CN204986391U - Empty surplus cold recovery system of formula liquid oxygen gasifier that bathes - Google Patents
Empty surplus cold recovery system of formula liquid oxygen gasifier that bathes Download PDFInfo
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- CN204986391U CN204986391U CN201520559232.0U CN201520559232U CN204986391U CN 204986391 U CN204986391 U CN 204986391U CN 201520559232 U CN201520559232 U CN 201520559232U CN 204986391 U CN204986391 U CN 204986391U
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- heat exchange
- exchange pipe
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- fin
- connecting tube
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Abstract
The utility model provides an empty surplus cold recovery system of formula liquid oxygen gasifier that bathes, bathes formula liquid oxygen gasifier, entrapment cover, fan, surplus cold recoverer, its characterized in that including the sky: the sky is bathed the formula liquid oxygen gasifier and is located entrapment cover below, and the entrapment is covered through pipeline order connection fan, surplus cold recoverer, the sky is bathed the formula liquid oxygen gasifier and is included finned heat exchanger, feed liquor pipe, outlet duct and frame, surplus cold recoverer, including shell, heat transfer chamber and heat exchange tube, in the shell was arranged in the heat transfer chamber, the ambient air entry had been seted up at the shell top, and low temperature gas outlet compressor the for has been seted up to the shell bottom, low temperature gas outlet connection low temperature gas storage tank for the compressor compressor for, heat transfer chamber bottom is equipped with low temperature air conditioning entry, and low temperature air conditioning entry is connected with the fan, and heat transfer chamber top is equipped with the new trend air outlet, and new trend air user is connected to the new trend air outlet. The utility model discloses realize surplus cold abundant recycle to reduce the power consumption that produces through electric refrigeration, save a large amount of energy resource consumptions.
Description
Technical field
The utility model relates to remaining cold recovery technology field, is specially cold reclaiming system more than a kind of empty bath formula oxygen evaporator.
Background technique
In industrial processes, often need to use compressed pressurized gas, and in the process of pressurized gas, cryogenic gas is compared with high-temperature gas, the displacement of cryogenic gas compressor is comparatively large, but owing to being subject to the impact of environment, what use during pressurized gas is the gas of higher temperature mostly, drastically influence the working efficiency of air compressor.
Current air processor, all needs to consume a large amount of cold to cool new wind, have that energy consumption is high, the wasting of resources, befouling environment shortcoming.
On the other hand in the process of sky bath formula oxygen evaporator work, vaporizer cold is discharged with surrounding atmosphere, causes cold to waste.
Model utility content
The technical problems to be solved in the utility model overcomes existing defect, cold reclaiming system more than a kind of empty bath formula oxygen evaporator is provided, by remaining cold recycling, when solving empty bath formula oxygen evaporator work in the past, the remaining cold of generation is directly discharged in air, cause the problem that cold wastes, efficiently solve at air compressor, the power consumption that in air processor working procedure, electricity refrigeration produces, the problems such as cooling energy consumption, realize remaining cold abundant recycling, thus be reduced by the power consumption of electricity refrigeration generation, saving mass energy consumes, effectively reduce entreprise cost, improve competitive ability.
The technical solution of the utility model is: cold reclaiming system more than a kind of empty bath formula oxygen evaporator, comprise empty bath formula oxygen evaporator, fume trap cover, blower fan, remaining cold recover, it is characterized in that: described empty bath formula oxygen evaporator is positioned at below fume trap cover, fume trap cover to be linked in sequence blower fan by pipeline, remaining cold recover, described empty bath formula oxygen evaporator comprises fin heat exchange pipe, liquid inlet pipe, steam outlet pipe and frame, described fin heat exchange pipe is totally eight row, often row ten arranges symmetrical composition, conducting is connected by connecting tube, along the flow direction of liquid medium, fin number from less to more, fin heat exchange pipe is fixed in frame, first fin heat exchange pipe lower end connects liquid inlet pipe, first fin heat exchange pipe side sets gradually the second fin heat exchange pipe, 3rd fin heat exchange pipe, 4th fin heat exchange pipe, 5th fin heat exchange pipe, 6th fin heat exchange pipe, 7th fin heat exchange pipe, 8th fin heat exchange pipe, 9th fin heat exchange pipe, tenth fin heat exchange pipe, first fin heat exchange pipe is the heat exchanging tube of band 4 fins, second fin heat exchange pipe is the heat exchanging tube of band 8 fins, 3rd fin heat exchange pipe, 4th fin heat exchange pipe, 5th fin heat exchange pipe, 6th fin heat exchange pipe, 7th fin heat exchange pipe, 8th fin heat exchange pipe, 9th fin heat exchange pipe, tenth fin heat exchange pipe is the heat exchanging tube of band 12 fins, first fin heat exchange pipe upper end is connected with the second fin heat exchange pipe upper end by connecting tube, second fin heat exchange pipe lower end is connected with the 3rd fin heat exchange pipe lower end by connecting tube, 3rd fin heat exchange pipe upper end is connected with the 4th fin heat exchange pipe upper end by connecting tube, 4th fin heat exchange pipe lower end is connected with the 5th fin heat exchange pipe lower end by connecting tube, 5th fin heat exchange pipe upper end is connected with the 6th fin heat exchange pipe upper end by connecting tube, 6th fin heat exchange pipe lower end is connected with the 7th fin heat exchange pipe lower end by connecting tube, 7th fin heat exchange pipe upper end is connected with the 8th fin heat exchange pipe upper end by connecting tube, 8th fin heat exchange pipe lower end is connected with the 9th fin heat exchange pipe lower end by connecting tube, 9th fin heat exchange pipe upper end is connected with the tenth fin heat exchange pipe upper end by connecting tube, tenth fin heat exchange pipe lower end connects steam outlet pipe, described remaining cold recover, comprise shell, heat exchanging chamber and heat exchanging tube, described heat exchanging chamber is placed in shell, cover top portion offers ambient air inlet, outer casing bottom offers compressor cryogenic gas and exports, compressor cryogenic gas outlet connects compressor cryogenic gas storage tank, cold gas entrance is provided with bottom described heat exchanging chamber, cold gas entrance is connected with blower fan, heat exchanging chamber top is provided with new wind air outlet slit, new wind air outlet slit connects new wind air user, described heat exchanging tube is fixedly mounted on the outer side wall of heat exchanging chamber, heat exchange liquid is injected with in described heat exchanging tube.
The beneficial effects of the utility model are: the utility model provides cold reclaiming system more than a kind of empty bath formula oxygen evaporator, by remaining cold recycling, when solving empty bath formula oxygen evaporator work in the past, the remaining cold of generation is directly discharged in air, cause the problem that cold wastes, efficiently solve at air compressor, the power consumption that in air processor working procedure, electricity refrigeration produces, the problems such as cooling energy consumption, realize remaining cold abundant recycling, thus be reduced by the power consumption of electricity refrigeration generation, saving mass energy consumes, effectively reduce entreprise cost, improve competitive ability.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the main TV structure schematic diagram of empty bath formula oxygen evaporator.
Fig. 3 is the plan structure schematic diagram of empty bath formula oxygen evaporator.
Fig. 4 is A-A place sectional view in Fig. 2.
Fig. 5 is B-B place sectional view in Fig. 2.
Fig. 6 is C-C place enlarged view in Fig. 2.
Fig. 7 is D place enlarged view in Fig. 2.
Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, in Fig. 7, 1. the first fin heat exchange pipe, 2. the second fin heat exchange pipe, 3. the 3rd fin heat exchange pipe, 4. the 4th fin heat exchange pipe, 5. the 5th fin heat exchange pipe, 6. the 6th fin heat exchange pipe, 7. the 7th fin heat exchange pipe, 8. the 8th fin heat exchange pipe, 9. the 9th fin heat exchange pipe, 10. the tenth fin heat exchange pipe, 11. liquid inlet pipes, 12. steam outlet pipes, 13. frames, 14. fume trap covers, 15. blower fans, 16. cold gas entrances, 17. new wind air users, 18. new wind air outlet slits, more than 19. cold recovers, 20. ambient air inlet, 21. heat exchanging chambers, 22. heat exchanging tubes, 23. shells, 24. compressor cryogenic gases export, 25. compressors cryogenic gas storage tank.
Embodiment
Below in conjunction with accompanying drawing, the utility model is further described.
As Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, shown in Fig. 7, the utility model is cold reclaiming system more than a kind of empty bath formula oxygen evaporator, comprise empty bath formula oxygen evaporator, fume trap cover 14, blower fan 15, remaining cold recover 19, it is characterized in that: described empty bath formula oxygen evaporator is positioned at below fume trap cover 14, fume trap cover 14 to be linked in sequence blower fan 15 by pipeline, remaining cold recover 19, described empty bath formula oxygen evaporator comprises fin heat exchange pipe, liquid inlet pipe 11, steam outlet pipe 12 and frame 13, fin heat exchange pipe is totally eight row, often row ten arranges symmetrical composition, conducting is connected by connecting tube, along the flow direction of liquid medium, fin number from less to more, fin heat exchange pipe is fixed in frame 13, first fin heat exchange pipe 1 lower end connects liquid inlet pipe 11, first fin heat exchange pipe 1 side sets gradually the second fin heat exchange pipe 2, 3rd fin heat exchange pipe 3, 4th fin heat exchange pipe 4, 5th fin heat exchange pipe 5, 6th fin heat exchange pipe 6, 7th fin heat exchange pipe 7, 8th fin heat exchange pipe 8, 9th fin heat exchange pipe 9, tenth fin heat exchange pipe 10, first fin heat exchange pipe 1 is the heat exchanging tube of band 4 fins, second fin heat exchange pipe 2 is the heat exchanging tube of band 8 fins, 3rd fin heat exchange pipe 3, 4th fin heat exchange pipe 4, 5th fin heat exchange pipe 5, 6th fin heat exchange pipe 6, 7th fin heat exchange pipe 7, 8th fin heat exchange pipe 8, 9th fin heat exchange pipe 9, tenth fin heat exchange pipe 10 is the heat exchanging tube of band 12 fins, first fin heat exchange pipe 1 upper end is connected with the second fin heat exchange pipe 2 upper end by connecting tube, second fin heat exchange pipe 2 lower end is connected with the 3rd fin heat exchange pipe 3 lower end by connecting tube, 3rd fin heat exchange pipe 3 upper end is connected with the 4th fin heat exchange pipe 4 upper end by connecting tube, 4th fin heat exchange pipe 4 lower end is connected with the 5th fin heat exchange pipe 5 lower end by connecting tube, 5th fin heat exchange pipe 5 upper end is connected with the 6th fin heat exchange pipe 6 upper end by connecting tube, 6th fin heat exchange pipe 6 lower end is connected with the 7th fin heat exchange pipe 7 lower end by connecting tube, 7th fin heat exchange pipe 7 upper end is connected with the 8th fin heat exchange pipe 8 upper end by connecting tube, 8th fin heat exchange pipe 8 lower end is connected with the 9th fin heat exchange pipe 9 lower end by connecting tube, 9th fin heat exchange pipe 9 upper end is connected with the tenth fin heat exchange pipe 10 upper end by connecting tube, tenth fin heat exchange pipe 10 lower end connects steam outlet pipe 12, described remaining cold recover 19, comprise shell 23, heat exchanging chamber 21 and heat exchanging tube 22, described heat exchanging chamber 21 is placed in shell 23, shell 23 top offers ambient air inlet 20, compressor cryogenic gas outlet 24 is offered bottom shell 23, compressor cryogenic gas outlet 24 connects compressor cryogenic gas storage tank 25, cold gas entrance 16 is provided with bottom described heat exchanging chamber 21, cold gas entrance 16 is connected with blower fan 15, heat exchanging chamber 21 top is provided with new wind air outlet slit 18, new wind air outlet slit 18 connects new wind air user 17, described heat exchanging tube 22 is fixedly mounted on the outer side wall of heat exchanging chamber 21, heat exchange liquid is injected with in described heat exchanging tube 22.
Working procedure of the present utility model: in Fig. 1, the direction of arrow is the direction of low-temperature liquid oxygen media flow, the low-temperature liquid oxygen medium of subzero about 196 DEG C enters 10000Nm by below liquid inlet pipe 11
3the sky bath formula oxygen evaporator of/h, low-temperature liquid oxygen medium produces a large amount of cold, cold mixes with air, form cryogenic gas, trapped through fume trap cover 14 by suction function by blower fan 15, by remaining cold recovery, the remaining cold of recovery enters heat exchanging chamber 21 and air (the air quantity 100000m entered from ambient air inlet 20
3/ h, temperature 35 DEG C, humidity 70%, water content 25.2g/kg) carry out cold exchange by heat exchanging tube 22, (air quantity 100000m after air is cooled
3/ h, temperature 24 DEG C, humidity 95%, water content 16.9g/kg), enter compressor cryogenic gas storage tank 25 by compressor cryogenic gas outlet 24, for air compressor, improve the working efficiency of air compressor;
Cryogenic gas is by the cold exchange of heat exchanging chamber 21, and Cooling capacity exchanging out, improves outlet temperature (the air quantity 10000m of cryogenic gas
3/ h, temperature 22 DEG C, humidity 54.7%, water content 9g/kg), enter new wind air user 17 from new wind air outlet slit 18, play the effect regulating process air;
The utility model is by remaining cold recycling, when solving empty bath formula oxygen evaporator work in the past, the remaining cold of generation is directly discharged in air, causes the problem that cold wastes, and efficiently solves the power consumption that electricity refrigeration produces in air compressor, air processor working procedure, the problems such as cooling energy consumption, realize remaining cold abundant recycling, thus be reduced by the power consumption of electricity refrigeration generation, save mass energy consumption, effectively reduce entreprise cost, improve competitive ability.
Claims (1)
1. cold reclaiming system more than an empty bath formula oxygen evaporator, comprise empty bath formula oxygen evaporator, fume trap cover, blower fan, remaining cold recover, it is characterized in that: described empty bath formula oxygen evaporator is positioned at below fume trap cover, fume trap cover to be linked in sequence blower fan by pipeline, remaining cold recover, described empty bath formula oxygen evaporator comprises fin heat exchange pipe, liquid inlet pipe, steam outlet pipe and frame, described fin heat exchange pipe is totally eight row, often row ten arranges symmetrical composition, conducting is connected by connecting tube, along the flow direction of liquid medium, fin number from less to more, fin heat exchange pipe is fixed in frame, first fin heat exchange pipe lower end connects liquid inlet pipe, first fin heat exchange pipe side sets gradually the second fin heat exchange pipe, 3rd fin heat exchange pipe, 4th fin heat exchange pipe, 5th fin heat exchange pipe, 6th fin heat exchange pipe, 7th fin heat exchange pipe, 8th fin heat exchange pipe, 9th fin heat exchange pipe, tenth fin heat exchange pipe, first fin heat exchange pipe is the heat exchanging tube of band 4 fins, second fin heat exchange pipe is the heat exchanging tube of band 8 fins, 3rd fin heat exchange pipe, 4th fin heat exchange pipe, 5th fin heat exchange pipe, 6th fin heat exchange pipe, 7th fin heat exchange pipe, 8th fin heat exchange pipe, 9th fin heat exchange pipe, tenth fin heat exchange pipe is the heat exchanging tube of band 12 fins, first fin heat exchange pipe upper end is connected with the second fin heat exchange pipe upper end by connecting tube, second fin heat exchange pipe lower end is connected with the 3rd fin heat exchange pipe lower end by connecting tube, 3rd fin heat exchange pipe upper end is connected with the 4th fin heat exchange pipe upper end by connecting tube, 4th fin heat exchange pipe lower end is connected with the 5th fin heat exchange pipe lower end by connecting tube, 5th fin heat exchange pipe upper end is connected with the 6th fin heat exchange pipe upper end by connecting tube, 6th fin heat exchange pipe lower end is connected with the 7th fin heat exchange pipe lower end by connecting tube, 7th fin heat exchange pipe upper end is connected with the 8th fin heat exchange pipe upper end by connecting tube, 8th fin heat exchange pipe lower end is connected with the 9th fin heat exchange pipe lower end by connecting tube, 9th fin heat exchange pipe upper end is connected with the tenth fin heat exchange pipe upper end by connecting tube, tenth fin heat exchange pipe lower end connects steam outlet pipe, described remaining cold recover, comprise shell, heat exchanging chamber and heat exchanging tube, described heat exchanging chamber is placed in shell, cover top portion offers ambient air inlet, outer casing bottom offers compressor cryogenic gas and exports, compressor cryogenic gas outlet connects compressor cryogenic gas storage tank, cold gas entrance is provided with bottom described heat exchanging chamber, cold gas entrance is connected with blower fan, heat exchanging chamber top is provided with new wind air outlet slit, new wind air outlet slit connects new wind air user, described heat exchanging tube is fixedly mounted on the outer side wall of heat exchanging chamber, heat exchange liquid is injected with in described heat exchanging tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520559232.0U CN204986391U (en) | 2015-07-24 | 2015-07-24 | Empty surplus cold recovery system of formula liquid oxygen gasifier that bathes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520559232.0U CN204986391U (en) | 2015-07-24 | 2015-07-24 | Empty surplus cold recovery system of formula liquid oxygen gasifier that bathes |
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| Publication Number | Publication Date |
|---|---|
| CN204986391U true CN204986391U (en) | 2016-01-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520559232.0U Expired - Fee Related CN204986391U (en) | 2015-07-24 | 2015-07-24 | Empty surplus cold recovery system of formula liquid oxygen gasifier that bathes |
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| CN (1) | CN204986391U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106641708A (en) * | 2016-11-07 | 2017-05-10 | 山东新兴重工科技发展有限公司 | Small natural gas gasification pry |
-
2015
- 2015-07-24 CN CN201520559232.0U patent/CN204986391U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106641708A (en) * | 2016-11-07 | 2017-05-10 | 山东新兴重工科技发展有限公司 | Small natural gas gasification pry |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160120 Termination date: 20190724 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |