CN106731267A - A kind of heating pipe method for purifying indoor air - Google Patents

A kind of heating pipe method for purifying indoor air Download PDF

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Publication number
CN106731267A
CN106731267A CN201611216503.8A CN201611216503A CN106731267A CN 106731267 A CN106731267 A CN 106731267A CN 201611216503 A CN201611216503 A CN 201611216503A CN 106731267 A CN106731267 A CN 106731267A
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CN
China
Prior art keywords
air
heating pipe
filtering
purifying indoor
screen pack
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
Application number
CN201611216503.8A
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Chinese (zh)
Inventor
李伟
李长安
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Anhui Yuantong Heating Technology Co Ltd
Original Assignee
Anhui Yuantong Heating Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Anhui Yuantong Heating Technology Co Ltd filed Critical Anhui Yuantong Heating Technology Co Ltd
Priority to CN201611216503.8A priority Critical patent/CN106731267A/en
Publication of CN106731267A publication Critical patent/CN106731267A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/56Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • B01D46/62Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
    • B01D46/64Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series arranged concentrically or coaxially
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS 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
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B01D46/0036Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D5/00Hot-air central heating systems; Exhaust gas central heating systems
    • F24D5/02Hot-air central heating systems; Exhaust gas central heating systems operating with discharge of hot air into the space or area to be heated
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F6/00Air-humidification, e.g. cooling by humidification
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS 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
    • A61L2209/00Aspects relating to disinfection, sterilisation or deodorisation of air
    • A61L2209/20Method-related aspects
    • A61L2209/21Use of chemical compounds for treating air or the like
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/06Polluted air

Abstract

A kind of heating pipe method for purifying indoor air, specific method is as follows:(1) air is blown into heating pipe using air blower, first airstrainer is set in the inlet end of heating pipe, floater filtering larger in air is fallen;(2) it is located at the rear portion of screen pack and twice metallic fiber sintered felt is set in heating pipe, air is after first is filtered, then carries out adsorption filtration by twice metallic fiber sintered felt, the particulate matter that can be crossed in air filtering;(3) second screen pack is set at the gas outlet of heating pipe, and the part harmful chemical component in the air after being warmed starts actively, not filtered out by preceding road, then carries out natural sterilization sterilization to air by second filtering;(4) humidification process is carried out to interior using humidifier while heating, reduces indoor aridity, the breathing comfort level of people can be improved, while the effect of humidification can also effectively prevent the propagation of breathing problem.

Description

A kind of heating pipe method for purifying indoor air
Technical field
The present invention relates to technical field of air purification, and in particular to a kind of heating pipe method for purifying indoor air.
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 construction simply, empty in the heating pipe of good purification Gas purifying method.
The technical problems to be solved by the invention are realized using following technical scheme:
A kind of heating pipe method for purifying indoor air, specific method is as follows:
(1) air is blown into heating pipe using air blower, first air mistake is set in the inlet end of heating pipe Filter screen, floater filtering larger in air is fallen;
(2) it is located at the rear portion of screen pack and twice metallic fiber sintered felt is set in heating pipe, air is by first After filtering, then adsorption filtration is carried out by twice metallic fiber sintered felt, the particulate matter that can be crossed in air filtering, to PM2.5's Filter efficiency is up to more than 95%;
(3) second screen pack, the part harmful in the air after being warmed are set at the gas outlet of heating pipe Study the separate beginning actively, do not filtered out by preceding road, then natural sterilization sterilization is carried out to air by second filtering, to air In the clearance of contaminants of chemical origin reach more than 98%;
(4) humidification process is carried out to interior using humidifier while heating, reduces indoor aridity, can improved The breathing comfort level of people, while the effect of humidification can also effectively prevent the propagation of breathing problem.
First screen pack is common commercial air screen pack, can be fallen floater filtering larger in air , prevent from entering space on inner pipeline plug plug metallic fiber sintered felt;
The surface of the second screen pack is provided with one layer of nano coating, by the catalytic action of nano coating, eliminates empty All kinds of harmful components and peculiar smell in gas, and natural sterilization sterilization is carried out to air.
The nano coating contains by the component of following parts by weight:
The nano coating forming method is:Nano titanium oxide, modified RE and calcium activated are mixed in mixer, Adhesive agent, Conductive graphite cream, nucleator and Tea Polyphenols are subsequently adding, 65-68 DEG C is warming up to, is thoroughly mixed, by second Screen pack impregnates in the mixture, then dries.
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:The inventive method is simple, it is easy to implement, and cost is relatively low, without any side effects, energy Enough eliminate all kinds of harmful components and peculiar smell in air, and natural sterilization sterilization carried out to air, in air chemically The clearance of pollutant reaches more than 98%.
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 Specific embodiment is closed, the present invention is expanded on further.
Embodiment 1
A kind of heating pipe method for purifying indoor air, specific method is as follows:
(1) air is blown into heating pipe using air blower, first air mistake is set in the inlet end of heating pipe Filter screen, floater filtering larger in air is fallen;
(2) it is located at the rear portion of screen pack and twice metallic fiber sintered felt is set in heating pipe, air is by first After filtering, then adsorption filtration is carried out by twice metallic fiber sintered felt, the particulate matter that can be crossed in air filtering, to PM2.5's Filter efficiency is up to more than 95%;
(3) second screen pack, the part harmful in the air after being warmed are set at the gas outlet of heating pipe Study the separate beginning actively, do not filtered out by preceding road, then natural sterilization sterilization is carried out to air by second filtering, to air In the clearance of contaminants of chemical origin reach more than 98%;
(4) humidification process is carried out to interior using humidifier while heating, reduces indoor aridity, can improved The breathing comfort level of people, while the effect of humidification can also effectively prevent the propagation of breathing problem.
First screen pack is common commercial air screen pack, can be fallen floater filtering larger in air , prevent from entering space on inner pipeline plug plug metallic fiber sintered felt;
The surface of the second screen pack is provided with one layer of nano coating, by the catalytic action of nano coating, eliminates empty All kinds of harmful components and peculiar smell in gas, and natural sterilization sterilization is carried out to air.
The nano coating contains by the component of following parts by weight:
The nano coating forming method is:Nano titanium oxide, modified RE and calcium activated are mixed in mixer, Adhesive agent, Conductive graphite cream, nucleator and Tea Polyphenols are subsequently adding, 65-68 DEG C is warming up to, is thoroughly mixed, by second Screen pack impregnates in the mixture, then dries.
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 inventive method can eliminate all kinds of harmful components and peculiar smell in air, and carry out natural sterilization to air and disappear Poison, the clearance to the contaminants of chemical origin in air reaches more than 98%, to 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 drops to 0ppm, removal rate 100% by 500ppm.So that through The contaminated air for crossing heating and ventilating pipeline is purified treatment.
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 (6)

1. a kind of heating pipe method for purifying indoor air, it is characterised in that specific method is as follows:
(1) air is blown into heating pipe using air blower, first airstrainer is set in the inlet end of heating pipe, Floater filtering larger in air is fallen;
(2) it is located at the rear portion of screen pack and twice metallic fiber sintered felt is set in heating pipe, air is by first filtering Afterwards, then by twice metallic fiber sintered felt adsorption filtration is carried out, the particulate matter that can be crossed in air filtering;
(3) second screen pack is set at the gas outlet of heating pipe, part harmful chemicals in the air after being warmed into Separately begin active, do not filtered out by preceding road, then natural sterilization sterilization is carried out to air by second filtering, in air The clearance of contaminants of chemical origin reaches more than 98%;
(4) humidification process is carried out to interior using humidifier while heating, reduces indoor aridity.
2. a kind of heating pipe method for purifying indoor air according to claim 1, it is characterised in that first filtering Net is common commercial air screen pack.
3. a kind of heating pipe method for purifying indoor air according to claim 1, it is characterised in that the second filtering The surface of net is provided with one layer of nano coating.
4. a kind of heating pipe method for purifying indoor air according to claim 3, it is characterised in that the nano coating contains Have by the component of following parts by weight:
5. a kind of heating pipe method for purifying indoor air according to claim 4, it is characterised in that described nucleator is Monocyclic carboxylate nucleator, specially benzoic acid sodium salt, benzoic acid aluminium salt, diphenyl acetic acid sodium salt or hexahydro-phthalic acid In the mixture of one or more.
6. a kind of heating pipe method for purifying indoor air according to claim 4, it is characterised in that the adhesive agent is for again Raw modified swill-cooked dirty oil.
CN201611216503.8A 2016-12-26 2016-12-26 A kind of heating pipe method for purifying indoor air Pending CN106731267A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611216503.8A CN106731267A (en) 2016-12-26 2016-12-26 A kind of heating pipe method for purifying indoor air

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611216503.8A CN106731267A (en) 2016-12-26 2016-12-26 A kind of heating pipe method for purifying indoor air

Publications (1)

Publication Number Publication Date
CN106731267A true CN106731267A (en) 2017-05-31

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CN201611216503.8A Pending CN106731267A (en) 2016-12-26 2016-12-26 A kind of heating pipe method for purifying indoor air

Country Status (1)

Country Link
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Citations (4)

* Cited by examiner, † Cited by third party
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
CN104603183A (en) * 2012-07-06 2015-05-06 阿克苏诺贝尔涂料国际有限公司 Method for producing a nanocomposite dispersion comprising composite particles|of inorganic nanoparticles and organic polymers
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
CN106009835A (en) * 2016-07-12 2016-10-12 余志娟 Anti-bacterial anti-mildew flame-retardant primer for indoor decoration

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104603183A (en) * 2012-07-06 2015-05-06 阿克苏诺贝尔涂料国际有限公司 Method for producing a nanocomposite dispersion comprising composite particles|of inorganic nanoparticles and organic polymers
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
CN106009835A (en) * 2016-07-12 2016-10-12 余志娟 Anti-bacterial anti-mildew flame-retardant primer for indoor decoration

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
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》", 30 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 *

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