CN204027373U - A kind of empty bath formula liquid nitrogen high pressure gasifier - Google Patents
A kind of empty bath formula liquid nitrogen high pressure gasifier Download PDFInfo
- Publication number
- CN204027373U CN204027373U CN201420488415.3U CN201420488415U CN204027373U CN 204027373 U CN204027373 U CN 204027373U CN 201420488415 U CN201420488415 U CN 201420488415U CN 204027373 U CN204027373 U CN 204027373U
- Authority
- CN
- China
- Prior art keywords
- heat exchange
- exchange pipe
- fin heat
- fin
- tube connector
- 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 - Fee Related
Links
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 239000007788 liquid Substances 0.000 title claims abstract description 12
- 229910052757 nitrogen Inorganic materials 0.000 title claims abstract description 8
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 230000008016 vaporization Effects 0.000 abstract description 5
- 238000009834 vaporization Methods 0.000 abstract description 5
- 238000010586 diagram Methods 0.000 description 3
- 239000006200 vaporizer Substances 0.000 description 2
- 238000003287 bathing Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A kind of empty bath formula liquid nitrogen high pressure gasifier, comprise fin heat exchange pipe, feed tube, escape pipe, tube connector, frame, it is characterized in that: fin heat exchange pipe is totally eight row, often row ten arranges symmetrical composition, conducting is connected by tube connector, 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 feed tube, first fin heat exchange pipe side sets gradually second, 3rd, 4th, 5th, 6th, 7th, 8th, 9th, tenth fin heat exchange pipe, first fin heat exchange pipe is the heat exchanger tube of band 4 fins, second fin heat exchange pipe is the heat exchanger tube of band 8 fins, 3rd, 4th, 5th, 6th, 7th, 8th, 9th, tenth fin heat exchange pipe is the heat exchanger tube of band 12 fins, first fin heat exchange pipe is connected with the second fin heat exchange pipe by tube connector.The utility model, by taking the mode that is linked in sequence between the heat exchanger tube that is arranged side by side, realizes the raising of vaporization efficency.
Description
Technical field
The utility model relates to air-bathing gasifier technical field, is specially a kind of empty bath formula liquid nitrogen high pressure gasifier.
Background technology
Many heat exchanger tubes in vaporizer are interconnected, and jointly form the carburetion system of heat exchanger tube more than, but in the connection of vaporizer heat exchanger tube, the connection between various heat exchange pipe is different, can cause the difference of vaporization efficency.
Summary of the invention
The technical problems to be solved in the utility model overcomes existing defect, provides a kind of empty bath formula liquid nitrogen high pressure gasifier, by taking the mode that is linked in sequence between the heat exchanger tube that is arranged side by side, realizes the raising of vaporization efficency.
The technical solution of the utility model is: a kind of empty bath formula liquid nitrogen high pressure gasifier, comprise fin heat exchange pipe, feed tube, escape pipe, tube connector, frame, it is characterized in that: fin heat exchange pipe is totally eight row, often row ten arranges symmetrical composition, conducting is connected by tube connector, 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 feed tube, 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 exchanger tube of band 4 fins, second fin heat exchange pipe is the heat exchanger 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 exchanger tube of band 12 fins, first fin heat exchange pipe upper end is connected with the second fin heat exchange pipe upper end by tube connector, second fin heat exchange pipe lower end is connected with the 3rd fin heat exchange pipe lower end by tube connector, 3rd fin heat exchange pipe upper end is connected with the 4th fin heat exchange pipe upper end by tube connector, 4th fin heat exchange pipe lower end is connected with the 5th fin heat exchange pipe lower end by tube connector, 5th fin heat exchange pipe upper end is connected with the 6th fin heat exchange pipe upper end by tube connector, 6th fin heat exchange pipe lower end is connected with the 7th fin heat exchange pipe lower end by tube connector, 7th fin heat exchange pipe upper end is connected with the 8th fin heat exchange pipe upper end by tube connector, 8th fin heat exchange pipe lower end is connected with the 9th fin heat exchange pipe lower end by tube connector, 9th fin heat exchange pipe upper end is connected with the tenth fin heat exchange pipe upper end by tube connector, tenth fin heat exchange pipe lower end connects escape pipe.
The beneficial effects of the utility model are: by taking the mode that is linked in sequence between the heat exchanger tube that is arranged side by side, realize the raising of vaporization efficency.
Accompanying drawing explanation
Fig. 1 is main TV structure schematic diagram of the present utility model.
Fig. 2 is plan structure schematic diagram of the present utility model.
Fig. 3 is left TV structure schematic diagram of the present utility model.
Fig. 4 is A-A place sectional view in Fig. 1.
Fig. 5 is B-B place sectional view in Fig. 1.
Fig. 6 is C-C place enlarged drawing in Fig. 1.
Fig. 7 is D place enlarged drawing in Fig. 1.
In Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, 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. feed tubes, 12. escape pipes, 13. frames.
Detailed description of the invention
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 a kind of empty bath formula liquid nitrogen high pressure gasifier, comprises fin heat exchange pipe, feed tube 11, escape pipe 12, tube connector, frame 13, it is characterized in that: fin heat exchange pipe is totally eight row, often row ten arranges symmetrical composition, conducting is connected by tube connector, along the flow direction of liquid medium, from less to more, fin heat exchange pipe is fixed in frame 13 fin number, first fin heat exchange pipe 1 lower end connects feed tube 11, first fin heat exchange pipe 1 side and 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 exchanger tube of band 4 fins, and the second fin heat exchange pipe 2 is the heat exchanger tube of band 8 fins, the 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 exchanger 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 tube connector, second fin heat exchange pipe 2 lower end is connected with the 3rd fin heat exchange pipe 3 lower end by tube connector, 3rd fin heat exchange pipe 3 upper end is connected with the 4th fin heat exchange pipe 4 upper end by tube connector, 4th fin heat exchange pipe 4 lower end is connected with the 5th fin heat exchange pipe 5 lower end by tube connector, 5th fin heat exchange pipe 5 upper end is connected with the 6th fin heat exchange pipe 6 upper end by tube connector, 6th fin heat exchange pipe 6 lower end is connected with the 7th fin heat exchange pipe 7 lower end by tube connector, 7th fin heat exchange pipe 7 upper end is connected with the 8th fin heat exchange pipe 8 upper end by tube connector, 8th fin heat exchange pipe 8 lower end is connected with the 9th fin heat exchange pipe 9 lower end by tube connector, 9th fin heat exchange pipe 9 upper end is connected with the tenth fin heat exchange pipe 10 upper end by tube connector, tenth fin heat exchange pipe 10 lower end connects escape pipe 12.
As can be seen here, the utility model, by taking the mode that is linked in sequence between the heat exchanger tube that is arranged side by side, realizes the raising of vaporization efficency.
Claims (1)
1. an empty bath formula liquid nitrogen high pressure gasifier, comprises fin heat exchange pipe, feed tube, escape pipe, tube connector, frame, it is characterized in that: fin heat exchange pipe is totally eight row, often row ten arranges symmetrical composition, conducting is connected by tube connector, along the flow direction of liquid medium, from less to more, fin heat exchange pipe is fixed in frame fin number, first fin heat exchange pipe lower end connects feed tube, and the 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, the first fin heat exchange pipe is the heat exchanger tube of band 4 fins, and the second fin heat exchange pipe is the heat exchanger tube of band 8 fins, the 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 exchanger tube of band 12 fins, first fin heat exchange pipe upper end is connected with the second fin heat exchange pipe upper end by tube connector, second fin heat exchange pipe lower end is connected with the 3rd fin heat exchange pipe lower end by tube connector, 3rd fin heat exchange pipe upper end is connected with the 4th fin heat exchange pipe upper end by tube connector, 4th fin heat exchange pipe lower end is connected with the 5th fin heat exchange pipe lower end by tube connector, 5th fin heat exchange pipe upper end is connected with the 6th fin heat exchange pipe upper end by tube connector, 6th fin heat exchange pipe lower end is connected with the 7th fin heat exchange pipe lower end by tube connector, 7th fin heat exchange pipe upper end is connected with the 8th fin heat exchange pipe upper end by tube connector, 8th fin heat exchange pipe lower end is connected with the 9th fin heat exchange pipe lower end by tube connector, 9th fin heat exchange pipe upper end is connected with the tenth fin heat exchange pipe upper end by tube connector, tenth fin heat exchange pipe lower end connects escape pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420488415.3U CN204027373U (en) | 2014-08-21 | 2014-08-21 | A kind of empty bath formula liquid nitrogen high pressure gasifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420488415.3U CN204027373U (en) | 2014-08-21 | 2014-08-21 | A kind of empty bath formula liquid nitrogen high pressure gasifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204027373U true CN204027373U (en) | 2014-12-17 |
Family
ID=52067218
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420488415.3U Expired - Fee Related CN204027373U (en) | 2014-08-21 | 2014-08-21 | A kind of empty bath formula liquid nitrogen high pressure gasifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204027373U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112503974A (en) * | 2020-11-06 | 2021-03-16 | 涡阳县华夏气体有限公司 | Gasifier for liquid oxygen |
-
2014
- 2014-08-21 CN CN201420488415.3U patent/CN204027373U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112503974A (en) * | 2020-11-06 | 2021-03-16 | 涡阳县华夏气体有限公司 | Gasifier for liquid oxygen |
| CN112503974B (en) * | 2020-11-06 | 2022-08-09 | 涡阳县华夏气体有限公司 | Gasifier for liquid oxygen |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: WUXI PHAETON CRYOTECH Co.,Ltd. Assignor: Yu Jun Contract record no.: 2015320010147 Denomination of utility model: Air shower type liquid nitrogen high-pressure vaporizer Granted publication date: 20141217 License type: Exclusive License Record date: 20151020 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160503 Address after: 214000 Mashan biological pharmaceutical industry park, Binhu District, Jiangsu, Wuxi Patentee after: WUXI PHAETON CRYOTECH Co.,Ltd. Address before: 214151, No. 85, Yu Cun, Yangxi village, Qian Qiao Town, Huishan District, Jiangsu, Wuxi Patentee before: Yu Jun |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141217 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |