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Coupling method of coal gasification technology and steam turbine generating technology

A technology of coal gasification and steam, which is used in the gasification of granular/powdered fuels, the petroleum industry, the manufacture of combustible gases, etc.

Active Publication Date: 2012-03-14
ENN SCI & TECH DEV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In other words, the above process of combining coal gasification and steam turbine power generation only utilizes the steam generated during the coal gasification process, that is, only the steam generated during the coal gasification process makes the coal gasification process and the steam turbine power generation process take place There is still room for improvement in the degree of energy integration and process integration

Method used

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  • Coupling method of coal gasification technology and steam turbine generating technology
  • Coupling method of coal gasification technology and steam turbine generating technology
  • Coupling method of coal gasification technology and steam turbine generating technology

Examples

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Embodiment 1

[0038] refer to Figure 4 , taking the pressurized fluidized bed gasification of bituminous coal as an example. The coal is crushed and ground to make coal powder with a particle size of less than 6 mm, and then sent from the coal bunker to the gasifier through a screw feeder, an atmospheric lock hopper, and a pressurized lock hopper (these four are not shown in the figure) . At the same time, oxygen and steam are fed into the gasification furnace as gasification agents. The operating temperature of the gasification furnace is about 900-1000° C. and the operating pressure is 1.0-2.6 MPa. Coal reacts with the above-mentioned gasifying agent at high temperature to generate gas rich in carbon monoxide, hydrogen, carbon dioxide, and methane. The post-reaction mixture exiting the gasifier includes coal gas, tar and unreacted gasification agent. The reacted mixture is exchanged with 23MPa water from the booster pump in the first heat exchanger, and the pressurized water is turned...

Embodiment 2

[0040] also refer to Figure 4 , taking the pressurized entrained entrained bed gasification of bituminous coal as an example. Coal is crushed and ground to make coal powder, mixed with water to make coal-water slurry, and then pumped (not shown in the figure) to the gasifier. At the same time, oxygen or air is fed into the gasification furnace as a gasification agent. The operating temperature of the gasification furnace is about 1400° C. and the operating pressure is 5.0 MPa. Coal reacts with the above-mentioned gasifying agent at high temperature to generate gas rich in carbon monoxide, hydrogen, carbon dioxide, and methane. The post-reaction mixture exiting the gasifier includes coal gas, tar and unreacted gasification agent. The reacted mixture is exchanged with 23MPa water from the booster pump in the first heat exchanger, and the pressurized water is turned into high-temperature and high-pressure steam with a temperature of 400°C and an absolute pressure of 15MPa, and...

Embodiment 3

[0042] In this embodiment, only step a adopts dry distillation and gasification of coal under air-isolated conditions, which can be low-temperature dry distillation (below 550°C), medium-temperature dry distillation (550°C-750°C), and high-temperature dry distillation (above 900°C), resulting in Dry distillation gas, all the other steps are identical with embodiment 1.

[0043] The advantages of the present invention are as follows:

[0044] The coupling method of the coal gasification process and the steam turbine power generation process of the present invention improves the energy efficiency of the system. First, the heat source in the Rankine cycle is taken from the sensible heat recovery of the reacted mixture after the gasification reaction, and no external heat source is needed, which saves the commonly used boiler and superheater. Secondly, the water cooled by the low-temperature and low-pressure gas after expansion and decompression is used to replace the 32°C water ...

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Abstract

The invention discloses a coupling method of a coal gasification technology and a steam turbine generating technology. The method comprises steps that: a high-temperature reacted mixture fetched from a coal gasification furnace is cooled by using water; generated high-temperature high-pressure steam is used in a Rankine circulation for generating; water and slag are removed from the reacted mixture, such that coal gas is obtained; the coal gas is processed through expansion decompressing, and is used for cooling the regular normal-temperature cooling water; the cooled cooling water is delivered into a condenser in the Rankine circulation, and serves as a cooling medium used for cooling exhaust steam. Therefore, generating efficiency of the Rankine circulation is improved.

Description

field of invention [0001] The invention relates to the field of polygeneration of coal, in particular to the field of gas-electricity cogeneration using coal as raw material. Background technique [0002] At present, coal gasification technology has been widely used in my country, but it is basically limited to the field of coal chemical industry, mainly to obtain tangible chemical products. In order to improve energy efficiency, the current development trend is to combine coal gasification technology with power generation technology, that is, to carry out so-called cogeneration of gas and electricity. Coal is used as raw material to co-produce syngas, electricity and heat. The syngas can be further combusted to generate electricity, or further processed into chemical products (such as synthetic ammonia, methanol, dimethyl ether, liquid fuel, etc.). Such a gas-power cogeneration process organically combines chemical processes with power production, and has achieved huge so...

Claims

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Application Information

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IPC IPC(8): C10J3/54C10J3/46C10B53/04C10J3/84C10J3/80F01D15/10
CPCY02E20/18Y02P20/129
Inventor 谷俊杰李金来甘中学
Owner ENN SCI & TECH DEV