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Medium and low coal temperature separate dry distillation system and method

A dry distillation and low temperature technology, applied in the field of coal pyrolysis dry distillation, can solve the problems of low normal pressure or slightly positive pressure of the calorific value of waste gas, difficult to improve the heating efficiency of external heat, collection of pyrolysis products, etc., and achieve high efficiency and rapid dehydration. Effect

Active Publication Date: 2016-04-20
王崇峰
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Problems solved by technology

[0005] However, as far as the current situation is concerned, the industrialization of coal dry distillation in China is still in its infancy, and most of them use vertical block coal pyrolysis furnaces. There are serious problems in the dry distillation process, such as the low calorific value of raw coal gas produced during dry distillation, low calorific value, Atmospheric pressure or slightly positive pressure is a common problem
The common problem in the current coal carbonization industry technology is that it does not fully consider and utilize the temperature-specific weight loss characteristics in the coal pyrolysis process, that is, it does not organically combine the pyrolysis characteristics of coal at different temperature stages. pyrolysis devices, but they basically work independently of each other, and the organic combination of heat, raw materials and products has not been realized. At the same time, the pyrolysis products of each stage cannot be collected separately, and tar and raw gas with high calorific value cannot be obtained. Therefore, designing a high-efficiency carbonization system that can realize the heating process of raw coal from room temperature to medium temperature is of great significance for promoting the industrialization of raw coal carbonization
At the same time, the current domestic coal carbonization has industrial advantages based on the external heating coal carbonization technology, and the main problems affecting the efficiency of the external heating coal carbonization are the coal propulsion method and heating efficiency. Most of the methods used are gravity propulsion based on vertical furnace, crawler conveying propulsion, furnace body rolling propulsion, etc. These raw coal propulsion methods have relatively large industrialization defects in actual use, and at the same time, it has been difficult to improve the heating efficiency of external heat. To a certain extent, it limits the industrial application of dry distillation of raw coal

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  • Medium and low coal temperature separate dry distillation system and method
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[0061] As the second preferred embodiment of the present invention, the medium and low temperature coal temperature fractional carbonization system, as attached image 3 with 4 shown in the above appended figure 2On the basis of the medium-low temperature external heating type screw pusher retort device 100 and the low temperature internal heating type rotary kiln retort device 200 in the first preferred embodiment shown, it further includes a medium temperature internal heat type rotary kiln retort device 300 , the medium temperature internal heat type rotary kiln retort device 300 The kiln retort device 300 is connected to the medium and low temperature external heating type screw pusher retort device 100, the composition structure and working of the medium and low temperature external heat type screw retort device 100 and the low temperature internal heat type rotary kiln retort device 200 in the second preferred embodiment process and attached figure 2 The first prefer...

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Abstract

The invention provides a medium and low coal temperature separate dry distillation system and method. The dry distillation system comprises a spiral pushing medium and low temperature external heating dry distillation device and a low temperature internal heating rotary kiln dry distillation device. A spiral pushing dry distillation chamber in the spiral pushing medium and low temperature external heating dry distillation device is arranged in a combustion chamber of the spiral pushing medium and low temperature external heating dry distillation device, burned smoke in the combustion chamber is circulated back into a rotary kiln cylinder, and solid-state materials in the rotary kiln cylinder are supplied into the spiral pushing dry distillation chamber. For the first time, dry distillation of coal is divided into two or more stages according to temperature, an internal heating rotary kiln and the external heating type spiral pushing dry distillation device are combined organically to achieve dry distillation; the rotary kiln is used for performing winnowing dust removal, preheating drying and dehydration on raw coal, and the external heating type spiral pushing dry distillation device realizes a high-efficiency medium and low temperature dry distillation process and precipitation of high calorific value raw gas and a tar product; the advantages of internal and external heating dry distillation equipment are fully combined, dry distillation efficiency, heat utilization efficiency and dry distillation product quality are greatly improved in a brand new mode, and the market popularization prospect is broad.

Description

technical field [0001] The invention belongs to the technical field of coal pyrolysis and dry distillation, and in particular relates to a medium and low temperature coal temperature fractional dry distillation system and a dry distillation method. Background technique [0002] Pulverized coal dry distillation technology, also known as coal dry distillation or coal pyrolysis, refers to the process of heating coal under air-isolated conditions to evaporate the tar and gas in the coal to obtain tar, gas, and semi-coke. This technology was first produced in the 19th century and originated in Germany. At the beginning of its invention, it was mainly used to produce coal tar, and also used to produce coke and fuel gas for ironmaking. Due to the high energy conversion rate of this technology, it has always been recognized at home and abroad. It is the third coal conversion technology alongside coal gasification and coal liquefaction, and it is also the development direction of cle...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10B53/04C10B57/02C10B57/14C10B15/00
CPCC10B15/00C10B53/04C10B57/02C10B57/14
Inventor 王崇峰
Owner 王崇峰
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