Method for coke dry quenching by coal internal heat smouldering

A dry coke quenching and low temperature technology, applied in the direction of indirect heating dry distillation, coke cooling, coke oven, etc., can solve the problems of lower gas calorific value, lower energy utilization efficiency, and unoptimized operating system, so as to reduce combustion products and nitrogen The effect of content and moisture reduction

Inactive Publication Date: 2009-08-26
XI'AN UNIVERSITY OF ARCHITECTURE AND TECHNOLOGY
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  • Abstract
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  • Application Information

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Problems solved by technology

[0003] For semi-coke production enterprises in Shanxi, Shanxi, Ningmeng and Ningmeng areas of our country, there are currently five main problems. First, the internal heat adopts the method of combustion heating with air and gas in the furnace, and the combustion exhaust gas is mixed into the gas. It not only reduces the calorific value of the gas, not only increases the processing capacity of the purification system, but also is not conducive to comprehensive utilization; second, the yield of tar is low, and the tar in the gas is washed by circulating water spray condensation method and separated by natural precipitation. The separation of tar is not complete; the third is that there is no reasonable way to use gas, and the gas is mainly discharged through direct combustion; the fourth is that the equipment and operating system have not been optimized; the fifth is that environmental pollution and ecological problems are prominent, and resources are wasted.
[0007] (1) A large amount of physical heat carried by semi-coke cannot be effectively recovered and utilized, resulting in a reduction in energy utilization efficiency;
[0008] (2) Porous semi-coke absorbs a large amount of water. According to relevant statistics, the water absorption of semi-coke can reach more than 45% of the weight of semi-coke, which cannot meet the needs of users. The finished product has to be baked and dehumidified again. The large energy consumption has become an urgent problem to be solved in the production and energy saving of enterprises

Method used

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  • Method for coke dry quenching by coal internal heat smouldering
  • Method for coke dry quenching by coal internal heat smouldering

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Experimental program
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specific Embodiment approach

[0030] The specific implementation method is: after the gas produced by dry distillation is separated and collected by tar, according to the technical requirements of dry distillation, part of the cold purified gas is returned to the dry distillation furnace through a circulating fan, and part of it is used to burn with combustion-supporting air (or oxygen) to generate high temperature , into the carbonization furnace from the lower part of the carbonization section of the carbonization furnace; the other part is introduced into the coke quenching section in the lower part of the carbonization furnace through a pressurized fan. The heated gas goes up from the upper part of the quenching section, enters the lower part of the carbonization section, and mixes with the high-temperature gas generated by combustion to form gas that meets the temperature and flow rate required by low-temperature carbonization. In order to ensure the cooling of the coke quenching process and the unifor...

Embodiment 1

[0034] Embodiment 1: the application of annual processing 600,000 tons semi-coke production plant

[0035] (1) Basic information:

[0036] The semi-coke production plant with an annual processing capacity of 600,000 tons adopts a vertical square furnace as the basic production equipment, air-assisted combustion, and a coal-to-coke ratio of 1.65:1. The tar yield is about 8%, and the combustion and circulation gas volume is 349Nm 3 / t 兰炭 , the amount of combustion air into the furnace is 190m 3 / t 兰炭 , The amount of gas used for drying is 35Nm 3 / t 兰炭 , the remaining gas volume per ton of coal is 460Nm 3 / t 兰炭 About (Shenmu dry-based raw coal as the benchmark), gas calorific value 6771-7106kJ / Nm 3 . The reference gas composition is as follows:

[0037] h 2 : 16.2%, CO: 14.49%, CO 2 : 7.41%, CH 4 : 5.68%, Nitrogen: 50.10%. Calorific value: 7029kJ / m 3 .

[0038] (2) Application method

[0039] Applied as figure 2shown. The high-temperature dry distillation gas ...

Embodiment 2

[0043] Embodiment 2: the application of the semi-coke production plant with an annual output of 600,000 tons

[0044] (1) Basic information

[0045] The semi-coke production plant with an annual processing capacity of 600,000 tons uses a vertical square furnace as the basic production equipment, with oxygen-enriched air for combustion, an oxygen-enriched ratio of 80%, a coal-to-coke ratio of 1.65:1, and a tar yield of about 8%. Combustion and circulating gas volume 519m 3 / t 兰炭 , the amount of oxygen-enriched air in the furnace is 50m 3 / t 兰炭 , The amount of gas used for drying is 35Nm 3 / t 兰炭 , the remaining gas volume per ton of coal is 260Nm 3 / t 兰炭 About (Shenmu dry-based raw coal as the benchmark), the calorific value of gas is 13102kJ / Nm 3 . The reference gas composition is as follows:

[0046] h 2 : 35.05%, CO 23.04%, CO 2 : 12.06%, CH 4 : 12.55%, Nitrogen: 9.85%. Calorific value of gas 13102kJ / m 3 .

[0047] (2) Application method

[0048] The applicat...

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Abstract

The invention discloses a method coke dry quenching by coal internal heat smouldering. In the method, high temperature carbonized coal gas produced by carbonized dry quenched coke is made into cool coal gas by washing and collecting tar; after the cool coal gas passes a circulating fan, part of the coal gas is introduced into a burner to be synthesized with high temperature waste gas into high temperature mixed gas satisfying the coal smouldering requirement; the high temperature mixed gas enters into a carbonization section of a coke oven to be used as a carbonization heat source; the other part of pure coal gas passing the circulating fan is introduced to a coke quenching and cooling section of a carbonization furnace by a booster fan to be used as an inertia medium of Ramsbottom coke and quenched coke; the cool coal gas passing the coke quenching and cooling section of the carbonization furnace absorbs the heat and then passes the carbonization section of the coke oven to carry out nonoxidation heating or weak-oxidation heating towards the coal together with the carbonization heat source to realize combustion-free circulation. The method simplifies the coke dry quenching technology, reduces the water content of the Ramsbottom coke, uses the heat of the Ramsbottom coke before coke quenching effectively, improves the utilization rate of the pure coal gas, reduces the use of combustion-supporting gas and accordingly reduces the energy consumption of the burner.

Description

technical field [0001] The invention relates to the technical fields of coal chemical industry, new energy and environmental protection, and relates to a coal dry distillation method, in particular to a coal internal thermal low-temperature dry distillation dry quenching method, which is suitable for the production process of semi-coke. Background technique [0002] Parts of northern my country are rich in coal resources and of good quality, which are low-ash, low-sulfur, low-phosphorus, and high-volatile weakly sticky and non-sticky coals. Utilizing this non-coking coal low-temperature dry distillation to refine ferroalloy coke (also known as semi-coke or semi-coke) industry is currently the main coal conversion industry in the local area. [0003] For semi-coke production enterprises in Shanxi, Shanxi, Ningmeng and Ningmeng areas of our country, there are currently five main problems. First, the internal heat adopts the method of combustion heating with air and gas in the ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10B57/14C10B47/02C10B39/02
Inventor 赵俊学李小明崔雅茹袁媛刘立李惠娟
Owner XI'AN UNIVERSITY OF ARCHITECTURE AND TECHNOLOGY
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