CN103017387A - Vapor condensed water waste heat utilizing device in production - Google Patents
Vapor condensed water waste heat utilizing device in production Download PDFInfo
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- CN103017387A CN103017387A CN2012105433541A CN201210543354A CN103017387A CN 103017387 A CN103017387 A CN 103017387A CN 2012105433541 A CN2012105433541 A CN 2012105433541A CN 201210543354 A CN201210543354 A CN 201210543354A CN 103017387 A CN103017387 A CN 103017387A
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- vapour
- condensed water
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- heat exchanger
- water inlet
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Abstract
The invention relates to a waste heat collection and utilizing device of vapor condensed water, in particular to a vapor condensed water waste heat utilizing device in the production. The vapor condensed water waste heat utilizing device comprises a vapor condensed water input pipe, wherein the pipe is connected with a heat exchanger, the heat exchanger is provided with a water return pipe, a vapor condensed water input pipe is serially connected with a heat mixer, and the heat mixer is provided with multiple vapor condensed water inlet; and the heat mixer is provided with a water outlet pipe, and the water outlet pipe is connected with a heat exchanger. The vapor condensed water waste heat utilizing device has the characteristics of compact structure, small land occupation area, high efficiency, large flexibility in operation, wide application range, convenience in installation and washing and the like and meets the energy-saving and environment-friendly requirement of the state on enterprises.
Description
Technical field
The present invention relates to the residual heat collection use device of steam condensate (SC), specifically the solidifying water residual heat using device of vapour in a kind of production.
Background technology
Need to use vapours to heat production in many industrial production, and all can condensation go out a large amount of water in steam uses, this part water contains a large amount of heat energy, but general just by the pipeline backflow, and its heat is not fully utilized.Such as, in engineering of producing crystalline dextrose, just need a large amount of steam, in the process that consumes a large amount of steam, tend to produce the solidifying water of a large amount of vapour during actual production, all have higher heat enthalpy value in the solidifying water of these vapour that just produced.Existing equipment is the solidifying water of simple application vapour and ignored heat in the solidifying water of vapour, because the solidifying coolant-temperature gage of vapour is uneven, can't directly utilize, so existing equipment just simply cools to the solidifying water of vapour, cause thermal loss, simultaneously resource is also caused serious waste.
Summary of the invention
Purpose of the present invention is exactly the problem that exists for solving prior art, and has designed the solidifying water residual heat using device of vapour in a kind of production.
Technical scheme of the present invention is: the solidifying water residual heat using device of vapour in a kind of production, comprise that vapour coagulates water inlet pipe, be connected with heat exchanger on the pipeline, heat exchanger is provided with return pipe, be in series with mixed hot device on the solidifying water inlet pipe of described vapour, described mixed hot device is provided with the solidifying water inlet of a plurality of vapour; Described mixed hot device is provided with an outlet pipe, and described outlet pipe is connected with heat exchanger.
The solidifying water inlet of described vapour connects the solidifying water inlet pipe of vapour of different temperatures, is equipped with flowmeter and solenoid electric valve on every solidifying water inlet pipe of vapour.
In order to allocate the water temperature in the mixed hot device, described mixed hot device is provided with cold water inlet.
In order when the solidifying coolant-temperature gage of vapour is not enough, to improve temperature, be provided with electric heater unit in the described mixed hot device, be provided with simultaneously temperature sensor in the mixed hot device and can monitor at any time water temperature in the mixed hot device.
In order to improve heat exchanger effectiveness, simplification device, described heat exchanger are plate type heat exchanger.
Beneficial effect of the present invention can draw by such scheme: owing to be added with mixed hot device before heat exchanger, the solidifying water of vapour of different temperatures is mixed first in mixed hot device, reach suitable temperature and enter heat exchanger again, make heat-exchange system more stable.The characteristics such as the present invention has compact conformation, floor space is little, efficient is high, operating flexibility is large, applied range, installation and easy to clean meet current national to the requirement of industry energy conservation environmental protection.
This shows that the present invention compared with prior art has substantive distinguishing features and progress, the beneficial effect of its enforcement also is apparent.
Description of drawings:
Fig. 1 is structural representation of the present invention;
Wherein, 1 is the solidifying water inlet pipe I of vapour, and 2 are the solidifying water inlet pipe II of vapour, and 3 are the solidifying water inlet pipe II of vapour, and 4 are mixed hot device, and 5 is cold water inlet, and 6 is temperature sensor, and 7 is return pipe, and 8 are, 9 are, 10 are.
The specific embodiment:
In order to understand better the present invention, explain in detail embodiments of the present invention below in conjunction with accompanying drawing.
The specific embodiment: as shown in Figure 1, the solidifying water residual heat using device of vapour in a kind of production, comprise mixed hot device 4, be connected with the solidifying water inlet pipe I 1 of vapour, the solidifying water inlet pipe II 2 of vapour, the solidifying water inlet pipe III 3 of vapour on the mixed hot device, mixed hot device 4 is provided with an outlet pipe and is connected with heat exchanger 8, and heat exchanger is provided with return pipe 7.Described mixed hot device 4 is provided with cold water inlet 5.Be equipped with flowmeter 10 and solenoid electric valve 9 on every vapour solidifying water inlet pipe, outlet pipe and the cold water pipe.Be provided with electric heater unit 1 in the described mixed hot device 4; Be provided with temperature sensor 6 in the mixed hot device 4.Described heat exchanger 8 is plate type heat exchanger.
Above-mentioned explanation is not to be limitation of the present invention, and the present invention also is not limited in above-mentioned giving an example, and the variation that those skilled in the art make in essential scope of the present invention, remodeling, interpolation or replacement also should belong to protection scope of the present invention.
Claims (5)
1. the solidifying water residual heat using device of vapour in the production, comprise that vapour coagulates water inlet pipe, be connected with heat exchanger on the pipeline, heat exchanger is provided with return pipe, it is characterized in that: be in series with mixed hot device on the solidifying water inlet pipe of described vapour, described mixed hot device is to be provided with the solidifying water inlet of a plurality of vapour; Described mixed hot device is provided with an outlet pipe, and described outlet pipe is connected with heat exchanger.
2. vapour coagulates the water residual heat using device in the production as claimed in claim 1, it is characterized in that: the solidifying water inlet of described vapour connects the solidifying water inlet pipe of vapour of different temperatures, is equipped with flowmeter and solenoid electric valve on every solidifying water inlet pipe of vapour.
3. vapour coagulates the water residual heat using device in the production as claimed in claim 1, it is characterized in that: described mixed hot device is provided with cold water inlet.
4. the solidifying water residual heat using device of vapour in the production as claimed in claim 3 is characterized in that: be provided with electric heater unit in the described mixed hot device; Be provided with temperature sensor in the mixed hot device.
5. vapour coagulates the water residual heat using device in the production as claimed in claim 1, and it is characterized in that: described heat exchanger is plate type heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105433541A CN103017387A (en) | 2012-12-16 | 2012-12-16 | Vapor condensed water waste heat utilizing device in production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105433541A CN103017387A (en) | 2012-12-16 | 2012-12-16 | Vapor condensed water waste heat utilizing device in production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103017387A true CN103017387A (en) | 2013-04-03 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012105433541A Pending CN103017387A (en) | 2012-12-16 | 2012-12-16 | Vapor condensed water waste heat utilizing device in production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103017387A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1880881A (en) * | 2005-06-13 | 2006-12-20 | 山东西王糖业有限公司 | Closed type recovery and utilization method for steam condensed water |
| CN1951829A (en) * | 2006-06-07 | 2007-04-25 | 江苏天舒电器有限公司 | Waste heat circulation energy-saving printing and dyeing water utilization method and system |
| CN202576403U (en) * | 2012-06-01 | 2012-12-05 | 宁波中瑞生物科技有限公司 | Cooling water circulating device for fermentation tank |
-
2012
- 2012-12-16 CN CN2012105433541A patent/CN103017387A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1880881A (en) * | 2005-06-13 | 2006-12-20 | 山东西王糖业有限公司 | Closed type recovery and utilization method for steam condensed water |
| CN1951829A (en) * | 2006-06-07 | 2007-04-25 | 江苏天舒电器有限公司 | Waste heat circulation energy-saving printing and dyeing water utilization method and system |
| CN202576403U (en) * | 2012-06-01 | 2012-12-05 | 宁波中瑞生物科技有限公司 | Cooling water circulating device for fermentation tank |
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Application publication date: 20130403 |