeDRv7CJdPUBPw70xCyxH8/G6j+c5 OgIAIJGIS4pLVNo8fFgJD2+dXZwjIz/CXjmhpzeBf0TOtMW1HefN27p1K9yVvHv3rlDYr2QgGhoq uF8AAACZbLBlyxY7OzvsnhB6mvaMjMj/kRGKYWD/eUxMSEgwAAAcTg165RJMYWFhRWUlAADhK8P/ FR2tkzOEnqY9gj4BkgMyODDYj2HXdQsLi9TUEy7OzmKxODU19eXLV8gpDodz+PBhkUjE8vU9kXpC QwaAaibsP1lNfR48KKT8HSOIjYufbHe00N/f39raWl5evmPHDvQP+umGDaWlpa2trf39/ZprKCsr g1c7Ll36wbVr16qrqzPOnp3//vs0Gi0qKqq+vl4Pr/4KbREAAFD/7FlKaiocglqzZg36//FNQQoL C9js4t7eXiSrBwaCIHNzcyaTGRQUHBamJfWUy+WeP38+Pz+/u7ubQqEoFApXV1d4ZZ+6VGDNEHqa rkAQpFAo4G610mQIcgrjJIlQKOzs7JRIJAwGw9raWu/MC4DQEwG+EP1xAjwh9ESAJ4SeCPCE0BMB nhB6IsATQk8EeELoiQBPCD0R4AmhJwI8IfREgCeEngjwhNATAZ78P/HnzMOImFY5AAAAAElFTkSu QmCC)
|
58,123
|
1,9750
|
0,0340
|
0,0150
|
0,0268
|
0,0004
|
0,0285
|
0,0004
|
|
56,108
|
1,0168
|
0,0181
|
0,0080
|
0,0360
|
0,0003
|
0,0420
|
0,0003
|
|
-
|
100,0000
|
2,2653
|
1,0000
|
-
|
0,1976
|
-
|
0,2063
|
;
;
МПа;
МПа;
МПа.
Таблица Е.4 - Пример расчета давления насыщенных паров при температуре минус 35°С
|
|
|
|
|
|
|
|
|
Компо-
нент
|
Моляр-
ная масса , г/моль
|
Массовая доля , %
|
|
Моля-
рная доля
|
при 0,1 МПа
|
|
при 0,5 МПа
|
|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAPZklEQVR4nO2ceVRTVx7HbxZCCBDZ ggJBWSQBA8GitSJo0aEM9KjYwQVoRaEKpwj2CG5wtAcdbW21i9o6rbZjq1iVg5y6QYEqQu0wbKVV URASUrZAgLCTkJD35o9o+hrI8rIAb8znr+Tm3t/95X3fu+vvPhwMw8AEdsBPtwMm0GESDGOYBMMY JsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjGESDGOYBMMYJsEwhkkwjEE0iJWh oaH29nYOh9PU1DQ0NCRPJJFI8+fPZzAYbm5uVlZWSkV+++234uLinTt3mpubG8QHJDAMj4+PAwBw OJw2mQEAZmZmE3+SSqWojBCJRG0y6wNOnxABqVRaVVVVUFBQUlLS1NTU09Mjk8mU8tjZ2bFYrJCQ kHXr1rHZbCLx2S2yf//+oqKi0tJSa2tr3d1XAYfDOXLkSH9/v0QigSCIQCBMmk0mk+HxeHNzc0dH x6ysrDlz5iB/7ezszMrKEggEY2NjMpmMQCBMKoZMJsPhcCQSycbG5uDBg56engb/O0h0FEwqlZaX l587d+727dt9fX0AADMzMy8vLz8/P19fX/lDI5PJuFzugwcP6uvrBwYGaDRaREREQkICk8msqalJ SkqaNWtWaWmpg4ODgf8TAMPDww8fPuzs7ORyuTdv3iwtLZ00W1BQ0Nq1a5lMppOTE5vNJpPJyF/F YvGDBw/4fD6Px7t161ZJScnE2xEAsGjRosjISG9vb2dnZ39//4ltiYGB0cPj8ZKSkmxsbOQWLC0t Y2Njb9y4wefzZTKZUuaBgYGKiordu3e7uroCAKhUqpeX16xZswAAc+fO/eOPP3RwABX9/f0ZGRmK J1sOHo9PTk7u7e3V0sjw8PBHH32kpCgAYOvWrV1dXUb1XwnUghUWFi5evFjh8cKFC/Py8sRiscaC v/766xtvvIFsVZydnZuamnRyGx3t7e3z589HXmg6nd7Y2IjKSH9/P/KPAwBsbW2rq6uN5LMq0AmW m5vr5OSk8Dg0NLShoUH74kKh8O2338bjnw1NqVRqVVUVSod1QSwWh4aGIq/1smXLhoeHURmBICg6 OhppxMfHRyAQGMlnVaAY1l+/fj0lJYXP58u/vvLKK1999RWDwdDegq2t7YkTJ2JiYuRfZTKZRCLR vrjO4PF4pUGgmZmZqpGIKuQjC2QKkUhEa0R/tBWssrIyPT29s7NT/tXBweGDDz7w8PBAW5+Njc3h w4cXLlwIABCLxQKBAK0Fg2CQ8TeRSFS0FlOGVvV1d3fv27ePw+HIv+JwuKSkpFdffVW3Kj08PDIy MshkMgRB8onO1DN79mylx0UHaDQahUIxiD/ao1kwGIa/+eabsrIyRQqdTt+8ebM+N9frr7++fPly GIa7urp0NqIPBnnCVM3MjIrmi15XV3fmzBkIghQpUVFRXl5e+tRqZWWVmJhIIpFGR0f1sfMCokEw GIazs7NbW1sVKZaWlpGRkfq33StXrmQwGIohjAkt0XDdeTzetWvXkCne3t7+/v76V2xvb79q1aqR kRH9Tb1QaFj8LSkpUYw15Pj7+yvWOPQkJSVFKBQaxNSLgzrBZDJZSUkJ/NfFxoCAAEP1tHp2hC8m 6prErq6uiooKZIq5uTmqmbIJg6NOsObm5o6ODmSKpaWlo6OjkV0yoQ51gnG5XKVht7W1ta2trZFd mgp0a9WnftY1EXV9mHwpHZlCpVKNvt8zJfT29tbW1upQyhjOoEKdYP/Hs9rCwkJVu5pqEIvFxnAG FYaJ6cAc5ubmDg4OqJo4GIa7u7una/FTwQsqWHh4+MmTJ9GWevfdd3Nzc43hj/aoE2ziZs9M6HUN AoVCcXZ21qGUMZxBhbpRInJzWY5EIpGHj5mYLtQ9Yba2tjjcX8Kq+vr6+vr6pnIq1tHRUVdX9/Tp U5FIRCKR3NzcfH193d3d/2+edbFY3NLS0tTY2MThiEQiKyur6Ohoe3t7VfnVCcZisWxsbORRbHIG Bwc7OjqYTKYhXVZBb2/v1+fOXczO5nA4iuEZkWhGp7usXr1mx44d3t5T4YbxaG5uvnnzZn5+fl1d nYWFhY+PD4vFmjNnDpE4SUjrn6iJ9+jp6WGz2Ur5T506ZfRAExjmcjlrVq9W8xh5e/vk5+draU0i kURERCCLx8XF6eBVXFwc0khERIREItHBzsDAwMnPPmMyGAAAJtP71OnTjY2NWppSJ5hMJlNyEQCw detWCIJ08FJ7+vv7o6L+Ia/O2trax8dn6dKlnp6eSpv6rq5z7927p43BGSXY47q6N9atIxAIBAIh Pj4ebbSdhjC33NxcpcvEZDLb2trQeomKk599hsfjqVTqO8nJZWVlXV1dQ0NDra2tOTlXlwcHI51Z vnxFT0+PRoMzR7A7d37y8/UFAFhYUI4cOToyMoLWBw2CCYXCJUuWIL0kEonZ2dloq1HF4OCgUChE pnQLBP7+bCcnp5ycHKlUqpS/tbV1zZo1SGcuX76isZYZIlhxUZG7uzsAwMzM7PA//6lbc6phx9nW 1nbjxo3IgIDx8fFLly4ZZKdYJBLt2bPnwoULyMT/VlRwOc1Zhw5t2LBBKb4aAECn0z/99NMFC3wU zhQVFUEQBl75+PPPZYlJic3NzQCAuC1b0nbtmvS8jEY0h2Zs3rw5MDAQmXL37t28vDwdKkMCw/DZ s2d/+eUXpXv/57KypYGBb8bGqiro6em5JW6LYjjC4/EkkjE9nTE2PB4vbVdaczMPAMD29z944ICl paVupjQL5ujomJmZSaVSFSljY2PHjh1rbGzUrUo5N27cOHbsWGpqKnJHFIZhBoORnp6u/v8ELw9W ZIB1On0jEomQcWC6IRaLtVlGkEjGPvzwWHVNDQCATCbv3bN33rx5uteqTbspkUj27t2rFCkVFRXV 3d2tQysMw3BBQYGrq+u2bdtGR0d1KN7Y2OjyfGEpav368fFx9fkn9mEhISEikQhtvUp9GJvN1ub8 y80bN6ye316vhYUNDQ2hrReJVtFqZmZmGRkZGzZsQCbm5eWlpKRwuVy0t0h+fv727ds9PDwOHz5s YWGBtjiQL2k+bxNZC1g6BLjDU/Wm45GR4TP/OjM8MgIAIBAIMdExem4oartab2Njc/LkSTwef/ny ZXkKDMNXr15taGg4ePBgeHi4NgujQ0ND58+fP3r0qKen55dffjlxrVJL+vqEw0NDAABra2po6N80 5heJREp7j6OjoxKJZOJ5LzVIJBKlOOXR0dGxMQ3d572Se/fuPdt4c3f3eC3sNQiC2tranjY0NPN4 4+PjNBqNxfL18po/cYQ1OaieR4FAsH37dqVTyRQKJTIy8ocffuDz+aoK8vn8a9euRUREkEik8PDw +vp6fZqFb8+fl7fPa9auHdGiUf3999+V1j9pNFptbS2qSpuampT6Hisrqzt37qgpIpPJtm/fpsj/ 5ptvldy9uyUubt68eYrZLYFAcHZ2TkxMevpUqxk06gN9o6OjX3/9tY+Pj5LwJBKJxWLFx8cfP378 ypUrOTk5OTk5V69e/eSTT+Lj4xcsWEAgEKytrfft26fNVFcNUqk0NiYGAGBpaXn79m2N+ZubmxUH nJCsXr26trZWY/8np7W1dcuWLROXylasWFFeXq5qRtXe3sZk/jmk8vDwcHZ2DgoKOnDgwOnTp5OS kuguLopfX3opoLJS82k5XY7MwjDM4XDee+89Fmvy/gP3HEUKlUqNiYm5e/fuxLkwWmpqamY7OgIA 3nprs6qBQ0tLS2ZmZlpaWkJCgre3t6o1SRcXl9jY2LS0tKysrIkDqO7u7qysrLS0tMTERDabrSo6 3dHRcf369WlpaZmZmS0tLUgLRYWFZLK54klaunTplStXBgYG5L9CEFRTUxOMWLtZvHhxM4+n/u/r 9RaB9vb2srKy+/fvV1dX8/l8oVCI3EEnk8mzZ892c3MLDg4OCwsLCAjQ/4SPTCbbuTP1zJl/eXh6 Xr9+3ZfFmjRbT09PUVGR4s0PqkYlEATJB/dkMjk8PBw5dQEADA4O/vjjj/KNAm2MEInEsLAw5Bn7 z0+fTt25U/6ZwWAWFBR4eLgrFa+uroqMXKcIJ9y1K+348eMEgurBoI73+V/p7+/ncrn3798vQlBZ WdnR0aHD6FkNZaWl9vb2FArlu+++M6BZI7E7PU1xnVet+tukJ8EhCNqdnq7I5uJCV9/BG0awqaG3 tzcs7DUAcOm7d4+NjU23O5pJfucdhRLr129Q1V/W1v5Koz17LvF4/IULF9XYxMyri8bHxz8+ceKn n+5s2rQpMyND/9Z1iqHRaKoaVSbTm+33bN8RgqAnT56osYMZwa5cvnzq1KmQkJUff3zCzs5uut1B jZrNWAsLC19fX8VX+exIVWZsCPZTcfGevXv82OyzZ79yQQyFZzjIc1kwUDe4Qx7vV7/IiQHBKisr U1JSHBxon3/+ubHf5GRYvBheigdLIBBM+uYjOXb2f7YZdDpdzeM40wVrqK/fsSN5XAb9+9/nAwIC ptsddLDZ/nbPz45wudzBwSFVOXHgmUI4HJ7BVHega0YLVl9fH5+Q0Nkl+OKLL15+ebGqbFKpVOOa 3rTg7e39UsBL8s9/8Hjy3ctJGR4Zln9wdHRcvGiRGpszV7D6J08S4uNb29rOnT3397+Hqco2PDy8 Oz29sKhoKn3TEgqFEhMdI1/VFQr7SkpKVOVsfPpsczE0NFTDkUmjTED05vHjx8sCA+fOm1dYWKgq j0gkevz48bZtb7u40B8+fDSV7mlPb2/vypUh8ksdFBTc19c3Mc9Af3/QsmUAAAca7f79X9QbnImH IR49epSYmFheXu7HZudeuzbp+QOpVNra2trQ0NDW1rZx4yam2nZ/GrGzszt06FB9/SY+v7OysuL7 7y8nJ7+jlOfWrVvVNTUEIjE1JTUwcKkGi8a5sXSnrKyU7een/RUhEAjfXbgw3V6rA4Kg7IsX5dHX rq5zi4qKkL+W/+c/TCYDh8NtjY8fGBjUaG1mCVZWWioPBNMeD09PpTXyGQgEQd9fuuTu5gYAcHZ2 fv/99ysqKqqrqt4/epROp8+ysdm3f79SuJ8q9FqtNzjZFy/mFxSgOujw8pIlO1NTp/6tajpQ9+jR +W+/LS4u5vP5FArF3NycTCYHBgZu2hS9YsVyLQMdZpZgLwLC3t7Orq6xsTH5y6HRvvLYJBjGwEBL YgKJSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxgmwTCGSTCMYRIMY5gEwxj/A21IX6E7EshsAAAA AElFTkSuQmCC)
|
30,070
|
6,0832
|
0,2023
|
0,0893
|
0,760
|
0,0679
|
0,775
|
0,0692
|
![](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAJAAAABWCAIAAACvlYhGAAAQAklEQVR4nO2ce1QT177H94S8TEwI D4NCBEQeYqxwqBVZojwKVVqVauvzHDyiR0GW9mjVot571rEvxaVLpVYUK/aiWIEKVKqgeCiP2lIQ LHINRXmUhyRAQgB5BBJm5v4xNidnAslMCEKu+fw1mez927+Z7zx+e+/fHghFUWDGdKBMtANmyGEW zMQwC2ZimAUzMcyCmRhmwUwMs2AmhlkwE8MsmIlhFszEMAtmYpgFMzHMgpkYZsFMDLNgJoZZMBPD LJiJQTWKld7e3tbW1vr6+rq6ut7eXmwnnU53dXV1d3d3dnaeOnUqrkplZeW9e/c++OADBoNhFB8w YBhGEASCICKFURSlUCgWFha4/QiCwDA8RiPjxJgEU6lUDx48yM3NLSgoqKurk8lkMAzjylhbWwuF wsDAwHfffXf+/PlU6osWU1NT8/LyoqOjjStYamrqzZs3BwcHVSoVBEEUygiPEBRFYRim0WhMJjMo KCgmJgZXICcn5+rVq4ODg0qlUrcRKpXKYDAWLly4f//+l6MZZFhOh0qlKikp+eqrr27fvt3V1QUA oNFobm5ur7322rx58zANYBhuaGioqqqqqanp6emZNm1aWFjY1q1bPTw8KioqoqKiLC0ti4qKbG1t jXg8jY2NDQ0NEomkvLw8KyurqalJuwyXyw0PDw8ICHB0dHR2dnZzc8MVaG1tra2tlUgkv/76a1ZW Vl1dnbYRNpsdFhYWEhIiEAhmzZrl6elJ8I4cKyh5Ghsbo6KieDye2vVNmzZlZ2dLJBIYhnGFe3p6 SktL9+/fP3PmTAAAl8t1c3OztLQEADg6OjY1NRngAEGqqqoWLVqEO14+n5+VlaXt52jU1tYuW7YM 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|
58,123
|
5,1272
|
0,0882
|
0,0389
|
0,034
|
0,0013
|
0,040
|
0,0016
|
|
58,123
|
7,0818
|
0,1218
|
0,0538
|
0,019
|
0,0010
|
0,021
|
0,0011
|
|
-
|
100,0000
|
2,2652
|
1,0000
|
-
|
0,1765
|
-
|
0,1840
|
;
;
МПа.
МПа;
МПа.
Библиография
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|
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[1]
|
РМГ 61
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Государственная система обеспечения единства измерений. Показатели точности, правильности, прецизионности методик количественного химического анализа. Методы оценки
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[2]
|
РМГ 76
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Государственная система обеспечения единства измерений. Внутренний контроль качества результатов количественного химического анализа
|
[3]
|
РМГ 91
|
Государственная система обеспечения единства измерений. Совместное использование понятий "погрешность измерения" и "неопределенность измерения". Общие принципы
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УДК 661.715-404:543.272.7:006.354
|
МКС 75.160.30
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Ключевые слова: сжиженные углеводородные газы, расчетный метод определения плотности, определение давления насыщенных паров
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