CN102865662A - Two-stage bathing wastewater recovery device - Google Patents
Two-stage bathing wastewater recovery device Download PDFInfo
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- CN102865662A CN102865662A CN2012103665099A CN201210366509A CN102865662A CN 102865662 A CN102865662 A CN 102865662A CN 2012103665099 A CN2012103665099 A CN 2012103665099A CN 201210366509 A CN201210366509 A CN 201210366509A CN 102865662 A CN102865662 A CN 102865662A
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Abstract
The invention discloses a two-stage bathing wastewater recovery device. An input port I of a heat exchanger is connected with a water collection tank containing bathing wastewater, an output port I of the heat exchanger is connected with an input port IV of an evaporator, an output port IV of the evaporator is connected with a drain outlet, a condenser is mounted in a heat collection case, and the evaporator, a compressor, the condenser and a throttling device form a two-stage heat extraction pipeline. The two-stage bathing wastewater recovery device is high in heat recovery rate, is efficient and energy-saving, safe and reliable, and can be used for houses, units, bath centers and the like.
Description
Technical field
The present invention relates to a kind of heat reclamation device, especially relate to a kind of bath wastewater two levels of thermal retracting device.
Background technology
Along with improving constantly of people's quality of the life, domestic hot-water's energy consumption constantly increases at the proportion of architectural energy consumption, in conventional bath system, that the higher bath wastewater of temperature enters sewerage after directly will using, so that the contained heat that is higher than environment temperature is wasted in the sewage, more serious for this loss of large-scale centralized formula bath system.Actual bath energy consumes the temperature difference only about 5 ℃, the bathing that contains a large amount of heat energy is landed water-white and has been entered in vain sewer, cause the consumption of bath water energy, the bathing Btu utilization only accounts for and adds 16.7% of the required heat of hot tap-water, remaining heat of 83.3% then is discharged, and wherein comprises the available energy of the temperature that is higher than environment.And the bath wastewater temperature stabilization, flow is suitable, and the potentiality of recuperation of heat are larger.Therefore, utilizing heat pump to reclaim the heat of bath wastewater, reduce part hot water preparation power consumption, is a kind of energy utilization mode of energy-conserving and environment-protective.Application number is the utility model patent of " 200620024573.9 ", a kind of air source hot pump water heater with waste heat recovery plant is disclosed, it comprises by air heat-exchange evaporimeter, the compressor that links to each other with the input of air heat-exchange evaporimeter, output two ends respectively, the working medium circulation loop that condenser forms, condenser is the thermal source of heat-exchanging water tank, heat-exchanging water tank is communicated with respectively hot water outlet and cooling water inlet, also comprise the wastewater heat exchange evaporimeter of being located in the waste water collector, its input, output are connected to respectively input, the output of air heat-exchange evaporimeter.Although this utility model makes the heat energy in the bath wastewater obtain the part utilization, heat recovery rate is lower, and heat energy of bathing waste water does not take full advantage of.
Summary of the invention
The objective of the invention is: provide a kind of heat recovery rate high, energy-efficient bath wastewater two levels of thermal retracting device.
Technical scheme of the present invention is: comprise compressor, condenser, heat exchanger, the input port I of heat exchanger connects the water leg of dress bath wastewater, the delivery outlet I of heat exchanger connects the input port IV of evaporimeter, the delivery outlet IV access discharge outlet of evaporimeter, form the one-level heat exchanging pipe between the input port I of heat exchanger and the delivery outlet I, another input port II of heat exchanger connects running water pipe, the delivery outlet II connects heat-collecting box, forms one-level heat-obtaining pipeline between the input port II of heat exchanger and the delivery outlet II; Condenser is housed in the heat-collecting box, another input port V of evaporimeter connects the delivery outlet V of condenser by throttling arrangement, the delivery outlet VI of evaporimeter connects compressor inlet, compressor outlet connects the input port VI of condenser, form the secondary heat exchange pipeline between the input port IV of evaporimeter and the delivery outlet IV, form secondary heat-obtaining pipeline between evaporimeter, compressor, condenser, the throttling arrangement.
Described heat exchanger is arranged in the water leg.
Described heat-collecting box is connected with control system.
Described compressor, evaporimeter, heat-collecting box are arranged in the housing.
The invention has the beneficial effects as follows: because the input port I of heat exchanger connects the water leg of dress bath wastewater, the delivery outlet I of heat exchanger connects the input port IV of evaporimeter, form the one-level heat exchanging pipe between the input port I of heat exchanger and the delivery outlet I, another input port II of heat exchanger connects running water pipe, the delivery outlet II connects heat-collecting box, form one-level heat-obtaining pipeline between the input port II of heat exchanger and the delivery outlet II, bath water flows into water leg, behind the heat in the heat exchanger absorption water leg, tap water heating is flowed into heat-collecting box, finish the one-level heat-obtaining.Owing to forming secondary heat-obtaining pipeline between evaporimeter, compressor, condenser, the throttling arrangement, through extracting the waste water of heat by the heat in the evaporimeter double absorption waste water for the first time, the compressed machine of refrigerant is collapsed into high temperature and high pressure gas, enter the condenser in the heat-collecting box, the condensation liquefaction heat release becomes liquid, simultaneously with the heating of the water in the heat-collecting box, thereby reaches the purpose of producing bath water, finish the secondary heat-obtaining, drain through the bath wastewater inflow sewer of second extraction heat.Simultaneously, heat-collecting box is connected with control system, and when the temperature in the heat-collecting box reached the bathing temperature, compressor quit work, by one-level heat-obtaining device continuous heat supply; When the temperature in the heat-collecting box does not reach the bathing temperature, by one-level, the simultaneously heat supply of secondary heat-obtaining device, move in circles with this.Heat recovery rate of the present invention is high, and is energy-efficient, safe and reliable, can be used for the places such as family, unit, bath center.
Description of drawings
Fig. 1 is structural representation of the present invention.
Figure labeling description: 1, condenser; 2, heat exchanger; 3, evaporimeter; 4, throttling arrangement; 5, compressor; 6; Shower nozzle; 7, heat-collecting box; 8, running water pipe.
The specific embodiment
Can find out from structural representation of the present invention shown in Figure 1, the present invention includes the parts such as compressor 5, condenser 1, heat exchanger 2, evaporimeter 3, throttling arrangement 4, heat-collecting box 7, shower nozzle 6.The input port I of heat exchanger 2 connects the water leg of dress bath wastewater, the delivery outlet I of heat exchanger 2 connects the input port IV of evaporimeter 3, the delivery outlet IV access discharge outlet of evaporimeter 3, and heat exchanger 2 is arranged in the water leg, and water leg is arranged on shower nozzle 6 belows.Form the one-level heat exchanging pipe between the input port I of heat exchanger 2 and the delivery outlet I, another input port II of heat exchanger 2 connects running water pipe 8, the delivery outlet II connects heat-collecting box 7, forms one-level heat-obtaining pipeline between the input port II of heat exchanger 2 and the delivery outlet II.Bath water flows into water leg, behind the heat that heat exchanger 2 is drawn in the water leg, tap water heating is flowed into heat-collecting box 7, finishes the one-level heat-obtaining.Condenser 1 is housed in the heat-collecting box 7, another input port V of evaporimeter 3 connects the delivery outlet V of condenser 1 by throttling arrangement 4, the delivery outlet VI of evaporimeter 3 connects compressor 5 imports, compressor 5 outlets connect the input port VI of condenser 1, form the secondary heat exchange pipeline between the input port IV of evaporimeter 3 and the delivery outlet IV, form secondary heat-obtaining pipeline between evaporimeter 3, compressor 5, condenser 1, the throttling arrangement 4.Waste water through extracting for the first time heat flows in the secondary water leg, by the heat in the evaporimeter 3 double absorption waste water, the compressed machine 5 of refrigerant is collapsed into high temperature and high pressure gas, enters the condenser 1 in the heat-collecting box 7, the condensation liquefaction heat release, become liquid, simultaneously the water in the heat-collecting box 7 is heated, thereby reach the purpose of producing bath water, finish the secondary heat-obtaining, bath wastewater through the second extraction heat is drained from discharge outlet inflow sewer, and the wastewater temperature of draining is only below 10 ℃.
Before bathing, the heat pump that is comprised of compressor 5, evaporimeter 3, condenser 1, throttling arrangement 4 etc. first provides bath hot water, used for bathing, after bath water flows into water leg, heat exchanger 2 is connected with running water pipe 8, behind the heat in the running water absorption water leg, hot water flows into heat-collecting box 7, finishes the one-level heat-obtaining.Because heat-collecting box 7 is connected with control system, along with the control of control system, when the temperature in the heat-collecting box 7 reached the bathing temperature, compressor 5 quit work, and the not heat supply of secondary heat-obtaining device is by one-level heat-obtaining device continuous heat supply.When the temperature in the heat-collecting box 7 does not reach the bathing temperature, by one-level, the simultaneously heat supply of secondary heat-obtaining device, move in circles with this.
Above itemizing the specific embodiment of the present invention, in claim scope of the present invention, can also make multiple improvement, all those skilled in the art without the resulting improvement of creative work all within protection domain of the present invention.
Claims (4)
1. bath wastewater two levels of thermal retracting device, comprise compressor (5), condenser (1), heat exchanger (2), it is characterized in that: the input port I of described heat exchanger (2) connects the water leg of dress bath wastewater, the delivery outlet I of heat exchanger (2) connects the input port IV of evaporimeter (3), the delivery outlet IV access discharge outlet of evaporimeter (3), form the one-level heat exchanging pipe between the input port I of heat exchanger (2) and the delivery outlet I, another input port II of heat exchanger (2) connects running water pipe (8), the delivery outlet II connects heat-collecting box (7), forms one-level heat-obtaining pipeline between the input port II of heat exchanger (2) and the delivery outlet II; Condenser (1) is housed in the described heat-collecting box (7), another input port V of evaporimeter (3) connects the delivery outlet V of condenser (1) by throttling arrangement (4), the delivery outlet VI of evaporimeter (3) connects compressor (5) import, compressor (5) outlet connects the input port VI of condenser (1), form the secondary heat exchange pipeline between the input port IV of evaporimeter (3) and the delivery outlet IV, form secondary heat-obtaining pipeline between evaporimeter (3), compressor (5), condenser (1), the throttling arrangement (4).
2. bath wastewater two levels of thermal retracting device according to claim 1, it is characterized in that: described heat exchanger (2) is arranged in the water leg.
3. bath wastewater two levels of thermal retracting device according to claim 1, it is characterized in that: described heat-collecting box (7) is connected with control system.
4. bath wastewater two levels of thermal retracting device according to claim 1, it is characterized in that: described compressor (5), evaporimeter (3), heat-collecting box (7) are arranged in the housing.
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CN2012103665099A CN102865662A (en) | 2012-09-28 | 2012-09-28 | Two-stage bathing wastewater recovery device |
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CN2012103665099A CN102865662A (en) | 2012-09-28 | 2012-09-28 | Two-stage bathing wastewater recovery device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103528265A (en) * | 2013-09-27 | 2014-01-22 | 刘明勇 | Sewage source directly-draining type heat pump system |
CN109974074A (en) * | 2019-03-29 | 2019-07-05 | 福建工程学院 | A kind of publilc baths residual neat recovering system and its control method |
Citations (6)
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CN200968714Y (en) * | 2006-11-18 | 2007-10-31 | 黄伟 | Heat pump water heater capable of comprehensive utilizing waste hot water |
CN200989660Y (en) * | 2006-12-01 | 2007-12-12 | 喻新程 | Immediate heating heat pump energy-saving water heater |
CN201081405Y (en) * | 2007-06-15 | 2008-07-02 | 深圳市宝美新能源有限公司 | Thermal cycling power-saving water heater |
WO2008094152A1 (en) * | 2007-02-01 | 2008-08-07 | Cotherm Of America Corporation | Heat transfer system and associated methods |
CN202281377U (en) * | 2011-11-09 | 2012-06-20 | 高亚民 | Special thermal energy cyclic utilization and hot-water supply system for bath |
CN202902612U (en) * | 2012-09-28 | 2013-04-24 | 泰安阿拉斯佳空调有限公司 | Two-stage bathing wastewater recovery device |
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2012
- 2012-09-28 CN CN2012103665099A patent/CN102865662A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN200968714Y (en) * | 2006-11-18 | 2007-10-31 | 黄伟 | Heat pump water heater capable of comprehensive utilizing waste hot water |
CN200989660Y (en) * | 2006-12-01 | 2007-12-12 | 喻新程 | Immediate heating heat pump energy-saving water heater |
WO2008094152A1 (en) * | 2007-02-01 | 2008-08-07 | Cotherm Of America Corporation | Heat transfer system and associated methods |
CN201081405Y (en) * | 2007-06-15 | 2008-07-02 | 深圳市宝美新能源有限公司 | Thermal cycling power-saving water heater |
CN202281377U (en) * | 2011-11-09 | 2012-06-20 | 高亚民 | Special thermal energy cyclic utilization and hot-water supply system for bath |
CN202902612U (en) * | 2012-09-28 | 2013-04-24 | 泰安阿拉斯佳空调有限公司 | Two-stage bathing wastewater recovery device |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103528265A (en) * | 2013-09-27 | 2014-01-22 | 刘明勇 | Sewage source directly-draining type heat pump system |
CN109974074A (en) * | 2019-03-29 | 2019-07-05 | 福建工程学院 | A kind of publilc baths residual neat recovering system and its control method |
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Application publication date: 20130109 |