CN1814555A - Cold district sewage cold-hot source sewage accompaning-heat treating device - Google Patents
Cold district sewage cold-hot source sewage accompaning-heat treating device Download PDFInfo
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- CN1814555A CN1814555A CN 200610009753 CN200610009753A CN1814555A CN 1814555 A CN1814555 A CN 1814555A CN 200610009753 CN200610009753 CN 200610009753 CN 200610009753 A CN200610009753 A CN 200610009753A CN 1814555 A CN1814555 A CN 1814555A
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Abstract
The invention relates to cold area sewage cold and heat source sewage heating process device. It includes heat pump assembly, processed sewage intake pipe, processed sewage outlet pipe, unprocessed sewage intake pipe, unprocessed sewage outlet pipe, intake end of evaporator, outlet of evaporator, and the outlet of condenser. The invention uses heat pump to distilling the heat quantity from purified water after processed by effluent treatment plant to transmit to the city sewage that needs to be processed by sewage biochemical treatment plant. The invention not only solves the antinomy between distilling the cold area sewage heat energy and sewage biochemical treatment temperature, but also solves the low temperature of sewage biochemical process itself.
Description
Technical field
The municipal effluent that the present invention relates to have handled heats the device that the former water (municipal effluent is untreated) of biochemical treatment is carried out in preparation as the heat pump Cooling and Heat Source.
Background technology
Develop all kinds of low level recyclability clean energies, have important energy saving and environment protection significance.Municipal effluent is one of low-phase energy, it comprises former water and sewage work's sewage of municipal wastewater pipe network, be the largest portion of city waste heat discharge amount, develop municipal effluent is one of effective measure of alleviating energy consumption and problem of environmental pollution effective and reasonablely.Municipal effluent is other Cooling and Heat Source relatively, and the big characteristics of fine quality of the amount of having are estimated 2010, and China's quantity of wastewater effluent will reach 72,000,000,000 m
3, can be to the air conditioning and heating of 20% buildings by the sewage heat energy that heat pump techniques reclaims.Sewage temperature is suitable simultaneously, between 10 ℃～25 ℃, is fit to Winter-summer dual purpose throughout the year, is the good low level Cooling and Heat Source of heat pump, and exploitation prospect is wide.
But the low temperature problem of the extraction of severe cold area sewage heat energy and sewage biochemical treatment is a pair of insoluble contradiction.Severe cold area sewage water temperature is relatively low, if the sewage water temperature is low excessively in the biochemical treatment process, sludge bulking, aeration tank can occurs and problem such as freeze, and water treatment efficiency will reduce, sewage load with handle after water quality be difficult to guarantee.Have to take insulation, heating to improve measures such as former water water temperature for this reason.If the heat energy before the sewage disposal is further developed extraction, certainly will will increase the weight of the seriousness of low temperature problem.
Summary of the invention
The purpose of this invention is to provide a kind of cold district sewage cold-hot source sewage accompaning thermal treatment unit, with the extraction of solution cold district sewage heat energy and the contradiction between the sewage biochemical treatment temperature.The cold district sewage cold-hot source sewage accompaning thermal treatment unit, it comprises heat pump set 1, dispose of sewage into pipe 4, the comb 5 of having disposed of sewage, untreated sewage are gone into pipe 6 and untreated sewage comb 7, disposed of sewage and be communicated with the input terminus of the vaporizer 1-1 of heat pump set 1 into pipe 4, the comb 5 of having disposed of sewage is communicated with the output terminal of vaporizer 1-1, untreated sewage is gone into the input terminus that pipe 6 is communicated with the condenser 1-2 of heat pump set 1, and untreated sewage comb 7 is communicated with the output terminal of the condenser 1-2 of heat pump set 1.Device of the present invention utilizes heat pump set 1 that the heat extraction that is treated as in the water of clean water by sewage work is come out, pass to the municipal effluent of preparation by sewage biochemical treatment factory and office reason, before sewage disposal, do not carry out energy recovery, to avoid the water temp in the biochemical processing procedure of sewage too low, after sewage disposal, this moment the heat extraction in the sewage come out to be used for sewage before the heat treated, improve former water water temperature to reach minimum or best biological existence condition, thereby the quality and the efficient of water treatment procedure have been guaranteed, device of the present invention had both solved the extraction of cold district sewage heat energy and the contradiction between the sewage biochemical treatment temperature, had solved the low temperature problem of sewage biochemical treatment itself again.
Description of drawings
Fig. 1 is the structural representation of embodiment one, Fig. 2 is the structural representation of embodiment two, Fig. 3 is the structural representation of embodiment three, Fig. 4 is the structural representation of embodiment four, Fig. 5 is the structural representation of embodiment five, Fig. 6 is the structural representation of embodiment six, and Fig. 7 is the structural representation of embodiment seven.
Embodiment
Embodiment one: specify present embodiment below in conjunction with Fig. 1.The cold district sewage accompaning-heat treating device, it by heat pump set 1, dispose of sewage into pipe 4, pipe 6 gone into by the comb 5 of having disposed of sewage, untreated sewage and untreated sewage comb 7 is formed, disposed of sewage and be communicated with the input terminus of the vaporizer 1-1 of heat pump set 1 into pipe 4, the comb 5 of having disposed of sewage is communicated with the output terminal of vaporizer 1-1, untreated sewage is gone into the input terminus that pipe 6 is communicated with the condenser 1-2 of heat pump set 1, and untreated sewage comb 7 is communicated with the output terminal of the condenser 1-2 of heat pump set 1.
Embodiment two: specify present embodiment below in conjunction with Fig. 2.The difference of present embodiment and embodiment one is: it also comprises bilayer sleeve interchanger 2, water pump 3, the input terminus of the condenser 1-2 of heat pump set 1 is communicated with an end of annular space between bilayer sleeve interchanger 2 middle external tube 2-1 and the interior pipe 2-2, the output terminal of condenser 1-2 is communicated with the input terminus of water pump 3, the output terminal of water pump 3 is communicated with the other end of annular space between bilayer sleeve interchanger 2 middle external tube 2-1 and the interior pipe 2-2, and the two ends of interior pipe 2-2 inner chamber go into pipe 6 with untreated sewage respectively and untreated sewage comb 7 is connected.Other composition is identical with embodiment one with mode of connection.In this device, as the annular space internal recycle of clean water between condenser 1-2 and outer tube 2-1 and interior pipe 2-2 of medium, untreated sewage flows in interior pipe, thereby reaches the heat transmission.Its advantage is: 1. have powerful anti-pollution function, simultaneously big flow velocity, high reynolds number heat exchange, heat transfer efficiency height; 2. can utilize existing water source heat pump units, system's initial cost is few.
Embodiment three: specify present embodiment below in conjunction with Fig. 3.The difference of present embodiment and embodiment two is: bilayer sleeve interchanger 2 is made up of outer tube 2-1, interior pipe 2-2 and three group fin 2-3 at least, fin 2-3 is fixed between the outside surface of the internal surface of outer tube 2-1 and interior pipe 2-2 and along the two length direction setting, and some groups of fin 2-3 are along the circumferential direction uniform distribution of interior pipe 2-2.So be provided with, give between outer tube 2-1 and the interior pipe 2-2 reliable axial support is provided.Other composition is identical with embodiment two with mode of connection.
Embodiment four: specify present embodiment below in conjunction with Fig. 4.The difference of present embodiment and embodiment two is: it also comprises baffle plate 2-4, junction block 2-5, a ring flange 2-6 and No. two ring flange 2-7, baffle plate 2-4 is fixed on the end of outer tube 2-1 and its sealing, the end of interior pipe 2-2 passes the outside at baffle plate 2-4, manage on the end of 2-2 in No. two ring flange 2-7 is fixed on, the end of junction block 2-5 is communicated with on the annular space between outer tube 2-1 and the interior pipe 2-2, be fixed with ring flange 2-6 on the other end of junction block 2-5 No. one, No. one ring flange 2-6 is parallel to ring flange 2-7 No. two.So be provided with, bilayer sleeve interchanger 2 is docked successively by two sections or multistage to be formed, and the split dismounting is very convenient, helps the dirt in replace tubes more or the purge tube.Other composition is identical with embodiment two with mode of connection.
Embodiment five: specify present embodiment below in conjunction with Fig. 5.The difference of present embodiment and embodiment two is: bilayer sleeve interchanger 2 is by several outer tubes 2-1, pipe 2-2 in several, sewage distribution piping 2-9, sewage collecting pipe 2-10, clean water distribution piping 2-11, clean water collecting pipe 2-12 forms, pipe 2-2 is arranged in the outer tube 2-1 in each, an end of pipe 2-2 inner chamber all is communicated with sewage distribution piping 2-9 in each, the other end of pipe 2-2 inner chamber all is communicated with sewage collecting pipe 2-10 in each, one end of the annular space between outer tube 2-1 and the interior pipe 2-2 is communicated with clean water distribution piping 2-11, and the other end of the annular space between outer tube 2-1 and the interior pipe 2-2 is communicated with clean water collecting pipe 2-12.So be provided with, the bilayer sleeve interchanger of present embodiment is equivalent to multibilayer double-tube heat exchanger in parallel again on the basis of embodiment two, and heat exchange efficiency is greatly improved.Other composition is identical with embodiment two with mode of connection.
Embodiment six: specify present embodiment below in conjunction with Fig. 6.The difference of present embodiment and embodiment one is: the condenser 1-2 of heat pump set 1 is by housing 1-2-1, electric motor 1-2-2, leading screw 1-2-3, some traverse baffle 1-2-4, several feed screw nuts 1-2-5 and prolong 1-2-6 form, some traverse baffle 1-2-4 are along the length direction of the housing 1-2-1 portion that evenly sets within it, leading screw 1-2-3 also screws with the feed screw nut 1-2-5 that is fixed on each traverse baffle 1-2-4 respectively through each traverse baffle 1-2-4, leading screw 1-2-3 passes the end of housing 1-2-1 and the motor shaft of electric motor 1-2-2 fixes to realize the input of rotary power, prolong 1-2-6 is through all traverse baffle 1-2-4, untreated sewage is gone into pipe 6 and is communicated with in the inner chamber of housing 1-2-1 one end, and untreated sewage comb 7 is communicated with in the inner chamber of the housing 1-2-1 the other end.During present embodiment work, feed refrigeration agent in the prolong 1-2-6, feed untreated sewage, the heat transferred untreated sewage that refrigeration agent is entrained in the housing 1-2-1.The intermittent both forward and reverse directions rotation of electric motor 1-2-2, make traverse baffle 1-2-4 linear reciprocating motion, in this device, traverse baffle 1-2-4 is as internal partition, increase the shell side of condenser, traverse baffle moves back and forth the disturbance of both having strengthened current, has increased heat transfer coefficient, can remove simultaneously the adhesion layer of pollutent in lip-deep outer dirt layer of prolong and the water source, improve heat exchange efficiency to a great extent.Present embodiment belongs to the reciprocating type antifouling direct heat exchange heat pump of screw rod.The advantage of this device is: 1. sewage and the direct heat exchange of refrigeration agent working medium, system synthesis thermo-efficiency height; 2. system's occupation of land is few, and the utility appliance energy consumption is low.Other composition is identical with embodiment one with mode of connection.
Embodiment seven: specify present embodiment below in conjunction with Fig. 7.The difference of present embodiment and embodiment one is: the condenser 1-2 of heat pump set 1 is by housing 1-2-1, electric motor 1-2-2, leading screw 1-2-3, scraper plate 1-2-8, feed screw nut 1-2-5, prolong 1-2-6 and spray equipment 1-2-9 form, feed screw nut 1-2-5 is fixed on the center of scraper plate 1-2-8, leading screw 1-2-3 passes scraper plate 1-2-8 and screws mutually with feed screw nut 1-2-5, prolong 1-2-6 passes scraper plate 1-2-8 and is parallel to leading screw 1-2-3, the end that passes housing 1-2-1 of leading screw 1-2-3 and the motor shaft of electric motor 1-2-2 fix to realize the input of rotary power, spray equipment 1-2-9 is fixed on the upper top place in the housing 1-2-1, the inner chamber of spray equipment 1-2-9 is gone into pipe 6 with untreated sewage and is connected, and untreated sewage comb 7 is communicated in the place, bottom of housing 1-2-1 inner chamber.During present embodiment work, feed refrigeration agent in the prolong 1-2-6, untreated sewage adds condenser by the spray mode, the heat transferred untreated sewage that refrigeration agent is entrained.The intermittent both forward and reverse directions rotation of electric motor 1-2-2 makes scraper plate 1-2-8 linear reciprocating motion.Present embodiment is utilized the spray heat exchanger principle, when pollutant load is big in the untreated sewage, very easily block in the condenser, be difficult to cleaning and safeguard, on prolong, increase scraper plate, single or several, move around and strengthen the current disturbance, enhancing heat transfer is removed the adhesion layer of pollutent in the outer dirt layer of pipe and the water source, raising heat exchange efficiency simultaneously.Current are in to drench and swash state in the device, and the heat-exchanging tube bundle spacing is bigger, and heat interchanging area more too.Other composition is identical with embodiment one with mode of connection.
Claims (7)
1, the cold district sewage cold-hot source sewage accompaning thermal treatment unit, it is characterized in that it comprises heat pump set (1), disposed of sewage into pipe (4), the comb (5) of having disposed of sewage, untreated sewage is gone into pipe (6) and untreated sewage comb (7), disposed of sewage and be communicated with the input terminus of the vaporizer (1-1) of heat pump set (1) into pipe (4), the comb (5) of having disposed of sewage is communicated with the output terminal of vaporizer (1-1), untreated sewage is gone into the input terminus that pipe (6) is communicated with the condenser (1-2) of heat pump set (1), and untreated sewage comb (7) is communicated with the output terminal of the condenser (1-2) of heat pump set (1).
2, cold district sewage cold-hot source sewage accompaning thermal treatment unit according to claim 1, it is characterized in that it also comprises bilayer sleeve interchanger (2), water pump (3), the input terminus of the condenser (1-2) of heat pump set (1) is communicated with an end of annular space between bilayer sleeve interchanger (2) middle external tube (2-1) and the interior pipe (2-2), the output terminal of condenser (1-2) is communicated with the input terminus of water pump (3), the output terminal of water pump (3) is communicated with the other end of annular space between bilayer sleeve interchanger (2) middle external tube (2-1) and the interior pipe (2-2), and the two ends of interior pipe (2-2) inner chamber go into pipe (6) with untreated sewage respectively and untreated sewage comb (7) is connected.
3, cold district sewage cold-hot source sewage accompaning thermal treatment unit according to claim 2, it is characterized in that bilayer sleeve interchanger (2) is made up of outer tube (2-1), interior pipe (2-2) and three group fins (2-3) at least, fin (2-3) is fixed between the outside surface of the internal surface of outer tube (2-1) and interior pipe (2-2) and along the two length direction setting, some groups of fins (2-3) are along the circumferential direction uniform distribution of interior pipe (2-2).
4, cold district sewage cold-hot source sewage accompaning thermal treatment unit according to claim 2, it is characterized in that it also comprises baffle plate (2-4), junction block (2-5), a ring flange (2-6) and No. two ring flanges (2-7), baffle plate (2-4) is fixed on the end of outer tube (2-1) and its sealing, the end of interior pipe (2-2) passes the outside at baffle plate (2-4), No. two ring flanges (2-7) are fixed on the end of interior pipe (2-2), one end of junction block (2-5) is communicated with on the annular space between outer tube (2-1) and the interior pipe (2-2), be fixed with a ring flange (2-6) on the other end of junction block (2-5), a ring flange (2-6) is parallel to No. two ring flanges (2-7).
5, cold district sewage cold-hot source sewage accompaning thermal treatment unit according to claim 2, it is characterized in that bilayer sleeve interchanger (2) is by several outer tubes (2-1), pipe (2-2) in several, sewage distribution piping (2-9), sewage collecting pipe (2-10), clean water distribution piping (2-11), clean water collecting pipe (2-12) is formed, pipe (2-2) all is arranged in the outer tube (2-1) in each, an end of pipe (2-2) inner chamber all is communicated with sewage distribution piping (2-9) in each, the other end of pipe (2-2) inner chamber all is communicated with sewage collecting pipe (2-10) in each, one end of the annular space between outer tube (2-1) and the interior pipe (2-2) is communicated with clean water distribution piping (2-11), and the other end of the annular space between outer tube (2-1) and the interior pipe (2-2) is communicated with clean water collecting pipe (2-12).
6, cold district sewage cold-hot source sewage accompaning thermal treatment unit according to claim 1, the condenser (1-2) that it is characterized in that heat pump set (1) is by housing (1-2-1), electric motor (1-2-2), leading screw (1-2-3), some traverse baffles (1-2-4), several feed screw nuts (1-2-5) and prolong (1-2-6) are formed, some traverse baffles (1-2-4) are along the length direction of housing (1-2-1) portion that evenly sets within it, leading screw (1-2-3) also screws with the feed screw nut (1-2-5) that is fixed on each traverse baffle (1-2-4) respectively through each traverse baffle (1-2-4), leading screw (1-2-3) passes the end of housing (1-2-1) and the motor shaft of electric motor (1-2-2) fixes, prolong (1-2-6) is through all traverse baffles (1-2-4), untreated sewage is gone into pipe (6) and is communicated with in the inner chamber of housing (1-2-1) end, and untreated sewage comb (7) is communicated with in the inner chamber of housing (1-2-1) the other end.
7, cold district sewage cold-hot source sewage accompaning thermal treatment unit according to claim 1, the condenser (1-2) that it is characterized in that heat pump set (1) is by housing (1-2-1), electric motor (1-2-2), leading screw (1-2-3), scraper plate (1-2-8), feed screw nut (1-2-5), prolong (1-2-6) and spray equipment (1-2-9) are formed, feed screw nut (1-2-5) is fixed on the center of scraper plate (1-2-8), leading screw (1-2-3) passes scraper plate (1-2-8) and screws mutually with feed screw nut (1-2-5), prolong (1-2-6) passes scraper plate (1-2-8) and is parallel to leading screw (1-2-3), the end that passes housing (1-2-1) of leading screw (1-2-3) and the motor shaft of electric motor (1-2-2) fix, spray equipment (1-2-9) is fixed on the upper top place in the housing (1-2-1), the inner chamber of spray equipment (1-2-9) is gone into pipe (6) with untreated sewage and is connected, and untreated sewage comb (7) is communicated in the place, bottom of housing (1-2-1) inner chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100097534A CN100357677C (en) | 2006-02-28 | 2006-02-28 | Cold district sewage cold-hot source sewage accompaning-heat treating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100097534A CN100357677C (en) | 2006-02-28 | 2006-02-28 | Cold district sewage cold-hot source sewage accompaning-heat treating device |
Publications (2)
| Publication Number | Publication Date |
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| CN1814555A true CN1814555A (en) | 2006-08-09 |
| CN100357677C CN100357677C (en) | 2007-12-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB2006100097534A Expired - Fee Related CN100357677C (en) | 2006-02-28 | 2006-02-28 | Cold district sewage cold-hot source sewage accompaning-heat treating device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103575156A (en) * | 2012-07-19 | 2014-02-12 | 上海典诗诚金能源科技有限公司 | Heat exchanger |
| CN113149340A (en) * | 2021-03-24 | 2021-07-23 | 白果科技股份公司 | Device for thermal recycling of sewage treatment and implementation method |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3014158A1 (en) * | 1979-04-19 | 1980-10-30 | John J Hunter | METHOD FOR LINING THE OPEN END OF A TUBE AND PIPE CONNECTION |
| DE3347815C2 (en) * | 1983-02-26 | 1986-07-31 | Johs. Burmester & Co GmbH, 2054 Geesthacht | Cleaning device for the evaporator device of a heat pump to extract heat from water |
| US5385645A (en) * | 1991-06-17 | 1995-01-31 | Y. T. Li Engineering, Inc. | Heat transfer apparatus with positive drive orbital whip rod |
| CN1412505A (en) * | 2002-12-04 | 2003-04-23 | 北京佩特姆科技发展有限公司 | Heat pump type crude oil heating system |
| CN2722176Y (en) * | 2004-07-29 | 2005-08-31 | 赵石冠 | Heat exchanging pipe |
| CN1285868C (en) * | 2005-04-26 | 2006-11-22 | 哈尔滨工业大学 | Heat exchange application method of transporting cold and heat source in straight flow from city native ground wastewater |
| CN1719179A (en) * | 2005-07-11 | 2006-01-11 | 刘庆久 | Pipe heat exchanger |
-
2006
- 2006-02-28 CN CNB2006100097534A patent/CN100357677C/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103575156A (en) * | 2012-07-19 | 2014-02-12 | 上海典诗诚金能源科技有限公司 | Heat exchanger |
| CN113149340A (en) * | 2021-03-24 | 2021-07-23 | 白果科技股份公司 | Device for thermal recycling of sewage treatment and implementation method |
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| Publication number | Publication date |
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| CN100357677C (en) | 2007-12-26 |
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Granted publication date: 20071226 Termination date: 20100228 |