JPS58173323A - Air conditioner - Google Patents

Air conditioner

Info

Publication number
JPS58173323A
JPS58173323A JP5432982A JP5432982A JPS58173323A JP S58173323 A JPS58173323 A JP S58173323A JP 5432982 A JP5432982 A JP 5432982A JP 5432982 A JP5432982 A JP 5432982A JP S58173323 A JPS58173323 A JP S58173323A
Authority
JP
Japan
Prior art keywords
air
adsorbent
bed
regeneration
moisture
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
Application number
JP5432982A
Other languages
Japanese (ja)
Inventor
Toshio Nakayama
敏男 中山
Takeshi Kanai
健 金井
Masumasa Hashimoto
益征 橋本
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.)
Tokyo Sanyo Electric Co Ltd
Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
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 Tokyo Sanyo Electric Co Ltd, Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP5432982A priority Critical patent/JPS58173323A/en
Publication of JPS58173323A publication Critical patent/JPS58173323A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-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
    • F24F3/12Air-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
    • F24F3/14Air-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
    • F24F3/1411Air-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
    • F24F3/1423Air-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1044Rotary wheel performing other movements, e.g. sliding

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Central Air Conditioning (AREA)

Abstract

PURPOSE:To simplify the maintenance and service with respect to the titled air conditioner without requiring any special machine or any control device for transporting an adsorbent by causing indoor air to flow through a flowpath of a circulating cycle, and utilizing the flow of indoor air to circulate the adsorbent, with respect to a fluidized bed type air conditioner using a moisture absorbent such as zeolite or a molecular sieve. CONSTITUTION:A fluid bed forming a dehumidifying bed 2 is of a multistage structure partitioned by wire nets 8, 8..., for example, and transports uprising air successively to upper stages as the uprising air agitates the adsorbent. On the other hand, the contact of air with the adsorbent causes the adsorbent to rise up in the same manner. In addition, a regeneration bed 1 is constituted so that the adsorbent which falls from a hopper 6 by gravity is developed onto a dispersion plate 9, and discharges moisture to uprising heated air. On the other hand, the adsorbent successively falls onto a dispersion plate 9 in a subsequent stage via a downcorner 10 opening in the vicinity of the dispersion plate 9. As the heated air supplied to the regeneration bed 1, is used heated air obtained by a solar heat collector 12, for example. On the other hand, air which air-conditions the interior of the room R flows into the dehumidifying bed 2 while involving the adsorbent of a high temperature, falling the regeneration bed output 18, and rises up while discharging moisture to the adsorbent in the dehumidifying bed 2. The thus obtained dry air is suitably humidified by a humidifier 18 and is recirculated within the room.

Description

【発明の詳細な説明】 本発明は、ゼオライトやモレキュラーシーブなどの水分
吸着剤を使用した空気調和装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an air conditioner using a moisture adsorbent such as zeolite or molecular sieve.

従来の空気調和装置は、一般に、モータで冷媒圧縮機を
駆動し、冷媒の相変化を利用して調温。
Conventional air conditioners generally use a motor to drive a refrigerant compressor and use phase changes in the refrigerant to regulate temperature.

―湿を行なう機構を有しているが、このような電気式冷
凍機では電気エネルギの消費量がかさむ上に、高い圧力
の冷媒の密閉サイクルを形成する必要があるため、故障
を生じ易く、保守にも手間を装する欠点がある。
-Although it has a humidification mechanism, such electric refrigerators consume a lot of electrical energy and require a closed cycle of high-pressure refrigerant, making them prone to breakdowns. It also has the disadvantage of being a hassle to maintain.

又、水分を吸着する粉状や粒状の吸着剤を用いた草気副
和機も古くから試用されているが1機構的には上記の電
気式冷凍機のように完成された域になく、各種の改良を
必要とする状況にある。
Additionally, Kusaki admixture machines that use powdered or granular adsorbents to adsorb moisture have been used for a long time, but mechanically they are not as complete as the electric refrigerators mentioned above. The situation is such that various improvements are required.

このような点に鑑みなされた本発明は、特別な密閉構造
や吸着剤搬送装置を用いることなく、わずかな電力と太
陽熱などの自然熱を活用して室内の調温とm湿とができ
る空気調和機を提供するものであり、以下に本発明の実
施例を示す図面に従い説明する。
In view of these points, the present invention has been developed to create an air system that can control indoor temperature and humidity by utilizing a small amount of electricity and natural heat such as solar heat, without using a special sealed structure or adsorbent conveying device. The present invention provides a harmonizer, and embodiments of the present invention will be described below with reference to the drawings.

図において、 +11121は例えば1球状化したシリ
カゲルやモレキュラーシーブなどの吸湿性粉体(以下吸
着剤という)の流動床であり、(1)は重力によって流
下する吸着剤と、下方の空気管(3:から流入する加熱
された空気とをM合することにより該吸着剤に吸収され
ている水分を除去する再生床、12)は鯨流動床円を流
れる空気から吸着剤に水分を吸収させる除湿床、(4j
は諌除湿床(2)から流出する吸着剤と空気との混合流
から熱を放散させる放熱器。
In the figure, +11121 is a fluidized bed of hygroscopic powder (hereinafter referred to as adsorbent) such as 1 spheroidal silica gel or molecular sieve, and (1) is the adsorbent flowing down by gravity and the air pipe (3) below. 12) is a regeneration bed that removes moisture absorbed by the adsorbent by combining heated air flowing in from the 12), a dehumidification bed that allows the adsorbent to absorb moisture from the air flowing through the whale fluidized bed circle. , (4j
is a radiator that dissipates heat from the mixed flow of adsorbent and air flowing out from the dehumidifying bed (2).

(51は放熱後の混合流から吸着剤を分離し、空気を室
内側(R)へ、吸着剤をホッパー(6)へ流下させるサ
イクロン型の分離装置であり、これらの再生床(1)、
除湿床(21,および分離装置(51は、除湿剤及び/
又は空気の流動できる管路(7)によって接続されて空
気流を用いた吸着剤の循環サイクルを形成している。
(51 is a cyclone type separation device that separates the adsorbent from the mixed flow after heat dissipation, and causes the air to flow toward the indoor side (R) and the adsorbent to flow down to the hopper (6); these regeneration beds (1),
The dehumidification bed (21) and the separation device (51 are the dehumidifier and/or
Alternatively, they are connected by a conduit (7) through which air can flow, forming a circulation cycle of the adsorbent using an air flow.

而して、除湿床12+を形成する流動床は2例えば。Thus, the number of fluidized beds forming the dehumidifying bed 12+ is two, for example.

金網f8J (81・・・で仕切られた多段構成となっ
ており。
It has a multi-stage structure divided by wire mesh f8J (81...).

上昇する空気が吸着剤を攪拌しながら、順次、上段へ輸
送する一方空気と吸湿剤との接触が同上するようになっ
ている。又、再生床11)は、第2図に示すように分散
板+91. +9ト・・と流下管(1(1,ati・・
・とを組み合わせた構成であり、重力によってホッパー
(6)から落下する吸着剤が1分散板(9)丘に拡げら
れ。
The rising air agitates the adsorbent and sequentially transports it to the upper stage, while the air and the moisture absorbent come into contact with each other at the same time. In addition, the regeneration bed 11) has a dispersion plate +91. +9 to... and the downstream pipe (1 (1, ati...
・The adsorbent falling from the hopper (6) by gravity is spread over one dispersion plate (9).

小孔a11を上昇する加熱された空気に水分を放出する
一方1分散板(9)の近くに開口する流下管G(1を経
て次段の分散板(91に落下し、上段と同様に水分を放
出しながら更に次の段の分散板・・・へと落下するよう
な構造を有している。この再生床litへ供給される加
熱空気には例えば、太陽熱集熱器a3によって得られた
熱が蓄えられている蓄熱1c131からポンプ(141
で加熱液を循環している気液熱交換器ttSに屋外(0
ノから供給される空気を通し、約100℃近くに加熱し
た空気が用いられ、一方、再生床+11から流出する湿
った空気は、尚、80℃近い温度を有しているため、ヒ
ートパイプを用いた熱回収器(161によって気液熱交
換器σ9に流入する罰の室外空気を予熱した後屋外(0
)へ排気される。
Moisture is released into the heated air rising through the small hole a11, while the flow pipe G (1) that opens near the dispersion plate (9) falls to the next dispersion plate (91), where it releases moisture in the same way as the upper stage. It has a structure in which the heated air is emitted and falls to the dispersion plate of the next stage...For example, the heated air supplied to this regeneration bed lit is Pump (141) from thermal storage 1c131 where heat is stored
Outdoors (0
The air heated to approximately 100°C is used through the air supplied from the regeneration bed +11, while the humid air flowing out from the regeneration bed +11 still has a temperature of approximately 80°C, so a heat pipe is used. After preheating the outdoor air flowing into the gas-liquid heat exchanger σ9 by the heat recovery device used (161), the outdoor air (0
) is exhausted.

一方、WP’1(RJを空51’l空気ハ、送風1!I
(171によって再生床出口G8から落下する高温の吸
着剤を巻き込みながら除湿床124 g=流入し、ここ
で吸着剤に水分を放出しつつ上昇していくため、約27
℃、湿#f50%で送風機(171に吸い込まれた室内
空気が除湿床12+を出るときはおよそ42℃、湿度1
011の吸着剤との混合流となっている。
On the other hand, WP'1 (empty RJ 51'l air ha, ventilation 1!I
(By 171, it flows into the dehumidifying bed 124 g while entraining the high temperature adsorbent that falls from the regeneration bed outlet G8, and rises while releasing moisture to the adsorbent, so approximately 27 g
℃, humidity #f50%, when the indoor air sucked into the blower (171) leaves the dehumidifying floor 12+, it is approximately 42℃, humidity 1
This is a mixed flow with the adsorbent No. 011.

このようにして得られた梢温度の高い乾燥空気の熱をヒ
ートパイプ型放熱器(4)で29℃程度にまで熱放散さ
せると、約2011の湿度の空気になるため、吸湿剤だ
けを分離装置(51で除くと、乾燥した空気が得られる
。0秒はこの空気の温度を更に下げて室内に供給するた
めの加湿器であり、この加湿器a・を使って水分を添加
下れば、水分が気化する際に使われる気化潜熱によって
、約18℃、湿度701gの空気が室内に還流できるこ
ととなる。
When the heat of the dry air with a high treetop temperature obtained in this way is dissipated to about 29℃ using a heat pipe type radiator (4), the air has a humidity of about 2011℃, so only the moisture absorbent is separated. When removed by the device (51), dry air is obtained.0 seconds is a humidifier that further lowers the temperature of this air and supplies it indoors. Due to the latent heat of vaporization used when water vaporizes, air with a temperature of approximately 18°C and humidity of 701g can be returned to the room.

尚、 (19は先に述べた再生床(1)へ供給する層外
空気供給ダクトの一例であり、上記吸着剤の循環サイク
ルを例示した数値のように作動させるために35℃、湿
度50g6の屋外空気を送風m■で吸入した後、加湿器
Qυで一旦、温度降下させ(約25tJこれにより、放
熱器(4)での熱放散を助ける一方、このようにして再
び昇温された空気を熱回収器a8.気液熱交換器fi9
を経て再生床11+に供給するようにしてもよく、或い
は又、排気口のから、そのまま屋外に排出しても良い。
(19 is an example of the extralayer air supply duct that supplies the above-mentioned regeneration bed (1), and in order to operate the circulation cycle of the adsorbent as shown in the example numerical values, it is heated at 35℃ and humidity of 50g6. After inhaling the outdoor air with the air blower m■, the temperature is lowered by the humidifier Qυ (approximately 25 tJ).This helps the heat dissipation in the radiator (4), and at the same time, the air heated in this way is heated again. Heat recovery device a8. Gas-liquid heat exchanger fi9
It may be supplied to the regeneration bed 11+ through the air outlet, or it may be directly discharged outdoors from the exhaust port.

尚、−上記の説明において示した空気温度および湿度は
1本発明の空気調和装置を構成する吸着剤の循環サイク
ルがどのように機能するかを示す目安としての理論値で
あり、実際の運転においては室内空気温度の条件、屋外
空気の条件も刻々と変化するため、その変化に応じて再
生床+11へ供給する加熱空気の温度、送風機αDの風
量、放熱器(4)へ流通される屋外空気の量、温闇、加
湿器aseuによる加湿量などを制細し、必要な温度と
湿度に調整された空気を室(R月二供給するようにされ
る。
The air temperature and humidity shown in the above explanation are theoretical values as a guideline for how the circulation cycle of the adsorbent that constitutes the air conditioner of the present invention functions, and in actual operation. Since indoor air temperature conditions and outdoor air conditions also change from moment to moment, the temperature of heated air supplied to regeneration floor +11, the air volume of blower αD, and the outdoor air distributed to radiator (4) are adjusted according to these changes. By controlling the amount of air, temperature, darkness, and amount of humidification by the ASEU humidifier, air adjusted to the required temperature and humidity is supplied to the room (twice a month).

又1本発明の空気調和装置を暖房に使用するときは、室
内空気を気液熱交換器09で直接に加熱して室(R月二
還流するようにダクト(I2)の接続を切替えるもので
あり、吸着剤は使用されない。
In addition, when the air conditioner of the present invention is used for heating, the connection of the duct (I2) is changed so that the indoor air is directly heated by the gas-liquid heat exchanger 09 and recirculated to the room (R). Yes, no adsorbent is used.

このように1本発明による空気調和装置は、流動床の吸
着剤を利用して直接に空気調和をするに際し、再生床出
口から吸着剤の分離装置出口に至る循環サイクルの流路
C:連続的に室内空気を流通させ、室内空気の流れを利
用して吸着剤の循環をさせつつ室内空気の温度と湿度を
調整できるようにしたので、吸S剤を再生床から除湿床
に輸送する特別な機器、制卿装置は必要とされず、この
ため、保守、サービスが簡略化された空気調和装置を得
ることができる。
As described above, in the air conditioner according to the present invention, when direct air conditioning is performed using the adsorbent in the fluidized bed, the flow path C of the circulation cycle from the regeneration bed outlet to the adsorbent separation device outlet is continuous. In this way, the temperature and humidity of the indoor air can be adjusted while circulating the adsorbent using the flow of indoor air. No equipment or control device is required, and therefore an air conditioner with simplified maintenance and service can be obtained.

又、吸着剤の循環サイクルは、空−する室内空気と直接
接触される開放型構造であり、熱源としても太陽熱やそ
の他の自然熱或いは工場からの排熱を利用することがで
きるなどエネルギ消費が少なく効率の良い空気調和装置
が得られる。
In addition, the circulation cycle of the adsorbent is an open structure in which it comes into direct contact with empty indoor air, and solar heat, other natural heat, or waste heat from factories can be used as a heat source, reducing energy consumption. A more efficient air conditioner can be obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

81図は本発明による空気調和装置の一実施例を示すシ
ステム構成図、1@2図は再生床の一例を示す部分拡大
端面図である。 第1図 第2翰
Fig. 81 is a system configuration diagram showing an embodiment of the air conditioner according to the present invention, and Fig. 1@2 is a partially enlarged end view showing an example of a regeneration bed. Figure 1, 2nd wire

Claims (1)

【特許請求の範囲】[Claims] +13  加熱された空気との直接接触によって吸着剤
の水分を除去する再生床と、該再生床から流下する吸着
剤と室内空気とを肩合しつつ上方へ流動する間に室内空
気の湿気を吸着剤に吸着させる除湿床と、除湿床から流
出する吸着剤と空気との混合流から熱を放散させ、かつ
、空気と吸着剤とを分ける分離装置と、これら再生床、
除湿床および分離装置を接続する管路とから空気流を用
いた吸着剤の循環サイクルを形成し、再生床出口から分
離装置出口に至る循環サイクルの流路に連続的に室内空
気を流通させて吸着剤を搬送させることにより、該室内
空気の水分を除去するようにしたことを特徴とする空気
調和装置。
+13 A regeneration bed that removes moisture from the adsorbent by direct contact with heated air, and a regeneration bed that aligns the adsorbent flowing down from the regeneration bed with indoor air and adsorbs moisture in the indoor air while flowing upward. A dehumidifying bed for adsorbing the adsorbent to the adsorbent, a separation device for dissipating heat from a mixed flow of the adsorbent and air flowing out from the dehumidifying bed and separating the air and the adsorbent, and a regeneration bed for these,
A circulation cycle of the adsorbent using air flow is formed from the dehumidification bed and the pipe connecting the separation device, and indoor air is continuously circulated through the flow path of the circulation cycle from the regeneration bed outlet to the separation device outlet. An air conditioner characterized in that moisture in indoor air is removed by transporting an adsorbent.
JP5432982A 1982-03-31 1982-03-31 Air conditioner Pending JPS58173323A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5432982A JPS58173323A (en) 1982-03-31 1982-03-31 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5432982A JPS58173323A (en) 1982-03-31 1982-03-31 Air conditioner

Publications (1)

Publication Number Publication Date
JPS58173323A true JPS58173323A (en) 1983-10-12

Family

ID=12967547

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5432982A Pending JPS58173323A (en) 1982-03-31 1982-03-31 Air conditioner

Country Status (1)

Country Link
JP (1) JPS58173323A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5496395A (en) * 1993-12-28 1996-03-05 Kureha Kagaku Kogyo Kabushiki Kaisha System for recovering organic solvent in soil
WO1997007873A1 (en) * 1995-08-22 1997-03-06 Lawrence Cioffi Voc control/solvent recovery system
US5904750A (en) * 1995-08-22 1999-05-18 Cowles; Harold R. VOC control/solvent recovery system
JP2002219327A (en) * 2001-01-30 2002-08-06 Denso Corp Dehumidifier
WO2023243328A1 (en) * 2022-06-17 2023-12-21 ウシオ電機株式会社 Carbon dioxide recovering method and carbon dioxide recovering system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5496395A (en) * 1993-12-28 1996-03-05 Kureha Kagaku Kogyo Kabushiki Kaisha System for recovering organic solvent in soil
WO1997007873A1 (en) * 1995-08-22 1997-03-06 Lawrence Cioffi Voc control/solvent recovery system
US5676738A (en) * 1995-08-22 1997-10-14 Cioffi; Lawrence VOC control/solvent recovery system
US5904750A (en) * 1995-08-22 1999-05-18 Cowles; Harold R. VOC control/solvent recovery system
JP2002219327A (en) * 2001-01-30 2002-08-06 Denso Corp Dehumidifier
JP4491973B2 (en) * 2001-01-30 2010-06-30 株式会社デンソー Dehumidifier
WO2023243328A1 (en) * 2022-06-17 2023-12-21 ウシオ電機株式会社 Carbon dioxide recovering method and carbon dioxide recovering system

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