CN201368618Y - Spray heat recovery device for wastewater - Google Patents

Spray heat recovery device for wastewater Download PDF

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Publication number
CN201368618Y
CN201368618Y CNU2009200628439U CN200920062843U CN201368618Y CN 201368618 Y CN201368618 Y CN 201368618Y CN U2009200628439 U CNU2009200628439 U CN U2009200628439U CN 200920062843 U CN200920062843 U CN 200920062843U CN 201368618 Y CN201368618 Y CN 201368618Y
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China
Prior art keywords
wastewater
pipe
fountain
heat recovery
water
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Expired - Fee Related
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CNU2009200628439U
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Chinese (zh)
Inventor
陈晓
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Chen Xiao
Meng Jianfeng
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Individual
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Priority to CNU2009200628439U priority Critical patent/CN201368618Y/en
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Publication of CN201368618Y publication Critical patent/CN201368618Y/en
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Expired - Fee Related legal-status Critical Current

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Abstract

The utility model belongs to the technical field of energy conservation, and particularly relates to a spray heat recovery device for wastewater, which can solve the problems in the prior art that the reuse of wastewater is unavailable and standardized machine units are absent. The utility model adopts the technical scheme that the spray heat exchanging device in a box type structure consists of two layers, i.e. an upper layer and a lower layer, wherein the upper layer is a spray tank and the lower layer is a wastewater tank; a water distributor, an evaporator and a catch basin are arranged in the spray tank; a wastewater sink is arranged in the wastewater tank; a circulating pump is mounted outside a box body; the water distributor is connected with the wastewater sink through the circulating pump; the evaporator inside the spray tank is connected with a condensing unit through a refrigerant pipeline; an invert U-shaped bend pipe and an overflow pipe are mounted on the outer surface of the spray tank in the position of the catch basin; a communicating pipe is arranged between the two ends of the invert U-shaped bend pipe; regulating valves are mounted on the communicating pipe and the overflow pipe; the catch basin is connected with the wastewater tank through the overflow pipe; and a discharge pipe with a valve is arranged at the bottom part of the external surface of the wastewater tank. The utility model can be applied to various places which are specialized in the heat recovery of wastewater.

Description

A kind of fountain wastewater heat recovery device
Technical field
The utility model belongs to field of energy-saving technology, is specifically related to a kind of fountain wastewater heat recovery device.
Background technology
Along with the raising day by day of expanding economy and people's living standard, the proportion of building energy consumption in the Chinese society total energy consumption is increasing, near 30%.In every building energy consumption, the energy consumption of hot-water supply is only second to the energy consumption of air-conditioning and heating, accounts for 26% of China's building total energy consumption, and annual national heat supply water consumption is about 100,000,000 tons of standard coals.Wastewater temperature after taking a shower, wash one's hands and face and washing is still higher, and pollution level is lighter; Some factories also can discharge the waste water of slight pollution.With the shower is example, and the wastewater temperature of discharge is generally 30-35 ℃, has good waste heat recovery and is worth.The waste heat that reclaims in these waste water can be used for supplying domestic hot-water and winter air-conditioning.
The wastewater heat exchange device is the important component part in the wastewater heat recovery device, and at present, the wastewater heat exchange device mainly contains shell-tube type, bushing type, immersion and fountain.Shell-tube type and double pipe heat exchanger stop up easily, and dirt is easy cleaning not, to the requirements in water quality height; The heat transfer coefficient of immersion heat exchanger is little, and the heat exchange area of requirement is big, and volume is big; And spray-type heat exchanger heat exchange efficiency height can effectively be avoided stopping up, and Fouling Cleaning is convenient.But use the wastewater heat recovery device of spray-type heat exchanger in the prior art, the cleaning fluid spray thrower need be set separately and clean liquid pump, and just directly discharge after the heat exchange of waste water spray, in fact, if wastewater temperature is higher, once the water temperature behind the spray can also continue to reclaim heat.And present wastewater heat recovery device does not form the standardization unit, is difficult to carry out mass production.
Summary of the invention
The purpose of this utility model is at above shortcomings in the prior art, providing a kind of can utilize the waste water behind the spray once more, and wastewater disposal basin and spray-type heat exchanger are combined, the fountain wastewater heat recovery device is designed to the wastewater heat recovery device of standardization unit.
The utility model is to realize above-mentioned purpose by the following technical solutions: this fountain wastewater heat recovery device, comprise fountain heat-exchanger rig and condensation unit, and the condensation unit comprises compressor, condenser, expansion valve and refrigerant tubing; The fountain heat-exchanger rig is bilevel box typed structure, and the upper strata is a spraying box, and lower floor is a waste water tank; Be provided with water-locator, evaporimeter and water leg in the spraying box, be provided with wastewater trough in the waste water tank, the casing outside is provided with circulating pump, and water-locator links to each other with wastewater trough by circulating pump, and the evaporimeter in the spraying box links to each other with the condensation unit by refrigerant tubing; The spraying box outer surface is equipped with inverted U-shaped bend pipe and overflow pipe, and water leg links to each other with waste water tank by overflow pipe, and overflow pipe is provided with valve.
The utlity model has following beneficial effect: the heat exchange efficiency height of (1) spray-type heat exchanger, can effectively avoid stopping up, Fouling Cleaning is convenient.(2) waste water behind the spray can be utilized once more.(3) wastewater disposal basin and spray-type heat exchanger are combined, floor space is little, and the fountain wastewater heat recovery device is designed to the standardization unit, is convenient to mass production.
Device of the present utility model can be applicable to the occasion of discharging slight pollution waste water such as bathhouse, bathing place, hotel, residential area and factory.
Description of drawings
Fig. 1 is the overall structure schematic diagram of the utility model embodiment.
Fig. 2 is the left side view of fountain heat-exchanger rig among Fig. 1.
Fig. 3 is the right side view of fountain heat-exchanger rig among Fig. 1.
Fig. 4 is the front view of fountain heat-exchanger rig among Fig. 1.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is described in further detail.
Referring to Fig. 1, Fig. 2, Fig. 3 and Fig. 4, the wastewater heat recovery device of the utility model embodiment comprises treatment device for water 1, fountain heat-exchanger rig 2 and condensation unit 3.Wherein, fountain heat-exchanger rig 2 is a box typed structure, and two-layer about being separated into, and the upper strata is a spraying box, and lower floor is a waste water tank, and the casing outside is provided with circulating pump 5, and casing is provided with the access door 20 that can open and close.Be provided with water-locator 6, evaporimeter 4 and water leg 9 in the spraying box from top to bottom successively, be provided with wastewater trough 10 in the waste water tank, water-locator 6 links to each other with wastewater trough 10 by circulating pump 5, and the evaporimeter 4 in the spraying box links to each other with condensation unit 3 by refrigerant tubing; The position of the water leg 9 of spraying box outer surface is equipped with inverted U-shaped bend pipe 8 and overflow pipe 11, be provided with communicating pipe between the two ends of inverted U-shaped bend pipe 8, be respectively equipped with valve 7 and control valve 12 on communicating pipe and the overflow pipe 11, water leg 9 links to each other with wastewater trough 10 by overflow pipe 11; The bottom of the outer surface of waste water tank is provided with tapping pipe 14, and tapping pipe is provided with valve 15.Condensation unit 3 includes compressor 17, condenser 16, expansion valve 18, power distribution cabinet 19, refrigerant tubing.The pipeline of collecting waste water links to each other with treatment device for water 1, and treatment device for water 1 links to each other with wastewater trough 10.Water leg 9 and wastewater trough 10 have insulation construction, and the outer surface of waste water tank is provided with liquid level gauge 13.
During this device work, waste water enters treatment device for water 1, flows into wastewater trough 10 after water treatment.Circulating pump 5 is evacuated to the waste water in the wastewater trough 10 water-locator 6 of evaporimeter 4 tops, waste water is sprinkled upon equably on the horizontal heat exchange tube of evaporimeter 4 by water-locator 6, form the liquid film of past current downflow on the surface of heat exchanger tube, carry out heat exchange with the cold-producing medium in the heat exchanger tube, the waste water after the heat release flows into water leg 9.Low-temperature low-pressure refrigerant liquid in the evaporimeter 4 absorbs the heat of vaporization of waste water, the gas that the evaporation back forms enters the compressor 17 of condensation unit 3, become high temperature and high pressure gas after the compression, condensation heat release in the condenser 16 of condensation unit then, liberated heat is with the water inlet heating of condenser 16.Condensed refrigerant liquid becomes the refrigerant liquid of low-temp low-pressure through behind the expansion valve 18, and evaporation so circulates in the refrigerant liquid inflow evaporator 4 of these low-temp low-pressures.
When the water level of water leg reached the position of overflow pipe 11, unnecessary water can flow out from inverted U-shaped bend pipe 8 and overflow pipe 11 simultaneously.Directly drain from the water that inverted U-shaped bend pipe 8 flows out, it is recycling that the higher relatively superficial water of water temperature enters wastewater trough 10 from overflow pipe 11 outflows.When wastewater flow rate is bigger, when the water level in the waste water tank reaches warning line, regulate flow in the overflow pipes 11 by control valve 12.
When this device is not worked, can open valve 7 on the inverted U-shaped bend pipe 8 and the valve 15 on the tapping pipe 14, the waste water in water leg 9 and the wastewater trough 10 are drained.When this device needs maintenance or cleaning, can open access door 20.When cleaning the horizontal heat exchange tube of evaporimeter 4, can adopt following method: open the valve 7 on the inverted U-shaped bend pipe 8, cleaning fluid is poured in the empty wastewater trough 10, utilize circulating pump 5 that cleaning fluid is evacuated to water-locator 6, cleaning fluid evenly is sprayed on the heat exchanger tube of evaporimeter 4 by water-locator 6, the cleaning fluid that cleaned behind the dirt flows out, and also cleaning fluid can be introduced wastewater trough 10 and recycle.
This device is a kind of standardization, modular unit, can select the unit of different sizes according to the flow of different occasion waste water for use, can many in parallel uses of unit.The occasion of or concentrated waste discharge big for wastewater flow can be provided with the balancing tank.

Claims (6)

1, a kind of fountain wastewater heat recovery device comprises fountain heat-exchanger rig and condensation unit, and the condensation unit comprises compressor, condenser, expansion valve and refrigerant tubing; It is characterized in that: the fountain heat-exchanger rig is bilevel box typed structure, and the upper strata is a spraying box, and lower floor is a waste water tank; Be provided with water-locator, evaporimeter and water leg in the spraying box, be provided with wastewater trough in the waste water tank, the casing outside is provided with circulating pump, and water-locator links to each other with wastewater trough by circulating pump, and the evaporimeter in the spraying box links to each other with the condensation unit by refrigerant tubing; The spraying box outer surface is equipped with inverted U-shaped bend pipe and overflow pipe, and water leg links to each other with waste water tank by overflow pipe, and overflow pipe is provided with valve.
2, fountain wastewater heat recovery device according to claim 1, it is characterized in that: be provided with communicating pipe between the two ends of inverted U-shaped bend pipe, communicating pipe is provided with valve.
3, fountain wastewater heat recovery device according to claim 1, it is characterized in that: water leg and wastewater trough have insulation construction.
4, fountain wastewater heat recovery device according to claim 1, it is characterized in that: the bottom of waste water tank outer surface is provided with tapping pipe, and tapping pipe is provided with valve.
5, according to claim 1 or 2 or 3 or 4 described fountain wastewater heat recovery devices, it is characterized in that: the casing of fountain heat-exchanger rig is provided with access door, and the waste water tank outer surface is provided with liquid level gauge.
6, fountain wastewater heat recovery device according to claim 5, it is characterized in that: it also comprises treatment device for water, and waste pipe links to each other with treatment device for water, and treatment device for water links to each other with waste water tank.
CNU2009200628439U 2009-01-06 2009-01-06 Spray heat recovery device for wastewater Expired - Fee Related CN201368618Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2009200628439U CN201368618Y (en) 2009-01-06 2009-01-06 Spray heat recovery device for wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2009200628439U CN201368618Y (en) 2009-01-06 2009-01-06 Spray heat recovery device for wastewater

Publications (1)

Publication Number Publication Date
CN201368618Y true CN201368618Y (en) 2009-12-23

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101846466A (en) * 2010-04-09 2010-09-29 胡长海 Waste water residual heat recovering device
CN103673567A (en) * 2012-09-26 2014-03-26 界首市南都华宇电源有限公司 Water vapor treating device for oxygen-free drying oven
CN104566960A (en) * 2013-10-23 2015-04-29 洛阳中懋环保设备有限公司 Mining area water source comprehensive utilization device for producing hot water

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101846466A (en) * 2010-04-09 2010-09-29 胡长海 Waste water residual heat recovering device
CN101846466B (en) * 2010-04-09 2011-09-14 胡长海 Waste water residual heat recovering device
CN103673567A (en) * 2012-09-26 2014-03-26 界首市南都华宇电源有限公司 Water vapor treating device for oxygen-free drying oven
CN104566960A (en) * 2013-10-23 2015-04-29 洛阳中懋环保设备有限公司 Mining area water source comprehensive utilization device for producing hot water

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20091211

Address after: East Lake road in Hunan province Xiangtan city Yuetang District No. 18, zip code: 411104

Co-patentee after: Meng Jianfeng

Patentee after: Chen Xiao

Address before: East Lake road in Hunan province Xiangtan city Yuetang District No. 18, zip code: 411104

Patentee before: Chen Xiao

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20091223

Termination date: 20110106