CN206853397U - A kind of adsorption tower device administered for medium-sized and small enterprises VOCs - Google Patents
A kind of adsorption tower device administered for medium-sized and small enterprises VOCs Download PDFInfo
- Publication number
- CN206853397U CN206853397U CN201720455798.8U CN201720455798U CN206853397U CN 206853397 U CN206853397 U CN 206853397U CN 201720455798 U CN201720455798 U CN 201720455798U CN 206853397 U CN206853397 U CN 206853397U
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- CN
- China
- Prior art keywords
- gas
- absorption tower
- drawer
- gas absorption
- mixing tank
- 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
Links
- 239000012855 volatile organic compound Substances 0.000 title claims abstract description 25
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 16
- 238000010521 absorption reaction Methods 0.000 claims abstract description 32
- 238000002156 mixing Methods 0.000 claims abstract description 22
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000002808 molecular sieve Substances 0.000 claims abstract description 17
- 238000012216 screening Methods 0.000 claims abstract description 10
- 230000002787 reinforcement Effects 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 67
- 239000002912 waste gas Substances 0.000 claims description 32
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 6
- 229910021536 Zeolite Inorganic materials 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000010457 zeolite Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- 230000001413 cellular effect Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 150000005826 halohydrocarbons Chemical class 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000002649 leather substitute Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model discloses a kind of adsorption tower device administered for medium-sized and small enterprises VOCs,Mainly include spinner flowmeter,Gas mixing tank,Gas absorption tower,The spinner flowmeter respectively with the gas mixing tank,Gas absorption tower connects,The gas absorption tower also includes air outlet,Drawer,Molecule screening washer,The air outlet is located at gas absorption top of tower,The air outlet other end is connected with fan inlet,The drawer is located on gas absorption tower,The molecule screening washer is located at the inside of gas absorption tower,Drawer also includes handle,Unit molecular sieve,Strengthen supporting plate,Baffle plate,The handle is located at the baffle surface,Handle is located at the outer surface of gas absorption tower with baffle plate,The unit molecular sieve is located at drawer inner surface,The reinforcement supporting plate is located at drawer bottom,It is not up to standard that the present apparatus can successfully manage medium-sized and small enterprises VOCs discharges,And economical rationality,Floor space is small.
Description
Technical field
It the utility model is related to air environmental pollution Treatment process field, and in particular to one kind is directed to medium-sized and small enterprises VOCs
The adsorption tower device of improvement.
Background technology
Volatile organic matter (VOCs) is the important pollutant for causing haze, has had a strong impact on air quality, animals and plants life
Long and human health, and there is potential safety hazard.It is mainly derived from machinery industry, surface anticorrosion, antirust treatment, plasthetics
The industry rows such as production, household electrical appliance, insulating materials, artificial leather industry, petrochemical industry, pharmaceuticals industry, printing industry, packaging for foodstuff
Put the major pollutants in waste gas.VOCs is divided into 8 classes by its chemical constitution:Alkanes, aromatic hydrocarbons, alkenes, halohydrocarbon, esters, aldehyde
Class, ketone and other chemicals.There is toxicity mostly and with stench, some or carcinogen, as vinyl chloride, benzene, toluene,
Dimethylbenzene etc..Moreover, most VOCs are inflammable, explosive, this brings many unsafe factors to enterprise's production.
Such as a kind of small tolerance VOCs disclosed in Chinese utility model 201520788775.X administers all-in-one, the device
Integrated level is high, small volume, and processing quality is good, but can not tackle some medium-sized and small enterprises, and the discharge of medium-sized and small enterprises waste gas is small,
Having a rest property produces, and exhaust gas concentration changes greatly, and organic exhaust gas concentration is relatively low, and floor space is smaller, and ability to shoulder economically is limited etc..Cause
This, there is provided safe and reliable to operation, economical rationality, capital expenditure and operating cost are reduced as far as possible, floor space is small, and energy consumption is low,
The VOCs Treatment process of actual motion effect energy stably reaching standard and the eager need that equipment is industry development.
The content of the invention
The purpose of this utility model is to provide a kind of adsorption tower device administered for medium-sized and small enterprises VOCs, can there is effect
Medium-sized and small enterprises VOCs is discharged not up to standard, there is provided safe and reliable to operation, economical rationality, reduce capital expenditure and running cost as far as possible
With floor space is small, and energy consumption is low, the equipment of the VOCs improvement of actual motion effect energy stably reaching standard.
The technical solution of the utility model is:A kind of adsorption tower device administered for medium-sized and small enterprises VOCs, mainly includes
Spinner flowmeter, gas mixing tank, gas absorption tower, the spinner flowmeter respectively with the gas mixing tank, gas absorption
Tower connects, and gas mixing tank also includes mixed gas outlet, deflector, exhaust gas inlet, waste gas and disperses the scattered pad of mouth, waste gas, described
Mixed gas outlet is located at gas mixing tank top, and the exhaust gas inlet is located at gas mixing tank outer surface and close to bottom position
Put, the waste gas disperses mouth one end and is connected with exhaust gas inlet, and the other end is downward perpendicular to base plane, the scattered pad position of the waste gas
In on gas absorption tower bottom, the deflector is located inside gas mixing tank, is connected with the inwall of gas mixing tank, the gas
Body adsorption tower also includes air outlet, drawer, molecule screening washer, and the air outlet is located at gas absorption top of tower, and air outlet is another
End is connected with fan inlet, and the drawer is located on gas absorption tower, and the molecule screening washer is located at the inside of gas absorption tower,
Drawer also includes handle, unit molecular sieve, strengthens supporting plate, baffle plate, and the handle is located at the baffle surface, handle and baffle plate
Positioned at the outer surface of gas absorption tower, the unit molecular sieve is located at drawer inner surface, and the reinforcement supporting plate is located at bottom of drawer
Portion.
Further, the unit molecular sieve individually can be dismantled and changed, extension fixture service life.
Further, the reinforcement supporting plate is distributed for bar shaped, effective bracing means, and does not influence device to VOCs's
Processing.
Further, the deflector and inwall tiltedly angle at 45 ° is obliquely, it is ensured that waste gas is carried out more fully
Processing.
Further, the waste gas disperses mouth outlet side and the scattered pad of the waste gas is vertical relative, ensure that waste gas enters
Waste gas is disperseed after the scattered pad of waste gas is hit after gas absorption tower, lifting device efficiency.
Operation principle of the present utility model is:Using zeolite molecular sieve, and it is processed into cellular, can effectively increases suction
Attached efficiency, reduce the useful load of molecular sieve, then molecular sieve is arranged to independent unit, conveniently can dismantle and change, utilize
Hydrophobic modified zeolite can effectively prevent influence of the moisture to zeolite adsorption performance in waste gas.Waste gas is after emission-control equipment
Handled again by biofiltration tower, VOCs treatment effeciencies improve.
Compared with prior art, the beneficial effects of the utility model are:For the VOCs Treatment process methods of medium-sized and small enterprises
Simply, rationally, it is economical and practical, effectively alleviate the problem of medium-sized and small enterprises waste gas discharges.
Brief description of the drawings
Fig. 1 is agent structure schematic diagram of the present utility model;
Fig. 2 is the utility model mixed gas tank schematic diagram;
Fig. 3 is the utility model drawer schematic diagram:
Wherein, 1- air outlets, 2- drawers, 3- molecules screening washer, 4- spinner flowmeters, 5- gas mixings tank, 6- gases are inhaled
Attached tower, 7- mixed gas outlets, 8- deflectors, 9- exhaust gas inlets, 10- handles, 11- unit molecules screening washer, 12- strengthen support
Plate, 13- baffle plates.
Embodiment
It is a kind of for medium-sized and small enterprises VOCs administer adsorption tower device, mainly include spinner flowmeter 4, gas mixing tank 5,
Gas absorption tower 6, spinner flowmeter 4 are connected with gas mixing tank 5, gas absorption tower 6 respectively, and gas mixing tank 5 also includes mixed
Gas outlet 7, deflector 8, exhaust gas inlet 9, the scattered mouth of waste gas, the scattered pad of waste gas are closed, mixed gas outlet 7 is located at gas mixing tank 5
Top, exhaust gas inlet 9 are located at the outer surface of gas mixing tank 5 and disperse mouth one end and exhaust gas inlet 9 close to bottom position, waste gas
Connection, the other end is downward perpendicular to base plane, and for the scattered pad of waste gas in the bottom interior wall of gas absorption tower 6, waste gas disperses mouth
Outlet side and the scattered pad of waste gas are vertical relative, ensure that waste gas obtains into waste gas after the scattered pad of shock waste gas after gas absorption tower
Scattered, lifting device efficiency, deflector 8 and inwall tiltedly angle at 45 ° are obliquely, it is ensured that waste gas is more fully located
Reason, gas absorption tower 6 also include air outlet 1, drawer 2, molecule screening washer 3, and air outlet 1 is located at the top of gas absorption tower 6, air-out
1 other end of mouth is connected with fan inlet, and drawer 2 is located on gas absorption tower 6, and molecule screening washer 3 is located at the interior of gas absorption tower 6
Portion, drawer 2 also include handle 10, unit molecular sieve 11, strengthen supporting plate 12, baffle plate 13, and handle 10 is located at the surface of baffle plate 13,
Handle 10 is located at the outer surface of gas absorption tower 6 with baffle plate 13, and unit molecular sieve 11 is located at the inner surface of drawer 2, unit molecular sieve
11 individually can dismantle and change, extension fixture service life, strengthen supporting plate 12 and are located at the bottom of drawer 2, strengthen supporting plate 12
It is distributed for bar shaped, effective bracing means, and does not influence processing of the device to VOCs.
Operation principle:Using zeolite molecular sieve, and it is processed into cellular, can effectively increases adsorption efficiency, reduce
The useful load of molecular sieve, then molecular sieve is arranged to independent unit, conveniently it can dismantle and change, utilize hydrophobic modified zeolite
Influence of the moisture to zeolite adsorption performance in waste gas can effectively be prevented.Waste gas passes through biofiltration again after emission-control equipment
Tower processing, VOCs treatment effeciencies improve.
To state according to desirable embodiment of the present utility model as enlightenment, pass through above-mentioned description, relevant staff
Various changes and amendments can be carried out in the range of without departing from this item utility model technological thought completely.This item is practical
New technical scope is not limited to the content on specification, it is necessary to determines that its is technical according to right
Scope.
Claims (5)
1. it is a kind of for medium-sized and small enterprises VOCs administer adsorption tower device, it is characterised in that mainly including spinner flowmeter (4),
Gas mixing tank (5), gas absorption tower (6), the spinner flowmeter (4) respectively with the gas mixing tank (5), gas absorption
Tower (6) connects, and gas mixing tank (5) also includes mixed gas outlet (7), deflector (8), exhaust gas inlet (9), waste gas and disperses mouth
(14), the scattered pad (15) of waste gas, the mixed gas outlet (7) are located at the top of gas mixing tank (5), exhaust gas inlet (9) position
In gas mixing tank (5) outer surface and close to bottom position, the waste gas disperses mouth (14) one end and connected with exhaust gas inlet (9)
Connect, the other end is downward perpendicular to base plane, and the scattered pad (15) of the waste gas is located in gas absorption tower (6) bottom interior wall, institute
State deflector (8) and be located at gas mixing tank (5) inside, be connected with the inwall of gas mixing tank (5), the gas absorption tower (6)
Also include air outlet (1), drawer (2), molecule screening washer (3), the air outlet (1) is located at the top of gas absorption tower (6), air-out
Mouth (1) other end is connected with fan inlet, and the drawer (2) is located on gas absorption tower (6), molecule screening washer (3) position
In the inside of gas absorption tower (6), drawer (2) also includes handle (10), unit molecular sieve (11), strengthens supporting plate (12), gear
Plate (13), the handle (10) are located at the baffle plate (13) surface, and handle (10) is located at gas absorption tower (6) with baffle plate (13)
Outer surface, the unit molecular sieve (11) are located at drawer (2) inner surface, and the reinforcement supporting plate (12) is located at drawer (2) bottom.
2. a kind of adsorption tower device administered for medium-sized and small enterprises VOCs as claimed in claim 1, it is characterised in that described
Unit molecular sieve (11) individually can be dismantled and changed.
3. a kind of adsorption tower device administered for medium-sized and small enterprises VOCs as claimed in claim 1, it is characterised in that described to add
Strong supporting plate (12) is distributed for bar shaped.
4. a kind of adsorption tower device administered for medium-sized and small enterprises VOCs as claimed in claim 1, it is characterised in that described to lead
Flowing plate (8) and inwall tiltedly angle at 45 ° are obliquely.
5. a kind of adsorption tower device administered for medium-sized and small enterprises VOCs as claimed in claim 1, it is characterised in that described useless
Qi leel raw edge (14) outlet side and the scattered pad (15) of the waste gas are vertical relative.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720455798.8U CN206853397U (en) | 2017-04-27 | 2017-04-27 | A kind of adsorption tower device administered for medium-sized and small enterprises VOCs |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720455798.8U CN206853397U (en) | 2017-04-27 | 2017-04-27 | A kind of adsorption tower device administered for medium-sized and small enterprises VOCs |
Publications (1)
Publication Number | Publication Date |
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CN206853397U true CN206853397U (en) | 2018-01-09 |
Family
ID=60822907
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CN201720455798.8U Expired - Fee Related CN206853397U (en) | 2017-04-27 | 2017-04-27 | A kind of adsorption tower device administered for medium-sized and small enterprises VOCs |
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CN108525510A (en) * | 2018-04-13 | 2018-09-14 | 衢州市衢江区土壤肥料技术推广站 | A kind of environment-friendly type absorption processing method of organic fertilizer production technology waste gas |
US10987443B1 (en) | 2020-07-03 | 2021-04-27 | Chio Kang Medical, Inc. | Container sterilization device and system, assembling method thereof, and use thereof |
US11085016B1 (en) | 2020-01-20 | 2021-08-10 | Chio Kang Medical, Inc. | Method for screening bacteria capable of degrading ethylene oxide |
US11103608B1 (en) | 2020-07-03 | 2021-08-31 | Chio Kang Medical, Inc. | Mobile pretreatment apparatus and an operating method thereof, and a mobile analysis apparatus and an operating method thereof |
US11103829B1 (en) | 2020-03-18 | 2021-08-31 | Chio Kang Medical, Inc. | Systems and methods for treating ethylene oxide waste gas |
US11110390B1 (en) | 2020-03-18 | 2021-09-07 | Chio Kang Medical, Inc. | Systems and methods for treating sterilization exhaust gas containing ethylene oxide |
US11123449B1 (en) | 2020-07-03 | 2021-09-21 | Chio Kang Medical, Inc. | Mobile sterilization system, mobile execution system, and mobile analysis system |
US11124438B2 (en) | 2020-01-20 | 2021-09-21 | Chio Kang Medical, Inc. | Alcaligenes faecalis for degrading ethylene oxide |
US11125498B1 (en) | 2020-03-18 | 2021-09-21 | Chio Kang Medical, Inc. | Gas liquefaction separator, gas liquefaction recovery system, and method for separating and recovering ethylene oxide |
US11123680B1 (en) | 2020-03-18 | 2021-09-21 | Chio Kang Medical, Inc. | Devices, systems, and methods for treating ethylene oxide waste gas |
US20210291105A1 (en) | 2020-03-19 | 2021-09-23 | Chio Kang Medical, Inc. | Ethylene Oxide Adsorption Tower and Recovery System, and Method for Recovering Ethylene Oxide |
WO2021184596A1 (en) * | 2020-03-19 | 2021-09-23 | Qiaokang Biotech (Guangdong) Co., LTD. | Ethylene oxide adsorption tower and recovery system, and method for recovering ethylene oxide |
US11130095B1 (en) | 2020-03-18 | 2021-09-28 | Chio Kang Medical, Inc. | Sterilization exhaust gas treating system and method for treating ethylene oxide-containing sterilization exhaust gas by using the same |
US11130939B2 (en) | 2020-01-20 | 2021-09-28 | Chio Kang Medical, Inc. | Bacteria for degrading ethylene oxide and uses thereof |
US11136253B1 (en) | 2020-03-18 | 2021-10-05 | Chio Kang Medical, Inc. | Microbiological treatment system for ethylene oxide exhaust gas |
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- 2017-04-27 CN CN201720455798.8U patent/CN206853397U/en not_active Expired - Fee Related
Cited By (17)
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CN108525510A (en) * | 2018-04-13 | 2018-09-14 | 衢州市衢江区土壤肥料技术推广站 | A kind of environment-friendly type absorption processing method of organic fertilizer production technology waste gas |
US11124438B2 (en) | 2020-01-20 | 2021-09-21 | Chio Kang Medical, Inc. | Alcaligenes faecalis for degrading ethylene oxide |
US11220667B2 (en) | 2020-01-20 | 2022-01-11 | Chio Kang Medical, Inc. | Bacteria for degrading ethylene oxide and applications thereof |
US11085016B1 (en) | 2020-01-20 | 2021-08-10 | Chio Kang Medical, Inc. | Method for screening bacteria capable of degrading ethylene oxide |
US11130939B2 (en) | 2020-01-20 | 2021-09-28 | Chio Kang Medical, Inc. | Bacteria for degrading ethylene oxide and uses thereof |
US11125498B1 (en) | 2020-03-18 | 2021-09-21 | Chio Kang Medical, Inc. | Gas liquefaction separator, gas liquefaction recovery system, and method for separating and recovering ethylene oxide |
US11110390B1 (en) | 2020-03-18 | 2021-09-07 | Chio Kang Medical, Inc. | Systems and methods for treating sterilization exhaust gas containing ethylene oxide |
US11103829B1 (en) | 2020-03-18 | 2021-08-31 | Chio Kang Medical, Inc. | Systems and methods for treating ethylene oxide waste gas |
US11123680B1 (en) | 2020-03-18 | 2021-09-21 | Chio Kang Medical, Inc. | Devices, systems, and methods for treating ethylene oxide waste gas |
US11130095B1 (en) | 2020-03-18 | 2021-09-28 | Chio Kang Medical, Inc. | Sterilization exhaust gas treating system and method for treating ethylene oxide-containing sterilization exhaust gas by using the same |
US11136253B1 (en) | 2020-03-18 | 2021-10-05 | Chio Kang Medical, Inc. | Microbiological treatment system for ethylene oxide exhaust gas |
US20210291105A1 (en) | 2020-03-19 | 2021-09-23 | Chio Kang Medical, Inc. | Ethylene Oxide Adsorption Tower and Recovery System, and Method for Recovering Ethylene Oxide |
WO2021184596A1 (en) * | 2020-03-19 | 2021-09-23 | Qiaokang Biotech (Guangdong) Co., LTD. | Ethylene oxide adsorption tower and recovery system, and method for recovering ethylene oxide |
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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: 20180109 |
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CF01 | Termination of patent right due to non-payment of annual fee |