CN106178815A - A kind of ozonolysis equipment and method - Google Patents
A kind of ozonolysis equipment and method Download PDFInfo
- Publication number
- CN106178815A CN106178815A CN201610636302.7A CN201610636302A CN106178815A CN 106178815 A CN106178815 A CN 106178815A CN 201610636302 A CN201610636302 A CN 201610636302A CN 106178815 A CN106178815 A CN 106178815A
- Authority
- CN
- China
- Prior art keywords
- ozone
- muscovitum
- molecular sieve
- heat pipe
- electrothermal ring
- 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.)
- Withdrawn
Links
- 238000000034 method Methods 0.000 title claims abstract description 22
- 238000005949 ozonolysis reaction Methods 0.000 title claims abstract description 14
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 45
- 239000002808 molecular sieve Substances 0.000 claims abstract description 34
- 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 34
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 238000001179 sorption measurement Methods 0.000 claims abstract description 13
- 238000010521 absorption reaction Methods 0.000 claims abstract description 6
- 230000007797 corrosion Effects 0.000 claims description 3
- 238000005260 corrosion Methods 0.000 claims description 3
- 238000009413 insulation Methods 0.000 claims description 3
- 238000005728 strengthening Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 9
- 239000003570 air Substances 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 4
- 239000002912 waste gas Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 239000003463 adsorbent Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000001066 destructive effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010919 dye waste Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000013056 hazardous product Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
-
- 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
- B01D53/005—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 heat treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/10—Single element gases other than halogens
- B01D2257/106—Ozone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/65—Employing advanced heat integration, e.g. Pinch technology
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The invention discloses a kind of ozonolysis equipment and method, this device includes Muscovitum Electrothermal ring, molecular sieve, air inlet, gas outlet, power supply；Described Muscovitum Electrothermal ring adds heat pipe in including, inside add the left end of heat pipe be provided with air inlet, in add the right-hand member of heat pipe and be provided with gas outlet, be provided with termination bottom described Muscovitum heating collar, be used for connecting power supply；A kind of ozone decomposed method of the present invention is molecular sieve adsorption and heating synergy ozone decomposition, when ozone gas is by adding heat pipe in Muscovitum Electrothermal ring, strengthened ozone self by the molecular sieve adsorption in inner tube to decompose, Muscovitum Electrothermal ring is brought rapidly up heat resolve absorption ozone over a molecular sieve simultaneously, discharge from gas outlet after ozone decomposed, the absorption property of molecular sieve recovers, and can be continuing with.The present invention uses molecular sieve adsorption ozone to strengthen self decomposition, adds heat pipe simultaneously ozone carries out continuous high-efficient decomposition in utilizing Muscovitum Electrothermal ring, and safety is high, and service life is long.
Description
Technical field
The invention belongs to environmental technology field, be specifically related to ozonolysis equipment and method.
Background technology
Ozone is pollutant common in ambient air and room air.Owing to ozone has extremely strong oxidisability, so
Relatively broad application is all had at the aspect such as deodorizing sterilizing, decoloring dye waste water.In recent years due to promote the use of ozonateur,
Disinfect box and ozone purification disinfector etc., add the extensive application of laser printer, photocopier etc., and result in various degree is smelly
Oxygen leakage or electrion release ozone, thus exacerbate the further deterioration of room air situation.When indoor environment ozone is dense
Degree gradually accumulation reaches 0.2mg/m3Time above, human body will be produced harm, bring threat to human health.So, by waste gas
In ozone carry out resolution process so that it is it is very important for being decomposed into non-hazardous material.
Conventional ozone decomposed method has heat resolve method and adsorption-decomposition function method.Heat resolve method is to be currently used in elimination to remain
The most popular technology of after-odour oxygen, ozone gas i.e. starts thermal decomposition at 30 DEG C, during higher than 300 DEG C, reaches in 1 ~ 2s
100% decomposes, and heats frequently with single channel resistance, although this decomposition method has the biggest disposal ability, but is heated to 300
DEG C power consumption height, and has danger；Adsorption-decomposition function method refers to that ozone gas Molecular Adsorption is in the suction with the biggest specific surface area
On attached dose of surface, thus strengthen self destructive effect, but it is organic to carry some volatility often carried in the waste gas of ozone
Thing can be enriched in adsorbent surface, makes adsorbent inactivate, and weakens the decomposition of ozone.
Summary of the invention
For problem above, the invention provides the effective ozonolysis equipment of a kind of energy-saving safe, adsorption-decomposition function and
Method.
A kind of ozonolysis equipment of the present invention, including Muscovitum Electrothermal ring, molecular sieve, air inlet, gas outlet, power supply；
Described Muscovitum Electrothermal ring adds heat pipe in including, inside add the left end of heat pipe be provided with air inlet, in add the right-hand member of heat pipe and be provided with and give vent to anger
Mouthful, it is provided with termination bottom described Muscovitum heating collar, is used for connecting power supply；
The implementation method of the ozonolysis equipment of the present invention is molecular sieve adsorption and heating synergy ozone decomposition method, and it is concrete
It is embodied as: when ozone gas is by adding heat pipe in Muscovitum Electrothermal ring, ozone molecule is attached on the molecular sieve surface in inner tube
Strengthening self to decompose, Muscovitum Electrothermal ring is brought rapidly up to 150 DEG C of accelerated decomposition ozone simultaneously, arranges from gas outlet after ozone decomposed
Going out, the absorption property of molecular sieve recovers, and can be continuing with.
Preferably, described Muscovitum Electrothermal ring running voltage is 220V.
Preferably, described Muscovitum Electrothermal ring is with 0.3～0.5mm corrosion resistant plate as shell, middle with high insulation high-temperature-resistant
Micarex be core.
Preferably, described molecular sieve is 13X HP type, product type: 0.5～1.0mm or 1.6～2.5mm.
The technology of the present invention beneficial effect:
The molecular sieve adsorption that the present invention provides and heating synergy ozone decomposition apparatus and method, lower 30 minutes of molecular sieve room temperature
Reach saturated, within during heating 50 minutes, just reach fully saturated, heating delays molecular sieve saturation time, improve molecular sieve adsorption
Ability and ozone self destructive effect；Molecular sieve has a significant impact improving heat resolve effect, a molecular sieve adsorption part
Ozone, extends the ozone time of staying in adding heat pipe so that ozone has sufficient time endothermic decomposition；Absorption is over a molecular sieve
Ozone be heated fast decoupled, also make the timely activity recovery of molecular sieve, extend service life.
Accompanying drawing explanation
Fig. 1 is molecular sieve adsorption of the present invention and heating synergy ozone decomposition apparatus structure schematic diagram；
Wherein, 1, Muscovitum Electrothermal ring, 101, in add heat pipe, 102, termination, 2, molecular sieve, 3, air inlet, 4, gas outlet,
5, power supply.
Detailed description of the invention
For ease of skilled artisan understands that the present invention, in conjunction with Figure of description, technical solution of the present invention is done into one
The explanation of step.
As it is shown in figure 1, a kind of ozonolysis equipment, mainly include Muscovitum Electrothermal ring 1, molecular sieve 2, air inlet 3, give vent to anger
Mouth 4, power supply 5；Described Muscovitum Electrothermal ring adds heat pipe 101 in including, the left end inside adding heat pipe is provided with the right side of air inlet 3, inner tube
End is provided with gas outlet 4, is provided with termination 12, is used for connecting power supply 5 bottom described Muscovitum heating collar；
The implementation method of described ozonolysis equipment is molecular sieve adsorption and heating synergy ozone decomposition method, and it implements
For: when ozone gas is by adding heat pipe 101 in Muscovitum Electrothermal ring 1, ozone molecule adds the molecule in heat pipe 101 in being attached to
Sieving and strengthen self decomposition on 2 surfaces, Muscovitum Electrothermal ring 1 is brought rapidly up to 150 DEG C of accelerated decomposition ozone simultaneously, after ozone decomposed
Discharging from gas outlet 3, the absorption property of molecular sieve recovers, and can be continuing with.
Described Muscovitum Electrothermal ring running voltage is 220V；Described Muscovitum Electrothermal ring with 0.3～0.5mm corrosion resistant plate is
Shell, the middle micarex with high insulation high-temperature-resistant is as core；Described molecular sieve is 13X HP type, its product type: 0.5-
1.0mm or 1.6-2.5mm.
The present invention is molecular sieve adsorption and heating synergy ozone decomposition apparatus and method, when it is embodied as, carries
The waste gas of ozone adds in the air inlet 3 on the right side of heat pipe enters Muscovitum Electrothermal ring 1 in passing through and adds heat pipe 11, inside adds in heat pipe 11
13X HP type molecular sieve 2 adsorb the ozone in waste gas carry out self decompose, Muscovitum Electrothermal ring 1 is brought rapidly up to 150 simultaneously
DEG C degree is delayed the saturated of molecular sieve, and makes ozone be heated fast decoupled, and the adsorption activity of molecular sieve recovers in time, extends and makes
Use the life-span.
Invention is exemplarily described by the present invention above in conjunction with accompanying drawing, it is clear that the present invention implements not by upper
State the restriction of mode, as long as the various unsubstantialities improvement that the method design that have employed the present invention is carried out with technical scheme, all exist
Within protection scope of the present invention.
Claims (5)
1. an ozonolysis equipment, it is characterised in that include Muscovitum Electrothermal ring, molecular sieve, air inlet, gas outlet, power supply；
Described Muscovitum Electrothermal ring adds heat pipe in including, inside add the left end of heat pipe be provided with air inlet, in add the right-hand member of heat pipe and be provided with and give vent to anger
Mouthful, it is provided with termination bottom described Muscovitum heating collar, is used for connecting power supply.
The method of ozonolysis equipment the most according to claim 1 is molecular sieve adsorption and heating synergy ozone decomposition
Method, it is implemented as: when ozone gas is by adding heat pipe in Muscovitum Electrothermal ring, ozone molecule adds in heat pipe in being attached to
Strengthening self on molecular sieve surface to decompose, Muscovitum Electrothermal ring is brought rapidly up to 150 DEG C of accelerated decomposition ozone, ozone decomposed simultaneously
After discharge from gas outlet, the absorption property of molecular sieve recovers, and can be continuing with.
3. according to the ozonolysis equipment described in claim 1 and 2, it is characterised in that described Muscovitum Electrothermal ring running voltage
For 220V.
Ozonolysis equipment the most according to claim 1, it is characterised in that described Muscovitum Electrothermal ring is with 0.3～0.5mm
Corrosion resistant plate is shell, and the middle micarex with high insulation high-temperature-resistant is as core.
Ozonolysis equipment the most according to claim 1, it is characterised in that described molecular sieve is 13X HP type, it produces
Product model: 0.5～1.0mm or 1.6～2.5mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610636302.7A CN106178815A (en) | 2016-08-05 | 2016-08-05 | A kind of ozonolysis equipment and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610636302.7A CN106178815A (en) | 2016-08-05 | 2016-08-05 | A kind of ozonolysis equipment and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106178815A true CN106178815A (en) | 2016-12-07 |
Family
ID=57498430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610636302.7A Withdrawn CN106178815A (en) | 2016-08-05 | 2016-08-05 | A kind of ozonolysis equipment and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106178815A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018154609A1 (en) * | 2017-02-22 | 2018-08-30 | RAGANELLI, Valerio | Process for preserving perishable goods |
| CN109663458A (en) * | 2017-10-13 | 2019-04-23 | 天津市华赛尔气体有限公司 | A kind of gas absorption tower with thermal decomposition function |
| CN119345850A (en) * | 2024-11-05 | 2025-01-24 | 昆明理工大学 | A device for purifying ozone and recovering oxygen |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19608512A1 (en) * | 1996-03-05 | 1997-09-11 | Filterprodukte Gmbh Ab | Catalyst for purification of exhaust air, especially from kitchens |
| CN201040221Y (en) * | 2007-04-23 | 2008-03-26 | 李永明 | Full-effect air filter ozone decomposing machine |
| CN201260772Y (en) * | 2008-08-28 | 2009-06-24 | 淄博前沿医疗器械有限公司 | Constant temperature heating ozone catalytic decomposer |
| CN203170197U (en) * | 2013-01-14 | 2013-09-04 | 盐城朗润环保科技有限公司 | Ozone resistant electric heater |
| CN103920362A (en) * | 2014-04-22 | 2014-07-16 | 常州友达环保科技有限公司 | Exhaust gas treatment device and method by virtue of online desorption and degradation |
| CN204637985U (en) * | 2015-04-14 | 2015-09-16 | 第二炮兵工程设计研究院 | A kind of ozone tail gas decomposer |
| CN105333514A (en) * | 2014-08-12 | 2016-02-17 | 静域(上海)科技有限公司 | Dielectric barrier low-temperature plasma air purifier |
-
2016
- 2016-08-05 CN CN201610636302.7A patent/CN106178815A/en not_active Withdrawn
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19608512A1 (en) * | 1996-03-05 | 1997-09-11 | Filterprodukte Gmbh Ab | Catalyst for purification of exhaust air, especially from kitchens |
| CN201040221Y (en) * | 2007-04-23 | 2008-03-26 | 李永明 | Full-effect air filter ozone decomposing machine |
| CN201260772Y (en) * | 2008-08-28 | 2009-06-24 | 淄博前沿医疗器械有限公司 | Constant temperature heating ozone catalytic decomposer |
| CN203170197U (en) * | 2013-01-14 | 2013-09-04 | 盐城朗润环保科技有限公司 | Ozone resistant electric heater |
| CN103920362A (en) * | 2014-04-22 | 2014-07-16 | 常州友达环保科技有限公司 | Exhaust gas treatment device and method by virtue of online desorption and degradation |
| CN105333514A (en) * | 2014-08-12 | 2016-02-17 | 静域(上海)科技有限公司 | Dielectric barrier low-temperature plasma air purifier |
| CN204637985U (en) * | 2015-04-14 | 2015-09-16 | 第二炮兵工程设计研究院 | A kind of ozone tail gas decomposer |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018154609A1 (en) * | 2017-02-22 | 2018-08-30 | RAGANELLI, Valerio | Process for preserving perishable goods |
| CN109663458A (en) * | 2017-10-13 | 2019-04-23 | 天津市华赛尔气体有限公司 | A kind of gas absorption tower with thermal decomposition function |
| CN119345850A (en) * | 2024-11-05 | 2025-01-24 | 昆明理工大学 | A device for purifying ozone and recovering oxygen |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205042345U (en) | Waste gas treatment device | |
| CN106178815A (en) | A kind of ozonolysis equipment and method | |
| CN204734747U (en) | Medical degassing unit of efficient | |
| CN207221701U (en) | A kind of photooxidation catalytic waste gas processing unit | |
| CN104399352B (en) | Novel VOCs treatment equipment and treatment process | |
| CN106890563A (en) | A kind of efficient ozone remover | |
| CN206275404U (en) | A kind of household tableware intelligent disinfecting storage cabinet | |
| CN106267272A (en) | Remains defrosting decontaminating apparatus | |
| CN206121478U (en) | A treatment facility for VOCs waste gas | |
| CN210688257U (en) | Organic waste gas treatment device | |
| CN203231304U (en) | Animal harmless treatment incinerator | |
| CN203061059U (en) | Constant-temperature bent pipeline type ozone catalytic cracking device | |
| CN201260772Y (en) | Constant temperature heating ozone catalytic decomposer | |
| CN202892487U (en) | Air deodorization sterilizer | |
| CN206325378U (en) | A kind for the treatment of and purification device for VOC | |
| CN210292151U (en) | Household ozone disinfection machine | |
| CN207056250U (en) | A kind of chemical emission processing equipment | |
| CN116255702A (en) | Sterilization and deodorization equipment and sterilization and deodorization method | |
| CN216968100U (en) | Gluing equipment for furniture processing | |
| CN201093505Y (en) | Environment-friendly medical refuse incinerator | |
| CN207153360U (en) | A kind of waste gas purification apparatus | |
| CN202892478U (en) | Ozone disinfection device | |
| CN218392992U (en) | Kitchen pretreatment workshop deodorizer | |
| CN218900294U (en) | Pipeline sterilizing machine | |
| CN205698629U (en) | Air cleaner |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20161207 |
|
| WW01 | Invention patent application withdrawn after publication |