JPS60238119A - Air dehumidification apparatus - Google Patents
Air dehumidification apparatusInfo
- Publication number
- JPS60238119A JPS60238119A JP59094111A JP9411184A JPS60238119A JP S60238119 A JPS60238119 A JP S60238119A JP 59094111 A JP59094111 A JP 59094111A JP 9411184 A JP9411184 A JP 9411184A JP S60238119 A JPS60238119 A JP S60238119A
- Authority
- JP
- Japan
- Prior art keywords
- air
- water vapor
- chamber
- pressurized
- dehumidified
- 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.)
- Pending
Links
Landscapes
- Central Air Conditioning (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Drying Of Gases (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野1
本発明は、空調用の除湿空気や、工業炉用、下水汚泥等
の低温乾燥用の脱湿空気を生成する場合に用いられる装
置で、詳しくは、除湿対象空気を加圧して該空気中の水
蒸気分圧を高める装置と、水蒸気を選択的に透過可能な
高分子膜で仕切られた2つの室の一方に前記加圧装置か
らの加圧空気を供給することにより、画室間での水蒸気
分圧差をもって加圧空気中の水蒸気を高分子膜を通して
他方の室に移行させて、加圧空気を除湿する水蒸気透過
装置とを設けである空気の除湿装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field 1] The present invention is an apparatus used to generate dehumidified air for air conditioning, industrial furnaces, and low-temperature drying of sewage sludge, etc. Specifically, it includes a device that pressurizes the air to be dehumidified to increase the partial pressure of water vapor in the air, and a device that applies pressure from the pressurization device to one of two chambers partitioned by a polymer membrane that is selectively permeable to water vapor. By supplying pressurized air, the water vapor in the pressurized air is transferred to the other chamber through the polymer membrane using the water vapor partial pressure difference between the compartments, and a water vapor permeation device is installed to dehumidify the pressurized air. The present invention relates to a dehumidifying device.
[従来技術]
従来のかかる空気の除湿装置としては、木出願人が先に
提案した特@t@58−1931003号を挙げること
ができる。 これは、前記水蒸気透過装置の一方に室に
除湿対象空気を加圧して供給し、他方の室に常圧空気を
供給することによって、画室間での水蒸気分圧差をもっ
て除湿対象空気中の水蒸気を他方の室に移行させて、除
湿対象空気を除湿する点を要旨とするものである。[Prior Art] As a conventional air dehumidifying device, there can be mentioned Toku@t@58-1931003, which was previously proposed by the same applicant. By supplying pressurized air to be dehumidified to one chamber of the water vapor permeation device and supplying normal pressure air to the other chamber, water vapor in the air to be dehumidified can be removed by using a water vapor partial pressure difference between the compartments. The gist is to move the air to the other chamber and dehumidify the air to be dehumidified.
しかし乍ら、前記の従来装置によるときは、次のような
問題があった。However, the conventional apparatus described above has the following problems.
つまり、水蒸気が高分子膜を透過する速度Q(cc/5
ec)は、水蒸気の透過係数をP(cc−躯一・sec
−amig)、一方の室の水蒸気分圧をP((aml
g入他方の室の水蒸気分圧をFuming)、高分子膜
の表面積をA(−人高分子膜の厚をZ(−)とした場合
!
で示され、これからも明らかなように、空気を高除湿す
るには、画室間での水蒸気分圧の差(P、Pt)を大き
くする必要がある。 他方、従来装置のように、他方の
室に常圧空気を供給する場合には、水蒸気分圧差を大き
くする際、一方の室に供給する除湿対象空気の水蒸気分
圧を上げなければならない。 従って、従来装置による
ときは、除湿対象空気を高除湿する場合、除湿対象空気
の水蒸気分圧を上げる上で、除湿対象空気を高加圧する
要があって、加圧装置の大型化、それに伴なうイニ多ヤ
ル及びランニングコストの高騰化を招来するのである。In other words, the rate of water vapor permeation through the polymer membrane Q (cc/5
ec) is the water vapor permeability coefficient P(cc-body unit・sec
-amig), and the water vapor partial pressure in one chamber is P((aml
The water vapor partial pressure in the other chamber is Fuming), and the surface area of the polymer membrane is A (-), and the thickness of the polymer membrane is Z(-)!.As is clear from this, the air In order to achieve high dehumidification, it is necessary to increase the difference in water vapor partial pressure (P, Pt) between the compartments.On the other hand, when normal pressure air is supplied to the other compartment as in conventional equipment, water vapor When increasing the partial pressure difference, it is necessary to increase the water vapor partial pressure of the air to be dehumidified that is supplied to one chamber. Therefore, when using conventional equipment, when dehumidifying the air to a high degree, the partial pressure of water vapor in the air to be dehumidified must be increased. In order to achieve this, it is necessary to highly pressurize the air to be dehumidified, which leads to an increase in the size of the pressurizing device and an accompanying increase in initial and running costs.
本発明は、かかる従来問題を解消しようとする点に目的
を有する。The present invention has an object to solve such conventional problems.
本発明による空気の除湿装置の特徴構成は、前記一方の
室からの除湿空気で、かつ、常圧に減圧された空気の一
部を前記他方の室に供給する供給路を設けである点にあ
り、それによる作用効果は次の通りである。A characteristic configuration of the air dehumidifier according to the present invention is that a supply path is provided for supplying part of the dehumidified air from the one chamber and the air reduced to normal pressure to the other chamber. The effects of this are as follows.
つまり、他方の室に対して、一方の室からの除湿空気で
、かつ、常圧忙減圧されていて、水蒸気分圧が非常に小
さい空気を供給して、一方の室に供給され九加圧空気を
除湿するから、一方の室に供給する除湿対象空気に対す
る加圧力を小さくし乍らも、画室間での水蒸気分圧差を
大きくして、除湿対象空気の水蒸気分圧を十分に小さく
することができる。In other words, dehumidified air from one chamber, which has been depressurized to normal pressure and has a very low partial pressure of water vapor, is supplied to the other chamber. Since the air is dehumidified, the pressure applied to the air to be dehumidified supplied to one chamber is reduced, while the water vapor partial pressure difference between the compartments is increased to sufficiently reduce the water vapor partial pressure of the air to be dehumidified. I can do it.
従って、本発明によれば、除湿対象空気を十分に除湿で
き乍らも、加圧装置の小型化とコストダクン及びランニ
ングコストの低減下を達成で自るに至った。Therefore, according to the present invention, while the air to be dehumidified can be sufficiently dehumidified, the pressurizing device can be made smaller and the cost and running costs can be reduced.
4M1図に示すよう忙、湿度が調節され九空気を生成す
る装置を構成するに、空気(al)を加圧して該空気(
Ill)中の涼蒸気分圧を高める加圧装置用と、これ力
為らの加圧空気(lρを冷却する装置Illと、水蒸気
を選択的に透過可能な高分子膜(3a)で仕切られ7’
j7つの室(3A)、(3B)の一方(3A)に前記冷
却装置(2)からの加圧冷却空気(aρを供給すること
により、画室(3A)、(3B)闇での水蒸気分圧差を
もって加圧冷却空気(a、)中の水蒸気を他方の室(3
B)に高分子膜(3a)を通して移行させて、加圧冷却
空気(−を除湿する水蒸気透過装置(3)と、これから
の除湿空気(a4)を常圧忙減圧する減圧弁(4)と、
減圧空気(as)を加湿して空気の湿度を調節する加湿
装置flslとを設ける。As shown in Figure 4M1, a device that generates air with controlled humidity is constructed by pressurizing air (al) and
A pressurizing device for increasing the partial pressure of cool steam in Ill) and a device Ill for cooling the pressurized air (lρ) are separated by a polymer membrane (3a) that is selectively permeable to water vapor. 7'
By supplying pressurized cooling air (aρ) from the cooling device (2) to one (3A) of the seven chambers (3A) and (3B), the water vapor partial pressure difference in the darkness between compartments (3A) and (3B) is reduced. the water vapor in the pressurized cooling air (a) to the other chamber (3).
A water vapor permeation device (3) that dehumidifies pressurized cooling air (-) by transferring it to B) through a polymer membrane (3a), and a pressure reducing valve (4) that depressurizes the dehumidified air (a4) to normal pressure. ,
A humidifier flsl is provided for humidifying reduced pressure air (AS) to adjust the humidity of the air.
而して、前記減圧空気(aρの一部を前記水蒸気透過装
置(S)における他方の室(3B)K供給する供給路(
6)を設けて、他方の室(3B)K常圧空気を供給する
場合よりも、両室(3A)、(3B)間での水蒸気分圧
を大とすべく構成する。A supply path (
6) is provided so that the water vapor partial pressure between the two chambers (3A) and (3B) is larger than that in the case where normal pressure air is supplied to the other chamber (3B).
前記水蒸気透過装置(3)は、加圧冷却空気(−と減圧
空気(!III)とを向流状態で高分子膜(3a)K沿
って流動させるべく構成されている。The water vapor permeation device (3) is configured to flow pressurized cooling air (-) and decompressed air (!III) along the polymer membrane (3a) K in a countercurrent state.
第8図に示すように、前記水蒸気透過装置(3)を加圧
装置用からの加圧空気を除湿対象とする状flK設け、
前記冷却装置(2)を、減圧弁(4)で減手続補正書
特許庁長官殿 昭和” ql Q48日1、事件の表示
2、発明の名称
空気の除混装置
3、補正をする者
事件との関係 特 許 出願人
4話 大阪(061374−1221■氏 名 (80
97) 弁理士 北 村 修5、補正命令の11付
7、 補正の内容
特許請求の範囲を別紙の通り訂正します。As shown in FIG. 8, the water vapor permeation device (3) is installed in a manner that dehumidifies pressurized air from a pressurization device,
The said cooling device (2) is reduced by using the pressure reducing valve (4). Relationship Patent Applicant Episode 4 Osaka (061374-1221) Name (80
97) Patent attorney Osamu Kitamura 5, Attachment 11, Attachment 7 of the amendment order, Contents of the amendment The scope of the patent claims will be corrected as shown in the attached sheet.
& 添付書類の目録
訂正後の特許請求の範囲を記載し九
書面 1通
代理人 弁理士 北 村 修
特許請求の範囲
■ 除眼対象空気を加圧して該空気中の水蒸気分圧を高
める装置1111と、水蒸気を選択的に透過可能な高分
子膜(8a)で仕切られ几コつの室(8A)、(8B)
の一方(3A)に前記加圧袋@ illからの加圧空気
を供給することにより、画室(8A)、(8B)間での
水蒸気分圧差をもって加圧空気中の水蒸気を高分子膜(
as)k通して他方の室(8B)K移行させて、加圧空
気を除湿する水蒸気透過装置(3)とを設けである空気
の除湿装置であって、前記一方の室(8A)からの除湿
空気で、かつ、常圧に減圧さnた空気の一部を前記他方
の室(8B)に供給する供給W!1161 k設けであ
る空気の除湿装置。& Nine documents stating the scope of patent claims after the correction of the list of attached documents 1 agent Patent attorney Osamu Kitamura Scope of patent claims ■ Device 1111 that pressurizes the air to be removed for eye removal and increases the partial pressure of water vapor in the air and tightly spaced chambers (8A) and (8B) partitioned by a polymer membrane (8a) that is selectively permeable to water vapor.
By supplying pressurized air from the pressurized bag @ ill to one side (3A) of the compartments (8A) and (8B), water vapor in the pressurized air is transferred to the polymer membrane (
as) a water vapor permeation device (3) for dehumidifying the pressurized air by moving the pressurized air through the other chamber (8B)K, the air dehumidifying device comprising: Supply W of dehumidified air and part of the air reduced to normal pressure to the other chamber (8B)! 1161K air dehumidifier.
■ 前記水蒸気透過装置(3)が、加圧空気と減圧空気
とを向流状態で高分子膜(8a)に沿って流動させるも
のである特許請求の範囲第0項に記載の空気の除湿装置
。(2) The air dehumidification device according to claim 0, wherein the water vapor permeation device (3) causes pressurized air and decompressed air to flow along the polymer membrane (8a) in a countercurrent state. .
■ 前記水蒸気透過装置(3)の一方の室(8A)K供
給さnる加圧空気が、加圧装置k illで加圧された
後、冷却さnた空気である特許請求の範囲第■項又ti
t第■項に記載の空気の除湿装置。(2) The pressurized air supplied to one chamber (8A) of the water vapor permeation device (3) is air that has been cooled after being pressurized by the pressurizing device (2). term ti
t. The air dehumidification device described in item (2).
Claims (1)
める装置(11と、水蒸気を選択的に透過可能な高分子
膜(3畠)で仕切られた2つの室(3A)、(3B)の
一方(3A)4C前記加圧装置山からの加圧空気を供給
することにより、両室(3A)、(3B)間での水蒸気
分圧差をもって加圧空気中の水蒸気を高分子膜(3a)
を通して他方の室(3B)K移行させて、加圧空気を除
湿する水蒸気透過袋fl(81とを設けである空気の除
湿装置であって、前記一方の室(3A)からの除湿空気
で、かつ、常圧に減圧された空気の一部を前記他方の室
(3B)に供給する供給路(6)を設けである空気の除
湿装置。 ■ 前記水蒸気透過装置(3)が、加圧空気と減圧空気
とを向流状態で高分子膜(3a)に沿って流動させるも
のである特許請求の範囲第0項に記載の空気の除湿装置
。 ■ 前記水蒸気透過装置(3)の一方の室(3A)に供
給される加圧空気が、加圧装置illで加圧された後、
冷却された空気である特許請求の範囲第0項又は第0項
に記載の空気の除湿装置。[Claims] ■ A device (11) that pressurizes the air to be dehumidified to increase the partial pressure of water vapor in the air, and two chambers separated by a polymer membrane (3 halves) that can selectively permeate water vapor. By supplying pressurized air from one of the chambers (3A) and (3B) (3A) and 4C, the water vapor partial pressure difference between both chambers (3A) and (3B) is used to increase the pressure in the pressurized air. Water vapor is transferred to a polymer membrane (3a)
An air dehumidifier is provided with a water vapor permeable bag fl (81) for dehumidifying pressurized air by transferring the pressurized air to the other chamber (3B) K through the dehumidified air from the one chamber (3A), and an air dehumidifier provided with a supply path (6) for supplying a part of the air reduced to normal pressure to the other chamber (3B). ■ The water vapor permeation device (3) supplies pressurized air The air dehumidification device according to claim 0, which causes the and decompressed air to flow in a countercurrent state along the polymer membrane (3a). ■ One chamber of the water vapor permeation device (3). After the pressurized air supplied to (3A) is pressurized by the pressurizing device ill,
The air dehumidification device according to claim 0 or 0, which is cooled air.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59094111A JPS60238119A (en) | 1984-05-10 | 1984-05-10 | Air dehumidification apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59094111A JPS60238119A (en) | 1984-05-10 | 1984-05-10 | Air dehumidification apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60238119A true JPS60238119A (en) | 1985-11-27 |
Family
ID=14101319
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59094111A Pending JPS60238119A (en) | 1984-05-10 | 1984-05-10 | Air dehumidification apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60238119A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4875908A (en) * | 1988-01-27 | 1989-10-24 | Hiroyasu Kikukawa | Process for selectively separating gaseous mixtures containing water vapor |
US4909810A (en) * | 1988-01-26 | 1990-03-20 | Asahi Glass Company Ltd. | Vapor permselective membrane |
US5118327A (en) * | 1989-10-05 | 1992-06-02 | Andrew Corporation | Dehumidifier for supplying gas having controlled dew point |
US5205842A (en) * | 1992-02-13 | 1993-04-27 | Praxair Technology, Inc. | Two stage membrane dryer |
US5681368A (en) * | 1995-07-05 | 1997-10-28 | Andrew Corporation | Dehumidifier system using membrane cartridge |
US5762690A (en) * | 1992-11-25 | 1998-06-09 | Andrew Corporation | Dehumidifier for supplying air using variable flow rate and variable pressure in a membrane dryer |
CN107036192A (en) * | 2017-04-20 | 2017-08-11 | 东莞理工学院 | A high-efficiency negative pressure membrane dehumidifier and high-efficiency dehumidification system |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56101534A (en) * | 1980-01-18 | 1981-08-14 | Horiba Ltd | Dehumidifier in gas analyzing device |
-
1984
- 1984-05-10 JP JP59094111A patent/JPS60238119A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56101534A (en) * | 1980-01-18 | 1981-08-14 | Horiba Ltd | Dehumidifier in gas analyzing device |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4909810A (en) * | 1988-01-26 | 1990-03-20 | Asahi Glass Company Ltd. | Vapor permselective membrane |
US4875908A (en) * | 1988-01-27 | 1989-10-24 | Hiroyasu Kikukawa | Process for selectively separating gaseous mixtures containing water vapor |
US5118327A (en) * | 1989-10-05 | 1992-06-02 | Andrew Corporation | Dehumidifier for supplying gas having controlled dew point |
US5205842A (en) * | 1992-02-13 | 1993-04-27 | Praxair Technology, Inc. | Two stage membrane dryer |
US5762690A (en) * | 1992-11-25 | 1998-06-09 | Andrew Corporation | Dehumidifier for supplying air using variable flow rate and variable pressure in a membrane dryer |
US5885329A (en) * | 1992-11-25 | 1999-03-23 | Andrew Corporation | Dehumidifier for supplying air using variable flow rate and variable pressure in a membrane dryer |
US5681368A (en) * | 1995-07-05 | 1997-10-28 | Andrew Corporation | Dehumidifier system using membrane cartridge |
CN107036192A (en) * | 2017-04-20 | 2017-08-11 | 东莞理工学院 | A high-efficiency negative pressure membrane dehumidifier and high-efficiency dehumidification system |
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