CN216005217U - Energy-saving application equipment for combined membrane oxygen generation - Google Patents

Energy-saving application equipment for combined membrane oxygen generation Download PDF

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Publication number
CN216005217U
CN216005217U CN202122686865.6U CN202122686865U CN216005217U CN 216005217 U CN216005217 U CN 216005217U CN 202122686865 U CN202122686865 U CN 202122686865U CN 216005217 U CN216005217 U CN 216005217U
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pipeline
oxygen
energy
module
oxygen generation
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CN202122686865.6U
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蔡纵
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HANGZHOU KELIN AIER QIYUAN EQUIPMENT CO Ltd
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HANGZHOU KELIN AIER QIYUAN EQUIPMENT CO Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
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Abstract

The utility model discloses an energy-conserving application apparatus of combination membrane system oxygen relates to system oxygen equipment field, including the air compressor machine, the lateral wall of air compressor machine is provided with first entry and first export, and first exit is connected with first pipeline, and first pipe connection has dry module, and dry module is connected with the second pipeline, and the second pipe connection has the oxygen boosting module, and the oxygen boosting module is connected with the third pipeline, and the third pipe connection has the booster compressor, and the booster compressor is provided with second entry and second export, and the third pipeline is connected with the second entry, and the second exit of booster compressor is connected with the oxygen output tube. The utility model discloses an adopt the combination of dry membrane and oxygen generation membrane to use, and quote the waste gas of unloading and carry out the dewatering of dry membrane for electric energy and effectual gas consumption that do not consume in purification and oxygen generation link, thereby obtain the most energy-conserving effect of optimization, and use dry + oxygen generation membrane, small, easily installation does not consume any electric energy, gas consumption, and no fault point, sustainable steady operation.

Description

Energy-saving application equipment for combined membrane oxygen generation
Technical Field
The utility model relates to an oxygen generating equipment field, in particular to energy-saving application equipment for combined membrane oxygen generation.
Background
The current oxygen generation methods mainly comprise three types: the method comprises the following steps of cryogenic liquefaction, pressure swing adsorption and membrane separation oxygen generation, wherein membrane oxygen generation is widely applied to the fields of combustion supporting, vehicle-mounted and civil use due to the characteristics of safety, reliability, small volume, convenience in movement, no need of installation, simplicity in operation and the like, the flow of any oxygen generation mode is basically the same, and 1, an air compressor provides a stable air source with a certain flow and a certain pressure; 2. the compressed air purification system consisting of the drying device and the filter provides clean compressed air, and the oxygen generation device separates oxygen in the air to obtain oxygen with certain purity.
The purification used at present: a cooling and drying machine: the power consumption, the volume is large, the miniaturization cannot be realized, and the number of faults is relatively large; a suction dryer: the power consumption or the gas consumption, large volume, no miniaturization and relatively more faults.
Therefore, it is necessary to develop an energy-saving application apparatus for combined membrane oxygen production to solve the above problems.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an energy-conserving application apparatus of combination membrane system oxygen to solve the purification of the present use that proposes in the above-mentioned background art: a cooling and drying machine: the power consumption, the volume is large, the miniaturization cannot be realized, and the number of faults is relatively large; a suction dryer: the problems of electric energy or gas consumption, large volume, no miniaturization and relatively more faults.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides an energy-conserving application apparatus of combination membrane system oxygen, includes the air compressor machine, the lateral wall of air compressor machine is provided with first entry and first export, and first exit is connected with first pipeline, first pipe connection has dry module, dry module is connected with the second pipeline, the second pipe connection has the oxygen boosting module, the oxygen boosting module is connected with the third pipeline, the third pipe connection has the booster compressor, the booster compressor is provided with second entry and second export, third pipeline and second entry linkage, the second exit of booster compressor is connected with the oxygen output tube.
Preferably, the drying module is provided with a third inlet and a third outlet, the oxygen enrichment module is connected with a fourth pipeline, and the fourth pipeline is connected with the third inlet of the drying module.
Preferably, the outer wall of the fourth pipeline is connected with a pressure gauge.
Preferably, the outer wall of the fourth pipeline is provided with a flow regulating valve.
Preferably, the outer walls of the first pipeline and the oxygen output pipe are both provided with control valves.
Preferably, the outer wall of the first pipeline is provided with a multi-stage filter.
The utility model discloses a technological effect and advantage:
the compressed air in the first pipeline is controlled by using a control valve, the compressed air in the first pipeline enters a drying module to be dried, the dried compressed air is conveyed to a second pipeline and then enters an oxygen enrichment module by using the second pipeline, the oxygen enrichment module conveys waste gas into a fourth pipeline, the emptied waste gas is introduced to carry out dehydration of the drying module, so that the electric energy and the effective gas consumption which are not consumed in purification and oxygen generation in a link are realized, the optimal most energy-saving effect is obtained, the dehydration is realized by using an outlet on the drying module, a pressure gauge is used for detecting the pressure in the fourth pipeline, the flow of the waste gas in the fourth pipeline is controlled by using a flow regulating valve, the dried compressed air enters the oxygen enrichment module and then enters a supercharger by using a third pipeline, and finally, outputting oxygen by using an oxygen output pipe, and by adopting the combined application of the drying membrane and the oxygen generation membrane and introducing the emptied waste gas to remove water from the drying membrane, the electric energy and the effective gas consumption which are not consumed in the purification and oxygen generation links are realized, so that the optimal most energy-saving effect is obtained, and the drying and oxygen generation membrane is used, has small volume, is easy to install, does not consume any electric energy and gas consumption, has no fault point, and can continuously and stably operate.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention;
fig. 2 is a schematic structural diagram of the drying module of the present invention.
In the figure: 1. an air compressor; 2. a first conduit; 3. a drying module; 4. a second conduit; 5. an oxygen enrichment module; 6. a third pipeline; 7. a supercharger; 8. an oxygen output pipe; 9. a fourth conduit; 10. a pressure gauge; 11. a flow regulating valve; 12. a control valve; 13. a multi-stage filter.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
The utility model provides an energy-conserving application apparatus of membrane system oxygen as shown in fig. 1-2, including air compressor machine 1, air compressor machine 1's lateral wall is provided with first entry and first export, and first exit is connected with first pipeline 2, first pipeline 2 is connected with dry module 3, dry module 3 is connected with second pipeline 4, second pipeline 4 is connected with oxygen boosting module 5, oxygen boosting module 5 is connected with third pipeline 6, third pipeline 6 is connected with booster compressor 7, booster compressor 7 is provided with second entry and second export, third pipeline 6 and second entry linkage, booster compressor 7's second exit is connected with oxygen output tube 8, and is small, easily install, do not consume any electric energy, the gas consumption, and no fault point, sustainable steady operation.
Simultaneously, drying module 3 is provided with third entry and third export, and oxygen boosting module 5 is connected with fourth pipeline 9, and fourth pipeline 9 and drying module 3's third entry are connected, can conveniently quote the waste gas of unloading and carry out drying module 3's dewatering for electric energy and effectual gas consumption that do not consume in purification and system oxygen link, thereby obtain the most energy-conserving effect of optimization.
In addition, the outer wall of the fourth pipeline 9 is connected with a pressure gauge 10, so that the pressure in the fourth pipeline 9 can be conveniently detected.
Next, the flow rate control valve 11 is provided on the outer wall of the fourth pipe 9, and the flow rate of the exhaust gas in the fourth pipe 9 can be easily controlled.
More specifically, the outer walls of the first pipeline 2 and the oxygen output pipe 8 are provided with control valves 12, so that the air entering and the oxygen output can be conveniently controlled.
It should be further noted that the outer wall of the first pipeline 2 is provided with a multi-stage filter 13, so as to conveniently filter the air compressed by the air compressor 1.
The utility model discloses the theory of operation:
the air compressor 1 is used for compressing air, the compressed air is conveyed into the first pipeline 2, the control valve 12 is used for controlling the compressed air in the first pipeline 2, the compressed air in the first pipeline 2 enters the drying module 3 for drying, the dried compressed air is conveyed into the second pipeline 4 and then enters the oxygen enrichment module 5 through the second pipeline 4, the oxygen enrichment module 5 conveys waste gas into the fourth pipeline 9, the emptied waste gas is introduced for dewatering of the drying module 3, so that electric energy and effective gas consumption which are not consumed in a purification and oxygen generation link are realized, the optimal energy-saving effect is obtained, the outlet on the drying module 3 is used for dewatering, the pressure in the fourth pipeline 9 is detected by using the pressure gauge 10, and the flow of the waste gas in the fourth pipeline 9 is controlled by using the flow regulating valve 11, the dried compressed gas enters the oxygen enrichment module 5 and then enters the supercharger 7 through the third pipeline 6, and finally the oxygen is output through the oxygen output pipe 8.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications and variations can be made in the embodiments or in part of the technical features of the embodiments without departing from the spirit and the scope of the invention.

Claims (6)

1. The utility model provides an energy-conserving application apparatus of combination membrane system oxygen which characterized in that: including the air compressor machine, the lateral wall of air compressor machine is provided with first entry and first export, and first exit is connected with first pipeline, first pipe connection has dry module, dry module is connected with the second pipeline, the second pipe connection has the oxygen boosting module, the oxygen boosting module is connected with the third pipeline, the third pipe connection has the booster compressor, the booster compressor is provided with the second and enters the mouth and the export of second, the third pipeline is connected with the second entry, the second exit of booster compressor is connected with the oxygen output tube.
2. The energy-saving application equipment of combined membrane oxygen generation according to claim 1, characterized in that: the drying module is provided with a third inlet and a third outlet, the oxygen enrichment module is connected with a fourth pipeline, and the fourth pipeline is connected with the third inlet of the drying module.
3. The energy-saving application equipment of combined membrane oxygen generation according to claim 2, characterized in that: and the outer wall of the fourth pipeline is connected with a pressure gauge.
4. The energy-saving application equipment of combined membrane oxygen generation according to claim 2, characterized in that: and a flow regulating valve is arranged on the outer wall of the fourth pipeline.
5. The energy-saving application equipment of combined membrane oxygen generation according to claim 1, characterized in that: the outer walls of the first pipeline and the oxygen output pipe are provided with control valves.
6. The energy-saving application equipment of combined membrane oxygen generation according to claim 1, characterized in that: the outer wall of the first pipeline is provided with a multi-stage filter.
CN202122686865.6U 2021-11-04 2021-11-04 Energy-saving application equipment for combined membrane oxygen generation Active CN216005217U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202122686865.6U CN216005217U (en) 2021-11-04 2021-11-04 Energy-saving application equipment for combined membrane oxygen generation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202122686865.6U CN216005217U (en) 2021-11-04 2021-11-04 Energy-saving application equipment for combined membrane oxygen generation

Publications (1)

Publication Number Publication Date
CN216005217U true CN216005217U (en) 2022-03-11

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202122686865.6U Active CN216005217U (en) 2021-11-04 2021-11-04 Energy-saving application equipment for combined membrane oxygen generation

Country Status (1)

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CN (1) CN216005217U (en)

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