CN201476169U - Bathwater heating device recovering and utilizing waste bathwater heat - Google Patents
Bathwater heating device recovering and utilizing waste bathwater heat Download PDFInfo
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- CN201476169U CN201476169U CN2009202267064U CN200920226706U CN201476169U CN 201476169 U CN201476169 U CN 201476169U CN 2009202267064 U CN2009202267064 U CN 2009202267064U CN 200920226706 U CN200920226706 U CN 200920226706U CN 201476169 U CN201476169 U CN 201476169U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Abstract
The utility model discloses a bathwater heating device which recovers and utilizes waste bathwater heat. The bathwater heating device comprises a waste water heat exchanger, a measurement and control device, a heat pump heating device and the like; a heat preservation drainpipe is connected with an inlet of a hair collector (1), an outlet of the hair collector (1) is connected with a waste water collecting pond (2), and a water inlet pipe of a waste water booster pump is connected with the waste water collecting pond (2); a preceding stage measurement and control device (11) is connected with a running water supply system and the waste water heat exchanger; and a heating circulation pump (14) is connected with a water inlet of a heat pump condenser heating device (15), and a water outlet of the heat pump condenser heating device (15) is connected with a high-level bathwater tank (16). The utility model utilizes and recovers waste heat, and increases the temperature of the running water from 15 DEG C to 25 DEG C through direct heat exchange, and then a heat pump evaporator utilizes the residual heat energy to heat the running water from 25 DEG C to 41 DEG C. The device utilizes the discharged waste water residual heat to heat bathwater, reduces energy consumption, has remarkable environmental protection effect and low running cost, and no three wastes are generated during the running process.
Description
Technical field
The utility model relates to a kind of device of bathhouse heating bath hot water, specifically, relates to the used bath wastewater of a kind of recovery bathhouse, and utilizes the device of the new bath water of its waste heat heating.
Background technology
The heating of bathhouse bath hot water is a main fuel with coal or natural gas always, in recent years, can reduce consumption though widely popularize the solar energy heating technology of application to coal or natural gas, but because the heat capacity of solar thermal collector is subjected to the restriction of weather conditions, can not guarantee the supply of bath hot water separately as a kind of stable mode of heating, so also must establish a cover fire coal or a gas fired-boiler in addition, to guarantee the normal operation of system.The present this system overwhelming majority adopts based on fire coal or gas fired-boiler, is the mode of heating of assisting with solar thermal collector.
Use the shortcoming of fire coal or gas fired-boiler, the one, consume primary energy, the 2nd, the waste residue toxic emission that is produced during operation can affect to environment, and particularly coal-burning boiler is bigger to the influence of environment, and therefore present most cities are to using coal-burning boiler to make the policy restriction.And the electric boiler of environmental protection is difficult to obtain owing to operating cost is higher promote.
Summary of the invention
The purpose of this utility model is to provide a kind of device of waste heat heating bath hot water of the bath wastewater that utilizes the bathhouse discharging.Because the waste heat of this device to reclaim, with a spot of power electricity consumption and electrical heating is auxilliary heating bath hot water, energy savings not only, and system does not produce any waste gas and waste residue when operation, do not increase wastewater discharge, carry out season of room temperature lowering at needs, the utility model can also provide low-temperature receiver to the water-cooling type air conditioning system of certain area, so environmental protection and energy-saving effect are very remarkable.Operating cost also is significantly less than fire coal or gas fired-boiler and electric boiler.
To achieve these goals, the utility model has adopted following technical scheme:
A kind of recycling shower waste water residual heat heating bath hot water device, it is by the insulation drainage pipeline, insulation hair collector, insulation wastewater collection pond, the waste water force (forcing) pump, the self-cleaning type filter, prime wastewater heat exchange device group, back level wastewater heat exchange device group, the waste water inspection shaft, the prime measure and control device, reservoir in the insulation high position, back level measure and control device, the heat cycles pump, the heat pump condenser heater, intermediary's water-circulating pump, be incubated high-order bath hot water case, the shower circulating pump, the concurrent heating electric boiler, the concurrent heating circulating pump, intermediary's water-circulating pump, the air-conditioning circulating pump, water supply pipe, middle warm water pipeline, compositions such as intermediary's waterpipe; Its main points are: the insulation drainpipe that comes from the bathroom connects the inlet of insulation hair collector, the outlet of insulation hair collector connects insulation wastewater collection pond, the water inlet pipe of waste water force (forcing) pump connects insulation wastewater collection pond, the outlet pipe of waste water force (forcing) pump connects dirt separator, the other end of dirt separator connects prime wastewater heat exchange device successively, heating (high temperature) end of back level wastewater heat exchange device, one termination tap water supply system of prime measure and control device, the other end connects the low-temperature end that is heated of prime wastewater heat exchange device successively, reservoir in the water outlet termination high position of prime wastewater heat exchange device, the water outlet termination waste water inspection shaft of back level wastewater heat exchange device, reservoir in the water inlet termination high position of back level measure and control device, water outlet termination heat cycles pump, the heat cycles pump connects heat pump condenser heater water inlet by valve, heat pump condenser heater delivery port connects high-order bathing water tank, concurrent heating electric boiler water inlet and concurrent heating circulating pump, concurrent heating electric boiler delivery port links to each other with high-order bathing water tank, the shower circulating pump is connected on the bottom of high-order bathing water tank, intermediary's circulating pump connects the heat pump condenser heater, and the air-conditioning circulating pump is connected across on intermediary's circulating pump and the pipeline that the heat pump condenser heater is connected.
Described prime wastewater heat exchange device group, back level wastewater heat exchange device group are made up of one or more wastewater heat exchange device.
Described heat pump condenser heater is made up of the condenser and the water circulating pump of many water resource heat pumps.
Main feature of the present utility model is: the bath wastewater that discharge in the bathroom pressurizes after filtering by prime wastewater heat exchange device group and back level wastewater heat exchange device group, successively forces reverse-flow cycle heat exchange with running water, intermediary's water; At first utilize the temperature difference between himself and the bath wastewater in prime wastewater heat exchange device, to finish the prime direct heat transfer from the running water of public supply mains; And then carry out the back level by the condenser of source pump and be heated to design temperature and deliver to the high-order bathing water tank of insulation.The thermal source of source pump is obtained from back level wastewater heat exchange device group in a looping fashion by intermediary's water.Whole device has wastewater heat exchange, running water just to heat, middle warm water heats again, five flow processs of bath hot water concurrent heating, intermediary water circulation.
The utility model has the advantages that:
(1) mode of heating is reliable, is not subjected to the influence of season and outside air temperature.
(2) carbon-containing fuel that do not use in service, discharging waste gas, waste residue do not have influence to surrounding environment.
(3) thermal source of heating bath hot water is discharged the waste heat of waste water from bathhouse self, it is a kind of reusing of energy source technology, with the residual heat resources of a spot of power with electricity repeated recycling bath wastewater, under individual cases, be aided with the electric boiler heating, its total " fuel " expense only is equivalent to 1/4 of gas fired-boiler mode of heating, with 2/15 of electric boiler mode of heating, remarkable in economical benefits.
Description of drawings
Accompanying drawing is an embodiment schematic diagram of the present utility model.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described in detail.
As shown in drawings, this recycling shower waste water residual heat heating bath hot water device comprises: the insulation hair is assembled pond 1, insulation wastewater collection pond 2, the waste water pump 3 of VFC, dirt separator 4, prime wastewater heat exchange device 5, prime wastewater heat exchange device 6, back level wastewater heat exchange device 7, back level wastewater heat exchange device 8, waste water inspection shaft 9, concurrent heating electric boiler 10, prime measure and control device 11, reservoir 12 in the insulation high position, back level measure and control device 13, heat cycles pump 14, heat pump condenser heater 15, high-order bathing water tank 16, shower circulating pump 17, concurrent heating circulating pump 18, intermediary's water-circulating pump 19, intermediary's water-circulating pump 20, air-conditioning circulating pump 21, the prime heat exchanger of this instance graph, back level heat exchanger and source pump are all by 2 configurations, in the actual engineering, back level heat exchanger and source pump are generally by 3 to 4 configurations.
Recycle that shower waste water residual heat heating bath hot water device is divided into that wastewater heat exchange, running water just heat, middle warm water heats again, bath hot water concurrent heating, five flow processs of intermediary's water circulation:
(1), wastewater heat exchange flow process: the bath wastewater temperature of being discharged by bathhouse is greatly about about 35 ℃, enter the insulation hair through the insulation drainage system and assemble pond 1, in hair is assembled the pond, exclude hair and some and enter insulation wastewater collection pond 2 along utilidor after than bigger material, there is certain water storage capacity in insulation wastewater collection pond, can store waste water greater than the device processes ability in the phase at water use peak.Waste water is forced to extrude by the VFC waste water pump 3 that is positioned at wastewater collection pond 2, along being incubated the waste pipe sequential flow through dirt separator 4, prime wastewater heat exchange device 5, prime wastewater heat exchange device 6, back level wastewater heat exchange device 7, be discharged to waste water inspection shaft 9 behind the back level wastewater heat exchange device 8, wherein dirt separator 4 is that bath wastewater is done further thin the filtration, bath wastewater is in prime wastewater heat exchange device 5 and prime wastewater heat exchange device 6, carry out direct heat transfer with reflux type and low temperature running water with 1: 1 flow proportional, its temperature is reduced to 25 ℃ after the heat exchange, in back level wastewater heat exchange device 7 and back level wastewater heat exchange device 8, carry out heat exchange subsequently with reflux type and intermediary's water, the low temperature intermediary water that is provided by the evaporimeter of source pump offers remaining waste heat in the bath wastewater evaporimeter of source pump in a looping fashion, guarantees the normal operation of source pump.Through after the level heat exchange, water temperature is reduced to the bath wastewater below 10 ℃, enters municipal sewage pipe network through waste water inspection shaft 9.
(2), the first heating procedure of running water: the prime measure and control device 11 of at first flowing through when the running water that is provided by public supply mains enters native system, the effect of prime measure and control device is: to running water filter, flow monitoring, temperature monitoring and flow control automatically, cooperates wastewater flow to realize the rational and effective heat transfer process.The running water that flows out from prime measure and control device 11 is along utilidor order inflow and outflow prime wastewater heat exchange device 6 and prime wastewater heat exchange device 5, running water utilizes the temperature difference between itself and the waste water to carry out direct heat transfer with waste water with countercurrent heat exchange method in the prime heat exchanger package, the flow proportional of running water and waste water is 1: 1, the temperature of running water is approximately drawn high 25 ℃ by 15 ℃ after the heat exchange, become middle warm water, enter reservoir 12 in the high position of insulation measure along utilidor.
(3), middle warm water heating procedure again: the middle warm water in the insulation high position in the reservoir 12 is level measure and control device 13 through utilidor is flowed through after, and the effect of back level measure and control device is the flow of warm water in controlling according to the artificial temperature value of setting; Accurately control the leaving water temperature of heating system.Warm water at the uniform velocity enters heat pump condenser heater 15 under the synergy of back level measure and control device 13 and heat cycles pump 14, heat pump condenser heater 15 is made up of the condenser and the water circulating pump of many water resource heat pumps, the middle warm water condenser of each source pump of inflow and outflow in order accurately is heated to the leaving water temperature of being controlled by back level measure and control device, and enters the high-order bath hot water case 16 of insulation measure along utilidor.
(4), bath hot water concurrent heating flow process: bath hot water concurrent heating flow process is a kind of complementary technical measures, and during water temperature in needs improve high-order bath hot water case 16, this concurrent heating circulation is necessary.Concurrent heating has dual mode: when system heat sources is sufficient, with concurrent heating circulating pump 18 hot water in the high-order bath hot water case 16 is forced to pass through heat pump condenser heater 15 heat temperature raising once more; When system heat sources is not enough, put into operation for the first time as system, or the heat breach appears in the intrasystem thermal cycle of other reasons, with concurrent heating circulating pump 18 hot water in the bath hot water case is forced to heat by concurrent heating electric boiler 10, be system's additional heat.
(5), intermediary's water circulation process: intermediary's hydromining demineralized water.The effect of intermediary's water is to utilize cryogenic conditions that the source pump evaporimeter provides to obtain the residue waste heat of bath wastewater and offer the evaporimeter of water resource heat pump continuously from back level wastewater heat exchange device group in a looping fashion.By the back level heat exchanger package that many wastewater heat exchange devices are formed, the height of every wastewater heat exchange device intermediary water leaving water temperature is different with the arrangement position priority of wastewater heat exchange device.Equally, also difference of the leaving water temperature of warm water in being heated of every heat pump condenser with the priority of heat pump condenser position.Each wastewater heat exchange device takes corresponding one by one configuration to form circulation line with the evaporimeter of each heat pump, and equipping rules is: low temperature intermediary water is joined warm water in the low temperature; High temperature intermediary water is joined warm water in the high temperature.Accompanying drawing intermediary water-circulating pump 20 and back level wastewater heat exchange device 8 match with the prime heat hot pump assembly of heat pump condenser heater 15.Intermediary's water-circulating pump 19 and back level wastewater heat exchange device 7 match with the back level heat hot pump assembly of heat pump condenser heater 15.According to on-the-spot actual, on the lower intermediary's water circulating pipe of temperature, as the water inlet end of accompanying drawing circulating pump 20, all right external circulating line is the air-conditioning system summer cooling of certain area, and this external mode can't influence the normal operation of this system.
For a design hot water deliverability is the bathing hot-water heating system of 40 cubic metres/hour small-sized bathhouse, with three kinds of different mode of heatings, that running water is as follows respectively from 15 ℃ of direct operating costs that are heated to 42 ℃ of hot water:
(1) adopts the heat pump mode heating
Owing to the prime heat transfer process of running water is arranged, so the heating starting point of running water is since 25 ℃
Electricity price: 0.65 yuan/degree, add heat: 40 * 1000 * (42-25)=68 * 10000kcal
Dispose three low profile thermal pump assemblys, heat pump distribution power: 51Kw x3,
Other water pump distribution power: 5.25Kw of waste water pump distribution power: 15Kw:
Total distribution power: 51 * 3+15+5.25=170.25KW
Power consumption: 170.25KWH, the electricity charge: 170.25 * 0.65=110.66 unit
The heating expense of every cubic metre of hot water: 110.66/40=2.77 unit
(2) adopt the natural gas boiler mode to heat
The thermal efficiency 85% of gas fired-boiler, electricity price: 0.65 yuan/degree,
Heating value of natural gas: the 8000kcal/ cubic meter, the natural gas gas price: 2.80 yuan/cubic metre,
Add heat: 40 * 1000 * (42-15)=108 * 10000kcal
Gas consumption: (108 * 10000kcal)/(8000 * 0.85)=158.8 cubic metre
Combustion gas expense: 158.8 * 2.80=444.64 unit
Water circulating pump power consumption: the 5.0KWH electricity charge: 5.0 * 0.65=3.25 unit
Add up to: 444.64+3.25=447.89 unit
The heating expense of every cubic metre of hot water: 447.89/40=11.20 unit
(3) adopt the electric boiler mode to heat
Electric boiler efficient 98%, electricity price: 0.65 yuan/degree
Calculate heating power: 40 * 1.163 * (42-15)=1256KW
Power consumption: 1256KWH
The electricity charge: (1256 * 0.65)/0.98=833.06 unit
The heating expense of every cubic metre of hot water: 833.06/40=20.83 unit
The expense ratio of three kinds of mode of heatings:
Heat pump: combustion gas: electrical heating=110.66: 447.89: 833.06=1: 4.05: 7.53
Claims (3)
1. recycle shower waste water residual heat heating bath hot water device for one kind, it is by the insulation drainage pipeline, insulation hair collector (1), insulation bath wastewater pond (2), waste water force (forcing) pump (3), self-cleaning type filter (4), prime wastewater heat exchange device group (5) (6), back level wastewater heat exchange device group (7) (8), waste water inspection shaft (9), prime measure and control device (11), reservoir (12) in the insulation high position, back level measure and control device (13), heat cycles pump (14), heat pump condenser heater (15), intermediary's water-circulating pump (19), be incubated high-order bath hot water case (16), shower circulating pump (17), concurrent heating circulating pump (18), intermediary's water-circulating pump (20), air-conditioning circulating pump (21), water supply pipe, middle warm water pipeline, compositions such as intermediary's waterpipe; It is characterized in that: the insulation drainpipe that comes from the bathroom connects the inlet of insulation hair collector (1), the outlet of insulation hair collector (1) connects insulation wastewater collection pond (2), the water inlet pipe of waste water force (forcing) pump (3) connects insulation wastewater collection pond (2), the outlet pipe of waste water force (forcing) pump (3) connects self-cleaning type filter (4), the other end of self-cleaning type filter (4) connects prime wastewater heat exchange device (5) successively, (6), back level wastewater heat exchange device (7), (8) temperature end, one termination tap water supply system of prime measure and control device (11), the other end successively with prime wastewater heat exchange device (6), (5) connect, reservoir (12) in the water outlet termination high position of prime wastewater heat exchange device (5), the water outlet termination waste water inspection shaft (9) of back level wastewater heat exchange device (8), reservoir (12) in the water inlet termination high position of back level measure and control device (13), water outlet termination heat cycles pump (14), heat cycles pump (14) connects heat pump condenser heater (15) water inlet by valve, heat pump condenser heater (15) delivery port connects high-order bathing water tank (16), concurrent heating electric boiler (10) water inlet and concurrent heating circulating pump (18), delivery port links to each other with high-order bathing water tank (16), shower circulating pump (17) is connected on the bottom of high-order bathing water tank (16), intermediary's circulating pump (19), (20) connect heat pump condenser heater (15), air-conditioning circulating pump (21) is connected on intermediary's circulating pump (20) and the pipeline that heat pump condenser heater (15) is connected.
2. recycling shower waste water residual heat heating bath hot water device according to claim 1 is characterized in that described prime wastewater heat exchange device group (5), (6), back level wastewater heat exchange device group (7), (8), is made up of one or more wastewater heat exchange device.
3. recycling shower waste water residual heat according to claim 1 heating bath hot water device is characterized in that described heat pump condenser heater (15) is made up of the condenser and the water circulating pump of many water resource heat pumps.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202267064U CN201476169U (en) | 2009-09-08 | 2009-09-08 | Bathwater heating device recovering and utilizing waste bathwater heat |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202267064U CN201476169U (en) | 2009-09-08 | 2009-09-08 | Bathwater heating device recovering and utilizing waste bathwater heat |
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| Publication Number | Publication Date |
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| CN201476169U true CN201476169U (en) | 2010-05-19 |
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| CN2009202267064U Expired - Fee Related CN201476169U (en) | 2009-09-08 | 2009-09-08 | Bathwater heating device recovering and utilizing waste bathwater heat |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102410671A (en) * | 2011-11-21 | 2012-04-11 | 东莞市瑞星空调设备有限公司 | Heat pump system utilizing hot waste water source |
| CN102538296A (en) * | 2011-07-16 | 2012-07-04 | 王政玉 | Multi-purpose thermal mechanism |
| CN103673385A (en) * | 2013-12-24 | 2014-03-26 | 天津英利新能源有限公司 | Photovoltaic industry energy-saving system |
| CN106524292A (en) * | 2016-12-09 | 2017-03-22 | 北京瑞宝利热能科技有限公司 | Waste heat recovering system for bathing wastewater |
| CN107695005A (en) * | 2017-10-24 | 2018-02-16 | 蚌埠市莱特汽车配件有限公司 | Automobile filter shell cleaning device |
| CN107726617A (en) * | 2017-11-13 | 2018-02-23 | 北京众信科源科技有限公司 | A kind of waste heat recovery hot water system |
| CN108240699A (en) * | 2016-12-26 | 2018-07-03 | 邹诗兵 | Energy-saving hot-water system |
| CN108592162A (en) * | 2018-06-07 | 2018-09-28 | 威海双信节能环保设备有限公司 | Heat pump integrates waste heat multiple-effect reuse bath hot water and prepares unit and preparation method |
| CN108716771A (en) * | 2018-06-07 | 2018-10-30 | 威海双信节能环保设备有限公司 | Industrial wastewater waste heat overlapping heat to power output device and method |
-
2009
- 2009-09-08 CN CN2009202267064U patent/CN201476169U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102538296A (en) * | 2011-07-16 | 2012-07-04 | 王政玉 | Multi-purpose thermal mechanism |
| CN102410671A (en) * | 2011-11-21 | 2012-04-11 | 东莞市瑞星空调设备有限公司 | Heat pump system utilizing hot waste water source |
| CN102410671B (en) * | 2011-11-21 | 2016-05-18 | 广东瑞星新能源科技有限公司 | A kind of heat pump that utilizes hot waste water source |
| CN103673385A (en) * | 2013-12-24 | 2014-03-26 | 天津英利新能源有限公司 | Photovoltaic industry energy-saving system |
| CN106524292A (en) * | 2016-12-09 | 2017-03-22 | 北京瑞宝利热能科技有限公司 | Waste heat recovering system for bathing wastewater |
| CN108240699A (en) * | 2016-12-26 | 2018-07-03 | 邹诗兵 | Energy-saving hot-water system |
| CN107695005A (en) * | 2017-10-24 | 2018-02-16 | 蚌埠市莱特汽车配件有限公司 | Automobile filter shell cleaning device |
| CN107726617A (en) * | 2017-11-13 | 2018-02-23 | 北京众信科源科技有限公司 | A kind of waste heat recovery hot water system |
| CN108592162A (en) * | 2018-06-07 | 2018-09-28 | 威海双信节能环保设备有限公司 | Heat pump integrates waste heat multiple-effect reuse bath hot water and prepares unit and preparation method |
| CN108716771A (en) * | 2018-06-07 | 2018-10-30 | 威海双信节能环保设备有限公司 | Industrial wastewater waste heat overlapping heat to power output device and method |
| CN108716771B (en) * | 2018-06-07 | 2023-05-19 | 威海双信节能环保设备有限公司 | Industrial wastewater waste heat cascade heat work conversion device and method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100519 Termination date: 20110908 |