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Drying and moulding integrated process for low rank coal

A low-rank coal and process technology, applied in the direction of non-progressive dryers, material forming presses, drying, etc., can solve problems such as dust, and achieve the effects of avoiding dust pollution, simple process flow, and good drying effect

Inactive Publication Date: 2009-05-27
DATANG INT CHEM TECH RESINST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The present invention aims to propose a new drying treatment method for low-rank coal, which overcomes the shortcomings of the prior art, integrates the drying and molding of low-rank coal, can efficiently remove moisture in low-rank coal, and simultaneously It can effectively solve the problems of dust, spontaneous combustion, backwater (tide) and other problems of low-rank coal after drying

Method used

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  • Drying and moulding integrated process for low rank coal

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0064] 1. Send the lignite that needs to be dried to the coal hopper 1. The moisture content of the lignite is about 33.4%. The lignite from the coal hopper 1 is sent to the crusher 3 through the belt conveyor 2 for crushing. The diameter is less than 25mm. The crushed lignite first passes through the quantitative feeder 4, and then continuously and stably feeds into the drum dryer 7 through the sealed scraper conveyor 5.

[0065] 2. The hot gas from the high-temperature heating device 6 is sent to the drum dryer 7, where the hot gas dries and dehydrates the lignite. The rotating speed of the drum dryer is set at 4r / min, the feeding speed is set at 16t / h, and the hot gas flow rate is 31000Nm 3 / h, the temperature is 700°C. The dried lignite is collected by a scraper conveyor 11, and the tail gas enters the bag filter 8 after drying.

[0066] 3. The air volume of the bag filter 8 in the dust treatment system is 30000-50000Nm 3 / h, the gas temperature at the inlet is 115-125...

example 2

[0071] 1. Send the lignite that needs to be dried to the coal hopper 1. The moisture content of the lignite is about 40%. The lignite from the coal hopper 1 is sent to the crusher 3 through the belt conveyor 2 for crushing. The diameter is less than 25mm. The crushed lignite first passes through the quantitative feeder 4, and then continuously and stably feeds into the drum dryer 7 through the sealed scraper conveyor 5.

[0072] 2. The hot gas from the high-temperature heating device 6 is sent to the drum dryer 7, where the hot gas dries and dehydrates the lignite. The rotating speed of the drum dryer is set at 4r / min, the feeding speed is set at 12t / h, and the hot gas flow rate is 31000Nm 3 / h, the temperature is 700°C. The dried lignite is collected by scraper conveyor 11, and the outlet gas enters bag filter 8.

[0073] 3. The air volume of the bag filter 8 in the dust treatment system is 30000-50000Nm 3 / h, the flue gas temperature at the inlet is 125-135°C; nitrogen i...

example 3

[0078] Other conditions are the same as example 1, just feed rate is increased to 25t / h, and molding pressure is increased to 10t / cm, and the moisture content of the unformed lignite particle after drying is not higher than 18% (mass ratio), and heat is no more than 18% (mass ratio). Less than 4500kcal / kg, the water content of the shaped coal is not higher than 9% (mass ratio) after inspection, and the heat is not lower than 5500kcal / kg.

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Abstract

The invention provides an integrated process for drying forming of low-rank coal. The process comprises the following steps: (1) crushing the low-rank coal to be dried so that the particle size of the crushed low-rank coal particles is less than 50 millimeters; (2) delivering the crushed low-rank coal into a roller dryer quantitatively; (3) rotating the roller dryer and introducing heating fluid to the roller dryer to heat the coal in a roller; (4) collecting the coal discharged from the roller dryer, and delivering the heating fluid, dust carried along with the heating fluid, and water vapor from the low-rank coal into a dust processing system; (5) classifying the low-rank coal collected from the roller dryer according to certain particle size, and delivering the low-rank coal with the particle size of larger than the certain particle size to a product warehouse as a first product; and (6) delivering the low-rank coal with the particle size of smaller than the certain particle size to an extrusion forming device through a sealed delivery device to be extruded and formed together with the coal dust collected from the dust processing system, and delivering the formed product to the product warehouse as a second product.

Description

technical field [0001] The invention relates to the field of coal drying treatment, in particular to an integrated drying and forming process of low-rank coal. Background technique [0002] my country's energy resources are dominated by coal, and coal consumption accounts for about 60% of my country's primary energy consumption. For a long time, bituminous coal and anthracite have been the main mining and utilization of coal resources in my country. With the continuous increase of energy consumption in my country and the excessive exploitation of bituminous coal and anthracite resources, the development and utilization of low-rank coal is becoming more and more important. [0003] Low-rank coal refers to coal with a lower degree of coalification, such as lignite and long-flame coal. Low-rank coal reserves account for about 50% of my country's total coal resources. However, due to the high moisture content of low-rank coal (usually 20wt%-60wt%) and low calorific value (usua...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10L5/06F26B11/00B30B11/22
Inventor 佟义英李春启付志新宋学平孙占秀李玉章代东邢凌燕曹立成
Owner DATANG INT CHEM TECH RESINST
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