JPH06235559A - Method and apparatus for controlling operation of air conditioning plant using absorption type refrigerator - Google Patents
Method and apparatus for controlling operation of air conditioning plant using absorption type refrigeratorInfo
- Publication number
- JPH06235559A JPH06235559A JP5022351A JP2235193A JPH06235559A JP H06235559 A JPH06235559 A JP H06235559A JP 5022351 A JP5022351 A JP 5022351A JP 2235193 A JP2235193 A JP 2235193A JP H06235559 A JPH06235559 A JP H06235559A
- Authority
- JP
- Japan
- Prior art keywords
- air
- refrigerant
- temperature
- absorbing liquid
- cooled
- 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
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は一般の住宅、小規模建物
等を対象とする吸収式冷凍機を用いて行う空調装置の運
転制御方法及びその装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an operation control method for an air conditioner and an apparatus for the same, which uses an absorption refrigerator for a general house or a small building.
【0002】[0002]
【従来の技術】吸収式冷凍機を用いた冷房方式は、再生
器で蒸発させた冷媒蒸気を水冷方式の凝縮器で凝縮さ
せ、この凝縮した液冷媒を蒸発器に導き、室内のファン
コイルユニットと冷凍機間を循環する冷熱媒(通常水)
を蒸発潜熱で冷却し、一方蒸発した冷媒蒸気を水冷方式
の吸収器で濃溶液(吸収液)に吸収させ、再び再生器に
戻すというサイクルで運転されるものである。そして、
この吸収式冷凍機の場合、室内側ファンコイルユニット
内に循環させる冷熱媒の温度を蒸発器において7℃前後
まで冷却し、この冷熱媒を室内のファンコイルユニット
内に循環させて室内空気を冷却して12℃前後で蒸発器に
戻す構成である。このためリチュウムブロマイド水溶液
を吸収液として使用する場合、吸収器内の吸収液の温度
を40℃前後に保つことが必要となり、この温度を維持す
るためには冷却塔を屋上等に設置して水冷回路で冷却す
る方法がとられている。2. Description of the Related Art In a cooling system using an absorption refrigerator, a refrigerant vapor evaporated in a regenerator is condensed in a water-cooled condenser, and the condensed liquid refrigerant is guided to an evaporator to produce a fan coil unit in a room. Heat medium (normal water) that circulates between the refrigerator and the refrigerator
Is cooled by latent heat of vaporization, while the evaporated refrigerant vapor is absorbed in a concentrated solution (absorption liquid) by a water-cooled absorber and returned to the regenerator. And
In the case of this absorption refrigerator, the temperature of the cooling / heating medium circulated in the indoor fan coil unit is cooled to around 7 ° C. in the evaporator, and this cooling / heating medium is circulated in the indoor fan coil unit to cool the indoor air. It is then returned to the evaporator at around 12 ° C. For this reason, when using an aqueous solution of lithium bromide as the absorbing liquid, it is necessary to keep the temperature of the absorbing liquid in the absorber at around 40 ° C. To maintain this temperature, install a cooling tower on the rooftop, etc. A circuit cooling method is adopted.
【0003】[0003]
【発明が解決しようとする課題】しかし、このような水
冷方式をとる従来の吸収式冷凍機を用いて行う空調装置
においては次のような欠点がある。 a.吸収器を水冷方式で温度管理(冷却)していること
から、設備が大型になると共に配管等にも多くの工事費
がかかり、よって一般住宅或いは小規模建物の冷房用に
は不利である。 b.室内のファンコイルユニットと冷凍機は、冷熱媒循
環用の配管で結ぶ必要があることから、工事費、設備費
が高額になる。 c.吸収式冷凍機において、吸収液にアンモニア水を使
用し、冷媒にアンモニアを使用したアンモニア吸収式冷
凍機が知られている。この冷凍機で小型のものの場合、
吸収器の冷却を空冷方式で行うものがある。しかし、こ
の方式の場合、室内のファンコイルユニットと蒸発器間
を循環する冷熱媒には水が使用されている。この理由
は、アンモニアが万一漏れた場合に、室内にこの漏れた
アンモニアが流入するのを防止するためである。このた
め、空冷で吸収器を冷却するアンモニア吸収式冷凍機の
場合でも、室内のファンコイルユニットと蒸発器間は冷
熱媒を循環させる方式となっており、この配管上の問題
がある。又、リチュウムブロマイド水溶液を使用する吸
収式冷凍機において吸収器を空冷するためには、放熱面
積を非常に大きくとる必要があり、住宅や小規模建物用
には向かない。 d.一方、蒸発器により直接室内空気を冷却する所謂パ
ッケージ型吸収式ガスエアコンが知られている。しか
し、このガスエアコンの場合、吸収器及び凝縮器の冷却
は水冷方式であり、この例の場合も配管上の問題があ
る。 e.ところで、吸収式冷凍機を運転する場合、その機能
を満足に発揮させるためには、吸収液の濃度は重要なフ
ァクターとなる。例えば、吸収液の濃度が濃くなれば、
吸収液の温度をそれ程下げないでも液冷媒の蒸発温度を
低く保つことはできるが、同時に吸収液が結晶を起す危
険性が高くなる。従って、空冷式の吸収式冷凍機におい
て、外気温度が上昇した場合には吸収液の結晶を防ぎな
がらいかに高濃度で運転するかがポイントになる。However, the air conditioner using the conventional absorption chiller adopting such a water cooling system has the following drawbacks. a. Since the absorber is temperature-controlled (cooled) by a water-cooling system, the equipment becomes large and a lot of construction costs are required for piping and the like, which is disadvantageous for cooling a general house or a small building. b. Since it is necessary to connect the indoor fan coil unit and the refrigerator with a pipe for circulating the cooling / heating medium, the construction cost and equipment cost are high. c. Among absorption type refrigerators, there is known an ammonia absorption type refrigerator in which ammonia water is used as an absorption liquid and ammonia is used as a refrigerant. If this refrigerator is a small one,
There is one that cools the absorber by an air cooling method. However, in the case of this method, water is used as the cooling / heating medium circulating between the fan coil unit and the evaporator in the room. The reason for this is to prevent the leaked ammonia from flowing into the room in the unlikely event that ammonia leaks. For this reason, even in the case of an ammonia absorption refrigerator that cools the absorber by air cooling, a system in which a cooling / heating medium is circulated between the fan coil unit and the evaporator in the room has a problem in this piping. Further, in an absorption refrigerator using an aqueous solution of lithium bromide, in order to air-cool the absorber, it is necessary to have a very large heat radiation area, which is not suitable for a house or a small building. d. On the other hand, there is known a so-called package type absorption gas air conditioner in which indoor air is directly cooled by an evaporator. However, in the case of this gas air conditioner, the cooling of the absorber and the condenser is a water cooling system, and this example also has a problem in piping. e. By the way, when operating an absorption chiller, the concentration of the absorption liquid is an important factor for satisfactorily exerting its function. For example, if the concentration of the absorption liquid becomes high,
The evaporation temperature of the liquid refrigerant can be kept low without lowering the temperature of the absorbing liquid so much, but at the same time, there is a high risk that the absorbing liquid will cause crystallization. Therefore, in the air-cooled absorption refrigerator, when the outside air temperature rises, the point is how to operate at a high concentration while preventing the absorption liquid from crystallizing.
【0004】本発明の目的は、一般住宅を含む小規模建
物用に実施化が可能な空冷式を採用した吸収式冷凍機を
用いて行う空調方法及びその装置において、外気温度に
関連させて吸収液の濃度を変化させながら常にその機能
を満足に発揮させながら運転を行う制御方法とその装置
を提案することである。An object of the present invention is to provide an air-conditioning method and apparatus using an air-cooling type absorption refrigerating machine which can be put into practice for small-scale buildings including general houses. It is an object to propose a control method and an apparatus for performing an operation while constantly exerting its function satisfactorily while changing the liquid concentration.
【課題を解決するための手段】本発明において提案する
吸収式冷凍機を用いて行う空調方法及びその装置の構成
は次のとおりである。The air-conditioning method using the absorption refrigerating machine proposed in the present invention and the structure of the apparatus are as follows.
【0005】1.吸収液としてリチュウムブロマイド水
溶液を主成分としたものを使用し、冷媒として水を使用
すると共に、冷房対象室内空気が通る通路内に蒸発器を
位置させて室内空気を直接冷却し、この冷却された冷気
をダクトを経由して直接室内に送風して冷房を行い、且
つ吸収器内の吸収液の温度管理を空冷方式により行うこ
とを特徴とする吸収式冷凍機を用いて行う空調装置にお
いて、外気温度に関連させて、冷媒液溜に貯蔵する冷媒
量を制御することにより、吸収液が結晶温度に至らない
範囲で、吸収液の濃度を常に高濃度に保ちながら運転を
行う吸収式冷凍機を用いて行う空調装置の運転制御方
法。1. Using an aqueous solution containing lithium bromide as the main component as the absorbing liquid, using water as the refrigerant, and directly cooling the indoor air by positioning the evaporator in the passage through which the room air to be cooled passes, and this cooled In an air conditioner that uses an absorption refrigerator to cool the air by directly blowing the cool air into the room through a duct to control the temperature of the absorbing liquid in the absorber, By controlling the amount of refrigerant stored in the refrigerant sump in relation to the temperature, an absorption refrigerator that operates while always maintaining a high concentration of the absorption liquid within the range where the absorption liquid does not reach the crystal temperature A method for controlling the operation of an air conditioner using the method.
【0006】2.リチュウムブロマイド水溶液を主成分
とした吸収液に冷媒としての水を吸収させた稀溶液を加
熱して冷媒蒸気を発生させる再生器と、発生した冷媒蒸
気を空冷方式により凝縮させる凝縮器と、冷房対象室内
の空気が通る通路内に組み込まれた蒸発器と、送風ファ
ンにより空冷するように構成された吸収器と、前記凝縮
器と蒸発器間に組み込まれた冷媒液溜と、前記吸収器を
空冷する外気温度を検出し、この外気温度により前記冷
媒液溜内に貯蔵する冷媒の量を制御して吸収液の濃度を
制御する制御器と、から成る吸収式冷凍機を用いて行う
空調装置の運転制御装置。2. A regenerator that generates a refrigerant vapor by heating a dilute solution in which water as a refrigerant is absorbed by an absorption liquid containing an aqueous solution of lithium bromide as a main component, a condenser that condenses the generated refrigerant vapor by an air cooling method, and an object to be cooled. An evaporator installed in a passage through which indoor air passes, an absorber configured to be air-cooled by a blower fan, a refrigerant liquid pool installed between the condenser and the evaporator, and the absorber being air-cooled. Of the outside air temperature to be detected, the controller for controlling the concentration of the absorbing liquid by controlling the amount of the refrigerant stored in the refrigerant liquid reservoir by the outside air temperature, and of the air conditioner using an absorption refrigerator Operation control device.
【作用】再生器内の作動液は再生器内で例えばガスバー
ナにより加熱されて冷媒蒸気を発生し、この冷媒蒸気は
分離器で分離されて凝縮器に至り、ここで空冷方式によ
り冷却されて凝縮し、蒸発器に至る。蒸発器内の蒸発筒
の外側には、ダクトを経由して室内の温かい、例えば27
℃の空気が循環している。蒸発筒内において冷媒液が蒸
発すると、この潜熱により27℃の室内空気は15℃程度ま
で冷却されてダクトを経由して室内に送風される。蒸発
器で蒸発した冷媒蒸気は吸収器に導かれ、ここで吸収液
(濃溶液)に吸収される。この吸収作用は発熱反応であ
り、吸収液は空冷される。吸収液が十分に冷却されて温
度が下がるほど、又吸収液の濃度が濃いほど、蒸発器で
の冷媒の蒸発温度は低くなる。The working fluid in the regenerator is heated in the regenerator by, for example, a gas burner to generate a refrigerant vapor, which is separated by a separator and reaches a condenser, where it is cooled and condensed by an air cooling method. And then to the evaporator. Outside the evaporation tube inside the evaporator, warm the room inside the
℃ air is circulating. When the refrigerant liquid evaporates in the evaporation cylinder, this latent heat cools the room air at 27 ° C to about 15 ° C and blows it indoors via the duct. The refrigerant vapor evaporated in the evaporator is guided to the absorber, where it is absorbed by the absorbing liquid (concentrated solution). This absorbing action is an exothermic reaction, and the absorbing liquid is cooled by air. The more sufficiently the absorption liquid is cooled and the temperature is lowered, and the higher the concentration of the absorption liquid is, the lower the evaporation temperature of the refrigerant in the evaporator is.
【0007】本吸収冷凍機は7℃の冷水を発生させるの
ではなく、15℃程度に室内空気を冷却すればよいので、
吸収器内の吸収液の温度は50℃程度にまで冷却されれば
十分である。従って、夏期の外気温度35℃程度の空気
で、吸収器を空冷するだけで、冷凍機としての機能が発
揮できることになる。吸収器で冷媒蒸気を吸収した作動
液(稀溶液)は再び再生器に戻る。Since this absorption refrigerating machine does not generate cold water of 7 ° C., but needs to cool the room air to about 15 ° C.,
It is sufficient if the temperature of the absorbing liquid in the absorber is cooled to about 50 ° C. Therefore, the function as a refrigerator can be exhibited only by air-cooling the absorber with the air having an outside air temperature of about 35 ° C in summer. The working fluid (dilute solution) that has absorbed the refrigerant vapor in the absorber returns to the regenerator again.
【0008】さて、上記冷房サイクルにおいて、吸収液
の温度が最も低下するところは、空冷される吸収器の周
辺である。当然のことながら、空冷であるからには吸収
液が外気温度より低下することはありえない。そこで制
御器は空冷用の外気温度を検出し、この外気温度で結晶
しない濃度にまで吸収液(濃溶液)の濃度を上昇させる
ことにより、吸収液結晶の懸念を排除しつつ、高外気温
時にも、蒸発器の蒸発温度を低く維持することができ
る。In the cooling cycle, the temperature of the absorbing liquid is the lowest around the air-cooled absorber. As a matter of course, since it is air-cooled, the absorption liquid cannot fall below the outside air temperature. Therefore, the controller detects the outside air temperature for air cooling and raises the concentration of the absorbing liquid (concentrated solution) to a concentration that does not crystallize at this outside air temperature, eliminating the concern of absorbing liquid crystals and at the time of high outside air temperature. Also, the evaporation temperature of the evaporator can be kept low.
【0009】具体的には、外気温度が高い場合には冷媒
液溜への冷媒貯蔵量を増やして吸収液の濃度を上げる。Specifically, when the outside air temperature is high, the refrigerant storage amount in the refrigerant reservoir is increased to increase the concentration of the absorbing liquid.
【0010】この制御は、吸収液の濃度を例えば高・中
・低の三段切り替え方式等のステップ制御でも、或いは
連続制御方式でもよい。This control may be a step control such as a three-step switching system of high / medium / low concentration, or a continuous control system for the concentration of the absorbing liquid.
【0011】[0011]
【実施例】図1に本発明を実施した単効用吸収式冷凍機
を用いて行う空調装置を示す。1は空調機本体、2は住
宅、3は煙突、4は室内空気の送風ダクト、5は吸気ダ
クトであって、空調機本体1の詳細な構成は図2に示さ
れている。EXAMPLE FIG. 1 shows an air conditioner using a single-effect absorption refrigerator according to the present invention. Reference numeral 1 is an air conditioner main body, 2 is a house, 3 is a chimney, 4 is an indoor air blow duct, and 5 is an intake duct. The detailed structure of the air conditioner main body 1 is shown in FIG.
【0012】図2において、6は燃料供給ライン、7は
燃焼制御弁にして、燃料の開閉と調整を行う。8はバー
ナ、9は再生器にして、吸収液としてリチュウムブロマ
イド水溶液が使用され、冷媒として水が使用されてい
る。この再生器9で発生した冷媒蒸気は分離器9aで分
離された後、管路10を経由して凝縮器11に導かれ、ここ
で送風ファン12により空冷されて凝縮し、冷媒液溜13に
一旦溜められる。冷媒液溜13の冷媒は管路14を経由して
蒸発器15の分配管16に導かれ、この分配管16からフィン
18付の多数の蒸発筒17内を流下する。蒸発器15は熱交換
室19内に位置し、この熱交換室19の入口20は前記吸気ダ
クト5に結ばれ、出口21は送風ダクト4に結ばれ、住宅
2内の冷房対象室内2aの空気がファン20aにより強制
対流する。この結果、蒸発筒17内を流下する冷媒は室内
から直接吸い込んだ空気により加熱されて蒸発し、この
蒸発潜熱で室内空気を冷却する。冷却された空気は出口
21から送風ダクト4を経由して吹出口4aから室内2a
に送風される。ここで温度の一例を示せば、室内2aの
空気温度が27℃の場合、冷却されて吹出口4aから室内
2aに吹き出す空気の温度は15℃である。In FIG. 2, 6 is a fuel supply line, and 7 is a combustion control valve for opening / closing and adjusting the fuel. 8 is a burner, 9 is a regenerator, an aqueous solution of lithium bromide is used as an absorbing liquid, and water is used as a refrigerant. The refrigerant vapor generated in the regenerator 9 is separated by the separator 9a and then guided to the condenser 11 via the pipe line 10, where it is air-cooled by the blower fan 12 to be condensed and stored in the refrigerant liquid reservoir 13. It is stored once. The refrigerant in the refrigerant reservoir 13 is guided to the distribution pipe 16 of the evaporator 15 via the pipe 14, and the distribution pipe 16 serves as a fin.
It flows down in a large number of evaporation cylinders 17 with 18. The evaporator 15 is located in the heat exchange chamber 19, the inlet 20 of the heat exchange chamber 19 is connected to the intake duct 5, the outlet 21 is connected to the air duct 4, and the air in the cooling target room 2a in the house 2 is Is forcedly convected by the fan 20a. As a result, the refrigerant flowing down in the evaporation cylinder 17 is heated by the air directly sucked from the room and evaporated, and the latent heat of evaporation cools the indoor air. Cooled air exit
21 from the blower duct 4 to the outlet 4a to the room 2a
Be blown to. Here, as an example of the temperature, when the temperature of the air in the room 2a is 27 ° C, the temperature of the air that is cooled and blown from the outlet 4a to the room 2a is 15 ° C.
【0013】蒸発器15を出た冷媒蒸気はフィン25付の多
数の吸収筒23内に入る。一方、再生器9で加熱され、分
離器9aで分離された吸収液は管路26を経由して吸収液
注入口(ノズル)24に導かれ、ここで吸収筒23内に入
る。吸収筒23は吸収液がその内壁面に沿って膜状に流下
するように工夫されており、この結果、吸収面積が広く
なっている。更に吸収筒23は前記した送風ファン12によ
り空冷される構造となっている。ここで吸収液は50℃前
後に空冷される。The refrigerant vapor exiting the evaporator 15 enters a large number of absorption cylinders 23 with fins 25. On the other hand, the absorption liquid heated by the regenerator 9 and separated by the separator 9 a is guided to the absorption liquid injection port (nozzle) 24 via the pipe 26, and enters the absorption cylinder 23 there. The absorption cylinder 23 is devised so that the absorption liquid flows down in a film shape along the inner wall surface thereof, and as a result, the absorption area is widened. Further, the absorption cylinder 23 is structured to be air-cooled by the blower fan 12 described above. Here, the absorption liquid is air-cooled at around 50 ° C.
【0014】吸収筒23において冷媒蒸気を吸収した吸収
液(稀溶液)は集液管27に集められ、管路28を経由して
再生器9に戻る。29は循環ポンプ、30は熱交換器であっ
て、濃溶液で稀溶液を加熱する機能を有している。The absorbing liquid (dilute solution) that has absorbed the refrigerant vapor in the absorbing cylinder 23 is collected in the collecting pipe 27 and returns to the regenerator 9 via the pipe 28. Reference numeral 29 is a circulation pump, and 30 is a heat exchanger, which has a function of heating a dilute solution with a concentrated solution.
【0015】図3は蒸発器15及び吸収器22の実施例を示
すもので、分配管16に導かれた冷媒液は、この分配管16
で多数の蒸発筒17内に流入し、この蒸発筒17の外側を流
れる室内の空気で加熱されて蒸発し、この蒸発潜熱で室
内空気は冷却される。蒸発した冷媒蒸気は、蒸発筒内に
続く吸収筒23内に入り、ここで吸収液注入口(ノズル)
24から注入された吸収液に吸収される。吸収筒23の外側
は送風ファン12により強制空冷されている。吸収筒23を
出た作動液は集液管27内に集められてから再生器9に戻
る。集液管27内の作動液は、管内の下半分に溜められ、
上半分は気相となっており、万一何れかの吸収筒23内で
吸収されずに集液管27内に到達した冷媒蒸気は、この気
相から別の吸収筒23内に入り、ここで吸収される。実施
例において、蒸発器15の蒸発筒17には傾斜がつけてある
が、筒内の構造を工夫することにより、垂直にすること
も可能である。FIG. 3 shows an embodiment of the evaporator 15 and the absorber 22. The refrigerant liquid introduced into the distribution pipe 16 is
At that time, the air flows into a large number of evaporation tubes 17 and is heated by the air in the room flowing outside the evaporation tubes 17 to be evaporated, and the indoor air is cooled by this latent heat of evaporation. The evaporated vapor of refrigerant enters the absorption cylinder 23 that follows the evaporation cylinder, where the absorption liquid injection port (nozzle)
It is absorbed by the absorption liquid injected from 24. The outside of the absorption cylinder 23 is forcedly cooled by the blower fan 12. The hydraulic fluid that has left the absorption cylinder 23 is collected in the liquid collection pipe 27 and then returns to the regenerator 9. The working fluid in the collecting pipe 27 is stored in the lower half of the pipe,
The upper half is in the gas phase, and the refrigerant vapor that has reached the inside of the collecting pipe 27 without being absorbed in any of the absorption tubes 23 enters the other absorption tube 23 from this gas phase, Absorbed by. In the embodiment, the evaporation cylinder 17 of the evaporator 15 is inclined, but it is possible to make it vertical by devising the structure inside the cylinder.
【0016】31は制御器にして、この制御器31は外気温
度センサー32からの外気温度の入力信号に基づき、バル
ブ33或いはバルブ34のいずれかを開とする制御信号を発
生する。Reference numeral 31 denotes a controller, which generates a control signal for opening either the valve 33 or the valve 34 on the basis of an outside air temperature input signal from an outside air temperature sensor 32.
【0017】次にその制御の内容を実施例で説明する。Next, the contents of the control will be described with reference to an embodiment.
【0018】実施例では吸収液の濃溶液と稀溶液との濃
度差は4%の運転例である。In the embodiment, the concentration difference between the concentrated solution of the absorbing solution and the dilute solution is 4%.
【0019】なお吸収液の濃度(%)と結晶温度(℃)
との関係及びその濃度においてある温度になったとき平
衡する冷媒の蒸発温度を示すと表1のとおりである。The concentration (%) of the absorbing liquid and the crystallization temperature (° C)
Table 1 shows the relationship between and the evaporation temperature of the refrigerant that equilibrates when the temperature reaches a certain temperature.
【0020】[0020]
【表1】 [Table 1]
【0021】いま稀溶液58%、濃溶液62%で、バルブ33
が開いて、冷媒溜の液面は図2においてAであったとす
る。濃溶液の結晶温度は25℃であるから、外気温度が25
℃以上あれば結晶の心配はない。したがって、吸収液の
温度を46℃に保てば蒸発器温度は9℃に保てる。Now, dilute solution 58%, concentrated solution 62%, valve 33
Is opened, and the liquid level of the refrigerant reservoir is assumed to be A in FIG. Since the crystal temperature of the concentrated solution is 25 ° C, the outside temperature is 25
If it is above ℃, there is no worry of crystals. Therefore, if the temperature of the absorbing liquid is kept at 46 ° C, the evaporator temperature can be kept at 9 ° C.
【0022】次に、例えば外気温度が35℃を超して、吸
収液の温度を46℃に保つことが困難になってきたとす
る。この状態で稀溶液60%、濃溶液64%の状態にサイク
ルを変更する。Next, assume that it becomes difficult to keep the temperature of the absorbing liquid at 46 ° C., for example, when the outside air temperature exceeds 35 ° C. In this state, change the cycle to 60% dilute solution and 64% concentrated solution.
【0023】上記制御は外気温度が設定値を超えると、
バルブ33が閉じバルブ34が開き、冷媒溜の液面が図2に
おいてBに上昇して、冷媒液溜13へ貯蔵する冷媒量が増
えることによって、運転サイクルの吸収液濃度が上昇す
ることになる。In the above control, when the outside air temperature exceeds the set value,
The valve 33 is closed, the valve 34 is opened, the liquid level of the refrigerant reservoir rises to B in FIG. 2, and the amount of the refrigerant stored in the refrigerant reservoir 13 increases, so that the concentration of the absorbing liquid in the operation cycle increases. .
【0024】このような制御が行われて、稀溶液濃度が
60%に上昇すると、表1に示すとおり、吸収液の温度が
50℃に上昇しても、蒸発器の温度は9℃に保てることに
なる。反対に外気温度が設定値よりも低下した場合に
は、逆の制御が行われて、吸収液の濃度が下げられる。By performing such control, the dilute solution concentration
When it rises to 60%, as shown in Table 1, the temperature of the absorbing liquid increases.
Even if the temperature rises to 50 ° C, the temperature of the evaporator can be kept at 9 ° C. On the contrary, when the outside air temperature is lower than the set value, the reverse control is performed to reduce the concentration of the absorbing liquid.
【0025】なお、上記実施例は単効用吸収式冷凍機を
用いた場合であるが、二重効用吸収式冷凍機に対しても
本発明はそのまま適用できる。Although the above-mentioned embodiment uses a single-effect absorption refrigerator, the present invention can be applied to a double-effect absorption refrigerator as it is.
【発明の効果】本発明は以上のように、空冷方式を採用
した吸収式冷凍機を利用した空調方法及びその装置にお
いて、吸収液の濃度を外気温度に関連して制御するよう
にしたため、結晶の危険を回避しながら、吸収器を空冷
温度で運転して、冷凍機の機能を満足に発揮させること
が可能になる。As described above, according to the present invention, the concentration of the absorbing liquid is controlled in relation to the outside air temperature in the air-conditioning method and the apparatus using the absorption type refrigerator adopting the air cooling system. It is possible to operate the absorber at the air-cooling temperature and to fully realize the function of the refrigerator while avoiding the risk of.
【図1】本発明に係る吸収式冷凍機を使用した空調装置
の説明図。FIG. 1 is an explanatory diagram of an air conditioner using an absorption refrigerator according to the present invention.
【図2】本発明に係る吸収式冷凍機の構成とその作用の
説明図。FIG. 2 is an explanatory view of the structure and operation of an absorption refrigerator according to the present invention.
【図3】蒸発器と吸収器の説明図。FIG. 3 is an explanatory diagram of an evaporator and an absorber.
1 空調機本体 2 住宅 3 煙突 4 送風ダクト 5 吸気ダクト 6 燃料供給ライン 7 燃料制御弁 8 バーナ 9 再生器 9a 分離器 10 管路 11 凝縮器 12 送風ファン 13 冷媒溜 14 管路 15 蒸発器 16 分配管 17 蒸発筒 18 フィン 19 熱交換室 20 入口 21 出口 22 吸収器 23 吸収筒 24 分配管 25 フィン 26 管路 27 集液管 28 管路 29 循環ポンプ 30 熱交換器 31 制御器 32 外気温度検出センサー 33 バルブ 34 バルブ 1 Air conditioner body 2 House 3 Chimney 4 Blower duct 5 Intake duct 6 Fuel supply line 7 Fuel control valve 8 Burner 9 Regenerator 9a Separator 10 Pipeline 11 Condenser 12 Blower fan 13 Refrigerant reservoir 14 Pipeline 15 Evaporator 16 minutes Piping 17 Evaporation tube 18 Fin 19 Heat exchange chamber 20 Inlet 21 Outlet 22 Absorber 23 Absorption tube 24 minutes Piping 25 Fin 26 Pipe line 27 Liquid collection pipe 28 Pipe line 29 Circulation pump 30 Heat exchanger 31 Controller 32 Outside temperature detection sensor 33 valve 34 valve
Claims (4)
液を主成分としたものを使用し、冷媒として水を使用す
ると共に、冷房対象室内空気が通る通路内に蒸発器を位
置させて室内空気を直接冷却し、この冷却された冷気を
ダクトを経由して直接室内に送風して冷房を行い、且つ
吸収器内の吸収液の温度管理を空冷方式により行うこと
を特徴とする吸収式冷凍機を用いて行う空調装置におい
て、外気温度に関連させて、冷媒液溜に貯蔵する冷媒量
を制御することにより、吸収液が結晶温度に至らない範
囲で、吸収液の濃度を常に高濃度に保ちながら運転を行
う吸収式冷凍機を用いて行う空調装置の運転制御方法。1. An absorbent containing an aqueous solution of lithium bromide as a main component is used, water is used as a refrigerant, and an evaporator is positioned in a passage through which the indoor air to be cooled is cooled to cool the indoor air directly. , The cooling air is blown directly into the room through a duct for cooling, and the temperature of the absorbing liquid in the absorber is controlled by an air cooling system. In an air conditioner, by controlling the amount of refrigerant stored in the refrigerant reservoir in relation to the outside air temperature, operation is performed while maintaining a high concentration of the absorbing liquid within the range where the absorbing liquid does not reach the crystal temperature. An operation control method for an air conditioner using an absorption refrigerator.
した吸収液に冷媒としての水を吸収させた稀溶液を加熱
して冷媒蒸気を発生させる再生器と、 発生した冷媒蒸気を空冷方式により凝縮させる凝縮器
と、 冷房対象室内の空気が通る通路内に組み込まれた蒸発器
と、 前記凝縮器と蒸発器間に組み込まれた冷媒液溜と、 送風ファンにより空冷するように構成された吸収器と、 前記吸収器を空冷する外気温度を検出し、この外気温度
により前記冷媒液溜内に貯蔵する冷媒の量を制御して吸
収液の濃度を制御する制御器と、 から成る吸収式冷凍機を用いて行う空調装置の運転制御
装置。2. A regenerator for generating a refrigerant vapor by heating a dilute solution in which water as a refrigerant is absorbed in an absorbent containing an aqueous solution of lithium bromide as a main component, and a condensing condenser for condensing the generated refrigerant vapor by an air cooling method. A condenser, an evaporator incorporated in a passage through which air in the room to be cooled passes, a refrigerant liquid reservoir incorporated between the condenser and the evaporator, and an absorber configured to be air-cooled by a blower fan, A controller for detecting the outside air temperature for air-cooling the absorber, controlling the amount of the refrigerant stored in the refrigerant liquid reservoir by the outside air temperature to control the concentration of the absorbing liquid, and an absorption refrigerator comprising: Operation control device for air conditioners.
1及び2記載の吸収式冷凍機を用いて行う空調装置の運
転制御方法。3. A method for controlling the operation of an air conditioner using the absorption refrigerating machine according to claim 1, which is carried out using a single-effect absorption refrigerating machine.
項1及び2記載の吸収式冷凍機を用いて行う空調装置の
運転制御装置。4. An operation control device for an air conditioner using the absorption refrigerating machine according to claim 1 or 2, which is carried out using a double-effect absorption refrigerating machine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5022351A JPH06235559A (en) | 1993-02-10 | 1993-02-10 | Method and apparatus for controlling operation of air conditioning plant using absorption type refrigerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5022351A JPH06235559A (en) | 1993-02-10 | 1993-02-10 | Method and apparatus for controlling operation of air conditioning plant using absorption type refrigerator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06235559A true JPH06235559A (en) | 1994-08-23 |
Family
ID=12080241
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5022351A Pending JPH06235559A (en) | 1993-02-10 | 1993-02-10 | Method and apparatus for controlling operation of air conditioning plant using absorption type refrigerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06235559A (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01267771A (en) * | 1988-04-19 | 1989-10-25 | Nec Corp | Key management board system for security |
JPH02103471U (en) * | 1989-02-01 | 1990-08-16 | ||
JPH03103579A (en) * | 1989-09-16 | 1991-04-30 | Matsushita Electric Works Ltd | Key deposit control system |
JPH03156079A (en) * | 1990-01-12 | 1991-07-04 | Matsushita Electric Works Ltd | Dispersion type coming-in and going-out control system |
JPH03275877A (en) * | 1990-03-23 | 1991-12-06 | Toshiba Corp | Exit/entrance controller for building |
JPH04203083A (en) * | 1990-11-30 | 1992-07-23 | Yamatake Honeywell Co Ltd | Key control box |
JPH04366287A (en) * | 1991-06-14 | 1992-12-18 | Mitsubishi Electric Corp | Key housing device |
-
1993
- 1993-02-10 JP JP5022351A patent/JPH06235559A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01267771A (en) * | 1988-04-19 | 1989-10-25 | Nec Corp | Key management board system for security |
JPH02103471U (en) * | 1989-02-01 | 1990-08-16 | ||
JPH03103579A (en) * | 1989-09-16 | 1991-04-30 | Matsushita Electric Works Ltd | Key deposit control system |
JPH03156079A (en) * | 1990-01-12 | 1991-07-04 | Matsushita Electric Works Ltd | Dispersion type coming-in and going-out control system |
JPH03275877A (en) * | 1990-03-23 | 1991-12-06 | Toshiba Corp | Exit/entrance controller for building |
JPH04203083A (en) * | 1990-11-30 | 1992-07-23 | Yamatake Honeywell Co Ltd | Key control box |
JPH04366287A (en) * | 1991-06-14 | 1992-12-18 | Mitsubishi Electric Corp | Key housing device |
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