CN201756539U - Two-section gas producer phenolic water treatment device - Google Patents

Two-section gas producer phenolic water treatment device Download PDF

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Publication number
CN201756539U
CN201756539U CN2010202801514U CN201020280151U CN201756539U CN 201756539 U CN201756539 U CN 201756539U CN 2010202801514 U CN2010202801514 U CN 2010202801514U CN 201020280151 U CN201020280151 U CN 201020280151U CN 201756539 U CN201756539 U CN 201756539U
Authority
CN
China
Prior art keywords
gas producer
phenolic water
water treatment
phenol
phenol water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2010202801514U
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Chinese (zh)
Inventor
崔桂欣
李伟
刘佳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ZIBO QIANGNENG ENERGY ENVIRONMENTAL PROTECTION EQUIPMENT CO Ltd
Original Assignee
ZIBO QIANGNENG ENERGY ENVIRONMENTAL PROTECTION EQUIPMENT CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ZIBO QIANGNENG ENERGY ENVIRONMENTAL PROTECTION EQUIPMENT CO Ltd filed Critical ZIBO QIANGNENG ENERGY ENVIRONMENTAL PROTECTION EQUIPMENT CO Ltd
Priority to CN2010202801514U priority Critical patent/CN201756539U/en
Application granted granted Critical
Publication of CN201756539U publication Critical patent/CN201756539U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

The utility model relates to a two-section gas producer phenolic water treatment device, which belongs to the field of gas producer phenolic water treatment equipment, and comprises a gas producer and a phenolic water tank matching with the gas producer. The two-section gas producer phenolic water treatment device is technically characterized in that a waste heat boiler, a heat exchanger and a phenolic water evaporator are sequentially arranged between the gas producer and the phenolic water tank by the aid of pipelines. As the two-section gas producer phenolic water treatment device is improved according to the shortcomings of equipment in the prior art, phenolic water is heated to run in a completely closed container without leading to any pollution to external environments, steam and air can be more sufficiently mixed, and the gasification effect of coal inside the gas producer is better than that of an original direct steam mixing mode. Accordingly, the two-section gas producer phenolic water treatment device has the advantages of simple structure, easy implementation, reliable running, complete phenolic water treatment and capability of obtaining better economic benefits and environment-protective effects.

Description

Two stage type gas generating furnace phenol water disposal device
Technical field
The utility model belongs to producer gas generator phenol water disposal apparatus field, is specifically related to a kind of two stage type gas generating furnace phenol water disposal device.
Background technology
Under the normal operating conditions of producer gas generator; inevitably produce part phenol water; if after the phenol water simple process with direct discharging of waste water; can cause severe contamination to environment; therefore each producer gas generator device fabrication producer is being devoted to solve the phenol water disposal problem for many years always; designed multiple phenol water disposal equipment; so that the phenol water that producer gas generator produces is in process of production fallen in reduction or safe handling; help environment protection; though existing in the market phenol water disposal equipment has also reached the purpose of phenol water disposal preferably; but in the production process of reality, find to still have a spot of phenol water to exist; also do not reach the purpose that phenol water is handled fully; so still need existing phenol water disposal equipment is further improved, to realize that phenol water is thorough; dispose completely, realize protection environment.
The utility model content
The purpose of this utility model is to solve above-mentioned deficiency of the prior art, and for prior art equipment provides a kind of simple in structure, easy to implement, reliable, phenol water disposal is two stage type gas generating furnace phenol water disposal device completely.
For achieving the above object, the utility model is achieved through the following technical solutions:
It is a kind of two stage type gas generating furnace phenol water disposal device, comprise producer gas generator, and with the phenol pond of producer gas generator coupling, the present technique main points are to set gradually waste heat boiler, interchanger and phenol water evaporimeter by pipeline between producer gas generator and the phenol pond.
Described phenol water evaporimeter top is saturator, and the bottom is an accumulator, and a side of saturator is provided with vapour pipe, and vapour pipe extends in the saturator, and the furnace bottom water seal of saturator top and producer gas generator links, and airduct links at the bottom of bottom and the producer gas generator.
In conjunction with the characteristics of phenol water, for improving the heat exchange effect, interchanger adopts spiral-plate exchanger.
In addition, for further realizing the processing fully of phenol water, the sewage draining exit of waste heat boiler, and the sewage draining exit of interchanger all links by the accumulator of pipeline and phenol water evaporimeter bottom, accumulator links by pipeline and phenol pond, even if still have a small amount of phenol water to exist like this, can carry out circular treatment once more, until the complete compliance with environmental protection requirements of phenol water.
The utility model is owing to be to improve at the specific aim that the deficiency that prior art equipment exists is carried out, and therefore the utlity model has simple in structurely, easy to implement, reliable, and phenol water disposal is advantage completely.
Description of drawings
Below in conjunction with accompanying drawing the utility model is described in further detail:
Fig. 1: mounting structure synoptic diagram of the present utility model.
Among the figure: 1 phenol pond; 2,3,5,6,8,9 pipelines; 4 waste heat boilers; 7 interchanger; 10 accumulators; 11 phenol water evaporimeters; 12 saturators; 13 vapour pipes.
Embodiment
As shown in Figure 1, this two stage type gas generating furnace phenol water disposal device, comprise producer gas generator, and with the phenol pond 1 of producer gas generator coupling, the present technique main points are to set gradually waste heat boiler 4, interchanger 7 and phenol water evaporimeter 11 by pipeline 3,5 between producer gas generator and the phenol pond 1.
Described phenol water evaporimeter 11 tops are saturator 12, the bottom is an accumulator 10, and a side of saturator 12 is provided with vapour pipe 13, and vapour pipe 13 extends in the saturator 12, the furnace bottom water seal of saturator 12 tops and producer gas generator links, and airduct links at the bottom of bottom and the producer gas generator.
In conjunction with the characteristics of phenol water, for improving the heat exchange effect, interchanger 7 adopts spiral-plate exchanger.
In addition, for further realizing the processing fully of phenol water, the sewage draining exit of waste heat boiler 4, and the accumulator 10 of the sewage draining exit of interchanger 7 bottom pipeline 6,9 and phenol water evaporimeter links, accumulator 10 links by pipeline 2 and phenol pond 1, even if still have a small amount of phenol water to exist like this, can carry out circular treatment once more, be evaporated fully until phenol water.
At first, the phenol water that produces in the coal gas process of cooling is all collected phenol pond 1, entering waste heat boiler 4 by phenol water pump heats, enter interchanger 7 then and carry out second-heating, nebulize at phenol water evaporimeter 11 tops spray again, return phenol pond 1 through accumulator 10 through the residue phenol water after the volatilization.In addition, the pipeline 6,9 that is provided with is respectively as the periodic blow down pipeline of waste heat boiler 4 and interchanger 7, in case gathering, impurity cause heat exchange efficiency to descend, the pipeline 8 that is provided with is as the overhaul reserve pipeline, so that can not influence the cooling effect of 4 pairs of coal gas of waste heat boiler when maintenance interchanger 7 and phenol water evaporimeter 11.
The utility model is owing to be to improve for the specific aim that the deficiency that prior art equipment exists is carried out, can solve well the situation that phenol water pollutes, in addition phenol water heating operation in fully airtight container, can not cause to the environment of outside any pollution, can mix steam and air more fully, the gasification result of coal is better than the mode of the direct mixing of original steam in the gas generator. Therefore the utlity model has simple in structurely, easy to implement, reliable, the disposal ability of supporting phenol water treatment system has reached 100%, and the phenol water treatment is complete, can obtain the preferably advantage of economic benefit and environment protecting.

Claims (4)

1. a two stage type gas generating furnace phenol water disposal device comprises producer gas generator, and with the phenol pond of producer gas generator coupling, it is characterized in that setting gradually waste heat boiler, interchanger and phenol water evaporimeter by pipeline between producer gas generator and the phenol pond.
2. two stage type gas generating furnace phenol water disposal device according to claim 1, it is characterized in that phenol water evaporimeter top is saturator, the bottom is an accumulator, one side of saturator is provided with vapour pipe, vapour pipe extends in the saturator, the furnace bottom water seal of saturator top and producer gas generator links, and airduct links at the bottom of bottom and the producer gas generator.
3. two stage type gas generating furnace phenol water disposal device according to claim 1 is characterized in that interchanger adopts spiral-plate exchanger.
4. two stage type gas generating furnace phenol water disposal device according to claim 1, the sewage draining exit that it is characterized in that waste heat boiler, and the sewage draining exit of interchanger all links by the accumulator of pipeline and phenol water evaporimeter bottom, and accumulator links by pipeline and phenol pond.
CN2010202801514U 2010-08-03 2010-08-03 Two-section gas producer phenolic water treatment device Expired - Fee Related CN201756539U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010202801514U CN201756539U (en) 2010-08-03 2010-08-03 Two-section gas producer phenolic water treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010202801514U CN201756539U (en) 2010-08-03 2010-08-03 Two-section gas producer phenolic water treatment device

Publications (1)

Publication Number Publication Date
CN201756539U true CN201756539U (en) 2011-03-09

Family

ID=43643809

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010202801514U Expired - Fee Related CN201756539U (en) 2010-08-03 2010-08-03 Two-section gas producer phenolic water treatment device

Country Status (1)

Country Link
CN (1) CN201756539U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102295958A (en) * 2011-07-21 2011-12-28 沧州恒达节能环保设备制造有限公司 Two-segment cold gas generating device
CN103965970A (en) * 2013-02-05 2014-08-06 栾涛 Treatment method for phenolic water produced by gas producer

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102295958A (en) * 2011-07-21 2011-12-28 沧州恒达节能环保设备制造有限公司 Two-segment cold gas generating device
CN102295958B (en) * 2011-07-21 2013-07-17 沧州恒达节能环保设备制造有限公司 Two-segment cold gas generating device
CN103965970A (en) * 2013-02-05 2014-08-06 栾涛 Treatment method for phenolic water produced by gas producer
CN103965970B (en) * 2013-02-05 2017-02-15 淄博英诺威圣节能科技有限公司 Treatment method for phenolic water produced by gas producer

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GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110309

Termination date: 20110803