Liquefied Natural Gas Pretreatment Equipment and Method Combining Membrane Separation and Temperature Swing Adsorption
A technology of liquefied natural gas and temperature swing adsorption, which is applied in separation methods, chemical instruments and methods, and gas treatment, and can solve problems such as large investment, numerous equipment, and complicated liquefied natural gas pretreatment process
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Embodiment 1
[0022] See attached figure 1. The liquefied natural gas pretreatment equipment combined with membrane separation and temperature swing adsorption includes a temperature swing adsorption heavy hydrocarbon removal system 1, a membrane separation system 2, a retentate gas cooling system 3, a temperature swing adsorption carbon dioxide removal system 4 and a regeneration gas booster 5; The heavy hydrocarbon removal system inlet pipe 11 of the temperature swing adsorption heavy hydrocarbon removal system 1 is used to feed raw natural gas; the heavy hydrocarbon removal system outlet pipe 12 of the temperature swing adsorption heavy hydrocarbon removal system 1 is separated from the membrane of the membrane separation system 2 through the pipeline. The inlet 21 is connected, and is used for the natural gas after the heavy hydrocarbon removal by the temperature swing adsorption deheavy hydrocarbon system 1 to enter the membrane separation system 2; The hydrocarbon system regeneration...
Embodiment 2
[0024] See attached figure 1. The liquefied natural gas pretreatment equipment combined with membrane separation and temperature swing adsorption includes a temperature swing adsorption heavy hydrocarbon removal system 1, a membrane separation system 2, a retentate gas cooling system 3, a temperature swing adsorption carbon dioxide removal system 4 and a regeneration gas booster 5; The heavy hydrocarbon removal system inlet pipe 11 of the temperature swing adsorption heavy hydrocarbon removal system 1 is used to feed raw natural gas; the heavy hydrocarbon removal system outlet pipe 12 of the temperature swing adsorption heavy hydrocarbon removal system 1 is separated from the membrane of the membrane separation system 2 through the pipeline. The inlet 21 is connected, and is used for the natural gas after the heavy hydrocarbon removal by the temperature swing adsorption deheavy hydrocarbon system 1 to enter the membrane separation system 2; The hydrocarbon system regeneration...
Embodiment 3
[0031] See attached figure 1. The liquefied natural gas pretreatment method combined with membrane separation and temperature swing adsorption adopts the above-mentioned liquefied natural gas pretreatment equipment combined with membrane separation and temperature swing adsorption, comprising the following steps:
[0032] In the first step, the raw natural gas with a pressure of 3-10 MPa and a carbon dioxide content higher than 2% passes through the filter 17 to filter solid and liquid impurities, and then enters the heavy hydrocarbon removal system inlet pipe 11 into the temperature swing adsorption heavy hydrocarbon removal system 1 for heavy hydrocarbon removal treatment ;
[0033] In the second step, after the heavy hydrocarbon content of the heavy hydrocarbon removal gas meets the requirements of natural gas liquefaction, it comes out from the outlet pipe 12 of the heavy hydrocarbon removal system, filters solid and liquid impurities through the filter 17, and then is he...
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