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Coke oven coat gas comprehensive utilization method

A coke oven gas and nitrogen technology, which is applied in the selection of absorbing solid gas purification, ammonia preparation/separation, etc., can solve the problems of coke oven gas containing more hydrogen, poisonous coke oven gas, and fast burning speed.

Inactive Publication Date: 2016-01-20
BAOJI TAIHE CHEM TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
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Problems solved by technology

[0005] 2. Coke oven gas is a colorless, odorous gas;
[0006] 3. Coke oven gas contains CO and a small amount of H 2 S is poisonous;
[0007] 4. Coke oven gas contains more hydrogen, has a fast combustion speed and a short flame;
[0008] 5. If the coke oven gas is not purified well, it will contain more tar and naphthalene, which will block the pipes and fittings and bring difficulties to the fire adjustment work;

Method used

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  • Coke oven coat gas comprehensive utilization method

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Embodiment Construction

[0023] The implementation of the present invention will be described in detail below with reference to the accompanying drawings and embodiments, so as to fully understand how the present invention applies technical means to solve technical problems and achieve the realization process of technical effects and implement them accordingly. It should be noted that, as long as there is no conflict, each embodiment of the present invention and each feature in each embodiment can be combined with each other, and the technical solutions formed are all within the protection scope of the present invention.

[0024] Specifically, as shown in the figure, a method for comprehensive utilization of coke oven gas includes:

[0025] The coke oven gas is pressurized to 0.05 MPa, and the harmful components tar, benzene, naphthalene and sulfur in the coke oven gas are removed through the temperature swing adsorption process.

[0026] The above-mentioned gas is sent to the compressor to be pressurized to...

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Abstract

The present invention discloses a coke oven coat gas comprehensive utilization method, which comprises that: coke oven coal gas is subjected to temperature swing adsorption (TSA), fine desulfurization and pressure swing adsorption (PSA) to extract hydrogen so as to form two gases such as a high hydrogen content gas and a desorbing gas with a methane content of 50%; nitrogen gas is supplemented for the high hydrogen content gas, and methanation purification and deammoniation synthesis are performed to generate a product liquid ammonia under conditions such as catalysis, high temperature and high pressure; and the desorbing gas is conveyed into a methane liquefaction system and is compressed to achieve 2.5 MPa, and then methane synthesis, decarbonization, dehydration purification, and cryogenic separation are performed so as to finally form the liquefied methane (LNG) product. With the scheme of the present invention, the coke oven coal gas can be subjected to comprehensive utilization to obtain the two products.

Description

Technical field [0001] The invention belongs to a method for comprehensive utilization of coke oven gas. Background technique [0002] Coke oven gas, also known as coke oven gas, belongs to high calorific value gas due to its many combustible components. It refers to a kind of combustible gas produced by mixing several bituminous coals into coking coal after high-temperature dry distillation in the coking oven, producing coke and tar products at the same time. It is a by-product of the coking industry and is generally used as a fuel. The added value is low. Coke oven gas is a mixture, and its yield and composition vary depending on the quality of coking coal and coking process conditions. Generally, 300~350m of coke oven gas can be produced per ton of dry coal. 3 (Standard status). Its main components are hydrogen (55%~60%) and methane (23%~27%), and also contain a small amount of carbon monoxide (5%~8%), unsaturated hydrocarbons above C2 (2%~4%), carbon dioxide (1.5%~3%), oxy...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01C1/04C10K1/32
Inventor 朱炳礼王万和高守东张军发赵亚维
Owner BAOJI TAIHE CHEM TECH CO LTD
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