CN206381794U - A kind of purification of gaseous benzene device - Google Patents

A kind of purification of gaseous benzene device Download PDF

Info

Publication number
CN206381794U
CN206381794U CN201621337573.4U CN201621337573U CN206381794U CN 206381794 U CN206381794 U CN 206381794U CN 201621337573 U CN201621337573 U CN 201621337573U CN 206381794 U CN206381794 U CN 206381794U
Authority
CN
China
Prior art keywords
purification
surfactant
pipeline
packed tower
air pump
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
CN201621337573.4U
Other languages
Chinese (zh)
Inventor
云凤刚
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.)
Tianjin jaten environmental protection equipment Limited by Share Ltd
Original Assignee
TIANJIN JIATENG 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 TIANJIN JIATENG ENVIRONMENTAL PROTECTION EQUIPMENT CO Ltd filed Critical TIANJIN JIATENG ENVIRONMENTAL PROTECTION EQUIPMENT CO Ltd
Priority to CN201621337573.4U priority Critical patent/CN206381794U/en
Application granted granted Critical
Publication of CN206381794U publication Critical patent/CN206381794U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Gas Separation By Absorption (AREA)

Abstract

The utility model discloses a kind of purification of gaseous benzene device, waste gas containing benzene in workshop is discharged into the bottom of packed tower using the first air pump in workshop, it is connected with packed tower upper end, the second air pump for discharging gas after purification, it is arranged at the surfactant mixed liquor shower above packing layer, the shower is connected with surfactant mixed liquor organization of supply, two sections of packing layers are provided with the packed tower, described filler layer is the stainless steel ripple net of ring-type, stainless steel ripple net has specific surface area big simultaneously, porosity is high, the advantages of total amount is light, in addition, silk screen also has strong capillarity, Qi Run seas performance can be improved, wet porosity is no better than thousand porositys, stainless steel cloth filler also has enough corrosion resistant performances.

Description

A kind of purification of gaseous benzene device
Technical field
The utility model is related to benzene exhaust air processing technology field, more particularly to a kind of purification of gaseous benzene device.
Background technology
In the case of production PX factories nominal situation, during production and transportation, the intermediate product or product of aromatic hydrocarbons Usual highly volatile, may leakage, generation poisonous fume.Generally, the gas containing benzene, toluene and dimethylbenzene is volatilized, referred to as 3 benzene waste gas.
Benzene is a kind of coal tar distillation or the product of petroleum cracking, colourless, transparent, the liquid with aromatic odor.Toluene It is the methyl-derivatives of benzene with dimethylbenzene, they are to the great toxicity of various life forms.When the 3 benzene waste gas in factory permeates into week Residential block is enclosed, when sucking high concentration " triphen " steam, the redox function of human inner cell is influenceed, using making cytoactive Reduction, ATP synthesis is reduced, and is suppressed the secretion of acetylcholine and is caused anesthesia, so these waste gas must be handled, with reduction pair The harm of near its circumference resident.
In consideration of it, this application provides a kind of purification of gaseous benzene device, to meet the demand that people are handled benzene exhaust air.
Utility model content
The purpose of this utility model is to provide a kind of purification of gaseous benzene device, to meet the need that people are handled benzene exhaust air Ask.
To realize the purpose of this utility model, the utility model provides a kind of purification of gaseous benzene device, including for receiving Collect the first air pump of waste gas, the packed tower that bottom is connected with the first air pump, be connected with packed tower upper end, for discharging only Second air pump of gas, the surfactant mixed liquor shower being arranged above packing layer, the shower and surface after change Activating agent mixed liquor organization of supply is connected, and is provided with two sections of packing layers in the packed tower, described filler layer be ring-type not Become rusty steel ripple net.
Wherein, the packed tower upper end is provided with demister with the exit that the second air pump is connected.
Wherein, the spray column lower end is connected with liquid withdrawal system, the liquid withdrawal system include by pipeline according to Regulating reservoir, biofilter, the sedimentation basin of secondary connection, sedimentation basin are connected by pipeline with water pump, the sedimentation basin and water pump it Between pipeline on be provided with the first magnetic valve.
Wherein, the surfactant mixed liquor organization of supply includes water pump, and the water pump is by being provided with the 4th electromagnetism The pipeline of valve is connected with intermixture case, and the intermixture case is connected with filtered water tank and surfactant case respectively by pipeline Lead to, and the 3rd magnetic valve, second flowmeter are provided with the pipeline between filtered water tank, with the pipeline between surfactant case On be provided with first flowmeter, the second magnetic valve.
Wherein, the surfactant is anion surfactant, and the anion surfactant is straight chain 12 Sodium alkyl benzene sulfonate or branched dodecylbenzene sulfonic acid sodium.
Compared with prior art, the beneficial effects of the utility model are, using the first air pump in workshop by car In waste gas containing benzene be discharged into the bottom of packed tower, be connected with packed tower upper end, for discharge purify after gas the second gas Pump, the surfactant mixed liquor shower being arranged above packing layer, the shower are supplied with surfactant mixed liquor Mechanism is connected, and two sections of packing layers are provided with the packed tower, and described filler layer is the stainless steel ripple net of ring-type, stainless steel Ripple net has the advantages that specific surface area is big, porosity is high, total amount is light simultaneously, in addition, silk screen also has strong capillarity, Qi Run seas performance can be improved, wet porosity is no better than thousand porositys, and stainless steel cloth filler also has enough corrosion resistant performances.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment;
In figure, the air pumps of 1- first, 2- packed towers, 3- regulating reservoirs, 4- biofilters, 5- sedimentation basins, the magnetic valves of 6- first, 7- Intermixture case, 8- first flowmeters, 9- surfactant casees, the magnetic valves of 10- second, the magnetic valves of 11- the 3rd, 12- filtered water tanks, 13- second flowmeters, the magnetic valves of 14- the 4th, 15- water pumps, 16- air-introduced machines, 17- demisters, 18- packing layers.
Embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.It should be appreciated that this place The specific embodiment of description only to explain the utility model, is not used to limit the utility model.
It should be noted that " connection " described herein and the word for expressing " connection ", such as " being connected ", " connected " etc., was both directly connected to including a certain part with another part, also passed through miscellaneous part and another portion including a certain part Part is connected.
It should be noted that term used herein above is merely to describe embodiment, and be not intended to restricted root According to the illustrative embodiments of the application.As used herein, unless the context clearly indicates otherwise, otherwise singulative Be also intended to include plural form, additionally, it should be understood that, when in this manual using belong to "comprising" and/or " bag Include " when, it indicates existing characteristics, step, operation, part or module, component and/or combinations thereof.
It should be noted that term " first " in the description and claims of this application and above-mentioned accompanying drawing, " Two " etc. be for distinguishing similar object, without for describing specific order or precedence.It should be appreciated that so using Data can exchange in the appropriate case, so that presently filed embodiment described herein for example can be with except herein Order beyond those of diagram or description is implemented.In addition, term " comprising " and " having " and their any deformation, it is intended that Be to cover it is non-exclusive include, for example, containing process, method, system, product or the equipment of series of steps or unit not Be necessarily limited to those steps or the unit clearly listed, but may include not list clearly or for these processes, side The intrinsic other steps of method, product or equipment or unit.
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the application can phase Mutually combination.
In figure, the air pumps of 1- first, 2- packed towers, 3- regulating reservoirs, 4- biofilters, 5- sedimentation basins, the magnetic valves of 6- first, 7- Intermixture case, 8- first flowmeters, 9- surfactant casees, the magnetic valves of 10- second, the magnetic valves of 11- the 3rd, 12- filtered water tanks, 13- second flowmeters, the magnetic valves of 14- the 4th, 15- water pumps, the air pumps of 16- second, 17- demisters, 18- packing layers.
As shown in figure 1, the utility model embodiment provides a kind of purification of gaseous benzene device, including for collecting waste gas Packed tower 2 that first air pump 1, bottom are connected with the first air pump 1, be connected with the upper end of packed tower 2, for discharging after purification Second air pump 16 of gas, the surfactant mixed liquor shower for being arranged at the top of packing layer 18, the shower and surface Activating agent mixed liquor organization of supply is connected, and two sections of packing layers 18 are provided with the packed tower 2, and described filler layer 18 is ring-type Stainless steel ripple net.
Wherein, the upper end of packed tower 2 is provided with demister 17 with the exit that the second air pump 16 is connected.
Wherein, the lower end of spray column 2 is connected with liquid withdrawal system, the liquid withdrawal system include by pipeline according to Regulating reservoir 3, biofilter 4, the sedimentation basin 5 of secondary connection, sedimentation basin 5 are connected by pipeline with water pump 15, the sedimentation basin 5 with The first magnetic valve 6 is provided with pipeline between water pump 15.By controlling the first magnetic valve 6, the liquid that water pump can be controlled to circulate Body.
Wherein, the surfactant mixed liquor organization of supply includes water pump 15, and the water pump 15 is by being provided with the 4th The pipeline of magnetic valve 14 is connected with intermixture case 7, the intermixture case 7 by pipeline respectively with filtered water tank 12 and surface-active Agent case 9 is connected, and the 3rd magnetic valve 11, second flowmeter 13 are provided with the pipeline between filtered water tank 12, is lived with surface First flowmeter 8, the second magnetic valve 10 are provided with pipeline between property agent case 9.Upper and lower liquid is internally provided with intermixture case Level sensor, the 3rd magnetic valve 11, second flowmeter 13, first flowmeter 8, the second magnetic valve 10, upper and lower liquid level sensor is equal It is connected with PLC, therefore, being automatically replenished for intermixture can be realized by PLC, when less than default liquid level When, control adds a certain amount of surfactant and a certain amount of clear water, when higher than liquid level, stops adding.
Wherein, the surfactant is anion surfactant, and the anion surfactant is straight chain 12 Sodium alkyl benzene sulfonate or branched dodecylbenzene sulfonic acid sodium.
Above-mentioned first air pump and the second air pump can be air-introduced machine.
Use process:By the mixed gas of the first air pump from the air inlet of packed tower bottom, the water containing surfactant is inhaled Receive agent in tower top to enter, still have part foam so setting demister before outlet, to remove in packing layer practical operation Foam.The filler of packed tower is divided to two sections, is inversely absorbed, and purified gas can reach emptying standard, be directly discharged into internal heat. The absorbing liquid rich in triphen is passed sequentially through after regulating reservoir, bio-oxidation pond and sedimentation basin processing after absorption, through circulating pump to tower top Reuse, to reduce the consumption of surfactant and clear water, and realizes wastewater zero discharge.
Described above is only preferred embodiment of the present utility model, it is noted that for the general of the art For logical technical staff, on the premise of the utility model principle is not departed from, some improvements and modifications can also be made, these change Enter and retouch and also should be regarded as protection domain of the present utility model.

Claims (5)

1. a kind of purification of gaseous benzene device, it is characterised in that including the first air pump for collecting waste gas, bottom and the first air pump The packed tower that is connected, be connected with packed tower upper end, for discharging the second air pump of gas after purification, being arranged at packing layer The surfactant mixed liquor shower of top, the shower is connected with surfactant mixed liquor organization of supply, described Two sections of packing layers are provided with packed tower, described filler layer is the stainless steel ripple net of ring-type.
2. purification of gaseous benzene device according to claim 1, it is characterised in that the packed tower upper end connects with the second air pump The exit connect is provided with demister.
3. purification of gaseous benzene device according to claim 1, it is characterised in that the spray column lower end is connected with liquid and returned Receiving apparatus, the liquid withdrawal system includes regulating reservoir, biofilter, the sedimentation basin being sequentially connected by pipeline, and sedimentation basin leads to Cross pipeline with water pump to be connected, the first magnetic valve is provided with the pipeline between the sedimentation basin and water pump.
4. purification of gaseous benzene device according to claim 1, it is characterised in that the surfactant mixed liquor supplies machine Structure includes water pump, and the water pump is connected by being provided with the pipeline of the 4th magnetic valve with intermixture case, and the intermixture case leads to Cross pipeline respectively with filtered water tank and surfactant case to be connected, and the 3rd electromagnetism is provided with the pipeline between filtered water tank First flowmeter, the second magnetic valve are provided with pipeline between valve, second flowmeter, with surfactant case.
5. purification of gaseous benzene device according to claim 1, it is characterised in that the surfactant is anionic surface Activating agent, the anion surfactant is linear alkyl benzene sulphonate or branched dodecylbenzene sulfonic acid sodium.
CN201621337573.4U 2016-12-08 2016-12-08 A kind of purification of gaseous benzene device Expired - Fee Related CN206381794U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621337573.4U CN206381794U (en) 2016-12-08 2016-12-08 A kind of purification of gaseous benzene device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621337573.4U CN206381794U (en) 2016-12-08 2016-12-08 A kind of purification of gaseous benzene device

Publications (1)

Publication Number Publication Date
CN206381794U true CN206381794U (en) 2017-08-08

Family

ID=59487782

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621337573.4U Expired - Fee Related CN206381794U (en) 2016-12-08 2016-12-08 A kind of purification of gaseous benzene device

Country Status (1)

Country Link
CN (1) CN206381794U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110237697A (en) * 2019-06-12 2019-09-17 河北科技大学 A kind of device of biological cleaning exhaust gas

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110237697A (en) * 2019-06-12 2019-09-17 河北科技大学 A kind of device of biological cleaning exhaust gas
CN110237697B (en) * 2019-06-12 2021-10-08 河北科技大学 Biological waste gas purifying device

Similar Documents

Publication Publication Date Title
JP2011524800A (en) Exhaust gas desulfurization method and exhaust gas desulfurization apparatus for a marine vessel
EP1645322B1 (en) Apparatus for removing nitrogen oxides
CN209138354U (en) Ship tail gas desulphurization system
CN206381794U (en) A kind of purification of gaseous benzene device
CN203253345U (en) Catalytic cracking flue gas desulfurization and dust removing tower
CN101597529A (en) Methane bio-desulfurization device
CN206621986U (en) A kind of desulfurization absorption plant
CN105217892B (en) Petrochemical comprehensive waste water treatment device and method
CN104772029B (en) Coupled double-region type high-efficiency flue gas mercury recovery device and application thereof
CN204543974U (en) A kind of heat-engine plant wet desulfurization water system rebalancing system
CN207462989U (en) Purifier containing methanol waste gas
CN110479043A (en) A kind of purification work system
AU2014279670B2 (en) Method and installation for removing sulphur from the digestate and the biogas of a digester
CN109224798A (en) A kind of desulfurization sulphuric acid plant and vehicular desulphurization plant
CN105349194B (en) A kind of offshore platform high gravity desulfurization device and method
CN203725014U (en) Hydrogen sulfide gas purification device
CN205773694U (en) Oily waste water treatment integrating device in float cabin
CN104971601A (en) Acid gas vertical reactor and processing method
CN209108831U (en) A kind of oil-containing emission-control equipment
CN209098578U (en) Crude oil loads device for recovering oil and gas onto ship
CN207307227U (en) A kind of toluene rectifying recovery system
CN205442718U (en) Reduce profit decker of emulsification volume
CN201441885U (en) Water-saving acid mist absorption device
CN206666312U (en) A kind of anti-clogging acidification reaction settling separation device
CN207943953U (en) Container-type amine purification device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: 301700 Wang Tang Village, mechang Town, Wuqing District, Tianjin

Patentee after: Tianjin jaten environmental protection equipment Limited by Share Ltd

Address before: 301700 Wang Tang Village, mechang Town, Wuqing District, Tianjin

Patentee before: Tianjin Jiateng Environmental Protection Equipment Co.,Ltd.

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

Granted publication date: 20170808

Termination date: 20191208