CN204027376U - A kind of empty bath formula liquid oxygen high pressure gasifier connected system - Google Patents
A kind of empty bath formula liquid oxygen high pressure gasifier connected system Download PDFInfo
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- CN204027376U CN204027376U CN201420488429.5U CN201420488429U CN204027376U CN 204027376 U CN204027376 U CN 204027376U CN 201420488429 U CN201420488429 U CN 201420488429U CN 204027376 U CN204027376 U CN 204027376U
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- heat exchange
- fin heat
- exchange pipe
- pipe
- liquid oxygen
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Abstract
A kind of empty bath formula liquid oxygen high pressure gasifier connected system, comprise fin heat exchange pipe, feed tube, escape pipe and tube connector, it is characterized in that: empty bath formula liquid oxygen high pressure gasifier connected system comprises the vaporization unit of two groups of symmetries, each vaporization unit is fixed in frame, often organize below vaporization unit and connect a feed liquor arm, feed liquor arm is connected to feed tube, often organize connection one below vaporization unit and go out gas branch pipe, go out gas branch pipe and be connected to escape pipe, often organize vaporization unit to arrange fin heat exchange pipe by four lines eight and form, first row first fin heat exchange pipe lower end connects a feed liquor arm, first fin heat exchange pipe side sets gradually second, 3rd and the 4th fin heat exchange pipe.The utility model low-temperature liquid oxygen medium flows in first row fin heat exchange pipe in a series arrangement, turn to flow in second row fin heat exchange pipe by tube connector again and so circulate, the temperature difference between liquid oxygen medium and air decreases, and is conducive to improving heat transfer effect, thus ensures good heat vaporized effect.
Description
Technical field
The utility model relates to air-bathing gasifier technical field, is specially a kind of empty bath formula liquid oxygen high pressure gasifier connected system.
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, a kind of empty bath formula liquid oxygen high pressure gasifier connected system is provided, low-temperature liquid oxygen medium by below feed tube through feed liquor arm, flow into the first fin heat exchange pipe in first row fin heat exchange pipe in a series arrangement, second fin heat exchange pipe, 3rd fin heat exchange pipe and the 4th fin heat exchange pipe, the 5th fin heat exchange pipe flowed in second row fin heat exchange pipe is turned to again by tube connector, 6th fin heat exchange pipe, 7th fin heat exchange pipe and the 8th fin heat exchange pipe, circulation like this, the temperature difference between liquid oxygen medium and air decreases, be conducive to improving heat transfer effect, thus ensure good heat vaporized effect.
The technical solution of the utility model is: a kind of empty bath formula liquid oxygen high pressure gasifier connected system, comprise fin heat exchange pipe, feed tube, escape pipe and tube connector, it is characterized in that: empty bath formula liquid oxygen high pressure gasifier connected system comprises the vaporization unit of two groups of symmetries, each vaporization unit is fixed in frame, often organize below vaporization unit and connect a feed liquor arm, feed liquor arm is connected to feed tube, often organize connection one below vaporization unit and go out gas branch pipe, go out gas branch pipe and be connected to escape pipe, often organize vaporization unit to arrange fin heat exchange pipe by four lines eight and form, first row first fin heat exchange pipe lower end connects a feed liquor arm, first fin heat exchange pipe side sets gradually the second fin heat exchange pipe, 3rd fin heat exchange pipe and the 4th fin heat exchange pipe, finally ranked eighth fin heat exchange pipe lower end to connect one and go out gas branch pipe, 8th fin heat exchange pipe side sets gradually the 7th fin heat exchange pipe, 6th fin heat exchange pipe and the 5th fin heat exchange pipe, centre is circulation section, 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 ranked fifth fin heat exchange pipe lower end by tube connector and second and is connected, 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 after circulation with go out gas branch pipe and be connected.
The beneficial effects of the utility model are: the utility model provides a kind of empty bath formula liquid oxygen high pressure gasifier connected system, low-temperature liquid oxygen medium by below feed tube through feed liquor arm, flow into the first fin heat exchange pipe in first row fin heat exchange pipe in a series arrangement, second fin heat exchange pipe, 3rd fin heat exchange pipe and the 4th fin heat exchange pipe, the 5th fin heat exchange pipe flowed in second row fin heat exchange pipe is turned to again by tube connector, 6th fin heat exchange pipe, 7th fin heat exchange pipe and the 8th fin heat exchange pipe, circulation like this, due to the first fin heat exchange pipe in first row fin heat exchange pipe, second fin heat exchange pipe, 3rd fin heat exchange pipe and this tube side liquid oxygen medium temperature of the 4th fin heat exchange pipe are from low to high, its adjacent i.e. the 8th fin heat exchange pipe, 7th fin heat exchange pipe, the environment temperature of the 6th fin heat exchange pipe and the 5th fin heat exchange pipe also from low to high, liquid oxygen medium is turning to the 5th fin heat exchange pipe entered in second row fin heat exchange pipe, 6th fin heat exchange pipe, when the 7th fin heat exchange pipe and the 8th fin heat exchange pipe, the temperature difference between itself and air decreases, be conducive to improving heat transfer effect, thus ensure good heat vaporized effect.
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.
In Fig. 1, Fig. 2,1. 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. feed tube, 10. escape pipe, 11. feed liquor arms, 12. go out gas branch pipe, 13. frames.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is further described.
As Fig. 1, shown in Fig. 2, the utility model is a kind of empty bath formula liquid oxygen high pressure gasifier connected system, comprise fin heat exchange pipe, feed tube 9, escape pipe 10 and tube connector, it is characterized in that: empty bath formula liquid oxygen high pressure gasifier connected system comprises the vaporization unit of two groups of symmetries, each vaporization unit is fixed in frame 13, often organize below vaporization unit and connect a feed liquor arm 11, feed liquor arm 11 is connected to feed tube 9, often organize connection one below vaporization unit and go out gas branch pipe 12, go out gas branch pipe 12 and be connected to escape pipe 10, often organize vaporization unit to arrange fin heat exchange pipe by four lines eight and form, first row first fin heat exchange pipe 1 lower end connects a feed liquor arm 11, first fin heat exchange pipe 1 side sets gradually the second fin heat exchange pipe 2, 3rd fin heat exchange pipe 3 and the 4th fin heat exchange pipe 4, finally ranked eighth fin heat exchange pipe 8 lower end to connect one and go out gas branch pipe 12, 8th fin heat exchange pipe 8 side sets gradually the 7th fin heat exchange pipe 7, 6th fin heat exchange pipe 6 and the 5th fin heat exchange pipe 5, centre is circulation section, 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 ranked fifth fin heat exchange pipe 5 lower end by tube connector and second and is connected, 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 after circulation with go out gas branch pipe 12 and be connected.
In Fig. 2, the direction of arrow is the direction of cryogenic medium flows, the low-temperature liquid oxygen medium of subzero about 196 DEG C by below feed tube 9 through feed liquor arm 11, flow into the first fin heat exchange pipe 1 in first row fin heat exchange pipe in a series arrangement, second fin heat exchange pipe 2, 3rd fin heat exchange pipe 3 and the 4th fin heat exchange pipe 4, the 5th fin heat exchange pipe 5 flowed in second row fin heat exchange pipe is turned to again by tube connector, 6th fin heat exchange pipe 6, 7th fin heat exchange pipe 7 and the 8th fin heat exchange pipe 8, circulation like this, due to the first fin heat exchange pipe 1 in first row fin heat exchange pipe, second fin heat exchange pipe 2, 3rd fin heat exchange pipe 3 and this tube side liquid oxygen medium temperature of the 4th fin heat exchange pipe 4 are from low to high, its adjacent i.e. the 8th fin heat exchange pipe 8, 7th fin heat exchange pipe 7, the environment temperature of the 6th fin heat exchange pipe 6 and the 5th fin heat exchange pipe 5 also from low to high, liquid oxygen medium is turning to the 5th fin heat exchange pipe 5 entered in second row fin heat exchange pipe, 6th fin heat exchange pipe 6, when the 7th fin heat exchange pipe 7 and the 8th fin heat exchange pipe 8, the temperature difference between itself and air decreases, be conducive to improving heat transfer effect, thus ensure good heat vaporized effect.
As can be seen here, the utility model provides a kind of empty bath formula liquid oxygen high pressure gasifier connected system, low-temperature liquid oxygen medium by below feed tube through feed liquor arm, flow into the first fin heat exchange pipe in first row fin heat exchange pipe in a series arrangement, second fin heat exchange pipe, 3rd fin heat exchange pipe and the 4th fin heat exchange pipe, the 5th fin heat exchange pipe flowed in second row fin heat exchange pipe is turned to again by tube connector, 6th fin heat exchange pipe, 7th fin heat exchange pipe and the 8th fin heat exchange pipe, circulation like this, the temperature difference between liquid oxygen medium and air decreases, be conducive to improving heat transfer effect, thus ensure good heat vaporized effect.
Claims (1)
1. an empty bath formula liquid oxygen high pressure gasifier connected system, comprise fin heat exchange pipe, feed tube, escape pipe and tube connector, it is characterized in that: empty bath formula liquid oxygen high pressure gasifier connected system comprises the vaporization unit of two groups of symmetries, each vaporization unit is fixed in frame, often organize below vaporization unit and connect a feed liquor arm, feed liquor arm is connected to feed tube, often organize connection one below vaporization unit and go out gas branch pipe, go out gas branch pipe and be connected to escape pipe, often organize vaporization unit to arrange fin heat exchange pipe by four lines eight and form, first row first fin heat exchange pipe lower end connects a feed liquor arm, first fin heat exchange pipe side sets gradually the second fin heat exchange pipe, 3rd fin heat exchange pipe and the 4th fin heat exchange pipe, finally ranked eighth fin heat exchange pipe lower end to connect one and go out gas branch pipe, 8th fin heat exchange pipe side sets gradually the 7th fin heat exchange pipe, 6th fin heat exchange pipe and the 5th fin heat exchange pipe, centre is circulation section, 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 ranked fifth fin heat exchange pipe lower end by tube connector and second and is connected, 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 after circulation with go out gas branch pipe and be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420488429.5U CN204027376U (en) | 2014-08-21 | 2014-08-21 | A kind of empty bath formula liquid oxygen high pressure gasifier connected system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420488429.5U CN204027376U (en) | 2014-08-21 | 2014-08-21 | A kind of empty bath formula liquid oxygen high pressure gasifier connected system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204027376U true CN204027376U (en) | 2014-12-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420488429.5U Active CN204027376U (en) | 2014-08-21 | 2014-08-21 | A kind of empty bath formula liquid oxygen high pressure gasifier connected system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204027376U (en) |
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2014
- 2014-08-21 CN CN201420488429.5U patent/CN204027376U/en active Active
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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 Science & Technology Co., Ltd. Assignor: Yu Jun Contract record no.: 2015320010147 Denomination of utility model: Communication system of air bathing type liquid oxygen 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 Science & Technology Co., Ltd. Address before: 214151, No. 85, Yu Cun, Yangxi village, Qian Qiao Town, Huishan District, Jiangsu, Wuxi Patentee before: Yu Jun |