CN105244830A - Water treatment system and heat recovery device - Google Patents
Water treatment system and heat recovery device Download PDFInfo
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- CN105244830A CN105244830A CN201510690465.9A CN201510690465A CN105244830A CN 105244830 A CN105244830 A CN 105244830A CN 201510690465 A CN201510690465 A CN 201510690465A CN 105244830 A CN105244830 A CN 105244830A
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- heat
- recovering apparatus
- energy recovering
- heat absorption
- bus duct
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Abstract
The invention discloses a heat recovery device. The device comprises heat absorbing oil which is used for absorbing the heat of a busbar, a liquid pipeline which is arranged along the longitudinal direction of the busbar and is used for accommodating the heat absorbing oil, and a heating device. The liquid pipeline comprises a liquid inlet end which is used for accommodating the heat absorbing oil which does not absorb heat and a liquid outlet end which is used for discharging the heat absorbing oil which absorbs heat. The heating device is connected with the liquid outlet end to use the heat. The liquid inlet end and the liquid outlet end are provided with check valves which prevent the heat absorbing oil from back flowing. The invention further discloses a water treatment system which comprises the heat recovery device. The heat recovery device uses the heat absorbing oil and the liquid pipeline to absorb and use the heat of the busbar. The heat of the busbar is effectively used and recovered.
Description
Technical field
The present invention relates to mechanical engineering technical field, particularly a kind of heat-energy recovering apparatus.The invention still further relates to a kind of water treatment system with this heat-energy recovering apparatus.
Background technology
Along with the fast development of China's economic construction, market increases day by day for the demand of the water treatment system with heat-energy recovering apparatus.
As everyone knows, emerging in large numbers of modernization project facility and matching equipment, the power consumption of all trades and professions increases sharply, especially particularly outstanding in architectural engineering building, large-sized workshop workshop, office block etc.As the traditional cable of transmission of electricity distribution, can not satisfy the demands now.Traditional multiway cable is in parallel makes troubles to engineering site construction connection, and the also joint conference of multiway cable causes larger labour's waste simultaneously.
China introduces bus duct product the fifties in last century from external, goes through several generations development, and existing general function product is mainly divided into concentration bus duct and air type two kinds.Air type bus causes the excessive environment temperature that causes of own loss too high because of kelvin effect and eddy current effect, and cause bus duct temperature ramps by air thermal radiation heat loss through conduction weak effect, bus-bars conductor is poorer in high temperature environment download stream performance, make the larger cross-sectional area of conductor of bus-bars conductor electric current larger, thus add a large amount of inputs of resource loss and people, material resources.
Therefore, the heat how utilizing bus duct to distribute is the current technical issues that need to address of those skilled in the art.
Summary of the invention
The object of this invention is to provide a kind of heat-energy recovering apparatus, this heat-energy recovering apparatus can solve the irretrievable problem of heat that bus duct distributes.Another object of the present invention is to provide a kind of water treatment system comprising above-mentioned heat-energy recovering apparatus.
For achieving the above object, the invention provides a kind of heat-energy recovering apparatus, comprising:
In order to absorb the heat absorption oil of bus duct heat;
The fluid pipeline holding described heat absorption oil is provided with along described busduct length direction; Described fluid pipeline comprises in order to hold without the liquid feeding end of the described heat absorption oil of heat absorption and the outlet end in order to be discharged by the described heat absorption oil after heat absorption;
The heater carrying out heat energy utilization is connected with described outlet end.
Preferably, described liquid feeding end and described outlet end are provided with the check-valves preventing the described oil that absorbs heat from refluxing.
Preferably, also comprise in order to provide power to described heat absorption oil and to pass through the kinetic pump of bus duct surface temperature described in the flow control of the described heat absorption oil of change.
Preferably, described kinetic pump be connected with control described kinetic pump flow velocity to guarantee described bus duct surface temperature at 40 DEG C to the control device within the scope of 50 DEG C.
Preferably, the arranged outside of described heat-energy recovering apparatus has the warming plate preventing heat from distributing.
Preferably, the number of described outlet end is two.
The present invention also provides a kind of water treatment system, the heat-energy recovering apparatus comprising water storage device and be connected with described water storage device; Described heat-energy recovering apparatus is the heat-energy recovering apparatus described in above-mentioned any one.
Preferably, described water treatment system comprises cooling water inlet and warm water outlet.
Relative to above-mentioned background technology, heat-energy recovering apparatus involved in the present invention, comprises fluid pipeline, arranges heat absorption oil in fluid pipeline; Heat absorption oil is utilized to absorb the heat of bus duct; In addition, fluid pipeline also arranges liquid feeding end and outlet end; Namely the heat absorption oil absorbing bus duct heat is discharged through outlet end, and outlet end is connected with heater; The heat motion that heat absorption oil so just can be utilized to absorb in heater, thus realizes the heat effect of heater.Adopt above-mentioned set-up mode, only utilize heat absorption oil and fluid pipeline just can absorb the heat of bus duct and utilize, thus effectively make use of the heat of bus duct, it is recycled.
In addition, the invention still further relates to a kind of water treatment system, the heat of the bus duct that this water treatment system utilizes above-mentioned heat absorption oil and fluid pipeline to absorb, processes sewage, thus has effectively saved the energy, improve the utilance of resource.
Accompanying drawing explanation
The structural representation that the heat-energy recovering apparatus that Fig. 1 provides for the embodiment of the present invention is connected with water treatment system.
Wherein:
Liquid feeding end 1, outlet end 2, heater 3, check-valves 4, control device 5, cooling water inlet 6, warm water outlet 7.
Embodiment
Core of the present invention is to provide a kind of heat-energy recovering apparatus, and this heat-energy recovering apparatus can reclaim the heat of bus duct; Another core of the present invention is to provide a kind of water treatment system comprising above-mentioned heat-energy recovering apparatus.
In order to make those skilled in the art understand the present invention program better, below in conjunction with the drawings and specific embodiments, the present invention is described in further detail.
Please refer to Fig. 1, the structural representation that the heat-energy recovering apparatus that Fig. 1 provides for the embodiment of the present invention is connected with water treatment system.
Embodiment about heat-energy recovering apparatus provided by the present invention, comprises fluid pipeline; Arrange heat absorption oil in fluid pipeline, this heat absorption oil can absorb the heat of bus duct.This paper is preferred is set to high-temperature insulation oil by heat absorption oil.That is, this heat absorption oil can bear 200 DEG C and above high temperature, and it has insulation property.Absorb heat oily dielectric strength preferably at more than 20KV,
In addition, fluid pipeline is arranged along busduct length direction; As a rule, because the length of bus duct is longer, conductor is installed in bus duct, and conductor distributes a large amount of heat energy in the course of the work, and fluid pipeline is arranged along the length wise of bus duct, and has heat absorption oil in fluid pipeline; So, heat absorption oil farthest can absorb the heat that bus duct distributes, thus reduces the temperature of bus duct, and the temperature of heat absorption oil is raised, and completes the process of heat absorption.
On this basis, fluid pipeline is provided with liquid feeding end 1 and outlet end 2; That is, heat absorption lower for temperature oil is sent in bus duct by the liquid feeding end 1 of fluid pipeline, and the heat absorption oil absorbing bus duct heat is discharged from the outlet end 2 of fluid pipeline, thus complete the flow process of heat absorption oil in bus duct, also complete the endothermic process to bus duct.
Heat absorption oil is discharged by outlet end 2 after absorbing the heat of bus duct, and the outlet end 2 of fluid pipeline is connected with heater 3; And heater 3 can utilize the heat of the bus duct that heat absorption oil absorbs, complete corresponding function.
Herein, heater 3 can be multiple device, does not make concrete restriction herein.
Adopt above-mentioned set-up mode, only utilize heat absorption oil and fluid pipeline just can absorb the heat of bus duct and utilize, thus effectively make use of the heat of bus duct, it is recycled.
For optimizing technique scheme, liquid feeding end 1 and the outlet end 2 of fluid pipeline also arrange check-valves 4; Check-valves 4 can prevent heat absorption oil from refluxing.
Specifically, utilize the check-valves 4 being arranged on liquid feeding end 1 and outlet end 2 can control the oily flow direction of absorbing heat, thus realize above-mentioned purpose.Certainly, according to actual needs, check-valves 4 can have multiple set-up mode, will repeat no more herein.
Further optimize the program, the power resources of heat absorption oil are provided by kinetic pump; Because kinetic pump controls the flow velocity size of heat absorption oil, thus the surface temperature of bus duct can be regulated.Specifically, if the power of kinetic pump is comparatively large, make the flow velocity of heat absorption oil comparatively large, so, heat absorption oil flows through the speed on bus duct surface, thus the heat of bus duct is pulled away quickly, and the temperature reduction ground on bus duct surface is very fast.Similar, if the power of kinetic pump is less, make the flow velocity of heat absorption oil lower, so, the speed that heat absorption oil flows through bus duct surface is lower, thus the heat of bus duct is more slowly pulled away, and the temperature on bus duct surface reduces slower.
Certainly, according to actual needs, the power size of kinetic pump can regulate at any time, with the operating efficiency of control bus rooved face temperature and/or heater 3.
According to actual needs, be provided with control device 5 herein, control device 5 is connected with kinetic pump, utilizes control device 5 to control the flow velocity of kinetic pump, thus guarantees bus duct surface temperature at 40 DEG C within the scope of 50 DEG C.
Certainly, control device 5 can also be provided with temperature sensor, and this temperature sensor is arranged on bus duct surface; When bus duct surface temperature exceedes preset value, control device 5 controls kinetic pump and accelerates, and makes the flow velocity of heat absorption oil larger, so, heat absorption oil flows through the speed on bus duct surface, thus the heat of bus duct is pulled away quickly, and the temperature on bus duct surface reduces ground comparatively fast.In addition, the preset value of bus duct surface temperature is not restricted to 40 DEG C to 50 DEG C, can also be arranged within other scopes.To repeat no more herein.
In order to ensure the efficiency of heat-energy recovering apparatus, have in the arranged outside of heat-energy recovering apparatus the warming plate preventing heat from distributing herein.
Utilize warming plate can protect heat-energy recovering apparatus be subject to external force impact and be damaged, and the heat of bus duct can not scatter and disappear to utilize warming plate effectively to guarantee, thus improve the organic efficiency of heat-energy recovering apparatus, improve the utilization rate of heat energy.Certainly, the concrete size shape of warming plate should be determined according to reality, not have ever made many restrictions herein.
For the situation of heavy current busbar, because the cross section of heavy current busbar is comparatively large, thus the cross section of bus duct is comparatively large, and namely the height of bus duct is higher, so, is two by the number of outlet end 2.That is, fluid pipeline is provided with a liquid feeding end 1 and two outlet ends 2, thus can reduce the temperature of outlet end 2, realizes the normal operation of heat-energy recovering apparatus.Certainly, according to actual needs, the number of outlet end 2 can also be set to three, four or more, will repeat no more herein.
In addition, it should be noted that, heat-energy recovering apparatus of the present invention is relative to other bus ducts, and the current capacity of bus duct of the present invention promotes 15%.In other words, in equal current-carrying situation, bus duct of the present invention decreases resource loss, saves non-ferrous metal.
The invention still further relates to a kind of water treatment system, the heat-energy recovering apparatus comprising water storage device and be connected with water storage device; Specifically as shown in Figure of description 1.Can find out, water treatment system, comprise cooling water inlet 6 and warm water outlet 7.
This paper is preferred is arranged at water storage device top by cooling water inlet 6, warm water outlet 7 is arranged at water storage device sidewall, and the outlet end 2 of fluid pipeline stretches into water storage device inside, thus processes water.
Specifically, utilize the cold water of heat to water storage device of the heat absorption oil of outlet end 2 to process, can use in the winter time, and reduce because of required electric energy or the natural gas equal energy source of heating that feed water, thus improve the utilance of the energy.
Especially, it should be noted that, heat-energy recovering apparatus involved in the present invention, every 100 meters of bus ducts are per hour can process domestic water (temperature of the water after process is between 40-50 DEG C) 15L.
Above water treatment system provided by the present invention and heat-energy recovering apparatus thereof are described in detail.Apply specific case herein to set forth principle of the present invention and execution mode, the explanation of above embodiment just understands method of the present invention and core concept thereof for helping.It should be pointed out that for those skilled in the art, under the premise without departing from the principles of the invention, can also carry out some improvement and modification to the present invention, these improve and modify and also fall in the protection range of the claims in the present invention.
Claims (8)
1. a heat-energy recovering apparatus, is characterized in that, comprising:
In order to absorb the heat absorption oil of bus duct heat;
The fluid pipeline holding described heat absorption oil is provided with along described busduct length direction; Described fluid pipeline comprises in order to hold without the liquid feeding end (1) of the described heat absorption oil of heat absorption and the outlet end (2) in order to be discharged by the described heat absorption oil after heat absorption;
The heater (3) carrying out heat energy utilization is connected with described outlet end.
2. heat-energy recovering apparatus according to claim 1, is characterized in that, described liquid feeding end (1) and described outlet end (2) are provided with the check-valves (4) preventing the described oil that absorbs heat from refluxing.
3. heat-energy recovering apparatus according to claim 1 and 2, is characterized in that, also comprises in order to provide power to described heat absorption oil and to pass through the kinetic pump of bus duct surface temperature described in the flow control of the described heat absorption oil of change.
4. heat-energy recovering apparatus according to claim 3, is characterized in that, described kinetic pump be connected with control described kinetic pump flow velocity to guarantee described bus duct surface temperature at 40 DEG C to the control device (5) within the scope of 50 DEG C.
5. heat-energy recovering apparatus according to claim 4, is characterized in that, the arranged outside of described heat-energy recovering apparatus has the warming plate preventing heat from distributing.
6. heat-energy recovering apparatus according to claim 5, is characterized in that, the number of described outlet end (2) is two.
7. a water treatment system, the heat-energy recovering apparatus comprising water storage device and be connected with described water storage device; It is characterized in that, described heat-energy recovering apparatus is the heat-energy recovering apparatus described in the claims 1 to 6 any one.
8. water treatment system according to claim 7, is characterized in that, described water treatment system comprises cooling water inlet (6) and warm water outlet (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510690465.9A CN105244830A (en) | 2015-10-22 | 2015-10-22 | Water treatment system and heat recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510690465.9A CN105244830A (en) | 2015-10-22 | 2015-10-22 | Water treatment system and heat recovery device |
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| Publication Number | Publication Date |
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| CN105244830A true CN105244830A (en) | 2016-01-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510690465.9A Pending CN105244830A (en) | 2015-10-22 | 2015-10-22 | Water treatment system and heat recovery device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106992446A (en) * | 2016-01-21 | 2017-07-28 | 浙江工业职业技术学院 | A kind of dustless falling temperature technique of controller switching equipment |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202648481U (en) * | 2012-05-14 | 2013-01-02 | 施耐德电器工业公司 | Liquid phase change heat transfer type pumping cooling system with booster pump |
| CN204204568U (en) * | 2014-10-21 | 2015-03-11 | 国家电网公司 | Transformer temperature-reducing heat-exchange device |
| CN204240846U (en) * | 2014-11-21 | 2015-04-01 | 陈旭 | A kind of air compressor machine heat reclaim unit of improvement |
| CN204514118U (en) * | 2014-12-07 | 2015-07-29 | 长沙韩众节能科技有限公司 | Waste heat recovery heat collector |
| CN205029279U (en) * | 2015-10-22 | 2016-02-10 | 上海振大电器成套有限公司 | Water processing system and heat recovery unit |
-
2015
- 2015-10-22 CN CN201510690465.9A patent/CN105244830A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202648481U (en) * | 2012-05-14 | 2013-01-02 | 施耐德电器工业公司 | Liquid phase change heat transfer type pumping cooling system with booster pump |
| CN204204568U (en) * | 2014-10-21 | 2015-03-11 | 国家电网公司 | Transformer temperature-reducing heat-exchange device |
| CN204240846U (en) * | 2014-11-21 | 2015-04-01 | 陈旭 | A kind of air compressor machine heat reclaim unit of improvement |
| CN204514118U (en) * | 2014-12-07 | 2015-07-29 | 长沙韩众节能科技有限公司 | Waste heat recovery heat collector |
| CN205029279U (en) * | 2015-10-22 | 2016-02-10 | 上海振大电器成套有限公司 | Water processing system and heat recovery unit |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106992446A (en) * | 2016-01-21 | 2017-07-28 | 浙江工业职业技术学院 | A kind of dustless falling temperature technique of controller switching equipment |
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| C06 | Publication | ||
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| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 201111 503, room nineteenth, 60 Zhonghui Road, Minhang District, Shanghai. Applicant after: Shanghai Zhengda Electrical Appliance Group Co., Ltd. Address before: 201111 503, room nineteenth, 60 Zhonghui Road, Minhang District, Shanghai. Applicant before: Shanghai Zhenda Electrical Appliance Complete Set Co., Ltd. |
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| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160113 |