CN107497185A - A kind of air purification method of temperature reaction processing - Google Patents
A kind of air purification method of temperature reaction processing Download PDFInfo
- Publication number
- CN107497185A CN107497185A CN201710635025.2A CN201710635025A CN107497185A CN 107497185 A CN107497185 A CN 107497185A CN 201710635025 A CN201710635025 A CN 201710635025A CN 107497185 A CN107497185 A CN 107497185A
- Authority
- CN
- China
- Prior art keywords
- air
- purification
- compression
- sent
- compressor
- 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.)
- Pending
Links
- 238000004887 air purification Methods 0.000 title claims abstract description 9
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 8
- 238000000746 purification Methods 0.000 claims abstract description 22
- 238000007906 compression Methods 0.000 claims abstract description 19
- 239000003054 catalyst Substances 0.000 claims abstract description 16
- 230000003197 catalytic Effects 0.000 claims abstract description 11
- 238000001816 cooling Methods 0.000 claims abstract description 11
- 239000000126 substance Substances 0.000 claims abstract description 11
- 238000004140 cleaning Methods 0.000 claims abstract description 10
- 238000001914 filtration Methods 0.000 claims abstract description 5
- 230000000630 rising Effects 0.000 claims abstract description 5
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000004781 supercooling Methods 0.000 claims 1
- 239000003344 environmental pollutant Substances 0.000 abstract description 3
- 231100000719 pollutant Toxicity 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 230000001699 photocatalysis Effects 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitrogen oxide Substances O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N AI2O3 Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 208000008425 Protein Deficiency Diseases 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000024881 catalytic activity Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000001808 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative Effects 0.000 description 1
- 230000003694 hair properties Effects 0.000 description 1
- 229910052813 nitrogen oxide Inorganic materials 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 230000001473 noxious Effects 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 230000002000 scavenging Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 230000002269 spontaneous Effects 0.000 description 1
- 235000010215 titanium dioxide Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- 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
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/28—Arrangement or mounting of filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/30—Arrangement or mounting of heat-exchangers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
- F24F5/001—Compression cycle type
-
- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/54—Free-cooling systems
Abstract
A kind of air purification method of temperature reaction processing, as follows：Air to be clean is filtered using filter, the air after filtering is sent into compressor and carries out adiabatic compression, the air to be clean makes atmosphere temperature rising to the active temperature of subsequent catalyst reacting middle catalyst after compressor adiabatic compression；Air after compression enters catalytic cleaner, and the harmful substance in air changes into harmless gas in the presence of catalyst；Purification air after catalytic cleaner is handled is subjected to heat exchange cooling by cooling heat exchanger；The purification air after heat exchange is sent into expanding machine afterwards and carries out adiabatic expansion, is depressured air cooling-down；Purification air Jing Guo adiabatic expansion is sent into damping equipment, the humidity of regulation purification air.The present invention can effectively remove the pollutant in air；Energy consumption can be significantly reduced.
Description
Technical field
The present invention relates to technical field of air purification, more particularly to a kind of air purification method of temperature reaction processing.
Background technology
In order to save the energy, the increase of modern architecture closure degree, due to its central air conditioner system scavenging utilities imperfection,
Cause indoor pollutant to discharge outdoor in time, cause IAQ to deteriorate.At present, the indoor air cleaning typically used
Change technology is usually：（1）Filtration method, this method can only filter out bulky grain thing in air, and can not remove waving in air
The harmful substances such as hair property organic matter, nitrogen oxides, oxysulfide, carbon monoxide；（2）Absorption method, this method is mainly using porous
Property sorbing material such as porous silica, activated carbon, activated alumina, ceramics or zeolite remove the noxious substance in air
Go, but this method needs different sorbing materials generally directed to different harmful substances, therefore to realize room truly
Interior air comprehensive decontamination difficulty is larger, although acticarbon can adsorb most harmful substance, due to its adsorbance
Limited, adsorbent needs frequent regeneration, particularly activated carbon to have the possibility of spontaneous combustion in more than 573K, is caused to regeneration sizable
Difficulty, limit its application.（3）Photocatalytic oxidation, this method are the photocatalytic activities using catalyst, are urging absorption
Redox reaction occurs for the VOCs for changing dielectric surface, is eventually converted into carbon dioxide, water and inorganic molecules material, due to
Cheap two wide material sources of TiO2, high to uv absorption rate, anti-light corrosivity, chemical stability and catalytic activity are high, and
There is no toxicity, have stronger suction-operated to many organic matters, thus turn into the most frequently used photochemical catalyst, the master of photocatalytic oxidation
Wanting advantage is：Capacity usage ratio is high, is generally operated at normal temperatures, no coupling product is formed, and the catalyst after use can be used
Physics and chemical method regeneration Posterior circle use, but this method can only degrade volatile organic matter, can not go denitrification and
The harmful substances such as oxysulfide.
Air treating in the market substantially can not fully and effectively purify the pollution in air with purification techniques
Thing, reach the requirement of Indoor Air Quality standards comprehensively, it would be highly desirable to which exploitation can effectively administer the method to purify the air of a room comprehensively.
The content of the invention
Present invention aim to address above-mentioned deficiency, there is provided a kind of air purification method of temperature reaction processing.
The present invention technical solution be：A kind of air purification method of temperature reaction processing, as follows：It will treat
Purification air is filtered using filter, removes the coarseparticulate in air, and the air after filtering is sent into compressor
Row adiabatic compression, the air to be clean make atmosphere temperature rising to subsequent catalyst reacting middle catalyst after compressor adiabatic compression
Active temperature, wherein compression heating after air themperature be 50-400 DEG C, volume compression ratio 3-6；Air after compression enters
Enter catalytic cleaner, the harmful substance in air changes into harmless gas in the presence of catalyst；It will pass through at catalytic cleaner
Purification air after reason carries out heat exchange cooling by cooling heat exchanger；The purification air after heat exchange is sent into expanding machine afterwards to carry out
Adiabatic expansion, air cooling-down is depressured, suitable for conveying, and the expanding machine adiabatic expansion is done work and is conveyed to the step
A) compressor in；Purification air Jing Guo adiabatic expansion is sent into damping equipment, the humidity of regulation purification air.
In the step c), the purification air after catalytic cleaner is handled is passed through in cooling heat exchanger and step a)
Air heat-exchange to be clean cooling.
The present invention has the following advantages：Atmosphere temperature rising is made to the active temperature of catalyst, the party using compressor adiabatic compression
Method is simple and easy, easy to operate, can effectively remove the pollutant in air；, will using expanding machine to the air cooling-down after purification
The expansion work of expanding machine is conveyed to compressor, for compressor operating, can significantly reduce energy consumption.
Embodiment
A kind of air purification method of temperature reaction processing of the present invention, as follows：Air to be clean is adopted
Filtered with filter, remove the coarseparticulate in air, the air after filtering is sent into compressor and carries out adiabatic compression,
The air to be clean makes atmosphere temperature rising to the active temperature of subsequent catalyst reacting middle catalyst after compressor adiabatic compression,
Air themperature wherein after compression heating is 50-400 DEG C, volume compression ratio 3-6；Air after compression enters catalytic purification
Device, the harmful substance in air change into harmless gas in the presence of catalyst；By the purification after catalytic cleaner is handled
Air carries out heat exchange cooling by cooling heat exchanger；The purification air after heat exchange is sent into expanding machine afterwards and carries out adiabatic expansion,
Air cooling-down is depressured, suitable for conveying, and the pressure being conveyed in the step a) that the expanding machine adiabatic expansion is done work
Contracting machine；Purification air Jing Guo adiabatic expansion is sent into damping equipment, the humidity of regulation purification air.
In the step c), the purification air after catalytic cleaner is handled is passed through in cooling heat exchanger and step a)
Air heat-exchange to be clean cooling.
Claims (1)
- A kind of 1. air purification method of temperature reaction processing, it is characterised in that：As follows：Air to be clean was used Filter is filtered, and removes the coarseparticulate in air, and the air after filtering is sent into compressor and carries out adiabatic compression, described Air to be clean makes atmosphere temperature rising to the active temperature of subsequent catalyst reacting middle catalyst after compressor adiabatic compression, wherein Air themperature after compression heating is 50-400 DEG C, volume compression ratio 3-6；Air after compression enters catalytic cleaner, empty Harmful substance in gas changes into harmless gas in the presence of catalyst；Purification air after catalytic cleaner is handled is led to Supercooling heat exchanger carries out heat exchange cooling；The purification air after heat exchange is sent into expanding machine afterwards and carries out adiabatic expansion, makes air Decrease temperature and pressure, suitable for conveying, and the compressor being conveyed in the step a) that the expanding machine adiabatic expansion is done work；Will Purification air by adiabatic expansion is sent into damping equipment, the humidity of regulation purification air.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710635025.2A CN107497185A (en) | 2017-07-30 | 2017-07-30 | A kind of air purification method of temperature reaction processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710635025.2A CN107497185A (en) | 2017-07-30 | 2017-07-30 | A kind of air purification method of temperature reaction processing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107497185A true CN107497185A (en) | 2017-12-22 |
Family
ID=60689853
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710635025.2A Pending CN107497185A (en) | 2017-07-30 | 2017-07-30 | A kind of air purification method of temperature reaction processing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107497185A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109520697A (en) * | 2018-11-09 | 2019-03-26 | 天津航空机电有限公司 | A kind of pilot system for simulating aircraft engine nacelle low temperature air inlet |
| CN110152444A (en) * | 2018-02-07 | 2019-08-23 | 彭万喜 | A method of pernicious gas is handled using high-efficiency adsorbent |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102974215A (en) * | 2012-12-28 | 2013-03-20 | 华微科技（苏州）有限公司 | Air purification method |
| CN203030189U (en) * | 2012-12-28 | 2013-07-03 | 华微科技（苏州）有限公司 | Air purification device |
| CN106765539A (en) * | 2016-11-09 | 2017-05-31 | 重庆睿容环保科技有限公司 | A kind of air purification method |
-
2017
- 2017-07-30 CN CN201710635025.2A patent/CN107497185A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102974215A (en) * | 2012-12-28 | 2013-03-20 | 华微科技（苏州）有限公司 | Air purification method |
| CN203030189U (en) * | 2012-12-28 | 2013-07-03 | 华微科技（苏州）有限公司 | Air purification device |
| CN106765539A (en) * | 2016-11-09 | 2017-05-31 | 重庆睿容环保科技有限公司 | A kind of air purification method |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110152444A (en) * | 2018-02-07 | 2019-08-23 | 彭万喜 | A method of pernicious gas is handled using high-efficiency adsorbent |
| CN109520697A (en) * | 2018-11-09 | 2019-03-26 | 天津航空机电有限公司 | A kind of pilot system for simulating aircraft engine nacelle low temperature air inlet |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR101143278B1 (en) | Air cleaner having regenerative filter, and method for regenerative of air cleaner filter | |
| JP5064600B2 (en) | Method and apparatus for recovering carbon dioxide in gas | |
| JP5098762B2 (en) | Method for recovering carbon dioxide in gas | |
| CN102679454A (en) | Indoor air purifying device | |
| CN107106965B (en) | Air cleaning system | |
| WO2017055094A1 (en) | Air cleaning by photocatalytic oxidation system | |
| CN203075822U (en) | Indoor air purifying device | |
| CN201582917U (en) | Air purifier | |
| KR101522890B1 (en) | Air purifier or air pollution control system using composite metal oxide low temperature catalyst | |
| CN107661681A (en) | A kind of flue gas pollutant purifying column | |
| CN106807177A (en) | The gas cleaning plant and purification method of a kind of removing VOCs | |
| CN107497185A (en) | A kind of air purification method of temperature reaction processing | |
| CN200973847Y (en) | Photocatalysis air purifier | |
| CN207025012U (en) | Industrial VOC Multi-grade exhaust gas concentration device | |
| JP5810488B2 (en) | Wastewater treatment system | |
| CN102974215B (en) | Air purification method | |
| JP2008188493A (en) | Water treatment apparatus | |
| CN101204589A (en) | Integrated air purification method | |
| KR100889639B1 (en) | Apparatus for destruction of volatile organic compounds | |
| JP2010142730A (en) | Wastewater treatment system | |
| JP2010214285A (en) | Gas treatment method | |
| CN206082107U (en) | Industry organic waste gas purification device | |
| KR101518320B1 (en) | Hybrid system for treating toxic gas | |
| CN203030189U (en) | Air purification device | |
| JP5861547B2 (en) | Wastewater treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20171222 |
|
| WD01 | Invention patent application deemed withdrawn after publication |