کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
761381 896625 2011 4 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Improved processes of light hydrocarbon separation from LNG with its cryogenic energy utilized
موضوعات مرتبط
مهندسی و علوم پایه مهندسی انرژی انرژی (عمومی)
پیش نمایش صفحه اول مقاله
Improved processes of light hydrocarbon separation from LNG with its cryogenic energy utilized
چکیده انگلیسی

Liquefied natural gas (LNG) often consists of some kinds of light hydrocarbons other than methane, such as ethane, propane and butane, which are of high additional value. By efficiently utilization of LNG cryogenic energy, these light hydrocarbons (C2+) can be separated from LNG with low power consumption and LNG is gasified meanwhile. Two novel light hydrocarbon separation processes are proposed in this paper. The first process uses a demethanizer working at higher pressure (about 4.5 MPa). The methane-riched natural gas from the demethanizer can be compressed to pipeline pressure with low power consumption. The other one uses a demethanizer working at lower pressure (about 2.4 MPa). By cascade utilization of LNG cryogenic energy, the methane-riched natural gas from the demethanizer is entirely re-liquefied. Then the liquid product is pressurized to pipeline pressure by pumps instead of compressors, reducing the power consumption greatly. By both of the two processes, liquefied ethane and LPG (liquefied petroleum gas, i.e. C3+) at atmosphere pressure can be obtained directly, and high ethane recovery rate can be gained. On the basis of one typical feed gas composition, the effects of the ethane content and the ethane price to the economics of the light hydrocarbon separation plants are studied, and the economics are compared for these two processes. The results show that recovering light hydrocarbons from LNG can gain great profits by both of the two processes, and from the view of economics, the low pressure process is better than the high pressure process.

Research highlights
► We propose two new light hydrocarbon separation processes utilizing LNG cold energy.
► Both processes produce liquefied ethane and LPG with high ethane recovery rate.
► CH4-riched gas from the high pressure process is compressed to final pressure.
► Re-liquefied CH4-riched gas from the low pressure one is pumped to final pressure.
► Both processes have good performance; the low pressure one is economically better.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Energy Conversion and Management - Volume 52, Issue 6, June 2011, Pages 2401–2404
نویسندگان
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