CN203685521U - Air compressor last-two-stage waste heat recovery system - Google Patents
Air compressor last-two-stage waste heat recovery system Download PDFInfo
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- CN203685521U CN203685521U CN201420052860.5U CN201420052860U CN203685521U CN 203685521 U CN203685521 U CN 203685521U CN 201420052860 U CN201420052860 U CN 201420052860U CN 203685521 U CN203685521 U CN 203685521U
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- heat exchanger
- water
- air
- air compressor
- outlet
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- 239000002918 waste heat Substances 0.000 title abstract description 8
- 238000011084 recovery Methods 0.000 title abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 61
- 230000005540 biological transmission Effects 0.000 claims description 9
- 239000000498 cooling water Substances 0.000 claims description 7
- 239000007789 gas Substances 0.000 abstract description 18
- 239000002699 waste material Substances 0.000 abstract description 8
- 230000006835 compression Effects 0.000 description 17
- 238000007906 compression Methods 0.000 description 17
- 238000005516 engineering process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 241000208340 Araliaceae Species 0.000 description 2
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 2
- 235000003140 Panax quinquefolius Nutrition 0.000 description 2
- 235000008434 ginseng Nutrition 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Abstract
The utility model provides an air compressor last-two-stage waste heat recovery system which comprises a front heat exchanger, a middle heat exchanger, a rear heat exchanger and a temperature control device. The two sides of the front heat exchanger, the two sides of the middle heat exchanger and the two sides of the rear heat exchanger are respectively a gas conveying side and a water conveying side, each water conveying side is provided with a water inlet and a water outlet, and each gas conveying side is provided with a gas inlet and a gas outlet. The water outlet of the rear heat exchanger is connected to the water inlet of the front heat exchanger through a water outlet pipeline, the water outlet of the front heat exchanger is connected to the water inlet of the middle heat exchanger through a water outlet pipeline, and the water inlet of the middle heat exchanger is connected to a water outlet pipeline of the front heat exchanger. Compared with the prior art, a large amount of waste heat generated in the last two stages of the air compressor can be fully utilized and recycled through the front heat exchanger, the middle heat exchanger and the rear heat exchanger, heat using efficiency is improved, and energy waste is avoided.
Description
Technical field
The utility model relates to residual heat of air compressor recovery technology, relates in particular to a kind of air compressor end two-stage residual neat recovering system, and it is widely used in centrifugal and piston type air compressor.
Background technique
Air compressor has become the main flow of world today air compressor development, and it can be widely used in the place that mining, machine-building, building, weaving, petrochemical industry and other need pressurized gas.Taking centrifugal or piston type air compressor as example, because it needs air to compress processing in running, be heat energy by the input electric energy conversion that has 90%, bring to cooler and wherein exceed 90% the heat energy air after compressed, by being dissipated with cooling medium heat exchange.Practice shows, air compressor in the end in the air compressing process of two-stage, by producing a large amount of waste heats, makes full use of this part waste heat and there is no at present effective heat recovery measure, caused a large amount of heat energy to be distributed and and recovery not yet in effect.
Given this, necessaryly provide a kind of residual neat recovering system that is applicable to air compressor end two-stage to solve above-mentioned technical problem.
Model utility content
The technical problem that the utility model solves is to provide a kind of air compressor end two-stage residual neat recovering system, for fully reclaiming the heat that air compressor pressurized air produces.
For solving the problems of the technologies described above, the utility model adopts following technological scheme: a kind of air compressor end two-stage residual neat recovering system, comprises anterior heat exchanger, Intermediate Heat Exchanger, rear portion heat exchanger and temperature control apparatus; The both sides of described anterior heat exchanger, Intermediate Heat Exchanger and rear portion heat exchanger are respectively gas transmission side and water delivery side, and described water delivery side is equipped with water intake and water outlet, and described gas transmission side is equipped with suction port and air outlet; The water outlet of described rear portion heat exchanger is connected to the water intake of described anterior heat exchanger by outlet conduit, the water outlet of described anterior heat exchanger is connected to the water intake of described Intermediate Heat Exchanger by outlet conduit, the water intake of described Intermediate Heat Exchanger is connected on the outlet conduit of described anterior heat exchanger.
Further, the pipeline of water intake one side of described anterior heat exchanger is provided with three-way control valve, and an output port of this three-way control valve is connected on the outlet conduit of anterior heat exchanger.
Further, the water outlet of described Intermediate Heat Exchanger is connected to hot junction by pipeline, and this pipeline is provided with two-way modulating valve and cooling-water temperature sensor; The water intake of described rear portion heat exchanger is introduced circulating water by intake pipe, and intake pipe is provided with three-way control valve.
Further, the pipeline of described anterior heat exchanger air outlet is provided with an air-temperature sensor; The suction port of described rear portion heat exchanger is connected to the air outlet of described Intermediate Heat Exchanger by pipeline, and the pipeline of the air outlet side of rear portion heat exchanger is provided with air-temperature sensor.
Further, described temperature control apparatus comprises a control centre, and this control centre is connected with three-way control valve, two-way modulating valve, cooling-water temperature sensor and air-temperature sensor.
Compared with prior art, before, during and after the two-stage residual neat recovering system utilization of air compressor described in the utility model end, three heat exchangers make full use of and reclaim a large amount of waste heats that produce in the two-stage of air compressor end, improve the utilization efficiency of heat, avoided energy waste.
Brief description of the drawings
Fig. 1 is the schematic diagram of air compressor described in the utility model end two-stage residual neat recovering system.
Embodiment
Refer to shown in Fig. 1, the utility model provides a kind of air compressor end two-stage residual neat recovering system 100, comprises anterior heat exchanger 10, Intermediate Heat Exchanger 20, rear portion heat exchanger 30 and temperature control apparatus 40.Described air compressor end two-stage is divided into: one-level compression set A and be positioned at the two-stage compression device B at one-level compression set A rear, it is for carrying out twice compression to air.
Described anterior heat exchanger 10 is connected between described one-level compression set A and two-stage compression device B, and described anterior heat exchanger 10 is provided with gas transmission side and water delivery side.The suction port 11 of described gas transmission side is connected to one-level compression set A, for pressurized gas is introduced in anterior heat exchanger 10, and the air outlet 12 of gas transmission side is connected to two-stage compression device B, again compress processing for the gas in anterior heat exchanger 10 being introduced to two-stage compression device B, wherein, the pipeline that connects described two-stage compression device B and anterior heat exchanger 10 air outlets 12 is provided with an air-temperature sensor 13, the temperature of the gas of discharging from air outlet 12 for Real-Time Monitoring.
The suction port 21 of described Intermediate Heat Exchanger 20 one end is connected with described two-stage compression device B, for introducing the pressurized air from two-stage compression device B, the air outlet 22 of the other end is connected to described rear portion heat exchanger 30, for aforementioned pressurized air is further guided in rear portion heat exchanger 30.
The suction port 31 of heat exchanger 30 one end, described rear portion is connected to the air outlet 22 of described Intermediate Heat Exchanger 20 by pipeline, the air outlet 32 of the other end is connected to air compressor, and these air outlet 32 sides are provided with air-temperature sensor 33.
Thus, pressurized gas has been realized following circulating path: the anterior heat exchanger 10-two-stage compression device B-Intermediate Heat Exchanger 20-of air compressor-one-level compression set A-rear portion heat exchanger 30-air compressor, solid arrow in ginseng Fig. 1, make the gas of air compressor end two-stage pass through 3 heat exchange equipments, realize sufficient heat exchange, improve the utilization ratio that pressurized air is produced to a large amount of waste heats, avoided waste heat to be distributed the problem of waste.
Meanwhile, the both sides of described anterior heat exchanger 10, Intermediate Heat Exchanger 20 and rear portion heat exchanger 30 are respectively gas transmission side and water delivery side, and described water delivery side is equipped with water intake and water outlet, wherein:
The water intake 34 of described rear portion heat exchanger 30 is introduced circulating water by intake pipe, and intake pipe is provided with three-way control valve 35; The water outlet 36 of described rear portion heat exchanger 30 is connected to the water intake 14 of described anterior heat exchanger 10 by outlet conduit, an output port of described three-way control valve 35 is connected on described outlet conduit.
The water outlet 15 of described anterior heat exchanger 10 is connected to the water intake 23 of described Intermediate Heat Exchanger 20 by outlet conduit, the pipeline of water intake 14 1 sides of described anterior heat exchanger 10 is provided with three-way control valve 15, and an output port of this three-way control valve 15 is connected on the outlet conduit of anterior heat exchanger 10.
26 of the water outlets of described Intermediate Heat Exchanger 20 are connected to hot junction by pipeline, and this pipeline is provided with two-way modulating valve 24 and cooling-water temperature sensor 25, and water intake 23 is connected on the outlet conduit of described anterior heat exchanger 10.
Thus, circulating water has been realized following circulating path: the anterior heat exchanger 10-of circulating water side-rear portion heat exchanger 30-Intermediate Heat Exchanger hot junction-circulating water side for 20-, the dotted arrow in ginseng Fig. 1.
Described temperature control apparatus 40 comprises a control centre, this control centre and three-way control valve 15,35, two-way modulating valve 24, cooling-water temperature sensor 25 and air-temperature sensor 13,33 are connected, and can obtain the temperature data of described cooling-water temperature sensor and air-temperature sensor, regulate and control described three-way control valve, two-way modulating valve according to this temperature data, the open degree of valve is changed, thereby further change the temperature of gas in pipelines and circulating water, ensured stable temperature.In the utility model preferred forms, described three-way control valve is shunting structure, and it has an input port and two output ports.
When operation, in circulating water side, reclaim the part of waste heat in pressurized air in rear portion heat exchanger 30, and make compressed air temperature be cooled to 30 ~ 35 DEG C, water temperature raises by a small margin; Enter again in anterior heat exchanger 10 and reclaim one-level compressed air waste-heat, air temperature is cooled to below 40 DEG C, water temperature raises again; Enter again Intermediate Heat Exchanger 20, reclaim two-stage compressed air waste heat.Circulation regulates temperature control through two logical electric proportional-regulation valves.
In air circulation side, pressurized air enters one-level compression set A, after compression increasing temperature and pressure, enters anterior heat exchanger 10, is cooled to below 40 DEG C; Enter two-stage compression device B again, enter Intermediate Heat Exchanger 20 after again compressing increasing temperature and pressure, part is cooling; Finally enter rear portion heat exchanger 30 and be water-cooled to 30 ~ 35 DEG C by low-temperature circulating.
In sum, the utility model is in the last two stage cycle system of air compressor, and before, during and after utilization, three heat exchangers make full use of and reclaim a large amount of waste heats that produce in the two-stage of air compressor end, have improved the utilization efficiency of heat, have avoided energy waste; Practice shows, heat recovery efficiency is very high, and single-stage can reach more than 80%, and the hot water temperature of generation is high, can reach and approach 90 DEG C, and utilize temperature parameter, convenient operation and the regulation and control of sensor technology energy Real-Time Monitoring heat exchanger water delivery side and gas transmission side.
The above; it is only most preferred embodiment of the present utility model; not the utility model is done to any pro forma restriction; any those of ordinary skill in the art; do not departing from technical solutions of the utility model scope situation; utilize the method content of above-mentioned announcement to make many possible variations and modification to technical solutions of the utility model, all belong to the scope of claims protection.
Claims (5)
1. an air compressor end two-stage residual neat recovering system, is characterized in that: comprise anterior heat exchanger, Intermediate Heat Exchanger, rear portion heat exchanger and temperature control apparatus; The both sides of described anterior heat exchanger, Intermediate Heat Exchanger and rear portion heat exchanger are respectively gas transmission side and water delivery side, and described water delivery side is equipped with water intake and water outlet, and described gas transmission side is equipped with suction port and air outlet; The water outlet of described rear portion heat exchanger is connected to the water intake of described anterior heat exchanger by outlet conduit, the water outlet of described anterior heat exchanger is connected to the water intake of described Intermediate Heat Exchanger by outlet conduit, the water intake of described Intermediate Heat Exchanger is connected on the outlet conduit of described anterior heat exchanger.
2. air compressor according to claim 1 end two-stage residual neat recovering system, it is characterized in that: the pipeline of water intake one side of described anterior heat exchanger is provided with three-way control valve, an output port of this three-way control valve is connected on the outlet conduit of anterior heat exchanger.
3. air compressor according to claim 2 end two-stage residual neat recovering system, is characterized in that: the water outlet of described Intermediate Heat Exchanger is connected to hot junction by pipeline, and this pipeline is provided with two-way modulating valve and cooling-water temperature sensor; The water intake of described rear portion heat exchanger is introduced circulating water by intake pipe, and intake pipe is provided with three-way control valve.
4. air compressor according to claim 2 end two-stage residual neat recovering system, is characterized in that: the pipeline of described anterior heat exchanger air outlet is provided with an air-temperature sensor; The suction port of described rear portion heat exchanger is connected to the air outlet of described Intermediate Heat Exchanger by pipeline, and the pipeline of the air outlet side of rear portion heat exchanger is provided with air-temperature sensor.
5. air compressor according to claim 3 end two-stage residual neat recovering system, is characterized in that: described temperature control apparatus comprises a control centre, and this control centre is connected with three-way control valve, two-way modulating valve, cooling-water temperature sensor and air-temperature sensor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420052860.5U CN203685521U (en) | 2014-01-27 | 2014-01-27 | Air compressor last-two-stage waste heat recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420052860.5U CN203685521U (en) | 2014-01-27 | 2014-01-27 | Air compressor last-two-stage waste heat recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203685521U true CN203685521U (en) | 2014-07-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420052860.5U Expired - Lifetime CN203685521U (en) | 2014-01-27 | 2014-01-27 | Air compressor last-two-stage waste heat recovery system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI672433B (en) * | 2017-12-29 | 2019-09-21 | 明基能源技術股份有限公司 | Heat recycle system |
-
2014
- 2014-01-27 CN CN201420052860.5U patent/CN203685521U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI672433B (en) * | 2017-12-29 | 2019-09-21 | 明基能源技術股份有限公司 | Heat recycle system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 200433 Building 201, Building 11, 128 Xiangyin Road, Yangpu District, Shanghai Patentee after: SHANGHAI RICHEN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 200433 Building 201, Building 11, 128 Xiangyin Road, Yangpu District, Shanghai Patentee before: SHANGHAI RICHEN CO.,LTD. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140702 |
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| CX01 | Expiry of patent term |