CN209034083U - Middle test run with exhaust gas pretreatment and exhaust gas Adsorption Concentration device - Google Patents
Middle test run with exhaust gas pretreatment and exhaust gas Adsorption Concentration device Download PDFInfo
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- CN209034083U CN209034083U CN201821291256.2U CN201821291256U CN209034083U CN 209034083 U CN209034083 U CN 209034083U CN 201821291256 U CN201821291256 U CN 201821291256U CN 209034083 U CN209034083 U CN 209034083U
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Abstract
The utility model has the middle test run of exhaust gas pretreatment and exhaust gas Adsorption Concentration device, it is characterised in that: including moveable car body, the car body is loaded with waste gas pre-treating device and exhaust gas Adsorption Concentration device；Waste gas pre-treating device and exhaust gas Adsorption Concentration device are sequentially connected in series, waste gas pre-treating device and exhaust gas Adsorption Concentration device are equipped with air inlet and air outlet, sequentially connected pipeline is equipped with opening/shutting valve, to carry out open and close as needed, in the other valve for being connected to sampling exhaust pipe and being located on exhaust pipe in the gas outlet of waste gas pre-treating device and exhaust gas Adsorption Concentration device.The pilot scale bassinet structure with exhaust gas pretreatment and exhaust gas Adsorption Concentration device is simple, design is reasonable, be conducive to carry out processing experiment and detection to the technical parameters such as design of Treatment of Waste Gas and technique arrangement flexiblely, avoid building the drawbacks of exhaust-gas treatment facilities are unable to satisfy the demand of processing exhaust gas.
Description
Technical field:
The utility model relates to a kind of middle test runs with exhaust gas pretreatment and exhaust gas Adsorption Concentration device.
Background technique:
Industrial waste gas refers to containing for the various discharge air generated in plant area, enterprise fuel combustion and production process
The general name of contaminant gases.
These exhaust gas have: carbon dioxide, carbon disulfide, hydrogen sulfide, fluoride, nitrogen oxides, chlorine, hydrogen chloride, an oxidation
Carbon, sulfuric acid (mist) lead mercury, beryllide, flue dust and industrial dust, are emitted into atmosphere, can pollute air.These substances are not by
Same approach respiratory tract enters the internal of people, and some directly generates harm, and there are also cumulative effect, the more serious harm of meeting for some
The health of people.
In order to solve the problems, such as industrial waste gas pollute, many factories also built processing polluted gas facility, but due to
Before building those facilities, after only being detected in advance to the exhaust gas of factory's discharge, the design and construction that are carried out according to theory
, often after actually building, handled exhaust gas is not able to satisfy the requirement of discharge, to cause the increase of construction cost.
Summary of the invention:
The purpose of this utility model is to be to provide a kind of pilot scale with exhaust gas pretreatment and exhaust gas Adsorption Concentration device
Vehicle, this has, and the pilot scale bassinet structure of exhaust gas pretreatment and exhaust gas Adsorption Concentration device is simple, design is reasonable, is conducive to flexible
Ground carries out processing experiment and detection to design of Treatment of Waste Gas and the technique technical parameters such as arrange, avoid building exhaust-gas treatment facilities without
Method meets the drawbacks of the needs of processing exhaust gas.
The utility model has the middle test run of exhaust gas pretreatment and exhaust gas Adsorption Concentration device, it is characterised in that: including can
Mobile car body, the car body are loaded with waste gas pre-treating device and exhaust gas Adsorption Concentration device.
Further, above-mentioned waste gas pre-treating device and exhaust gas Adsorption Concentration device are sequentially connected in series, waste gas pre-treating device
Air inlet and air outlet are equipped with exhaust gas Adsorption Concentration device, sequentially connected pipeline is equipped with opening/shutting valve, according to need
Carry out open and close, the gas outlet of waste gas pre-treating device and exhaust gas Adsorption Concentration device it is other be connected to sampling exhaust pipe and
The valve being located on exhaust pipe.
Further, above-mentioned waste gas pre-treating device successively includes dry filter, scrubbing tower and oil absorbent material.
Further, electrostatic preprocessor is equipped between above-mentioned scrubbing tower and oil absorbent material.
Further, the waste water of above-mentioned oil absorbent material delivery outlet passes through coagulative precipitation tank and water filtering ponds.
Further, above-mentioned exhaust gas Adsorption Concentration device successively includes active carbon adsorber and/or zeolite adsorber.
Further, the tail gas mouth out of air inlet end connection the installed container of oil absorbent material of above-mentioned active carbon adsorber.
The utility model has exhaust gas pretreatment and the middle test run of exhaust gas Adsorption Concentration device when in use, can be driven to
The factory for needing to carry out exhaust-gas treatment allows exhaust gas by the air intake of the outlet port of piping connection factory test run in this
Waste gas pre-treating device is only first passed through, samples and is detected from the tail gas that waste gas pre-treating device is discharged；Then allow exhaust gas
Only pass through waste gas pre-treating device and exhaust gas Adsorption Concentration device, from exhaust gas Adsorption Concentration device be discharged tail gas in sample into
Row detection；Determine it is using construction waste gas pre-treating device or exhaust gas pretreatment by the result of above two sampling Detection
Device and exhaust gas Adsorption Concentration device；When above-mentioned detection is by waste gas pre-treating device or by waste gas pre-treating device and exhaust gas absorption
Enrichment facility can meet the requirement of plant gas processing, then later period factory can be according to waste gas pre-treating device or exhaust gas
Pretreatment unit and exhaust gas Adsorption Concentration device are designed and construct, only the waste gas pre-treating device at the scene or by exhaust gas
Pretreatment unit and exhaust gas Adsorption Concentration device are different from the processing scale of construction of middle test run, and therefore, the utility model can give the later period
Practical build provides more accurately reference, is conducive to avoid the phenomenon that doing over again after site operation building course, is substantially shorter
Construction period and cost.
Detailed description of the invention:
Fig. 1 is the organigram of the utility model；
Fig. 2 is the principle organigram of waste gas pre-treating device；
Fig. 3 is the local structure schematic diagram of Fig. 2；
Fig. 4 is the principle organigram of exhaust gas Adsorption Concentration device；
Fig. 5 is the organigram of Fig. 1 another kind embodiment；
Fig. 6 is the principle organigram of waste gas purification apparatus；
Fig. 7 is the principle organigram of medicament deodoriser；
Fig. 8 is the principle organigram of UV photocatalyst；
Fig. 9 is the principle organigram of waste gas pre-treating device another kind embodiment；
Figure 10 is the connection structure diagram of waste gas pre-treating device, exhaust gas Adsorption Concentration device and waste gas purification apparatus.
Specific embodiment:
The utility model method is described in further detail below with reference to embodiment.It should be strongly noted that this
The protection scope of utility model should include but is not limited to technology contents disclosed in the present embodiment.
The utility model has exhaust gas pretreatment and the middle test run of exhaust gas Adsorption Concentration device includes moveable car body 1,
The car body is loaded with waste gas pre-treating device A and exhaust gas Adsorption Concentration device B.Above-mentioned car body can be lorry, container drags
Vehicle etc..
One of embodiment, in order to meet the needs of exhaust-gas treatment, above-mentioned waste gas pre-treating device A successively includes dry type
Filter A1, scrubbing tower A2 and oil absorbent material A4.Or waste gas pre-treating device A successively include dry filter A1, scrubbing tower A2,
Electrostatic preprocessor A3 and oil absorbent material A4.
Principle of the dry filter A1 based on inertial separation, forcing load air-flow, repeatedly member changes direction, those compare in this way
The particle (the pollution particle i.e. in exhaust gas) of air weight will be adhered on wall surface or filter screen, and air does not hinder particularly then
Hinder and continues to move；There are mainly two types of patterns for dry filter: dry band rotating filter and bag filter.Dry band rotation filtering
Device, through gear, drives dry band (product replacement also can be used in a kind of lint shape product that nylon yarn is made into) to turn by motor
It is dynamic.Air is filtered by dust when dry band.The dry adhering dust that takes is more and more, and doing band resistance will increase.When more than regulation
When value (about 150Pa), the differential manometer with contact connects motor, makes dry band rotation, dry band dusty is rolled,
One section of clean dry band is unfolded simultaneously.When air drag restores normal, it is automatically stopped rotation.This filter clogging effect is very
Height, up to 97% or more, and not oil-containing in filtered air.The disadvantage is that dry band cannot be used again after.Bag filter is to make sky
Gas through filter bag dirt accumulation on bag.When dust is accumulated to (such as 1000Pa) when pressure difference being made to reach a certain value, certainly on filter bag
It is dynamic to be blown into blowback air (being supplied by individual Roots blower), the dust on bag is blown off, is accumulated in following ash bucket simultaneously
Periodically discharge.When pressure difference drops to a certain value (such as 560Pa), blowback is automatically stopped.Filter bag is by wool felt and staple fibre
It is made into (as felt), the size and number of bag depend on the size of air capacity.This filter clogging effect is also very high, 98%
More than, not oil-containing in filtered air can be automatically controled, easy to operate.The dust content of air is unrestricted, and adaptability is good.
The disadvantage is that resistance is larger, it is 600~1200Pa, the too big area of air humidity or season, filter bag is easy blocking.Filter bag uses the longevity
Order about 3~5a.Above-mentioned dry filter can be the HT-40AMP model pocket type of Guangdong Heng Tian filter plant Co., Ltd production
Filter.
Scrubbing tower A2 is a kind of gas purification equipment.It is can change on the basis of floating filler layer gas purifier
And then generate, it is widely used in the pre-treatment of industrial waste gas purifying, dedusting etc., clean-up effect is fine.To coal gas chemical industry
For skill, gas washing is inevitable, and whatsoever Coal Gasification Technology all uses the operation of this unit.Due to its working principle class
Like washing process, therefore named scrubbing tower.Scrubbing tower is made of tower body, column plate, reboiler.Reboiler is generally with steaming in use
Vapour heating, condenser circulating water heat conducting.Balance should be established before use, that is, is passed through purer product component steam and condensation
Water adjusts its evaporation capacity and regurgitant volume, certain thickness liquid can be accumulated on column plate, just when mixing gas component is passed through
Cleaning function can be played rapidly.What a liquid level, a few points such as two temperature and two pressure differences are controlled in use.
That is scrubbing tower liquid level, gas inlet temperature, tower top temperature, pressure reduction between tower (difference of scrubbing tower inlet pressure and tower top pressure) are cold
Condenser pressure difference (difference of tower top and condensator outlet pressure).In general, the higher the better for gas inlet temperature, can prevent impurity
Solidification or liquefaction not can enter scrubbing tower, but can not be too high, to prevent system because temperature is excessively high and not easy to control.Control temperature
While also need guarantee gas flow rate, i.e. the pressure of import cannot be too small, so that dust can enter scrubbing tower.Mixed gas is passed through
After scrubbing tower, portion gas can be condensed into liquid and stay in tower reactor, and the temperature for adjusting reboiler evaporates liquid upwards, then adjusts
Condenser makes liquid reflux to column plate, forms a balance.Due to there is certain thickness liquid on column plate, so meeting between scrubbing tower tower
There is certain pressure difference, pressure difference should be made to keep constant as far as possible when adjusting reboiler could form a balance.It is answered when adjusting tower top temperature
It prevents that temperature is excessively high and makes that impurity vaporizes or distillation is gas and cannot play cleaning function, but condensation temperature is also unsuitable too low, prevents
Only Product liquid influences to use in condenser hydrops.It is noted also while being put more than paying attention to and adjusts scrubbing tower with reboiler
Liquid level it should be made slowly to go up to prevent in tower bottoms the excessively high generation precipitating of impurity concentration.
Electrostatic preprocessor is existing equipment, can be the model produced by Hangzhou LQ Environmental Engineering Co., Ltd.
The exhaust gas electrostatic treatment equipment of LGJD, its working principle is that: under electric field action, the free ion in air will be to two Ghandler motions
Dynamic, voltage is higher, electric field strength is higher, and the movement velocity of ion is faster.Due to the movement of ion, interpolar forms electric current.It opens
When the beginning, the free ion in air is few, and electric current is less.After voltage is increased to certain numerical value, the ion near discharge electrode is obtained
Higher energy and speed, when they hit the neutral atom in air, neutral atom can resolve into positive and negative ion, this existing
As referred to as air ionization.Above-mentioned electrostatic preprocessor utilizes the principle to be made.The electrostatic preprocessor is in the application equipment
It can be apolegamy equipment, i.e., a root canal in parallel road and valve between scrubbing tower A2 and oil absorbent material installation container A 43, to be not required to
Ignore the equipment when wanting, i.e. waste gas pre-treating device A can successively include dry filter A1, scrubbing tower A2 and oil absorbent material A4.
Oil absorbent material A4 is made of the superfine fibre textile cloth of lipophilicity, is free of chemical agent, not will cause secondary public affairs
Evil, can absorb rapidly the liquid such as greasy dirt, organic solvent, hydrocarbon, the vegetable oil of weight decades of times itself.Oil absorbent material can be with
It is the SHC16110329-03 oil absorbent material of the model of Dongying Han De oil equipment Co., Ltd production.Oil absorbent material A4 is mounted on one
It installs in container A 43, and it is with inlet, outlet.
One of embodiment, in order to which the waste water for handling scrubbing tower carries out water process, in the liquid by oil absorbent material A4
(waste water) passes through coagulative precipitation tank A5 and water filtering ponds A7, and the coagulative precipitation tank A5, which is one, can contain the concave of waste water
Container, the waste water come out from coagulative precipitation tank A5 enter water filtering ponds A7, which is internal with multi-layer water filtering
The container containing of A71 is netted, exhaust gas passes sequentially through dry filter A1, scrubbing tower A2, electrostatic preprocessor A3 and oil absorbent material A4 mistake
Filter treated tail gas carries out exhaust gas sampling Detection, and waste water is sampled after also passing through coagulative precipitation tank A5 and water filtering ponds A7
Detection, and when the exhaust gas of sampling meets national emission standard, then it is only necessary to construction waste gas pre-treating device A for the factory
Waste gas treatment equipment, only the facility treating capacity of site operation is different from the treating capacity of the application；And giving up when sampling
Gas is unsatisfactory for national emission standard, opens the valve 31 between waste gas pre-treating device A and exhaust gas Adsorption Concentration device B, makes to give up
Gas can be handled further across exhaust gas Adsorption Concentration device B.
Oil absorbent material A4 is placed in the container with import and export, exhaust gas and waste water point after oil absorbent material A4
Not Chu tail gas mouth, go out the discharge of waste water mouth, the tail gas sample port of waste gas pre-treating device A, which is located at, should go out tail gas mouth A41, should go out tail gas
Mouth namely the air inlet for connecting past exhaust gas Adsorption Concentration device B；Waste water mouth A42 connects the entrance toward coagulative precipitation tank A5 out, gives up
Water sample port is located at the discharge mouth of a river of water filtering ponds A7.
Dry filter A1, scrubbing tower A2, electrostatic preprocessor A3 and oil absorbent material A4 are existing product, and the application adopts
With with existing identical principle and structure, it is the volume-diminished of those components that only the treating capacity of exhaust gas or waste water is different, with
Meet mountable on vehicle.
One of embodiment, above-mentioned exhaust gas Adsorption Concentration device B successively include that active carbon adsorber B1 and/or zeolite are inhaled
Adnexa B2, air inlet end connection the installed container A 43 of oil absorbent material of above-mentioned active carbon adsorber go out tail gas mouth A41.
Active carbon adsorber B1 is a kind of dry type waste gas treatment equipment.By cabinet and it is seated in the intracorporal absorbing unit group of case
At.It is divided into plurality of specifications according to the quantity of absorbing unit and air quantity, it is more that activated carbon adsorption case selects different fillers can handle
Kind different exhaust gas mainly include three major class: 1, acid waste gas and acid mist (such as: NO<sub>2</sub>,<sub>2</sub>
SO<sub>4</sub>, HCL, HF etc.) 2, alkaline exhaust gas (such as: NH<sub>3</sub>deng) 3, organic exhaust gas and stink (example
Such as: benzene class, phenols, alcohols, ethers, tincture class)；It can be the model KS- of Ke Sen Environmental Protection Technology Co., Ltd, Huizhou City production
HX active carbon adsorber or activated carbon adsorption case.
Zeolite adsorber B2 is identical as active carbon adsorber B1 structure, and only filler therein is using zeolite.
Active carbon adsorber B1 and/or boiling are entered by the tail gas for going out tail gas mouth A41 output of the installed container A 43 of oil absorbent material
Stone absorber B2, handles exhaust gas further, and the tail gas exported from the output end of zeolite adsorber B2 is defeated through piping
It is sent to waste gas purification apparatus C, while other second for being connected to sampling second exhaust pipe 6 and being located on second exhaust pipe on pipeline
Valve 7 is sampled detection by the tail gas that second exhaust pipe is discharged, and is located in advance with obtaining the tail gas of factory discharge by exhaust gas
Whether up to standard manage device A and exhaust gas Adsorption Concentration device B processing.
The utility model has exhaust gas pretreatment and the middle test run of exhaust gas Adsorption Concentration device when in use, can be driven to
The factory for needing to carry out exhaust-gas treatment is allowed useless by the air intake A0 of the outlet port of piping connection factory test run in this
Gas only first passes through waste gas pre-treating device, samples and is detected from the tail gas that waste gas pre-treating device is discharged；It then allows useless
Gas only passes through waste gas pre-treating device and exhaust gas Adsorption Concentration device, samples from the tail gas that exhaust gas Adsorption Concentration device is discharged
It is detected；Determine located in advance using construction waste gas pre-treating device or exhaust gas by the result of above two sampling Detection
Manage device and exhaust gas Adsorption Concentration device；When above-mentioned detection is by waste gas pre-treating device or by waste gas pre-treating device and exhaust gas suction
Attached enrichment facility can meet the requirement of plant gas processing, then later period factory can be according to waste gas pre-treating device or useless
Gas pretreatment unit and exhaust gas Adsorption Concentration device are designed and construct, only the waste gas pre-treating device at the scene or by giving up
Gas pretreatment unit and exhaust gas Adsorption Concentration device are different from the processing scale of construction of middle test run, therefore, after the utility model can be given
Phase practical construction provides more accurately reference, is conducive to avoid the phenomenon that doing over again after site operation building course, can contract significantly
Short construction period and cost.Mark has sent special exhaust gas inspection center (during such as various regions Environmental Protection Agency examines respectively after above-mentioned sampling
Heart etc.) it tests.
Another embodiment, in order to meet the demand of different exhaust-gas treatments, waste gas pre-treating device A and exhaust gas absorption are dense
Compression apparatus B is also connected with waste gas purification apparatus C, waste gas pre-treating device A, exhaust gas Adsorption Concentration device B and waste gas purification apparatus C-shaped
At waste gas treatment equipment 2；Waste gas pre-treating device A, exhaust gas Adsorption Concentration device B and waste gas purification apparatus C be sequentially connected in series, and
Waste gas pre-treating device A, exhaust gas Adsorption Concentration device B and waste gas purification apparatus C are equipped with air inlet and air outlet, are sequentially connected
Pipeline be equipped with opening/shutting valve, to carry out open and close as needed, such as it is only necessary to when waste gas pre-treating device, then close and give up
The first valve 31 connected between gas pretreatment unit, exhaust gas Adsorption Concentration device, and need waste gas pre-treating device and exhaust gas
When Adsorption Concentration device, then the second valve 32 connected between exhaust gas Adsorption Concentration device and waste gas purification apparatus is closed, opened
First valve 31 is connected to pumping on the gas outlet of waste gas pre-treating device, exhaust gas Adsorption Concentration device and waste gas purification apparatus side
Sample exhaust pipe 4 and the valve 5 being located on exhaust pipe.
One of embodiment, in order to realize further exhaust-gas treatment, above-mentioned waste gas purification apparatus C includes secondary exhaust gas
Deodorizing device C1 and exhaust gas apparatus for destroying C2, secondary exhaust gas deodorizing device C1 and exhaust gas apparatus for destroying C2 and exhaust gas Adsorption Concentration are filled
The exhaust emission tube for setting B is to be connected in parallel, and the tail gas selective exported from exhaust gas Adsorption Concentration device B is removed into secondary exhaust gas
Taste device C1 or exhaust gas apparatus for destroying C2.
Further, above-mentioned secondary exhaust gas deodorizing device C1 includes medicament deodoriser C4 and UV photocatalyst C5 and plasma
Deodoriser C6.The medicament deodoriser C4 is the container C41 with inlet, outlet, is equipped in container and is used for deodorization
Medicament C42, which can be active plant medicament, such as the deodorization for the model GL-A2 that Jinan Guan Long chemical company produces
The air inlet pipe of agent, container C41 is located at medicament C42 liquid level hereinafter, the escape pipe of container C41 is located at medicament C42 liquid level or more；UV light
Catalyst converter is the closed container C51 with inlet, outlet, and closed container air inlet is lower than gas outlet, in closed container
Equipped with UV photocatalysis fluorescent tube C52, UV photocatalysis fluorescent tube C52 be it is horizontal positioned, UV photocatalysis fluorescent tube C52 is in inlet, outlet saliva
Between prosposition is set；Plasma deodoriser can be the LB-FD low-temperature plasma of Cangzhou City De Tong environmental protection equipment Co., Ltd production
Exhaust gas device, for plasma deodoriser working principle under the action of extra electric field, what medium discharge generated largely takes energy electron bombardment
Contaminant molecule makes its ionization, dissociation and excitation, has then just caused physics, the chemical reaction of a series of complex, makes complicated big
Molecular contaminants are changed into simple small molecule safe material, or poisonous and harmful substance is made to be transformed into nontoxic or less toxic low evil
Substance, to enable pollutant degradation removal.
Further, above-mentioned exhaust gas apparatus for destroying C2 is heat accumulating type heating power incinerator RTO, its original of heat accumulating type heating power incinerator
Reason is that the organic matter (VOCs) in exhaust gas is oxidized to corresponding carbon dioxide and water at high temperature, to purify exhaust gas, and is returned
The heat released when exhaust gas decomposes is received, three Room RTO exhaust gas decomposition efficiencies reach 99% or more, and heat recovery efficiency reaches 95%
More than.RTO main structure is made of combustion chamber, regenerative chamber and switching valve etc..Different thermal energy can be selected to return according to actual needs
Debit's formula and switching valve mode.Heat accumulating type heating power incinerator is a kind of efficient VOCs treatment equipment, is fired with traditional catalysis
Burning, direct-fired thermal oxidation furnace (TO) are compared, and with the thermal efficiency high (>=95%), operating cost is low, can handle low concentration in Wind Volume
The features such as exhaust gas, when concentration is slightly higher, can also carry out secondary waste heat recycling, substantially reduce production and operation cost.
It is also provided with condenser in a device, the end that enters of the condenser is connected to the useless out of exhaust gas Adsorption Concentration device B
Gas port, what the outlet of condenser may be coupled to exhaust gas Adsorption Concentration device B enters exhaust gas port, to form circulation.
Pressure sensor can be equipped on dry filter A1 and container for installing oil absorbent material A4, in scrubbing tower A2
It is interior to be equipped with pH sensor and liquid level detector, electrostatic preprocessor A3, UV photocatalyst C5 and plasma deodoriser C6
Overload, electric leakage and temperature detector are inside installed；Active carbon adsorber B1 and zeolite adsorber B2 is equipped with temperature detector, stores
Temperature, pressure detector and temperature control adjuster are equipped in hot type heating power incinerator.Secondary exhaust gas deodorizing device C1 is equipped with liquid level
Detector, above-mentioned valve can with formula manual switch or and electric-controlled switch, sensor, instrument, which are shown etc., to be connected in intelligent control
The heart, intelligent control center can be interacted with man-machine interface, can also be by wirelessly being counted with cloud server and remote terminal
According to exchange.
The application kinds of processes is bound on a vehicle, and the validity and warp of resolution are determined for exhaust gas difference operating condition
Ji property.It avoids and carries out secondary rectification after directly doing engineering again.Practicability is high；Kinds of processes is bound on a vehicle, and system can
To automatically adjust to technological parameter, it is provided with automatic sampling, detection, record before and after each process section, is conducive to engineering skill
Art personnel analyze experimental data.There are inflammable and explosive risk in waste gas cleaning system, second level safeguard procedures are set in the present apparatus,
Two kinds of instrument are set in entering the pipeline before purification device, monitor the temperature and monitoring concentration of gas, level-one is yellow report
Alert, measure is to adjust temperature, gas concentration, and alarm；Second level is red alarm, and measure is starting automatic fire extinguisher, gas
Staged isolation, release, and alarm.
The working method of test run in the embodiment, the middle test run with exhaust gas pretreatment and exhaust gas Adsorption Concentration device
Including moveable car body, the car body is loaded with waste gas treatment equipment；The waste gas treatment equipment includes exhaust gas pretreatment dress
It sets, exhaust gas Adsorption Concentration device and waste gas purification apparatus；Waste gas treatment equipment includes waste gas pre-treating device, exhaust gas Adsorption Concentration
Device and waste gas purification apparatus are to be sequentially connected in series, and waste gas pre-treating device, exhaust gas Adsorption Concentration device and waste gas purification apparatus
Air inlet and air outlet are equipped with, sequentially connected pipeline is equipped with opening/shutting valve, to carry out open and close as needed, such as only
When needing waste gas pre-treating device, then the first valve connected between waste gas pre-treating device, exhaust gas Adsorption Concentration device is closed,
And when needing waste gas pre-treating device and exhaust gas Adsorption Concentration device, then close exhaust gas Adsorption Concentration device and waste gas purification apparatus
Between the second valve for connecting, open the first valve, filled in waste gas pre-treating device, exhaust gas Adsorption Concentration device and waste gas purification
The other valve for being connected to sampling exhaust pipe and being located on exhaust pipe in the gas outlet set；The portion exported by factory, it is optional
The output after waste gas pre-treating device of selecting property is sampled detection or by waste gas pre-treating device and exhaust gas Adsorption Concentration
Output is sampled detection or after waste gas pre-treating device and exhaust gas Adsorption Concentration device and waste gas purification apparatus after device
Output is sampled detection, and the tail gas index obtained by sampling Detection is that site operation is needed to pacify come the exhaust gas for determining the factory
It fills waste gas pre-treating device or waste gas pre-treating device and exhaust gas Adsorption Concentration device or passes through waste gas pre-treating device and give up
The attached enrichment facility of aspiration and waste gas purification apparatus.
The above is only the preferred embodiment of the present invention, it is all done according to present utility model application the scope of the patents it is equal
Deng variation and modification, it should all belong to the covering scope of the utility model.
Claims (1)
1. a kind of middle test run with exhaust gas pretreatment and exhaust gas Adsorption Concentration device, it is characterised in that: including moveable vehicle
Body, the car body are loaded with waste gas pre-treating device and exhaust gas Adsorption Concentration device；The waste gas pre-treating device and exhaust gas are inhaled
Attached enrichment facility is sequentially connected in series, and waste gas pre-treating device and exhaust gas Adsorption Concentration device are equipped with air inlet and air outlet, successively
The pipeline of connection is equipped with opening/shutting valve, to carry out open and close as needed, fills in waste gas pre-treating device and exhaust gas Adsorption Concentration
The other valve for being connected to sampling exhaust pipe and being located on exhaust pipe in the gas outlet set；The waste gas pre-treating device successively includes
Dry filter, scrubbing tower and oil absorbent material；Electrostatic preprocessor is equipped between the scrubbing tower and oil absorbent material；The oil absorbent material is defeated
The waste water of outlet passes through coagulative precipitation tank and water filtering ponds；The exhaust gas Adsorption Concentration device successively include active carbon adsorber and
Or zeolite adsorber；Air inlet end connection the installed container of oil absorbent material of the active carbon adsorber goes out tail gas mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821291256.2U CN209034083U (en) | 2018-08-10 | 2018-08-10 | Middle test run with exhaust gas pretreatment and exhaust gas Adsorption Concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821291256.2U CN209034083U (en) | 2018-08-10 | 2018-08-10 | Middle test run with exhaust gas pretreatment and exhaust gas Adsorption Concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209034083U true CN209034083U (en) | 2019-06-28 |
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ID=67030688
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821291256.2U Expired - Fee Related CN209034083U (en) | 2018-08-10 | 2018-08-10 | Middle test run with exhaust gas pretreatment and exhaust gas Adsorption Concentration device |
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| Country | Link |
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| CN (1) | CN209034083U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117019399A (en) * | 2023-07-24 | 2023-11-10 | 广州华科环保工程有限公司 | Integrated equipment for classifying pretreatment after centralized collection of multicomponent organic waste gas |
-
2018
- 2018-08-10 CN CN201821291256.2U patent/CN209034083U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117019399A (en) * | 2023-07-24 | 2023-11-10 | 广州华科环保工程有限公司 | Integrated equipment for classifying pretreatment after centralized collection of multicomponent organic waste gas |
| CN117019399B (en) * | 2023-07-24 | 2024-04-05 | 广州华科环保工程有限公司 | Integrated equipment for classifying pretreatment after centralized collection of multicomponent organic waste gas |
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Granted publication date: 20190628 |