CN206504347U - Centralization catalysis burning all-in-one - Google Patents

Centralization catalysis burning all-in-one Download PDF

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Publication number
CN206504347U
CN206504347U CN201720167432.0U CN201720167432U CN206504347U CN 206504347 U CN206504347 U CN 206504347U CN 201720167432 U CN201720167432 U CN 201720167432U CN 206504347 U CN206504347 U CN 206504347U
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CN
China
Prior art keywords
chamber
heat exchanger
centralization
catalyst
catalysis burning
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
CN201720167432.0U
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Chinese (zh)
Inventor
吕昌刚
梁瑞
杨东顺
仪章立
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.)
QINGDAO LOOBO HONGYE ENVIRONMENTAL TECHNOLOGY DEVELOPMENT Co Ltd
Original Assignee
QINGDAO LOOBO HONGYE ENVIRONMENTAL TECHNOLOGY DEVELOPMENT Co Ltd
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Priority to CN201720167432.0U priority Critical patent/CN206504347U/en
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Publication of CN206504347U publication Critical patent/CN206504347U/en
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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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  • Incineration Of Waste (AREA)

Abstract

The utility model discloses a kind of centralization catalysis burning all-in-one, including on base:Filtration system includes filter chamber and filter, the outlet connecting fan of filter chamber;Control system, is arranged on the top of filter chamber;Environment protection purifying system includes heat exchanger, heating chamber and catalyst chamber, heat exchanger connecting fan, first passage is provided between the side of heat exchanger and heating chamber, second channel is provided between catalyst chamber and the opposite side of heat exchanger, pending VOC gases enter heat exchanger after being filtered through filtration system, and entering heating chamber and catalyst chamber through first passage successively, the fresh air come out from catalyst chamber enters heat exchanger through second channel, discharges.The utility model, before VOC catalysis heating, is exchanged heat with the gas of discharge, for improving VOC temperature, the required fuel before VOC catalysis heating is reduced, this equipment integrates filtration system, control system, Environmental Safety system etc., it is to avoid the cumbersome process such as Assembling.

Description

Centralization catalysis burning all-in-one
Technical field
The utility model is related to centralization catalysis burning waste gas cleaning equipment, and in particular to a kind of centralization catalysis burning one Body machine.
Background technology
The industrial site of the industry such as painting workshop, pharmaceutical factory, chemical plant, automobile maintenance workshop and light industry and machinery in part, A large amount of VOC waste gas can be produced, one of conventional VOC administering methods are Production by Catalytic Combustion Process, i.e., directly heated normal temperature VOC to catalysis temperature Degree, is then discharged out, and such a method is, it is necessary to which substantial amounts of fuel heats VOC, and the high temperature for the gas entrained with discharged is then unrestrained in vain Expense is fallen.The equipment of catalysis heating needs to assemble at the scene in addition, adds the triviality and the amount of labour of construction.
Therefore, existing VOC exhaust-gas treatments mode village head can cause the wastings of resources such as heat, field make-up equipment increase to apply The problem of work triviality and the amount of labour.
Utility model content
Technical problem to be solved in the utility model is that existing VOC exhaust-gas treatments mode village head can cause heat etc. to provide The problem of source is wasted, field make-up equipment increase is constructed triviality and amount of labour.
In order to solve the above-mentioned technical problem, the technical scheme that the utility model is used is to provide a kind of centralization catalysis combustion All-in-one is burnt, including on base:
Filtration system, including filter chamber and the filter in the filter chamber, the gas outlet of the filter chamber connect Give a dinner for a visitor from afar one end of machine;
Control system, is arranged on the top of the filter chamber;
Environment protection purifying system, including heat exchanger, heating chamber and the catalyst chamber being successively set in casing, the heat exchanger connect Connect the other end of the blower fan, between the side of the heat exchanger and the heating chamber be provided with first passage, the catalyst chamber with Second channel is provided between the opposite side of the heat exchanger;
Pending VOC gases through the filtration system filter after enter the heat exchanger, and through the first passage according to Secondary the entrance heating chamber and the catalyst chamber, the fresh air come out from the catalyst chamber are described through second channel entrance Heat exchanger, and discharge.
In such scheme, the middle part of the casing is provided with diaphragm plate, the casing is divided into upper chamber and lower chambers, institute Heat exchanger is stated positioned at the bottom chamber, the heating chamber and the catalyst chamber are successively set in the upper chamber, the horizontal stroke Between the inwall of one end of dividing plate and the casing first passage is formed provided with gap.
In such scheme, the other end of the diaphragm plate is bent to form midfeather, the midfeather and the casing The second channel is formed between inwall, the both sides of the second channel are respectively turned on the catalyst chamber and the heat exchanger.
In such scheme, the medial surface of the casing has one layer of heat-insulation layer connected using riveting method.
In such scheme, be equipped with the heat exchanger, heating chamber and the catalyst chamber for detection temperature, pressure and The detection means of wind speed, the detection means connects the control system.
In such scheme, air inlet and fresh air inlet, the air inlet are respectively equipped with the lateral surface of the filter chamber Outside connects connection new air-valve on the outside of intake valve, the fresh air inlet.
In such scheme, the rear side of the filter chamber is provided with gas bag, and the gas bag connects the intake valve and institute respectively State new air-valve and provide gas pressure for it.
In such scheme, connected between the blower fan and the filter chamber by air inlet flexible pipe, the blower fan and institute State and connected by air outlet flexible pipe between heat exchanger.
In such scheme, the catalyst chamber is built with catalyst, and the top of the catalyst chamber, which is provided with, to be bolted Access hole.
In such scheme, the venting of dust explosion mouthful of the second channel is communicated with the outside of the catalyst chamber.
In such scheme, the top of the second channel is provided with pressure alarm indicator, and the pressure alarm indicator is with control System connection.
The utility model, before VOC catalysis heating, is exchanged heat with the gas of discharge, for improving VOC temperature, reduction Required fuel before VOC catalysis heating, cost-effective safe, this equipment pacifies filtration system, control system, environmental protection Total system etc. integrates, it is to avoid the cumbersome process such as Assembling, saves labo r resources.
Brief description of the drawings
Fig. 1 is front view of the present utility model;
Fig. 2 is top view of the present utility model.
Embodiment
The utility model is described in detail with reference to Figure of description.
As shown in Figure 1 and Figure 2, the utility model provides a kind of centralization catalysis burning all-in-one, including installed in base Filtration system, control system 2 and environment protection purifying system on 1, wherein filtration system include filter chamber 3 and installed in filter chamber 3 Connection intake valve on the outside of air inlet and fresh air inlet, air inlet is respectively equipped with interior filter 31, the lateral surface of filter chamber 3 32, for the entrance of the VOC gases of control process, new air-valve 33 is connected on the outside of fresh air inlet, for controlling entering for live gas Enter.
The rear side of filter chamber 3 is provided with gas bag 34, and gas bag 34 connects intake valve 32 and new air-valve 33 and provides gas for it respectively Body pressure.Gas bag 34 agitate effect under, pending VOC gases through air inlet after intake valve 32 by entering filter chamber 3 It is interior, tentatively filtered by filter 31.
One end of the gas outlet connecting fan 4 of filter chamber 3, blower fan 4 is arranged on filter chamber rear portion, blower fan 4 and filter chamber 3 it Between connected by air inlet flexible pipe 41, blower fan 4 operate as the all-in-one provide air draught power source, by filter chamber 3 filter after Gas be inhaled into by air inlet flexible pipe 41 in blower fan 4.
Control system 2 is arranged on the top of filter chamber 3, it is preferred that control system 2 is improved using the control of PLC automatic safes Intelligence degree.
Environment protection purifying system includes being successively set on heat exchanger 6, heating chamber 7 and catalyst chamber 8 in casing 5, casing 5 it is interior Side is provided with one layer of heat-insulation layer 51 connected using riveting method, and heat-insulation layer 51 is by heat exchanger 6, heating chamber 7 and catalyst chamber 8 Sealed envelope, prevents personnel from scalding and the thermal loss in casing 5.
The middle part of casing 5 is provided with diaphragm plate 55, and 5 points by casing of diaphragm plate 55 is upper chamber and lower chambers, and heat exchanger 6 is located at Bottom chamber, heating chamber 7 and catalyst chamber 8 are successively set in upper chamber, and both are arranged side by side.The connecting fan 4 of heat exchanger 6 it is another One end, specifically, being connected between blower fan 4 and heat exchanger 6 by air outlet flexible pipe 42, the sealing of air outlet flexible pipe 42 and resistance to deformation Ability is strong, and the gas after filter chamber 3 is filtered is pumped into heat exchanger 6 by blower fan, and VOC and discharge are realized in heat exchanger 6 Gas is exchanged heat, for improving VOC temperature, the required fuel before reduction VOC catalysis heating, cost-effective security It is high.
Between one end of diaphragm plate 55 and the inwall of casing 5 first passage 56 is formed provided with gap.Exchanged heat by heat exchanger 6 Gas afterwards is entered in upper chamber by first passage 56 by lower chambers, and sequentially enters heating chamber 7 and catalyst chamber 8.Diaphragm plate 55 other end is bent to form midfeather 58, and second channel 57, second channel are formed between midfeather 58 and the inwall of casing 5 57 both sides are respectively turned on catalyst chamber 8 and heat exchanger 6.Electric heater is provided with heating chamber 7, is existed into the gas in heating chamber 7 Heat in heating chamber 7, be heated to catalytic temperature.
Gas after heat-treated enters in catalyst chamber 8, and catalytic reaction is carried out in catalyst chamber 8.Catalyst chamber 8 built with Catalyst, the species of catalyst can be customized according to different VOC, and the top of catalyst chamber 8 is provided with the inspection being bolted Mouth 53 is repaiied, it is convenient that periodic inspection is carried out to catalyst chamber 8, while being also convenient for changing different catalyst.
Enter heat exchanger 6 from the gas of catalyst chamber 8 out through second channel 57, and discharged by discharge duct 54, is vented Pipeline 54 is the small taper in the big outside in inner side, is easy to the stable discharge of gas.The outside of catalyst chamber 8 is communicated with second channel 57 Venting of dust explosion mouthfuls 52, the top of second channel 57 is provided with pressure alarm indicator, and pressure alarm indicator is connected with control system 2, when from catalysis When the gas pressure that room 8 comes out exceedes preset value, pressure alarm indicator sounds, while the control of control system 2 venting of dust explosion mouthful 52 opens drop Low-pressure.
Detection means 9, the connection control of detection means 9 are equipped with the utility model, heat exchanger 6, heating chamber 7 and catalyst chamber 8 System processed.Specifically, detection means 9 includes pressure detecting, pressure differential detection, temperature detection and wind speed measurement, moment detection casing 5 Pressure, temperature or situations such as wind speed, keep it in optimized scope, improve the intelligentized control method ability of whole equipment.
The utility model, before VOC catalysis heating, is exchanged heat with the gas of discharge, for improving VOC temperature, reduction Required fuel before VOC catalysis heating, cost-effective safe, this equipment pacifies filtration system, control system, environmental protection Total system etc. integrates, it is to avoid the cumbersome process such as Assembling, saves labo r resources.
The utility model is not limited to above-mentioned preferred forms, and anyone should learn that under enlightenment of the present utility model The structure change made, it is every that there is same or like technical scheme with the utility model, each fall within guarantor of the present utility model Within the scope of shield.

Claims (10)

1. centralization catalysis burning all-in-one, it is characterised in that including on base:
Filtration system, including filter chamber and the filter in the filter chamber, the gas outlet connection wind of the filter chamber One end of machine;
Control system, is arranged on the top of the filter chamber;
It is provided with environment protection purifying system, including heat exchanger, heating chamber and the catalyst chamber being successively set in casing, the heat exchanger Heat exchanger and the other end for connecting the blower fan, are provided with first passage, institute between the side of the heat exchanger and the heating chamber State and second channel is provided between the opposite side of catalyst chamber and the heat exchanger;
Pending VOC gases enter the heat exchanger after being filtered through the filtration system, and enter successively through the first passage Enter the heating chamber and the catalyst chamber, the fresh air come out from the catalyst chamber enters the heat exchange through the second channel Device, and discharge.
2. centralization catalysis burning all-in-one as claimed in claim 1, it is characterised in that the middle part of the casing is provided with tabula Plate, is divided into upper chamber and lower chambers by the casing, and the heat exchanger is located at the bottom chamber, the heating chamber and described urges Change room to be successively set in the upper chamber, institute is formed provided with gap between the inwall of one end of the diaphragm plate and the casing State first passage.
3. centralization catalysis burning all-in-one as claimed in claim 2, it is characterised in that the other end bending of the diaphragm plate Midfeather is formed, the second channel, the both sides of the second channel are formed between the midfeather and the inwall of the casing It is respectively turned on the catalyst chamber and the heat exchanger.
4. centralization catalysis burning all-in-one as claimed in claim 1, it is characterised in that the medial surface of the casing is provided with One layer of heat-insulation layer using riveting method connection.
5. centralization catalysis burning all-in-one as claimed in claim 1, it is characterised in that the heat exchanger, heating chamber and institute State the detection means being equipped with catalyst chamber for detection temperature, pressure and wind speed, the detection means connection control system System.
6. centralization catalysis burning all-in-one as claimed in claim 1, it is characterised in that divide on the lateral surface of the filter chamber She You not air inlet and fresh air inlet, the air inlet outside connection intake valve, the fresh air inlet outside connection new air-valve, institute The rear side for stating filter chamber is provided with gas bag, and the gas bag connects the intake valve and the new air-valve and provides gas pressure for it respectively Power.
7. centralization catalysis burning all-in-one as claimed in claim 1, it is characterised in that the blower fan and the filter chamber it Between connected by air inlet flexible pipe, connected between the blower fan and the heat exchanger by air outlet flexible pipe.
8. centralization catalysis burning all-in-one as claimed in claim 1, it is characterised in that the catalyst chamber is built with catalysis Agent, the top of the catalyst chamber is provided with the access hole being bolted.
9. centralization catalysis burning all-in-one as claimed in claim 1, it is characterised in that the outside of the catalyst chamber, which is provided with, to be connected Lead to the venting of dust explosion mouthful of the second channel.
10. centralization catalysis burning all-in-one as claimed in claim 9, it is characterised in that the top of the second channel is set There is pressure alarm indicator, the pressure alarm indicator is connected with control system.
CN201720167432.0U 2017-02-23 2017-02-23 Centralization catalysis burning all-in-one Expired - Fee Related CN206504347U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720167432.0U CN206504347U (en) 2017-02-23 2017-02-23 Centralization catalysis burning all-in-one

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720167432.0U CN206504347U (en) 2017-02-23 2017-02-23 Centralization catalysis burning all-in-one

Publications (1)

Publication Number Publication Date
CN206504347U true CN206504347U (en) 2017-09-19

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720167432.0U Expired - Fee Related CN206504347U (en) 2017-02-23 2017-02-23 Centralization catalysis burning all-in-one

Country Status (1)

Country Link
CN (1) CN206504347U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108413420A (en) * 2018-05-09 2018-08-17 东莞市中海明环保科技有限公司 Integrated organic waste gas catalytic combustion device
CN108592059A (en) * 2018-07-25 2018-09-28 上海兰宝环保科技有限公司 A kind of catalytic combustion device for organic waste gases
CN108826323A (en) * 2018-06-13 2018-11-16 江苏诺伊拓环保工程有限公司 A kind of catalysis burning waste gas processing system for medium and small air quantity
CN117663162A (en) * 2023-10-20 2024-03-08 山东泽轩环保科技有限公司 Industrial waste gas combustion treatment device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108413420A (en) * 2018-05-09 2018-08-17 东莞市中海明环保科技有限公司 Integrated organic waste gas catalytic combustion device
CN108826323A (en) * 2018-06-13 2018-11-16 江苏诺伊拓环保工程有限公司 A kind of catalysis burning waste gas processing system for medium and small air quantity
CN108592059A (en) * 2018-07-25 2018-09-28 上海兰宝环保科技有限公司 A kind of catalytic combustion device for organic waste gases
CN117663162A (en) * 2023-10-20 2024-03-08 山东泽轩环保科技有限公司 Industrial waste gas combustion treatment device
CN117663162B (en) * 2023-10-20 2024-05-03 山东泽轩环保科技有限公司 Industrial waste gas combustion treatment device

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

Granted publication date: 20170919

Termination date: 20210223

CF01 Termination of patent right due to non-payment of annual fee