Simulation of chemical and technological processes of a hydrocarbon preparation plant
Autor: | O. M. Khukhryanskyy, V. V. Kovtun, V. F. Moiseev, V. M. Marenok, Oleksandr Oleksandrovych Liaposhchenko, O. Ye. Starynskyy |
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Rok vydání: | 2019 |
Předmět: |
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chemistry.chemical_classification Process equipment business.industry Fossil fuel Separator (oil production) Compressed natural gas Bandwidth throttling propane-butane low-tonnage Thermodynamic model Hydrocarbon chemistry computer simulation Environmental science Process engineering business throttle effect |
Zdroj: | JOURNAL OF HYDROCARBON POWER ENGINEERING. 6:7-13 |
ISSN: | 2415-3370 2311-1399 |
DOI: | 10.31471/2311-1399-2019-1(11)-7-13 |
Popis: | This article presents a low-tonnage oil and gas processing plant (OGPP-20), its main process equipment and the operating principle. Three methods for producing a liquefied propane-butane fraction and designs of the equipment for its implementing are proposed: compression and condensation, compression and further throttling which allows the compressed gas cool to lower temperatures and rectification. The results of numerical studies of the methods of producing liquefied propane-butane in the Aspen HYSYS program for the thermodynamic model of Peng–Robinson substantiate the method of obtaining the liquefied propane-butane fraction and its design. |
Databáze: | OpenAIRE |
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