Minitype skid-mounted single-level mixed refrigerant natural gas liquefaction system and method thereof
A technology of mixing refrigerant and natural gas, applied in refrigeration and liquefaction, liquefaction, gas fuel and other directions, can solve the problems of complex process, large differences in biogas natural gas components, and many equipment, etc. low consumption effect
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Embodiment 1
[0051] Natural gas molar composition 92% CH 4 +4%C 3 h 8 +4%N 2 , pressure 1.2MPa, temperature 30°C, flow rate 1kmol / h; mixed refrigerant flow rate 2.84kmol / h. The specific steps of the small skid-mounted single-stage mixed refrigerant natural gas liquefaction process are as follows:
[0052] 1. Natural gas raw material is compressed to 2.8MPa by two-stage compressors (first-stage compressor 1, natural gas second-stage compressor 3), and then passed through coolers (natural gas first-stage cooler 2, natural gas second-stage water cooler 4) Cool to 40°C;
[0053] 2. The natural gas cooled in step 1 enters deacidification tower 5 and dehydration tower 6 to remove CO 2 , H 2 S, H 2 O and other impurities;
[0054] 3. The natural gas purified in step 2 is cooled to -60°C (heavy hydrocarbon separation temperature) through the first stage heat exchanger 7 and then enters the heavy hydrocarbon separator 8 to obtain heavy hydrocarbons from the bottom;
[0055] 4. The natural ...
Embodiment 2
[0065] Natural gas molar composition 90% CH 4 +6%C 3 h 8 +4%N 2 , pressure 1.7MPa, temperature 25°C, flow rate 1kmol / h, mixed refrigerant flow rate 2.79kmol / h. The specific steps of the small skid-mounted single-stage mixed refrigerant natural gas liquefaction process are as follows:
[0066] 1. Natural gas raw material is compressed to 2.8MPa by two-stage compressors (first-stage compressor 1, natural gas second-stage compressor 3), and then passed through coolers (natural gas first-stage cooler 2, natural gas second-stage water cooler 4) Cool to 40°C;
[0067] 2. The natural gas cooled in step 1 enters deacidification tower 5 and dehydration tower 6 to remove CO 2 , H 2 S, H 2 O and other impurities;
[0068] 3. The natural gas purified in step 2 is cooled to -60°C (heavy hydrocarbon separation temperature) through the first stage heat exchanger 7 and then enters the heavy hydrocarbon separator 8 to obtain heavy hydrocarbons from the bottom.
[0069] 4. The natural ...
Embodiment 3
[0079] Natural gas molar composition 80% CH 4 +6%C 3 h 8 +14%N 2 , pressure 2.8MPa, temperature 20°C, flow rate 1kmol / h, mixed refrigerant flow rate 2.85kmol / h. The specific steps of the small skid-mounted single-stage mixed refrigerant natural gas liquefaction process are as follows:
[0080] 1. The raw material pressure of natural gas reaches 2.8MPa, so the natural gas compression link can be omitted;
[0081] 2. Natural gas enters deacidification tower 5 and dehydration tower 6 to remove CO 2 , H 2 S, H 2 O and other impurities;
[0082] 3. The natural gas purified in step 2 is cooled to -60°C (heavy hydrocarbon separation temperature) through the first stage heat exchanger 7 and then enters the heavy hydrocarbon separator 8 to obtain heavy hydrocarbons from the bottom.
[0083] 4. The natural gas after removing heavy hydrocarbons in step 3 is cooled to -159°C through the second stage heat exchanger 9;
[0084] 5. The natural gas obtained in step 4 passes through a...
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