Methanation technology for preparing SNG from coal-based synthetic gas
A coal-based synthesis gas and methanation technology, applied in the petroleum industry, gas fuel, fuel, etc., can solve the problems of increasing power consumption of cycle gas, increasing equipment investment, and large amount of cycle gas
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Embodiment 1
[0025] according to figure 1 As shown in the process flow, the pressure is 1.0MPa, and the space velocity is 10000h -1 of syngas and the total sulfur in the syngas is less than 0.1*10 -6 , scaling factor f=(n H2 -n CO2 ) / (n CO +n CO2 )=2.8, the obtained syngas composition (vol%) is: H 2 : 67.08%, CH 4 : 9.2%, CO: 21.17%, CO 2 : 2.05%, N 2 : 0.5%. Synthetic gas is divided into four streams (fresh gas A, B, C, D), fresh gas A is mixed with the gas that has been heat-exchanged by the circulating gas preheater E4 to form a reverse and one-stage intake air, and then enters through the feed gas heater E3 In the first stage of the first methane synthesis reactor R2, the gas inlet temperature is 280°C, and the temperature rises to 510°C after the reaction. After the first stage of reaction, the outlet gas is mixed with the fresh gas B of the second stage to form a first stage of reaction. The second stage enters the first methane In the second stage of the synthesis reactor ...
Embodiment 2
[0027] according to figure 1 As shown in the process flow, the pressure is 5.5MPa, and the space velocity is 20000h -1 of syngas and the total sulfur in the syngas is less than 0.1*10 -6 , scaling factor f=(n H2 -n CO2 ) / (n CO +n CO2 )=3.1, the obtained syngas composition (vol%) is: H 2 : 69.5%, CH4 : 8.21%, CO: 19.84%, CO 2 : 1.95%, N 2 : 0.5%. Synthetic gas is divided into four streams (fresh gas A, B, C, D), fresh gas A is mixed with the gas that has been heat-exchanged by the circulating gas preheater E4 to form a reverse and one-stage intake air, and then enters through the feed gas heater E3 In the first stage of the first methane synthesis reactor R2, the gas inlet temperature is 280°C, and the temperature rises to 530°C after the reaction. After the first stage of reaction, the outlet gas is mixed with the fresh gas B of the second stage to form a first stage of reaction. The second stage enters the first methane In the second stage of the synthesis reactor R2...
Embodiment 3
[0029] according to figure 1 As shown in the process flow, the pressure is 8MPa, and the space velocity is 30000h -1 of syngas and the total sulfur in the syngas is less than 0.1*10 -6 , scaling factor f=(n H2 -n CO2 ) / (n CO +n CO2 )=3.0, the obtained synthesis gas composition (vol%) is: H 2 : 68.5%, CH 4 : 8.82%, CO: 20.23%, CO 2 : 1.95%, N 2 : 0.5%. Synthetic gas is divided into four streams (fresh gas A, B, C, D), fresh gas A is mixed with the gas that has been heat-exchanged by the circulating gas preheater E4 to form a reverse and one-stage intake air, and then enters through the feed gas heater E3 In the first section of the first methane synthesis reactor R2, the gas inlet temperature is 290°C, and the temperature rises to 535°C after the reaction. After the first stage of reaction, the outlet gas is mixed with the fresh gas B of the second stage to form a first stage of reaction. The second stage enters the first methane In the second stage of the synthesis r...
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