CN1962030A - Apparatus for circulating regenerated air and drying compressed air by use of fan - Google Patents
Apparatus for circulating regenerated air and drying compressed air by use of fan Download PDFInfo
- Publication number
- CN1962030A CN1962030A CN 200510115596 CN200510115596A CN1962030A CN 1962030 A CN1962030 A CN 1962030A CN 200510115596 CN200510115596 CN 200510115596 CN 200510115596 A CN200510115596 A CN 200510115596A CN 1962030 A CN1962030 A CN 1962030A
- Authority
- CN
- China
- Prior art keywords
- air
- gas tank
- valve
- regeneration
- heating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Landscapes
- Drying Of Gases (AREA)
Abstract
The invention relates to a device which uses aerator to circulate regenerate air and dry the compressed air, wherein it comprises two dehumidify regenerating air pots and the aerated valve for selectively feeding air to the pots; feeding tube for feeding dried compressed air to the regenerating air pot; the heater for heating the external low-pressure air of aerator, while its valve is opened to heat the low-pressure air; the valve of cooler is opened, it will cools the compressed air from aerator to feed into regenerating air pot; when heating, the water of dehumidifier will be discharged, and the second cooler will cool the dry air, to be circulated.
Description
Technical field
The present invention relates to utilize the drying device of sorbent (dehumidizer) with the moisture removal that contains in the compressed air.Be on compressed-air actuated drying device, air blast to be set particularly, will in the dehumidifying gas tank, the water utilization extraneous air of sorption heat dehumidification, with the air circulation cooling regeneration of dehumidification.In this process, the compression drying air does not have a bit loss, thereby this drying device has extraordinary energy-saving effect.
Background technology
In general, the Chemical Engineering that the compressed air drier of removing the moisture that contains in the air production line, paint line, contact wetting that are widely used in the various automation equipments that must use dry air, semiconductor fabrication factory promptly can initiating chamical reaction, the fields such as protection that metering detects utensil.Compressed air drier can divide two classes substantially: the one, utilize refrigerant condenser that compressed-air actuated temperature is reduced after, make the freezing type of the condensate moisture dehumidifying that contains in the air; Join dehumidizer in the gas tank besides and allow the air that contains moisture pass through, make in the countless close pore of airborne moisture sorption on dehumidizer and realize air dried sorption type through this gas tank.
The sorption type drying device is divided into the non-heated type and two kinds of the heated types that must have thermal source that does not need thermal source by renovation process.Owing to there is not thermal source, there is the shortcoming that consumption rate is big, energy resource consumption is also bigger of regeneration air in the non-heated type; Because thermal source is arranged, have regeneration air and consume the advantage little, that energy resource consumption is little in the heated type.
The technology of general sorption type thermal regeneration drying device constitutes and function simply is described below, be that it comprises: the dehumidifying gas tank that two sizes are identical is (when flowing into humid air in the dehumidifying gas tank, another dehumidifying gas tank will use as the regeneration gas tank), wherein add dehumidizer (or sorbent, hygroscopic agent); Be placed in the upper and lower, be used to change the compressed air direction so that the valve that is used alternatingly of function of dehumidifying and regeneration gas tank; Discharge compressed-air actuated discharge valve during regeneration; Reduce the muffler of discharging noise; The heater (modes such as electrical heating or Steam Heating) that is used for air heat during regeneration; And in control panel of timer and temperature controller etc. is housed.The conversion of the heating in dry engineering and the reengineer process, cool time and dehumidifying gas tank, regeneration gas tank realizes control by timer.Temperature controller is used for regulating the heating-up temperature of heater, and the part compression drying air of uniform temperature flows into the regeneration gas tank, and sorption is had the dehumidizer of moisture to play heating, peels off moisture and then dry effect.After the heating engineering finishes, heater will quit work automatically, at this moment, still have part compression drying air to continue to flow into the regeneration gas tank, play cooling effect.Fig. 1 is the formation schematic diagram of the sorption type drying device heater of external.As shown in the figure, its main composition comprises:
Be arranged on the direction conversion valve (30) that the bottom of device, the air that contains moisture (WA) that can flow into from the outside are supplied with to left and right two gas tanks (10,20) selectivity; Two the moisture the air that contains moisture (WA) that flows through from its inside can be removed and become dry air (DA) dehumidifying and regeneration gas tank (10,20); The muffler of the noise that sends when eliminating spraying high-pressure gas (cleaning muffler, 60); For prevent dry air (DA) and when regeneration necessary regeneration air mix four (pneumatic) stop valves (70,71,72,73) that are arranged on dehumidifying gas tank (10,20) top mutually; Heater (electric heater, 80) to the regeneration air heating; The control panel of control heater etc.; And safety valve (40,50).In this device, the air that contains moisture after the bottom of the regeneration gas tank (10) through being arranged at the drawing left side flows into, just is called dry engineering (Drying) in the process that becomes dry air (DA) in the flow process of upper end by direction conversion valve (30).A part of heater via (80) of dry air (DA) becomes hot-air (hot air), after flowing into from the upper end of the regeneration gas tank (20) of figure right side of face, move to the bottom, play heat effect in the time of setting, this process is called heating engineering (Heating).After heating finished, the power supply (or steam valve) of heater (80) cut off automatically, and heated dehumidizer begins to cool down, and this process is called cooling engineering (Cooling).This cooling procedure also is to carry out in the time of setting, and during this, required that part of dry air all will become humid air (WA) and is discharged in the atmosphere during regeneration.All these processes reached after the predefined time on the control panel, and regeneration gas tank (20), the reengineer that dry engineering can be transformed into the right side can be transformed in the dehumidifying gas tank (10) in left side and carry out, and so repeatedly, carries out continuous operation.
At this, required dry air (DA) is relevant when heater (80) heat that energy resource consumption is mainly required with installing flow and regeneration.The heat of required heater (80) is that compressed air whenever reaches 1000m
3Need 15KW during/HR, regeneration air loss about 8%.(90) are two ventilation pressure valve doors among the figure, and (91) are to regulate the by-pass valve control that regeneration air is banished, and (92) are thermometers, and (93) are pressure gauges, and (94) are pores.
Fig. 2 is the schematic diagram of heater blower exhaust (adorning the heated type of heater blower outward).
As shown in the figure, though the heated type of heater blower is identical with foregoing outer dress heater formula inscape, its difference is to have increased air blast (100).The dry engineering of this device is identical with outer dress heater formula; During reengineer, adorn the heater formula outward and must use a part of dry air (DA), and in this device, after air blast (100) sucked extraneous air, used heater via (80) heating back; Cooling is the same with the heater fitted outside during engineering uses a part of compression drying air.Therefore, this device consumes the required energy of saturation moisture in the employed atmosphere when removing heating than outer dress heater formula more aspect energy consumption, and simultaneously, the motor of air blast also will consume a part of electric power, and this is the shortcoming of this device.
Foregoing sorption type drying device will be accomplished an amount of use during necessary energy (dry air or electric power, steam etc.) when using regeneration, and saves the effect that just can obtain energy savings as much as possible.Wherein, the energy resource consumption during regeneration is inevitably, also is limited on energy-conservation.At the bigger compression drying engineering of energy resource consumption, though adopted several different methods, obtained some energy-conservation effects,, just at last without any consumption, on too high aridity (low more good more) and still unsolved at present technical problem, do not obtain substantial progress yet.
Summary of the invention
The technical problem to be solved in the present invention:
The present invention is with reference to the practical problem of above-mentioned existence, following technical task is proposed, promptly do not use the compression drying air,, the atmosphere that utilization is supplied with by air blast reaches the purpose of regeneration but heating, circulate cooling, thereby guaranteed when keeping the compressed air drying degree reduction significantly of energy resource consumption.Simultaneously, low pressure regeneration (0.1～0.3kg/cm
2) noise pollution when having guaranteed mechanical stability and having eliminated compressed air by pore, the drying device of environment-friendly type is provided for the user.
In order to solve the problems of the technologies described above, the present invention is pursued round the sorption type air dry-set---keep compressed-air actuated aridity constant in, how to reduce the problem of the regeneration required energy and compressed-air actuated consumption, done a large amount of effort.This also is the practical problem that most air dry-set manufacturing enterprise is faced.That is, under the situation that the target predetermined value of dry air aridity remains unchanged, if can be when regeneration the bigger compressed air of consumes energy loss not, then it will be the energy savings mode of more satisfactoryization of sorption type air dry-set.
Utilize air blast that the air in the atmosphere is flow in the regeneration gas tank when core of the present invention is regeneration, during heating, because the heat of compression (80 degree Celsius) of air blast is arranged, the heater heat of consumption is less; During cooling, do not use compressed air, but directly circulate, when having kept the air aridity, realized cooling, thereby obtain energy-conservation effect with atmospheric air.
For this reason, the invention provides a kind of device that utilizes air blast to make regeneration air circulation, compressed air drying, it is characterized in that, comprise: two dehumidifying and the gas tank (10 of regenerating, 20) moisture removal in the air that contains moisture (WA) that, it will pass through internally makes it change dry air (DA) into; And air pressure valve (30,33), the air that contains moisture (WA) selectivity that it will flow into from the outside is supplied with to left and right dehumidifying and the regeneration gas tank (10,20) of being placed in; And wherein cancelled utilize extraneous air heater via heating that will be by air blast (100) and that supply with to regeneration gas tank (20) through cooling, in the circular regeneration formula air dry-set, through the feeding pipe of the dried compressed-air actuated part of dehumidifying gas tank to the supply of regeneration gas tank;
Wherein, give the outer low pressure air heat of supplying with by air blast (100) with heater (80), when heater valve (81) when opening, can be to the low-pressure air after the regeneration gas tank is supplied with heating; After heating finishes, move diametical cooler valve (111) when opening, after cooler (110) cooling, supply with regeneration gas tank (20) by air blast (100) compressed and supplied air with heater valve (81); Under heating, in be contained in moisture in the heating and dehumidification agent in regeneration gas tank (20) and be stripped from fully and be discharged in the atmosphere, second cooler (120) with the dry air cooling after, under the effect of air blast (100), continue to circulate.
Effect of the present invention:
As mentioned above, when keeping compressed-air actuated aridity, because necessary compressed air when not having the regeneration of consumes energy loss maximum, the Utopian as a comparison sorption type air dry-set of the present invention has been obtained extraordinary effect aspect energy savings.
In addition, the present invention utilizes air blast that extraneous air is flow in the regeneration gas tank, during heating, because the heat of compression (80 degree Celsius) of air blast is arranged, can use the heater of low capacity; During cooling, consumption of compressed air not, but utilize extraneous air directly to circulate, in the aridity that keeps air, realize cooling, thereby obtained good energy-saving effect.
Description of drawings
Fig. 1 is that existing heater fitted outside compressed air drier constitutes schematic diagram;
Fig. 2 is that existing heater, air blast exhaust compressed air drier constitute schematic diagram;
Fig. 3 is that heating engineering of the present invention constitutes schematic diagram;
Fig. 4 is that cooling engineering of the present invention constitutes schematic diagram;
Fig. 5 is that the engineering of all pressing of the present invention constitutes schematic diagram;
Fig. 6 is that discharge engineering of the present invention constitutes schematic diagram;
Fig. 7 is the characteristic comparison chart of the present invention and existing scheme.
The specific embodiment
This device is described in detail as follows:
Of the present inventionly utilize air blast as shown in the figure, the schematic diagram of the heating system of heating engineering when Fig. 3 is drying as the schematic representation of apparatus of regeneration air circulation, compressed air drying.
Wherein cancelled the air pressure valve (30,33) that the air that contains moisture (WA) selectivity that will flow into from the outside is supplied with to be placed in left and right dehumidifying and regeneration gas tank (10,20); Cancelled and to have made its two dehumidifying that change dry air (DA) into and gas tank (10,20) of regenerating from the moisture removal the air that contains moisture (WA) that its inside is passed through; Cancelled that utilize will be by the extraneous air heater via heating of air blast (100) and the circular regeneration formula air dry-set of supplying with to regeneration gas tank (20) through cooling, and through the feeding pipe of the dried compressed-air actuated part of dehumidifying gas tank to the supply of regeneration gas tank.
Give the outer low pressure air heat of supplying with by air blast (100) with heater (80), when heater valve (81) when opening, can be to the low-pressure air after the regeneration gas tank is supplied with heating; After heating finishes, move diametical cooler valve (111) when opening, after cooler (110) cooling, supply with regeneration gas tank (20) by air blast (100) compressed and supplied air with heater valve (81); Be contained in the air that heat of heating and dehumidification agent of regeneration gas tank (20) in the utilization, after second cooler (120) cooled off again, continuation circulated under the effect of air blast (100).What more than introduce is the element that increases newly.
In above-mentioned, the outlet place that discharges air through regeneration gas tank (20) is equipped with by-pass valve control (PV1, PV2), in the time of will heating by the extraneous air of air blast (100), valve (PV2) is opened and is implemented discharging, during cooling, in order to realize circulating to air blast (100), (PV1, that is opening in PV2) will close valve.Valve (PV1) is connected with muffler (60), valve (PV2) control steam vent (PN).The extraneous air inlet port of air blast (100) is equipped with filter (101) and inhaling valve (102) successively.Supply with cooler (120) from the regeneration air that regeneration gas tank (20) flows out through air pressure valve (32), get back to air blast (100) through the regeneration air of cooler (120) by air pressure valve (103) and realize circulation.The open and close action of air pressure valve (30,33) is just in time opposite, thereby has realized containing the normal inflow of the air (WA) of moisture.Air pressure valve (31,32) and air pressure valve (30,33) bridge-type connect, and the open and close action also is just in time opposite, regeneration air can be discharged to the outside, and these two valve sets have constituted and enter and exit valve system (D1).Pneumatic stopping valve (70,71,72,73) also is to connect with bridge-type, and the outlet of dehumidifying gas tank (10) connects valve (70), and dry air (DA) is discharged through this valve.The hot-air supply that adds of regeneration gas tank (20) is controlled by air pressure valve (73).Gas from regeneration gas tank (20) to dehumidifying gas tank (10), from dehumidifying gas tank (10) when regeneration gas tank (20) flows, valve (70,73) is to transfer off status to from opening state, the open and close state of valve (71,72) is respective opposite with it just in time.
So among the present invention who constitutes, valve (the 1V1 of compression humid air (WA) through opening, 30) bottom of first gas tank of dehumidizer (gas tank (10) promptly dehumidifies) flows into from filling into, and in the process of moving up, become dry air (DA), enter dry engineering phase by valve (70) and connecting pipe.Meanwhile, another second gas tank (gas tank (20) of promptly regenerating) that is filled with dehumidizer enters the heating engineering phase.In this heating engineering, air blast starts, and suction inlet valve (102), heater valve (81) and valve (73,72, PV2) open, valve (102,111, PV1) close.Thereupon, extraneous air sucks the low-pressure air (0.1～0.3kg/cm of discharge by filter (101) and suction inlet valve (102)
2) by heater valve (81) under the heating of the heater (81) that starts simultaneously with air blast, reach predefined temperature, pass through the top inflow of valve (73) again from second gas tank (gas tank (20) of promptly regenerating), in the flow process of bottom, dehumidizer is played heat effect, and the moisture of separating that is heated from dehumidizer is discharged in the atmosphere by valve (32) and through valve (PV2) and tap (PN).The state of discharging air this moment is the humid air that keeps uniform temperature, be discharged in the atmosphere after, in the quite a while, carry out heat exchange with extraneous air, the moisture in the humid air of discharge is separated.The time length of this heating engineering is decided by time controller or the setting in advance of temperature controller that be arranged on outlet.
After finishing, the heating engineering will enter the cooling engineering phase.As shown in Figure 4, after dry engineering in first gas tank (gas tank (10) promptly dehumidifies) and the heating engineering in second gas tank (gas tank (20) of promptly regenerating) finish, promptly entered cooling stage.In this stage, air blast (100) is in starting state always, the power supply of steam or heater (80) is cut off, inhaling valve (102), heater valve (81), muffler and discharge valve (PV1, PV2) close simultaneously, valve (103), cooler valve (111) are opened, at this moment, be filled in the air in the cooling system, under the continuous action of air blast (100), circulate; The cooling of the dehumidizer that heats in order to heat in the engineering, the air that will come out after second cooler (120) will be heated cools off, and under the secondary action again of air blast (100), continues circulation; First cooler (110) will be compressed into low-pressure air (0.1～0.3kg/cm in air blast (100)
2) time heat of compression cooling after, continuity cold air is supplied to second gas tank, the gas tank of promptly regenerating (20).The time length of this cooling engineering also is to be regulated and control by time controller and the setting in advance of temperature controller that is arranged on the outlet place.This cooling engineering is brought into play high dehumidifying efficiency to the dehumidizer with the low more characteristic of the high more dehumidification rate of temperature and is very important in the dry engineering of the next one.
What carry out after the cooling engineering finishes is all to press engineering, as shown in Figure 5.When air blast (100) starts, inhaling valve (102) is opened, under cooler valve (111) and valve (32) closed condition, open valve (EV), make a part of compression drying air enter second gas tank by valve (73), promptly regenerate in the gas tank (20), pressure is wherein slowly risen,, all press to be completed into when rising to when identical with pressure in the gas tank that dehumidifies (10).Humid air flows into valve (33,72,71) and opens, and valve (30,32,70,73) is closed, and humid air flows into from the bottom of regeneration gas tank (20), moves to top.This process is exactly that gas tank switches.
Discharge after gas tank switches, as shown in Figure 6.After gas tank switches, open than the valve (PV1) that valve (PV2) is little, the compressed air that is filled in first gas tank (gas tank (10) promptly dehumidifies) is discharged in extraneous air inchmeal by muffler (60), and the pressure in dehumidifying gas tank (10) drops to 0kg/cm
2Gas tank switches also just have been finished.
First gas tank as described above (gas tank (10) promptly dehumidifies) is to dry engineering, second gas tank (gas tank (20) of the promptly regenerating) handoff procedure to dry engineering, (the heating of the reengineer of dehumidifying gas tank (10), cooling) reengineer with the regeneration gas tank (20) that had moved moves in the same way, these actions are according to the preestablishing of time controller, can be continuously, carry out repeatedly.
The present invention (the air blast regeneration air of the outer dress of heater is circulating) who adopts above-mentioned identical process and basic mode are at the comparative result of the consumption of aspects such as regeneration air, heater, air blast and cooling and expense aspect as shown in Figure 7.As can be seen from Figure 7, the present invention, promptly the expense of the air blast circulation heated type of the outer dress of heater is minimum, is economic way.This is because the mode that the recirculation of removal moisture drying air of the present invention takes extraneous air to import in the low pressure mode, institute's calorific requirement is few during heating, and not merely heating, reinstated other cooling circuit during cooling, the structure of two cooling machine systems had both guaranteed the systemic circulation of participating in directly of extraneous air, guaranteed again to cool off under the condition of air aridity in the maintenance system, reduced energy resource consumption.
Claims (2)
1. device that utilizes air blast to make regeneration air circulation, compressed air drying, it is characterized in that, comprise: two dehumidifying and the gas tank (10,20) of regenerating, the moisture removal in the air that contains moisture (WA) that it will pass through internally makes it change dry air (DA) into; And air pressure valve (30,33), the air that contains moisture (WA) selectivity that it will flow into from the outside is supplied with to left and right dehumidifying and the regeneration gas tank (10,20) of being placed in; And wherein cancelled utilize extraneous air heater via heating that will be by air blast (100) and that supply with to regeneration gas tank (20) through cooling, in the circular regeneration formula air dry-set, through the feeding pipe of the dried compressed-air actuated part of dehumidifying gas tank to the supply of regeneration gas tank;
Wherein, give the outer low pressure air heat of supplying with by air blast (100) with heater (80), when heater valve (81) when opening, can be to the low-pressure air after the regeneration gas tank is supplied with heating; After heating finishes, move diametical cooler valve (111) when opening, after cooler (110) cooling, supply with regeneration gas tank (20) by air blast (100) compressed and supplied air with heater valve (81); Under heating, in be contained in moisture in the heating and dehumidification agent in regeneration gas tank (20) and be stripped from fully and be discharged in the atmosphere, second cooler (120) with the dry air cooling after, under the effect of air blast (100), continue to circulate.
2. the device that utilizes air blast to make regeneration air circulation, compressed air drying as claimed in claim 1, it is characterized in that, be provided with the by-pass valve control (PV1 whether control discharges through regeneration gas tank (20) to the outlet place that the external world discharges air, PV2), in the time will heating by the extraneous air of air blast supply, (PV1 PV2) opens valve, and air is discharged; During cooling, (PV1 PV2) closes valve, and air is circulated under the effect of air blast.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101155960A CN100446842C (en) | 2005-11-07 | 2005-11-07 | Apparatus for circulating regenerated air and drying compressed air by use of fan |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101155960A CN100446842C (en) | 2005-11-07 | 2005-11-07 | Apparatus for circulating regenerated air and drying compressed air by use of fan |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1962030A true CN1962030A (en) | 2007-05-16 |
| CN100446842C CN100446842C (en) | 2008-12-31 |
Family
ID=38081359
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005101155960A Active CN100446842C (en) | 2005-11-07 | 2005-11-07 | Apparatus for circulating regenerated air and drying compressed air by use of fan |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100446842C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105485763A (en) * | 2015-11-17 | 2016-04-13 | 袁一军 | Dehumidification method and system |
| CN111122278A (en) * | 2018-10-31 | 2020-05-08 | 株式会社Hctm | Particle measurement system |
| CN113727893A (en) * | 2019-02-25 | 2021-11-30 | 纳博特斯克汽车零部件有限公司 | Air supply system, control method for air supply system, and control program for air supply system |
| EP4324546A1 (en) * | 2020-01-02 | 2024-02-21 | Atlas Copco Airpower, naamloze vennootschap | Drying device and method for drying compressed gas |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3847578A (en) * | 1967-03-29 | 1974-11-12 | C Munters | Apparatus for drying compressed air |
| JPS56152726A (en) * | 1980-04-28 | 1981-11-26 | Ishikawajima Harima Heavy Ind Co Ltd | Dryer device for compressor |
| CN1027737C (en) * | 1986-02-14 | 1995-03-01 | 气动技术有限公司 | Gas drying apparatus |
| CN2205240Y (en) * | 1994-06-12 | 1995-08-16 | 阎荣风 | Waste heat directly heating and regenerating device of gas adsorption drying agent |
| CN2225293Y (en) * | 1995-04-25 | 1996-04-24 | 蒋宗传 | Energy saving micro thermal regenerating air drier |
-
2005
- 2005-11-07 CN CNB2005101155960A patent/CN100446842C/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105485763A (en) * | 2015-11-17 | 2016-04-13 | 袁一军 | Dehumidification method and system |
| CN111122278A (en) * | 2018-10-31 | 2020-05-08 | 株式会社Hctm | Particle measurement system |
| CN113727893A (en) * | 2019-02-25 | 2021-11-30 | 纳博特斯克汽车零部件有限公司 | Air supply system, control method for air supply system, and control program for air supply system |
| EP4324546A1 (en) * | 2020-01-02 | 2024-02-21 | Atlas Copco Airpower, naamloze vennootschap | Drying device and method for drying compressed gas |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100446842C (en) | 2008-12-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106679002B (en) | A kind of dehumidification by condensation and the compound Fresh air handing device and method of solution dehumidification | |
| KR100609840B1 (en) | Compressed air dryer for recycling heat by blower | |
| CN108626816A (en) | A kind of humidity step processing unit of low moisture environments | |
| CN100446842C (en) | Apparatus for circulating regenerated air and drying compressed air by use of fan | |
| JP2004531377A (en) | Method for regenerating moisture-loaded process air and apparatus for implementing the method | |
| CN108644933A (en) | The working method of multistage recuperation of heat Fresh air handing device for central air conditioner system | |
| KR20170000934A (en) | Purge and non-purge type compressed air dryer that recycling tank using dryed and compressed air in cooling process and compressed air drying method | |
| CN201028928Y (en) | Indoor dehumidifier | |
| CN208154958U (en) | A kind of heat pump drying equipment | |
| CN104789709A (en) | Low-energy-consumption drying device | |
| CN115999333B (en) | Compressed air dryer and adsorbent regeneration method thereof | |
| CN209165623U (en) | A kind of energy-saving Revolving wheel dehumidification apparatus handling hot environment | |
| CN107062442A (en) | A kind of energy-saving air processing system | |
| CN106537048B (en) | Desiccant cooling equipment | |
| KR101728241B1 (en) | compressed air dryer that recycling the compress air in cooling process and compressed air drying method | |
| CN210638201U (en) | Solution dehumidification unit | |
| CN212426487U (en) | Mould-proof heat pump clothes dryer | |
| CN211739813U (en) | Dehumidifying and drying energy-saving system | |
| CN209857546U (en) | Energy-conserving drying equipment dehumidifies | |
| CN106813349A (en) | A kind of energy-saving air processing system with secondary return air | |
| KR200405286Y1 (en) | Compressed air dryer for recycling heat by blower | |
| CN207031233U (en) | A kind of sludge drying device | |
| CN106801969A (en) | A kind of energy-saving fresh air system | |
| CN110145830A (en) | A kind of wet independent process integration apparatus of air heat using solution dehumidification | |
| CN206609076U (en) | A kind of energy-saving air processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |