System and method for preparing LNG and co-producing hydrogen by deeply purifying coke oven gas

A coke oven gas and deep purification technology, which is applied in combustible gas purification, chemical instruments and methods, combustible gas purification/transformation, etc., can solve the problems of affecting the stable operation of the system, increasing operating costs, and low hydrogen yield, and achieves the goal of using The effect of prolonging life, reducing investment, and making acid with high concentration

Active Publication Date: 2021-06-15
SEDIN ENG
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  • Abstract
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  • Application Information

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Problems solved by technology

[0012] In order to solve the current comprehensive utilization of coke oven gas, it will affect the stable operation of the post-system, cause compressor blockage, cause premature desulfurization of fine desulfurization agent and increase operating costs, high sulfur content in coke oven gas returned to the coke oven, and To solve the technical problem of making the yield of hydrogen relatively low, the present invention provides a system and method for deep purification of coke oven gas to LNG and co-production of hydrogen

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  • System and method for preparing LNG and co-producing hydrogen by deeply purifying coke oven gas

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Embodiment Construction

[0039] The present invention will be further described in detail below with reference to the accompanying drawings and examples.

[0040] Such as figure 1 As shown, the embodiment of the present invention provides a system of coke oven gas depth purification, LNG joint hydrogen, including pre-washing tower 1, desulfurization tower 2, decarbonate tower 3, first absorbent tower 4, second absorbent tower 5, stripper 6, first reboiler 7, first gas liquid separator 8, second gas liquid separator 9, first cold tank 10, second cold tank 11, second reboiler 12, The three gas separator 13, the separation column 14, and the methane tube 15, wherein the preamble tower 1 is an overweight rotating device, wherein the gas cabinet is inlet with the first heat exchanger 18 and the lower portion of the pre-washed tower 1 103 is connected, the liquid phase outlet 102 of the pre-washing tower 1 is connected to the gas-liquid separation device 20, the gas outlet 107 at the top of the pre-washing towe...

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Abstract

The invention provides a system and a method for preparing LNG and co-producing hydrogen by deeply purifying coke oven gas, and belongs to the field of coke oven gas purification. A pre-washing tower is arranged as a supergravity rotating device, so that the coke oven gas subjected to benzene removal can be subjected to primary impurity removal in the pre-washing tower through a supergravity rotating technology, and harmful substances such as dust, benzene, tar, naphthalene, ammonia and sulfur in the coke oven gas subjected to benzene removal are deeply removed; and the problems that sulfur and ammonia in the coke oven gas exceed the standard to influence stable operation of a system, tar and naphthalene in the coke oven gas can cause blockage of a compression system, and the operation cost is increased due to the fact that a desulfurization adsorbent for fine desulfurization loses efficacy in advance due to abnormal coarse desulfurization are solved. Through pretreatment, the coke oven gas does not need to be desulfurized after returning to the coke oven, so that the investment and desulfurization waste liquid can be reduced. CH4, CO and H2 are separated out through coke oven gas cryogenic separation, then LNG is prepared through methanation reaction, and meanwhile, a high-purity hydrogen product is produced as a byproduct.

Description

Technical field [0001] The present invention relates to the field of coke oven gas purification technology, and more particularly to a system and method of coke oven gas depth purification, LNG co-produced hydrogen gas. Background technique [0002] Coke oven gas is an important by-product obtained in the coke process. The study of the composition of coke oven gas in recent years has been quite mature. The coke oven gas belongs to the medium heat value, the hydrogen content is 50% ~ 60%, and the methane is 22% to 24%, including huge utilization value. In the production of coke, a large number of coke oven gas is generated. If a coke oven gas calculation is produced in accordance with the production of 1 ton of coke, my country's annual coke oven gas generation is basically maintained at 180 billion cubic meters, of which 45-50% is about 45-50%. The coke oven gas returns the coke oven, and the remaining coke oven gas is considerable. Therefore, how to recycle the coke oven gas on ...

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10K1/16C10K1/00C10K1/32C10L3/10C01B3/50C07C7/04C07C7/12C07C7/00C07C9/04
CPCC01B3/50C07C7/005C07C7/04C07C7/12C10K1/002C10K1/004C10K1/005C10K1/16C10K1/32C10L3/10C07C9/04F25J3/0223F25J3/0233F25J3/0252F25J3/0266F25J2200/40F25J2200/70F25J2200/76F25J2205/04F25J2205/40F25J2205/64F25J2210/06F25J2210/14F25J2250/02F25J2270/02Y02C20/40
Inventor 王贵尚书娟左永飞范辉刁秀辉郝成浩张琦宇李刚
Owner SEDIN ENG
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