CN202953821U - Medical oxygen source oxygen production system of controllable oxygen concentration - Google Patents
Medical oxygen source oxygen production system of controllable oxygen concentration Download PDFInfo
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- CN202953821U CN202953821U CN 201220556551 CN201220556551U CN202953821U CN 202953821 U CN202953821 U CN 202953821U CN 201220556551 CN201220556551 CN 201220556551 CN 201220556551 U CN201220556551 U CN 201220556551U CN 202953821 U CN202953821 U CN 202953821U
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Abstract
The utility model provides a medical oxygen source oxygen production system of controllable oxygen concentration. The medical oxygen source oxygen production system of the controllable oxygen concentration comprises a first oxygen production system and a second oxygen production system. The first oxygen production system and the second oxygen production system are respectively connected with an oxygen concentration controlling device. The medical oxygen source oxygen production system of the controllable oxygen concentration is simple in structure. The fact that the concentration prepared by an oxygen generator used in the present market can meet the requirements of the new standard is guaranteed. The concentration of the oxygen prepared by two sets of oxygen production system is controlled by one set of the oxygen concentration controlling device at the same time. The medical oxygen source oxygen production system of the controllable oxygen concentration is low in transforming cost and reasonable in layout. Space occupation of equipment is reduced.
Description
Technical field
The utility model relates to the medical facilities technical field, specifically a kind of medical oxygen source oxygen generation system of controlled oxygen gas concentration.
Background technology
The oxygenerator for preparing high-concentration oxygen is the indispensable medical facilities of hospital.At present, the oxygenerator of selling on market and hospital is used, be all generally that " the medical molecular sieve oxygen generation equipment current techique standard " come into effect on October 1st, 1998 carried out according to State Pharmaceutical Administration's issue.In this standard, the concentration of the oxygen of supplying with for the medical center oxygen generation system is defined as (93 ± 3) %.But in the recent period,, house and town and country construction section combine with State Administration for Quality Supervision and Inspection and Quarantine and have issued " the medical gas project technical specifications ", in 1 day August in 2012, come into effect.In this standard, the concentration of the oxygen of supplying with for the medical center oxygen generation system is defined as>=and 93%, with last standard, be enhanced.If, still use current oxygen generating plant, the oxygen of preparation obviously, its concentration is the requirement that can't meet new standard.If the technical specifications new according to this changed current used oxygen generating plant, its cost is also huge, is difficult to promotion and implementation in reality.
The utility model content
In view of the deficiencies in the prior art and defect, the purpose of this utility model is to provide a kind of medical oxygen source oxygen generation system of controlled oxygen gas concentration.
In order to achieve the above object, the utility model has adopted following technical scheme:
A kind of medical oxygen source oxygen generation system of controlled oxygen gas concentration, comprise oxygen generation system, and described oxygen generation system comprises the first oxygen generation system, the second oxygen generation system, and this first oxygen generation system, the second oxygen generation system are connected with the oxygen concentration control device respectively;
Described the first oxygen generation system comprises the first air compressor, the first cooling driers that pipeline connects, this first cooling driers is connected with the air storage tank pipeline, this triangular connecting pipeline is provided with filtration unit, and the first oxygenerator is connected on this air storage tank by pipeline;
Described the second oxygen generation system comprises the second air compressor, the second cooling driers that pipeline connects, this second cooling driers is connected with the air storage tank pipeline, this triangular connecting pipeline is provided with filtration unit, and the second oxygenerator is connected on this air storage tank by pipeline;
Described oxygen concentration control device comprises controller and gas circuit connection portion;
This gas circuit connection portion comprises: detect tank, it is connected with the first oxygenerator, the second oxygenerator respectively by pipeline, in this detection tank, is provided with the oxygen concentration analyser; The oxygen gas-holder, it is connected with this detection tank by pipeline, the aspirating pipeline that this oxygen gas-holder is provided with baroceptor and goes pipe network to be connected with oxygen, this aspirating pipeline is provided with air delivery valve and oxygen omnibus bar, and this air delivery valve is arranged between oxygen gas-holder and oxygen omnibus bar; This oxygen gas-holder also is connected with above-mentioned air storage tank pipeline, on its connecting pipeline, is provided with supercharger;
Described oxygen concentration analyser, baroceptor, air delivery valve, oxygen omnibus bar, supercharger are electrically connected to this controller respectively.
As optimal technical scheme of the present utility model: described filtration unit comprises grade one filter, secondary filter, tertiary filter; This grade one filter is separately positioned on the connecting pipeline between the first air compressor, the first cooling driers and the second air compressor, the second cooling driers between connecting pipeline on; This secondary filter, tertiary filter are successively set on respectively on the connecting pipeline between the first cooling driers and air storage tank and on the connecting pipeline between the second cooling driers and air storage tank.
As optimal technical scheme of the present utility model: described controller comprises programmable logic controller, and this programmable logic controller is provided with external power interface, control module, acoustic-optic alarm and control signal output interface; Switch power supply is electrically connected to this programmable logic controller respectively with data acquisition module, on this data acquisition module, is provided with analog input interface.
As optimal technical scheme of the present utility model: described data acquisition module is AD converter.
As optimal technical scheme of the present utility model: between described oxygen gas-holder and air delivery valve, be provided with sterilizing filter.
As optimal technical scheme of the present utility model: described detection tank is provided with baroceptor, and it is electrically connected to this controller.
As optimal technical scheme of the present utility model: described oxygen gas-holder is provided with air pressure overload protection valve, and this air pressure overload protection valve is electrically connected to this controller.
Compared with prior art, the utility model is simple in structure, can guarantee that the concentration of oxygen prepared by oxygenerator that existing market is used reaches the requirement of new criteria; Simultaneously, the concentration of the oxygen that uses a set of oxygen concentration control device control two cover oxygen generation systems to prepare, improvement cost is cheap, rationally distributed, reduces taking up room of equipment.
The accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The structural representation that Fig. 2 is the utility model middle controller.
The electric control theory figure that Fig. 3 is the utility model middle controller.
Embodiment
Refer to Fig. 1, the medical oxygen source oxygen generation system of controlled oxygen gas concentration comprises the first oxygen generation system, the second oxygen generation system, and this first oxygen generation system, the second oxygen generation system are connected with the oxygen concentration control device respectively.
Described the first oxygen generation system comprises the first air compressor 401, the first cooling driers 501 that pipeline connects, and this first cooling driers 501 is connected with air storage tank 209 pipelines, and this triangular connecting pipeline is provided with filtration unit; This filtration unit comprises grade one filter 301, secondary filter 302 and tertiary filter 303.This grade one filter 301 is arranged on the connecting pipeline between the first air compressor 401, the first cooling driers 501; This secondary filter 302, tertiary filter 303 are successively set on respectively on the connecting pipeline between the first cooling driers 501 and air storage tank 209.The first oxygenerator 601 is connected on this air storage tank 209 by pipeline.
Described the second oxygen generation system comprises the second air compressor 402, the second cooling driers 502 that pipeline connects, and this second cooling driers 502 is connected with air storage tank 209 pipelines, and this triangular connecting pipeline is provided with filtration unit; This filtration unit comprises grade one filter 301, secondary filter 302, tertiary filter 303.This grade one filter 301 is arranged on the connecting pipeline between the second air compressor 402, the second cooling driers 502; This secondary filter 302, tertiary filter 303 are successively set on the connecting pipeline between the second cooling driers 502 and air storage tank 209.The second oxygenerator 602 is connected on this air storage tank 209 by pipeline.
Described oxygen concentration control device comprises controller 10 and gas circuit connection portion.
Refer to Fig. 2 and Fig. 3, this controller 10 comprises programmable logic controller 101, and this programmable logic controller 101 is provided with external power interface 102, for connecting the AC220V power supply; Control module 103, as panel push button etc., for setting controller 10; Acoustic-optic alarm 106 and control signal output interface 107; And the switch power supply 105 and data acquisition module 104 that with programmable logic controller 101, are electrically connected to; Switch power supply 105 is used to instrument that the working power of DC24V is provided; Data acquisition module 104 is provided with analog input interface 108, for gathering simulating signal, and this analog signal conversion is become to the data storage cell of digital data transmission to programmable logic controller 101.In the present embodiment, this data acquisition module 104 is AD converter.
Please again consult Fig. 1, described gas circuit connection portion comprises: detect tank 201, it is connected with the first oxygenerator 601, the second oxygenerator 602 that oxygen source is provided respectively by pipeline, is provided with oxygen concentration analyser (not shown) in this detection tank 201; Oxygen gas-holder 203, it is connected with this detection tank 201 by pipeline, the aspirating pipeline 206 that this oxygen gas-holder 203 is provided with the baroceptor (not shown) and goes pipe network 205 to be connected with oxygen, this aspirating pipeline 206 is provided with air delivery valve 207 and oxygen omnibus bar 208, and this air delivery valve 207 is arranged between oxygen gas-holder 203 and oxygen omnibus bar 208; This oxygen gas-holder 203 also is connected with above-mentioned air storage tank 209 pipelines, is provided with supercharger 210 on its connecting pipeline.
Described oxygen concentration analyser, baroceptor, air delivery valve 207, oxygen omnibus bar 208, supercharger 210 are electrically connected to this controller 10 respectively.
The oxygen concentration analyser detects the oxygen concentration in tank 201 for Real-Time Monitoring, and sends the oxygen concentration simulating signal to controller 10.
Baroceptor is for the atmospheric pressure value in Real-Time Monitoring oxygen gas-holder 203, and feedback pressure signal is to controller 10.In specific implementation process, for improving the stability of system, also be provided with the baroceptor (not shown) be electrically connected to controller 10 on described detection tank 201, this baroceptor is spare part; When the baroceptor on oxygen gas-holder 203 damages, the baroceptor detected on tank 201 can be worked voluntarily, to guarantee system stable operation.Simultaneously; also be provided with air pressure overload protection valve (not shown) on described oxygen gas-holder 203; this air pressure overload protection valve is electrically connected to this controller 10; atmospheric pressure value in oxygen gas-holder 203 is during higher than safety value; controller 10 sends opening signal and opens this air pressure overload protection valve; reduce the air pressure in oxygen gas-holder 203, prevent the generation of security incident.
What this system provided is medical oxygen source, for improving the degree of cleaning of oxygen source, between described oxygen gas-holder 203 and air delivery valve 207, is provided with sterilizing filter 214.
When the first oxygen generation system, the second oxygen generation system work, air in atmosphere is respectively after the first air compressor 401, the second air compressor 402 compressions, after removing most of water or mist of oil by grade one filter 301, enter respectively again the first cooling driers 501, the second cooling driers 502 is cooling, make the vaporous water molecule in pressurized air further be liquefied as liquid state water, after the first cooling driers 501, the second cooling driers 502 self dewater, the remaining micro-moisture of air is further removed airborne moisture through second, third grade of strainer 302,303.Water content very low (approximate dry air) in air now, air after treatment enters air storage tank 209 for the first oxygenerator 601, the second oxygenerator 602.
The first oxygenerator 601, the second oxygenerator 602 are made respectively oxygen, and by pipeline by oxygen delivery to detecting tank 201 and oxygen gas-holder 203, the oxygen concentration analyser detected in tank 201 carries out Real-Time Monitoring to the concentration of oxygen, and sends the oxygen concentration simulating signal to controller 10.
As the concentration of oxygen reaches oxygen concentration set(ting)value 93.2%, controller 10 output opening signals are to the air delivery valve 207 arranged on the aspirating pipeline 206 of oxygen gas-holder 203, air delivery valve 207 is opened, and the oxygen in oxygen gas-holder 203 is delivered to oxygen through aspirating pipeline 206 and removes pipe network 205.
As the concentration of oxygen does not reach oxygen concentration set(ting)value 93.2%, controller 10 output closure signal, opening signal are respectively to the air delivery valve 207 and oxygen omnibus bar 208 that arrange on the aspirating pipeline 206 of oxygen gas-holder 203; Air delivery valve 207 is closed, and oxygen gas-holder 203 stops removing pipe network 205 air feed to oxygen; And oxygen omnibus bar 208 is opened, by oxygen omnibus bar 208, to oxygen, go pipe network 205 to provide concentration oxygen up to standard.
Use oxygen safety for what guarantee that oxygen removes pipe network 205, by oxygen omnibus bar 208 air feed the time, oxygen omnibus bar 208 Real-time Feedback air pressure signals are to controller 10; Atmospheric pressure value in oxygen omnibus bar 208 is during lower than threshold value, controller 10 output shutdown signals with opening signal respectively to oxygen omnibus bar 208 and air delivery valve 207; Oxygen omnibus bar 208 is closed, and air delivery valve 207 is opened, and oxygen gas-holder 203 normally removes pipe network 205 air feed to oxygen, until the atmospheric pressure value in oxygen omnibus bar 208 is higher than threshold value; Then, then by controller 10 output closure signal with opening signal respectively to air delivery valve 207 and oxygen omnibus bar 208, air delivery valve 207 is closed, oxygen omnibus bar 208 is reworked.
When air delivery valve 207 is closed, oxygen gas-holder 203 raises with the air pressure detected in tank 201, and by its atmospheric pressure value of baroceptor Real-Time Monitoring on oxygen gas-holder 203; Air pressure raises, and in air, nitrogen partial pressure increases, and the molecular sieve in oxygenerator is easier to absorb nitrogen, the corresponding rising of the concentration of the oxygen of preparing;
As oxygen concentration reaches oxygen concentration set(ting)value 93.2%, controller 10 output opening signals, shutdown signal are respectively to air delivery valve 207 and oxygen omnibus bar 208; Air delivery valve 207 is opened, and the normal air feed of oxygen gas-holder to oxygen removes pipe network 205; And oxygen omnibus bar 208 is closed;
As the air pressure at oxygen gas-holder 203 is increased to first threshold, the HVT high voltage threshold that this first threshold is oxygen gas-holder 203, and when oxygen concentration does not return to oxygen concentration set(ting)value 93.2% yet, controller 10 output opening signals are to the supercharger 210 of being located between oxygen gas-holder 203 and air storage tank 209, supercharger 210 work, the gas extraction that oxygen concentration in oxygen gas-holder 203 is below standard is to air storage tank 209, and is back to the first oxygenerator 601, the second oxygenerator 602 oxygen again; Because the concentration of oxygen the gas that is back to oxygenerator from air storage tank 209 is higher, after the first oxygenerator 601, the second oxygenerator 602 oxygen again, the concentration of the oxygen of output can be gone up fast to oxygen concentration set(ting)value 93.2%.When supercharger 210 work, when the air pressure of oxygen gas-holder 203 is reduced to Second Threshold, the low pressure threshold that this Second Threshold is oxygen gas-holder 203, controller 10 output shutdown signals are to supercharger 210, supercharger 210 quits work, when the air pressure of oxygen gas-holder 203 is increased to first threshold, supercharger is reworked, until the concentration of the oxygen of the first oxygenerator 601, the second oxygenerator 602 preparations reaches oxygen concentration set(ting)value 93.2%.
The foregoing is only preferred embodiment of the present utility model, not be used for limiting practical range of the present utility model; Every equivalence of doing according to the utility model changes and revises, and all by the scope of the utility model claims, is covered.
Claims (7)
1. the medical oxygen source oxygen generation system of a controlled oxygen gas concentration, comprise oxygen generation system, it is characterized in that: described oxygen generation system comprises the first oxygen generation system, the second oxygen generation system, and this first oxygen generation system, the second oxygen generation system are connected with the oxygen concentration control device respectively;
Described the first oxygen generation system comprises the first air compressor, the first cooling driers that pipeline connects, this first cooling driers is connected with the air storage tank pipeline, this triangular connecting pipeline is provided with filtration unit, and the first oxygenerator is connected on this air storage tank by pipeline;
Described the second oxygen generation system comprises the second air compressor, the second cooling driers that pipeline connects, this second cooling driers is connected with the air storage tank pipeline, this triangular connecting pipeline is provided with filtration unit, and the second oxygenerator is connected on this air storage tank by pipeline;
Described oxygen concentration control device comprises controller and gas circuit connection portion;
This gas circuit connection portion comprises: detect tank, it is connected with the first oxygenerator, the second oxygenerator respectively by pipeline, in this detection tank, is provided with the oxygen concentration analyser; The oxygen gas-holder, it is connected with this detection tank by pipeline, the aspirating pipeline that this oxygen gas-holder is provided with baroceptor and goes pipe network to be connected with oxygen, this aspirating pipeline is provided with air delivery valve and oxygen omnibus bar, and this air delivery valve is arranged between oxygen gas-holder and oxygen omnibus bar; This oxygen gas-holder also is connected with above-mentioned air storage tank pipeline, on its connecting pipeline, is provided with supercharger;
Described oxygen concentration analyser, baroceptor, air delivery valve, oxygen omnibus bar, supercharger are electrically connected to this controller respectively.
2. the medical oxygen source oxygen generation system of controlled oxygen gas concentration according to claim 1, it is characterized in that: described filtration unit comprises grade one filter, secondary filter, tertiary filter; This grade one filter is separately positioned on the connecting pipeline between the first air compressor, the first cooling driers and the second air compressor, the second cooling driers between connecting pipeline on; This secondary filter, tertiary filter are successively set on respectively on the connecting pipeline between the first cooling driers and air storage tank and on the connecting pipeline between the second cooling driers and air storage tank.
3. the medical oxygen source oxygen generation system of controlled oxygen gas concentration according to claim 1, it is characterized in that: described controller comprises programmable logic controller, and this programmable logic controller is provided with external power interface, control module, acoustic-optic alarm and control signal output interface; Switch power supply is electrically connected to this programmable logic controller respectively with data acquisition module, on this data acquisition module, is provided with analog input interface.
4. the medical oxygen source oxygen generation system of controlled oxygen gas concentration according to claim 3, it is characterized in that: described data acquisition module is AD converter.
5. the medical oxygen source oxygen generation system of controlled oxygen gas concentration according to claim 1, is characterized in that: between described oxygen gas-holder and air delivery valve, be provided with sterilizing filter.
6. the medical oxygen source oxygen generation system of controlled oxygen gas concentration according to claim 1, it is characterized in that: described detection tank is provided with baroceptor, and it is electrically connected to this controller.
7. the medical oxygen source oxygen generation system of controlled oxygen gas concentration according to claim 1, it is characterized in that: described oxygen gas-holder is provided with air pressure overload protection valve, and this air pressure overload protection valve is electrically connected to this controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220556551 CN202953821U (en) | 2012-10-26 | 2012-10-26 | Medical oxygen source oxygen production system of controllable oxygen concentration |
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| Application Number | Priority Date | Filing Date | Title |
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| CN 201220556551 CN202953821U (en) | 2012-10-26 | 2012-10-26 | Medical oxygen source oxygen production system of controllable oxygen concentration |
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| CN202953821U true CN202953821U (en) | 2013-05-29 |
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| CN 201220556551 Expired - Lifetime CN202953821U (en) | 2012-10-26 | 2012-10-26 | Medical oxygen source oxygen production system of controllable oxygen concentration |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103879966A (en) * | 2014-01-23 | 2014-06-25 | 中山和佳医疗科技有限公司 | Variable frequency supercharging system and oxygen preparation system |
| CN104310315A (en) * | 2014-10-09 | 2015-01-28 | 吉林市卓欣康泰医疗科技有限公司 | Oxygen generation system for medical center and using method thereof |
| CN106198116A (en) * | 2015-05-06 | 2016-12-07 | 王勤 | A kind of medical oxygen concentration sampling equipment |
| CN109613859A (en) * | 2018-12-06 | 2019-04-12 | 深圳市德达康健股份有限公司 | A kind of molecular-sieve oxygen generator and its control system, method |
-
2012
- 2012-10-26 CN CN 201220556551 patent/CN202953821U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103879966A (en) * | 2014-01-23 | 2014-06-25 | 中山和佳医疗科技有限公司 | Variable frequency supercharging system and oxygen preparation system |
| CN104310315A (en) * | 2014-10-09 | 2015-01-28 | 吉林市卓欣康泰医疗科技有限公司 | Oxygen generation system for medical center and using method thereof |
| CN106198116A (en) * | 2015-05-06 | 2016-12-07 | 王勤 | A kind of medical oxygen concentration sampling equipment |
| CN109613859A (en) * | 2018-12-06 | 2019-04-12 | 深圳市德达康健股份有限公司 | A kind of molecular-sieve oxygen generator and its control system, method |
| CN109613859B (en) * | 2018-12-06 | 2021-12-28 | 深圳市德达医疗科技集团有限公司 | Molecular sieve oxygen generator and control system and method thereof |
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Granted publication date: 20130529 |
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