Low-carbon acid gas removal technique and system for high methane gas
A process method, methane-enriched technology, applied in gas fuel, petroleum industry, fuel and other directions, can solve huge environmental, industrial development disputes and restrictions, etc., to reduce atmospheric emissions, reduce construction investment and operation consumption, and economic benefits. obvious effect
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[0022] Example 1 :
[0023] See figure 2 , The crude gas produced by SHELL waste boiler process pulverized coal gasification technology enters the shift methanation system, the temperature of the crude gas is 167℃, the pressure is 3.8MPa (A), the CO content is 70.96% (dry basis, volume), H 2 The content is 19.97% (dry basis, volume), CO 2 The content is 7.58% (dry basis, volume). The crude gas reacts in the shift methanation system to produce CO rich 2 And CH 4 After cooling and gas-liquid separation treatment, the methane-rich gas is sent to the low carbon dioxide gas removal system of the present invention. The temperature is controlled at about 40°C, the pressure is about 3.0MPa (A), and CO 2 The content is 69.49% (dry basis, volume), CH 4 The content is 28.20% (dry basis, volume).
[0024] In the present invention, the methane-rich gas is first cooled to about 10°C by 1# methane-rich gas cooler 1, and then enters the methane-rich gas water washing tower 2, and the boiler feed...
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[0025] Example 2 :
[0026] See figure 2 , The crude gas produced by GE's coal water slurry gasification technology enters the shift methanation system. The temperature of the crude gas is 242℃, the pressure is 6.5MPa (A), and the CO content is 41.77% (dry basis, volume). 2 The content is 34.81% (dry basis, volume), CO 2 The content is 22.72% (dry basis, volume). The crude gas reacts in the shift methanation system to produce CO rich 2 And CH 4 After cooling and gas-liquid separation treatment, the methane-rich gas is sent to the low carbon dioxide gas removal system of the present invention. The temperature is controlled at about 40°C, the pressure is about 5.5MPa (A), and CO 2 The content is 69.32% (dry basis, volume), CH 4 The content is 29.35% (dry basis, volume).
[0027] In the present invention, the methane-rich gas is first cooled to about 15°C by 1# methane-rich gas cooler 1, and then enters the methane-rich gas water washing tower 2, and the boiler feed water cooled to ...
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