Method for producing liquefied natural gas by automatically supplementing carbon by using retort gas as raw material
A technology for liquefied natural gas and dry distillation gas, which is applied in the direction of gas fuel, combustible gas purification, combustible gas purification/transformation, etc., can solve the problems of complex process, difficult coal dry distillation enterprise promotion, large one-time investment, etc., to achieve simple process, Improvement of environmental quality and low investment in equipment
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Embodiment 1
[0098] Limestone ore composition (wt%): CaO 54.3%, burning loss rate 42.7%, impurity 3.0%.
[0099] The furnace coal is composed of 30% lean coal, 35% 1 / 3 coking coal, 20% fat coal and 15% main coking coal; its quality index (wt%): V adf 30.0%, A d 13.5%, FC d 60.6%, S t,d 0.67%, cohesion index G=74, fineness (≤3mm)=73.6%.
[0100] The coal into the furnace was tested in a 40kg small coke oven (the furnace charge was isolated from the air and continuously heated for 24 hours, the temperature of the center of the furnace charge reached 1100°C before being released from the furnace, and it was cooled to room temperature after coke quenching): the gas production rate of the furnace charge was 353.4 Nm 3 / t; In dry distillation gas before adding carbonate carbon replenishing raw materials: H 2 60.1%, CH 4 22.8%, CO6.8%, CO 2 2.3%, the rest is N 2 、C m h n , O 2 Wait. CO 2 The conversion ratio is calculated as 0.60, and the hydrogen-to-carbon ratio is calculated as 3.0...
Embodiment 2
[0113] Dolomite ore composition (wt%): CaO 30.4%, MgO 21.7%, burning loss rate 47.4%, impurity 0.46%.
[0114] The furnace coal is composed of 30% lean coal, 35% 1 / 3 coking coal, 20% fat coal and 15% main coking coal; its quality index (wt%): V adf 30.0%, A d 13.5%, FC d 60.6%, S t,d 0.67%, cohesion index G=74, fineness (≤3mm)=73.6%.
[0115] The coal into the furnace was tested in a 40kg small coke oven (the charge was continuously heated for 20 hours without air, and the center temperature of the charge reached 1050°C before being released from the furnace, and it was cooled to room temperature after coke quenching): the gas production rate of the charge into the furnace was 353.4 Nm 3 / t; In dry distillation gas before adding carbonate carbon replenishing raw materials: H 2 57.5%, CH 4 24.5%, CO7.5%, CO 2 2.8%, the rest is N 2 、C m h n , O 2 Wait. CO 2 The conversion ratio is calculated as 0.55, and the hydrogen-to-carbon ratio is calculated as 3.20. According ...
Embodiment 3
[0128] Siderite composition (wt%): FeO 52.7%, burning loss rate 26.3%, impurity 21.0%.
[0129] The furnace coal is composed of 30% lean coal, 35% 1 / 3 coking coal, 20% fat coal and 15% main coking coal; its quality index (wt%): V adf 30.0%, A d 13.5%, FC d 60.6%, S t,d 0.67%, cohesion index G=74, fineness (≤3mm)=73.6%.
[0130] The coal into the furnace was tested in a 40kg small coke oven (the charge was continuously heated for 15 hours in isolation from the air, the center temperature of the charge reached 950°C before being released from the furnace, and it was cooled to normal temperature after coke quenching): the gas production rate of the charge into the furnace was 353.4 Nm 3 / t; In dry distillation gas before adding carbonate carbon replenishing raw materials: H 2 54.5%, CH 4 25.5%, CO10.7%, CO 2 3.7%, the rest is N 2 、C m h n , O 2 Wait. CO 2 The conversion ratio is calculated as 0.55, and the hydrogen-to-carbon ratio is calculated as 3.10. According to ...
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