CN107763760A - The low dew point rotary wheel dehumidifying unit of normal temperature - Google Patents
The low dew point rotary wheel dehumidifying unit of normal temperature Download PDFInfo
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- CN107763760A CN107763760A CN201711187501.5A CN201711187501A CN107763760A CN 107763760 A CN107763760 A CN 107763760A CN 201711187501 A CN201711187501 A CN 201711187501A CN 107763760 A CN107763760 A CN 107763760A
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Abstract
The invention discloses a kind of low dew point rotary wheel dehumidifying unit of normal temperature, including one-level runner heat exchanger, two level runner heat exchanger, preceding surface cooler, middle surface cooler, rear surface cooling device, one-level regenerative heater and secondary regenerator heater, one-level runner heat exchanger, which is distinguished, sets coagulation moisture absorption area and one-level regeneration desorption area, two level runner heat exchanger, which is distinguished, sets two stage treatment moisture absorption area, secondary regenerator is desorbed area and secondary regenerator cooling zone, fresh air is separated into two-way after preceding surface cooler and coagulation moisture absorption area form mixing wind with return air successively, mixing wind passes through middle surface cooler successively all the way, blown behind two stage treatment moisture absorption area and rear surface cooling device to arid region, another way mixing wind passes through secondary regenerator cooling zone successively, one-level regenerative heater, secondary regenerator is desorbed area, secondary regenerator heater and one-level regeneration are desorbed area's heel row to outdoor.The rotary wheel dehumidifying unit air-flow is steady, overall loine pressure is balanced, energy-saving, industrial and mineral is stable.
Description
Technical field
The present invention relates to rotary dehumidifier technical field, more particularly, to a kind of low dew point rotary wheel dehumidifying unit of normal temperature.
Background technology
Sorption dehumidifiers are acknowledged as mentioning the freezing of CFC ' s compressions and removed with its significant energy-conservation and environment-friendly advantage
One of wet one preferred technique, rotary wheel dehumidifying function is rapid, simple and effective reduction air humidity, using industrial exhaust heat, useless
The low grade heat energies such as heat, solar energy, natural gas are the renewable sources of energy, non-environmental-pollution, and energy consumption is low.It is widely used in food, doctor
Medicine, electronics, electrical equipment, chemical industry etc. have the industry of humidity requirement.As shown in fig. 1, the low dew-point dehumidifying group of current conventional type
In have the disadvantage that：1. single processing blower fan, local head is excessive, and air-flow is easily revealed, and the unstable noise of system is big, and overbottom pressure can
Tonality is few.2. regeneration wind is derived from the cold rear side of middle table, the middle cold cold invalid increase of consumption of table.3. regeneration wind invalid reduces 20 by middle table is cold
More than DEG C.
The content of the invention
In view of the shortcomings of the prior art, technical problem to be solved is to provide that a kind of air-flow is steady, integral tube to the present invention
Balanced, energy-saving, industrial and mineral the is stable low dew point rotary wheel dehumidifying unit of normal temperature of road pressure.
The present invention is to be addressed above-mentioned technical problem by the following technical programs.
The low dew point rotary wheel dehumidifying unit of normal temperature, including one-level runner heat exchanger, two level runner heat exchanger, preceding surface cooler, in
Between surface cooler, rear surface cooling device, one-level regenerative heater and secondary regenerator heater, one-level runner heat exchanger distinguish set one-level at
Moisture absorption area and one-level regeneration desorption area are managed, two level runner heat exchanger, which is distinguished, sets two stage treatment moisture absorption area, secondary regenerator desorption area
With secondary regenerator cooling zone, fresh air is separated into after preceding surface cooler and coagulation moisture absorption area form mixing wind with return air successively
Two-way, air-supply is to arid region after middle surface cooler, two stage treatment moisture absorption area and rear surface cooling device successively for mixing wind all the way, separately
Mixing wind is successively by secondary regenerator cooling zone, one-level regenerative heater, secondary regenerator desorption area, secondary regenerator heater all the way
Desorption area's heel row is regenerated to outdoor with one-level.
Preferably, also include the first processing blower fan and second processing blower fan, it is cold in one-level runner heat exchanger and middle table
First processing blower fan is set between device, second processing blower fan is set between two level runner heat exchanger and rear surface cooling device.
Preferably, also including regeneration blower fan, mixing wind is sent into secondary regenerator cooling zone by the first processing blower fan, then leads to
Cross behind one-level regeneration desorption area and drain into outdoor through regenerating blower fan.
Preferably, two stage treatment moisture absorption area, secondary regenerator desorption area and secondary regenerator cooling zone are respectively 30 to 60 degree
Sector region, 30 to 60 degree sector regions and 240 to 300 degree sector regions.
Beneficial effects of the present invention：
1. pair processing blower fan, air-flow is steady, and overbottom pressure adjustability is more.
2. regeneration blower fan make it that overall loine pressure is balanced (to treatment region), regeneration overbottom pressure adjustability is more, and regeneration, processing are let out
Drain low.
3. cold front side during regeneration wind is derived from, enters 40 DEG C or so of two level runner temperature, in passing through relative to conventional type regeneration wind
Two level runner is re-fed into after cold cooling, have 20 DEG C on energy-saving efficiency, and excessively middle cold blast rate reduce after in cold energy consumption for cooling
Therewith will be low.
4. reachable more than -70 DEG C of dew point of blowing, stable conditions.
Brief description of the drawings
It is intended to be easy to describe preferred embodiment in conjunction with the following drawings, does not form limiting the scope of the invention.
Fig. 1 is the structural representation of the low dew-point dehumidifying group of prior art；
Fig. 2 is the structural representation of the embodiment of the present invention.
In figure：1- one-level runner heat exchangers, 2- two level runner heat exchangers, surface cooler before 3-, surface cooler among 4-, table after 5-
Cooler, 6- one-level regenerative heaters, 7- secondary regenerator heaters, 8- first handle blower fan, 9- second processing blower fans, 10- regeneration
Blower fan.
Embodiment
In order to facilitate the present invention is understood, below in conjunction with the accompanying drawings in the preferred embodiment of the invention that provides the present invention is entered
The detailed description of row.
As shown in Fig. 2 the low dew point rotary wheel dehumidifying unit of the normal temperature of the embodiment of the present invention, including one-level runner heat exchanger 1, two
Level runner heat exchanger 2, preceding surface cooler 3, middle surface cooler 4, rear surface cooling device 5, one-level regenerative heater 6 and secondary regenerator heater
7, one-level runner heat exchanger 1, which is distinguished, sets coagulation moisture absorption area and one-level regeneration desorption area, and two level runner heat exchanger 2 is distinguished and set
Put two stage treatment moisture absorption area, secondary regenerator desorption area and secondary regenerator cooling zone.As one embodiment, two stage treatment moisture absorption
Area, secondary regenerator desorption area and secondary regenerator cooling zone are respectively 60 degree of sector regions, 60 degree of sector regions and 240 degree of fan sections
Domain.Can be according to needed for actual conditions, two stage treatment moisture absorption area is arranged to 30 to 60 degree sector regions, and secondary regenerator desorption area is set
Into 30 to 60 degree sector regions, secondary regenerator cooling zone is arranged to 240 to 300 degree sector regions.
In the present embodiment, fresh air is cooled to 12 degree and the heat exchange heating of coagulation moisture absorption area by preceding surface cooler 3 successively
After to 38 degree with return air formed mixing wind be separated into two-way again, all the way mixing wind pass through successively middle surface cooler 4 be cooled to 12 degree,
Air-supply to arid region, another way mixing wind passes through successively after being cooled again by rear surface cooling device 5 by the heat exchange of two stage treatment moisture absorption area
The heat exchange of secondary regenerator cooling zone is crossed to be warming up to 70 degree, 135 degree are heated to through one-level regenerative heater 6, being desorbed area through secondary regenerator
Heat exchange is cooled to 45 degree, 10 degree are heated to through secondary regenerator heater 7 and regenerate desorption area heat exchange cooling heel row extremely by one-level
It is outdoor.Wherein, temperature variations have different amplitudes of variation under the restriction of the factors such as actual air volume size variation.
First processing blower fan 8 is set between one-level runner heat exchanger 1 and middle surface cooler 4, in two level runner heat exchanger 2
Second processing blower fan 9 is set between rear surface cooling device 5.Using double processing blower fans, air-flow is steady, by handling blower fan by adjusting
Frequency, overbottom pressure adjustability is more.
Further, in addition to regeneration blower fan 10, mixing wind are sent into secondary regenerator by the first processing blower fan 8 and cooled down
Area, then regenerate to be desorbed behind area by one-level and drain into outdoor through regenerating blower fan 10.
Regeneration blower fan make it that overall loine pressure is balanced, and regeneration overbottom pressure adjustability is more, and regeneration, processing leakage are extremely low.
Compares figure 1 and Fig. 2 are understood, wind is regenerated in the embodiment of the present invention and is derived from front side of middle surface cooler, it is cold to enter secondary regenerator
But 35 degree of area, secondary regenerator cooling zone is re-fed into after the cooling of middle surface cooler with the regeneration wind of prior art, there are 20 DEG C
On energy-saving efficiency, and excessively among after surface cooler air quantity reduces, middle surface cooler energy consumption for cooling also therewith will be low, realizes energy-conservation
The purpose of consumption reduction, meanwhile, it can also reduce two level runner heat exchanger heat consumption.
Some technical terms used in the present invention are intended merely to facilitate description, are not construed as limiting the invention,
The present invention is not limited to above-described preferable embodiment, the public affairs that can be known based on those skilled in the art
Know technology or use and be capable of the various modifications of equivalence replacement and the embodiment of change in the prior art, it is every to be based on this hair
Bright spirit or technical concept, should be included in the scope of the protection.
Claims (4)
1. the low dew point rotary wheel dehumidifying unit of normal temperature, it is characterized in that：Including one-level runner heat exchanger（1）, two level runner heat exchanger
（2）, preceding surface cooler（3）, middle surface cooler（4）, rear surface cooling device（5）, one-level regenerative heater（6）With secondary regenerator heater
（7）, one-level runner heat exchanger（1）Distinguish and coagulation moisture absorption area and one-level regeneration desorption area, two level runner heat exchanger are set（2）
Distinguish and set two stage treatment moisture absorption area, secondary regenerator desorption area and secondary regenerator cooling zone, fresh air to pass through preceding surface cooler successively（3）
Two-way is separated into after forming mixing wind with coagulation moisture absorption area and return air, mixing wind passes through middle surface cooler successively all the way（4）、
Two stage treatment moisture absorption area and rear surface cooling device（5）After blow to arid region, another way mixing wind cools down by secondary regenerator successively
Area, one-level regenerative heater（6）, secondary regenerator desorption area, secondary regenerator heater（7）Desorption area's heel row is regenerated to room with one-level
Outside.
2. the low dew point rotary wheel dehumidifying unit of normal temperature according to claim 1, it is characterized in that：Also include the first processing blower fan
（8）With second processing blower fan（9）, in one-level runner heat exchanger（1）With middle surface cooler（4）Between set first processing blower fan
（8）, in two level runner heat exchanger（2）With rear surface cooling device（5）Between set second processing blower fan（9）.
3. the low dew point rotary wheel dehumidifying unit of normal temperature according to claim 1, it is characterized in that：Also include regeneration blower fan（10）,
Mixing wind passes through the first processing blower fan（8）Secondary regenerator cooling zone is sent into, then is regenerated and is desorbed behind area through regenerating blower fan by one-level
（10）Drain into outdoor.
4. the low dew point rotary wheel dehumidifying unit of normal temperature according to claim 1, it is characterized in that：Two stage treatment moisture absorption area, two level
Regeneration desorption area and secondary regenerator cooling zone are respectively 30 to 60 degree sector regions, 30 to 60 degree sector regions and 240 to 300 degree
Sector region.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711187501.5A CN107763760A (en) | 2017-11-24 | 2017-11-24 | The low dew point rotary wheel dehumidifying unit of normal temperature |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711187501.5A CN107763760A (en) | 2017-11-24 | 2017-11-24 | The low dew point rotary wheel dehumidifying unit of normal temperature |
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| CN107763760A true CN107763760A (en) | 2018-03-06 |
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| CN201711187501.5A Pending CN107763760A (en) | 2017-11-24 | 2017-11-24 | The low dew point rotary wheel dehumidifying unit of normal temperature |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109340935A (en) * | 2018-11-13 | 2019-02-15 | 东莞信易电热机械有限公司 | A kind of two-in-series rotary wheel dehumidifying drying system |
| CN110375396A (en) * | 2019-08-13 | 2019-10-25 | 河南中瑞制冷科技有限公司 | A kind of large size depth dehumidification system and its working method |
| CN110822570A (en) * | 2019-11-19 | 2020-02-21 | 常州纺织服装职业技术学院 | Control method of rotary wheel dehumidification device with forced dehumidification function |
| CN113390133A (en) * | 2021-05-12 | 2021-09-14 | 上海应用技术大学 | Dew removing system with dehumidifying wheel |
| CN114060972A (en) * | 2021-10-20 | 2022-02-18 | 瀚润特环保设备（江苏）有限公司 | High-temperature heat pump dehumidifier |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002320817A (en) * | 2001-04-24 | 2002-11-05 | Takasago Thermal Eng Co Ltd | Dehumidifying device and dehumidifying method |
| CN203518066U (en) * | 2013-09-18 | 2014-04-02 | 深圳市优利美科技有限公司 | Fresh air mixing regeneration air rotary dehumidifier |
| CN203803338U (en) * | 2014-01-04 | 2014-09-03 | 马军 | Low-dew-point air dehumidifying device |
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2017
- 2017-11-24 CN CN201711187501.5A patent/CN107763760A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002320817A (en) * | 2001-04-24 | 2002-11-05 | Takasago Thermal Eng Co Ltd | Dehumidifying device and dehumidifying method |
| CN203518066U (en) * | 2013-09-18 | 2014-04-02 | 深圳市优利美科技有限公司 | Fresh air mixing regeneration air rotary dehumidifier |
| CN203803338U (en) * | 2014-01-04 | 2014-09-03 | 马军 | Low-dew-point air dehumidifying device |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109340935A (en) * | 2018-11-13 | 2019-02-15 | 东莞信易电热机械有限公司 | A kind of two-in-series rotary wheel dehumidifying drying system |
| CN110375396A (en) * | 2019-08-13 | 2019-10-25 | 河南中瑞制冷科技有限公司 | A kind of large size depth dehumidification system and its working method |
| CN110822570A (en) * | 2019-11-19 | 2020-02-21 | 常州纺织服装职业技术学院 | Control method of rotary wheel dehumidification device with forced dehumidification function |
| CN113390133A (en) * | 2021-05-12 | 2021-09-14 | 上海应用技术大学 | Dew removing system with dehumidifying wheel |
| CN114060972A (en) * | 2021-10-20 | 2022-02-18 | 瀚润特环保设备（江苏）有限公司 | High-temperature heat pump dehumidifier |
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Application publication date: 20180306 |