Coal gasification sewage comprehensive treatment method

A coal gasification sewage and comprehensive treatment technology, applied in the direction of multi-stage water/sewage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. To ensure compliance with emission standards and other issues

Active Publication Date: 2016-04-13
CHINA PETROLEUM & CHEM CORP
View PDF11 Cites 13 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The advantage is that it can obtain a higher removal rate of ammonia nitrogen and total nitrogen. The disadvantage is that the addition of an organic carbon source increases the production cost, and the second is that a large amount of excess activated sludge is produced, which brings secondary pollution, and the disposal cost of the excess sludge Relatively high, indirectly increasing

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Coal gasification sewage comprehensive treatment method
  • Coal gasification sewage comprehensive treatment method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0090] With a gas production capacity of 100,000 m3 / h coal gasification unit as an example, assuming that there is no water loss during the washing process, the amount of desalted water in the washing tower is 100m 3 / h, the sewage discharge is 100m 3 / h. In the discharged sewage, the conductivity is 4000μS / cm, the total hardness is 1000mg / L, the COD is 500mg / L, the ammonia nitrogen is 300mg / L, and the chloride ion is 300mg / L.

[0091] The first step is flocculation and sedimentation. Add 1-2ppm polyacrylamide to the sewage, and after the pipeline mixer fully mixes and reacts with suspended matter such as fly ash in the sewage, it enters the sedimentation tank through the diversion pipe of the radial flow sedimentation tank, and the sedimentation time is 4 hours. Suspended matter settles to the bottom of the pond, and the slag is discharged every 4 hours, and sent to the ash yard.

[0092] The second step is security filtering. Sewage to remove suspended solids is filtere...

Embodiment 2

[0100] With gas production of 2 million m 3 / h coal gasification unit as an example, assuming that there is no water loss during the washing process, the amount of desalinated water in the washing tower is 2000m 3 / h, the sewage discharge is 2000m 3 / h. In the discharged sewage, the conductivity is 4500μS / cm, the total hardness is 1100mg / L, the COD is 500mg / L, the ammonia nitrogen is 300mg / L, and the chloride ion is 400mg / L.

[0101] The first step is flocculation and sedimentation. Add 1-2ppm polyacrylamide to the sewage, and after the pipeline mixer fully mixes and reacts with suspended solids such as fly ash in the sewage, it enters the sedimentation tank through the diversion pipe of the radial flow sedimentation tank, and the sedimentation time is 3 hours. Suspended matter settles to the bottom of the pool, and the slag is discharged every 4 hours, and sent to the gasification slag field.

[0102] The second step is security filtering. Sewage to remove suspended soli...

Embodiment 3

[0111] With a gas production capacity of 500,000 m 3 / h coal gasification unit as an example, assuming that there is no water loss during the washing process, the desalinated water volume of the washing tower is 500m 3 / h, the sewage discharge is 500m 3 / h. In the discharged sewage, the conductivity is 3500μS / cm, the total hardness is 900mg / L, the COD is 500mg / L, the ammonia nitrogen is 300mg / L, and the chloride ion is 250mg / L.

[0112] The first step is flocculation and sedimentation. Add 1-2ppm polyacrylamide to the sewage, and after the pipeline mixer fully mixes with the suspended matter such as fly ash in the sewage, it enters the sedimentation tank through the diversion pipe of the radial flow sedimentation tank, and the sedimentation time is 5 hours. Suspended matter settles to the bottom of the pool, and the slag is discharged every 4 hours, and sent to the gasification slag field.

[0113] The second step is security filtering. Sewage to remove suspended solids i...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
Conductivityaaaaaaaaaa
Conductivityaaaaaaaaaa
Conductivityaaaaaaaaaa
Login to view more

Abstract

The invention relates to the field of sewage treatment, and specifically relates to a coal gasification sewage comprehensive treatment method. The method comprises the following steps: flocculation sedimentation, cartridge filtration, electro-adsorption desalination, alkali-addition softening precipitation and pH regulation, precision filtration, gasification membrane ammonia removing, shortcut nitrification and denitrification, and deep carbonization and nitrification. According to the method, sewage is subjected to desalination treatment and recycling from the source, such that desalinated water is saved, production cost is reduced, treatment scale and investment of subsequent treatment equipment are reduced, and treatment effect is improved.

Description

technical field [0001] The invention belongs to the field of sewage treatment, and in particular relates to a comprehensive treatment method for coal gasification sewage. Background technique [0002] Coal gasification is the first unit process of coal chemical industry, using coal water slurry gasification technology to produce H 2 and CO. The principle is that the coal-water slurry and pure oxygen are sprayed out at high speed through the nozzle, mixed and atomized in parallel flow, and under the conditions of pressure 6.5MPa and temperature about 1400°C, flame-type non-catalytic partial oxidation reaction is carried out in the gasifier. Coal slurry temperature rise and water evaporation, coal pyrolysis volatilization, residual carbon combustion gasification and chemical reaction between gases, etc., finally generate CO, H 2 Raw gas as the main component. The ash and slag are discharged in a liquid state, and the crude gas is sent to the downstream conversion process. ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C02F9/14
Inventor 潘咸峰邹宗海李波黄斌王建娜张广
Owner CHINA PETROLEUM & CHEM CORP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products

Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic.

© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap