CN203095618U - Medical molecular sieve oxygen preparing system - Google Patents
Medical molecular sieve oxygen preparing system Download PDFInfo
- Publication number
- CN203095618U CN203095618U CN 201320127499 CN201320127499U CN203095618U CN 203095618 U CN203095618 U CN 203095618U CN 201320127499 CN201320127499 CN 201320127499 CN 201320127499 U CN201320127499 U CN 201320127499U CN 203095618 U CN203095618 U CN 203095618U
- Authority
- CN
- China
- Prior art keywords
- tower
- oxygen
- valve
- control valve
- molecular sieve
- 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.)
- Expired - Lifetime
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- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 64
- 239000001301 oxygen Substances 0.000 title claims abstract description 64
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 64
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 11
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 11
- 238000001816 cooling Methods 0.000 claims description 11
- 230000000844 anti-bacterial effect Effects 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 239000002912 waste gas Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 abstract description 3
- 238000005057 refrigeration Methods 0.000 abstract 2
- 239000000428 dust Substances 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 238000001514 detection method Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 230000003749 cleanliness Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002640 oxygen therapy Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000011146 sterile filtration Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
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- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model relates to a medical molecular sieve oxygen preparing system which comprises an air compressor (1) connected with a refrigeration dryer (12), wherein the refrigeration dryer (2) is connected with an air balancing tank (3) which is respectively connected with an efficient filter, an ultra-fine filter and an oil removing filter; the oil removing filter is connected with an oxygen generator (4) through a control valve; the oxygen generator (4) comprises a tower A (4-1), the exhaust valve of which is connected with an oxygen balancing tank (5) through a control valve; the tower A (4-1) is further connected with a tower B (4-2) through a blowback valve; a pressure equalizing valve is further installed between the tower A (4-1) and the tower B (4-2); the exhaust valve of the tower B (4-2) is further connected with the oxygen balancing tank (5) through a control valve; and the oxygen balancing tank (5) is further connected with a degerming device. The oxygen preparing system adopts a multistage filtering system to meet the standard of no oil and no dust, so that the cleanness and purity of oxygen sources are ensured.
Description
Technical field
Utility model relates to a kind of medical molecular sieve oxygen generation system.
Background technology
Traditional hospital's oxygen supply mode is oxygen cylinder to be transported to the ward patient is carried out oxygen supply, and this mode is not only clumsy, has also increased medical personnel's labour intensity, and oxygen cylinder belongs to high pressure vessel in addition, has potential safety hazard.
Though medical institutions' concentrated oxygen supply mode has overcome the loaded down with trivial details shortcoming of carrying oxygen cylinder, and solved the problem that in ward placement force container brings potential safety hazard, but the oxygen supply quality does not often reach the use standard, and the pipeline oxygen therapy of long distance can bring secondary pollution, and the supply safety of medical oxygen still is difficult to ensure.
The utility model content
Technical problem to be solved in the utility model is, a kind of medical molecular sieve oxygen generation system is provided, and can provide does not have oily, dustless, dry and aseptic medical oxygen.To overcome the defective of existing medical oxygen plenum system.
It is as follows that the utility model solves the problems of the technologies described above the technical scheme that is adopted:
Medical molecular sieve oxygen generation system, it is characterized in that: comprise air compressor, air compressor is connected with cooling driers by the main line strainer, and cooling driers is connected with the air balance jar, and the air balance jar is connected with high efficiency filter, super fine filter, oil removal filter respectively; Wherein oil removal filter is connected with oxygen generator by control valve, oxygen generator comprises the A tower, the vent valve of A tower is connected with the oxygen surge tank by control valve, the A tower also is connected with the B tower by the blowback valve, between A tower and the B tower equalizing valve is installed also, the vent valve of B tower also connects described oxygen surge tank by control valve; The oxygen surge tank also is connected with bactericidal device.
A tower and B tower also are connected with the sound damper that is used for discharging waste gas respectively.
Also comprise the PLC automatic control device, the PLC automatic control device respectively with described air compressor, cooling driers, the air balance jar, oxygen generator and oxygen surge tank are electrically connected; The PLC automatic control device also respectively with described control valve, described vent valve is electrically connected.
Positively effect of the present utility model is:
By control and detection system, make air compressor, cooling driers, oxygen generator collaborative work, produce safely, totally meet the pure source of oxygen that patient uses.System features in convenient alleviates medical personnel's labour intensity.
Medical molecular sieve oxygen generation system, system oxygen main frame adopts the cascade filtration system, and reaching does not have the dustless standard of oil, guarantees the cleanliness factor and the purity of source of oxygen.
The use of oxygen surge tank, the one, store oxygen, the 2nd, make oxygen reach the pressure of transport pipe, make the terminal oxygen pressure reach the use standard.
Control and detection system adopts PLC to control automatically, and is simple to operate, guaranteed the safe operation of oxygen generation system.
Description of drawings
Accompanying drawing 1 explanation structural representation of the present utility model.
Embodiment
Further specify the utility model below in conjunction with the drawings and specific embodiments.
The utility model comprises air compressor 1, and air compressor 1 is connected with cooling driers 2 by the main line strainer, and cooling driers 2 is connected with air balance jar 3, and air balance jar 3 is connected with high efficiency filter, super fine filter and oil removal filter respectively.Wherein oil removal filter is connected with oxygen generator 4 by control valve, oxygen generator 4 comprises the A tower 4-1 that is used for absorbed air nitrogen, the vent valve of A tower 4-1 is connected with oxygen surge tank 5 by control valve, A tower 4-1 also is connected with the B tower 4-2 of the nitrogen that is used to purge its absorption of desorb by the blowback valve, between A tower 4-1 and the B tower 4-2 equalizing valve is installed also, the vent valve of B tower 4-2 also connects described oxygen surge tank 5 by control valve; A tower 4-1 and B tower 4-2 also are connected with the sound damper that is used for discharging waste gas respectively.Oxygen surge tank 5 also is connected with bactericidal device.
When the utility model uses, air is after air compressor 1 compression, through oily water separation and the pre-filtering of main line strainer, remove impurity, enter cooling driers 2 drying that further dewaters then, pressurized air enters air balance jar 3, pass through high efficiency filter again, the processing of super fine filter and oil removal filter, there is not oil, dustless, after exsiccant pressurized air carries out voltage regulation of voltage regulation by control valve, enter A tower 4-1, molecular sieve adsorption in the A tower 4-1 is fallen airborne nitrogen, and the oxygen major part that is not adsorbed enters oxygen surge tank 5 through control valve, small portion oxygen enters B tower 4-2 through the blowback valve, purges the nitrogen of its absorption of desorb, through control valve, the sound damper emptying.A tower 4-1 absorption equalizing valve when saturated is opened, and the gas of A tower 4-1 enters B tower 4-2, two pressure tower equilibriums, this moment, A tower 4-1 vent valve was opened, and gas is through the sound damper emptying in the A tower 4-1, and B tower 4-2 air inlet absorption simultaneously, desorb, equal crush-cutting change, step above repeating so constantly produces oxygen.The oxygen that oxygen surge tank 5 comes out is through further Sterile Filtration, and the standard patients that reaches medical oxygen fully uses.
The utility model also comprises the PLC automatic control device, the PLC automatic control device respectively with described air compressor 1, cooling driers, air balance jar 3, oxygen generator 4 and oxygen surge tank 5 is electrically connected, the PLC automatic control device also respectively with described control valve, described vent valve is electrically connected.
Claims (3)
1. medical molecular sieve oxygen generation system, it is characterized in that: comprise air compressor (1), air compressor (1) is connected with cooling driers (2) by the main line strainer, cooling driers (2) is connected with air balance jar (3), and air balance jar (3) is connected with high efficiency filter, super fine filter, oil removal filter respectively; Wherein oil removal filter is connected with oxygen generator (4) by control valve, oxygen generator (4) comprises A tower (4-1), the vent valve of A tower (4-1) is connected with oxygen surge tank (5) by control valve, A tower (4-1) also is connected with B tower (4-2) by the blowback valve, between A tower (4-1) and the B tower (4-2) equalizing valve is installed also, the vent valve of B tower (4-2) also connects described oxygen surge tank (5) by control valve; Oxygen surge tank (5) also is connected with bactericidal device.
2. medical molecular sieve oxygen generation as claimed in claim 1 system, it is characterized in that: A tower (4-1) and B tower (4-2) also are connected with the sound damper that is used for discharging waste gas respectively.
3. medical molecular sieve oxygen generation as claimed in claim 1 or 2 system, it is characterized in that: also comprise the PLC automatic control device, the PLC automatic control device respectively with described air compressor (1), cooling driers (2), air balance jar (3), oxygen generator (4) and oxygen surge tank (5) are electrically connected; The PLC automatic control device also respectively with described control valve, described vent valve is electrically connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320127499 CN203095618U (en) | 2013-03-20 | 2013-03-20 | Medical molecular sieve oxygen preparing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320127499 CN203095618U (en) | 2013-03-20 | 2013-03-20 | Medical molecular sieve oxygen preparing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203095618U true CN203095618U (en) | 2013-07-31 |
Family
ID=48847037
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320127499 Expired - Lifetime CN203095618U (en) | 2013-03-20 | 2013-03-20 | Medical molecular sieve oxygen preparing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203095618U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109084099A (en) * | 2018-08-20 | 2018-12-25 | 安徽国科生物科技有限公司 | Accurate oxygen oxygen system processed |
-
2013
- 2013-03-20 CN CN 201320127499 patent/CN203095618U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109084099A (en) * | 2018-08-20 | 2018-12-25 | 安徽国科生物科技有限公司 | Accurate oxygen oxygen system processed |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Monitor for integrated parameters of medical molecular sieve oxygen generation system Effective date of registration: 20150707 Granted publication date: 20130731 Pledgee: Silicon Valley Bank Co.,Ltd. Pledgor: YANTAI BEACON MEDICAL SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: 2015310000026 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 264004, Che 8 Road, Wolong Economic Zone, Zhifu District, Shandong, Yantai Patentee after: YANTAI BEACON MEDICAL TECHNOLOGY Co.,Ltd. Address before: 264004, Che 8 Road, Wolong Economic Zone, Zhifu District, Shandong, Yantai Patentee before: YANTAI BEACON MEDICAL SCIENCE & TECHNOLOGY Co.,Ltd. |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PM01 | Change of the registration of the contract for pledge of patent right |
Change date: 20160301 Registration number: 2015310000026 Pledgor after: YANTAI BEACON MEDICAL TECHNOLOGY Co.,Ltd. Pledgor before: YANTAI BEACON MEDICAL SCIENCE & TECHNOLOGY Co.,Ltd. |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20180309 Granted publication date: 20130731 Pledgee: Silicon Valley Bank Co.,Ltd. Pledgor: YANTAI BEACON MEDICAL TECHNOLOGY Co.,Ltd. Registration number: 2015310000026 |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: No.8 cheshan Road, Zhifu District, Yantai City, Shandong Province Patentee after: Huasheng Medical Technology Co.,Ltd. Address before: 264004 No.8 cheshan Road, Wolong economic Park, Zhifu District, Yantai City, Shandong Province Patentee before: YANTAI BEACON MEDICAL TECHNOLOGY Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130731 |