CN210674759U - Flue gas purification type waste heat recoverer - Google Patents
Flue gas purification type waste heat recoverer Download PDFInfo
- Publication number
- CN210674759U CN210674759U CN201921290258.4U CN201921290258U CN210674759U CN 210674759 U CN210674759 U CN 210674759U CN 201921290258 U CN201921290258 U CN 201921290258U CN 210674759 U CN210674759 U CN 210674759U
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- Prior art keywords
- pipe
- flue gas
- storehouse
- connecting box
- purification
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- Expired - Fee Related
Links
- 238000000746 purification Methods 0.000 title claims abstract description 68
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 55
- 239000003546 flue gas Substances 0.000 title claims abstract description 54
- 239000002918 waste heat Substances 0.000 title claims abstract description 28
- 238000003860 storage Methods 0.000 claims abstract description 36
- 239000000945 filler Substances 0.000 claims abstract description 29
- 239000007921 spray Substances 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 34
- 239000003814 drug Substances 0.000 claims description 11
- 230000026683 transduction Effects 0.000 claims description 11
- 238000010361 transduction Methods 0.000 claims description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 5
- 238000009826 distribution Methods 0.000 claims description 4
- 239000000919 ceramic Substances 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 13
- 238000006243 chemical reaction Methods 0.000 abstract description 12
- 230000005540 biological transmission Effects 0.000 abstract description 7
- 239000007789 gas Substances 0.000 abstract description 6
- 239000002440 industrial waste Substances 0.000 abstract description 4
- 238000004140 cleaning Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 230000008569 process Effects 0.000 description 8
- 238000011084 recovery Methods 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 239000000779 smoke Substances 0.000 description 5
- 238000002955 isolation Methods 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000008213 purified water Substances 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000006698 induction Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- DOBUSJIVSSJEDA-UHFFFAOYSA-L 1,3-dioxa-2$l^{6}-thia-4-mercuracyclobutane 2,2-dioxide Chemical compound [Hg+2].[O-]S([O-])(=O)=O DOBUSJIVSSJEDA-UHFFFAOYSA-L 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910000892 beryllide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910000370 mercury sulfate Inorganic materials 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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- Treating Waste Gases (AREA)
Abstract
The utility model relates to an industrial waste gas treatment technical field just discloses a flue gas purification formula waste heat recoverer, including reservoir and storage bucket, the right side fixed mounting in reservoir has the connecting box, the connecting pipe intercommunication is passed through with the left side of storage bucket in the right side of connecting box, the top fixed mounting of connecting box has the delivery pump, the top fixed mounting in reservoir has the left purification storehouse that is located the connecting box, the inside that purifies the storehouse is provided with the purification filler, the input of delivery pump and connecting box are through the conveyer pipe intercommunication that is located the connecting box right side, the output intercommunication of delivery pump has the right side that runs through the purification storehouse and extends to the spray line that purifies the filler top. This gas cleaning formula waste heat recoverer can accomplish preliminary purification treatment to the flue gas, avoids the flue gas to carry the heat and consumes complete back in transmission process, and the molecular activity descends and leads to reaction rate to reduce, and the reaction is incomplete, improves the follow-up treatment effect of flue gas and efficiency.
Description
Technical Field
The utility model relates to an industrial waste gas treatment technical field specifically is a flue gas purification formula waste heat recoverer.
Background
Industrial waste gas, which is a generic term for various pollutant-containing gases discharged into the air during the combustion and production processes of fuels in plant areas of enterprises, includes: carbon dioxide, carbon disulfide, hydrogen sulfide, fluoride, nitrogen oxide, chlorine, hydrogen chloride, carbon monoxide, plumbous mercury sulfate, beryllide, smoke and dust and productive dust, the atmosphere of discharging into, can the polluted air, these materials get into people's internal through different route respiratory tracts, some directly produce harm, some have the accumulation effect in addition, can be more serious harm people's health, different materials have different influence, industrial waste gas generally carries a large amount of heat energy, if carry out recycle to its heat energy of carrying, will reduce a large amount of energy losses.
Traditional waste heat recoverer is realizing flue gas waste heat recovery back, can't carry out preliminary purification treatment to the flue gas, and the flue gas follow-up treatment that leads to the heat to lose completely in the transmission process is troublesome, and the process is more complicated, and the treatment effect is relatively poor, so has proposed a flue gas purification formula waste heat recoverer and has solved the above-mentioned problem that proposes.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
The utility model provides a not enough to prior art, the utility model provides a flue gas purification formula waste heat recoverer possesses advantages such as flue gas preliminary purification, has solved traditional waste heat recoverer and after realizing flue gas waste heat recovery, can't carry out preliminary purification treatment to the flue gas, and the flue gas follow-up treatment that leads to the heat complete loss in the transmission process is troublesome, and the process is more complicated, the relatively poor problem of treatment effect.
(II) technical scheme
For the purpose of realizing the preliminary purification of the above-mentioned flue gas, the utility model provides a following technical scheme: a flue gas purification type waste heat recoverer comprises a water storage bin and a medicine storage barrel, wherein a connecting box is fixedly mounted on the right side of the water storage bin, the right side of the connecting box is communicated with the left side of the medicine storage barrel through a connecting pipe, a conveying pump is fixedly mounted at the top of the connecting box, a purification bin positioned on the left side of the connecting box is fixedly mounted at the top of the water storage bin, purification filler is arranged inside the purification bin, the input end of the conveying pump is communicated with the connecting box through a conveying pipe positioned on the right side of the connecting box, the output end of the conveying pump is communicated with a spray pipe penetrating through the right side of the purification bin and extending to the upper side of the purification filler, a spray head positioned inside the purification bin is fixedly mounted at the outer part of the spray pipe, a filter plate positioned above the spray head is fixedly mounted inside the purification bin, a discharge pipe is communicated with the top, the left side intercommunication in reservoir storehouse has the water changing pipe, the left side intercommunication in purification storehouse has the induction pipe that is located the overflow pipe top, the top fixed mounting in induction pipe has the transduction storehouse that is located the purification storehouse left, the top intercommunication in transduction storehouse has the intake pipe, the inside fixed mounting in transduction storehouse has quantity to be two division boards, the inside fixed mounting in transduction storehouse has the heat pipe that runs through two division boards, the outside of heat pipe all is provided with radiating fin.
Preferably, the bottom of the medicine storage barrel is provided with a support frame, and the outside of the connecting pipe is provided with a flow limiting valve.
Preferably, the purification filler is an activated carbon particle filler, a bearing plate positioned at the bottom of the purification filler is fixedly installed inside the purification bin, and small holes distributed densely are formed in the top of the bearing plate.
Preferably, the filter plate is covered with the filter plate that intensive pore is filled with the ceramic granule in the surface, the right side in water storage storehouse is seted up the intercommunication mouth.
Preferably, the outside of trading the water pipe is provided with the control valve, the connector has all been seted up to the left and right sides in transduction storehouse.
Preferably, the heat pipe is vertical setting, the heat pipe is equidistant array distribution, radiating fin is equidistant vertical intensive distribution.
(III) advantageous effects
Compared with the prior art, the utility model provides a flue gas purification formula waste heat recoverer possesses following beneficial effect:
the flue gas purification type waste heat recoverer comprises a water storage bin, a chemical storage barrel, a neutralizing agent, a preheating pipeline, a conveying pump, a filter plate, a heat exchange pipe, a preheating pipe, a heat conduction pipe, a partition plate, a heat dissipation fin, a preheating pipe, a spraying pipe, a spray nozzle, a spray pipe, a spray filler, a purification filler, a solution and a purification filler, wherein when the flue gas purification type waste heat recoverer is used, purified water is guided into the water storage bin through the water, and finally, the flue gas flows to the next procedure through the discharge pipe, so that after waste heat recovery is carried out on the flue gas, preliminary purification treatment can be completed on the flue gas, the situation that after the flue gas carries heat and is completely consumed in the transmission process, the reaction rate is reduced due to the reduction of molecular activity, the reaction is incomplete, and the subsequent treatment effect and efficiency of the flue gas are improved.
Drawings
FIG. 1 is a schematic structural view of the present invention;
fig. 2 is an enlarged schematic view of the structure at a position a of the present invention.
In the figure: 1 water storage bin, 2 medicine storage barrels, 3 connecting boxes, 4 connecting pipes, 5 delivery pumps, 6 purifying bins, 7 purifying fillers, 8 delivery pipes, 9 spraying pipes, 10 spray heads, 11 filter plates, 12 discharge pipes, 13 overflow pipes, 14 water changing pipes, 15 leading-in pipes, 16 energy conversion bins, 17 air inlet pipes, 18 isolation plates, 19 heat conducting pipes and 20 heat radiating fins.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-2, a flue gas purification type waste heat recovery device comprises a water storage tank 1 and a medicine storage barrel 2, wherein a connecting box 3 is fixedly installed on the right side of the water storage tank 1, the right side of the connecting box 3 is communicated with the left side of the medicine storage barrel 2 through a connecting pipe 4, a support frame is arranged at the bottom of the medicine storage barrel 2, a flow limiting valve is arranged outside the connecting pipe 4, a delivery pump 5 is fixedly installed on the top of the connecting box 3, the type of the delivery pump 5 can be 150-8, a purification bin 6 positioned on the left side of the connecting box 3 is fixedly installed on the top of the water storage tank 1, a purification filler 7 is arranged inside the purification bin 6, the purification filler 7 is an activated carbon particle filler, a bearing plate positioned at the bottom of the purification filler 7 is fixedly installed inside the purification bin 6, densely distributed small holes are arranged on the top of the bearing plate, the input end of the delivery, the output end of the delivery pump 5 is communicated with a spray pipe 9 which penetrates through the right side of the purification bin 6 and extends to the upper part of the purification filler 7, a spray head 10 positioned in the purification bin 6 is fixedly arranged outside the spray pipe 9, a filter plate 11 positioned above the spray head 10 is fixedly arranged inside the purification bin 6, the filter plate 11 is a filter plate with the surface covered with dense pores and the inside filled with ceramic particles, the right side of the water storage bin 1 is provided with a communication port, the top of the purification bin 6 is communicated with a discharge pipe 12, the left side of the bottom end of the purification bin 6 is communicated with an overflow pipe 13, the left side of the water storage bin 1 is communicated with a water exchange pipe 14, the left side of the purification bin 6 is communicated with an inlet pipe 15 positioned above the overflow pipe 13, the top of the inlet pipe 15 is fixedly provided with a transduction bin 16 positioned at the left side of the purification bin 6, the outside of the water exchange pipe 14 is, the energy conversion bin 16 is fixedly provided with two isolation plates 18, the energy conversion bin 16 is fixedly provided with heat conduction pipes 19 penetrating through the two isolation plates 18, the outside of each heat conduction pipe 19 is provided with a heat radiation fin 20, the heat conduction pipes 19 are vertically arranged, the heat conduction pipes 19 are distributed in an equidistant array, the heat radiation fins 20 are vertically and densely distributed in an equidistant manner, when in use, purified water is led into the water storage bin 1 through the water change pipe 14, the medicine storage bucket 2 adds a neutralizing agent into the connecting box 3, the left side and the right side of the energy conversion bin 16 are connected into a preheating pipeline, smoke carrying heat enters the heat conduction pipes 19 through the air inlet pipe 17, the isolation plates 18 isolate the smoke from air to be preheated, the smoke leads the heat out to preheat the air to be preheated through the heat radiation fins 20, and the smoke after heat conduction enters the purification bin 6 through the lead-in pipe 15, the solution after 5 through conveyer pipe 8 will connect 3 inside mixes of case passes through spray tube 9 and shower nozzle 10 and sprays the operation to the top of purifying filler 7, the flue gas passes and purifies filler 7, purify and block with the large granule by the solution that inside contains and purify filler 7, the solution is through purifying the inside that filler 7 got into water storage storehouse 1, the flue gas is carried out the fine particle that carries internally through filter 11 after the preliminary purification and is blocked once more, the flue gas flows through discharge pipe 12 to next process at last, make and carry out waste heat recovery back to the flue gas, can accomplish preliminary purification treatment to the flue gas, avoid the flue gas to carry the heat and consume completely the back in transmission process, molecular activity descends and leads to reaction rate to reduce, the reaction is incomplete, improve flue gas follow-up treatment effect and efficiency.
To sum up, when the flue gas purification type waste heat recoverer is used, purified water is led into the water storage bin 1 through the water changing pipe 14, a neutralizer is added into the connecting box 3 through the chemical storage barrel 2, the left side and the right side of the energy changing bin 16 are connected into a preheating pipeline, flue gas carrying heat enters the interior of the heat conducting pipe 19 through the air inlet pipe 17, the flue gas and air to be preheated are isolated through the isolating plate 18, the heat is led out through the heat radiating fins 20 to preheat the air to be preheated, the flue gas after heat conduction enters the purification bin 6 through the leading-in pipe 15, the mixed solution in the connecting box 3 is sprayed to the top of the purification filler 7 through the spraying pipe 9 and the spray head 10 by the delivery pump 5 through the delivery pipe 8, the flue gas passes through the purification filler 7, and is purified and blocked by the solution and the purification filler 7, and the solution enters the water storage bin 1 through the purification filler 7, the flue gas is carried out through filter 11 after tentatively purifying and is carried out the slight granule that carries internally and block once more, the flue gas flows through discharge pipe 12 next process at last, make carry out waste heat recovery back to the flue gas, can accomplish preliminary purification treatment to the flue gas, avoid the flue gas to carry the heat and consume completely the back in transmission process, molecular activity descends and leads to reaction rate to reduce, the reaction is incomplete, improve follow-up treatment effect and the efficiency of flue gas, traditional waste heat recoverer has been solved and after realizing flue gas waste heat recovery, can't carry out preliminary purification treatment to the flue gas, it is troublesome to lead to the flue gas follow-up treatment of heat complete loss in transmission process, the process is more complicated, the relatively poor problem of treatment effect.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a flue gas purification formula waste heat recoverer, includes water storage storehouse (1) and medicine storage barrel (2), its characterized in that: the right side of the water storage bin (1) is fixedly provided with a connecting box (3), the right side of the connecting box (3) is communicated with the left side of the medicine storage barrel (2) through a connecting pipe (4), the top of the connecting box (3) is fixedly provided with a conveying pump (5), the top of the water storage bin (1) is fixedly provided with a purifying bin (6) positioned on the left side of the connecting box (3), the purifying bin (6) is internally provided with a purifying filler (7), the input end of the conveying pump (5) is communicated with the connecting box (3) through a conveying pipe (8) positioned on the right side of the connecting box (3), the output end of the conveying pump (5) is communicated with a spray pipe (9) which penetrates through the right side of the purifying bin (6) and extends to the upper part of the purifying filler (7), the outer part of the spray pipe (9) is fixedly provided with a spray head (10) positioned in the purifying bin (6), the inner part of the purifying bin (6) is fixedly provided with a, the top intercommunication of purifying storehouse (6) has discharge pipe (12), the bottom left side intercommunication of purifying storehouse (6) has overflow pipe (13), the left side intercommunication of water storage storehouse (1) has water changing pipe (14), the left side intercommunication of purifying storehouse (6) has leading-in pipe (15) that are located overflow pipe (13) top, the top fixed mounting of leading-in pipe (15) has and is located purifying storehouse (6) left transduction storehouse (16), the top intercommunication of transduction storehouse (16) has intake pipe (17), the inside fixed mounting in transduction storehouse (16) has quantity to be division board (18) two, the inside fixed mounting in transduction storehouse (16) has heat pipe (19) that run through two division boards (18), the outside of heat pipe (19) all is provided with radiating fin (20).
2. The flue gas purification type waste heat recoverer according to claim 1, wherein: the bottom of the medicine storage barrel (2) is provided with a support frame, and the outside of the connecting pipe (4) is provided with a flow limiting valve.
3. The flue gas purification type waste heat recoverer according to claim 1, wherein: the purification filler (7) is an activated carbon particle filler, a bearing plate positioned at the bottom of the purification filler (7) is fixedly arranged in the purification bin (6), and small holes distributed densely are formed in the top of the bearing plate.
4. The flue gas purification type waste heat recoverer according to claim 1, wherein: the filter plate (11) is covered with the filter plate that intensive pore inside was filled with ceramic particle on the surface, the right side in water storage storehouse (1) is seted up the intercommunication mouth.
5. The flue gas purification type waste heat recoverer according to claim 1, wherein: the outside of trading water pipe (14) is provided with the control valve, the connector has all been seted up to the left and right sides in transduction storehouse (16).
6. The flue gas purification type waste heat recoverer according to claim 1, wherein: the heat pipe (19) is vertical, the heat pipe (19) is equidistant array distribution, and the radiating fins (20) are equidistant vertical intensive distribution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921290258.4U CN210674759U (en) | 2019-08-10 | 2019-08-10 | Flue gas purification type waste heat recoverer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921290258.4U CN210674759U (en) | 2019-08-10 | 2019-08-10 | Flue gas purification type waste heat recoverer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210674759U true CN210674759U (en) | 2020-06-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921290258.4U Expired - Fee Related CN210674759U (en) | 2019-08-10 | 2019-08-10 | Flue gas purification type waste heat recoverer |
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| Country | Link |
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| CN (1) | CN210674759U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111981497A (en) * | 2020-08-12 | 2020-11-24 | 甘肃富士特暖通科技有限公司 | Boiler energy-saving device |
| CN111992019A (en) * | 2020-08-31 | 2020-11-27 | 合肥江海智慧泵站数据科技有限责任公司 | Integration wisdom pump station deodorizing device |
-
2019
- 2019-08-10 CN CN201921290258.4U patent/CN210674759U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111981497A (en) * | 2020-08-12 | 2020-11-24 | 甘肃富士特暖通科技有限公司 | Boiler energy-saving device |
| CN111981497B (en) * | 2020-08-12 | 2022-09-13 | 甘肃富士特暖通科技有限公司 | Boiler energy-saving device |
| CN111992019A (en) * | 2020-08-31 | 2020-11-27 | 合肥江海智慧泵站数据科技有限责任公司 | Integration wisdom pump station deodorizing device |
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Address after: No. 118, Gaoyou Xinke Road, Yangzhou City, Jiangsu Province 225600 Patentee after: Yangzhou Zhongkang Technology Group Co.,Ltd. Address before: 225600 Xinke Road, Chengnan New Economic Zone, Gaoyou City, Yangzhou City, Jiangsu Province Patentee before: Yangzhou Zhongkang environmental protection equipment Co.,Ltd. |
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Effective date of registration: 20230727 Address after: No. 118-2, Xinke Road, Gaoyou South Economic New Area, Yangzhou City, Jiangsu Province 225605 Patentee after: Jiangsu Kangyuanfeng Equipment Technology Co.,Ltd. Address before: No. 118, Gaoyou Xinke Road, Yangzhou City, Jiangsu Province 225600 Patentee before: Yangzhou Zhongkang Technology Group Co.,Ltd. |
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