CN111773873A - Ozone and waste gas integrated treatment equipment for molecular sieve production - Google Patents
Ozone and waste gas integrated treatment equipment for molecular sieve production Download PDFInfo
- Publication number
- CN111773873A CN111773873A CN202010538743.XA CN202010538743A CN111773873A CN 111773873 A CN111773873 A CN 111773873A CN 202010538743 A CN202010538743 A CN 202010538743A CN 111773873 A CN111773873 A CN 111773873A
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- tower
- waste gas
- pipeline
- ozone
- inlet pipe
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- 239000002912 waste gas Substances 0.000 title claims abstract description 66
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 29
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 21
- 239000007789 gas Substances 0.000 claims abstract description 61
- 238000001816 cooling Methods 0.000 claims abstract description 36
- 238000002485 combustion reaction Methods 0.000 claims abstract description 22
- 239000000428 dust Substances 0.000 claims abstract description 18
- 238000005507 spraying Methods 0.000 claims abstract description 7
- 239000004744 fabric Substances 0.000 claims abstract description 5
- 238000001179 sorption measurement Methods 0.000 claims description 39
- 230000001954 sterilising effect Effects 0.000 claims description 27
- 238000004659 sterilization and disinfection Methods 0.000 claims description 20
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 15
- 238000012423 maintenance Methods 0.000 claims description 14
- 239000007921 spray Substances 0.000 claims description 14
- 229910052799 carbon Inorganic materials 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 238000012546 transfer Methods 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000004321 preservation Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 abstract description 4
- 239000012535 impurity Substances 0.000 description 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000007539 photo-oxidation reaction Methods 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/007—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by irradiation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0423—Beds in columns
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
- F23G7/066—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/91—Bacteria; Microorganisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/804—UV light
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/14—Gaseous waste or fumes
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses ozone waste gas integrated treatment equipment for molecular sieve production, which comprises a waste gas combustion tower, wherein an ozone waste gas inlet pipe is connected to the outer part of the lower part of the waste gas combustion tower, a switching pipeline is arranged on the outer part of the upper part of the waste gas combustion tower, a waste gas heat preservation tower is connected to the outer part of the switching pipeline, a dispersing inlet pipe is connected to the lower part of the side edge of the waste gas heat preservation tower, a tail gas burner is connected to the outer part of the dispersing inlet pipe, a dust removal pipeline is connected to the outer part of the bottom end of a spraying cooling tower, a collecting top tower is connected to the outer end of the dust removal pipeline, a high-temperature cloth bag dust remover is installed at the bottom of the collecting top tower, a cleaning pipeline is connected between the collecting top tower and. This integrative treatment facility of ozone waste gas for molecular sieve production can be convenient handle molecular sieve ozone tail gas from the multiaspect, effectively improves the effect of tail gas treatment, makes the tail gas treatment effect optimize more.
Description
Technical Field
The invention relates to the technical field of molecular sieves, in particular to ozone and waste gas integrated treatment equipment for molecular sieve production.
Background
The molecular sieve is an artificially synthesized hydrated aluminosilicate (zeolite) or natural zeolite with the function of screening molecules, a large amount of ozone tail gas can be generated in the production process of the molecular sieve, and in order to reach the tail gas emission standard, the tail gas treatment work is required to ensure that the tail gas can reach the emission standard.
The tail gas treatment equipment for producing the existing molecular sieve has the advantages of simple treatment process, single treatment function, inconvenience in multi-direction treatment of molecular sieve ozone tail gas and the condition that the tail gas treatment effect needs to be improved.
Disclosure of Invention
The invention aims to provide ozone waste gas integrated treatment equipment for molecular sieve production, which solves the problem that tail gas treatment equipment for molecular sieve production, which is provided in the background art, is inconvenient to treat molecular sieve ozone tail gas in multiple directions.
In order to achieve the purpose, the invention provides the following technical scheme: an ozone waste gas integrated treatment device for molecular sieve production comprises a waste gas combustion tower, wherein an ozone waste gas inlet pipe is connected to the outer portion of the lower portion of the waste gas combustion tower, a switching pipeline is arranged on the outer portion of the upper portion of the waste gas combustion tower, a waste gas heat preservation tower is connected to the outer portion of the switching pipeline, a dispersing inlet pipe is connected to the lower portion of the side edge of the waste gas heat preservation tower, a tail gas burner is connected to the outer portion of the dispersing inlet pipe, a cooling pipeline is connected to the outer end of the tail gas burner, a spraying cooling tower is arranged on the outer portion of the cooling pipeline, a dust removal pipeline is connected to the outer end of the spraying cooling tower, a collecting top tower is connected to the outer end of the dust removal pipeline, a high-temperature cloth bag dust remover is arranged at the bottom of the collecting top tower, a cleaning pipeline is connected between the collecting top tower and, and back row pipeline outer end is connected with the adsorption tower that disinfects, ultraviolet sterilizer is installed to the inside top of adsorption tower that disinfects, and disinfects the inside below of adsorption tower and install the active carbon adsorption layer, the adsorption tower that disinfects side external connection has discharge pipe, and installs the fan on the discharge pipe.
Preferably, the waste gas combustion tower and the tail gas combustor are respectively connected with a primary heating gas inlet pipe and a secondary heating gas inlet pipe outside, and the top of the tail gas combustor is connected with an oxygen inlet pipe.
Preferably, the outer part of the bottom end of the sterilizing adsorption tower is connected with a sterilizing tower bracket, and a maintenance window is arranged on the outer part of the side edge of the sterilizing adsorption tower.
Preferably, the outside of the top end of the spraying cooling tower is connected with a water liquid inlet pipe, and the outside of the bottom end of the spraying cooling tower is provided with a cooling tower support.
Preferably, the maintenance window and the discharge pipeline are mutually staggered, and the height of the maintenance window and the height of the activated carbon adsorption layer correspond to each other.
Compared with the prior art, the invention has the beneficial effects that: this integrative treatment facility of ozone waste gas for molecular sieve production can be convenient handle molecular sieve ozone tail gas from the multiaspect, effectively improves the effect of tail gas treatment, makes the tail gas treatment effect optimize more. This integrative treatment facility of ozone waste gas for molecular sieve production can carry out combustion treatment to tail gas through the second grade heats, and can get rid of the impurity in the tail gas through light oxidation and active carbon adsorption's mode, improves tail gas treatment effect.
Drawings
FIG. 1 is a schematic structural diagram of a main view of an ozone-waste gas integrated treatment device for molecular sieve production according to the present invention;
FIG. 2 is a schematic view of the high-temperature bag-type dust collector of the ozone and waste gas integrated treatment device for molecular sieve production;
FIG. 3 is a schematic left view structural diagram of a sterilization adsorption tower of the ozone and waste gas integrated treatment equipment for molecular sieve production.
In the figure: 1. the waste gas combustion tower, 2, the switching pipeline, 3, the waste gas heat preservation tower, 4, the cleaning pipeline, 5, collect the top tower, 6, the high temperature sack cleaner, 7, the return line, 8, water liquid advances the pipe, 9, the back row pipeline, 10, the sterilization adsorption tower, 11, oxygen advances the pipe, 12, the fan, 13, ultraviolet sterilizer, 14, ultraviolet sterilizer, 15, ozone waste gas advances the pipe, 16, the first order gas that heats advances the pipe, 17, the dispersion advances the pipe, 18, the second order gas that heats advances the pipe, 19, the tail gas combustor, 20, the cooling pipeline, 21, the dust removal pipeline, 22, the spraying cooling tower, 23, the cooling tower support, 24, the active carbon adsorption layer, 25, the sterilization tower support, 26, the maintenance window.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-3, the present invention provides a technical solution: an ozone waste gas integrated treatment device for molecular sieve production comprises a waste gas combustion tower 1, an ozone waste gas inlet pipe 15 is connected to the outer portion of the lower portion of the waste gas combustion tower 1, a transfer pipeline 2 is installed on the outer portion of the upper portion of the waste gas combustion tower 1, a primary heating gas inlet pipe 16 and a secondary heating gas inlet pipe 18 are respectively connected to the outer portions of the waste gas combustion tower 1 and a tail gas combustor 19, an oxygen inlet pipe 11 is connected to the top of the tail gas combustor 19, natural gas can enter the waste gas combustion tower 1 and the tail gas combustor 19 through the primary heating gas inlet pipe 16 and the secondary heating gas inlet pipe 18 to provide combustion energy, the oxygen inlet pipe 11 can facilitate air to enter the tail gas combustor 19, a waste gas heat preservation tower 3 is connected to the outer portion of the transfer pipeline 2, a dispersion inlet pipe 17 is connected to the lower portion of the side edge of the waste gas heat preservation tower 3, and, the outer end of the tail gas combustor 19 is connected with a cooling pipeline 20, a spray cooling tower 22 is arranged outside the cooling pipeline 20, the top end of the spray cooling tower 22 is externally connected with a water liquid inlet pipe 8, a cooling tower support 23 is arranged outside the bottom end of the spray cooling tower 22, the cooling tower support 23 can support the spray cooling tower 22 to suspend a dust removal pipeline 21, cooling water liquid can enter the spray cooling tower 22 through the water liquid inlet pipe 8, the bottom end of the spray cooling tower 22 is externally connected with the dust removal pipeline 21, the outer end of the dust removal pipeline 21 is connected with a collecting top tower 5, a high-temperature cloth bag dust remover 6 is arranged at the bottom of the collecting top tower 5, a cleaning pipeline 4 is connected between the collecting top tower 5 and the waste gas heat preservation tower 3, a reflux pipeline 7 is connected between the bottom of the high-temperature cloth bag dust remover 6 and the spray cooling tower 22, and the outer end of the back row pipeline 9 is connected with a sterilization adsorption tower 10, the bottom of the sterilization adsorption tower 10 is externally connected with a sterilization tower bracket 25, and the side of the sterilization adsorption tower 10 is externally provided with a maintenance window 26, the structure enables the sterilization adsorption tower 10 to be supported by the sterilization tower bracket 25, the maintenance window 26 is positioned at the side position of the sterilization adsorption tower 10, the maintenance window 26 and the discharge pipeline 14 are mutually staggered, the height of the maintenance window 26 and the height of the active carbon adsorption layer 24 are mutually corresponding, the structure enables a user to replace the active carbon adsorption layer 24 through the maintenance window 26, the discharge pipeline 14 can not interfere the use of the maintenance window 26, the ultraviolet sterilizer 13 is arranged above the inside of the sterilization adsorption tower 10, the active carbon adsorption layer 24 is arranged below the inside of the sterilization adsorption tower 10, the side of the sterilization adsorption tower 10 is externally connected with the discharge pipeline 14, and the fan 12 is arranged on the discharge pipeline 14, this structure makes the ozone waste gas that the molecular sieve processing that gets into this equipment produced can carry out the second grade through waste gas burning tower 1 and tail gas combustor 19 and intensifies the burning, makes ozone waste gas can high temperature combustion processing impurity, and waste gas can reduce impurity content through photo-oxidation and active carbon adsorption, effectively improves the exhaust-gas treatment effect.
The working principle is as follows: when the ozone and waste gas integrated treatment equipment for molecular sieve production is used, firstly, a user can introduce ozone tail gas into a waste gas combustion tower 1 through an ozone and waste gas inlet pipe 15, then gas is added into the waste gas combustion tower 1 through a primary heating gas inlet pipe 16 to primarily raise the temperature of the tail gas in the waste gas combustion tower 1, then the heated gas is introduced into a waste gas heat-insulating tower 3 through a transfer pipeline 2 for heat insulation, at the moment, the waste gas in the waste gas heat-insulating tower 3 is introduced into a tail gas combustor 19 through a plurality of layers of dispersing inlet pipes 17, then gas and oxygen are introduced into the tail gas combustor 19 through a secondary heating gas inlet pipe 18 and an oxygen inlet pipe 11, so that the tail gas in the tail gas combustor 19 can be fully combusted and primarily treated, and then the tail gas to be subsequently treated in the tail gas combustor 19 enters the interior of a spray cooling tower 22 on a cooling tower support 23 through a cooling pipeline 20 to be cooled, the waste gas dust in spray cooling tower 22 and the waste gas heat preservation tower 3 can be respectively through dust removal pipeline 21 and during clean pipeline 4 gets into and collects top tower 5, then get into among the high temperature sack cleaner 6 and be handled, among the dustless waste gas of discharge can get into spray cooling tower 22 again through backflow pipeline 7 in the high temperature sack cleaner 6, then tail gas after the cooling can get into the sterilization adsorption tower 10 on the sterilization tower support 25 through back row pipeline 9 among, then tail gas is in proper order through ultraviolet sterilizer 13 and active carbon adsorption layer 24 by photo-oxidation and impurity adsorption, tail gas after the processing can be discharged through discharge tube 14 through fan 12 attraction, when the user needs to change active carbon adsorption layer 24, can open the maintenance window 26 of sterilization adsorption tower 10 side in order to change active carbon adsorption layer 24, thereby accomplish a series of work.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that various changes in the embodiments and/or modifications of the invention can be made, and equivalents and modifications of some features of the invention can be made without departing from the spirit and scope of the invention.
Claims (5)
1. The utility model provides an integrative treatment facility of ozone waste gas for molecular sieve production, includes waste gas burning tower (1), its characterized in that: the ozone waste gas collecting device is characterized in that an ozone waste gas inlet pipe (15) is connected to the outer portion of the lower portion of the waste gas combustion tower (1), a transfer pipeline (2) is installed on the outer portion of the upper portion of the waste gas combustion tower (1), a waste gas heat-insulating tower (3) is connected to the outer portion of the transfer pipeline (2), a dispersing inlet pipe (17) is connected to the lower portion of the side edge of the waste gas heat-insulating tower (3), a tail gas burner (19) is connected to the outer portion of the dispersing inlet pipe (17), a cooling pipeline (20) is connected to the outer end of the tail gas burner (19), a spraying cooling tower (22) is installed to the outer portion of the cooling pipeline (20), a dust removing pipeline (21) is connected to the outer end of the dust removing pipeline (21), a collecting top tower (5) is connected to the bottom of the collecting top tower (5), a high-temperature cloth bag dust remover, high temperature sack cleaner (6) bottom and spray and be connected with backflow pipeline (7) between cooling tower (22), and spray cooling tower (22) external connection have back row pipeline (9) to back row pipeline (9) outer end is connected with sterilization adsorption tower (10), ultraviolet sterilizer (13) are installed to sterilization adsorption tower (10) inside top, and just sterilization adsorption tower (10) inside below installs active carbon adsorption layer (24), sterilization adsorption tower (10) side external connection has emission pipeline (14), and installs fan (12) on emission pipeline (14).
2. The ozone and waste gas integrated treatment equipment for molecular sieve production according to claim 1, characterized in that: the waste gas combustion tower (1) and the tail gas combustor (19) are respectively connected with a primary heating gas inlet pipe (16) and a secondary heating gas inlet pipe (18) at the outer part, and the top of the tail gas combustor (19) is connected with an oxygen inlet pipe (11).
3. The ozone and waste gas integrated treatment equipment for molecular sieve production according to claim 1, characterized in that: the sterilizing adsorption tower is characterized in that a sterilizing tower support (25) is connected to the outer portion of the bottom end of the sterilizing adsorption tower (10), and a maintenance window (26) is installed on the outer portion of the side edge of the sterilizing adsorption tower (10).
4. The ozone and waste gas integrated treatment equipment for molecular sieve production according to claim 1, characterized in that: the top end of the spray cooling tower (22) is externally connected with a water liquid inlet pipe (8), and the bottom end of the spray cooling tower (22) is externally provided with a cooling tower support (23).
5. The ozone and waste gas integrated treatment equipment for molecular sieve production according to claim 3, characterized in that: the maintenance windows (26) and the discharge pipeline (14) are mutually staggered, and the heights of the maintenance windows (26) and the activated carbon adsorption layer (24) correspond to each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010538743.XA CN111773873A (en) | 2020-06-13 | 2020-06-13 | Ozone and waste gas integrated treatment equipment for molecular sieve production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010538743.XA CN111773873A (en) | 2020-06-13 | 2020-06-13 | Ozone and waste gas integrated treatment equipment for molecular sieve production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111773873A true CN111773873A (en) | 2020-10-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010538743.XA Pending CN111773873A (en) | 2020-06-13 | 2020-06-13 | Ozone and waste gas integrated treatment equipment for molecular sieve production |
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| Country | Link |
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| CN (1) | CN111773873A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112473932A (en) * | 2020-11-09 | 2021-03-12 | 朱应好 | Movable grading dust removal type complete set crusher set |
Citations (7)
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|---|---|---|---|---|
| JP2001182554A (en) * | 1999-12-22 | 2001-07-06 | Tokyo Metropolis | Waste gas ozone treatment system using gas turbine |
| US20140031584A1 (en) * | 2012-07-19 | 2014-01-30 | P2 Science, Inc. | Ozonolysis Operations for Generation of Reduced and/or Oxidized Product Streams |
| CN205717254U (en) * | 2016-04-29 | 2016-11-23 | 陈聪 | The high-efficiency environment friendly exhaust gas processing device that a kind of chemical plant is special |
| CN108031278A (en) * | 2017-10-25 | 2018-05-15 | 威洁（石狮）中水回用技术有限公司 | A kind of inorganization house exhaust processing unit and method |
| CN110404342A (en) * | 2019-08-29 | 2019-11-05 | 东华工程科技股份有限公司 | A kind of complete processing equipment of original position thermal desorption exhaust gas |
| CN110813368A (en) * | 2019-11-28 | 2020-02-21 | 上海绿强新材料有限公司 | A kind of preparation method of ozone decomposition catalyst in high-humidity exhaust gas |
| CN210584471U (en) * | 2019-02-20 | 2020-05-22 | 深圳科莱环保科技有限公司 | Ozone waste gas purifying equipment |
-
2020
- 2020-06-13 CN CN202010538743.XA patent/CN111773873A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001182554A (en) * | 1999-12-22 | 2001-07-06 | Tokyo Metropolis | Waste gas ozone treatment system using gas turbine |
| US20140031584A1 (en) * | 2012-07-19 | 2014-01-30 | P2 Science, Inc. | Ozonolysis Operations for Generation of Reduced and/or Oxidized Product Streams |
| CN205717254U (en) * | 2016-04-29 | 2016-11-23 | 陈聪 | The high-efficiency environment friendly exhaust gas processing device that a kind of chemical plant is special |
| CN108031278A (en) * | 2017-10-25 | 2018-05-15 | 威洁（石狮）中水回用技术有限公司 | A kind of inorganization house exhaust processing unit and method |
| CN210584471U (en) * | 2019-02-20 | 2020-05-22 | 深圳科莱环保科技有限公司 | Ozone waste gas purifying equipment |
| CN110404342A (en) * | 2019-08-29 | 2019-11-05 | 东华工程科技股份有限公司 | A kind of complete processing equipment of original position thermal desorption exhaust gas |
| CN110813368A (en) * | 2019-11-28 | 2020-02-21 | 上海绿强新材料有限公司 | A kind of preparation method of ozone decomposition catalyst in high-humidity exhaust gas |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112473932A (en) * | 2020-11-09 | 2021-03-12 | 朱应好 | Movable grading dust removal type complete set crusher set |
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