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Method for preparing hydrogen by coal gasification

A coal gasification and hydrogen technology, applied in chemical instruments and methods, hydrogen production, hydrogen and other directions, can solve the problems of high methane content and low conversion rate of coal char

Inactive Publication Date: 2009-02-25
EAST CHINA UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
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Problems solved by technology

Although this method improves the purity of hydrogen, its disadvantages are: the conversion rate of coal char is low, and the methane content in the gas product is high (methane will generate carbon monoxide in the catalytic reforming conversion process)

Method used

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  • Method for preparing hydrogen by coal gasification
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  • Method for preparing hydrogen by coal gasification

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Experimental program
Comparison scheme
Effect test

Embodiment

[0040] "Two-stage" coal gasification hydrogen production method

[0041] (1) Thermal cracking of raw coal (first stage operation):

[0042]The raw coal, the mixture of raw coal and calcium hydroxide (wherein the content of calcium hydroxide is 10wt%) or the mixture of raw coal and calcium carbonate (wherein the content of calcium carbonate is 10wt%) is placed in the fixed bed pyrolysis reactor respectively, in Under the same conditions [i.e. under normal pressure (1atm) and air isolation], heating for pyrolysis, the pyrolysis temperature is 500°C to 900°C, and the distribution of the pyrolysis products is as follows: figure 2 shown.

[0043] Among them, the gas components are volatilized and separated out from the reactor, and the gas components are quantitatively analyzed by gas chromatography. The results are shown in image 3 ;

[0044] The tar product was collected in a cold trap, the amount of tar was analyzed by gravimetric method, and the benzene, toluene and xylene...

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Abstract

The invention relates to a method for preparing hydrogen by coal gasification. The method for preparing hydrogen includes the following steps: (1) thermal cracking of coal is carried out under the condition of isolating from air and at the temperature of 900 DEG C to essentially obtain coal thermal cracking gas, tarre and coal coke, and the coal thermal cracking gas and the tarre are removed to obtain the coal coke; (2) at the temperature below 800 DEG C, a gasifying agent is used for gasifying the coal coke obtained from the step (1) to obtain coal coke gas, and the obtained coal coke gas is purified to obtain a target object. In the invention, a 'two-stage type' gasifying method is adopted for gasifying coal, and the obtained coal coke gas (the coal coke gas contains about 70v / v% of hydrogen, less than 3v / v% of carbon monoxide and no methane) is used as the 'raw material gas' for preparing hydrogen. Therefore, a methane catalytic reforming technique and a carbon monoxide conversion process in a post treatment process can be omitted, and a beforehand desulfuration process required in these techniques can also be omitted, that is to say, pure hydrogen can be prepared only after the processes of removing acidic gas and purifying a little residual gas.

Description

technical field [0001] The invention relates to a method for preparing hydrogen, in particular to a method for preparing hydrogen by gasification of coal. Background technique [0002] The key process of coal hydrogen production is the coal gasification process. Existing coal gasification technologies (or devices) include: Lurgi moving bed gasifier, Winkler fluidized bed gasifier, Kopper-Totzek and Shell entrained bed with dry feed Gasifier, as well as Texaco with wet feed and entrained bed gasifier developed by Huatong East China University of Science and Technology and other units. [0003] The gas products obtained by the above-mentioned coal gasification technology (or device) contain hydrogen, carbon monoxide, carbon dioxide, methane, nitrogen and a small amount of hydrogen sulfide gas, etc., and the content of hydrogen is very low. Therefore, in order to produce hydrogen with higher purity, a conversion and separation process with lengthy steps and harsh process cond...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/06C01B3/32C10J3/00
CPCY02E60/36
Inventor 王杰曹建勤姜明泉
Owner EAST CHINA UNIV OF SCI & TECH
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