CN1483505A - Adsorption dehumidifier - Google Patents

Adsorption dehumidifier Download PDF

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Publication number
CN1483505A
CN1483505A CNA03152396XA CN03152396A CN1483505A CN 1483505 A CN1483505 A CN 1483505A CN A03152396X A CNA03152396X A CN A03152396XA CN 03152396 A CN03152396 A CN 03152396A CN 1483505 A CN1483505 A CN 1483505A
Authority
CN
China
Prior art keywords
chamber
adsorption
desorption
cavity unit
type dehumidifier
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
Application number
CNA03152396XA
Other languages
Chinese (zh)
Other versions
CN1301147C (en
Inventor
川上由基人
一郎
松本真一郎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Seibu Giken Environmental Protection Energy Saving Equipment Changshu Co ltd
Original Assignee
SAIBU GIKEN KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SAIBU GIKEN KK filed Critical SAIBU GIKEN KK
Publication of CN1483505A publication Critical patent/CN1483505A/en
Application granted granted Critical
Publication of CN1301147C publication Critical patent/CN1301147C/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26—Drying gases or vapours
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F24F3/1411—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
    • F24F3/1423—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant with a moving bed of solid desiccants, e.g. a rotary wheel supporting solid desiccants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/06—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00—Devices or apparatus used for air treatment
    • F24F2203/10—Rotary wheel
    • F24F2203/1032—Desiccant wheel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00—Devices or apparatus used for air treatment
    • F24F2203/10—Rotary wheel
    • F24F2203/1068—Rotary wheel comprising one rotor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00—Devices or apparatus used for air treatment
    • F24F2203/10—Rotary wheel
    • F24F2203/1088—Rotary wheel comprising three flow rotor segments
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00—Devices or apparatus used for air treatment
    • F24F2203/10—Rotary wheel
    • F24F2203/1096—Rotary wheel comprising sealing means

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Gases (AREA)

Abstract

To provide an adsorption type dehumidifier which has a very simple structure without the necessity of applying insulation, and is manufactured with high productivity. An adsorption chamber 3 having a plane contacting with the end face of a honeycomb rotor 1 and forming an adsorption zone on the opposite face, and a desorption chamber 4 forming a desorption zone are made in the adsorption type dehumidifier. A pair of chamber units 2 and 14 where the adsorption chamber 3 and the desorption chamber 4 are formed so as to be separated from each other are made, and attached so as to contact with both end faces of the honeycomb rotor 1.

Description

The absorption type dehumidifier
Technical field
The present invention relates to a kind of absorption type dehumidifier, particularly be applicable to the absorption type dehumidifier of the air of the low dew point of supply.
Background technology
Because the absorption type dehumidifier has the air that is more suitable for supplying with low dew point than freezing type dehumidifier, in recent years in the factory that needs the strict control air regime with prevent that the application of food aspect mouldy etc. from having obtained quick popularization.Particularly adopt the absorption type dehumidifier of the cellular rotor that is attached with moisture absorbers such as colloidal silica or zeolite, obtain popularizing widely owing to having the low characteristics of price simple in structure.
Adopt the absorption type dehumidifier of so cellular rotor to have the cavity that is divided into adsorption zone and desorption zone (taking off ゾ one Application) to the cellular rotor of major general, or on this basis the cavity of affix cooling zone again.The example of this cavity can be referring to Japanese Patent Application Publication clear and 58 years No. 119323 communique.
In aforesaid cavity, the air of high temperature flows in desorption zone, and when its heat during to the conduction of cooling zone and adsorption zone, can make flow air temperature decline in the desorption zone, not only cause the waste of the energy, and can make to cooling zone and adsorption zone flow air temperature and rise and the problem that causes absorption property to descend.
For this reason, need have stable on heating heat-barrier material with foaming silicones or glass fibre etc. and coat desorption zone, but production efficiency is low.
Summary of the invention
The object of the present invention is to provide a kind of absorption type dehumidifier, employing is extremely simply constructed and is not needed to apply heat insulation processing, and the production efficiency height.
Above-mentioned purpose of the present invention is achieved in that a kind of absorption type dehumidifier, wherein, be provided with a pair of cavity unit, described cavity unit has and the contacted plane of the end face of cellular rotor, have adsorption chamber that forms adsorption zone and the desorption chamber that forms desorption zone at its opposing face, described adsorption chamber and desorption chamber are to form with separated state respectively, and described a pair of cavity unit is to assemble with the contacted form of each end face of cellular rotor respectively.
Absorption type dehumidifier of the present invention wherein, by having and the fitting tightly of the end face of the plane of the contacted sealed width of end face of cellular rotor and cellular rotor, and guarantees to prevent leakage between each chamber of cavity unit.
Absorption type dehumidifier of the present invention wherein, is only separated the length that deducts the wall thickness of each chamber from sealed width between each chamber of cavity unit.
Absorption type dehumidifier of the present invention, wherein, each cavity unit is integrally formed by foundry goods.
Description of drawings
Fig. 1 is the A-A cutaway view that illustrates among Fig. 2 of embodiment of absorption type dehumidifier of the present invention;
Fig. 2 is the front view that an example of absorption type dehumidifier of the present invention is shown;
Fig. 3 is the stereogram that an example of absorption type dehumidifier of the present invention is shown;
Fig. 4 is the vertical view that an example of absorption type dehumidifier of the present invention is shown;
Fig. 5 is the B-B cutaway view that illustrates among Fig. 2 of embodiment of absorption type dehumidifier of the present invention;
Fig. 6 is the upward view that an example of absorption type dehumidifier of the present invention is shown;
Fig. 7 is the mobile stereogram of air that absorption type dehumidifier of the present invention is shown;
Fig. 8 is the C-C cutaway view that illustrates among Fig. 1 of embodiment of absorption type dehumidifier of the present invention.
Wherein, description of reference numerals is as follows:
1 dehumidifying rotor
2 upper chamber unit,
3 adsorption chambers,
4 desorption chambers,
5 clean rooms,
6 planar portions
7,8,9 air scoops,
10 lower cavity unit,
11 adsorption chambers,
12 desorption chambers
13 clean rooms,
14 planar portions,
15,16,17 air scoops
18,19,20,21,22,23 bolts hole
The specific embodiment
Absorption type dehumidifier of the present invention, be provided with a pair of cavity unit, described cavity unit has and the contacted plane of the end face of cellular rotor, have adsorption chamber that forms adsorption zone and the desorption chamber that forms desorption zone at its opposing face, described adsorption chamber and desorption chamber are to form with separated state respectively, and described a pair of cavity unit is to assemble with the contacted form of each end face of cellular rotor respectively.
Embodiment
Describe absorption type dehumidifier of the present invention below with reference to the accompanying drawings in detail.Fig. 1 is the A-A cutaway view of Fig. 2, and Fig. 3 is the B-B cutaway view of Fig. 2.1 is dehumidifying rotor in Fig. 2, is to form honeycomb shape by inorganic fibre papers such as ceramic papers, and the such hygroscopic agent of colloidal silica or zeolite is attached to and forms on the cellular inorganic fibre paper.And dehumidifying rotor 1 is driven by the geared dynamo (not shown).
The 2nd, the upper chamber unit is for example made by aluminium casting or die casting.Upper chamber unit 2 has adsorption chamber 3, desorption chamber 4 (taking off チ ヤ Application バ one) and clean room 5, promptly with the position, plane 6 of the contacted upper chamber of the end face of dehumidifying rotor 1 unit 2 on form adsorption chamber 3, desorption chamber 4 and clean room 5, as Fig. 1, Fig. 3 and shown in Figure 4, each chamber is separated mutually.
In addition, in adsorption chamber 3, desorption chamber 4 and clean room 5, be respectively arranged with air scoop 7,8,9.
The 10th, the lower cavity unit, this lower cavity unit 10 has the shape with upper chamber unit 2 symmetries, as as the Fig. 6 of bottom view and shown in Figure 5 as B-B cutaway view among Fig. 2, also be provided with adsorption chamber 11, desorption chamber 12 and clean room 13 equally on the planar portions 14 of lower cavity unit 10, each chamber is separated mutually.
As shown in Figure 6, on adsorption chamber 11, be provided with air scoop 15, on desorption chamber 12, be provided with air scoop 16, in clean room 13, be provided with air scoop 17.
Fig. 8 is the C-C cutaway view among Fig. 1.Sealed width W between each district must guarantee that in order to guarantee not blank gas between each district enough width are arranged as can be seen from Figure 8.Owing to have this width W, separate the size consistent with this width so can make between adsorption chamber 3 among Fig. 8 and the clean room 5.Strictly speaking, only separate the length that deducts the wall thickness of each chamber from sealed width W between each chamber.
And in view of the above, the inner face of each chamber is directly towards the lower surface of planar portions 6 as can be known from Fig. 8.Thereby when making the cavity unit, the situation of foundry goods is next in this way can not need inner core, also can easily make by the ejection formation of die casting or synthetic resin.
The adsorption chamber 3 of upper chamber unit 2 is relative to setting across dehumidifying rotor 1 with the adsorption chamber 11 of lower cavity unit 10, and the desorption chamber 4 of upper chamber unit 2 also is relative to setting across dehumidifying rotor 1 with the desorption chamber 12 of lower cavity unit 10.And the clean room 13 of the clean room 5 of upper chamber unit 2 and lower cavity unit 10 also is relative to setting across dehumidifying rotor 1.
The place, 3 summits of the planar portions 6 of upper chamber unit 2 is formed with bolt hole 18,19 and 20 respectively, and the place, 3 summits of the planar portions 14 of lower cavity unit 10 is formed with bolt hole 21,22 and 23 respectively.Thereby penetrate bolt hole 18 and bolt hole 22 and fix with a root stay bolt (not shown), same, bolt hole 20 and bolt hole 23 and bolt hole 19 and bolt hole 21 also penetrate and fix with a stay bolt respectively.Become between upper chamber unit 2 and lower cavity unit 10 clamping thus and the state of dehumidifying rotor 1.The pressure of this dehumidifying rotor 1 of clamping can rotate freely with dehumidifying rotor 1 and the planar portions 6 of cavity unit, upper and lower part and 14 and the end face of dehumidifying rotor 1 between the state that can not leak air be as the criterion.
Action to the absorption type dehumidifier of the present invention of above structure describes below.Make dehumidifying rotor 1 rotation by driving belt (not shown) etc., simultaneously processed air flows in the adsorption chamber 3 of upper chamber unit 2 from air scoop 7.So as shown in Figure 7, processed air is by dehumidifying rotor 1, enters adsorption chamber 11 after becoming dry air, discharges from air scoop 15.At air scoop 15 pipeline etc. is installed, thereby carries dry air to the activity of dry air.
When processed air passed through dehumidifying rotor 1, processed airborne moisture was produced heat of adsorption by the adsorbents adsorb in the dehumidifying rotor 1.The temperature of the dry air that passes through from the adsorption chamber 11 of lower cavity unit 10 raises thus.As shown in Figure 5, because adsorption chamber 11 is separated with clean room 13, the heat of adsorption chamber 11 can not conduct to clean room 13.
In order to remove moisture adsorbed in the dehumidifying rotor 1, need in the desorption chamber 12 of lower cavity unit 10, carry about 100 ℃～150 ℃ hot blast.So, this hot blast is by in the process of dehumidifying rotor 1, is adsorbed on moisture in the dehumidifying rotor 1 by desorb, and the air of high humility is discharged by the desorption chamber 4 of upper chamber unit 2.
So, the air of being sent here by the clean room 5 of upper chamber unit 2 is by dehumidifying rotor 1.When the dehumidifying rotor 1, be cooled owing to separating the dehumidifying rotor 1 that suck is raised temperature, the air that enters the clean room 13 of lower cavity unit 10 is simultaneously heated up.
Heated up owing to enter the air of clean room 13, the air of Pai Chuing heats with the heater (not shown) more thus, and sends into desorption chamber 12, thereby can carry out the recovery of energy.
More than be all be provided with in upper chamber unit and the lower cavity unit adsorption chamber, desorption chamber and clean room example, can in upper chamber unit and lower cavity unit, not establish the clean room yet, only establish adsorption chamber and desorption chamber.
Because of the aforesaid formation of absorption type dehumidifier of the present invention, adsorption chamber, desorption chamber and clean room are independent separately in upper chamber unit and the lower cavity unit, separate mutually, and the conduction of heat can not take place between each chamber, therefore do not need to apply heat insulation processing.
And because adsorption chamber, desorption chamber and clean room are independent separately, separate mutually, thereby can guarantee that enough big sealed width W is arranged between each chamber, can fully guarantee sealing effectiveness.
And because absorption type dehumidifier of the present invention, making contacts with adsorber rotor and air-tightness is good planar portions, adsorption chamber, desorption chamber and clean room that can one, thus utilize the moulding of foundry goods or die casting or synthetic resin easily to produce in batches.

Claims (4)

1, a kind of absorption type dehumidifier, it is characterized in that, be provided with a pair of cavity unit, described cavity unit has and the contacted plane of the end face of cellular rotor, have adsorption chamber that forms adsorption zone and the desorption chamber that forms desorption zone at its opposing face, described adsorption chamber and desorption chamber are to form with separated state respectively, and described a pair of cavity unit is to assemble with the contacted form of each end face of cellular rotor respectively.
2, absorption type dehumidifier as claimed in claim 1 is characterized in that, by having and the fitting tightly of the end face of the plane of the contacted sealed width of end face of cellular rotor and cellular rotor, and guarantees to prevent leakage between each chamber of cavity unit.
3, absorption type dehumidifier as claimed in claim 2 is characterized in that, only separates the length that deducts the wall thickness of each chamber from sealed width between each chamber of cavity unit.
4, absorption type dehumidifier as claimed in claim 1 is characterized in that, each cavity unit is integrally formed by foundry goods.
CNB03152396XA 2002-07-31 2003-07-31 Adsorption dehumidifier Expired - Lifetime CN1301147C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2002222711A JP3827155B2 (en) 2002-07-31 2002-07-31 Adsorption dehumidifier
JP2002222711 2002-07-31

Publications (2)

Publication Number Publication Date
CN1483505A true CN1483505A (en) 2004-03-24
CN1301147C CN1301147C (en) 2007-02-21

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CNB03152396XA Expired - Lifetime CN1301147C (en) 2002-07-31 2003-07-31 Adsorption dehumidifier

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JP (1) JP3827155B2 (en)
KR (1) KR101004659B1 (en)
CN (1) CN1301147C (en)
TW (1) TW200401661A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106731478A (en) * 2015-11-24 2017-05-31 杰智环境科技股份有限公司 Horizontal runner and fluid purification processing system
CN107202463A (en) * 2016-03-18 2017-09-26 青岛海尔智能技术研发有限公司 The control method of rotary-type drier and refrigeration plant and refrigeration plant

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103140273B (en) * 2010-01-22 2016-06-08 新加坡国立大学 Moisture trap and dehumanization method
JP5453490B2 (en) 2011-12-21 2014-03-26 財團法人工業技術研究院 Dehumidification and release device and system
BR112018070208B1 (en) 2016-03-31 2023-01-31 Inventys Thermal Technologies Inc ADSORTIVE GAS SEPARATOR
KR102136290B1 (en) 2017-11-28 2020-08-26 주식회사 엔바이온 Low Energy Consumption Concentrating Rotor For Treating Malodor And VOCs Gases, And Treating System Comprising The Same

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SE429301B (en) * 1981-12-30 1983-08-29 Munters Ab Carl SET ON DRYING A GAS AND APPLIANCE FOR PERFORMING THE SET
JPH0245126U (en) * 1988-09-22 1990-03-28
JPH04284812A (en) * 1991-03-12 1992-10-09 Sumitomo Seika Chem Co Ltd Method for enriching oxygen in air and device therefor
JP2750996B2 (en) * 1993-09-08 1998-05-18 ニチアス株式会社 Organic solvent vapor adsorption device
JPH08141346A (en) * 1994-11-17 1996-06-04 Mitsubishi Heavy Ind Ltd Rotary gas separation device using pressure swing adsorption method
JPH11137944A (en) * 1997-11-05 1999-05-25 Toho Kako Kensetsu Kk Gas treating device
JP2001179034A (en) * 1999-12-22 2001-07-03 Flair Japan Inc Drying equipment for air or gas

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106731478A (en) * 2015-11-24 2017-05-31 杰智环境科技股份有限公司 Horizontal runner and fluid purification processing system
CN107202463A (en) * 2016-03-18 2017-09-26 青岛海尔智能技术研发有限公司 The control method of rotary-type drier and refrigeration plant and refrigeration plant

Also Published As

Publication number Publication date
CN1301147C (en) 2007-02-21
TW200401661A (en) 2004-02-01
KR101004659B1 (en) 2011-01-04
KR20040012565A (en) 2004-02-11
JP2004057994A (en) 2004-02-26
TWI296942B (en) 2008-05-21
JP3827155B2 (en) 2006-09-27

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Effective date of registration: 20160715

Address after: 215500 Jiangsu Province, Southeast of Changshu Economic Development Zone No. 8 Jin Lin Lu

Patentee after: SEIBU GIKEN ENVIRONMENTAL PROTECTION ENERGY SAVING EQUIPMENT (CHANGSHU) CO.,LTD.

Address before: Shiga County, Fukuoka, Japan

Patentee before: KABUSHIKIGAISYA SEIBU-GIKEN

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20070221