CN210952412U - High-efficient multistage condensation water pitcher structure - Google Patents
High-efficient multistage condensation water pitcher structure Download PDFInfo
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- CN210952412U CN210952412U CN201921629866.3U CN201921629866U CN210952412U CN 210952412 U CN210952412 U CN 210952412U CN 201921629866 U CN201921629866 U CN 201921629866U CN 210952412 U CN210952412 U CN 210952412U
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- heat exchange
- tank
- tray
- atomizing
- condensing
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Abstract
The utility model relates to a high-efficient multistage condensation water pitcher structure, including bearing the base, the condensate tank, the heat transfer board, a heat exchanger, the atomizing spout, the atomizing pump, the circulating pump, waste heat recovery device and control circuit, the condensate tank is connected with bearing the base up end, the condensate tank includes the jar body and bears the tray, the tray inlays in jar internally, cut apart into a condensation chamber and a catch chamber with jar body top-down, atomizing spout equipartition is bearing the tray up end, the heat transfer board inlays in the condensation chamber and distributes along condensation chamber axis top-down, the heat exchanger inlays in the catch chamber, the atomizing pump, the circulating pump, waste heat recovery device and control circuit all inlay in bearing the base. The utility model discloses an aspect simple structure integrates the degree height, and the commonality is good, and on the other hand system operation energy consumption is low to can effectively improve the waste heat resource recovery utilization ratio in the comdenstion water, thereby reach the purpose that improves comdenstion water recovery regeneration efficiency and reduce the operating cost.
Description
Technical Field
The utility model relates to a condensate water treatment device, exactly a high-efficient multistage condensation water pitcher structure.
Background
In industrial production, especially in the operation of equipment such as industrial kilns and crucibles, a large amount of condensed water is used or generated and needs to be recycled, but the condensed water returned by the equipment such as the industrial kilns and the like is often the water body with too high temperature or the high temperature steam and the steam are mixed with the water body, so the condensed water needs to be recycled after condensation, therefore, a condensation tank is one of important equipment for recycling the condensed water, the usage amount is large, the currently used condensation tank equipment is often the heat exchange operation between one or more heat exchangers arranged in a closed cavity and the high temperature returned condensed water, on one hand, the high temperature condensed water is cooled, on the other hand, the waste heat of the high temperature condensed water is recycled, and although the traditional condensation water tank equipment can meet the use requirements, the equipment has large structure, complex structure, low integration degree, low cost and the like, The construction and maintenance difficulty is large, the cost is high, meanwhile, the heat exchange efficiency is balanced and lower, the current condensing tank can only meet the cooling operation requirements of condensed water in specific forms such as water bodies and steam, the use flexibility and the universality are relatively poor, and the actual use requirements are difficult to effectively meet.
Therefore, in order to solve the above problems, it is urgently needed to develop a new structure of the condensate tank to meet the needs of practical use.
SUMMERY OF THE UTILITY MODEL
To exist not enough on the prior art, the utility model provides a high-efficient multistage condensation water pitcher structure, this utility model discloses an aspect simple structure integrates the degree height, and the commonality is good, can effectively satisfy the needs that high-temperature water, high-temperature steam and high-temperature vapor mixture high-efficient condensation retrieved the operation, and on the other hand system operation energy consumption is low to can effectively improve the waste heat resource recovery utilization ratio in the condensate water, thereby reach the purpose that improves condensate water recovery regeneration efficiency and reduce the working cost.
In order to achieve the above purpose, the utility model discloses a realize through following technical scheme:
a high-efficiency multistage condensed water tank structure comprises a bearing base, a condensing tank, heat exchange plates, a heat exchanger, atomizing nozzles, an atomizing pump, a circulating pump, a waste heat recovery device, a temperature sensor and a control circuit, wherein the bearing base is a frame structure with a rectangular cross section and is distributed in parallel with a horizontal plane, at least one condensing tank is connected with the upper end face of the bearing base, the axis of the condensing tank is distributed in a way of being vertical to the horizontal plane, the condensing tank comprises a tank body and a bearing tray, the tank body is a closed cavity structure with a rectangular axial cross section, a water outlet is formed in the bottom of the tank body, an emergency pressure relief valve is formed in the top of the tank body, a water inlet, at least one heat exchange medium inlet and at least one heat exchange medium return port are formed in the side wall of the condensing tank, the tray is embedded in the tank body and is distributed coaxially with the tank body, the interval between the tray, the tray is uniformly provided with a plurality of through holes, the condensation chamber and the water storage chamber are communicated with each other through the through holes, a plurality of atomizing nozzles are arranged on the upper end surface of the bearing tray in an evenly distributed mode around the axis of the bearing tray, an included angle of 0-60 degrees is formed between the atomizing nozzles, the atomizing nozzles are connected in parallel and are respectively communicated with the water inlet through a guide pipe, at least two heat exchange plates are embedded in the condensation chamber and are distributed from top to bottom along the axis of the condensation chamber, the heat exchange plates are in a round platform-shaped hollow tubular structure coaxially distributed with the condensation chamber, each heat exchange plate is connected with the inner surface of the tank body corresponding to the condensation chamber through a bearing keel, the outer diameter of the lower end surface of each heat exchange plate is 80-90% of the inner diameter of the condensation chamber, the outer diameter of the upper end surface is 10-30% of the inner diameter of the condensation chamber, the heat exchange plates are mutually connected in parallel and are respectively, temperature sensor quantity and heat transfer board, heat exchanger quantity are unanimous, all establish at least one temperature sensor on every heat transfer board, the heat exchanger, atomizing pump, circulating pump, waste heat recovery device and control circuit all inlay in bearing the weight of the base, wherein the water inlet intercommunication of atomizing pump and condensate tank, waste heat recovery device passes through the heat transfer medium inflow mouth and the heat transfer medium backward flow mouth intercommunication of circulating pump and condensate tank, control circuit respectively with atomizing pump, circulating pump, waste heat recovery device, temperature sensor electrical connection.
Furthermore, when the number of the condensing tanks is two or more, the condensing tanks are connected in parallel and are uniformly distributed around the axis of the bearing base.
Furthermore, the height of the bearing base is 1/5-1/2 of the height of the condensation tank, the bottom of the condensation tank is embedded in the bearing base, and the distance between the bottom of the condensation tank and the bottom of the bearing base is 1/4-3/4 of the height of the bearing base.
Further, the heat transfer board include heat exchange tube, corrugated metal plate, wherein the corrugated metal plate cladding is at heat exchange tube up end and terminal surface down, and parallel distribution between the corrugated metal plate of heat exchange tube up end and terminal surface down.
Furthermore, a plurality of through holes are uniformly distributed on the metal corrugated plate, the aperture of each through hole is not more than 3 mm, the axial line of each through hole is parallel to the axial line of the condensation tank, and the total area of the through holes is 30% -60% of the total area of the surface of the metal corrugated plate.
Furthermore, in the heat exchange plates, the distance between two adjacent heat exchange plates is not less than 10 cm,
furthermore, the bearing keel is of an annular frame structure which is coaxially distributed with the condensing tank.
Furthermore, the control circuit is a circuit system based on a DSP chip, and is additionally provided with at least one serial port data communication port.
The utility model discloses an aspect simple structure integrates the degree height, and the commonality is good, can effectively satisfy the needs of the high-efficient condensation recovery operation of high-temperature water, high-temperature steam and high-temperature water vapor mixture, and on the other hand system operation energy consumption is low to can effectively improve waste heat resource recovery utilization ratio in the condensate water, thereby reach the purpose that improves comdenstion water recovery regeneration efficiency and reduce the operating cost.
Drawings
The present invention will be described in detail with reference to the accompanying drawings and specific embodiments;
fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
In order to make the utility model realize, the technical end, the creation characteristics, the achievement purpose and the efficacy are easy to understand and understand, and the utility model is further explained by combining the specific implementation mode.
Fig. 1 shows a high-efficiency multistage condensed water tank structure, which comprises a bearing base 1, a condensing tank 2, a heat exchange plate 3, a heat exchanger 4, an atomizing nozzle 5, an atomizing pump 6, a circulating pump 7, a waste heat recovery device 8, a temperature sensor 9 and a control circuit, wherein the bearing base 1 is a frame structure with a rectangular cross section and is distributed in parallel with a horizontal plane, and at least one condensing tank 2 is connected with the upper end face of the bearing base 1 and is distributed with the axis thereof vertical to the horizontal plane.
In this embodiment, the condensing tank 2 includes a tank 21 and a carrying tray 22, wherein the tank 21 is a closed cavity structure with a rectangular axial cross section, the bottom of the tank is provided with a water outlet 23, the top of the tank is provided with an emergency pressure relief valve 24, the side wall of the tank is provided with a water inlet 25, at least one heat exchange medium inlet 26 and at least one heat exchange medium return port 27, the tray 22 is embedded in the tank 21 and coaxially distributed with the tank 21, the distance between the tray 22 and the bottom of the tank 21 is 1/5-1/2 of the effective height of the tank 21, the tray 22 divides the tank 21 into a condensing chamber 101 and a water storage chamber 102 from top to bottom, the tray is uniformly distributed with a plurality of through holes 28, the condensing chamber 101 and the water storage chamber 102 are mutually communicated through the through holes 28, a plurality of atomizing nozzles 5 are uniformly distributed on the upper end surface of the carrying tray 22 around the, the atomizing nozzles 5 are connected in parallel and are respectively communicated with the water inlet 25 through a guide pipe, at least two heat exchange plates 3 are embedded in the condensing chamber 101 and are distributed from top to bottom along the axis of the condensing chamber 101, the heat exchange plates 3 are in a round platform-shaped hollow tubular structure which is coaxially distributed with the condensing chamber 101, each heat exchange plate 3 is connected with the inner surface of the tank body corresponding to the condensing chamber 101 through a bearing keel 11, the outer diameter of the lower end surface of each heat exchange plate 3 is 80% -90% of the inner diameter of the condensing chamber 101, the outer diameter of the upper end surface of each heat exchange plate 3 is 10% -30% of the inner diameter of the condensing chamber 101, the heat exchange plates 3 are connected in parallel and are respectively communicated with a heat exchange medium inflow 26 port and a heat exchange medium return port 27 through guide pipes, at least one heat exchanger 4 is embedded in the water storage chamber 102 and is respectively communicated with the heat exchange medium inflow 26, every heat transfer board 3, all establish at least one temperature sensor 9 on the heat exchanger 4, atomizing pump 6, circulating pump 7, waste heat recovery device 8 and control circuit all inlay in bearing base 1, wherein atomizing pump 6 and condensate tank 2's water inlet 25 intercommunication, waste heat recovery device 8 passes through circulating pump 7 and condensate tank 2's heat transfer medium inflow port 26 and heat transfer medium backward flow mouth 27 intercommunication, control circuit respectively with atomizing pump 6, circulating pump 7, waste heat recovery device 8, temperature sensor 9 electrical connection.
When two or more than two condensing tanks 2 are provided, the condensing tanks 2 are connected in parallel and are uniformly distributed around the axis of the bearing base 1.
Meanwhile, the height of the bearing base 1 is 1/5-1/2 of the height of the condensation tank 2, the bottom of the condensation tank is embedded in the bearing base 1, and the distance between the bottom of the condensation tank and the bottom of the bearing base 1 is 1/4-3/4 of the height of the bearing base 1.
In addition, the heat exchange plate 3 include heat exchange tube 31, corrugated metal plate 32, wherein corrugated metal plate 32 cladding is at heat exchange tube 31 up end and terminal surface down, and parallel distribution between the corrugated metal plate 32 of heat exchange tube 31 up end and terminal surface down, simultaneously corrugated metal plate 32 on a plurality of thru holes 33 of equipartition, thru hole 33 aperture is not more than 3 millimeters, axis and 2 axis parallel distribution of condensation jar, and the total area of thru hole 33 is 30% -60% of the total area of corrugated metal plate 32 surface.
Preferably, in the heat exchange plates 3, the distance between two adjacent heat exchange plates 3 is not less than 10 cm,
preferably, the bearing keel 11 is an annular frame structure coaxially distributed with the condensation tank 2.
In this embodiment, the control circuit is a circuit system based on a DSP chip, and is further provided with at least one serial data communication port.
In the specific implementation of the novel cooling system, firstly, a bearing base, a condensing tank, a heat exchange plate, a heat exchanger, an atomizing nozzle, an atomizing pump, a circulating pump, a waste heat recovery device, a temperature sensor and a control circuit which form the novel cooling system are assembled, then the novel cooling system is installed at a specified working position through the bearing base, and then the atomizing pump is communicated with an external high-temperature condensed water return pipeline; and the waste heat recovery device is communicated with an external heat energy system, and finally, the control circuit is connected with the external power supply circuit and the monitoring system in a data communication manner, so that the novel assembly is completed.
In the concrete operation of the novel condensation water cooling device, firstly, the high-temperature backflow condensation water of an external high-temperature condensation water backflow pipeline, the water vapor or the mixture of the condensation water and the water vapor are secondarily pressurized through the atomizing pump, and are atomized and sprayed through the atomizing nozzle, then, the high-temperature high-pressure condensation water mist is sprayed into the condensation chamber of the condensation tank from bottom to top along the axis of the condensation tank, and sequentially passes through the lower surfaces of the heat exchange plates when the high-temperature high-pressure condensation water mist runs from bottom to top along the axis of the condensation tank, so as to carry out preliminary heat exchange, cooling and condensation, the condensation water falls back from top to bottom under the action of gravity when rising to the upper part of the condensation chamber, and carries out secondary heat exchange with the upper end surfaces of the heat exchange plates in the condensation chamber, finally, the condensation water is converged into the water storage chamber of the condensation, when the heat exchange plate and the heat exchanger perform heat exchange cooling operation on the condensate water, the circulating flow of a heat exchange medium among the waste heat recovery device, the heat exchange plate and the heat exchanger is realized through the circulating pump, so that the waste heat of the condensate water is recycled by the waste heat recovery device, and the purpose of flexibly adjusting the waste heat recovery efficiency of the condensate water is achieved by adjusting the temperature of the heat exchange medium in the waste heat recovery device.
In addition, this novel structural, indirect heating equipment at different levels all concentrates along the condensate tank top-down and distributes to very big improvement this novel structural configuration integrate and the modularization degree.
The utility model discloses an aspect simple structure integrates the degree height, and the commonality is good, can effectively satisfy the needs of the high-efficient condensation recovery operation of high-temperature water, high-temperature steam and high-temperature water vapor mixture, and on the other hand system operation energy consumption is low to can effectively improve waste heat resource recovery utilization ratio in the condensate water, thereby reach the purpose that improves comdenstion water recovery regeneration efficiency and reduce the operating cost.
It will be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that the foregoing embodiments and descriptions are provided only to illustrate the principles of the present invention without departing from the spirit and scope of the present invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (8)
1. The utility model provides a high-efficient multistage condensation water pitcher structure which characterized in that: the high-efficiency multistage condensate water tank structure comprises a bearing base, a condensate tank, heat exchange plates, a heat exchanger, an atomizing nozzle, an atomizing pump, a circulating pump, a waste heat recovery device, a temperature sensor and a control circuit, wherein the bearing base is a frame structure with a rectangular cross section and is distributed in parallel with a horizontal plane, at least one condensate tank is connected with the upper end face of the bearing base, the axis of the condensate tank is distributed in a vertical direction with the horizontal plane, the condensate tank comprises a tank body and a bearing tray, the tank body is a closed cavity structure with a rectangular axial cross section, a water outlet is arranged at the bottom of the tank body, an emergency pressure relief valve is arranged at the top of the tank body, a water inlet, at least one heat exchange medium inlet and at least one heat exchange medium return port are arranged on the side wall of the tank body, the tray is embedded in the tank body and is distributed, the tray divides the tank body into a condensing chamber and a water storage chamber from top to bottom, a plurality of through holes are uniformly distributed on the tray, the condensing chamber and the water storage chamber are communicated with each other through the through holes, a plurality of atomizing nozzles are uniformly distributed on the upper end surface of the carrying tray around the axis of the carrying tray and form an included angle of 0-60 degrees with the axis of the tank body, the atomizing nozzles are connected in parallel and are respectively communicated with the water inlet through a guide pipe, at least two heat exchange plates are embedded in the condensing chamber and distributed from top to bottom along the axis of the condensing chamber, the heat exchange plates are in a round platform-shaped hollow tubular structure coaxially distributed with the condensing chamber, each heat exchange plate is connected with the inner surface of the tank body corresponding to the condensing chamber through a carrying keel, the outer diameter of the lower end surface of each heat exchange plate is 80-90% of the inner diameter of the condensing chamber, the outer diameter of the upper end surface is 10-30% of the, at least one of the heat exchangers is embedded in the water storage chamber and is respectively communicated with a heat exchange medium inflow port and a heat exchange medium backflow port through a flow guide pipe, the quantity of the temperature sensors is consistent with that of the heat exchange plates and the quantity of the heat exchangers, at least one temperature sensor is arranged on each heat exchange plate and the heat exchanger, the atomizing pump, the circulating pump, the waste heat recovery device and the control circuit are embedded in the bearing base, the atomizing pump is communicated with the water inlet of the condensing tank, the waste heat recovery device is communicated with the heat exchange medium inflow port and the heat exchange medium backflow port of the condensing tank through the circulating pump, and the control circuit is respectively electrically connected with the atomizing pump, the circulating pump.
2. The high-efficiency multi-stage condensed water tank structure according to claim 1, wherein when the number of the condensing tanks is two or more, the condensing tanks are connected in parallel and are uniformly distributed around the axis of the bearing base.
3. A high efficiency multi-stage condensate tank structure as claimed in claim 1, wherein the height of the carrying base is 1/5-1/2 of the height of the condensate tank, the bottom of the condensate tank is embedded in the carrying base, and the distance between the bottom of the carrying base and the bottom of the carrying base is 1/4-3/4 of the height of the carrying base.
4. The high-efficiency multistage condensed water tank structure according to claim 1, wherein the heat exchange plate comprises a heat exchange tube and corrugated metal plates, wherein the corrugated metal plates are coated on the upper end surface and the lower end surface of the heat exchange tube, and the corrugated metal plates on the upper end surface and the lower end surface of the heat exchange tube are distributed in parallel.
5. A high-efficiency multi-stage condensed water tank structure as claimed in claim 4, wherein a plurality of through holes are uniformly distributed on the metal corrugated plate, the aperture of each through hole is not more than 3 mm, the axes of the through holes are parallel to the axis of the condensed tank, and the total area of the through holes is 30-60% of the total area of the surface of the metal corrugated plate.
6. A high efficiency multi-stage condensed water tank structure as claimed in claim 1, wherein the distance between two adjacent heat exchange plates is not less than 10 cm.
7. A high efficiency multi-stage condensed water tank structure as claimed in claim 1, wherein the bearing keel is a ring frame structure coaxially distributed with the condensed tank.
8. The high-efficiency multi-stage condensed water tank structure as claimed in claim 1, wherein the control circuit is a DSP chip-based circuit system, and is further provided with at least one serial port data communication port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921629866.3U CN210952412U (en) | 2019-09-27 | 2019-09-27 | High-efficient multistage condensation water pitcher structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921629866.3U CN210952412U (en) | 2019-09-27 | 2019-09-27 | High-efficient multistage condensation water pitcher structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210952412U true CN210952412U (en) | 2020-07-07 |
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ID=71379608
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921629866.3U Expired - Fee Related CN210952412U (en) | 2019-09-27 | 2019-09-27 | High-efficient multistage condensation water pitcher structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210952412U (en) |
-
2019
- 2019-09-27 CN CN201921629866.3U patent/CN210952412U/en not_active Expired - Fee Related
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| 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: 20200707 Termination date: 20210927 |