CN205425215U - Energy -conserving dehumidification heating device of integration - Google Patents
Energy -conserving dehumidification heating device of integration Download PDFInfo
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- CN205425215U CN205425215U CN201620217824.9U CN201620217824U CN205425215U CN 205425215 U CN205425215 U CN 205425215U CN 201620217824 U CN201620217824 U CN 201620217824U CN 205425215 U CN205425215 U CN 205425215U
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- air
- surface cooler
- cold wind
- dehumidification
- cooled surface
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Abstract
The utility model discloses an energy -conserving dehumidification heating device of integration, its structure still can include other auxiliary structure including business turn over tuber pipe way, evaporimeter, air -cooled surface cooler, compressor, low pressure table, high pressure gauge, oil and gas separator. The utility model discloses a brand -new energy -conserving dehumidification heating device adopts the internal energy conversion completely, accomplishes dehumidification and heating process, the specific implementation mode be the refrigerant through the high pressure compression to the dehumidification of cooling down of the normal humid gas of normal atmospheric temperature, obtain dry cold wind, the air -cooled surface cooler of dry cold wind diffusion entering utilizes produced self high temperature of compressor compression refrigeration agent to heat dry cold wind, so recycle, reached that simple structure, area are little, technological parameter control is stable, cost of maintenance is low, the extremely low dehumidification heating purpose of energy consumption.
Description
Technical field
This utility model relates to a kind of integrated energy-saving dehumidifying heater, particularly for the equipment needed process gas (such as: air) heating and dehumidification, belongs to medicine, chemical industry, material, food apparatus field.
Background technology
At present, in fields such as medicine, chemical industry, material, food, it is frequently necessary to gas at normal temperature (such as: air) is carried out pretreatment, manufacturing technique requirent could be met, the operations such as special dry, the coating at pharmaceutical industry, need to use hot gas (such as: air), are evaporated moisture or solvent, humidity, to dry, the efficiency of coating and final water balance, has vital effect.And under hot and humid environmental condition, owing to the absolute humidity of air is big, dry, the quality of coating and efficiency all can not get ensureing reliably, the means that gas (such as: air) dehumidifying necessitates.
At present, in order to allow gas (such as: air) reach reliable and technological requirement accurately, through carrying out pretreatment frequently with following several ways: 1. in order to obtain high-temperature gas (such as: air), generally use electrical heating or steam-heated mode, process gas (such as: air) is heated；2. in order to obtain low humid gas (such as: air), generally use the mode of condensation at low temperature dehumidifying, process gas (such as: air) is dehumidified；3. in order to obtain the gas (such as: air) of high temperature drying, then it is to use two kinds and the mode deposited carries out the post-heating that dehumidifies.Its principle is, water is down to low temperature by refrigeration unit, then by surface exchange device, process gas (such as: air) is lowered the temperature with cold water, reach the purpose of dehumidifying, cold air (such as: air) after dehumidifying, then obtain required humiture with electrical heating or steam heating.
For ensureing product quality, and meeting specific technological requirement, be necessary for obtaining high-temperature dry air (such as: air), generally use the mode that two covering devices use simultaneously, there is a lot of defects in which: 1. equipment assembling is loaded down with trivial details, and time cost increases；2. equipment build and occupation of land space are big；3. process parameter control is unstable；4. accessory and consumable accessory increase, and maintenance cost increases；5. energy consumption is greatly increased.
Summary of the invention
Technical problem to be solved in the utility model is to overcome the deficiencies in the prior art, it is provided that the integrated energy-saving dehumidifying heater that a kind of simple in construction, floor space are little, process parameter control is stable, maintenance cost is low, energy consumption is extremely low.
For solving above-mentioned technical problem, the utility model proposes technical scheme is.
This energy-conservation dehumidifying heater is made up of parts such as air inlet/outlet pipeline, vaporizer, air-cooled surface cooler, compressor, low-pressure meter, high pressure gauge, gs-oil separators.
Refrigerated medium after compression carries out cool-down dehumidification by vaporizer to ambient temperature and moisture gas, obtains being dried cold wind.
Dry cold wind diffuses into air-cooled surface cooler, utilizes compressor compresses cold-producing medium self high temperature produced to heat dry cold wind.
Cold-producing medium after heat exchange is thrown away and be there is higher temperature, then the spiral case tubular type surface cooler through circulating carries out second heat exchange to it.
Cold-producing medium after exchange will enter next circulation again, so recycles, and reaches the effect that dehumidifying is heated, reduced energy consumption.
Compared with prior art, this utility model has the advantage that energy-conservation dehumidifying heater, fully utilized dehumidifying energy is changed, and reaches the purpose of heating, and simple in construction, floor space are little, process parameter control is stable, maintenance cost is low, energy consumption is extremely low, production cost is substantially reduced.
Accompanying drawing explanation
Fig. 1, for this utility model without water-cooling structure schematic diagram.
Marginal data.
1-compressor, 2-high pressure gauge, 3-freon pipeline, the air-cooled surface cooler of 4-, 5-spiral case tubular type surface cooler, 6-capillary tube, the air-cooled bellows of 7-, 8-vaporizer, 9-gs-oil separator, 10-low-pressure meter, 11-water tower pump, 12-water tower circulating water pipe, 13-water tower, 14-ambient temperature and moisture wind, 15-air channel, the air channel of 16-confession equipment.Yellow-freon pipeline, blueness-chilled water pipeline, green-wind pipeline.
Fig. 2, for this utility model band water-cooling structure schematic diagram.
Marginal data.
1-compressor, 2-high pressure gauge, the air-cooled surface cooler of 3-, 4-spiral case tubular type surface cooler, 5-capillary tube, 6-chilled water, 7-vaporizer, 8-water tank, 9-gs-oil separator, 10-freon pipeline, 11-low-pressure meter, 12-water tower chilled water pipeline, 13-water tower pump, 14-water tower, 15-water-cooled surface cooler water pump, 16-water-cooled surface cooler, 17-air channel, 18-water-cooled surface cooler conduit pipeline, 19-ambient temperature and moisture wind, the air channel of 20-confession equipment.Yellow-freon pipeline, blueness-chilled water pipeline, green-wind pipeline, red frame-optional part.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described in detail.It should be appreciated that detailed description of the invention described herein is merely to illustrate and explains this utility model, it is not limited to this utility model.
Embodiment one.
In conjunction with accompanying drawing 1, according to a kind of integrated energy-saving dehumidifying heater of the present utility model, it is made up of for the air channel of equipment 1-compressor, 2-high pressure gauge, 3-freon pipeline, the air-cooled surface cooler of 4-, 5-spiral case tubular type surface cooler, 6-capillary tube, the air-cooled bellows of 7-, 8-vaporizer, 9-gs-oil separator, 10-low-pressure meter, 11-water tower pump, 12-water tower circulating water pipe, 13-water tower, 14-ambient temperature and moisture wind, 15-air channel, 16-.
Cold-producing medium passes through 1-compressor compresses, by 8-vaporizer to 14-ambient temperature and moisture wind cool-down dehumidification, obtains being dried cold wind.
Dry cold wind diffuses into the air-cooled surface cooler of 4-, utilizes 1-compressor compresses cold-producing medium self high temperature produced to heat dry cold wind.
Higher temperatures cold-producing medium after heat exchange, the second heat exchange consisted of 5-spiral case tubular type surface cooler, 11-water tower pump, 12-water tower circulating water pipe, 13-water tower is lowered the temperature again.
Cold-producing medium after exchange will enter next circulation again, so recycles, and reaches the effect that dehumidifying is heated, reduced energy consumption.
Embodiment two.
In conjunction with accompanying drawing 2, according to a kind of integrated energy-saving dehumidifying heater of the present utility model, it is made up of for the air channel of equipment 1-compressor, 2-high pressure gauge, the air-cooled surface cooler of 3-, 4-spiral case tubular type surface cooler, 5-capillary tube, 6-chilled water, 7-vaporizer, 8-water tank, 9-gs-oil separator, 10-freon pipeline, 11-low-pressure meter, 12-water tower chilled water pipeline, 13-water tower pump, 14-water tower, 15-water-cooled surface cooler water pump, 16-water-cooled surface cooler, 17-air channel, 18-water-cooled surface cooler conduit pipeline, 19-ambient temperature and moisture wind, 20-.
Cold-producing medium passes through 1-compressor compresses, by 8-vaporizer, water in 8-water tank is implemented cooling, and cold water is pumped in 6-water-cooled surface cooler by 15-water-cooled surface cooler water pump, ambient temperature and moisture gas is carried out cool-down dehumidification, obtains being dried cold wind.
Dry cold wind diffuses into the air-cooled surface cooler of 3-, utilizes 1-compressor compresses cold-producing medium self high temperature produced to heat dry cold wind.
Higher temperatures cold-producing medium after heat exchange, the second heat exchange consisted of 4-spiral case tubular type surface cooler, 12-water tower chilled water pipeline, 13-water tower pump, 14-water tower is lowered the temperature again.
Cold-producing medium after exchange will enter next circulation again, so recycles, and reaches the effect that dehumidifying is heated, reduced energy consumption.
Although this utility model is open as above with preferred embodiment; but it is not for limiting this utility model in fact; any those skilled in the art are without departing from spirit and scope of the present utility model; can make possible variation and amendment, protection domain the most of the present utility model should be defined in the range of standard with this utility model claim.
Claims (1)
1. an integrated energy-saving dehumidifying heater, including air inlet/outlet pipeline, vaporizer, air-cooled surface cooler, compressor, low-pressure meter, high pressure gauge, gs-oil separator, it is characterized in that, refrigerated medium after compression carries out cool-down dehumidification by vaporizer to ambient temperature and moisture gas, obtain being dried cold wind, dry cold wind diffuses into air-cooled surface cooler, utilize compressor compresses cold-producing medium self high temperature produced that dry cold wind is heated, higher temperatures cold-producing medium after heat exchange, spiral case tubular type surface cooler through circulation carries out second heat exchange to it again, enter back into next circulation, so recycle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620217824.9U CN205425215U (en) | 2016-03-22 | 2016-03-22 | Energy -conserving dehumidification heating device of integration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620217824.9U CN205425215U (en) | 2016-03-22 | 2016-03-22 | Energy -conserving dehumidification heating device of integration |
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| Publication Number | Publication Date |
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| CN205425215U true CN205425215U (en) | 2016-08-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620217824.9U Active CN205425215U (en) | 2016-03-22 | 2016-03-22 | Energy -conserving dehumidification heating device of integration |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112516696A (en) * | 2020-11-18 | 2021-03-19 | 威海众海智能科技有限公司 | Constant-temperature and constant-humidity air treatment equipment and method |
-
2016
- 2016-03-22 CN CN201620217824.9U patent/CN205425215U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112516696A (en) * | 2020-11-18 | 2021-03-19 | 威海众海智能科技有限公司 | Constant-temperature and constant-humidity air treatment equipment and method |
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