CN204154008U - A kind of fermentation tank sterilization waste hot steam heat reclamation device - Google Patents
A kind of fermentation tank sterilization waste hot steam heat reclamation device Download PDFInfo
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- CN204154008U CN204154008U CN201420542246.7U CN201420542246U CN204154008U CN 204154008 U CN204154008 U CN 204154008U CN 201420542246 U CN201420542246 U CN 201420542246U CN 204154008 U CN204154008 U CN 204154008U
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Abstract
The utility model discloses a kind of fermentation tank sterilization waste hot steam heat reclamation device, comprise fermentation tank sterilization waste hot steam discharge pipe, whirlwind separator, First Heat Exchanger, boiler, circulating pump and the second heat exchanger, fermentation tank sterilization waste hot steam discharge pipe is communicated with the air inlet of whirlwind separator, the gas outlet of whirlwind separator is communicated with the hot inlet of First Heat Exchanger, the cold flow outlet of First Heat Exchanger is communicated with the cold inlet of First Heat Exchanger through hot water cyclesystem, hot water circulating device comprises the boiler by pipeline connection, circulating pump and the second heat exchanger, hot water circulating device is communicated with water source by water compensating valve.The utility model has the features such as recuperation of heat utilization rate is high, energy-saving and environmental protection.
Description
Technical field
The utility model relates to a kind of fermentation tank sterilization waste hot steam heat reclamation device.
Background technology
In current biological fermentation engineering, extensively high, large-minded by the vapor (steam) temperature got rid of after moise-heat sterilization, sterilization, be directly discharged in the industry at present, cause a large amount of energy wastes.High-temperature tail gas discharge also pollutes environment simultaneously.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of fermentation tank sterilization waste hot steam heat reclamation device, the features such as recuperation of heat utilization rate is high, energy-saving and environmental protection that it has.
For solving the problems of the technologies described above, technical solution adopted in the utility model is:
A kind of fermentation tank sterilization waste hot steam heat reclamation device, comprise fermentation tank sterilization waste hot steam discharge pipe, whirlwind separator, First Heat Exchanger, boiler, circulating pump and the second heat exchanger, fermentation tank sterilization waste hot steam discharge pipe is communicated with the air inlet of whirlwind separator, the gas outlet of whirlwind separator is communicated with the hot inlet of First Heat Exchanger, the cold flow outlet of First Heat Exchanger is communicated with the cold inlet of First Heat Exchanger through hot water cyclesystem, hot water circulating device comprises the boiler by pipeline connection, circulating pump and the second heat exchanger, hot water circulating device is communicated with water source by water compensating valve.
The utility model improves further and is:
Whirlwind separator is positioned at the below of First Heat Exchanger, the top of First Heat Exchanger is provided with steam-water separator, the import of steam-water separator is communicated with the hot outlets of First Heat Exchanger, the center line of whirlwind separator, First Heat Exchanger and steam-water separator coincides, be provided with header tank below the discharge outlet of whirlwind separator, header tank is communicated with boiler.
Hot water circulating device also comprises electronic scale remover.
The cold inlet of First Heat Exchanger is communicated with header tank by antifreeze tapping valve.
The beneficial effect adopting technique scheme to produce is:
The utility model comprises fermentation tank sterilization waste hot steam discharge pipe, whirlwind separator, First Heat Exchanger, boiler, circulating pump and the second heat exchanger, fermentation tank sterilization waste hot steam discharge pipe is communicated with the air inlet of whirlwind separator, the gas outlet of whirlwind separator is communicated with the hot inlet of First Heat Exchanger, the cold flow outlet of First Heat Exchanger is communicated with the cold inlet of First Heat Exchanger through hot water cyclesystem, hot water circulating device comprises by the boiler of pipeline connection, circulating pump and the second heat exchanger, and hot water circulating device is communicated with water source by water compensating valve.The cooling water (high-temperature water) of First Heat Exchanger 3 circulates through hot water cyclesystem, heat exchange is carried out to the steam entering First Heat Exchanger 3 and absorbs heat, simultaneously in the second heat exchanger 6 release heat, waste heat recovery recycling is carried out by the cooling water of the second heat exchanger 6, when the heating agent (water) of hot water cyclesystem produces certain loss, carry out supply by water compensating valve 8.Whirlwind separator is positioned at the below of First Heat Exchanger, the top of First Heat Exchanger is provided with steam-water separator, the import of steam-water separator is communicated with the hot outlets of First Heat Exchanger, the center line of whirlwind separator, First Heat Exchanger and steam-water separator coincides, be provided with header tank below the discharge outlet of whirlwind separator, header tank is communicated with boiler.Condensed water is reclaimed, has saved water resource.The utility model has the features such as recuperation of heat utilization rate is high, energy-saving and environmental protection.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In the accompanying drawings: 1, fermentation tank sterilization waste hot steam discharge pipe; 2, whirlwind separator; 3, First Heat Exchanger; 4, boiler; 5, circulating pump; 6, the second heat exchanger; 7, water source; 8, water compensating valve; 9, steam-water separator; 10, header tank; 11, electronic scale remover; 12, antifreeze tapping valve.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is further elaborated.
Embodiment is as shown in Figure 1 known, the present embodiment comprises fermentation tank sterilization waste hot steam discharge pipe 1, whirlwind separator 2, First Heat Exchanger 3, boiler 4, circulating pump 5 and the second heat exchanger 6, fermentation tank sterilization waste hot steam discharge pipe 1 is communicated with the air inlet of whirlwind separator 2, the gas outlet of whirlwind separator 2 is communicated with the hot inlet of First Heat Exchanger 3, the cold flow outlet of First Heat Exchanger 3 is communicated with through the cold inlet of hot water cyclesystem with First Heat Exchanger 3, hot water circulating device comprises the boiler 4 by pipeline connection, circulating pump 5 and the second heat exchanger 6, hot water circulating device is communicated with water source 7 by water compensating valve 8.
The present embodiment whirlwind separator 2 is positioned at the below of First Heat Exchanger 3, the top of First Heat Exchanger 3 is provided with steam-water separator 9, the import of steam-water separator 9 is communicated with the hot outlets of First Heat Exchanger 3, the center line of whirlwind separator 2, First Heat Exchanger 3 and steam-water separator 9 coincides, be provided with header tank 10 below the discharge outlet of whirlwind separator 2, header tank 10 is communicated with boiler 4.
The present embodiment hot water circulating device also comprises electronic scale remover 11.
Operation principle:
Solid particle polluter to be separated through whirlwind separator 2 and to reduce steam flow rate with the impact of minimizing to equipment by fermentation tank sterilization waste hot steam discharge pipe 1 high velocity vapor of discharging, enter First Heat Exchanger 3 afterwards and carry out heat exchange, carry out the residue preventing trace amount of steam after heat exchange to be separated through steam-water separator 9, the high-temperature water become by steam-condensation is recycled to header tank 10 after being separated; Pump into boiler 4 again.
The cooling water (high-temperature water) of First Heat Exchanger 3 circulates through hot water cyclesystem, heat exchange is carried out to the steam entering First Heat Exchanger 3 and absorbs heat, simultaneously in the second heat exchanger 6 release heat, waste heat recovery recycling is carried out by the cooling water of the second heat exchanger 6, when the heating agent (water) of hot water cyclesystem produces certain loss, carry out supply by water compensating valve 8.
Claims (4)
1. a fermentation tank sterilization waste hot steam heat reclamation device, it is characterized in that: comprise fermentation tank sterilization waste hot steam discharge pipe (1), whirlwind separator (2), First Heat Exchanger (3), boiler (4), circulating pump (5) and the second heat exchanger (6), described fermentation tank sterilization waste hot steam discharge pipe (1) is communicated with the air inlet of whirlwind separator (2), the gas outlet of described whirlwind separator (2) is communicated with the hot inlet of First Heat Exchanger (3), the cold flow outlet of described First Heat Exchanger (3) is communicated with through the cold inlet of hot water cyclesystem with First Heat Exchanger (3), described hot water circulating device comprises by the boiler of pipeline connection (4), circulating pump (5) and the second heat exchanger (6), described hot water circulating device is communicated with water source (7) by water compensating valve (8).
2. a kind of fermentation tank sterilization waste hot steam heat reclamation device according to claim 1, it is characterized in that: described whirlwind separator (2) is positioned at the below of First Heat Exchanger (3), the top of described First Heat Exchanger (3) is provided with steam-water separator (9), the import of described steam-water separator (9) is communicated with the hot outlets of described First Heat Exchanger (3), described whirlwind separator (2), the center line of First Heat Exchanger (3) and steam-water separator (9) coincides, header tank (10) is provided with below the discharge outlet of described whirlwind separator (2), described header tank (10) is communicated with boiler (4).
3. a kind of fermentation tank sterilization waste hot steam heat reclamation device according to claim 1, is characterized in that: described hot water circulating device also comprises electronic scale remover (11).
4. a kind of fermentation tank sterilization waste hot steam heat reclamation device according to claim 2, is characterized in that: the cold inlet of described First Heat Exchanger (3) is communicated with header tank (10) by antifreeze tapping valve (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420542246.7U CN204154008U (en) | 2014-09-17 | 2014-09-17 | A kind of fermentation tank sterilization waste hot steam heat reclamation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420542246.7U CN204154008U (en) | 2014-09-17 | 2014-09-17 | A kind of fermentation tank sterilization waste hot steam heat reclamation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204154008U true CN204154008U (en) | 2015-02-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420542246.7U Expired - Fee Related CN204154008U (en) | 2014-09-17 | 2014-09-17 | A kind of fermentation tank sterilization waste hot steam heat reclamation device |
Country Status (1)
| Country | Link |
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| CN (1) | CN204154008U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105462814A (en) * | 2016-01-21 | 2016-04-06 | 王新东 | Efficient and energy-saving type biological fermentation tank and matched pipe network system thereof |
| CN108949508A (en) * | 2018-08-29 | 2018-12-07 | 天津科技大学 | A kind of fermentor residual neat recovering system and waste heat reclaiming process |
-
2014
- 2014-09-17 CN CN201420542246.7U patent/CN204154008U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105462814A (en) * | 2016-01-21 | 2016-04-06 | 王新东 | Efficient and energy-saving type biological fermentation tank and matched pipe network system thereof |
| CN105462814B (en) * | 2016-01-21 | 2018-09-18 | 王新东 | High-efficiency and energy-saving type biological fermentation tank and its mating pipe network system |
| CN108949508A (en) * | 2018-08-29 | 2018-12-07 | 天津科技大学 | A kind of fermentor residual neat recovering system and waste heat reclaiming process |
| CN108949508B (en) * | 2018-08-29 | 2023-10-03 | 天津科技大学 | Fermentation tank waste heat recovery system and waste heat recovery process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 055550 Xicheng District Xinxing Road, Ningjin, Hebei, China, No. 116, No. Patentee after: Hebei Yuxing bioengineering Limited by Share Ltd Address before: 055550 Xicheng District Xinxing Road, Ningjin, Hebei, China, No. 116, No. Patentee before: Hebei Yuxing Biological Engineering Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150211 Termination date: 20190917 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |