CN204027398U - A kind of energy-saving empty bath formula liquid nitrogen converter - Google Patents

A kind of energy-saving empty bath formula liquid nitrogen converter Download PDF

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Publication number
CN204027398U
CN204027398U CN201420485914.7U CN201420485914U CN204027398U CN 204027398 U CN204027398 U CN 204027398U CN 201420485914 U CN201420485914 U CN 201420485914U CN 204027398 U CN204027398 U CN 204027398U
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heat exchange
exchange pipe
fin heat
fin
pipe
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俞军
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Wuxi Phaeton Science & Technology Co Ltd
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Abstract

A kind of energy-saving empty bath formula liquid nitrogen converter, comprise fin heat exchange pipe, feed tube, escape pipe, tube connector, frame, it is characterized in that: fin heat exchange pipe is totally ten 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 and the second fin heat exchange pipe lower end connect feed tube, first fin heat exchange pipe side sets gradually second, 3rd, 4th, 5th, 6th, 7th, 8th, 9th, tenth fin heat exchange pipe, first, second, 3rd, 4th fin heat exchange pipe is the heat exchanger tube of band 8 fins.The utility model, by taking between the heat exchanger tube that is arranged side by side alternately connected mode, realizes the raising of vaporization efficency, simultaneously, a main pipeline is connected above every two row fin heat exchange pipes, both saved pipeline material, and reached again the effect of uniform flow samming, improve vaporization efficency.

Description

A kind of energy-saving empty bath formula liquid nitrogen converter
Technical field
The utility model relates to air-bathing gasifier technical field, is specially a kind of energy-saving empty bath formula liquid nitrogen converter.
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, and the difference of pipeline material use amount.
Summary of the invention
The technical problems to be solved in the utility model overcomes existing defect, a kind of energy-saving empty bath formula liquid nitrogen converter is provided, by taking between the heat exchanger tube that is arranged side by side alternately connected mode, realize the raising of vaporization efficency, meanwhile, connect a main pipeline above every two row fin heat exchange pipes, both saved pipeline material, reach again the effect of uniform flow samming, improve vaporization efficency.
The technical solution of the utility model is: a kind of energy-saving empty bath formula liquid nitrogen converter, comprises fin heat exchange pipe, feed tube, escape pipe, tube connector, frame, it is characterized in that: fin heat exchange pipe is totally ten 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 and the second fin heat exchange pipe lower end connect 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, second fin heat exchange pipe, 3rd fin heat exchange pipe, 4th fin heat exchange pipe is the heat exchanger tube of band 8 fins, the 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, the 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, the every two row fin heat exchange pipe upper ends of tenth fin heat exchange pipe connect a main pipeline, symmetrically form, have five main pipelines, first fin heat exchange pipe upper end is connected with the 4th fin heat exchange pipe upper end by tube connector, second fin heat exchange pipe upper end is connected with the 3rd fin heat exchange pipe upper end by tube connector, 3rd fin heat exchange pipe lower end is connected with the 6th fin heat exchange pipe lower 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 and the 6th fin heat exchange pipe upper end connect a section of main pipeline by tube connector, and another section of main pipeline connects the 7th fin heat exchange pipe upper end successively by tube connector, 8th fin heat exchange pipe upper end, 9th fin heat exchange pipe upper end, tenth fin heat exchange pipe upper end, the 7th fin heat exchange pipe lower end and the 8th fin heat exchange pipe lower end are connected to out gas branch pipe, and the 9th fin heat exchange pipe lower end and the tenth fin heat exchange pipe lower end are connected to out gas branch pipe, go out gas branch pipe and are connected to escape pipe.
The beneficial effects of the utility model are: by taking between the heat exchanger tube that is arranged side by side alternately connected mode, i.e. the first fin heat exchange pipe, the 4th fin heat exchange pipe, the 5th fin heat exchange pipe head and the tail connection successively, second fin heat exchange pipe, the 3rd fin heat exchange pipe, the 6th fin heat exchange pipe successively head and the tail connect, form two spaced branch roads, the temperature difference is worked in coordination, and realizes the raising of vaporization efficency.Simultaneously, fin heat exchange pipe is the structure of different fin number, less fin structure is adopted at its porch heat exchanger tube, because fin is few, just fall few in the environment temperature of its surrounding, improve the heat exchange property of fin heat exchange pipe, along with medium temperature progressively heats raising, the increase of heat exchanger tube fin number, can have good heat transfer effect; Simultaneously, the every two row fin heat exchange pipe upper ends of 5th fin heat exchange pipe, the 6th fin heat exchange pipe, the 7th fin heat exchange pipe, the 8th fin heat exchange pipe, the 9th fin heat exchange pipe, the tenth fin heat exchange pipe connect a main pipeline, symmetrically form, compared with connecting a main pipeline with every a line fin heat exchange pipe upper end, save pipeline material half, and this kind of connected mode, can reach the effect of uniform flow samming, 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 A-A place sectional view in Fig. 1.
Fig. 4 is B-B place sectional view in Fig. 1.
Fig. 5 is C place enlarged drawing in Fig. 1.
In Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5,1. 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. main pipelines, 12. feed tubes, 13. escape pipes, 14. go out gas branch pipe, 15. 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, shown in Fig. 5, the utility model is a kind of energy-saving empty bath formula liquid nitrogen converter, comprises fin heat exchange pipe, feed tube 12, escape pipe 13, tube connector, frame 15, it is characterized in that: fin heat exchange pipe is totally ten 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 15 fin number, first fin heat exchange pipe 1 lower end and the second fin heat exchange pipe 2 lower end connect feed tube, and the 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, second fin heat exchange pipe 2, 3rd fin heat exchange pipe 3, 4th fin heat exchange pipe 4 is the heat exchanger tube of band 8 fins, the 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, the 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, the every two row fin heat exchange pipe upper ends of tenth fin heat exchange pipe 10 connect a main pipeline 11, symmetrically form, have five main pipelines 11, first fin heat exchange pipe 1 upper end is connected with the 4th fin heat exchange pipe 4 upper end by tube connector, second fin heat exchange pipe 2 upper end is connected with the 3rd fin heat exchange pipe 3 upper end by tube connector, 3rd fin heat exchange pipe 3 lower end is connected with the 6th fin heat exchange pipe 6 lower 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 and the 6th fin heat exchange pipe 6 upper end connect a section of main pipeline 11 by tube connector, and another section of main pipeline 11 connects the 7th fin heat exchange pipe 7 upper end successively by tube connector, 8th fin heat exchange pipe 8 upper end, 9th fin heat exchange pipe 9 upper end, tenth fin heat exchange pipe 10 upper end, 7th fin heat exchange pipe 7 lower end and the 8th fin heat exchange pipe 8 lower end are connected to out gas branch pipe 14,9th fin heat exchange pipe 9 lower end and the tenth fin heat exchange pipe 10 lower end are connected to out gas branch pipe 14, go out gas branch pipe 14 and are connected to escape pipe 13.
First fin heat exchange pipe 1, second fin heat exchange pipe 2, the 3rd fin heat exchange pipe 3, the 4th fin heat exchange pipe 4, the 5th fin heat exchange pipe 5, the 6th fin heat exchange pipe 6 are arranged in order, but alternately connect when connecting, i.e. the first fin heat exchange pipe 1, the 4th fin heat exchange pipe 4, the 5th fin heat exchange pipe 5 head and the tail connection successively, second fin heat exchange pipe 2, the 3rd fin heat exchange pipe 3, the 6th fin heat exchange pipe 6 successively head and the tail connect, form two spaced branch roads, the temperature difference is worked in coordination, and realizes the raising of vaporization efficency; Simultaneously, fin heat exchange pipe is the structure of different fin number, less fin structure is adopted at its porch heat exchanger tube, because fin is few, just fall few in the environment temperature of its surrounding, improve the heat exchange property of fin heat exchange pipe, along with medium temperature progressively heats raising, the increase of heat exchanger tube fin number, can have good heat transfer effect; Simultaneously, the every two row fin heat exchange pipe upper ends of 5th fin heat exchange pipe 5, the 6th fin heat exchange pipe 6, the 7th fin heat exchange pipe 7, the 8th fin heat exchange pipe 8, the 9th fin heat exchange pipe 9, the tenth fin heat exchange pipe 10 connect a main pipeline 11, symmetrically form, compared with connecting a main pipeline with every a line fin heat exchange pipe upper end, save pipeline material half, and this kind of connected mode, can reach the effect of uniform flow samming, realize the raising of vaporization efficency.
As can be seen here, the utility model, by taking between the heat exchanger tube that is arranged side by side alternately connected mode, realizes the raising of vaporization efficency, meanwhile, connect a main pipeline above every two row fin heat exchange pipes, both saved pipeline material, reach again the effect of uniform flow samming, improve vaporization efficency.

Claims (1)

1. an energy-saving empty bath formula liquid nitrogen converter, comprises fin heat exchange pipe, feed tube, escape pipe, tube connector, frame, it is characterized in that: fin heat exchange pipe is totally ten 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 and the second fin heat exchange pipe lower end connect 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, second fin heat exchange pipe, 3rd fin heat exchange pipe, 4th fin heat exchange pipe is the heat exchanger tube of band 8 fins, the 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, the 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, the every two row fin heat exchange pipe upper ends of tenth fin heat exchange pipe connect a main pipeline, symmetrically form, have five main pipelines, first fin heat exchange pipe upper end is connected with the 4th fin heat exchange pipe upper end by tube connector, second fin heat exchange pipe upper end is connected with the 3rd fin heat exchange pipe upper end by tube connector, 3rd fin heat exchange pipe lower end is connected with the 6th fin heat exchange pipe lower 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 and the 6th fin heat exchange pipe upper end connect a section of main pipeline by tube connector, and another section of main pipeline connects the 7th fin heat exchange pipe upper end successively by tube connector, 8th fin heat exchange pipe upper end, 9th fin heat exchange pipe upper end, tenth fin heat exchange pipe upper end, the 7th fin heat exchange pipe lower end and the 8th fin heat exchange pipe lower end are connected to out gas branch pipe, and the 9th fin heat exchange pipe lower end and the tenth fin heat exchange pipe lower end are connected to out gas branch pipe, go out gas branch pipe and are connected to escape pipe.
CN201420485914.7U 2014-08-21 2014-08-21 A kind of energy-saving empty bath formula liquid nitrogen converter Active CN204027398U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105486148A (en) * 2015-12-31 2016-04-13 无锡辉腾科技有限公司 Finned heat exchange tube for air bath type vaporizer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105486148A (en) * 2015-12-31 2016-04-13 无锡辉腾科技有限公司 Finned heat exchange tube for air bath type vaporizer

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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: Energy-saving air bath type liquid nitrogen 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