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Influence of mid-point temperature of heavy hydrocarbons separator to the liquefaction process for small LNG plant
- Source :
- IOP Conference Series: Materials Science and Engineering. 162:012007
- Publication Year :
- 2016
- Publisher :
- IOP Publishing, 2016.
-
Abstract
- In liquefied natural gas (LNG) process production, one of the important units is heavy hydrocarbon removal unit to prevent freezing during liquefaction. For small scale of LNG plant, this unit is usually integrated with main heat exchanger. Feed is obtained from main heat exchanger then flows to separator to separate liquid from gas. The separator operating condition is called as Midpoint condition. Selecting Midpoint conditions have impact to light hydrocarbon losses, Specific Brake Horse Power (SBHP) process, and heating value of LNG. Hence understanding of selecting this condition and its effect to light hydrocarbon losses, SBHP process, and HHV of LNG will help to design more efficient LNG plant. According to study, the lower of Mid-Point temperature will result in lower SBHP, lower of light hydrocarbon losses, and increase LNG of HHV value. Meanwhile, the higher Mid-Point pressure will result in lower SBHP, higher light hydrocarbon losses, and lower LNG of HHV value. The change of Mid-Point pressures have more impact to light hydrocarbon losses than SBHP process.
- Subjects :
- chemistry.chemical_classification
Engineering
Petroleum engineering
Waste management
business.industry
020209 energy
Liquefaction
Separator (oil production)
02 engineering and technology
010502 geochemistry & geophysics
01 natural sciences
Hydrocarbon
chemistry
Heat exchanger
0202 electrical engineering, electronic engineering, information engineering
Heat of combustion
business
0105 earth and related environmental sciences
Liquefied natural gas
Subjects
Details
- ISSN :
- 1757899X and 17578981
- Volume :
- 162
- Database :
- OpenAIRE
- Journal :
- IOP Conference Series: Materials Science and Engineering
- Accession number :
- edsair.doi...........ebe799e3bd8fc6f66b55765d716969f1
- Full Text :
- https://doi.org/10.1088/1757-899x/162/1/012007