CN207065535U - A kind of vapor condensed water waste-heat recovery device - Google Patents
A kind of vapor condensed water waste-heat recovery device Download PDFInfo
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- CN207065535U CN207065535U CN201720908087.1U CN201720908087U CN207065535U CN 207065535 U CN207065535 U CN 207065535U CN 201720908087 U CN201720908087 U CN 201720908087U CN 207065535 U CN207065535 U CN 207065535U
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- water
- centrifugation
- drainpipe
- pipe
- heater
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Abstract
A kind of vapor condensed water waste-heat recovery device is the utility model is related to, including vacuum condenser, heater, the scattered vapour device of centrifugation, water tank, isobaric displacement can and Multistage drainer, the bottom of the vacuum condenser are connected with the bottom of the heater by ammonia pipe；The top that the top of the heater dissipates vapour device with the centrifugation is connected by steam pipe, and its underpart is connected with the bottom that the centrifugation dissipates vapour device by the first drainpipe；The top that the centrifugation dissipates vapour device is connected with the water tank by connecting tube.Compared with the prior art, the utility model heater utilizes the heat syrup of spontaneous evaporation steam, and heater can make full use of waste-heat syrup, can continuous production use, spontaneous evaporation efficiency high, reach the saving energy.
Description
Technical field
Heat recovery technology field is the utility model is related to, more particularly to a kind of vapor condensed water waste-heat recovery device.
Background technology
In the production process of sugar refinery, substantial amounts of moisture evaporation in syrup is fallen, could crystallize, be concentrated by evaporation after syrup concentration
During, substantial amounts of vapor condensed water is produced, can not be finished in the production of these vapor condensed waters, surplus is larger, and these vapor condensed water temperature
Up to 90 degree~95 degree of degree, has compared with multi-energy.Many sugar refinery are directly rejected to these vapor condensed waters in circulating water pool, do not fill
Divide and reclaim its waste heat, cause the significant wastage of the energy, meanwhile, the burden of circulating water processing is also increased, increases power consumption.Mesh
Before, also there is the method that high temperature vapor condensed water is directly heated to low temperature sugarcane juice, make full use of the waste heat of high temperature vapor condensed water, but due to water
Heat transfer coefficient is relatively low, need to consume that equipment is bigger, and organic efficiency is poor, and vapor condensed water also has substantial amounts of waste heat also to underuse.
Utility model content
The purpose of this utility model is to provide a kind of vapor condensed water waste-heat recovery device, and technical problem to be solved is：Water
Heat transfer coefficient it is relatively low, need to consume that equipment is bigger, and organic efficiency is poor, vapor condensed water also has substantial amounts of waste heat also to underuse.
The technical scheme that the utility model solves above-mentioned technical problem is as follows：A kind of vapor condensed water waste-heat recovery device, including
Vacuum condenser, heater, centrifugation dissipate vapour device, water tank, isobaric displacement can and Multistage drainer, under the vacuum condenser
Portion is connected with the bottom of the heater by ammonia pipe；The top that the top of the heater dissipates vapour device with the centrifugation leads to
Steam pipe connection is crossed, and its underpart is connected with the bottom that the centrifugation dissipates vapour device by the first drainpipe；The centrifugation dissipates vapour
The top of device is connected with the water tank by connecting tube；The centrifugation dissipate the bottom of vapour device by the second drainpipe with it is described
The top connection of isobaric displacement can, the centrifugation dissipates the middle part of vapour device and the top of the isobaric displacement can is connected by balance pipe
It is logical；The bottom of the isobaric displacement can is connected with the bottom of the Multistage drainer by water-supply-pipe, the Multistage drainer
Top is connected with the second drainpipe.
The beneficial effects of the utility model are：Vacuum condenser accesses high temperature vapor condensed water, under condition of negative pressure successively
Evaporated vapor is produced from, spontaneous evaporation steam is delivered to heater, heater utilizes the heat syrup of spontaneous evaporation steam, can
Continuous production uses, and spontaneous evaporation efficiency high, reaches the saving energy；Centrifugation dissipates vapour device can be effectively by the cold water progress of water tank input
Vaporization, the cold water vapour after vaporization is inputted to heater by steam pipe, the cold water after vaporization and spontaneous evaporation steam hybrid energy
Further such that the radiating of spontaneous evaporation steam is more complete, heater can make full use of waste-heat syrup.
On the basis of above-mentioned technical proposal, the utility model can also do following improvement.
Further, the centrifugation dissipates the bottom of vapour device and connected with the top of the isobaric displacement can by the second drainpipe
Logical, the middle part that the centrifugation dissipates vapour device is connected with the top of the isobaric displacement can by balance pipe；The isobaric displacement can
Bottom be connected with the bottom of the Multistage drainer by water-supply-pipe, the top of the Multistage drainer is connected with the 3rd draining
Pipe.
It is using the above-mentioned further beneficial effect of scheme：In heater liquefied water by the first drainpipe transmit to from
The heart dissipates vapour device, centrifuges scattered vapour device and liquefied water is transmitted to isobaric displacement can, balance pipe and can put down by the second drainpipe again
Weighing apparatus centrifugation dissipates the air pressure in vapour device and isobaric displacement can, and isobaric displacement can is again transmitted liquefied water to multistage by water-supply-pipe
Water trap, Multistage drainer are again discharged liquefied water by the 3rd drainpipe, realize liquefied water recycling.
Further, the ammonia pipe, steam pipe, the first drainpipe, connecting tube, the second drainpipe, balance pipe, water-supply-pipe and
Switch valve is provided with second drainpipe.
It is using the above-mentioned further beneficial effect of scheme：Switch valve is easy to adjust the flow of air-flow or current, is easy to pair
Whole device is controlled.
Further, the upper inner of the isobaric displacement can is provided with water feed apparatus, the water feed apparatus and the water tank
Connected by connecting tube.
It is using the above-mentioned further beneficial effect of scheme：Water feed apparatus can carry out water-carrying capacity with regulating tank, and control is cold
Water vapor efficiency, lift utilization rate of waste heat.
Brief description of the drawings
Fig. 1 is a kind of connection diagram of vapor condensed water waste-heat recovery device of the utility model.
In accompanying drawing, the list of parts representated by each label is as follows：
1st, vacuum condenser, 2, heater, 3, centrifugation dissipate vapour device, 4, water tank, 5, isobaric displacement can, 6, multistage draining
Device, 7, ammonia pipe, 8, steam pipe, the 9, first drainpipe, 10, connecting tube, the 11, second drainpipe, 12, balance pipe, 13, water delivery
Pipe, the 14, the 3rd drainpipe, 15, switch valve.
Embodiment
Principle of the present utility model and feature are described below in conjunction with accompanying drawing, example is served only for explaining this practicality
It is new, it is not intended to limit the scope of the utility model.
As shown in figure 1, a kind of vapor condensed water waste-heat recovery device, including vacuum condenser 1, heater 2, the scattered vapour device of centrifugation
3rd, water tank 4, isobaric displacement can 5 and Multistage drainer 6, the bottom of the vacuum condenser 1 and the bottom of the heater 2 pass through
Ammonia pipe 7 connects；The top that the top of the heater 2 dissipates vapour device 3 with the centrifugation is connected by steam pipe 8, and under it
The bottom that portion dissipates vapour device 3 with the centrifugation is connected by the first drainpipe 9；The centrifugation dissipate the top of vapour device 3 with it is described
Water tank 4 is connected by connecting tube 10.
Vacuum condenser 1 accesses high temperature vapor condensed water, evaporated vapor is successively produced under condition of negative pressure, by spontaneous evaporation
Steam is delivered to heater 2, heater 2 using spontaneous evaporation steam heat syrup, can continuous production use, spontaneous evaporation effect
Rate is high, reaches the saving energy；Centrifugation, which dissipates vapour device 3, to be effectively vaporized the cold water that water tank 4 inputs, by the cold water after vaporization
Vapour is inputted to heater 2 by steam pipe 8, and the cold water after vaporization is with spontaneous evaporation steam hybrid energy further such that spontaneous evaporation is steamed
Steam and heat sinking is more complete, and heater 2 can make full use of waste-heat syrup.
In above-described embodiment, the bottom that the centrifugation dissipates vapour device 3 passes through the second drainpipe 11 and the isobaric displacement can 5
Top connection, the middle part that the centrifugation dissipates vapour device 3 is connected with the top of the isobaric displacement can 5 by balance pipe 12；Institute
The bottom for stating isobaric displacement can 5 is connected with the bottom of the Multistage drainer 6 by water-supply-pipe 13, the Multistage drainer 6
Top is connected with the 3rd drainpipe 14.
Liquefied water is transmitted to centrifugation by the first drainpipe 9 in heater 2 dissipates vapour device 3, centrifuges scattered vapour device 3 and again will
Liquefied water is transmitted to isobaric displacement can 5, the energy equilibrium centrifugation of balance pipe 12 by the second drainpipe 11 to be dissipated vapour device 3 and waits pressure
Air pressure in water pot 5, isobaric displacement can 5 are again transmitted liquefied water to Multistage drainer 6, Multistage drainer by water-supply-pipe 13
6 are again discharged liquefied water by the 3rd drainpipe 14, realize liquefied water recycling.
It is the ammonia pipe 7, steam pipe 8, the first drainpipe 9, connecting tube 10, the second drainpipe 11, flat in above-described embodiment
Switch valve 15 is provided with weighing apparatus pipe 12, the drainpipe 14 of water-supply-pipe 13 and the 3rd.
Switch valve 15 is easy to adjust the flow of air-flow or current, is easy to be controlled whole device.
In above-described embodiment, the upper inner of the isobaric displacement can 5 is provided with water feed apparatus, the water feed apparatus and institute
Water tank 4 is stated to connect by connecting tube 10.
Water feed apparatus can carry out water-carrying capacity with regulating tank 4, control cold water vaporization efficency, lift utilization rate of waste heat.
Preferred embodiment of the present utility model is the foregoing is only, it is all in this practicality not to limit the utility model
Within new spirit and principle, any modification, equivalent substitution and improvements made etc., guarantor of the present utility model should be included in
Within the scope of shield.
Claims (4)
- A kind of 1. vapor condensed water waste-heat recovery device, it is characterised in that：Vapour is dissipated including vacuum condenser (1), heater (2), centrifugation Device (3), water tank (4), isobaric displacement can (5) and Multistage drainer (6), the bottom of the vacuum condenser (1) add with described The bottom of hot device (2) is connected by ammonia pipe (7)；The top of the heater (2) dissipates the top of vapour device (3) with the centrifugation Connected by steam pipe (8), and its underpart is connected with the bottom that the centrifugation dissipates vapour device (3) by the first drainpipe (9)；Institute The top for stating the scattered vapour device (3) of centrifugation is connected with the water tank (4) by connecting tube (10).
- A kind of 2. vapor condensed water waste-heat recovery device according to claim 1, it is characterised in that：The centrifugation dissipates vapour device (3) Bottom connected with the top of the isobaric displacement can (5) by the second drainpipe (11), it is described centrifugation dissipate vapour device (3) in Portion is connected with the top of the isobaric displacement can (5) by balance pipe (12)；The bottom of the isobaric displacement can (5) with it is described more The bottom of level water trap (6) is connected by water-supply-pipe (13), and the top of the Multistage drainer (6) is connected with the 3rd drainpipe (14)。
- A kind of 3. vapor condensed water waste-heat recovery device according to claim 2, it is characterised in that：The ammonia pipe (7), steam pipe (8), the first drainpipe (9), connecting tube (10), the second drainpipe (11), balance pipe (12), water-supply-pipe (13) and the 3rd drainpipe (14) switch valve (15) is provided with.
- 4. according to a kind of any one of claims 1 to 3 vapor condensed water waste-heat recovery device, it is characterised in that：It is described to wait pressure The upper inner of water pot (5) is provided with water feed apparatus, and the water feed apparatus is connected with the water tank (4) by connecting tube (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720908087.1U CN207065535U (en) | 2017-07-25 | 2017-07-25 | A kind of vapor condensed water waste-heat recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720908087.1U CN207065535U (en) | 2017-07-25 | 2017-07-25 | A kind of vapor condensed water waste-heat recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207065535U true CN207065535U (en) | 2018-03-02 |
Family
ID=61517406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720908087.1U Expired - Fee Related CN207065535U (en) | 2017-07-25 | 2017-07-25 | A kind of vapor condensed water waste-heat recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207065535U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107300165A (en) * | 2017-07-25 | 2017-10-27 | 广西农垦糖业集团红河制糖有限公司 | A kind of vapor condensed water waste-heat recovery device |
-
2017
- 2017-07-25 CN CN201720908087.1U patent/CN207065535U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107300165A (en) * | 2017-07-25 | 2017-10-27 | 广西农垦糖业集团红河制糖有限公司 | A kind of vapor condensed water waste-heat recovery device |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180302 Termination date: 20190725 |