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Lignite drying, sloshing dust-removing and washing process

A drying and technological technology, applied in the direction of drying solid materials, non-progressive dryer, heating to dry solid materials, etc., to achieve the effect of preventing thermal decomposition, shallow buried layer and low price

Inactive Publication Date: 2011-07-13
TIANHUA INST OF CHEM MACHINERY & AUTOMATION +2
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

There is no technology and equipment successfully applied to lignite drying in our country

Method used

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  • Lignite drying, sloshing dust-removing and washing process

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Embodiment Construction

[0026] Below, the present invention is described further with reference to accompanying drawing:

[0027] The wet coal powder enters the steam pipe rotary dryer 2 through the feeding belt 1 for drying. The water vapor used for drying enters from the rotary joint at the discharge end of the dryer, and enters the heat exchange tube through the steam chamber. The wet pulverized coal is in contact with the steam pipe for heat exchange, and the moisture in it is continuously evaporated. The dried product is discharged from the discharge port and transported to the next section through the discharge belt 3. The condensed water generated by steam heat exchange enters the condensate tank 4 through the rotary joint, and then is transported to the next section by the condensate pump 5 . The tail gas produced in the drying process is firstly dedusted in the discharge box (gravity settling chamber) at the tail of the dryer, then discharged from the top of the discharge box, and then ent...

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Abstract

The invention relates to a lignite drying, sloshing dust-removing and washing process which comprises the steps: wet pulverized coal enters a drying machine through a feeding belt for drying, drying hot steam enters from a rotary joint at a discharging end of the drying machine and enters a heat exchange pipe after passing through a steam chamber, the wet pulverized coal is in contact with a steam pipe for exchanging heat and drying, and a dried product is discharged from a discharging hole and conveyed to the next section through a discharging belt; condensed water generated by steam heat exchange enters a condensed liquid tank through the rotary joint and is conveyed to the next section through a condensation liquid pump; the tail gas generated in the drying process is subjected to primary dedusting in a discharging box arranged on the tail part of the drying machine and is discharged from the top of a discharging box and then enters a sloshing dust remover; washed waste liquid is discharged from the bottom of the sloshing dust remover, and waste liquid discharged by the sloshing dust remover is conveyed by adopting a sewage pump. Materials are dried by adopting steam latent heat, dried tail gas is washed through gravity settling and sloshing dust-removing, the tail gas is ensured to reach the standard for emission, and dangers of firing and exploding during dry-method dust removing are avoided.

Description

technical field [0001] The invention relates to the technical field of lignite drying, which is a high-moisture lignite drying process using impulse dust removal and washing, and can also be used for drying other pulverized coals. [0002] Properties of lignite [0003] 1. Lignite is a high-moisture, high-volatile coal that must be dried before it can be used as fuel. [0004] 2. The moisture content of lignite is high, the particle size of raw coal after crushing is large, and the drying time required is long; the volatile content of lignite is high, and the volatile content of lignite will be lost after long-term high-temperature drying, reducing the effective components, and spontaneous combustion will occur in severe cases . [0005] 3. The moisture to be removed in the lignite drying process is water, but the drying process will produce some volatile matter and dust. Lignite is a flammable and explosive medium, so the dryer must be airtight. [0006] 4. The tail gas af...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10L9/00C10L5/00F26B3/24B01D50/00
CPCC10L9/00F26B11/04
Inventor 赵旭李盈海窦岩岳永飞詹仲福史晋文
Owner TIANHUA INST OF CHEM MACHINERY & AUTOMATION
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