Combined method and combined system based on low-rank coal pyrolysis, water vapor coke quenching and water gas producing hydrogen

A water gas and water vapor technology, applied in separation methods, chemical instruments and methods, gasification processes, etc., can solve the problems of high operating costs, expensive raw materials, waste of water and heat sources, etc., and achieve full utilization of waste heat and less impurities in water gas. , Guaranteed quality effect

Active Publication Date: 2017-07-14
新疆缘捷瀚科技有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The existing hydrogen production methods mainly include: hydrogen production by electrolysis of water, oxygen production by hydrocarbons, oxygen production by natural gas, hydrogen production by methanol, hydrogen production by coal gasification, etc. These methods are due to expensive raw materials, high energy consumption, large investment in process equipment, and difficult operation process. High cost, high cost of pure hydrogen products
In addition, the hot semi-coke after low-temperature carbonization of coal is mainly quenched with water to cool down, and then dried again, which seriously wastes water and heat sources, and the quality of semi-coke products is poor due to secondary pollution.

Method used

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  • Combined method and combined system based on low-rank coal pyrolysis, water vapor coke quenching and water gas producing hydrogen

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Effect test

Embodiment 1

[0052] This embodiment provides a combined method for hydrogen production based on low-rank coal pyrolysis, steam, coke quenching, and water gas, including the following steps:

[0053] (1) Enter the semi-coke with a temperature of 600°C produced by the low-temperature carbonization furnace, and the oxygen-enriched air reacts with part of the semi-coke and then burns. The heat obtained from the combustion makes the remaining semi-coke warm up to 1000°C, and the obtained high-temperature semi-coke slowly descends;

[0054] (2) Continuously inject water vapor at 200°C upwards to make it pass upwards along the gap of the descending high-temperature semi-coke, and perform heat exchange with the high-temperature semi-coke;

[0055] (3) The water vapor heated to above 427°C through the heat exchange undergoes a gasification reaction with part of the high-temperature semi-coke, and the main component is H 2 and CO water gas;

[0056] (4) Collect water gas with a gas collecting umbre...

Embodiment 2

[0062] This embodiment provides a system for hydrogen production based on low-rank coal pyrolysis, steam quenching, and water gas; the system includes a three-stage water gas generator, and the water gas generator is preferably a cylinder with an outer steel cylinder lined with a refractory material Body structure; the water gas generator includes a warming bin, a water gas generating bin, and a semi-coke cooling bin connected sequentially from top to bottom through the semi-coke channel;

[0063] in:

[0064] The semi-coke inlet at the top of the temperature increasing chamber is connected to the semi-coke outlet of the low-temperature carbonization furnace; an air distribution burner and a high-temperature flue gas channel are arranged in the temperature increasing chamber;

[0065] The bottom of the water gas generating bin is provided with a steam injector with an upward spout; the upper part of the water gas generating bin is provided with a water gas collecting umbrella,...

Embodiment 3

[0068] This embodiment provides a system based on low-rank coal pyrolysis water vapor coke quenching water gas hydrogen production, such as figure 1 shown. In the system:

[0069]The feed port of the red-hot semi-coke warming bin 1 is connected to the coke outlet of the retort furnace, the air distributor 2 is installed in the middle of the warming bin 1, and the upper part of the warming bin 1 is equipped with a flue gas chamber 3 through the carbonization of the bridge pipe and the pyrolysis furnace The chambers are connected; the upper port of the water gas generating chamber 4 is connected with the lower port of the red-hot semi-coke temperature increasing chamber 1, the water vapor injector 5 is installed at the bottom of the water gas generating chamber 4, and the water gas collecting umbrella 6 is installed at the upper part of the water gas generating chamber 4; coke quenching by spraying The upper port of the bin 7 is connected with the lower port of the water gas ge...

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Abstract

The invention relates to a combined method and a combined system based on low-rank coal pyrolysis, water vapor coke quenching and water gas producing hydrogen. The method includes the steps of: 1) increasing temperature of semicoke generated in a low temperature dry distillation furnace and enabling the semicoke to move down slowly; 2) continuously spraying water vapor upwardly so that heat exchange is carried out between the water vapor and the high-temperature semicoke; 3) after temperature increase through the heat exchange, performing a gasification reaction to the water vapor and a part of the high-temperature semicoke to generate water gas; 4) collecting, purifying and separating the water gas to produce H2 and CO, and performing a reaction to the CO to obtain H2, and mixing and purifying all of the H2 to obtain pure H2; and 5) in a moving down process, carrying out heat exchange to the other part of the high-temperature semicoke, which is not subjected to the gasification reaction, with the water vapor to reduce the temperature, and cooling the semicoke further and outputting the semicoke. In the invention, a hydrogen production method, which has lowest cost, is found for coal tar hydrogenation, wherein the raw material, semicoke, which is low in cost and high in quality, is completely utilized, and a coke quenching system and a hydrogen production system are optimized and integrated. The combined method has simplified process route, is convenient and safe to carry out, and is beneficial to industrial development of clean and high-effective utilization of coal.

Description

technical field [0001] The invention relates to the technical field of clean and efficient utilization of coal, in particular to a combined method and system based on low-rank coal pyrolysis, steam coke quenching, and water gas hydrogen production. Background technique [0002] With the adjustment of the national energy strategy, the clean and efficient utilization of coal is listed as the eighth among the 100 major projects in my country's 13th Five-Year Plan. At present, the clean and efficient utilization of coal resources mainly includes: high-volatility and low-rank coal low-temperature pyrolysis pyrolysis upgrading, coal tar hydrogenation to fuel oil, raw gas power generation, synthetic fuels and production of high value-added chemical product raw materials. Among them, coal tar hydrogenation to produce diesel, gasoline and other fuel products requires a large amount of pure hydrogen raw materials. The existing hydrogen production methods mainly include: hydrogen prod...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10J3/46C10K1/10C10K3/04B01D53/047B01D53/22
CPCB01D53/047B01D53/22C10J3/466C10J2300/0976C10K1/10C10K3/04Y02P20/129
Inventor 袁继海袁涛
Owner 新疆缘捷瀚科技有限公司
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