CN208660784U - Intelligent catalytic converter - Google Patents
Intelligent catalytic converter Download PDFInfo
- Publication number
- CN208660784U CN208660784U CN201821200164.9U CN201821200164U CN208660784U CN 208660784 U CN208660784 U CN 208660784U CN 201821200164 U CN201821200164 U CN 201821200164U CN 208660784 U CN208660784 U CN 208660784U
- Authority
- CN
- China
- Prior art keywords
- exhaust gas
- strainer
- area
- cabinet
- purifying area
- 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
Links
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 16
- 238000000746 purification Methods 0.000 claims abstract description 36
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000007539 photo-oxidation reaction Methods 0.000 claims abstract description 18
- 239000011490 mineral wool Substances 0.000 claims abstract description 17
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000000428 dust Substances 0.000 claims abstract description 8
- 238000001914 filtration Methods 0.000 claims abstract description 8
- 230000001954 sterilising effect Effects 0.000 claims abstract description 6
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 5
- 238000006243 chemical reaction Methods 0.000 claims abstract description 4
- 239000013618 particulate matter Substances 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 47
- 230000008859 change Effects 0.000 claims description 6
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 claims description 5
- 230000035807 sensation Effects 0.000 claims description 3
- 239000002912 waste gas Substances 0.000 claims description 3
- 238000000354 decomposition reaction Methods 0.000 claims description 2
- 238000005086 pumping Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 238000013461 design Methods 0.000 abstract description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 12
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 12
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 12
- 238000000034 method Methods 0.000 description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 239000001301 oxygen Substances 0.000 description 9
- 229910052760 oxygen Inorganic materials 0.000 description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 8
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 6
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 6
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 5
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 4
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- -1 sulphur hydrogen Chemical class 0.000 description 4
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 4
- 239000012855 volatile organic compound Substances 0.000 description 4
- 239000005864 Sulphur Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000002440 industrial waste Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 2
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 150000001345 alkine derivatives Chemical class 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000006385 ozonation reaction Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 150000003568 thioethers Chemical class 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000790917 Dioxys <bee> Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 238000011953 bioanalysis Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005367 electrostatic precipitation Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of intelligent catalytic converter, including cabinet, it is provided with a purification cavity in cabinet, the left side and right side front end of cabinet are fixedly installed several link plates;It is disposed with mineral wool strainer, pocket type strainer, ozone purification area, UV photooxidation purifying area and top purifying area from bottom to up in purification cavity, ozone purification is provided with ozonizer in area;UV ultraviolet lamp and ballast are provided in UV photooxidation purifying area;Drawer type strainer is provided in the purifying area of top;Diameter is greater than 15 microns of pollution particulate matter in mineral wool strainer filtering exhaust gas;The dust that diameter is 10 microns or more in pocket type strainer filtering exhaust gas, ozone purification area is to exhaust gas sterilizing;UV photooxidation purifying area is by exhaust gas conversion Cheng Shui and carbon dioxide;Drawer type strainer removes Litter remaining in removing exhaust gas.Above-mentioned technical proposal, it is reasonable in design, structure is simple, manufacturing cost is low, easy to maintain, production and operating cost is lower and good purification.
Description
Technical field
The utility model relates to purification technology fields, and in particular to a kind of intelligence catalytic converter.
Background technique
Industrial waste gas can be divided into dedusting, desulphurization denitration technology, organic exhaust gas VOC removal etc. according to the difference of pollutant,
For particulate pollutant particle size, industrial waste gas treating method mainly has dry method, four class of wet process, filtering and electrostatic, the most frequently used
Be exactly sack cleaner (filtering), cyclone dust collector (dry method), bubble dust collector (wet process) etc..It is wanted with to efficiency of dust collection
The raising asked, electrostatic precipitation also gradually begin to use.It is handled at present international and domestic for industrial waste gas, at organic exhaust gas
The method of reason mainly has physical method, chemical method, bioanalysis, including absorption, directly burning, catalysis burning, chemical oxidation, biological filter
The processing means such as pond.
China is directed to VOCs treatment technique at present and mainly has at this stage: isolation method, combustion method, absorption process, condensation method,
Plasma low-temperature catalytic oxidation, absorption method etc..Existing waste gas treatment equipment is relatively more, and most for the treatment of effect is not
It is good, although have beginning when high treating effect, using a period of time, treatment effect just substantially reduced, and some device structures are multiple
It is miscellaneous, equipment volume is big, cost is high, maintenance is frequent, production and operating cost is higher, the practicability is poor, more difficult popularization.
Utility model content
In view of the deficienciess of the prior art, the purpose of this utility model is to provide a kind of reasonable in design, structures
Simply, manufacturing cost is low, easy to maintain, production and operating cost is lower and the intelligent catalytic converter of good purification.
To achieve the above object, the utility model provides following technical solution: a kind of intelligence catalytic converter, including case
Body is provided with a purification cavity in the cabinet, and the cabinet lower end is provided with an exhaust gas inlet, the left end of the cabinet
Face and right side front end are fixedly installed several link plates;Mineral wool filter is disposed in the purification cavity from bottom to up
Net, pocket type strainer, ozone purification area, UV photooxidation purifying area and top purifying area are provided with ozonizer in the ozone purification area;
UV ultraviolet lamp and ballast are provided in the UV photooxidation purifying area;Drawer type strainer is provided in the top purifying area;Institute
State the pollution particulate matter that diameter in mineral wool strainer filtering exhaust gas is greater than 15 microns;Diameter is in the pocket type strainer filtering exhaust gas
10 microns or more of dust, the ozone purification area is to exhaust gas sterilizing, and stench or change foul gas in waste gas decomposition;
The UV photooxidation purifying area removes the peculiar smell in gas, and by exhaust gas conversion Cheng Shui and carbon dioxide;The removal of drawer type strainer is useless
Remaining Litter in gas.
The utility model is further arranged to: six roots of sensation ozonizer, and every ozonizer is arranged in the ozone purification area altogether
Diameter be 45mm, length 150mm.
The utility model is further arranged to: eight UV ultraviolet lamps and eight towns are arranged in the UV photooxidation purifying area altogether
Device is flowed, the diameter of every UV ultraviolet lamp is 15mm, length 970mm, power 80w;The power of every ballast is 150w.
The utility model is further arranged to: the length of the drawer type strainer of the top purifying area is 1186mm, wide
Degree is 1060mm, is highly 20mm.
The utility model is further arranged to: two filter bags are at least set on the pocket type strainer, and each filter bag
Length is 1280mm, width 410mm, is highly 20mm.
The utility model is further arranged to: two filter bags are at least set on the pocket type strainer, and each filter bag
Length is 1280mm, width 410mm, is highly 20mm.
The utility model is further arranged to: the length of the mineral wool strainer is 1060mm, width 593mm, height
Degree is 20mm.
The utility model is further arranged to: the mineral wool strainer and pocket type strainer detachably connect with cabinet respectively
It connects;The cabinet is located at top purifying area top position and is provided with bellows, is provided with blower in the bellows, is incited somebody to action by blower
Cabinet is discharged in gas after filter.
The utility model is further arranged to: case lid is provided on before the cabinet, the case lid passes through pin shaft
It is constituted with the link plate of alignment hinged.
The utility model has the advantages that: compared with prior art, the utility model structure setting is more reasonable, and exhaust gas is from useless
Gas import is greater than 15 microns of pollution particulate matters by mineral wool strainer removal diameter, then removes 10 microns or more powder by filter bag
Dirt, the exhaust gas after initial filter regional processing flow to next purge segment-ozone purification area, and multiple groups are installed in ozone purification area
High energy ozone generator tube, decompose stench, change foul gas such as: ammonia, trimethylamine, hydrogen sulfide, first sulphur hydrogen, methyl mercaptan, methyl sulfide,
Methyl disulfide, carbon disulfide and styrene, sulfide H2S, VOC class, benzene homologues, benzene,toluene,xylene, styrene, acetone,
Butanone, ethyl acetate, formaldehyde, acetaldehyde, ethyl acetate, styrene, alkane, alkene, alkynes, aromatic hydrocarbon, phenol, hydrogen sulfide, mercaptan,
The molecular chain structure of thioether, ammonia, while playing the role of sterilizing;Treated gas is then sent through UV photooxidation purifying area,
It is irradiated using UV ultraviolet beam, changes the molecular structure of gas, high-molecular compound is made to be degraded into low molecular compound, UV is purple
Outer Line beam can effectively decompose the oxygen molecule in air and generate free oxygen, i.e. active oxygen, because the taken positron-electron of free oxygen is uneven
Weighing apparatus thus need to oxygen molecule ining conjunction with, and then generation special wavelength ozone, UV+O2 → O+O (active oxygen), O+O2 → O3 is (smelly
Oxygen), Pre-Ozonation on Organic Matter has extremely strong oxidation, has very strong scavenging effect to peculiar smell, converts it into water and dioxy
Change carbon;Enter the drawer type strainer in high-efficient purification area by pretreated exhaust gas, drawer type strainer filters out remaining Litter, row
Release clean air.It is reasonable in design, structure is simple, manufacturing cost is low, it is easy to maintain, production and operating cost it is lower and
Good purification.
The utility model is described in further detail with specific embodiment with reference to the accompanying drawings of the specification.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model embodiment;
Fig. 2 is the structural schematic diagram of the utility model embodiment cabinet;
Fig. 3 is the structural schematic diagram of the utility model embodiment part.
Specific embodiment
Referring to figure 1, figure 2 and figure 3, a kind of intelligent catalytic converter disclosed by the utility model, including cabinet 1, the case
A purification cavity 11 is provided in body 1,1 lower end of cabinet is provided with an exhaust gas inlet 12, the left side of the cabinet 1
Several link plates 2 are fixedly installed with right side front end;It is disposed with mineral wool from bottom to up in the purification cavity 11
Strainer 3, pocket type strainer 4, ozone purification area 13, UV photooxidation purifying area 14 and top purifying area 15, in the ozone purification area 13
It is provided with ozonizer 5;UV ultraviolet lamp 6 and ballast 7 are provided in the UV photooxidation purifying area 14;In the top purifying area 15
It is provided with drawer type strainer 8;The mineral wool strainer 3 filters the pollution particulate matter that diameter in exhaust gas is greater than 15 microns;The bag
Formula strainer 4 filters the dust that diameter is 10 microns or more in exhaust gas, and the ozone purification area 13 decomposes exhaust gas sterilizing
Stench or change foul gas in exhaust gas;The UV photooxidation purifying area 14 removes the peculiar smell in gas, and by exhaust gas conversion Cheng Shui
And carbon dioxide;Drawer type strainer 8 removes Litter remaining in removing exhaust gas.
Preferably, the quantity of the link plate 2 is at least arranged two, and each link plate 2 passes through existing screw
It is connected and fixed with the left side of cabinet 1 or right side front end;The mineral wool strainer 3 and 8 left and right ends of drawer type strainer cover
Equipped with existing directive slide track, each directive slide track passes through existing screw and is connected and fixed;It is arranged on pocket type strainer 4 existing
Locating rack, pocket type strainer 4 by locating rack and purification cavity 11 inner wall be connected by screw to fixation;Every ozonizer 5
It is threadedly coupled with existing attachment base in ozone purification area 13;Every UV ultraviolet lamp 6 with it is existing in UV photooxidation purifying area 14
Lamp holder be threadedly coupled and fix, every ballast 7 is connected and fixed by existing screw.
To keep the utility model structure setting more reasonable, preferably, in ozone purification area 13 described in the present embodiment
Six roots of sensation ozonizer 5 is set altogether, and the diameter of every ozonizer 5 is 45mm, length 150mm.
Eight UV ultraviolet lamps 6 and eight ballasts 7 are set altogether in the UV photooxidation purifying area 14, every UV ultraviolet lamp 6
Diameter is 15mm, length 970mm, power 80w;The power of every ballast 7 is 150w.
The length of the drawer type strainer 8 of the top purifying area 15 is 1186mm, width 1060mm, is highly 20mm.
Two filter bags are at least set on the pocket type strainer 4, and the length of each filter bag is 1280mm, width 410mm,
Height is 20mm.
The length of the mineral wool strainer 3 is 1060mm, width 593mm, is highly 20mm.
The mineral wool strainer 3 and pocket type strainer 4 are detachably connected with cabinet 1 respectively;The cabinet 1 is located at top purification
15 top position of area is provided with bellows 16, is provided with blower in the bellows 16, and case is discharged in filtered gas by blower
Body 1.
Case lid 9 is provided on before the cabinet 1, the case lid 9 is made up of pin shaft and the link plate 2 of alignment and cuts with scissors
It connects.
When practical application, exhaust gas is greater than 15 microns of pollution particulate matters by mineral wool strainer removal diameter from exhaust gas inlet,
10 microns or more dust, the exhaust gas after initial filter regional processing are removed by filter bag again and flow to next purge segment-ozone
Multiple groups high energy ozone generator tube is installed in purifying area, ozone purification area, is decomposed stench, is changed foul gas such as: ammonia, trimethylamine, sulphur
Change hydrogen, first sulphur hydrogen, methyl mercaptan, methyl sulfide, methyl disulfide, carbon disulfide and styrene, sulfide H2S, VOC class, benzene homologues,
Benzene,toluene,xylene, styrene, acetone, butanone, ethyl acetate, formaldehyde, acetaldehyde, ethyl acetate, styrene, alkane, alkene,
Alkynes, aromatic hydrocarbon, phenol, hydrogen sulfide, mercaptan, thioether, ammonia molecular chain structure, while playing the role of sterilizing;By place
The gas of reason is then sent through UV photooxidation purifying area, is irradiated using UV ultraviolet beam, changes the molecular structure of gas, make producing high-molecular
It closes object and is degraded into low molecular compound, UV ultraviolet beam can effectively decompose the oxygen molecule in air and generate free oxygen, i.e., active
Oxygen, so need to be in conjunction with oxygen molecule because of the taken positron-electron imbalance of free oxygen, and then generates the ozone of special wavelength, UV+O2
→ O+O (active oxygen), O+O2 → O3 (ozone), Pre-Ozonation on Organic Matter have extremely strong oxidation, have to peculiar smell very strong clear
Except effect, water and carbon dioxide are converted it into;Enter the drawer type strainer in high-efficient purification area, drawer by pretreated exhaust gas
Formula strainer filters out remaining Litter, gives off clean air.It is reasonable in design, structure is simple, manufacturing cost is low, maintenance
Convenient, production and operating cost is lower and good purification.
Above-described embodiment is served only for that the utility model is further described, no to the specific descriptions of the utility model
It can be interpreted as the restriction to scope of protection of the utility model, the technician of this field is according to the content pair of above-mentioned utility model
The utility model is made some nonessential modifications and adaptations and is each fallen within the protection scope of the utility model.
Claims (8)
1. a kind of intelligence catalytic converter, including cabinet (1), the cabinet (1) is interior to be provided with a purification cavity (11), described
Cabinet (1) lower end is provided with an exhaust gas inlet (12), it is characterised in that: the left side and right side front end of the cabinet (1)
It is fixedly installed several link plates (2);Be disposed in the purification cavity (11) from bottom to up mineral wool strainer (3),
Pocket type strainer (4), ozone purification area (13), UV photooxidation purifying area (14) and top purifying area (15), the ozone purification area
(13) ozonizer (5) are provided in;UV ultraviolet lamp (6) and ballast (7) are provided in the UV photooxidation purifying area (14);It is described
Drawer type strainer (8) are provided in top purifying area (15);Diameter is greater than 15 microns in mineral wool strainer (3) the filtering exhaust gas
Pollution particulate matter;The dust that diameter is 10 microns or more in pocket type strainer (4) the filtering exhaust gas, the ozone purification area
(13) to exhaust gas sterilizing, and stench or change foul gas in waste gas decomposition;The UV photooxidation purifying area (14) removes gas
Peculiar smell in body, and by exhaust gas conversion Cheng Shui and carbon dioxide;Drawer type strainer (8) removes Litter remaining in removing exhaust gas.
2. a kind of intelligent catalytic converter according to claim 1, it is characterised in that: in the ozone purification area (13) altogether
It is arranged six roots of sensation ozonizer (5), and the diameter of every ozonizer (5) is 45mm, length 150mm.
3. a kind of intelligent catalytic converter according to claim 2, it is characterised in that: in the UV photooxidation purifying area (14)
Eight UV ultraviolet lamps (6) and eight ballasts (7) are set altogether, the diameter of every UV ultraviolet lamp (6) is 15mm, length 970mm,
Power is 80w;The power of every ballast (7) is 150w.
4. a kind of intelligent catalytic converter according to claim 3, it is characterised in that: the pumping of the top purifying area (15)
The length of drawer formula strainer (8) is 1186mm, width 1060mm, is highly 20mm.
5. a kind of intelligent catalytic converter according to claim 4, it is characterised in that: on the pocket type strainer (4) at least
Two filter bags are set, and the length of each filter bag is 1280mm, width 410mm, is highly 20mm.
6. a kind of intelligent catalytic converter according to claim 5, it is characterised in that: the length of the mineral wool strainer (3)
Degree is 1060mm, width 593mm, is highly 20mm.
7. a kind of intelligent catalytic converter according to claim 1 or 6, it is characterised in that: the mineral wool strainer (3) and
Pocket type strainer (4) is detachably connected with cabinet (1) respectively;The cabinet (1) is located at the setting of top purifying area (15) top position
Have bellows (16), be provided with blower in the bellows (16), filtered gas is discharged by cabinet (1) by blower.
8. a kind of intelligent catalytic converter according to claim 1, it is characterised in that: set on before the cabinet (1)
It is equipped with case lid (9), the case lid (9) is made up of hinged pin shaft and the link plate (2) of alignment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201821200164.9U CN208660784U (en) | 2018-07-27 | 2018-07-27 | Intelligent catalytic converter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821200164.9U CN208660784U (en) | 2018-07-27 | 2018-07-27 | Intelligent catalytic converter |
Publications (1)
Publication Number | Publication Date |
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CN208660784U true CN208660784U (en) | 2019-03-29 |
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Family Applications (1)
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CN201821200164.9U Active CN208660784U (en) | 2018-07-27 | 2018-07-27 | Intelligent catalytic converter |
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CN (1) | CN208660784U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108654344A (en) * | 2018-07-27 | 2018-10-16 | 江向前 | Intelligent catalytic converter |
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2018
- 2018-07-27 CN CN201821200164.9U patent/CN208660784U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN108654344A (en) * | 2018-07-27 | 2018-10-16 | 江向前 | Intelligent catalytic converter |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20190606 Address after: Room 1495, 518 Shuangdian Road, Huinan Town, Pudong New Area, Shanghai, 201399 Patentee after: Shanghai Qianchuang Environmental Protection Technology Co., Ltd. Address before: 325000 Liule Road 322, Liushi Town, Yueqing City, Wenzhou City, Zhejiang Province Patentee before: Jiang Xiangqian |
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TR01 | Transfer of patent right |