CN205570046U - Concentrated purifier of waste gas multistage absorption - Google Patents

Concentrated purifier of waste gas multistage absorption Download PDF

Info

Publication number
CN205570046U
CN205570046U CN201620355955.3U CN201620355955U CN205570046U CN 205570046 U CN205570046 U CN 205570046U CN 201620355955 U CN201620355955 U CN 201620355955U CN 205570046 U CN205570046 U CN 205570046U
Authority
CN
China
Prior art keywords
district
secondary cycles
tank
circulation zone
outer circulation
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.)
Active
Application number
CN201620355955.3U
Other languages
Chinese (zh)
Inventor
岳仁亮
王建平
齐丛亮
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.)
Jiangsu Zhongke Ruisai Environmental Engineering Co., Ltd.
Original Assignee
JIANGSU ZHONGKE RUISAI POLLUTION CONTROL ENGINEERING 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 JIANGSU ZHONGKE RUISAI POLLUTION CONTROL ENGINEERING Co Ltd filed Critical JIANGSU ZHONGKE RUISAI POLLUTION CONTROL ENGINEERING Co Ltd
Priority to CN201620355955.3U priority Critical patent/CN205570046U/en
Application granted granted Critical
Publication of CN205570046U publication Critical patent/CN205570046U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a concentrated purifier of waste gas multistage absorption, it is sealed casing, top -down is equipped with outer circulation zone and interior circulation zone in the casing, be equipped with secondary circulation zone between interior circulation zone and the outer circulation zone, the bottom of casing is equipped with the extrinsic cycle jar, inner loop jar and secondary circulation jar, interior circulation zone, secondary circulation zone and outer circulation zone's top all is equipped with and sprays the pipeline, secondary circulation zone and outer circulation zone's bottom all is equipped with an album liquid board, be equipped with the import of new liquid on the extrinsic cycle jar, the extrinsic cycle jar, it connects respectively at outer circulation zone to be equipped with the transfer line on secondary circulation jar and the inner loop jar, secondary circulation zone and interior circulation zone's shower on the road, outer circulation zone's collection liquid board passes through the water inlet that return line connects secondary circulation jar, secondary circulation zone's collection liquid board passes through the water inlet that return line connects the inner loop jar, the utility model discloses according to the processing requirement of waste gas in the actual production, to handle through different device structures, the device structure is nimble, the convenient regulation, the waste gas absorption rate is high, has reduced the treatment cost of enterprise.

Description

Multi-grade exhaust gas absorbs thickening-purification technology device
Technical field
This utility model relates to recovery and the cleaning equipment field of industrial waste gas, particularly relates to a kind of Multi-grade exhaust gas and absorbs thickening-purification technology device.
Background technology
Producing large quantity of exhaust gas in chemical industry or industrial processes, these waste gas need through post processing, remove the harmful substance in removing exhaust gas, and then just can be discharged in air;The mode using corresponding liquid to absorb is one of conventional operational means of exhaust-gas treatment, typically uses to be passed through in liquid medium waste gas and processes;Or waste gas is processed by the mode using liquid spray.
In spray operating process, waste gas directly contacts with spray water mist, absorb the harmful substance in waste gas, but owing to the liquid of spray is in atmosphere by action of gravity, its liquid hurtles down to the bottom of spray column, and liquid fails to be fully contacted with the harmful substance in gas, and liquid medium utilization rate is the highest, exhaust-gas treatment cost is high, because there is these problems.
Therefore the process waste gas in the way of liquid medium circulated sprinkling is occurred in that, but the liquid medium recycled due to itself, in single spray operating process, liquid can not concentrate for gas, waste liquid after absorption operation is same concentration, when it is circulated spray, although certain concentration can be carried out, but when its concentration is excessive, itself absorption efficiency is substantially reduced, and after its absorbtivity is saturated, then can not absorb the harmful substance in waste gas, the harmful substance in waste gas can be caused to absorb insufficient, reaction affects the treatment effect of waste gas.
And for different types of waste gas, need to use different liquid mediums and spray equipment to absorb, single spray-absorption structure is difficult to meet the demand of its actual production.
Summary of the invention
For the problem of above-mentioned existence, this utility model purpose is to provide a kind of diverse in function, and waste gas absorption is effective, and liquid medium can make full use of, and the Multi-grade exhaust gas of flexible can absorb thickening-purification technology device according to the actual requirements.
nullIn order to achieve the above object,The technical solution adopted in the utility model is as follows: a kind of Multi-grade exhaust gas absorbs thickening-purification technology device,Described purifier is the housing sealed,Housing bottom is provided with waste gas inlet,Case top is provided with offgas outlet,The lower section of housing inner exhaust gas outlet is provided with except fog-zone,In housing, waste gas inlet is arranged over Perforated plate distributor,Except being provided with outer circulation district and inner circulation zone in housing between fog-zone and Perforated plate distributor from top to bottom,Secondary cycles district it is provided with between inner circulation zone and outer circulation district,The bottom of housing is provided with outer circulation tank、Interior circulating tank and secondary cycles tank,Described inner circulation zone、The top in secondary cycles district and outer circulation district is equipped with spray pipeline,The bottom in described secondary cycles district and outer circulation district is equipped with liquid collecting plate,Outer circulation tank is provided with new liquid import,Described outer circulation tank、Secondary cycles tank and interior circulating tank are provided with tube for transfusion and are connected to outer circulation district、On the spray pipeline of secondary cycles district and inner circulation zone,The bottom of outer circulation district liquid collecting plate is connected on the water inlet of secondary cycles tank by reflux pipe,The bottom of secondary cycles district liquid collecting plate is connected on the water inlet of interior circulating tank by reflux pipe.
As a kind of improvement of the present utility model, when being not provided with secondary cycles tank and secondary cycles district in described housing, the reflux pipe below outer circulation district liquid collecting plate is connected directly between on the water inlet of interior circulating tank;When this device is applied to the high liquid medium of absorption efficiency with waste gas, it is only necessary to two-stage spray-absorption structure can complete the absorption of waste gas and process work, it is not necessary to unnecessary secondary cycles district and secondary cycles tank, the production carrying out reduction device with this and use cost.
As a kind of improvement of the present utility model, when being provided with multiple secondary cycles tank and secondary cycles district in described housing, adjacent Liang Ge secondary cycles district, the reflux pipe in secondary cycles district, top is connected on the water inlet of the corresponding secondary cycles tank in secondary cycles district below;When this device is applied to the low liquid medium of absorption efficiency and waste gas, needing to add multistage spray equipment, the concentration of the liquid medium of multi-stage spray is inversely proportional to its setting height(from bottom), it is ensured that the evolution effect of final waste gas.
As a kind of improvement of the present utility model, described interior circulating tank is directly connected with inner circulation zone, and the bottom of described interior circulating tank is provided with sewage draining exit;Inner circulation zone is the first order reaction zone of gas, is the afterbody reaction zone of liquid medium simultaneously, has maximally utilized liquid medium, it is ensured that it can fully absorb, and then discharges waste liquid by sewage draining exit.
As a kind of improvement of the present utility model, the lower section of the spray pipeline in described inner circulation zone, secondary cycles district and outer circulation district is equipped with assist absorption filler;By assist absorption filler, the harmful substance in waste gas is absorbed, also increase waste gas and the contact area of liquid and time of contact simultaneously.
Device of the present utility model coordinates the absorbent of correspondence simultaneously, various waste gas can be carried out efficient absorption purification;If desired, can circulating tank, interior circulating tank and secondary cycles tank subpackage different component absorbing liquid outside, it is achieved a tower purifies complex component waste gas.
The utility model has the advantage of: this utility model, according to the process requirement of waste gas in actual production, selects different liquid mediums and different apparatus structures to process, the flexible structure of device own, convenient selection and regulation;During spray column absorbs, waste gas is processed by the mode using multiple stage circulation spray, the absorbance of waste gas is high, and by multistage absorption, and correspondence is more the thinnest toward upper strata waste gas component, the absorbing liquid used is the newest, strengthening assimilation effect, and purifying waste gas simultaneously, be conducive to reclaiming waste gas useful constituent by concentrating, liquid medium utilization rate is high, reduces the exhaust-gas treatment cost of enterprise.
Accompanying drawing explanation
Fig. 1 is apparatus structure sketch of the present utility model;
Fig. 2 is to be not provided with secondary cycles tank and the structure diagram in secondary cycles district in this utility model;
Fig. 3 is to be provided with multiple secondary cycles tank and the structure diagram in secondary cycles district in this utility model;
Wherein, 1 housing, 2 waste gas inlets, 3 offgas outlet, 4 Perforated plate distributors, 5 remove fog-zone, 6 outer circulation districts, 7 secondary cycles districts, 7 ' secondary cycles districts, 8 inner circulation zone, 9 outer circulation tanks, 10 secondary cycles tanks, 10 ' secondary cycles tanks, circulating tank in 11,12 sewage draining exits, 13 new liquid imports, 14 spray pipelines, 15 tube for transfusions, 16 liquid collecting plates, 17 reflux pipes.
Detailed description of the invention
This utility model is described in further detail by explanation and detailed description of the invention below in conjunction with the accompanying drawings.
Embodiment 1 :nullSuch as Fig. 1、A kind of Multi-grade exhaust gas shown in 2 and 3 absorbs thickening-purification technology device,Described purifier is the housing 1 sealed,The bottom of housing 1 is provided with waste gas inlet 2,The top of housing 1 is provided with offgas outlet 3,The lower section of housing 1 inner exhaust gas outlet 3 is provided with except fog-zone 5,In housing 1, waste gas inlet 2 is arranged over Perforated plate distributor 4,Except being provided with outer circulation district 6 and inner circulation zone 8 in housing 1 between fog-zone 5 and Perforated plate distributor 4 from top to bottom,Secondary cycles district 7 it is provided with between inner circulation zone 6 and outer circulation district 8、7’,The bottom of housing 1 is provided with outer circulation tank 9、Interior circulating tank 11 and secondary cycles tank 10、10’,Described inner circulation zone 8、Secondary cycles district 7、7 ' and the top in outer circulation district 6 be equipped with spray pipeline 14,Described secondary cycles district 7、7 ' and the bottom in outer circulation district 6 be equipped with liquid collecting plate 16,Outer circulation tank 9 is provided with new liquid import 13,Described outer circulation tank 9、Secondary cycles tank 10、10 ' are provided with tube for transfusion 15 with interior circulating tank 11 is connected to outer circulation district 6、Secondary cycles district 7、7 ' and inner circulation zone 8 spray pipeline 14 on,The bottom of outer circulation district 6 liquid collecting plate 16 is connected on the water inlet of secondary cycles tank 10 by reflux pipe 17,Secondary cycles district 10 or 10 ' bottom of liquid collecting plate 16 is connected on the water inlet of interior circulating tank 11 by reflux pipe 17.
Embodiment 2 :During as in figure 2 it is shown, be not provided with secondary cycles tank 10 and secondary cycles district 7 in housing 1, the reflux pipe 17 below outer circulation district 6 liquid collecting plate 16 is connected directly between on the water inlet of interior circulating tank 9;When this device is applied to the high liquid medium of absorption efficiency with waste gas, it is only necessary to two-stage spray pipeline 14 can complete the absorption of waste gas and process work, it is not necessary to unnecessary secondary cycles district 7 and secondary cycles tank 10, the production carrying out reduction device with this and use cost.
Embodiment 3 :As shown in Figure 3, when being provided with multiple secondary cycles tank 10,10 ' and secondary cycles district 7,7 ' in housing 1, adjacent Liang Ge secondary cycles district 7,7 ', the reflux pipe 17 in secondary cycles district, top 7 is connected on the water inlet of the corresponding secondary cycles tank 10 ' in secondary cycles district 7 ' below;When this device is applied to the low liquid medium of absorption efficiency and waste gas, needing to add multistage spray pipeline 14, the concentration of the liquid medium of multi-stage spray is inversely proportional to its setting height(from bottom), it is ensured that the evolution effect of final waste gas.
Embodiment 4 :As shown in Figure 1,2 and 3, interior circulating tank 11 is directly connected with inner circulation zone 8, and the bottom of described interior circulating tank 11 is provided with sewage draining exit 12;Inner circulation zone 8 is the first order reaction zone of gas, is the afterbody reaction zone of liquid medium simultaneously, has maximally utilized liquid medium, it is ensured that it can fully absorb, and then discharges waste liquid by sewage draining exit 12.
Embodiment 5 :As shown in Figure 1,2 and 3, the lower section of the spray pipeline 14 in inner circulation zone 8, secondary cycles district 7,7 ' and outer circulation district 6 is equipped with assist absorption filler;By assist absorption filler, the harmful substance in waste gas is absorbed, also increase waste gas and the contact area of liquid and time of contact simultaneously, the internal structure of device own is flexible, secondary cycles district 7 or 7 ' quantity can select to install or dismounting according to actual demand.
Embodiment 6 :As shown in Figure 1,2 and 3, the tube for transfusion 15 of this device being equipped with distribution pipeline and detection valve, its main purpose is the concentration in order to detect the liquid medium before each layer sprays, and conveniently its spray flux is carried out flexible, to be applicable to the demand of actual production.
Embodiment 7 :nullAs shown in Figure 1,Use and Fig. 1 uses inner circulation zone 8,Secondary cycles district 7,Three grades of absorbing structures in outer circulation district 6,Waste gas initially enters inner circulation zone 8,Spray pipeline 14 carries out spray operation,Remove the part harmful substance in removing exhaust gas,Liquid after spray enters interior circulating tank 11,Waste gas persistently rises in tower body,Enter secondary cycles district 7,Spray through spray pipeline 14,Gas after spray persistently rises,Liquid after spray is after liquid collecting plate 16 is collected,Interior circulating tank 11 is flowed back into by reflux pipe 17,Waste gas race way 6 outside is after spray operation,Waste gas discharges this device by offgas outlet,Liquid is after liquid collecting plate 16 is collected,Secondary cycles tank 10 is entered by reflux pipe 17,Wherein the water inlet of liquid is arranged on outer circulation tank 9,Use this device to containing 75% ethanol、The exhaust-gas treatment of 25% positive third fat,The spray liquid selected is water,Absorb ethanol component in concentration and recovery waste gas;Ethanol ult rec reaches 95%, and in the interior circulating tank 11 of multiple stage circulation final bottom concentrated solution, the concentration of alcohol of liquid reaches 30%~35%.
Being only preferred embodiment of the present utility model it should be noted that above-mentioned, be not used for limiting protection domain of the present utility model, the combination in any made on the basis of above-described embodiment or equivalents belong to protection domain of the present utility model.

Claims (5)

  1. null1. a Multi-grade exhaust gas absorbs thickening-purification technology device,Described purifier is the housing sealed,Housing bottom is provided with waste gas inlet,Case top is provided with offgas outlet,The lower section of housing inner exhaust gas outlet is provided with except fog-zone,In housing, waste gas inlet is arranged over Perforated plate distributor,It is characterized in that,Except being provided with outer circulation district and inner circulation zone in housing between fog-zone and Perforated plate distributor from top to bottom,Secondary cycles district it is provided with between inner circulation zone and outer circulation district,The bottom of housing is provided with outer circulation tank、Interior circulating tank and secondary cycles tank,Described inner circulation zone、The top in secondary cycles district and outer circulation district is equipped with spray pipeline,The bottom in described secondary cycles district and outer circulation district is equipped with liquid collecting plate,Outer circulation tank is provided with new liquid import,Described outer circulation tank、Secondary cycles tank and interior circulating tank are provided with tube for transfusion and are connected to outer circulation district、On the spray pipeline of secondary cycles district and inner circulation zone,The bottom of outer circulation district liquid collecting plate is connected on the water inlet of secondary cycles tank by reflux pipe,The bottom of secondary cycles district liquid collecting plate is connected on the water inlet of interior circulating tank by reflux pipe.
  2. Multi-grade exhaust gas the most according to claim 1 absorbs thickening-purification technology device, it is characterised in that when being not provided with secondary cycles tank and secondary cycles district in described housing, the reflux pipe below outer circulation district liquid collecting plate is connected directly between on the water inlet of interior circulating tank.
  3. Multi-grade exhaust gas the most according to claim 1 absorbs thickening-purification technology device, it is characterized in that, when being provided with multiple secondary cycles tank and secondary cycles district in described housing, adjacent Liang Ge secondary cycles district, the reflux pipe in secondary cycles district, top is connected on the water inlet of the corresponding secondary cycles tank in secondary cycles district below.
  4. Multi-grade exhaust gas the most according to claim 1 absorbs thickening-purification technology device, it is characterised in that described interior circulating tank is directly connected with inner circulation zone, and the bottom of described interior circulating tank is provided with sewage draining exit.
  5. Multi-grade exhaust gas the most according to claim 1 absorbs thickening-purification technology device, it is characterised in that the lower section of the spray pipeline in described inner circulation zone, secondary cycles district and outer circulation district is equipped with assist absorption filler.
CN201620355955.3U 2016-04-26 2016-04-26 Concentrated purifier of waste gas multistage absorption Active CN205570046U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620355955.3U CN205570046U (en) 2016-04-26 2016-04-26 Concentrated purifier of waste gas multistage absorption

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620355955.3U CN205570046U (en) 2016-04-26 2016-04-26 Concentrated purifier of waste gas multistage absorption

Publications (1)

Publication Number Publication Date
CN205570046U true CN205570046U (en) 2016-09-14

Family

ID=56861247

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620355955.3U Active CN205570046U (en) 2016-04-26 2016-04-26 Concentrated purifier of waste gas multistage absorption

Country Status (1)

Country Link
CN (1) CN205570046U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106377968A (en) * 2016-12-01 2017-02-08 合力泰科技股份有限公司 Dust removing and recycling system for granulation column

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106377968A (en) * 2016-12-01 2017-02-08 合力泰科技股份有限公司 Dust removing and recycling system for granulation column

Similar Documents

Publication Publication Date Title
CN107285525A (en) A kind of down-stream processing equipment
CN105771553A (en) Low-concentration formaldehyde waste gas collecting and processing technique and special equipment
CN204093277U (en) Trimethylamine waste gas pollution control and treatment system
CN204365080U (en) Waste gas utilization purifier
CN205570046U (en) Concentrated purifier of waste gas multistage absorption
CN105344224B (en) A kind of styrene waste gases processing method
CN203829859U (en) Waste gas dust purifying and recovering tower
CN102078747A (en) Organic waste gas treating and recycling device and method
CN107854930A (en) A kind of waste gas processing method and processing system
CN201809203U (en) Resin adsorption waste-water processing and steam desorption regeneration device
CN205235705U (en) Styrene exhaust treatment device
CN104587799B (en) Device and method for processing complex organic waste gas components and recycling resources
CN210814530U (en) Printing exhaust treatment device
CN208694662U (en) A kind of photooxidation catalytic waste gas processing unit
CN203155041U (en) Dichloromethane exhaust gas treatment system
CN203610015U (en) Toluene waste gas recovery device for mica tape products
CN203620499U (en) Waste gas treatment system
CN206881453U (en) One kind mixing organic waste-gas purification and energy processing system
CN206276190U (en) A kind of simple recyclable continuous absorbent charcoal adsorber for using
CN204952568U (en) Waste gas purification apparatus
WO2014117571A1 (en) System for recovering sulfur dioxide from tail gas by using water washing
CN201492964U (en) Cooling dissolving and absorbing device of organic waste gases purification and recovery system
CN204134441U (en) The steam-condensation filter of waste oil purifying device
CN205760446U (en) Purification of chemical waste gas system
CN106524780A (en) Fuel gas waste heat recovery device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20180404

Address after: A group of villagers' committee of the people's Federation of Yancheng City Pavilion in 224001 Jiangsu Province

Patentee after: Yancheng Zhongke Rui Environmental Engineering Co., Ltd.

Address before: 224001 No. 666 environmental protection Avenue, Yancheng City environmental protection science and Technology City, Jiangsu Province

Patentee before: JIANGSU ZHONGKE RUISAI POLLUTION CONTROL ENGINEERING CO., LTD.

TR01 Transfer of patent right
CP01 Change in the name or title of a patent holder

Address after: 224001 Group of Minlian Villagers'Committee in Tinghu New Area, Yancheng City, Jiangsu Province

Patentee after: Jiangsu Zhongke Ruisai Environmental Engineering Co., Ltd.

Address before: 224001 Group of Minlian Villagers'Committee in Tinghu New Area, Yancheng City, Jiangsu Province

Patentee before: Yancheng Zhongke Rui Environmental Engineering Co., Ltd.

CP01 Change in the name or title of a patent holder