Medium-low rank coal pyrolysis and gasification system and medium-low rank coal pyrolysis and gasification method

A pyrolysis gasification and low-rank coal technology, which is applied in the field of coal chemical industry, can solve the problems of low dust removal efficiency of the first-stage cyclone dust collector, large amount of dust in coal pyrolysis gas, and complex tar treatment process, so as to reduce the burden of dust removal , avoid equipment corrosion, avoid the effects of pipe and equipment blockage

Active Publication Date: 2015-10-28
北京恒丰亚业科技发展有限公司
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  • Summary
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  • Application Information

AI Technical Summary

Problems solved by technology

[0004] For the current pyrolysis-gasification, pyrolysis-combustion and other low-rank coal polygeneration process systems, because the dust removal efficiency of the first-stage cyclone dust collector is not high, the amount of dust in the coal pyrolysis gas is large, and the quality of tar is not high, resulting in subsequent The tar treatment process is comp

Method used

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  • Medium-low rank coal pyrolysis and gasification system and medium-low rank coal pyrolysis and gasification method
  • Medium-low rank coal pyrolysis and gasification system and medium-low rank coal pyrolysis and gasification method
  • Medium-low rank coal pyrolysis and gasification system and medium-low rank coal pyrolysis and gasification method

Examples

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Embodiment 1

[0041] See figure 1 , middle and low rank coal pyrolysis gasification system, including pyrolysis reactor 5, first cyclone separator 8, first semi-coke bin 10, gasification reactor 15, second cyclone separator 16, second descending bed 17 and the second semi-coke bin 18;

[0042] At the top of the pyrolysis reactor 5, there is an inlet for medium and low rank coal. The medium and low rank coal is used as the raw coal. device 5.

[0043]The pyrolysis reactor wall is provided with a synthesis gas inlet 6, the gas discharge pipe at the upper part of the pyrolysis reactor 5 is connected to the air inlet pipe of the first cyclone separator 8, and the ash discharge port at the bottom of the first cyclone separator 8 is connected to the described In the first semi-coke bin 10, the gas outlet at the top of the first cyclone separator 8 is connected with a first descending bed 9, and the bottom of the first descending bed 9 is also connected with the first semi-coke bin 10 and the bo...

Embodiment 2

[0058] A middle and low rank coal pyrolysis gasification system comprises a pyrolysis reactor, a first cyclone separator, a first semi-coke bin, a gasification reactor, a second cyclone separator and a second semi-coke bin. The medium and low rank coal is used as the raw coal, which is extracted from the raw coal bunker with a bucket, crushed by a crusher, and transported to the pyrolysis reactor through a feeding screw.

[0059] In the system of this embodiment, the pyrolysis reactor is a regenerative rotary furnace (moving bed), and a synthesis gas inlet is arranged on the pyrolysis reactor; a hot semi-coke discharge screw is arranged at the bottom of the pyrolysis reactor. The hot semi-coke discharge screw is connected to the semi-coke inlets on the walls of the first descending bed and the second descending bed.

[0060] Other settings of the system are the same as those in Example 1.

[0061] Using the system of this embodiment, the composition of long-flame coal is trea...

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Abstract

The present invention provides a medium-low rank coal pyrolysis and gasification system, which comprises a pyrolysis reactor, a first cyclone separator, a second cyclone separator, a first semi-coke bin, a second semi-coke bin, a gasification reactor and a first downer, wherein the pyrolysis reactor is provided with a synthetic gas inlet and is connected with the first cyclone separator, the cyclone separator is connected with the first semi-coke bin and the first downer, the bottom portion of the pyrolysis reactor is connected with a gasification semi-coke screw and a hot-state semi-coke discharge screw, the gasification semi-coke screw is connected with the gasification reactor, and the hot-state semi-coke discharge screw is connected with the first downer and a second downer. According to the present invention, the hot-state pyrolysis semi-coke is adopted as the dust removal and desulfurization adsorbent of the coarse synthetic gas, such that the dust content and the sulfur content in the coarse synthetic gas meet the downstream treatment requirements after the first-stage cyclone dust removal and the downer second-stage dust removal are performed; the partial synthetic gas refluxes to the pyrolysis reactor and the hydrogen content in the synthetic gas is high so as to provide the important effect on the lightweight of the pyrolysis tar; and the with the combined way, the low rank coal pyrolysis and gasification is achieved while the high quality tar and the high quality synthetic gas can be obtained.

Description

technical field [0001] The invention belongs to the field of coal chemical industry, and in particular relates to a method and a system for the pyrolysis and gasification of middle and low rank coal. Background technique [0002] my country's energy structure is characterized by rich coal, poor oil, and little gas. Coal resources have been the dominant energy source in my country for a long period of time. my country's proven coal reserves are 114.5 billion tons, of which medium and low rank coal (lignite, low metamorphic bituminous coal) accounts for about 55.15% of the country's reserves. Because low-rank coal has the characteristics of high moisture content, easy weathering, difficult sorting, and unsuitable for long-distance transportation and storage, its comprehensive utilization is greatly limited. Among them, direct combustion power generation is one of the most common utilization methods. According to incomplete statistics, more than 90% of lignite in my country is...

Claims

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Application Information

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IPC IPC(8): C10B53/04C10B57/18C10J3/60C10J3/84
Inventor 梅磊张宏伟陈水渺吴道洪
Owner 北京恒丰亚业科技发展有限公司
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