CN201748566U - Air optimization device - Google Patents
Air optimization device Download PDFInfo
- Publication number
- CN201748566U CN201748566U CN2010201668652U CN201020166865U CN201748566U CN 201748566 U CN201748566 U CN 201748566U CN 2010201668652 U CN2010201668652 U CN 2010201668652U CN 201020166865 U CN201020166865 U CN 201020166865U CN 201748566 U CN201748566 U CN 201748566U
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- Prior art keywords
- air
- oxygen
- optimized
- axis
- valve
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- 238000005457 optimization Methods 0.000 title abstract description 7
- 238000000926 separation method Methods 0.000 claims abstract description 9
- 239000002808 molecular sieve Substances 0.000 claims description 16
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 16
- 239000000428 dust Substances 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 5
- 230000000844 anti-bacterial effect Effects 0.000 claims description 4
- 239000002250 absorbent Substances 0.000 claims description 2
- 230000002745 absorbent Effects 0.000 claims description 2
- 239000003610 charcoal Substances 0.000 claims description 2
- 239000006185 dispersion Substances 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 abstract description 26
- 229910052760 oxygen Inorganic materials 0.000 abstract description 26
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 20
- 230000000694 effects Effects 0.000 abstract description 3
- 238000001514 detection method Methods 0.000 abstract 2
- 238000000746 purification Methods 0.000 abstract 2
- 230000001706 oxygenating effect Effects 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 238000000034 method Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- -1 oxygen ion Chemical class 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000013016 damping Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 2
- 238000005660 chlorination reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000006213 oxygenation reaction Methods 0.000 description 2
- 238000005201 scrubbing Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
Images
Landscapes
- Central Air Conditioning (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
An air optimization device comprises an air supply device and an air pretreatment device in sequential connection, and further comprises a control system, a detection device and a solenoid valve connected with the air pretreatment device, wherein the detection device is in electric connection with the control system; the solenoid valve is in electric connection with the control system; and the solenoid valve is also connected with two shunt-wound air optimization branch circuits, one branch circuit is provided with a purification device, and the other branch circuit is provided with a separation oxygenating device. The air optimization device has good purification effect, large treatment capacity and capability of adjusting and controlling oxygen content.
Description
Technical field
The utility model relates to a kind of air processor.
Background technology
Room air produces material impact to people's health, air purification method commonly used promptly is at air conditioner room air to be carried out on the thermoregulator basis, the an amount of outdoor fresh air of introducing, and air optimizational function parts such as process ventilator and air cleaning machine are to its humidity, cleanliness factor, after pure and fresh degree optimization is regulated, be injected into it indoor successively again, with the dilution of its matter and the increase of amount, squeeze gradually with displacement and fall indoor original foul atmosphere, thereby be reached for the purpose that human body provides healthy high-quality air, the forms of air-conditioning that adopt realize that it is not good that it has clean-up effect more in the practice, treating capacity is little, can't regulate problems such as oxygen content.
The utility model content
The technical problems to be solved in the utility model is that to overcome existing air-conditioning be the defective of the air cleaning system of representative, and a kind of clean-up effect is good, treating capacity is big, the air optimization method and the special processor thereof of adjustable controlled oxygen content and provide.
In order to solve the problems of the technologies described above, the utility model provides following technical scheme:
A kind of air is optimized device, comprise the air-supply arrangement, the air pretreatment unit that connect successively, it is characterized in that: described air is optimized device and is also comprised control system, checkout gear, the magnetic valve that is connected with pretreatment unit, described checkout gear is electrically connected with control system, and described magnetic valve is electrically connected with control system; Described magnetic valve is also optimized branch road with the air of two parallel connections and is connected, and the one branch road is established purifier, and another branch road is established the separation oxygen-increasing device.
Further be improved to, pretreatment unit is meant any or the arbitrarily combination in bactericidal unit, decomposer, dust arrester, the wash mill.Be provided with behind the described separation oxygen-increasing device and increase the negative oxygen ion device, separation oxygen-increasing device employing molecular sieve.Described purifier is washing tank and/or absorbent charcoal adsorber.
Separate between oxygen-increasing device and the magnetic valve and establish distributing valve, described distributing valve comprises cylindrical spool and valve casing; Establish through hole on the described cylindrical spool, its quantity is: each separates 3 of the through holes that dispersion is established in oxygen-increasing device unit, and wherein the axis of 2 through holes is parallel, and the axis of 1 through hole intersects at an angle with the axis of these 2 through holes in addition; Described valve casing is the tubular body that cooperates with spool, splits double passage in through hole.Preferred angle is that the axis of 1 through hole in addition of described cylindrical spool and the axis of these 2 through holes are square crossing.Preferably, the axis of 1 through hole in addition of cylindrical spool and the axis of these 2 through holes are square crossing.
Control system comprises process chip and display control panel etc., and control chip controls its action for magnetic valve, air compressor machine, a way solenoid valve etc. by the detected value signal of processing checkout gear or the artificial input signal of panel thereby export control signal again.
This optimization device in steps jar, cabinet, the casing of unit establish the deslagging valve port, can regularly artificial cleaned and changed tank body and solution, and establish check-valves each other, prevent that gas and solution from flowing backwards.Pressure vessel is established Pressure gauge and safety valve, when abnormal conditions such as superpressure occur, can shut down and warning by chip controls.The medicament of configuration can be changed according to actual detected, and part technology can increase and decrease as required.For the requirement of not isometric space and particular surroundings, can design concrete technology and operating system according to this principle.
After the start, air compressor machine or blower fan air supply, and pass through bactericidal unit successively, decomposer, dust arrester, wash mill etc., through magnetic valve, at this moment, the air quality analyzer is measured airborne oxygen content, and with transfer of data to control system, thereby the branch road of rational allocation air process: the oxygen content that (1) is measured when the air quality analyzer in the setting scope time (as more than 21%, below 25%), purify (as washing with magnetic valve guiding air, absorption) program, humidification (also can add useful smell of people etc.) is arranged at last to indoor again.(2) when air quality analyzer mensuration oxygen concentration (as less than 21%) when setting is following, carry out molecular sieve with magnetic valve guiding air and separate the oxygenation processing, start distributing valve, molecular sieve is isolated oxygen and nitrogen, discharges such as nitrogen is outdoor, the oxygen input is indoor, thereby increase oxygen concentration, also can install animating electrode additional, produce negative oxygen ion isoreactivity composition, or install oxygen content that damping device (3) measures when the air quality analyzer additional greater than 25% the time, return program (1) with magnetic valve guiding air.
So repeatedly, air quality is remained help most the good state of human body respiration.
It is scientific and reasonable that air of the present utility model is optimized the apparatus and method flow process, required system disposes easily, and operation supervise and control is convenient, and pure, the rational high-quality air of component can be provided, its treating apparatus be can also reduce or increase according to actual needs, thereby more production, life application conditions satisfied.
Description of drawings
Accompanying drawing is used to provide further understanding of the present utility model, and constitutes the part of specification, is used from explanation the utility model with embodiment one of the present utility model, does not constitute restriction of the present utility model.In the accompanying drawings:
Fig. 1 is the structural representation that the utility model air is optimized device;
The air of Fig. 2 the utility model Fig. 1 is optimized the structural representation of the distributing valve of device;
The structural representation of the spool of the distributing valve of Fig. 3 the utility model Fig. 2.
The specific embodiment
Below in conjunction with accompanying drawing preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein only is used for description and interpretation the utility model, and be not used in qualification the utility model.
As shown in Figure 1, a kind of air is optimized device, comprise the screen cloth 1 that connects successively, air compressor 2, chlorination equipment 3, decomposer 4, dust arrester 5 and wash mill 6, chlorination equipment 3, decomposer 4, dust arrester 5 and wash mill 6 are formed pretreatment system, this air is optimized device and is also comprised control system 13, checkout gear 14, distribution system 15, and the magnetic valve 7 that is connected with pretreatment unit, magnetic valve 7 is optimized branch road with the air of two parallel connections and is connected, the one branch road is established purifier, it comprises wash mill 11, adsorbent equipment 12, another branch road is established distributing valve, 2 components are from oxygen-increasing device molecular sieve tower 8 and negative oxygen ion generation device 9, and the exhaust outlet front end is provided with damping device 10; Checkout gear 14 is electrically connected with control system 13, and magnetic valve 7, air compressor 2, dust arrester 5, molecular sieve 8, negative oxygen ion generation device 9 are electrically connected with control system 13 respectively.
Controller is selected STC single-chip microcomputer or MSP430 single-chip microcomputer for use.Air compressor machine can be selected according to the interior space, is pressure 0.3～0.5MPa, the quiet oilless air compressor of capacity more than 110 liters.The molecular sieve high oxygen molecular sieve group of 5A, the optional specifications and models in market are more.Dedusting is with sack cleaner or HIROSS series 007-Q or P filter.Measuring-control of air is selected beam split digital display IAQ monitor for use.Above Equipment Market type kind religion is many, can select replacement as requested for use.
As shown in Figure 2, control system control motor, the running of motor-driven distributing valve.Distributing valve comprises cylindrical spool 71 and valve casing 72; Establish 2 groups of totally 6 through holes 73 on the cylindrical spool, 3 through holes, 73 corresponding 1 separation oxygen-increasing device unit of each group are molecular sieve tower 8, wherein the axis of one group 2 through holes 73 is parallel, and the axis of 1 through hole 73 and the axis of these 2 through holes 73 are square crossing in addition; The tubular body that valve casing 72 is and spool 71 mates is split 12 passages, cooperates the through hole 73 of spool 71 to use.When spool forwarded No. 1 molecular sieve tower position to, right-hand member 2 through holes 73 alignd with right-hand member 4 passages on the valve casing 72 and form two paths on the spool 71, and a path is given 1# molecular sieve inflation pressurization, and a route 1# molecular sieve is discharged oxygen.Simultaneously, left end 1 through hole 73 aligns with left end 2 passages on the valve casing 72 and forms the 3rd path on the spool 71, and Third Road is connected No. 2 molecular sieve towers, release pressure, discharges nitrogen.When spool 71 forwarded No. 2 molecular sieve tower positions to, No. 1 tower was discharged nitrogen, and No. 2 tower is discharged oxygen.Spool continues to rotate, and No. 1, No. 2 the molecular sieve tower alternately adds the oxygen of cutting down output, release denitrogen, continuous firing.
Sterilization, washing, humidification program are used special spiral valve gas scrubbing jar (having applied for a patent and obtained to award reason).Spiral valve gas scrubbing jar has the valve of making screw type around newel, when lighter gas feed irritate in during cleaning solution, bubble floating pastes surface helix rising under the valve.Spiral rises and has increased gas and cleaning solution contact-making surface, makes reaction more abundant, also can reduce noise.When heavier impurity is separated out, sink to the spiral downslide gradually of valve upper surface under the impurity.Because valve just in time separates gas and impurity,, make separation more abundant so reduced of the influence of come-up gas to sinking impurity.
After the start, air compressor machine or blower fan air supply, and pass through bactericidal unit successively, decomposer, dust arrester, wash mill etc., through magnetic valve, at this moment, the air quality analyzer is measured airborne oxygen content, and with transfer of data to control system, thereby the branch road of rational allocation air process: the oxygen content that (1) is measured when the air quality analyzer in the setting scope time (as more than 21%, below 25%), purify (as washing with magnetic valve guiding air, absorption) program, humidification (also can add useful smell of people etc.) is arranged at last to indoor again.(2) when air quality analyzer mensuration oxygen concentration (as less than 21%) when setting is following, carry out molecular sieve with magnetic valve guiding air and separate the oxygenation processing, distributing valve starts, molecular sieve is isolated oxygen and nitrogen, discharges such as nitrogen is outdoor, the oxygen input is indoor, thereby increase oxygen concentration, also can install animating electrode additional, produce negative oxygen ion isoreactivity composition, or install oxygen content that damping device (3) measures when the air quality analyzer additional greater than 25% the time, return program (1) with distributing valve guiding air.
Claims (6)
1. an air is optimized device, comprise the air-supply arrangement, the air pretreatment unit that connect successively, separate oxygen-increasing device, it is characterized in that: described air is optimized device and is also comprised control system, checkout gear, the magnetic valve that is connected with pretreatment unit, described checkout gear is electrically connected with control system, and described magnetic valve is electrically connected with control system; Described magnetic valve is also optimized branch road with the air of two parallel connections and is connected, and the one branch road is established purifier, and another branch road is established the separation oxygen-increasing device.
2. air according to claim 1 is optimized device, it is characterized in that: described air pretreatment unit is meant any or the combination arbitrarily in bactericidal unit, decomposer, dust arrester, the wash mill.
3. air according to claim 1 is optimized device, it is characterized in that: described separation oxygen-increasing device adopts molecular sieve.
4. air according to claim 1 is optimized device, and it is characterized in that: described purifier is washing tank and/or absorbent charcoal adsorber.
5. air according to claim 1 is optimized device, and it is characterized in that: establish distributing valve between described separation oxygen-increasing device and the magnetic valve, described distributing valve comprises cylindrical spool and valve casing; Establish through hole on the described cylindrical spool, its quantity is: each separates 3 of the through holes that dispersion is established in oxygen-increasing device unit, and wherein the axis of 2 through holes is parallel, and the axis of 1 through hole intersects at an angle with the axis of these 2 through holes in addition; Described valve casing is the tubular body that cooperates with spool, splits double passage in through hole.
6. air according to claim 5 is optimized device, it is characterized in that: the axis of 1 through hole in addition of described cylindrical spool and the axis of these 2 through holes are square crossing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201668652U CN201748566U (en) | 2010-04-22 | 2010-04-22 | Air optimization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201668652U CN201748566U (en) | 2010-04-22 | 2010-04-22 | Air optimization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201748566U true CN201748566U (en) | 2011-02-16 |
Family
ID=43583241
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201668652U Expired - Fee Related CN201748566U (en) | 2010-04-22 | 2010-04-22 | Air optimization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201748566U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102235724A (en) * | 2010-04-22 | 2011-11-09 | 陈曦 | Method and special device for air optimization |
-
2010
- 2010-04-22 CN CN2010201668652U patent/CN201748566U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102235724A (en) * | 2010-04-22 | 2011-11-09 | 陈曦 | Method and special device for air optimization |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 438000 Huanggang City, Hubei province Huangzhou District qingzhuanhu Road No. 186 (Ding Lihua court) 2-1101 Patentee after: Chen Xi Address before: 730000 Gansu province Lanzhou city Qilihe District Yan Ping Village 1 Beiyuan No. 2 (formerly 103) Patentee before: Chen Xi |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110216 Termination date: 20160422 |