Dewatering drying method for fine slag slurry in coal gasification system and dewatering drying system used by dewatering drying method

A technology of coal gasification and fine slag, which is applied in chemical instruments and methods, separation methods, water/sewage treatment, etc., can solve the problem of drying treatment of fine slag slurry with low waste heat utilization rate, reduce the waste heat utilization rate of low-pressure flash steam, and cannot directly As a boiler fuel, etc., it can improve energy utilization efficiency, reduce equipment investment costs, and reduce costs.

Inactive Publication Date: 2017-09-15
EAST CHINA UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the low-pressure flash steam generally directly uses a large amount of circulating cooling water for condensation. On the one hand, it needs to consume a large amount of cooling water; The efficiency is usually low, which reduces the waste heat utilization rate of the low-pressure flash steam, so the low-pressure flash steam needs to be further rationally utilized to reduce the energy consumption of the gasification system and improve the energy utilization efficiency of the device
[0003] Dry fine slag can be obtained by dehydrating the fine slag slurry obtained from the concentration of slag water. The dehydration process of fine slag slurry generally adopts mechanical filtration. The mechanical filtration unit occupies a large area, and the actual operation of the industry is poor at present. There are big problems in the long-term operation of the device; after mechanical filtration, the water content of the fine residue filter cake is between 50% and 60%, and the dehydration effect is poor, resulting in poor sanitation conditions in the filter system workshop and related sites such as fine residue transportation and storage
In addition, the fine slag has high carbon content and high combustible content, which has certain use value and can be used as boiler or other raw materials. However, the high water content of the filter cake causes certain difficulties for the subsequent reuse of fine slag, and cannot be directly As a boiler fuel, fine slag with high water content also has many inconveniences in transportation and storage, so further dehydration and drying are required for the fine slag to be recycled.
[0004] In view of the above problems, it is necessary to propose a new technical solution to solve the technical problems of the above-mentioned low utilization rate of waste heat and drying treatment of fine slag slurry

Method used

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  • Dewatering drying method for fine slag slurry in coal gasification system and dewatering drying system used by dewatering drying method
  • Dewatering drying method for fine slag slurry in coal gasification system and dewatering drying system used by dewatering drying method
  • Dewatering drying method for fine slag slurry in coal gasification system and dewatering drying system used by dewatering drying method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Embodiment 1 slag water concentration and dehydration drying system

[0035] figure 1 Shown is the schematic flow chart of the slag water concentration and fine slag slurry dehydration and drying of the coal gasification system of the preferred embodiment of the present invention, wherein the low-pressure flash evaporator 1, the vacuum flash evaporator 2 and the settling tank 3 form the slag water concentration unit, and the air heating Device 4, hydrocyclone 5, spray dryer 6, condenser 7, separator 8 and vacuum pump 9 form a fine slag slurry dehydration drying unit.

[0036] In the slag water concentration unit, the slag water S1 produced by the coal gasification system (the concentrated black water of the evaporative hot water tower) is flashed through the low-pressure flash evaporator 1 to generate the low-pressure flash concentrated black water S2 and the low-pressure flash steam S3; the low-pressure flash concentrated black water The water S2 is flashed through th...

Embodiment 2

[0038] The treatment of the slag water that embodiment 2 coal-water slurry gasification plant produces

[0039] The slag water produced by a certain coal-water slurry gasification device using coal as raw material is processed through the slag water concentration and dehydration drying system of Example 1, wherein the fine slag slurry S6 obtained by the settling tank has a solid content of 20%, and the fine slag is controlled The processing capacity of the slurry S6 is 8630.0kg / h, and 4884kg / h of low-pressure flash steam S3 is extracted as the heat source of the air heater 4 . The main logistics data of the treatment process in this embodiment are shown in Table 1.

[0040] Table 1 embodiment 2 main logistics parameters

[0041]

[0042] As can be seen from Table 1, adopt processing method of the present invention, this embodiment can reach following beneficial effect:

[0043]1. In this embodiment, the low-pressure flash steam S3 is used as the heat source of the air hea...

Embodiment 3

[0046] Embodiment 3 Treatment of slag water produced by pulverized coal gasification unit

[0047] The slag water produced by a pulverized coal gasification device using coal as raw material is processed through the slag water concentration and dehydration drying system of Example 1, wherein the fine slag slurry S6 obtained by the settling tank has a solid content of 15%, and the fine slag slurry S6 is controlled The processing capacity is 8630.0kg / h, and 3307kg / h low-pressure flash steam S3 is extracted as the heat source of the air heater 4 . The main logistics data of the treatment process in this embodiment are shown in Table 2.

[0048] Table 2 embodiment 3 main logistics parameters

[0049]

[0050] As can be seen from Table 2, adopt processing method of the present invention, this embodiment can reach following beneficial effect:

[0051] 1. In this embodiment, the low-pressure flash steam S3 is used as the heat source of the air heater 4 to heat the air S10, and t...

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Abstract

The invention discloses a dewatering drying method for fine slag slurry in coal gasification system, which comprises the following steps that (a) the fine slag slurry produced by the coal gasification system is pre-dewatered by a pre-dehydration and concentration device to obtain the concentrated fine slag slurry; (b) a waste heat resource produced by the coal gasification system exchanges heat with air for heating the air into hot air; (c) the concentrated fine slag slurry and the hot air are fed into a spray dryer at the same time, so that heat and mass transfer is carried out by the direct contact between the concentrated fine slag slurry and the hot air in the spray dryer, and after most of the water is removed, the concentrated fine slag slurry flows out at the bottom and becomes dry fine slag. The invention also discloses a dewatering drying system used by the method. According to the method, the waste heat resource produced by the coal gasification system is used for heating the air, and then the heated hot air is used for drying the concentrated fine slag slurry by a spray dewatering drying technology, so that the waste heat resource can be fully utilized, the equipment cost and the influence on the site environment can be reduced, and the discharged dry fine slag can be further utilized directly.

Description

technical field [0001] The invention relates to the technical field of processing fine slag slurry in a coal gasification system, in particular to a dehydration and drying method for fine slag slurry in a coal gasification system and a dehydration drying system used therefor. Background technique [0002] In the coal gasification system, coal is transformed into fuel gas or chemical synthesis gas through entrained flow gasification, which contains a large amount of fly ash that needs to be purified and removed. At present, the relatively mature synthesis gas purification process is wet purification, which uses water to quench and wash the synthesis gas to remove fly ash and acid gas in the synthesis gas. The wet purification process will produce a large amount of slag water (black water). The slag water is usually concentrated by flash evaporation and sedimentation to obtain a fine slag slurry, and a large amount of low-pressure flash steam will be generated during the conce...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/36C02F1/06C02F1/16B01D47/06B01D53/00B01D53/26C02F103/18
CPCB01D47/06B01D53/002B01D53/265B01D53/266B01D2257/80C02F1/001C02F1/06C02F1/16C02F1/36C02F2103/18C02F2303/10
Inventor 代正华刘海峰谢安东梁钦锋郭晓镭许建良郭庆华龚欣王辅臣于广锁王亦飞陈雪莉李伟锋王兴军赵辉陆海峰龚岩刘霞王立
Owner EAST CHINA UNIV OF SCI & TECH
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