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Coal pulverizing system and method for large-proportion blending combustion of bituminous coal of steel ball coal mill

The technology of a steel ball coal mill and a pulverizing system is applied in the field of iron and steel environmental protection, and can solve the problems of insufficient drying output of the pulverizing system, increasing the proportion of mixed burning bituminous coal, and low temperature of the powder mixture.

Active Publication Date: 2021-07-23
武汉钢电股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, bituminous coal has higher moisture than lean coal and is flammable and explosive. The pulverizing system will have hidden dangers such as insufficient drying output, low temperature of the powder mixture, high exhaust gas temperature of the boiler, and safe operation. This limits the further expansion of bituminous coal blending. Proportion

Method used

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  • Coal pulverizing system and method for large-proportion blending combustion of bituminous coal of steel ball coal mill
  • Coal pulverizing system and method for large-proportion blending combustion of bituminous coal of steel ball coal mill
  • Coal pulverizing system and method for large-proportion blending combustion of bituminous coal of steel ball coal mill

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0117] 1. If figure 1 As shown, the embodiment of the present invention provides a pulverizing system for a large proportion of mixed-fired bituminous coal in steel ball mills, including:

[0118] Coal feeding device for collecting mixed coal;

[0119] The coal grinding device 2 is used to crush the mixed coal to obtain crushed materials; the coal grinding device 2 is provided with a first inlet A and a first outlet B;

[0120] Coarse powder separator 31 is used to separate the crushed materials to obtain coarse coal powder; the coarse powder separator is provided with a second inlet and a second outlet, and the second the inlet communicates with the first outlet of the coal mill;

[0121] The fine powder separator 32 is used to separate the coarse coal powder to obtain fine coal powder. The fine powder separator is provided with a third inlet, a third outlet and a exhaust gas outlet. The fine powder The third inlet of the separator communicates with the second outlet of the ...

Embodiment 2

[0135] The embodiment of the present invention provides a pulverizing system for a large proportion of bituminous coal mixed with steel ball coal mills, which is the same as that of Example 1. The proportion of bituminous coal in the mixed coal is 60%, and the cold air at the outlet of the blower is directly mixed into the coal mill. The inlet method can no longer meet the requirement that the outlet temperature of the coal mill is below 80°C. The method of closing the cold air pipe and performing hot air cooling is adopted. The method includes the following steps:

[0136] 1) Through the raw coal transportation chain 12, the mixed coal is sent from the coal feeding device 1 to the coal grinding device 2, crushed by the coal grinding device 2 for 16 minutes, and then passes through the pulverized coal pipeline from the first outlet B to the coarse powder separator 31, The fine powder separator 32 is connected to separate coal powder;

[0137] 2) 8-10 tons / hour of unqualified c...

Embodiment 3

[0143] The embodiment of the present invention provides a pulverizing system for burning bituminous coal with a large proportion of steel ball mills, which is the same as that of Example 1. The proportion of bituminous coal in the mixed coal is 70%, and the cold air pipe is closed and hot air is cooled. method, the method comprising the steps of:

[0144] 1) Through the raw coal transportation chain 12, the mixed coal is sent from the coal feeding device 1 to the coal grinding device 2, crushed by the coal grinding device 2 for 16 minutes, and then passes through the pulverized coal pipeline from the first outlet B to the coarse powder separator 31, The fine powder separator 32 is connected to separate coal powder;

[0145] 2) 8-10 tons / hour of unqualified pulverized coal is returned to the coal grinding device 2 for reprocessing, and 35-37 tons / hour of qualified coal powder is sent to the pulverized coal collection device 4 and merged with the exhausted gas from the top of th...

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Abstract

The embodiment of the invention discloses a coal pulverizing system and method for large-proportion blending combustion of bituminous coal of a steel ball coal mill. The system comprises a coal milling device, a separation device and a pulverized coal collection device which are connected in sequence, and further comprises an air supply device which is used for obtaining first cooling air; an air preheating device which is used for preheating part of the first cooling air to obtain preheated air and conveying part of the preheated air to the coal milling device to dry the mixed coal to obtain dried mixed coal; a cooling device which is used for cooling part of the preheating air to obtain second cooling air and conveying part of the second cooling air to the coal milling device to obtain cooled and crushed materials; and a powder feeding device which is used for conveying the fine-particle-size coal powder to a boiler and conveying part of the second cooling air to the powder feeding device to provide positive pressure. The system can obviously improve the pulverized coal combustion performance and improve the boiler combustion efficiency.

Description

technical field [0001] The embodiments of the present invention relate to the technical field of iron and steel environmental protection, and in particular to a pulverizing system and method for a steel ball coal mill to burn a large proportion of bituminous coal. Background technique [0002] Steam coal can be divided into four categories: anthracite, lean coal, bituminous coal and lignite according to the amount of volatile matter on a dry ash-free basis. Bituminous coal is coal with a relatively high degree of coalification. Its appearance is gray-black to black, and it contains bituminous substances similar to tar. The volatile matter is about 10-40%, the relative density is 1.25-1.35, and the calorific value is about 27-37MJ / kg. Lean coal is the coal with the highest degree of coalification. It has no cohesiveness and does not produce colloids when heated; the carbon content is as high as 90%, the calorific value is high, the ignition temperature is high, the flame is ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F23K1/00F23K3/02F26B21/00F25D1/00F01D25/32
CPCF23K1/00F23K3/02F26B21/001F26B21/004F25D1/00F01D25/32F23K2201/1003F23K2201/103F23K2201/1006F23K2201/20F23K2201/30F23K2203/201Y02E20/34
Inventor 曾晶张华马宏明张鲁峻郭凤萍吴世南贺宇张超冯浩张凯
Owner 武汉钢电股份有限公司