CN201050462Y - Air compressor residual heat hot water, steamer set - Google Patents
Air compressor residual heat hot water, steamer set Download PDFInfo
- Publication number
- CN201050462Y CN201050462Y CNU2007200526417U CN200720052641U CN201050462Y CN 201050462 Y CN201050462 Y CN 201050462Y CN U2007200526417 U CNU2007200526417 U CN U2007200526417U CN 200720052641 U CN200720052641 U CN 200720052641U CN 201050462 Y CN201050462 Y CN 201050462Y
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- Prior art keywords
- air compressor
- hot water
- residual heat
- vaporizer
- heat
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to the air compressor technical field, particularly to waste heat hot water and a steam engine unit of an air compressor. An oil output pipe of the air compressor passes through respectively a cryogen generator and an evaporator and then is connected to a separation cylinder; the cryogen generator is connected with a condenser which is connected with the evaporator which is connected with an absorber, a pipe for the water waiting for heating passes through the absorber and then is educed out. After being educed out from the absorber, the pipe for the water waiting for heating is connected to a flash evaporation cylinder. The utility model uses the oil low temperature heat source of the waste heat of the air compressor as the driving heat source of the unit, so that the heat energy can be recycled and bring high temperature water and saturated evaporation, two-stage or multi-stage serial connection can form medium and high temperature evaporation.
Description
Technical field:
The utility model relates to the air compressor technical field, particularly residual heat of air compressor hot water, steam unit.
Background technique:
Air compressor is used very extensive in present industrial production, and it is mainly used in electronics, oil, electric power, electrical equipment, medicine, chemical industry, automobile, weaving, food, environmental protection, aviation, machinery, tobacco, printing etc. and each industry of row.Present most of air compressor still has oily air compressor, and when air compressor was worked, oily and oily vapour all had very high temperature, but these heats but do not receive rational application, and major part is directly distributed in air by blower fan.China is the nervous country of an energy, industrialized production needs a large amount of energy safeguards, vital action water, air-conditioning work or the like all need a large amount of energy, and this widely used manufacturing mechanism of picture air compressor, its a large amount of heat resources that have but do not receive rational application, and have formed very how-do-you-do.
The model utility content:
The purpose of this utility model is to provide residual heat of air compressor hot water, steam unit at the deficiencies in the prior art.
For achieving the above object, the utility model adopts following technological scheme:
After passing cryogen generator and vaporizer respectively, the oil gas output pipeline of air compressor is connected to splitter cylinder; The cryogen generator connects condenser, and condenser connects vaporizer, and vaporizer connects adsorber, draws after the pipeline of the water of waiting to heat up passes adsorber.
The pipeline of the described water of waiting to heat up is connected to the flash distillation cylinder after adsorber is drawn.
The pipeline of described water to be cooled is drawn after passing in the condenser.
Be connected with solution heat exchanger between described generator and the adsorber.
Be connected with first cryogenic fluid pump on the liquid-transport pipe-line between described base of evaporator solution and the top duct.
Be connected with second cryogenic fluid pump on the pipeline of described condenser connection vaporizer.
The beneficial effects of the utility model are: use the driving heat source of the oil gas low-temperature heat source of residual heat of air compressor as the unit refrigeration agent; The refrigerant vapour condensation in condenser that takes place in the generator; The cryogen water that condenses in the condenser pumps in the vaporizer by second cryogenic fluid pump; Flash to refrigerant vapour and enter in the adsorber on the evaporator tube surface, by the concentrated solution of spray on the adsorber pipeline absorbed, the absorption heat of emitting when concentrated solution absorbs refrigerant vapour is the interior hot water of heating pipe directly, and the hot water temperature in the pipe is constantly raise; High-temperature-hot-water can directly utilize or flow into step-down flash distillation in the flash distillation cylinder; The steam that flash distillation produced can use as a kind of power heat source that does not have operating cost by the thermal insulation pipe pass to daily life and the required steam utilization place of industrial technology; Thereby reduce the cost of production of enterprise, win enterprise profit, improve the competitiveness.
Description of drawings:
Below in conjunction with accompanying drawing the utility model is further described:
Fig. 1 is a structural principle schematic representation of the present utility model
Embodiment:
See accompanying drawing 1, the oil gas output pipeline 11 of air compressor 12 is connected to splitter cylinder 13 after passing cryogen generator 8 and vaporizer 3 respectively; Cryogen generator 8 connects condensers 5, and condenser 5 connects vaporizers 3, and vaporizer 3 connects adsorbers 2, draws after the pipeline 10 of the water of waiting to heat up passes adsorber 2, and the water after drawing is heated, and promptly exports high-temperature-hot-water.
The pipeline 10 of the described water of waiting to heat up is connected to flash distillation cylinder 1 after adsorber 2 is drawn, flash distillation cylinder 1 can be exported saturated vapour, high-temperature steam during secondary or multi-stage serial connection can form; Promptly go out high-temperature-hot-water without the step-down flash distillation.
The pipeline 14 of described water to be cooled is drawn after passing in the condenser 5.
Be connected with solution heat exchanger 9 between described cryogen generator 8 and the adsorber 2, also be connected with solution pump 7 on the pipeline between cryogen generator 8 and the adsorber 2.
Be connected with first cryogenic fluid pump 4 on the liquid-transport pipe-line between described vaporizer 3 bottom solution and the top duct, the refrigerant cycle in the vaporizer 3 is used.
Be connected with second cryogenic fluid pump 6 on the pipeline of described condenser 5 connection vaporizers 3.
Principle of the present utility model is as follows: cryogen generator 8 and vaporizer 3 use the driving heat source of the oil/gas low-temperature heat source of residual heat of air compressor as unit; The refrigerant vapour condensation in condenser 5 that takes place in the generator 8; Condensing into cryogen water in the condenser 5 pumps in the vaporizer 3 by second cryogenic fluid pump 6.Flashing to refrigerant vapour on vaporizer 3 tube-surfaces enters in the adsorber 2, by the concentrated solution of spray on adsorber 2 pipelines absorbed, concentrated solution discharges the directly interior hot water of heating pipe of a large amount of absorption heat when absorbing refrigerant vapour, the hot water temperature in the pipe is constantly raise.High-temperature-hot-water can directly utilize or flow into step-down flash distillation in the flash distillation cylinder 1.The steam that flash distillation produced can use as a kind of power heat source that does not have operating cost by the thermal insulation pipe pass to daily life and the required steam utilization place of industrial technology.Thereby reduce the cost of production of enterprise, win enterprise profit, improve the competitiveness.
The utility model can alleviate the heavy economic burden that the energy occupies the expenses of taxation for particularly national provincial emphasis energy monitor enterprise of enterprise, energy consumption rich and influential family.Can contain on the socio-economic development road that to the launching out and excessively adopting of non-renewable energy resources papermaking enterprise makes full use of residual heat of air compressor steam, the hot water unit can reduce putting into operation of 1/4 above steam boiler; It is a revolutionary technology behave of response energy-saving and emission-reduction policy.
Claims (6)
1. residual heat of air compressor hot water, steam unit, it is characterized in that: the oil gas output pipeline (11) of air compressor (12) is connected to splitter cylinder (13) after passing cryogen generator (8) and vaporizer (3) respectively; Cryogen generator (8) connects condenser (5), and condenser (5) connects vaporizer (3), and vaporizer (3) connects adsorber (2), draws after the pipeline (10) of the water of waiting to heat up passes adsorber (2).
2. residual heat of air compressor hot water according to claim 1, steam unit is characterized in that: the pipeline (10) of the water of waiting to heat up is connected to flash distillation cylinder (1) after adsorber (2) is drawn.
3. residual heat of air compressor hot water according to claim 1 and 2, steam unit is characterized in that: the pipeline of water to be cooled (14) is drawn after passing in the condenser (5).
4. residual heat of air compressor hot water according to claim 3, steam unit is characterized in that: be connected with solution heat exchanger (9) between cryogen generator (8) and the adsorber (2).
5. residual heat of air compressor hot water according to claim 4, steam unit is characterized in that: be connected with first cryogenic fluid pump (4) on the liquid-transport pipe-line between vaporizer (3) bottom solution and the top duct.
6. residual heat of air compressor hot water according to claim 5, steam unit is characterized in that: be connected with second cryogenic fluid pump (6) on the pipeline of condenser (5) connection vaporizer (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200526417U CN201050462Y (en) | 2007-06-12 | 2007-06-12 | Air compressor residual heat hot water, steamer set |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200526417U CN201050462Y (en) | 2007-06-12 | 2007-06-12 | Air compressor residual heat hot water, steamer set |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201050462Y true CN201050462Y (en) | 2008-04-23 |
Family
ID=39336948
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200526417U Expired - Fee Related CN201050462Y (en) | 2007-06-12 | 2007-06-12 | Air compressor residual heat hot water, steamer set |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201050462Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105972858A (en) * | 2016-06-29 | 2016-09-28 | 杭州华电双冠能源科技有限公司 | System and method for supplying energy and storing energy by utilizing waste heat of air compressor |
| CN110762003A (en) * | 2019-10-17 | 2020-02-07 | 浙江迪贝电气股份有限公司 | Drying device for treating compressed air by utilizing waste heat of screw air compressor |
-
2007
- 2007-06-12 CN CNU2007200526417U patent/CN201050462Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105972858A (en) * | 2016-06-29 | 2016-09-28 | 杭州华电双冠能源科技有限公司 | System and method for supplying energy and storing energy by utilizing waste heat of air compressor |
| CN110762003A (en) * | 2019-10-17 | 2020-02-07 | 浙江迪贝电气股份有限公司 | Drying device for treating compressed air by utilizing waste heat of screw air compressor |
| CN110762003B (en) * | 2019-10-17 | 2024-06-07 | 浙江迪贝电气股份有限公司 | Drying device for treating compressed air by utilizing waste heat of screw air compressor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080423 Termination date: 20150612 |
|
| EXPY | Termination of patent right or utility model |