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Method and system for producing hydrogen of different purity grades by using semi-coke coke oven gas

A coke oven gas and hydrogen technology, applied in the field of coal chemical industry, can solve problems such as difficulty in recovering blue carbon coke oven gas, and achieve the effects of reducing emissions and easy disposal of recovered resources.

Active Publication Date: 2015-08-05
陕西氢纯能源科技有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, it is worth noting that the hydrogen concentration (>50%) in ordinary coke oven gas is significantly higher than that of the semi-coke coke oven gas (20-30%) mentioned in this patent, while the nitrogen content is much less than the latter, Therefore, it is difficult to say that the relevant technologies have direct reference significance for the recovery of semi-coke coke oven gas.

Method used

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  • Method and system for producing hydrogen of different purity grades by using semi-coke coke oven gas
  • Method and system for producing hydrogen of different purity grades by using semi-coke coke oven gas
  • Method and system for producing hydrogen of different purity grades by using semi-coke coke oven gas

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Embodiment 1

[0044] A method for producing hydrogen of different purity grades by using semi-coke coke oven gas, comprising the following steps:

[0045] 1) Pressurize the semi-coke coke oven gas and cool it to separate the heavy component impurities in the coke oven gas, such as tar, naphthalene, aromatic compounds, etc., to obtain clean gas;

[0046] 2) The clean gas is pressurized twice and mixed with superheated steam. Under the action of catalyst A at a temperature of 600°C and a pressure of 2 MPa, the methane in the clean gas reacts with superheated steam to obtain A mixed gas A comprising hydrogen and carbon monoxide, wherein the ratio of the moles of superheated steam to the moles of carbon atoms is 2.5, and the catalyst A is mainly composed of Ni and Al 2 o 3 Prepared for carrier. The chemical equation for the reaction is:

[0047]

[0048] 3) After the mixed gas A is cooled, it reacts under the action of Fe-Cr catalyst, so that the carbon monoxide in the mixed gas A reacts ...

Embodiment 2

[0054] A method for producing hydrogen of different purity grades by using semi-coke coke oven gas, comprising the following steps:

[0055] 1) Pressurize the semi-coke coke oven gas and cool it to separate the heavy component impurities in the coke oven gas, such as tar, naphthalene, aromatic compounds, etc., to obtain clean gas;

[0056] 2) The clean gas is pressurized twice and mixed with superheated steam. Under the action of catalyst A at a temperature of 900°C and a pressure of 1 MPa, the methane in the clean gas reacts with superheated steam to obtain Mixed gas A containing hydrogen and carbon monoxide, wherein the ratio of moles of superheated steam to moles of carbon atoms is 4.5, wherein the catalyst A is prepared with noble metal Au as an active component and MgO as a carrier. The chemical equation for the reaction is:

[0057]

[0058] 3) After the mixed gas A is cooled down, it reacts under the action of the Co-Mo catalyst, so that the carbon monoxide in the m...

Embodiment 3

[0064] A method for producing hydrogen of different purity grades by using semi-coke coke oven gas, comprising the following steps:

[0065] 1) Pressurize the semi-coke coke oven gas and cool it to separate the heavy component impurities in the coke oven gas, such as tar, naphthalene, aromatic compounds, etc., to obtain clean gas;

[0066] 2) After secondary pressurization, the clean gas is mixed with superheated steam. Under the action of catalyst A at a temperature of 700°C and a pressure of 1.5MPa, the methane in the clean gas reacts with superheated steam. Obtain the mixed gas A that comprises hydrogen and carbon monoxide, wherein, the ratio of superheated steam mole number and carbon atom mole number is 3, and wherein, described catalyst A is to take precious metal Pt as active component, with SiO 2 , ZrO 2 and TiO 2 Prepared for carrier. The chemical equation for the reaction is:

[0067]

[0068] 3) After the mixed gas A is cooled, it reacts under the action of P...

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Abstract

The invention discloses a method for preparing hydrogen with different purity levels by use of semi-coke coke oven gas and a system thereof, belonging to the technical field of coal chemical industry. The method comprises the following steps of: refining the associated coke oven gas of semi-coke; performing pressurization, freezing and impurity removal; mixing the associated coke oven gas with excessive water vapor, and carrying out a catalytic reforming reaction of methane to obtain hydrogen; after the product is cooled, feeding the product into a water gas shift membrane reactor for reaction as well as separation; performing membrane separation to obtain a first-level hydrogen product, and meanwhile, promoting the water gas reaction to realize deep conversion from carbon monoxide to hydrogen and reduce the concentration of the carbon monoxide to below 1%; dehydrating the product of the water gas conversion reaction, and feeding into a metal hydride temperature swing adsorption separation device to obtain the second-level hydrogen; and finally, treating the purge gas mainly containing nitrogen and carbon dioxide easily. According to the method disclosed by the invention, hydrogen is prepared by use of semi-coke coke oven gas, and hydrogen products with different purity levels are obtained by use of membrane separation and the temperature swing adsorption separation technology based on metal hydride, thereby achieving double aims of resource recovery and emission reduction.

Description

Technical field: [0001] The invention belongs to the field of coal chemical industry, and relates to a method and a system for producing hydrogen of different purity grades by utilizing semi-coke coke oven gas. Background technique: [0002] Semi-coke, also known as semi-coke, is a high-quality carbon material produced by low-temperature pyrolysis of coal, which can be used in various occasions including the metallurgical industry. In the low-temperature pyrolysis process (at a temperature of about 600 °C), coke oven gas is produced as a by-product, and its composition is relatively complex, as shown in Table 1. However, it is different from the usual coke oven gas obtained by high-temperature coking. Except for nitrogen, the contents of other components in the mixed gas are not too high, and the overall calorific value is also low (about 7113-8368kJ / Nm 3 ), therefore, in the industry, in addition to providing part of the heat required for pyrolysis as fuel, a large amount ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/38C01B3/50
Inventor 杨福胜李云王玉琪张诗伟张凡魏凌霄
Owner 陕西氢纯能源科技有限公司