CN106669304A - Efficient air filtering module used on heating pipeline - Google Patents
Efficient air filtering module used on heating pipeline Download PDFInfo
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- CN106669304A CN106669304A CN201611216670.2A CN201611216670A CN106669304A CN 106669304 A CN106669304 A CN 106669304A CN 201611216670 A CN201611216670 A CN 201611216670A CN 106669304 A CN106669304 A CN 106669304A
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- air
- metal plate
- foam metal
- filtering module
- air filtering
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- 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
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
- A61L9/014—Deodorant compositions containing sorbent material, e.g. activated carbon
-
- 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
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
-
- 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
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0028—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions provided with antibacterial or antifungal means
-
- 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
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0036—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
-
- 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
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0038—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions with means for influencing the odor, e.g. deodorizing substances
-
- 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
-
- 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
- B01D53/8603—Removing sulfur compounds
- B01D53/8612—Hydrogen sulfide
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2209/00—Aspects relating to disinfection, sterilisation or deodorisation of air
- A61L2209/20—Method-related aspects
- A61L2209/21—Use of chemical compounds for treating air or the like
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/06—Polluted air
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Public Health (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Veterinary Medicine (AREA)
- Epidemiology (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Fats And Perfumes (AREA)
Abstract
The invention provides an efficient air filtering module used on a heating pipeline. The efficient air filtering module comprises a framework, wherein a porous foam metal plate is arranged in the framework; the porosity reaches about 90 percent; the air can smoothly pass through the porous foam metal plate; an air purifying agent layer is arranged on the surface of the porous foam metal plate; the air purification layer is formed by performing drying treatment on the porous foam metal plate after the porous foam metal plate is soaked in the air purifying agent. The efficient air filtering module has the advantages that the structural design is simple and reasonable; various harmful ingredients and foreign smell in the air can be eliminated; in addition, the air is naturally sterilized and disinfected; the removal rate on chemical contaminants in the air reaches 98 percent or higher.
Description
Technical field
The present invention relates to technical field of air purification, and in particular to a kind of Efficient air filter module on heating pipe
Block.
Background technology
Heating and ventilating pipeline sends airduct, central air-conditioning ventilation duct, industrial supply and exhaust ventilation duct, environment friendly system back to as cleaning system
The common components of suction airduct, but current heating and ventilating pipeline does not possess good air-filtering ability.And with for many years to sky
The continuous accumulation of the various harmful substances of discharge, air quality has been subjected to serious pollution, particulate matter in air and various
The life security that toxic and harmful pollutant gives people brings serious threat.It is no matter indoor or outdoor, deposited in air
Biological pollutant (bacterium, virus, fungal spore, dust, dust mite), smell pollution thing, contaminants of chemical origin (second-hand-cigarette,
The hazardous air pollutants of formaldehyde, benzene homologues, factory and vehicle discharge), airborne suspended particle pollutant (PM2.5) etc..Institute
Interior is entered directly into the contaminated air by heating and ventilating pipeline, human body can be had undesirable effect.
The content of the invention
The technical problems to be solved by the invention are to improve a kind of Efficient air filtering module on heating pipe,
With filtering, sterilizing, deodorization functions, IAQ is improved.
The technical problems to be solved by the invention are realized using following technical scheme：
A kind of Efficient air filtering module on heating pipe, including a framework, are provided with porous in the framework
Gap foam metal plate, its porosity reaches 90% or so, and air can be allowed to pass through, the table of the concrete dynamic modulus foam metal plate
Face be provided with a layer of air purification oxidant layer, the purification of air oxidant layer be by the concrete dynamic modulus foam metal plate in air purifying preparation
After dipping again drying and processing and formed；
The drying is dried using circulating air, circulating air is passed through from concrete dynamic modulus foam metal plate, by space
Wall is also dried, and effect by wind-force is unlikely to make the space of concrete dynamic modulus foam metal plate to block, and hot blast temperature is controlled in 65-
82℃；
The air purifying preparation is made up of the component of following parts by weight：
The preparation method of the air purifying preparation is：By nano titanium oxide, modified RE and calcium activated in mixer
Mix, be subsequently adding adhesive agent, Conductive graphite cream, nucleator and Tea Polyphenols, be warming up to 65-68 DEG C, be thoroughly mixed, formed
Air purifying preparation.
Described nucleator is monocyclic carboxylate nucleator, specially benzoic acid sodium salt, benzoic acid aluminium salt, diphenyl acetic acid
The mixture of one or more in sodium salt or hexahydro-phthalic acid.By adding nucleator, good dispersion between material,
Compatibility is good, improves filtering adsorption effect.
The adhesive agent is regenerating and modifying waste oil, with stronger adsorption function, is had well to the particulate matter in air
Filtering adsorption effect.
Tea Polyphenols (TP) is the polyphenol compound of the separating-purifying from tealeaves particularly green tea, is the chief active of tealeaves
Composition, with extensive pharmacological action.Research has shown that Tea Polyphenols can suppress the GTF enzymes of bacterium, with calcium activated and nanometer titanium dioxide
Titanium is coordinated, and with catalysis, can play sterilized to air sterillization.
The modified RE is modified RE oxide, primarily serves catalytic action.
The processing method of the regenerating and modifying waste oil is as follows：
(1) using the waste oil produced in food and drink as raw material, vessel in heating to 70-90 DEG C of state is put into, keeps 30
Minute or so, part moisture evaporation is fallen, and the scum on surface is filtered off；
(2) in the waste oil input reactor in step (1), will open agitating function, mixing speed control 260~
280 revs/min, continuously stir 40 minutes or so, stop stirring, input atlapulgite is decolourized, atlapulgite and waste oil
Weight ratio be 2~6: 100；65-68 DEG C is maintained the temperature at, is continuously stirred 12 hours, carried out when temperature is down to 40 DEG C or so
Filtration treatment, collects liquid fat stand-by；
Used again after the semisolid atlapulgite recycling that above-mentioned filtering is produced；
(3) liquid fat is put into reactor, is warming up to 65-75 DEG C, put into formic acid, open stirring, continuously stir 30 points
Clock, then adds ethanol from the head tank of reactor, and unlatching is uniformly mixed；
The inventory of formic acid is the 3.5% of waste oil gross weight, the inventory of ethanol and the mol ratio of waste oil inventory
1.1:0.6；
(4) steam valve is opened, reactor is heated up, controlling reaction temperature is kept for 80 minutes at 80~120 DEG C,
It is then turned on reactor to be stirred, mixing speed is controlled at 260~280 revs/min, continuously stirs 60 minutes, terminating reaction；
(5) after reaction terminates, stratification is carried out to reactant, takes upper strata oil separator, by upper strata oil separator transfer
Into fractionation kettle, kettle temperature is risen, at 70 DEG C, normal pressure reclaims the complete ethanol of unreacted to control temperature；
(6) after ethanol is reclaimed and terminated, fractionation kettle is heated up to 90 DEG C or so, is incubated 6 hours, then stand 30 hours, divided and go
Lower floor's waste acid water, upper strata crude product is transferred in autoclave rectifying column, controls 120~150 DEG C of tower top temperature, vacuum pressure 1200
~1500Pa, reflux ratio 1：1 fractionation, obtains regenerating waste oil crude product；
(7) regeneration waste oil crude product is first neutralized with alkali lye, then is washed to neutrality, divided after removing water, oil reservoir carries out vapor
Distillation, remaining product is evaporated in vacuo, and removes low-boiling-point substance and water, then obtain final product regenerating and modifying waste oil through press filtration.
The beneficial effects of the invention are as follows：Structure design advantages of simple of the present invention, eliminate air in all kinds of harmful components and
Peculiar smell, and natural sterilization sterilization is carried out to air, the clearance to the contaminants of chemical origin in air reaches more than 98%.
Brief description of the drawings
Fig. 1 is filtering module structure chart of the present invention.
Specific embodiment
In order that technological means, creation characteristic, reached purpose and effect that the present invention is realized are easy to understand, tie below
Conjunction is specifically illustrating, and the present invention is expanded on further.
Embodiment 1
As shown in figure 1, a kind of Efficient air filtering module on heating pipe, including a framework 1, framework 1 is connected
Concrete dynamic modulus foam metal plate 2 is provided with the air inlet of warm wind pipeline 3, framework 1, its porosity reaches 90% or so, energy
Enough allow air to pass through, the surface of concrete dynamic modulus foam metal plate 2 is provided with layer of air purification oxidant layer, purification of air oxidant layer be by
Concrete dynamic modulus foam metal plate 2 impregnate in the air purifying preparation after again drying and processing and formed；Drying is dried using circulating air,
Circulating air is passed through from concrete dynamic modulus foam metal plate, space inwall is also dried, and be unlikely to make by the effect of wind-force many
The space of celled foam metallic plate is blocked, and hot blast temperature is controlled at 65-82 DEG C；
The air purifying preparation is made up of the component of following parts by weight：
The preparation method of the air purifying preparation is：By nano titanium oxide, modified RE and calcium activated in mixer
Mix, be subsequently adding adhesive agent, Conductive graphite cream, nucleator and Tea Polyphenols, be warming up to 65-68 DEG C, be thoroughly mixed, formed
Air purifying preparation.
The adhesive agent is, with stronger adsorption function, there is good filtering adsorption effect to the particulate matter in air.
Tea Polyphenols (TP) is the polyphenol compound of the separating-purifying from tealeaves particularly green tea, is the chief active of tealeaves
Composition, with extensive pharmacological action.Research has shown that Tea Polyphenols can suppress the GTF enzymes of bacterium, with calcium activated and nanometer titanium dioxide
Titanium is coordinated, and with catalysis, can play sterilized to air sterillization.
The processing method of the regenerating and modifying waste oil is as follows：
(1) using the waste oil produced in food and drink as raw material, vessel in heating to 70-90 DEG C of state is put into, keeps 30
Minute or so, part moisture evaporation is fallen, and the scum on surface is filtered off；
(2) in the waste oil input reactor in step (1), will open agitating function, mixing speed control 260~
280 revs/min, continuously stir 40 minutes or so, stop stirring, input atlapulgite is decolourized, atlapulgite and waste oil
Weight ratio be 2~6: 100；65-68 DEG C is maintained the temperature at, is continuously stirred 12 hours, carried out when temperature is down to 40 DEG C or so
Filtration treatment, collects liquid fat stand-by；
Used again after the semisolid atlapulgite recycling that above-mentioned filtering is produced；
(3) liquid fat is put into reactor, is warming up to 65-75 DEG C, put into formic acid, open stirring, continuously stir 30 points
Clock, then adds ethanol from the head tank of reactor, and unlatching is uniformly mixed；
The inventory of formic acid is the 3.5% of waste oil gross weight, the inventory of ethanol and the mol ratio of waste oil inventory
1.1:0.6；
(4) steam valve is opened, reactor is heated up, controlling reaction temperature is kept for 80 minutes at 80~120 DEG C,
It is then turned on reactor to be stirred, mixing speed is controlled at 260~280 revs/min, continuously stirs 60 minutes, terminating reaction；
(5) after reaction terminates, stratification is carried out to reactant, takes upper strata oil separator, by upper strata oil separator transfer
Into fractionation kettle, kettle temperature is risen, at 70 DEG C, normal pressure reclaims the complete ethanol of unreacted to control temperature；
(6) after ethanol is reclaimed and terminated, fractionation kettle is heated up to 90 DEG C or so, is incubated 6 hours, then stand 30 hours, divided and go
Lower floor's waste acid water, upper strata crude product is transferred in autoclave rectifying column, controls 120~150 DEG C of tower top temperature, vacuum pressure 1200
~1500Pa, reflux ratio 1：1 fractionation, obtains regenerating waste oil crude product；
(7) regeneration waste oil crude product is first neutralized with alkali lye, then is washed to neutrality, divided after removing water, oil reservoir carries out vapor
Distillation, remaining product is evaporated in vacuo, and removes low-boiling-point substance and water, then obtain final product regenerating and modifying waste oil through press filtration.
Embodiment 2
As shown in figure 1, a kind of Efficient air filtering module on heating pipe, including a framework 1, framework 1 is connected
Concrete dynamic modulus foam metal plate 2 is provided with the air inlet of warm wind pipeline 3, framework 1, its porosity reaches 90% or so, energy
Enough allow air to pass through, the surface of concrete dynamic modulus foam metal plate 2 is provided with layer of air purification oxidant layer, purification of air oxidant layer be by
Concrete dynamic modulus foam metal plate 2 impregnate in the air purifying preparation after again drying and processing and formed；Drying is dried using circulating air,
Circulating air is passed through from concrete dynamic modulus foam metal plate, space inwall is also dried, and be unlikely to make by the effect of wind-force many
The space of celled foam metallic plate is blocked, and hot blast temperature is controlled at 65-82 DEG C；
The air purifying preparation is made up of the component of following parts by weight：
The preparation method of the air purifying preparation is：By nano titanium oxide, modified RE and calcium activated in mixer
Mix, be subsequently adding adhesive agent, Conductive graphite cream, nucleator and Tea Polyphenols, be warming up to 65-68 DEG C, be thoroughly mixed, formed
Air purifying preparation.
The adhesive agent is, with stronger adsorption function, there is good filtering adsorption effect to the particulate matter in air.
Tea Polyphenols (TP) is the polyphenol compound of the separating-purifying from tealeaves particularly green tea, is the chief active of tealeaves
Composition, with extensive pharmacological action.Research has shown that Tea Polyphenols can suppress the GTF enzymes of bacterium, with calcium activated and nanometer titanium dioxide
Titanium is coordinated, and with catalysis, can play sterilized to air sterillization.
The processing method of the regenerating and modifying waste oil is as follows：
(1) using the waste oil produced in food and drink as raw material, vessel in heating to 70-90 DEG C of state is put into, keeps 30
Minute or so, part moisture evaporation is fallen, and the scum on surface is filtered off；
(2) in the waste oil input reactor in step (1), will open agitating function, mixing speed control 260~
280 revs/min, continuously stir 40 minutes or so, stop stirring, input atlapulgite is decolourized, atlapulgite and waste oil
Weight ratio be 2~6: 100；65-68 DEG C is maintained the temperature at, is continuously stirred 12 hours, carried out when temperature is down to 40 DEG C or so
Filtration treatment, collects liquid fat stand-by；
Used again after the semisolid atlapulgite recycling that above-mentioned filtering is produced；
(3) liquid fat is put into reactor, is warming up to 65-75 DEG C, put into formic acid, open stirring, continuously stir 30 points
Clock, then adds ethanol from the head tank of reactor, and unlatching is uniformly mixed；
The inventory of formic acid is the 3.5% of waste oil gross weight, the inventory of ethanol and the mol ratio of waste oil inventory
1.1:0.6；
(4) steam valve is opened, reactor is heated up, controlling reaction temperature is kept for 80 minutes at 80~120 DEG C,
It is then turned on reactor to be stirred, mixing speed is controlled at 260~280 revs/min, continuously stirs 60 minutes, terminating reaction；
(5) after reaction terminates, stratification is carried out to reactant, takes upper strata oil separator, by upper strata oil separator transfer
Into fractionation kettle, kettle temperature is risen, at 70 DEG C, normal pressure reclaims the complete ethanol of unreacted to control temperature；
(6) after ethanol is reclaimed and terminated, fractionation kettle is heated up to 90 DEG C or so, is incubated 6 hours, then stand 30 hours, divided and go
Lower floor's waste acid water, upper strata crude product is transferred in autoclave rectifying column, controls 120~150 DEG C of tower top temperature, vacuum pressure 1200
~1500Pa, reflux ratio 1：1 fractionation, obtains regenerating waste oil crude product；
(7) regeneration waste oil crude product is first neutralized with alkali lye, then is washed to neutrality, divided after removing water, oil reservoir carries out vapor
Distillation, remaining product is evaporated in vacuo, and removes low-boiling-point substance and water, then obtain final product regenerating and modifying waste oil through press filtration.
The application can play catalytic action by setting filtering module, eliminate all kinds of harmful components in air and different
Taste, and carry out natural sterilization sterilization to air, reaches more than 98% to the clearance of the contaminants of chemical origin in air, right
The filter efficiency of PM2.5 up to more than 95%, to PM0.3 filter efficiencies up to more than 80%, concentration of hydrogen sulfide is by under 500ppm
It is down to 0ppm, removal rate 100%.So that being purified treatment by the contaminated air of heating and ventilating pipeline.
General principle of the invention and principal character and advantages of the present invention has been shown and described above.The technology of the industry
Personnel it should be appreciated that the present invention is not limited to the above embodiments, simply explanation described in above-described embodiment and specification this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and modifications of the present invention are possible, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appending claims and its
Equivalent thereof.
Claims (4)
1. a kind of Efficient air filtering module on heating pipe, it is characterised in that including a framework, the framework connection
Concrete dynamic modulus foam metal plate is provided with the air inlet of warm wind pipeline, the framework, the concrete dynamic modulus foam metal plate
Surface is provided with layer of air purification oxidant layer, and the purification of air oxidant layer is in air purifying preparation by the concrete dynamic modulus foam metal plate
After middle dipping again drying and processing and formed.
2. a kind of Efficient air filtering module on heating pipe according to claim 1, it is characterised in that described
Drying is dried using circulating air, circulating air is passed through from concrete dynamic modulus foam metal plate, and space inwall is also dried.
3. a kind of Efficient air filtering module on heating pipe according to claim 2, it is characterised in that described
Hot blast temperature is controlled at 65-82 DEG C.
4. a kind of Efficient air filtering module on heating pipe according to claim 1, it is characterised in that described
The porosity of concrete dynamic modulus foam metal plate reaches 90%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611216670.2A CN106669304A (en) | 2016-12-26 | 2016-12-26 | Efficient air filtering module used on heating pipeline |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611216670.2A CN106669304A (en) | 2016-12-26 | 2016-12-26 | Efficient air filtering module used on heating pipeline |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106669304A true CN106669304A (en) | 2017-05-17 |
Family
ID=58870581
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201611216670.2A Pending CN106669304A (en) | 2016-12-26 | 2016-12-26 | Efficient air filtering module used on heating pipeline |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203928156U (en) * | 2014-06-24 | 2014-11-05 | 马元海 | The air-purifying module of heating and ventilating pipeline with porous metal carrier nano coating |
| CN104667646A (en) * | 2015-01-23 | 2015-06-03 | 北京博源恒升高科技有限公司 | Waste gas dust removing method and dust removing agent |
| CN105771424A (en) * | 2016-03-25 | 2016-07-20 | 成都易态科技有限公司 | Porous material, preparation method thereof and filtering element applying porous material |
| KR20170006444A (en) * | 2015-07-08 | 2017-01-18 | 김광식 | The apparatus for cleaning a air |
-
2016
- 2016-12-26 CN CN201611216670.2A patent/CN106669304A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203928156U (en) * | 2014-06-24 | 2014-11-05 | 马元海 | The air-purifying module of heating and ventilating pipeline with porous metal carrier nano coating |
| CN104667646A (en) * | 2015-01-23 | 2015-06-03 | 北京博源恒升高科技有限公司 | Waste gas dust removing method and dust removing agent |
| KR20170006444A (en) * | 2015-07-08 | 2017-01-18 | 김광식 | The apparatus for cleaning a air |
| CN105771424A (en) * | 2016-03-25 | 2016-07-20 | 成都易态科技有限公司 | Porous material, preparation method thereof and filtering element applying porous material |
Non-Patent Citations (5)
| Title |
|---|
| 刘志坚: "《聚合物成核剂》", 29 February 2012, 中国石化出版社 * |
| 季祥等: "《生物质能源及废物利用新技术》", 31 December 2012, 吉林大学出版社 * |
| 张爱联: "《生物化学与分子生物学实验教程》", 31 January 2009, 中国农业大学出版社 * |
| 李科等: "《液态金属泡沫演化动力学理论与模型》", 31 May 2014, 吉林大学出版社 * |
| 汪用文: "《中国茶产品加工》", 30 June 2011, 上海科学技术出版社 * |
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