CN103861409A - Air purification treatment system - Google Patents
Air purification treatment system Download PDFInfo
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- CN103861409A CN103861409A CN201210536460.7A CN201210536460A CN103861409A CN 103861409 A CN103861409 A CN 103861409A CN 201210536460 A CN201210536460 A CN 201210536460A CN 103861409 A CN103861409 A CN 103861409A
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Abstract
The invention relates to an air purification treatment system, which comprises an air pressurization device, a primary purifier, a secondary purifier, a pressure reducing valve, a two-stage pressure stabilizing speed regulator, an organic matter filter and a gas flow meter, wherein the air pressurization device, the primary purifier, the secondary purifier, the pressure reducing valve, the two-stage pressure stabilizing speed regulator, the organic matter filter and the gas flow meter are sequentially connected in series through pipeline. According to the present invention, air is supplied for the primary purifier through the air pressurization device, sequentially passes through the secondary purifier, the pressure reducing valve, the two-stage pressure stabilizing speed regulator, the organic matter filter and the gas flow meter, and outflows from the gas flow meter outlet, wherein the particulate matters in the purified air is less than or equal to 0.01 mum, the dew point is -60 to -20 DEG C, and the volatile organic matter TVOC content in the gas is 0.1-1 ppb. According to the air purification treatment system, various components are independent and can be conveniently subjected to upgrading and replacement, the structure is compact, the assembly is convenient, the gas treatment effect is good, the low relative humidity can be provided, the solid particles with a particle size of 0.01 mum can be filtered out, organic macromolecules and the like can be filtered out, and the stable high-performance can be maintained for a long time.
Description
Technical field
The present invention relates to gas analysis technology field, relate in particular to a kind of air cleaning treatment system.
Background technology
Adopting in gas analysis technology analyzes, conventionally need to low dew point, clean gas gas or the carrier gas as a setting of low content of organics, so that disturb the content of impurity to reduce in rational scope in source of the gas.
For example number of patent application ZL 201120075054-gas purification filter, has invented the combined filtration chamber device of miillpore filter and activated carbon filter cloth.The renovation process of number of patent application ZL 201010233688-gas purifier and molecular sieve thereof, has invented and has adopted attemperating unit molecular sieve in clarifier to be carried out to the method for in-situ regeneration.Number of patent application ZL 200680021966-gas purifier and method for gas purification, the method for having invented the loading of definite cleanser.
Foregoing invention there is no the requirement of the satisfied clean gas of realizing low humidity, low content of organics of method.
Therefore the present invention has designed a kind of air cleaning treatment system, to address the above problem.
Summary of the invention
The object of the present invention is to provide a kind of air cleaning treatment system.
For achieving the above object, the technical solution used in the present invention is:
A kind of air cleaning treatment system, comprises air pressurized equipment, primary purifying device, second cleaner, pressure-reducing valve, secondary voltage stabilizing speed regulator, the organic matter filter of contacting by pipeline successively) and gas flowmeter formation; Primary purifying device discharge outlet, second cleaner discharge outlet are for draining, and pressure-reducing valve adjusting knob, secondary voltage stabilizing speed regulator adjusting knob are for adjustments of gas pressure or flow velocity.
Air pressurized equipment is compressor or the steel cylinder that pressure-air is housed.
Primary purifying device is two lattice oil water separators, comprises air cleaner, pressure-reducing valve; Clean for to source of the gas of air cleaner, can filter the airborne moisture of compression and airborne oil gas, avoids moisture and oil gas with gas access to plant, and its filtering accuracy is generally 0.1-5 μ m; Pressure-reducing valve can carry out voltage stabilizing to source of the gas, make source of the gas in steady state, can reduce to suddenly change because of source of the gas air pressure time, be 0.5-10Mpa to the damage range of regulation of the hardware such as valve or actuator, primary purifying device is for removing airborne liquid steam and the aerosol particle that is greater than 5 μ m.
Second cleaner is high polymer diaphragm air dryer, is SMC(China) the IDG series macromolecular membrane air dryer of Co., Ltd.
Organic matter filter interior is filled with the sorbing material of water suction and adsorb organic compound, comprises one or two or more kinds in silica gel, molecular sieve, activated carbon, calcium chloride.
Secondary voltage stabilizing speed regulator (8) is voltage stabilization and current stabilization valve, can regulate the function of the size of air-flow in gas circuit and gas stabilization, makes in gas circuit gas flow maintenance constant.
Air is offered after primary purifying device, successively by second cleaner, pressure-reducing valve, secondary voltage stabilizing speed regulator, organic matter filter and gas flowmeter by air pressurized equipment, is flowed out by gas flowmeter gas outlet.
The final particle being purified in rear air gas is less than or equal to 0.01 μ m; Final institute obtain in gas dew point spend to-20 for-60 degree; The final volatile organic matter TVOC content being obtained in gas is 0.1-1ppb.
Accompanying drawing explanation
Fig. 1 is a kind of schematic diagram of air cleaning treatment system.
The specific embodiment
Embodiment 1:
A kind of air cleaning treatment system, comprises that air pressurized equipment 1, primary purifying device 2, second cleaner 4, pressure-reducing valve 6, secondary voltage stabilizing speed regulator 8, organic matter filter 10 and the gas flowmeter 11 of contacting by pipeline successively form; Primary purifying device discharge outlet 3, second cleaner discharge outlet 5 are for draining, and pressure-reducing valve adjusting knob 7, secondary voltage stabilizing speed regulator adjusting knob 9 are for adjustments of gas pressure or flow velocity.
Air pressurized equipment is compressor or the steel cylinder that pressure-air is housed.
Primary purifying device 2 is two lattice oil water separators, comprises air cleaner, pressure-reducing valve;
Second cleaner is high polymer diaphragm air dryer, is SMC(China) the IDG series macromolecular membrane air dryer of Co., Ltd.
Organic matter filter interior is filled with the sorbing material of water suction and adsorb organic compound, comprises one or two or more kinds in silica gel, molecular sieve, activated carbon, calcium chloride.
Secondary voltage stabilizing speed regulator 8 is voltage stabilization and current stabilization valve, can regulate the function of the size of air-flow in gas circuit and gas stabilization, makes in gas circuit gas flow maintenance constant.
Air is offered after primary purifying device 2, successively by second cleaner 4, pressure-reducing valve 6, secondary voltage stabilizing speed regulator 8, organic matter filter 10 and gas flowmeter 11 by air pressurized equipment 1, is flowed out by gas flowmeter 11 gas outlets.
Wherein, second cleaner adopts high polymer diaphragm air dryer IDG1, sorbing material in organic matter filter is calcium chloride, when gas flow is 0.5 liter/min, final obtain particle in gas for being less than 0.1um, the dew point of gas is-20 degree, and the volatile organic matter TVOC content in gas is 1ppb.
Embodiment 2:
A kind of air cleaning treatment system, comprises that air pressurized equipment 1, primary purifying device 2, second cleaner 4, pressure-reducing valve 6, secondary voltage stabilizing speed regulator 8, organic matter filter 10 and the gas flowmeter 11 of contacting by pipeline successively form; Primary purifying device discharge outlet 3, second cleaner discharge outlet 5 are for draining, and pressure-reducing valve adjusting knob 7, secondary voltage stabilizing speed regulator adjusting knob 9 are for adjustments of gas pressure or flow velocity.
Air pressurized equipment is compressor or the steel cylinder that pressure-air is housed.
Primary purifying device 2 is two lattice oil water separators, comprises air cleaner, pressure-reducing valve;
Second cleaner is high polymer diaphragm air dryer, is SMC(China) the IDG series macromolecular membrane air dryer of Co., Ltd.
Organic matter filter interior is filled with the sorbing material of water suction and adsorb organic compound, comprises one or two or more kinds in silica gel, molecular sieve, activated carbon, calcium chloride.
Secondary voltage stabilizing speed regulator 8 is voltage stabilization and current stabilization valve, can regulate the function of the size of air-flow in gas circuit and gas stabilization, makes in gas circuit gas flow maintenance constant.
Air is offered after primary purifying device 2, successively by second cleaner 4, pressure-reducing valve 6, secondary voltage stabilizing speed regulator 8, organic matter filter 10 and gas flowmeter 11 by air pressurized equipment 1, is flowed out by gas flowmeter 11 gas outlets.
Wherein, second cleaner adopts high polymer diaphragm air dryer IDG10, sorbing material in organic matter filter is molecular sieve and two kinds of packing materials of activated carbon, when gas flow is 1 liter/min, final obtain particle in gas for being less than 0.1um, the dew point of gas is-60 degree, and the volatile organic matter TVOC content in gas is 0.1ppb.
Embodiment 3:
A kind of air cleaning treatment system, comprises that air pressurized equipment 1, primary purifying device 2, second cleaner 4, pressure-reducing valve 6, secondary voltage stabilizing speed regulator 8, organic matter filter 10 and the gas flowmeter 11 of contacting by pipeline successively form; Primary purifying device discharge outlet 3, second cleaner discharge outlet 5 are for draining, and pressure-reducing valve adjusting knob 7, secondary voltage stabilizing speed regulator adjusting knob 9 are for adjustments of gas pressure or flow velocity.
Air pressurized equipment is compressor or the steel cylinder that pressure-air is housed.
Primary purifying device 2 is two lattice oil water separators, comprises air cleaner, pressure-reducing valve;
Second cleaner is high polymer diaphragm air dryer, is SMC(China) the IDG series macromolecular membrane air dryer of Co., Ltd.
Organic matter filter interior is filled with the sorbing material of water suction and adsorb organic compound, comprises one or two or more kinds in silica gel, molecular sieve, activated carbon, calcium chloride.
Secondary voltage stabilizing speed regulator 8 is voltage stabilization and current stabilization valve, can regulate the function of the size of air-flow in gas circuit and gas stabilization, makes in gas circuit gas flow maintenance constant.
Air is offered after primary purifying device 2, successively by second cleaner 4, pressure-reducing valve 6, secondary voltage stabilizing speed regulator 8, organic matter filter 10 and gas flowmeter 11 by air pressurized equipment 1, is flowed out by gas flowmeter 11 gas outlets.
Wherein, second cleaner adopts high polymer diaphragm air dryer IDG30, sorbing material in organic matter filter is silica gel and two kinds of materials of activated carbon, when gas flow is 3 liters/min, final obtain particle in gas for being less than 0.1um, the dew point of gas is-20 degree, and the volatile organic matter TVOC content in gas is 0.1ppb.
Claims (5)
1. an air cleaning treatment system, is characterized in that:
Comprise that air pressurized equipment (1), primary purifying device (2), second cleaner (4), pressure-reducing valve (6), secondary voltage stabilizing speed regulator (8), organic matter filter (10) and the gas flowmeter (11) of contacting by pipeline successively form;
Primary purifying device (2) is two lattice oil water separators, comprises air cleaner, pressure-reducing valve;
Second cleaner is high polymer diaphragm air dryer;
Organic matter filter interior is filled with the sorbing material of water suction and adsorb organic compound;
Air is offered after primary purifying device (2), successively by second cleaner (4), pressure-reducing valve (6), secondary voltage stabilizing speed regulator (8), organic matter filter (10) and gas flowmeter (11) by air pressurized equipment (1), is flowed out by gas flowmeter (11) gas outlet.
2. air cleaning treatment system according to claim 1, is characterized in that: air pressurized equipment is compressor or the steel cylinder that pressure-air is housed.
3. air cleaning treatment system according to claim 1, is characterized in that:
High polymer diaphragm air dryer is SMC(China) the IDG series macromolecular membrane air dryer of Co., Ltd;
Sorbing material in organic matter filter is one or two or more kinds in silica gel, molecular sieve, activated carbon, calcium chloride.
4. air cleaning treatment system according to claim 1, is characterized in that:
Secondary voltage stabilizing speed regulator (8) is voltage stabilization and current stabilization valve.
5. air cleaning treatment system according to claim 1, is characterized in that:
The final particle being purified in rear air gas is less than or equal to 0.01um; Final institute obtain in gas dew point spend to-20 for-60 degree; The final volatile organic matter TVOC content being obtained in gas is 0.1-1ppb.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210536460.7A CN103861409A (en) | 2012-12-12 | 2012-12-12 | Air purification treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210536460.7A CN103861409A (en) | 2012-12-12 | 2012-12-12 | Air purification treatment system |
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| CN103861409A true CN103861409A (en) | 2014-06-18 |
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| CN201210536460.7A Pending CN103861409A (en) | 2012-12-12 | 2012-12-12 | Air purification treatment system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107023841A (en) * | 2016-02-01 | 2017-08-08 | 山东星火科学技术研究院 | A kind of air cleaning system |
| CN111023713A (en) * | 2019-03-11 | 2020-04-17 | 北京诺维新材科技有限公司 | Solid drying method and system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201423228Y (en) * | 2008-12-15 | 2010-03-17 | 济南海纳特科技有限公司 | Air supply purifying and drying device |
| CN201500497U (en) * | 2009-08-18 | 2010-06-09 | 武汉市天虹仪表有限责任公司 | Zero-air generator |
| CN202056512U (en) * | 2011-03-21 | 2011-11-30 | 安徽省电力公司阜阳供电公司 | Multi-machine shared pressure stabilization, drying, purifying and air supply device |
| CN202185245U (en) * | 2011-07-18 | 2012-04-11 | 天津舜天达天然气有限公司 | Novel air compressor unit |
| CN102641644A (en) * | 2011-02-16 | 2012-08-22 | 习建华 | Waste gas treatment air purification device |
| JP2014077060A (en) * | 2012-10-10 | 2014-05-01 | Metawater Co Ltd | Methane fermentation gas purification process and purification system |
-
2012
- 2012-12-12 CN CN201210536460.7A patent/CN103861409A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201423228Y (en) * | 2008-12-15 | 2010-03-17 | 济南海纳特科技有限公司 | Air supply purifying and drying device |
| CN201500497U (en) * | 2009-08-18 | 2010-06-09 | 武汉市天虹仪表有限责任公司 | Zero-air generator |
| CN102641644A (en) * | 2011-02-16 | 2012-08-22 | 习建华 | Waste gas treatment air purification device |
| CN202056512U (en) * | 2011-03-21 | 2011-11-30 | 安徽省电力公司阜阳供电公司 | Multi-machine shared pressure stabilization, drying, purifying and air supply device |
| CN202185245U (en) * | 2011-07-18 | 2012-04-11 | 天津舜天达天然气有限公司 | Novel air compressor unit |
| JP2014077060A (en) * | 2012-10-10 | 2014-05-01 | Metawater Co Ltd | Methane fermentation gas purification process and purification system |
Non-Patent Citations (1)
| Title |
|---|
| 郭维强等: "气源干燥的方法及氮气干燥源的应用", 《液压与气动》, no. 11, 20 November 2003 (2003-11-20), pages 51 - 53 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107023841A (en) * | 2016-02-01 | 2017-08-08 | 山东星火科学技术研究院 | A kind of air cleaning system |
| CN111023713A (en) * | 2019-03-11 | 2020-04-17 | 北京诺维新材科技有限公司 | Solid drying method and system |
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Application publication date: 20140618 |