Proceedings of the 1st Annual Gas Processing Symposium 2009
DOI: 10.1016/b978-0-444-53292-3.50021-3
|View full text |Cite
|
Sign up to set email alerts
|

Development in Mixed Refrigerant Cycles Used in Olefin Plants

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

0
8
0

Year Published

2010
2010
2023
2023

Publication Types

Select...
9

Relationship

0
9

Authors

Journals

citations
Cited by 9 publications
(8 citation statements)
references
References 4 publications
0
8
0
Order By: Relevance
“…If the initial gas temperature is lower than the maximum inversion temperature (μ JT = 0) then the temperature decreases as a result of the choking process. For all gases (except helium, H 2 , and Ne), the peak inversion temperature is higher than the environment. , Therefore, to decrease the H 2 temperature using the J–T process, it is necessary to first cool its temperature to less than the H 2 inversion temperature (205 K). As a result, H 2 gas cannot be liquefied at ambient temperature only by using the J–T process, and a precooling process is necessary …”
Section: Description Of Liquid Hydrogen Technologiesmentioning
confidence: 99%
“…If the initial gas temperature is lower than the maximum inversion temperature (μ JT = 0) then the temperature decreases as a result of the choking process. For all gases (except helium, H 2 , and Ne), the peak inversion temperature is higher than the environment. , Therefore, to decrease the H 2 temperature using the J–T process, it is necessary to first cool its temperature to less than the H 2 inversion temperature (205 K). As a result, H 2 gas cannot be liquefied at ambient temperature only by using the J–T process, and a precooling process is necessary …”
Section: Description Of Liquid Hydrogen Technologiesmentioning
confidence: 99%
“…Typically, in conventional olefin plants, propene refrigeration cycles (assumed as "Refrigerant 1") are used to cool streams to −35 °C and ethene refrigeration (assumed as "Refrigerant 4") is utilised to cool to around −100 °C. 81 Therefore, literature was sought to find both the energy source and intensity of such refrigeration cycles.…”
Section: Life-cycle Assessment (Lca)mentioning
confidence: 99%
“…Ethylene plants are important industrial plants where paraffin feedstocks such as ethane, propane and naphtha are processed and converted into ethylene. The ethylene production is economically important but highly energy-intensive process [42]. Steam cracking of naphtha at high temperatures is the most common method for ethylene production.…”
Section: Ethylene Plant and Liquid Emissionsmentioning
confidence: 99%