CN205135941U - Hydrothermal air compressor machine waste heat recovery system of exportable multiple temperature - Google Patents

Hydrothermal air compressor machine waste heat recovery system of exportable multiple temperature Download PDF

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Publication number
CN205135941U
CN205135941U CN201520719509.1U CN201520719509U CN205135941U CN 205135941 U CN205135941 U CN 205135941U CN 201520719509 U CN201520719509 U CN 201520719509U CN 205135941 U CN205135941 U CN 205135941U
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CN
China
Prior art keywords
water
temperature
air compressor
rising pipe
heat recovery
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Expired - Fee Related
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CN201520719509.1U
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Chinese (zh)
Inventor
赵家柱
吴鹏
梁海峰
曹文明
史宣菊
陈曦
魏强
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HEFEI DESHUN ELECTRICAL EQUIPMENT Co Ltd
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HEFEI DESHUN ELECTRICAL EQUIPMENT Co Ltd
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Priority to CN201520719509.1U priority Critical patent/CN205135941U/en
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Publication of CN205135941U publication Critical patent/CN205135941U/en
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Abstract

The utility model discloses a hydrothermal air compressor machine waste heat recovery system of exportable multiple temperature, this waste heat recovery system includes oil piping system and waterway system. Oil piping system mainly includes the air compressor machine, enters the oil pipe way, plate heat exchanger and play oil pipe way, and waterway system mainly includes water intake pipe, plate heat exchanger and total outlet pipe way. Total outlet pipe way fork is three at least branch outlet pipe ways, and including a low temperature outlet pipe way and two at least high temperature outlet pipe ways, two high temperature outlet pipe ways include first high temperature outlet pipe way and second high temperature outlet pipe way, set up the connection according to parallel between all branch outlet pipe ways, every the high temperature outlet pipe all is equipped with electric heating system on the road. The utility model discloses an air compressor machine waste heat recovery system has adopted the mode of " one -level heat transfer + second grade electrical heating ", can realize that many pipelines go out water simultaneously and different temperatures hot water goes out simultaneously to the leaving water temperature upper limit can be improved, complex operating condition's such as large -scale semiconductor enterprise application demand can be satisfied.

Description

A kind of waste heat recovery system of air compressor of exportable various temperature hot water
Technical field
The utility model relates to heat recovery and air compressor technical field, is specifically related to a kind of waste heat recovery system of air compressor of exportable various temperature hot water.
Background technique
Waste heat recovery system of air compressor is widely adopted in the industrial environment such as colliery, factory.Existing residual neat recovering system realizes the heat exchange between the deep fat of air compressor output and cold water, is cooled by the oil that air compressor exports, and exports hot water, significantly improves heat utilization rate, reduces mechanical disorder, extends the equipment use time.
Existing waste heat recovery system of air compressor substantially only arranges a rising pipe, and in the application of some more complicated operating modes, as in some Semiconductor enterprises, in different working environments, usually need the hot water supply of different temperatures, existing waste heat recovery system of air compressor cannot meet this demand; In addition, require the water temperature of more than 60 DEG C under this kind of working environment, and the exportable water temperature upper limit of existing waste heat recovery system of air compressor is generally at 30 DEG C more.Therefore, be necessary to develop and a kind ofly can export multiple different temperatures hot water and the larger waste heat recovery system of air compressor of output temperature scope simultaneously.
Summary of the invention
The utility model provides a kind of waste heat recovery system of air compressor of exportable various temperature hot water, and this waste heat recovery system of air compressor can export the hot water of various temperature simultaneously, and the water-exit temperature upper limit up to 80 DEG C, can fully meet the application demand of complex working condition.
The technical solution of the utility model is as follows:
A waste heat recovery system of air compressor for exportable various temperature hot water, described residual neat recovering system comprises oil-way system and water circuit system.Oil-way system mainly comprises air compressor, in-line, plate type heat exchanger and outlet line, and water circuit system mainly comprises inlet pipeline, plate type heat exchanger and total rising pipe.Total rising pipe fork is at least three and branches out water lines, and comprise a low temperature rising pipe and at least two high-temperature water outlet pipelines, two high-temperature water outlet pipelines comprise the first high-temperature water outlet pipeline and the second high-temperature water outlet pipeline; All branching out between water lines arranges connection according to parallel way; Every bar high-temperature water outlet pipeline is equipped with electric heating system.
Preferably, the bifurcation approach of total rising pipe is as follows: total rising pipe is divided into two to branch out water lines through three-way valve, wherein one is low temperature rising pipe, and another branches out water lines and is divided into the first high-temperature water outlet pipeline and the second high-temperature water outlet pipeline through three-way valve again.
Preferably, the pipeline front end of described low temperature rising pipe, the first high-temperature water outlet pipeline and the second high-temperature water outlet pipeline is equipped with electric control valve.
More preferably, described electric control valve controls by PLC.
Preferably, the line end of described low temperature rising pipe is provided with the wet pit with water storage and heat insulation function.
Preferably, the tubing that described in-line, outlet line, inlet pipeline, total rising pipe, low temperature rising pipe, the first high-temperature water outlet pipeline and the second high-temperature water outlet pipeline use is soft rubber pipe and soft rubber pipe is wrapped with thermal insulation layer.
Preferably, described electric heating system can be immediately heating water heater.
The technique effect that the utility model realizes is as follows:
The pattern that waste heat recovery system of air compressor of the present utility model have employed " one-level heat exchange+secondary electric heating ", by setting up the mode of electric heating system at high-temperature water outlet pipeline to improve water-exit temperature, solve the difficult problem that traditional only dependence oil temperature heat exchange water-exit temperature is low, be lifted out coolant-temperature gage to 80 DEG C; Meanwhile, because many branch out water lines and to be connected in parallel to each other setting, the water outlet simultaneously of many pipelines can be realized and different temperatures hot water goes out simultaneously, the application demand of the complex working conditions such as large-scale Semiconductor enterprises can be met; In addition, the utility model structure is simple, only need by access three-way valve transformation pipeline on the basis of traditional waste heat recovery system of air compressor, then on different pipeline, increases electric heating system can realize, simple to operate, avoids large-scale equipment to transform.
Oil pipe of the present utility model, water pipe all select soft rubber tubing to substitute the hard tubing of original standard gauge, not only reduce cost, and are convenient to install connection, greatly improve efficiency of construction.
Modulating valve in the utility model etc. are all controlled by PLC, and automaticity is high; In addition, waste heat recovery system of air compressor of the present utility model can carry communication module, is convenient to telecontrol, enables staff according to the startup of actual production situation telecontrol respective valves, closedown, stopping and valve opening.
Accompanying drawing explanation
Fig. 1 is the waste heat recovery system of air compressor structural representation of the exportable various temperature hot water of embodiment 1;
Fig. 2 is the waste heat recovery system of air compressor structural representation of the exportable various temperature hot water of embodiment 2;
Wherein:
1---air compressor, 2---in-line, 21---inlet pressure sensor, 22---filler opening temperature transducer, 3---outlet line, 31---oil outlet pressure transducer, 32---temperature at outlet sensor, 4---plate type heat exchanger, 5---inlet pipeline, 51---water purifying plant, 52---water intake pressure transducer, 53---water intake temperature transducer, 6---total rising pipe, 61---flow control valve, 62---water pump, 63---outlet temperature sensor, 64---water outlet pressure transducer, 65---No. 1 three-way valve, 66---No. 2 three-way valve, 67---low temperature rising pipe, 68---the first high-temperature water outlet pipeline, 681---the first electric heating system, 69---the second high-temperature water outlet pipeline, 691---the second electric heating system, 610---electric control valve, 611---wet pit, 612---No. 3 three-way valve, 613---third high temperature rising pipe, 6131---the 3rd electric heating system, 7---oil circuit three-way valve.
Embodiment
Below in conjunction with specific embodiments the technical solution of the utility model is clearly and completely described.
embodiment 1
Accompanying drawing 1 is the waste heat recovery system of air compressor structural representation of the exportable various temperature hot water of embodiment 1.The working procedure of the waste heat recovery system of air compressor of the exportable various temperature hot water of the present embodiment is as follows:
The deep fat flowed out in air compressor 1 flows into plate type heat exchanger 4 through in-line 2, in plate type heat exchanger 4 with the cold water generation heat exchange flowed into by inlet pipeline 5 after, flow back in air compressor 1 through outlet line 3 by plate type heat exchanger 4 again, achieve cooling of deep fat, again reuse simultaneously; Water through heat exchange then flows out plate type heat exchanger 4 by total rising pipe 6, total rising pipe 6 is divided into two to branch out water lines through No. 1 three-way valve 65, wherein one is low temperature rising pipe 67, and another branches out water lines and is divided into again the first high-temperature water outlet pipeline 68 and the second high-temperature water outlet pipeline 69 through No. 2 three-way valve 66; Low temperature rising pipe 67 does not establish heating equipment, the water wherein flowed keeps identical temperature with the water in total rising pipe 6, the front end of low temperature rising pipe 67 is provided with electric control valve 610 near No. 1 three-way valve 65 place, for controlling the water flow in low temperature rising pipe 67, the end of low temperature rising pipe 67 is provided with the wet pit 611 with thermal insulation property, to hold the low-temperature water heating that low temperature rising pipe 67 flows out; First high-temperature water outlet pipeline 68 and the second high-temperature water outlet pipeline 69 are equipped with electric heating system, for the first high-temperature water outlet pipeline 68, the low-temperature water heating flowing into this pipeline promotes temperature after electric heating, become high-temperature-hot-water, electric heating system front end is provided with electric control valve 610, to control the low-temperature water heating flow of inflow first electric heating system 681.
In-line 2 is disposed with inlet pressure sensor 21 and filler opening temperature transducer 22 along oil-feed direction, filler opening temperature transducer 22 for monitoring the temperature of the oil of in-line 2 internal flow, to prevent its temperature anomaly; Inlet pressure sensor 21 for monitoring the pressure of the oil of in-line 2 internal flow, to prevent oil pressure abnormal.
Outlet line 3 is disposed with temperature at outlet sensor 32 and oil outlet pressure transducer 31 along fuel-displaced direction, oil outlet pressure transducer 31 for monitoring the pressure of the oil of oil-piping 3 internal flow, to prevent oil pressure abnormal; Temperature at outlet sensor 32 in order to monitor the temperature of the oil of oil-piping 3 internal flow, to prevent its temperature anomaly.
Inlet pipeline 5 is provided with water purifying plant 51, water intake pressure transducer 52 and water intake temperature transducer 53 successively along on water inlet direction, and water intake water purifying plant 51 can filter out impurity larger in inlet pipeline 5, particle, sandstone and Ca 2+, Mg 2+, prevent fouling and blocking pipe; Water intake pressure transducer 52 for monitoring the pressure of the water of waterpipe 5 internal flow, to prevent pressure anomaly; Water intake temperature transducer 53 is in order to monitor the temperature of the water of waterpipe 5 internal flow to prevent its temperature anomaly.
Total rising pipe 6 is along water outlet direction being provided with successively flow control valve 61, water pump 62, outlet temperature sensor 63 and water outlet pressure transducer 64, flow control valve 61 is in order to control the flow of water in total rising pipe 6, water pump 62 flows out in total rising pipe 6 in order to impel water, outlet temperature sensor 63 in order to monitor the temperature of the water of total rising pipe 6 internal flow, to control its water-exit temperature; Water outlet pressure transducer 64 for monitoring the pressure of the water of total rising pipe 6 internal flow, to prevent pressure anomaly.The water temperature that can detect according to outlet temperature sensor 63 carrys out the aperture of adjust flux control valve 61: when water temperature is higher than setting value, flow control valve 61 increases corresponding aperture, and the flow of water increases, the corresponding decline of temperature; When water temperature is lower than setting value, flow control valve 61 reduces corresponding aperture to reduce flow, improves water-exit temperature.When flow control valve 11 aperture reaches 100%, when water temperature is still higher than setting value, water pump 12 can be controlled and open, and regulate its rotating speed, improve the flow of water further, reduce water-exit temperature, be finally stable at setting value.
Also be provided with the three-way valve 7 in parallel with plate type heat exchanger 4 between in-line 2 with outlet line 3, in order to ensure the regular path of the rear oil duct of heat exchanger shutdown, air compressor sink normally worked.
In the utility model, the first electric heating system 681 and the second electric heating system 691 can select instant electric water heater or storage-type electric water heater as required.Instant electric water heater carrys out rapid heating flowing water by electrons heat components and parts, instant-heating, need not wait for, without the need to being equipped with water storage tank, usually can start heating within the several seconds, is applicable to water consumption less or do not fix, but needs the occasion of Quick water exit at any time; Storage-type electric water heater refers to long-term or temporary reservoir hot water after water heating, needs water storage tank, is applicable to water consumption and fixes or comparatively large, and do not need the occasion of Quick water exit at any time.In the present embodiment, the first electric heating system 681 selects instant electric water heater, without the need to configuring wet pit; Second electric heating system selects storage-type electric water heater, is therefore configured with the wet pit 611 with water storage and heat insulation function.
embodiment 2
Accompanying drawing 2 is waste heat recovery system of air compressor structural representations of the exportable various temperature hot water of embodiment 2.The working procedure of the waste heat recovery system of air compressor of the exportable various temperature hot water of the present embodiment is as follows:
The deep fat flowed out in air compressor 1 flows into plate type heat exchanger 4 through in-line 2, in plate type heat exchanger 4 with the cold water generation heat exchange flowed into by inlet pipeline 5 after, flow back in air compressor 1 through outlet line 3 by plate type heat exchanger 4 again, achieve cooling of deep fat, again reuse simultaneously; Water through heat exchange then flows out plate type heat exchanger 4 by total rising pipe 6, total rising pipe 6 is divided into two to branch out water lines through No. 1 three-way valve 65, wherein one is low temperature rising pipe 67, another branches out water lines and is divided into again the first high-temperature water outlet pipeline 68 and branch line through No. 2 three-way valve 66, and branch line is divided into the second high-temperature water outlet pipeline 69 and third high temperature rising pipe 613 through No. 3 three-way valve 612 again; Low temperature rising pipe 67 does not establish heating equipment, the water wherein flowed keeps identical temperature with the water in total rising pipe 6, the front end of low temperature rising pipe 67 is provided with electric control valve 610 near No. 1 three-way valve 65 place, for controlling the water flow in low temperature rising pipe 67, the end of low temperature rising pipe 67 is provided with the wet pit 611 with thermal insulation property, to hold the low-temperature water heating that low temperature rising pipe 67 flows out; First high-temperature water outlet pipeline 68, second high-temperature water outlet pipeline 69 and third high temperature rising pipe 613 are equipped with electric heating system, and described electric heating system is immediately heating water heater.
The waste heat recovery system of air compressor of above embodiment to exportable various temperature hot water provided by the utility model is described in detail, and the explanation of above embodiment just understands method of the present utility model and core concept thereof for helping; For one of ordinary skill in the art, according to thought of the present utility model, all will change in specific embodiments and applications, in sum, this description should not be construed as restriction of the present utility model.

Claims (7)

1. the waste heat recovery system of air compressor of an exportable various temperature hot water, described residual neat recovering system comprises oil-way system and water circuit system, in oil-way system, deep fat flows into plate type heat exchanger (4) through in-line (2) by air compressor (1), in plate type heat exchanger (4) with the cold water generation heat exchange flowed into by inlet pipeline (5) after, flow back in air compressor (1) through outlet line (3) by plate type heat exchanger (4) again, water through heat exchange then flows out plate type heat exchanger (4) by total rising pipe (6), in-line (2) is disposed with inlet pressure sensor (21) and filler opening temperature transducer (22) along oil-feed direction, outlet line (3) is disposed with temperature at outlet sensor (32) and oil outlet pressure transducer (31) along fuel-displaced direction, inlet pipeline (5) is provided with water purifying plant (51) successively along on water inlet direction, water intake pressure transducer (52) and water intake temperature transducer (53), total rising pipe (6) is along water outlet direction being provided with successively flow control valve (61), water pump (62), outlet temperature sensor (63) and water outlet pressure transducer (64), it is characterized in that: total rising pipe (6) comprises at least three and branches out water lines, comprise a low temperature rising pipe (67) and at least two high-temperature water outlet pipelines, article two, high-temperature water outlet pipeline comprises the first high-temperature water outlet pipeline (68) and the second high-temperature water outlet pipeline (69), respectively branch out between water lines and connection is set according to parallel way, on upper and the second high-temperature water outlet pipeline (69) of first high-temperature water outlet pipeline (68), also correspondence is provided with the first electric heating system (681) and the second electric heating system (691) respectively.
2. the waste heat recovery system of air compressor of a kind of exportable various temperature hot water according to claim 1, it is characterized in that: described total rising pipe (6) is divided into two to branch out water lines through No. 1 three-way valve (65), wherein one is low temperature rising pipe (67), and another branches out water lines and is divided into the first high-temperature water outlet pipeline (68) and the second high-temperature water outlet pipeline (69) through No. 2 three-way valve (66).
3. the waste heat recovery system of air compressor of a kind of exportable various temperature hot water according to claim 1, is characterized in that: the pipeline front end of described low temperature rising pipe (67), the first high-temperature water outlet pipeline (68) and the second high-temperature water outlet pipeline (69) is equipped with electric control valve (610).
4. the waste heat recovery system of air compressor of a kind of exportable various temperature hot water according to claim 3, is characterized in that: described electric control valve (610) controls by PLC.
5. the waste heat recovery system of air compressor of a kind of exportable various temperature hot water according to claim 1, is characterized in that: the line end of described low temperature rising pipe (67) is provided with the wet pit (611) with water storage and heat insulation function.
6. the waste heat recovery system of air compressor of a kind of exportable various temperature hot water according to claim 1, is characterized in that: the tubing that described in-line (2), outlet line (3), inlet pipeline (5), total rising pipe (6), low temperature rising pipe (67), the first high-temperature water outlet pipeline (68) and the second high-temperature water outlet pipeline (69) use is soft rubber pipe; Described soft rubber pipe is wrapped with thermal insulation layer.
7. the waste heat recovery system of air compressor of a kind of exportable various temperature hot water according to claim 1, is characterized in that: described first electric heating system (681) and the second electric heating system (691) are immediately heating water heaters.
CN201520719509.1U 2015-09-17 2015-09-17 Hydrothermal air compressor machine waste heat recovery system of exportable multiple temperature Expired - Fee Related CN205135941U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105179203A (en) * 2015-09-17 2015-12-23 合肥德顺机电设备有限公司 Air compressor waste heat recycling system capable of outputting hot water at various temperatures

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105179203A (en) * 2015-09-17 2015-12-23 合肥德顺机电设备有限公司 Air compressor waste heat recycling system capable of outputting hot water at various temperatures

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Granted publication date: 20160406

Termination date: 20210917