Method for preparing hydrogen and LNG from coke oven gas

A technology of coke oven gas and hydrogen, applied in the direction of chemical instruments and methods, hydrogen, gas fuel, etc., can solve the problems of wasting precious resources, environmental pollution, etc., achieve huge economic and social benefits, reduce investment and operating costs, filter The effect of simple process

Inactive Publication Date: 2018-06-19
SICHUAN HENGRI GAS ENG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
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Problems solved by technology

[0004] At present, part of coke oven gas is used to generate electricity, part is used to produce methanol and hydrogen, and a considerable part is directly burned and discharged. The energy

Method used

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  • Method for preparing hydrogen and LNG from coke oven gas

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Embodiment

[0035] Example: as attached figure 1 Shown, a kind of coke oven gas produces the method for hydrogen and LNG, comprises the following steps:

[0036] (1) Electric decoking 8, using a tubular electric detarring device, the voltage used is selected from 40 to 60KV, and most of the tar, benzene, naphthalene and other liquid droplets and water particles in the raw material gas are removed in the high-voltage corona electric field;

[0037] (2) The compression system pressurizes the coke oven gas;

[0038] (3) Utilize BOG gas of LNG (the BOG gas refers to the gas after LNG is passively heated and gasified) to cool the raw coke oven gas, and further remove tar, benzene, naphthalene and other substances in the coke oven gas;

[0039] (4) Through the pretreatment of the TSA process, remove macromolecular impurities, such as tar, benzene, naphthalene, etc.;

[0040] (5) Two-stage desulfurization by wet method plus dry method to remove sulfide in coke oven gas;

[0041] (6) After two...

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Abstract

The invention provides a method for preparing hydrogen and LNG from coke oven gas. The method comprises the following steps: electric decoking; boosting of the coke oven gas by a compression system; cooling of the raw gas coke oven gas by using the BOG gas (the BOG gas is a gas formed after the passive heating gasification of LNG) of LNG in order to further remove tar, benzene, naphthalene and like substances in the coke oven gas; and pretreatment using a TSA process to finely remove macromolecular impurities, such as tar, benzene, naphthalene and the like; wet and dry two-stage desulfurization for removing sulfides in the coke oven gas; two-stage low pressure shifting for a reaction of CO and water vapor to form CO2 and hydrogen; and pressurization using a compressor, an MDEA solution process for removing carbon dioxide, a membrane separation technology for separating hydrogen and methane, separation, concentration and purification of the hydrogen and methane, and dehydration, demercuration and liquefaction of the separated high-concentration methane to obtain the LNG. The coke oven gas is finally converted into the hydrogen and the LNG which have high values, so the energy of thecoke oven gas is fully used, and the environment is protected.

Description

technical field [0001] The invention relates to the technical field of coke oven gas treatment, in particular to a method for producing hydrogen and LNG from coke oven gas. Background technique [0002] Coke oven gas, also known as coke oven gas, has many combustible components and belongs to high calorific value gas, crude gas or raw gas. It is a combustible gas produced when coke and tar products are produced after high-temperature dry distillation of coking coal in the coking oven, and is a by-product of the coking industry. Its main components are hydrogen (55%-60%) and methane (23%-27%), and also contain a small amount of carbon monoxide (5%-8%), C 2 The above unsaturated hydrocarbons [0003] (2% ~ 4%), carbon dioxide (1.5% ~ 3%), oxygen (0.3% ~ 0.8%)), nitrogen (3% ~ 7%) and sulfides. Among them, hydrogen, methane, carbon monoxide, C 2 The above unsaturated hydrocarbons are combustible components, and carbon dioxide, nitrogen, and oxygen are non-flammable componen...

Claims

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Application Information

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IPC IPC(8): C10L3/12C01B3/12
CPCC01B3/12C01B2203/0288C01B2203/0405C01B2203/0415C01B2203/0475C10L3/12C10L2290/06C10L2290/542C10L2290/545C10L2290/548
Inventor 唐脯林
Owner SICHUAN HENGRI GAS ENG CO LTD
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