JP2002250573A - Air conditioner - Google Patents

Air conditioner

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Publication number
JP2002250573A
JP2002250573A JP2001048708A JP2001048708A JP2002250573A JP 2002250573 A JP2002250573 A JP 2002250573A JP 2001048708 A JP2001048708 A JP 2001048708A JP 2001048708 A JP2001048708 A JP 2001048708A JP 2002250573 A JP2002250573 A JP 2002250573A
Authority
JP
Japan
Prior art keywords
heat
refrigerant
vapor compression
heat exchanger
recovery means
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.)
Withdrawn
Application number
JP2001048708A
Other languages
Japanese (ja)
Inventor
Koichi Endo
浩一 遠藤
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.)
Denso Corp
Original Assignee
Denso Corp
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 Denso Corp filed Critical Denso Corp
Priority to JP2001048708A priority Critical patent/JP2002250573A/en
Publication of JP2002250573A publication Critical patent/JP2002250573A/en
Withdrawn legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PROBLEM TO BE SOLVED: To highly maintain energy utilization rate even in either cooling or heating operation. SOLUTION: In cooling operation, heat that is collected by a solar energy collector 30 is thrown into an adsorption type refrigerating machine 20 for cooling the high-pressure side refrigerant of a vapor compression type heat pump 10 using the adsorption type refrigerating machine 20. On the other hand, in heating operation, the low-pressure side refrigerant of the vapor compression type heat pump 10 is heated by heat that is collected by the solar energy collector 30, and at the same time is heated by the vapor compression type heat pump 10, thus performing heating using heat that is collected by the solar energy collector 30 and heat that is recovered by an outdoor heat exchanger 12, hence effectively utilizing heat that is collected by the solar energy collector 30 either in cooling operation or in heating operation and highly maintaining the energy utilization rate.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、蒸気圧縮式ヒート
ポンプ(吸着式冷凍機)及び吸着式冷凍機を組み合わせ
た空調装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air conditioner combining a vapor compression heat pump (adsorption refrigerator) and an adsorption refrigerator.

【0002】[0002]

【従来の技術】蒸気圧縮式ヒートポンプ及び吸着式冷凍
機を組み合わせた空調装置として、例えば特開平11−
223414号公報に記載の発明では、吸着式冷凍機に
より圧縮機の吐出側の冷媒を冷却することにより、蒸気
圧縮式冷凍機の高圧側冷媒を低下させて圧縮機の圧縮仕
事を減少させている。
2. Description of the Related Art An air conditioner combining a vapor compression heat pump and an adsorption refrigerator is disclosed in, for example,
In the invention described in Japanese Patent No. 223414, the refrigerant on the discharge side of the compressor is cooled by the adsorption refrigerator, whereby the high pressure side refrigerant of the vapor compression refrigerator is reduced, and the compression work of the compressor is reduced. .

【0003】[0003]

【発明が解決しようとする課題】しかし、仮に、単純に
そのまま、上記公報に記載の発明を冷暖房切換可能な空
調装置に適用すると、冷房運転時には、前述のごとく、
圧縮機の圧縮仕事を減少させて空調装置の効率を向上さ
せることができるものの、暖房時においては、暖房能力
が吸着式冷凍機に吸熱されてしまい、暖房能力が低下し
てしまう。
However, if the invention described in the above publication is simply applied to an air conditioner capable of switching between cooling and heating, as described above, during cooling operation,
Although the compression work of the compressor can be reduced to improve the efficiency of the air conditioner, at the time of heating, the heating capacity is absorbed by the adsorption refrigerator, and the heating capacity is reduced.

【0004】また、この問題を回避するには、太陽熱温
水器にて回収した太陽熱を使用せずに外部に放出する
か、床暖房等の他の暖房機器に回収した太陽熱を使用す
る等の手段が考えられるが、太陽熱を使用せずに外部に
放出する手段では、エネルギーの利用効率が低くなり、
他の暖房機器に回収した太陽熱を使用するでは、温水配
管等の取り回しが複雑になってしまう。
In order to avoid this problem, the solar heat recovered by the solar water heater is discharged to the outside without using it, or the solar heat recovered by other heating equipment such as floor heating is used. However, the method of releasing the heat to the outside without using solar heat reduces the efficiency of energy use,
If the solar heat collected by another heating device is used, the arrangement of hot water piping and the like becomes complicated.

【0005】本発明は、上記点に鑑み、冷房運転時及び
暖房運転時のいずれの場合においてもエネルギー利用率
を高く維持することを目的とする。
[0005] In view of the above, it is an object of the present invention to maintain a high energy utilization rate in both a cooling operation and a heating operation.

【0006】[0006]

【課題を解決するための手段】本発明は、上記目的を達
成するために、請求項1に記載の発明では、圧縮機(1
1)、室外熱交換器(12)、減圧器(13)及び室内
熱交換器(14)を有する蒸気圧縮式ヒートポンプ(1
0)と、冷媒の蒸発により冷凍能力を発揮し、かつ、そ
の蒸発した冷媒を吸着するとともに、加熱されることに
より吸着していた冷媒を脱離する吸着剤(Si)が収納
された吸着器(21)を有する吸着式冷凍機(20)
と、熱を回収する熱回収手段(30)とを備え、冷房運
転時には、熱回収手段(30)により回収した熱を吸着
式冷凍機(20)に投入して、吸着式冷凍機(20)及
び蒸気圧縮式ヒートポンプ(10)により冷房を行い、
暖房運転時には、熱回収手段(30)により回収した
熱、及び室外熱交換器(12)にて回収した熱により暖
房を行うことを特徴とする。
According to the present invention, in order to achieve the above object, a compressor (1) is provided.
1) A vapor compression heat pump (1) having an outdoor heat exchanger (12), a decompressor (13), and an indoor heat exchanger (14).
0), an adsorber that exhibits a refrigerating ability by evaporating the refrigerant, and that stores the adsorbent (Si) that adsorbs the evaporated refrigerant and desorbs the adsorbed refrigerant when heated. Adsorption refrigerator having (21) (20)
And a heat recovery means (30) for recovering heat. During cooling operation, the heat recovered by the heat recovery means (30) is supplied to the adsorption refrigerator (20), and the adsorption refrigerator (20) And cooling by a vapor compression heat pump (10),
During the heating operation, heating is performed by heat recovered by the heat recovery means (30) and heat recovered by the outdoor heat exchanger (12).

【0007】これにより、熱回収手段(30)により回
収した熱、及び室外熱交換器(12)にて回収した熱に
より暖房を行うこととなるので、熱回収手段(30)に
より回収した熱を、冷房運転時及び暖房運転時のいずれ
の場合においても有効に利用でき、エネルギー利用率を
高く維持ことができる。
[0007] Thus, since the heating is performed by the heat recovered by the heat recovery means (30) and the heat recovered by the outdoor heat exchanger (12), the heat recovered by the heat recovery means (30) is removed. In both the cooling operation and the heating operation, it can be effectively used, and the energy utilization rate can be maintained high.

【0008】請求項2に記載の発明では、圧縮機(1
1)、室外熱交換器(12)、減圧器(13)及び室内
熱交換器(14)を有する蒸気圧縮式ヒートポンプ(1
0)と、冷媒の蒸発により冷凍能力を発揮し、かつ、そ
の蒸発した冷媒を吸着するとともに、加熱されることに
より吸着していた冷媒を脱離する吸着剤(Si)が収納
された吸着器(21)を有する吸着式冷凍機(20)
と、熱を回収する熱回収手段(30)とを備え、冷房運
転時には、熱回収手段(30)により回収した熱を吸着
式冷凍機(20)に投入して、吸着式冷凍機(20)及
び蒸気圧縮式ヒートポンプ(10)により冷房を行い、
暖房運転時には、熱回収手段(30)により回収した熱
を蒸気圧縮式ヒートポンプ(10)に与えて、その与え
た熱及び室外熱交換器(12)にて回収した熱により暖
房を行うことを特徴とする。
According to the invention described in claim 2, the compressor (1)
1) A vapor compression heat pump (1) having an outdoor heat exchanger (12), a decompressor (13), and an indoor heat exchanger (14).
0), an adsorber that exhibits a refrigerating ability by evaporating the refrigerant, and that stores the adsorbent (Si) that adsorbs the evaporated refrigerant and desorbs the adsorbed refrigerant when heated. Adsorption refrigerator having (21) (20)
And a heat recovery means (30) for recovering heat. During cooling operation, the heat recovered by the heat recovery means (30) is supplied to the adsorption refrigerator (20), and the adsorption refrigerator (20) And cooling by a vapor compression heat pump (10),
During the heating operation, heat recovered by the heat recovery means (30) is supplied to the vapor compression heat pump (10), and heating is performed by the supplied heat and the heat recovered by the outdoor heat exchanger (12). And

【0009】これにより、熱回収手段(30)により回
収した熱、及び室外熱交換器(12)にて回収した熱に
より暖房を行うこととなるので、熱回収手段(30)に
より回収した熱を、冷房運転時及び暖房運転時のいずれ
の場合においても有効に利用でき、エネルギー利用率を
高く維持ことができる。
[0009] Thus, since the heating is performed by the heat recovered by the heat recovery means (30) and the heat recovered by the outdoor heat exchanger (12), the heat recovered by the heat recovery means (30) is recovered. In both the cooling operation and the heating operation, it can be effectively used, and the energy utilization rate can be maintained high.

【0010】請求項3に記載の発明では、圧縮機(1
1)、室外熱交換器(12)、減圧器(13)及び室内
熱交換器(14)を有する蒸気圧縮式ヒートポンプ(1
0)と、冷媒の蒸発により冷凍能力を発揮し、かつ、そ
の蒸発した冷媒を吸着するとともに、加熱されることに
より吸着していた冷媒を脱離する吸着剤(Si)が収納
された吸着器(21)を有する吸着式冷凍機(20)
と、熱を回収する熱回収手段(30)とを備え、冷房運
転時には、熱回収手段(30)により回収した熱を吸着
式冷凍機(20)に投入して吸着式冷凍機(20)にて
蒸気圧縮式ヒートポンプ(10)の高圧側冷媒を冷却
し、暖房運転時には、熱回収手段(30)により回収し
た熱にて蒸気圧縮式ヒートポンプ(10)の低圧側の冷
媒を加熱しながら、蒸気圧縮式ヒートポンプ(10)に
て暖房を行うことを特徴とする。
According to the third aspect of the present invention, the compressor (1
1) A vapor compression heat pump (1) having an outdoor heat exchanger (12), a decompressor (13), and an indoor heat exchanger (14).
0), an adsorber that exhibits a refrigerating ability by evaporating the refrigerant, and that stores the adsorbent (Si) that adsorbs the evaporated refrigerant and desorbs the adsorbed refrigerant when heated. Adsorption refrigerator having (21) (20)
And a heat recovery means (30) for recovering heat. In cooling operation, the heat recovered by the heat recovery means (30) is supplied to the adsorption refrigerator (20) to be supplied to the adsorption refrigerator (20). To cool the high-pressure side refrigerant of the vapor compression heat pump (10) during heating operation, while heating the low pressure side refrigerant of the vapor compression heat pump (10) with heat recovered by the heat recovery means (30). The heating is performed by a compression heat pump (10).

【0011】これにより、熱回収手段(30)により回
収した熱、及び室外熱交換器(12)にて回収した熱に
より暖房を行うこととなるので、熱回収手段(30)に
より回収した熱を、冷房運転時及び暖房運転時のいずれ
の場合においても有効に利用でき、エネルギー利用率を
高く維持ことができる。
[0011] Thus, since the heating is performed by the heat recovered by the heat recovery means (30) and the heat recovered by the outdoor heat exchanger (12), the heat recovered by the heat recovery means (30) is reduced. In both the cooling operation and the heating operation, it can be effectively used, and the energy utilization rate can be maintained high.

【0012】なお、熱回収手段(30)は、請求項4に
記載の発明のごとく、太陽熱を回収する太陽熱集熱器と
することが望ましい。
Preferably, the heat recovery means (30) is a solar heat collector for recovering solar heat, as in the fourth aspect of the present invention.

【0013】因みに、上記各手段の括弧内の符号は、後
述する実施形態に記載の具体的手段との対応関係を示す
一例である。
Incidentally, the reference numerals in parentheses of the above means are examples showing the correspondence with specific means described in the embodiments described later.

【0014】[0014]

【発明の実施の形態】本実施形態は、本発明に係る空調
装置を一般家庭用空調装置に適用したものであって、1
0(太い一転鎖線で囲まれた範囲)は蒸気圧縮式ヒート
ポンプ(蒸気圧縮式冷凍機)であり、20(細い一点鎖
線で囲まれた範囲)は吸着式冷凍機を示している。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In this embodiment, an air conditioner according to the present invention is applied to a general household air conditioner.
0 (range surrounded by a thick chain line) indicates a vapor compression heat pump (vapor compression refrigerator), and 20 (range surrounded by a thin dashed line) indicates an adsorption refrigerator.

【0015】ここで、蒸気圧縮式ヒートポンプ10は、
冷媒を圧縮する圧縮機11、室外空気と冷媒とを熱交換
する室外熱交換器(以下、室外器と略す。)12、冷媒
を減圧膨張させる膨張弁(減圧器)13、室内に吹き出
す空気と冷媒とを熱交換する室内熱交換器(以下、室内
器と略す。)14、冷媒を気相冷媒と液相冷媒とに分離
して余剰冷媒を蓄えるとともに、本実施形態では分離し
た気相冷媒を圧縮機11の吸入側に供給するアキュムレ
ータ15、及び圧縮機11から吐出された冷媒を室外器
12側に流通させる場合と、室内器14側に流通させる
場合とを切り換える四方弁(切り換え手段)16等から
構成されている。
Here, the vapor compression heat pump 10
A compressor 11 for compressing the refrigerant, an outdoor heat exchanger (hereinafter abbreviated as an outdoor unit) 12 for exchanging heat between the outdoor air and the refrigerant, an expansion valve (decompressor) 13 for decompressing and expanding the refrigerant, and air blown into the room. An indoor heat exchanger (hereinafter, abbreviated as an indoor unit) 14 for exchanging heat with the refrigerant, the refrigerant is separated into a gas-phase refrigerant and a liquid-phase refrigerant, and the surplus refrigerant is stored. Accumulator 15 for supplying refrigerant to the suction side of compressor 11 and a four-way valve (switching means) for switching between a case where refrigerant discharged from compressor 11 is circulated to outdoor unit 12 and a case where refrigerant is circulated to indoor unit 14. 16 and the like.

【0016】そして、本実施形態では、圧縮機11、室
外器12、アキュムレータ15、四方弁16、及び室外
器12に空気を送風する送風機12aをケーシング(図
示せず。)に収納して1つのユニット(固まり)とし、
膨張弁13、室内器14及び室内器14に空気を送風す
る送風機14aをケーシング(図示せず。)に収納して
1つのユニット(固まり)としている。以下、圧縮機1
1等からなるユニットを室外ユニット10aと呼び、室
内器14等からなるユニットを室内ユニット10bと呼
ぶ。
In this embodiment, the compressor 11, the outdoor unit 12, the accumulator 15, the four-way valve 16, and the blower 12a that blows air to the outdoor unit 12 are housed in a casing (not shown). Unit (lump)
The expansion valve 13, the indoor unit 14, and the blower 14a for blowing air to the indoor unit 14 are housed in a casing (not shown) to form one unit (lump). Hereinafter, compressor 1
A unit including the indoor unit 14 and the like is referred to as an outdoor unit 10a, and a unit including the indoor unit 14 and the like is referred to as an indoor unit 10b.

【0017】一方、吸着式冷凍機20は、略真空(0.
1mmHg以下)に保たれた容器(吸着器)内の液冷媒
(本実施形態では、水)の蒸発により冷凍能力を発揮す
るものであり、この吸着式冷凍機20には、図2に示す
ように、液冷媒および蒸発した蒸気冷媒を吸着する吸着
剤(本実施形態では、シリカゲル)Siが収納された吸
着器21a、21b、液冷媒Lrと熱交換媒体(本実施
形態では、エチレングリコール系の不凍液が混入された
水)との間で熱交換を行う第1熱交換器22a、22
b、及び吸着剤Siと熱交換媒体との間で熱交換を行う
第2熱交換器23a、23bが設けられている。
On the other hand, the adsorption refrigerator 20 is substantially vacuum (0.
A refrigerant (in the present embodiment, water) in a container (adsorber) kept at 1 mmHg or less) exerts a refrigeration capacity by evaporating. As shown in FIG. Adsorbers (in the present embodiment, silica gel) for adsorbing liquid refrigerant and evaporated vapor refrigerant, adsorbers 21a and 21b, in which liquid refrigerant Lr and a heat exchange medium (in this embodiment, an ethylene glycol-based First heat exchangers 22a, 22 for performing heat exchange with the antifreeze liquid).
b and second heat exchangers 23a and 23b for performing heat exchange between the adsorbent Si and the heat exchange medium.

【0018】なお、以下、吸着器21a、21bを総称
するときは吸着器21と表記し、第1熱交換器22a、
22bを総称するときは第1熱交換器22と表記し、第
2熱交換器23a、23bを総称するときは第2熱交換
器23と表記する。
Hereinafter, when the adsorbers 21a and 21b are collectively referred to as the adsorber 21, the first heat exchanger 22a,
22b is referred to as a first heat exchanger 22, and the second heat exchangers 23a and 23b are referred to as a second heat exchanger 23.

【0019】また、24は、液冷媒Lrの蒸発により第
1熱交換器22にて冷却された熱交換媒体と室外器12
を流出した冷高圧側媒との間で熱交換を行う第3熱交換
器であり、25は吸着剤Siが蒸気冷媒を吸着する際に
発生する熱(吸着熱)を外気中に放熱するための放熱器
である。なお、41〜43は熱交換媒体を循環させる第
1〜3ポンプであり、44〜47は熱交換媒体の循環経
路を切り換える第1〜4四方電磁弁である。
Further, reference numeral 24 denotes a heat exchange medium cooled by the first heat exchanger 22 by evaporation of the liquid refrigerant Lr and the outdoor unit 12.
Is a third heat exchanger that exchanges heat with the cold and high-pressure side medium that has flowed out, and 25 radiates heat (adsorption heat) generated when the adsorbent Si adsorbs the vapor refrigerant into the outside air. Radiator. In addition, 41 to 43 are first to third pumps for circulating the heat exchange medium, and 44 to 47 are first to fourth four-way solenoid valves for switching the circulation path of the heat exchange medium.

【0020】ここで、蒸気圧縮式ヒートポンプ10の高
圧側冷媒とは、圧縮機11から吐出して膨張弁13にて
減圧させる前の冷媒を言い、その圧力は圧縮機11の吐
出圧に略等しい。また、蒸気圧縮式ヒートポンプ10の
低圧側冷媒とは、膨張弁13にて減圧された後、圧縮機
11に吸入される前の冷媒を言い、その圧力は冷媒の蒸
発圧力に略等しい。
Here, the high-pressure side refrigerant of the vapor compression heat pump 10 is a refrigerant discharged from the compressor 11 before being decompressed by the expansion valve 13, and its pressure is substantially equal to the discharge pressure of the compressor 11. . The low-pressure side refrigerant of the vapor compression heat pump 10 refers to a refrigerant that has been decompressed by the expansion valve 13 and has not yet been drawn into the compressor 11, and the pressure thereof is substantially equal to the evaporation pressure of the refrigerant.

【0021】また、図1中、30は太陽熱を回収して熱
交換媒体を加熱する太陽熱集熱器(熱回収手段)であ
り、この太陽熱集熱器30に回収された熱(太陽熱にて
加熱された熱交換媒体)は、後述するように、吸着式冷
凍機20(吸着剤Si)又は第4熱交換器26を介して
蒸気圧縮式ヒートポンプ10に供給される。
In FIG. 1, reference numeral 30 denotes a solar heat collector (heat recovery means) for recovering solar heat and heating the heat exchange medium, and heat collected by the solar heat collector 30 (heating by solar heat). The heat exchange medium thus obtained is supplied to the vapor compression heat pump 10 via the adsorption refrigerator 20 (adsorbent Si) or the fourth heat exchanger 26, as described later.

【0022】このとき、第3、4熱交換器24、26を
流通する熱交換媒体は、室外器12と膨張弁13とを繋
ぐ冷媒配管10dを流通する冷媒と熱交換するように配
設されている。
At this time, the heat exchange medium flowing through the third and fourth heat exchangers 24 and 26 is arranged to exchange heat with the refrigerant flowing through the refrigerant pipe 10d connecting the outdoor unit 12 and the expansion valve 13. ing.

【0023】因みに、27は熱交換媒体が一方向のみに
流通することを許容する逆止弁であり、48は太陽熱集
熱器30にて加熱された熱交換媒体を第4熱交換器26
に供給する場合と、吸着器21(吸着式冷凍機20)に
供給する場合とを切り換える三方切換弁である。
Incidentally, reference numeral 27 denotes a check valve which allows the heat exchange medium to flow in only one direction, and 48 denotes a heat exchange medium heated by the solar heat collector 30 to the fourth heat exchanger 26.
This is a three-way switching valve that switches between supplying to the adsorber 21 and supplying to the adsorber 21 (adsorption refrigerator 20).

【0024】そして、本実施形態では、吸着式冷凍機2
0、第3、4熱交換器24、26、及び室外ユニット1
0aと室内ユニット10bとを繋ぐ冷媒配管10c、1
0dとをケーシング内に収納してユニット化している。
以下、このユニット(太い二点鎖線で囲まれた範囲)2
0aを吸着冷凍ユニット20aと呼ぶ。
In the present embodiment, the adsorption refrigerator 2
0, 3rd, 4th heat exchangers 24, 26, and outdoor unit 1
0a and the refrigerant pipe 10c, which connects the indoor unit 10b, 1
0d is housed in a casing to form a unit.
Hereafter, this unit (range surrounded by a thick two-dot chain line) 2
0a is referred to as an adsorption refrigeration unit 20a.

【0025】次に、本実施形態に係る空調装置の作動を
述べる。
Next, the operation of the air conditioner according to this embodiment will be described.

【0026】1.冷房運転時 圧縮機11を稼働させて蒸気圧縮式ヒートポンプ10を
稼働させるとともに、第1〜3ポンプ41〜43を稼働
させる。
1. During the cooling operation The compressor 11 is operated to operate the vapor compression heat pump 10 and the first to third pumps 41 to 43 are operated.

【0027】このとき、蒸気圧縮式ヒートポンプ10で
は、圧縮機11→四方弁16→室外器12→膨張弁13
→室内器14→アキュムレータ15→圧縮機11の順に
冷媒を循環させる。これにより、室内器14にて室内に
吹き出す空気から熱を奪って蒸発した冷媒は、室外器1
2にて室内に吹き出す空気から奪った熱を放熱して凝縮
する。
At this time, in the vapor compression heat pump 10, the compressor 11 → the four-way valve 16 → the outdoor unit 12 → the expansion valve 13
The refrigerant is circulated in the order of the indoor unit 14 → the accumulator 15 → the compressor 11. As a result, the refrigerant that has taken heat from the air that is blown into the room in the indoor unit 14 and evaporates is removed from the outdoor unit 1.
In step 2, the heat taken from the air blown into the room is radiated and condensed.

【0028】一方、吸着式冷凍機20では、第1〜4四
方電磁弁44〜47及び三方切換弁48を作動させて、
冷凍能力を発揮して吸着状態にある吸着器21(例えば
吸着器21a)の第1熱交換器22(この例では第1熱
交換器22a)と第3熱交換器24との間に熱交換媒体
を循環させて蒸気圧縮式ヒートポンプ10の高圧側冷媒
を冷却するとともに、吸着状態にある吸着器21(この
例では吸着器21a)の第2熱交換器23(この例では
第2熱交換器23a)と放熱器25との間に熱交換媒体
を循環させる。
On the other hand, in the adsorption refrigerator 20, the first to fourth four-way solenoid valves 44 to 47 and the three-way switching valve 48 are operated,
Heat is exchanged between the first heat exchanger 22 (in this example, the first heat exchanger 22a) and the third heat exchanger 24 of the adsorber 21 (for example, the adsorber 21a) in the adsorption state by exhibiting the refrigerating capacity. The medium is circulated to cool the high-pressure side refrigerant of the vapor compression heat pump 10, and the second heat exchanger 23 (the second heat exchanger in this example) of the adsorber 21 (in this example, the adsorber 21a) in the adsorption state. A heat exchange medium is circulated between 23a) and the radiator 25.

【0029】同時に、再生状態(吸着剤Siに吸着した
蒸気冷媒を脱離させる状態)にある吸着器21(この例
では吸着器21b)の第2熱交換器23(この例では第
2熱交換器23b)と太陽熱集熱器30側との間で熱交
換媒体を循環させるとともに、再生状態にある吸着器2
1(この例では吸着器21b)の第1熱交換器22(こ
の例では第1熱交換器22a)と放熱器25との間に熱
交換媒体を循環させる。
At the same time, the second heat exchanger 23 (the second heat exchange in this example) of the adsorber 21 (the adsorber 21b in this example) in the regeneration state (the state in which the vapor refrigerant adsorbed by the adsorbent Si is desorbed). The heat exchange medium is circulated between the heat exchanger 23b) and the solar heat collector 30 side, and the adsorber 2 in the regeneration state is circulated.
The heat exchange medium is circulated between the first heat exchanger 22 (first heat exchanger 22a in this example) of the first heat exchanger 1 (adsorber 21b in this example) and the radiator 25.

【0030】そして、所定時間ごとに、吸着状態にある
吸着器22と再生状態にある吸着器22とを切り換える
運転する。なお、所定時間は、吸着剤Siの吸着能力や
脱離量等を考慮して適宜選定されるものである。
Then, an operation of switching between the adsorber 22 in the adsorption state and the adsorber 22 in the regeneration state is performed at predetermined time intervals. The predetermined time is appropriately selected in consideration of the adsorbing capacity of the adsorbent Si and the amount of desorption.

【0031】2.暖房運転時 圧縮機11を稼働させて蒸気圧縮式ヒートポンプ10を
稼働させるとともに、第2ポンプ42を稼働させる。
2. During the heating operation, the compressor 11 is operated to operate the vapor compression heat pump 10 and the second pump 42 is operated.

【0032】このとき、蒸気圧縮式ヒートポンプ10で
は、圧縮機11→四方弁16→室内器14→膨張弁13
→室外器12→アキュムレータ15→圧縮機11の順に
冷媒を循環させる。これにより、室外器12にて外気か
ら熱を奪って蒸発した冷媒は、室内器14にて外気から
奪った熱を室内に吹き出す空気に放熱して凝縮する。
At this time, in the vapor compression heat pump 10, the compressor 11 → the four-way valve 16 → the indoor unit 14 → the expansion valve 13
The refrigerant is circulated in the order of → the outdoor unit 12 → the accumulator 15 → the compressor 11. Thus, the refrigerant that has taken heat from the outside air and evaporated in the outdoor unit 12 radiates the heat taken from the outside air in the indoor unit 14 to the air that is blown into the room and condenses.

【0033】一方、吸着式冷凍機20は停止させるとと
もに、三方切換弁48を作動させて、太陽熱集熱器30
に回収された熱(太陽熱にて加熱された熱交換媒体)を
第4熱交換器26に供給して蒸気圧縮式ヒートポンプ1
0の低圧側冷媒を加熱する。
On the other hand, the adsorption type refrigerator 20 is stopped, and the three-way switching valve 48 is operated to operate the solar heat collector 30.
The heat (heat exchange medium heated by solar heat) recovered to the fourth heat exchanger 26 is supplied to the vapor compression heat pump 1
0 low-pressure side refrigerant is heated.

【0034】次に、本実施形態の特徴(作用効果)を述
べる。
Next, the features (effects) of this embodiment will be described.

【0035】本実施形態によれば、冷房運転時には、太
陽熱集熱器30により回収した熱を吸着式冷凍機20に
投入して着式冷凍機20にて蒸気圧縮式ヒートポンプ1
0の高圧側冷媒を冷却するので、吸着式冷凍機20及び
蒸気圧縮式ヒートポンプ10の両者により冷房を行うこ
ととなる。
According to the present embodiment, during the cooling operation, the heat recovered by the solar heat collector 30 is supplied to the adsorption refrigerator 20, and the vapor compression heat pump 1 is
Since the high pressure side refrigerant of 0 is cooled, cooling is performed by both the adsorption refrigerator 20 and the vapor compression heat pump 10.

【0036】したがって、蒸気圧縮式ヒートポンプ10
単独で冷房を行う場合に比べて、蒸気圧縮式ヒートポン
プ10の高圧側冷媒圧力が上昇してしまうことを抑制し
つつ、少ない消費動力にて冷房運転を行うことができ
る。
Therefore, the vapor compression heat pump 10
Compared with the case where cooling is performed alone, the cooling operation can be performed with less power consumption while suppressing the increase in the high-pressure side refrigerant pressure of the vapor compression heat pump 10.

【0037】また、暖房運転時には、太陽熱集熱器30
により回収した熱にて蒸気圧縮式ヒートポンプ10の低
圧側冷媒を加熱しながら、蒸気圧縮式ヒートポンプ10
にて暖房を行うので、太陽熱集熱器30により回収した
熱を蒸気圧縮式ヒートポンプ10に与えて、その与えた
熱及び室外器12にて回収した熱により暖房を行うこと
となる。
During the heating operation, the solar heat collector 30
While heating the low pressure side refrigerant of the vapor compression heat pump 10 with the heat recovered by
In this case, the heat recovered by the solar heat collector 30 is supplied to the vapor compression heat pump 10, and heating is performed by the supplied heat and the heat recovered by the outdoor unit 12.

【0038】したがって、暖房運転時には、太陽熱集熱
器30により回収した熱、及び室外器12にて回収した
熱により暖房を行うこととなるので、蒸気圧縮式ヒート
ポンプ10単独で暖房を行う場合に比べて、少ない消費
動力にて暖房運転を行うことができる。延いては、冷房
運転時及び暖房運転時のいずれの場合においてもエネル
ギー利用率を高く維持することができる。
Therefore, during the heating operation, the heating is performed by the heat recovered by the solar heat collector 30 and the heat recovered by the outdoor unit 12, so that the heating is performed in comparison with the case of performing the heating by the vapor compression heat pump 10 alone. Thus, the heating operation can be performed with less power consumption. As a result, the energy utilization rate can be kept high in both the cooling operation and the heating operation.

【0039】ところで、本実施形態では、吸着式冷凍機
20、第3、4熱交換器24、26、及び室外ユニット
10aと室内ユニット10bとを繋ぐ冷媒配管10c、
10dとをケーシング内に収納して吸着冷凍ユニット2
0aを構成しているので、図3に示すように、吸着冷凍
ユニット20aの個数を容易に増減することができる。
In the present embodiment, the adsorption refrigerator 20, the third and fourth heat exchangers 24 and 26, and the refrigerant pipe 10c connecting the outdoor unit 10a and the indoor unit 10b,
10d is stored in a casing, and the adsorption refrigeration unit 2
0a, the number of adsorption refrigeration units 20a can be easily increased or decreased as shown in FIG.

【0040】したがって、吸着冷凍ユニット20aの個
数を調節することにより、容易に吸着式冷凍機20側の
能力(冷凍能力)を調節することができるので、異なる
仕様の空調装置に対して、大幅な設計変更を行うことな
く安価に対応することができる。
Therefore, by adjusting the number of the adsorption refrigeration units 20a, it is possible to easily adjust the capacity (refrigeration capacity) of the adsorption chiller 20 side. It is possible to cope cheaply without changing the design.

【0041】(その他の実施形態)上述の実施形態で
は、吸着剤Siとしてシリカゲルを用いたが、本発明は
これに限定されるものではなく、吸着剤Siとして活性
炭、ゼオライト、活性アルミナなどを用いてもよい。
(Other Embodiments) In the above embodiment, silica gel was used as the adsorbent Si. However, the present invention is not limited to this, and activated carbon, zeolite, activated alumina, etc. were used as the adsorbent Si. You may.

【0042】また、上述の実施形態では、液冷媒として
水を用いたが、本発明はこれに限定されるものではな
く、アルコール、フロンなど吸着剤Siに吸着されるも
のであれば、その他の物であってもよい。
In the above-described embodiment, water is used as the liquid refrigerant. However, the present invention is not limited to this, and other liquids may be used as long as they are adsorbed by the adsorbent Si such as alcohol and chlorofluorocarbon. It may be a thing.

【0043】また、上述の実施形態では、暖房運転時
に、低圧側冷媒のうち室外器12に流入する前の冷媒を
太陽熱集熱器30にて回収した熱により加熱したが、本
発明はこれに限定されるものではなく、例えば室外器1
2から流入した冷媒を太陽熱集熱器30にて回収した熱
により加熱してもよい。
In the above-described embodiment, during the heating operation, the refrigerant of the low-pressure side refrigerant before flowing into the outdoor unit 12 is heated by the heat recovered by the solar heat collector 30, but the present invention applies to this. It is not limited, for example, the outdoor unit 1
The refrigerant flowing from 2 may be heated by the heat recovered by the solar heat collector 30.

【0044】また、上述の実施形態では、熱回収手段と
して太陽熱集熱器30を用いたが、本実施形態はこれに
限定されるものではなく、河川、地熱、太陽熱等の自然
界に存在する自然熱エネルギー、又は発電機のエンジン
や燃料電池等の機器からの廃熱を回収することにより熱
回収手段を構成してもよい。
Further, in the above-described embodiment, the solar heat collector 30 is used as the heat recovery means. However, the present embodiment is not limited to this, and natural heat existing in the natural world such as rivers, geothermal heat, solar heat, etc. The heat recovery means may be configured by recovering thermal energy or waste heat from a generator engine or a fuel cell or the like.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施形態に係る空調装置の模式図であ
る。
FIG. 1 is a schematic diagram of an air conditioner according to an embodiment of the present invention.

【図2】本発明の実施形態に係る吸着冷凍ユニットの模
式図である。
FIG. 2 is a schematic diagram of an adsorption refrigeration unit according to an embodiment of the present invention.

【図3】本発明の実施形態に係る空調装置の変形例を示
す模式図である。
FIG. 3 is a schematic diagram showing a modification of the air conditioner according to the embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10…蒸気圧縮式ヒートポンプ、10a…室外ユニッ
ト、10b…室内ユニット、20…吸着式冷凍機、20
a…吸着冷凍ユニット、21…吸着器、24…第3熱交
換器、26…第4熱交換器、30…太陽熱集熱器(熱回
収手段)。
DESCRIPTION OF SYMBOLS 10 ... Vapor compression heat pump, 10a ... Outdoor unit, 10b ... Indoor unit, 20 ... Adsorption type refrigerator, 20
a: adsorption refrigeration unit, 21: adsorber, 24: third heat exchanger, 26: fourth heat exchanger, 30: solar heat collector (heat recovery means).

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 圧縮機(11)、室外熱交換器(1
2)、減圧器(13)及び室内熱交換器(14)を有す
る蒸気圧縮式ヒートポンプ(10)と、 冷媒の蒸発により冷凍能力を発揮し、かつ、その蒸発し
た冷媒を吸着するとともに、加熱されることにより吸着
していた冷媒を脱離する吸着剤(Si)が収納された吸
着器(21)を有する吸着式冷凍機(20)と、 熱を回収する熱回収手段(30)とを備え、 冷房運転時には、前記熱回収手段(30)により回収し
た熱を前記吸着式冷凍機(20)に投入して、前記吸着
式冷凍機(20)及び前記蒸気圧縮式ヒートポンプ(1
0)により冷房を行い、 暖房運転時には、前記熱回収手段(30)により回収し
た熱、及び前記室外熱交換器(12)にて回収した熱に
より暖房を行うことを特徴とする空調装置。
A compressor (11), an outdoor heat exchanger (1)
2) a vapor compression heat pump (10) having a decompressor (13) and an indoor heat exchanger (14); exhibits a refrigerating ability by evaporating the refrigerant, adsorbs the evaporated refrigerant, and is heated. An adsorbent refrigerator (20) having an adsorber (21) containing an adsorbent (Si) for desorbing a refrigerant adsorbed by the heat exchanger, and a heat recovery means (30) for recovering heat. During the cooling operation, the heat recovered by the heat recovery means (30) is supplied to the adsorption refrigerator (20), and the adsorption refrigerator (20) and the vapor compression heat pump (1) are supplied.
The air conditioner according to claim 1, wherein cooling is performed by 0), and during heating operation, heating is performed by heat recovered by the heat recovery means (30) and heat recovered by the outdoor heat exchanger (12).
【請求項2】 圧縮機(11)、室外熱交換器(1
2)、減圧器(13)及び室内熱交換器(14)を有す
る蒸気圧縮式ヒートポンプ(10)と、 冷媒の蒸発により冷凍能力を発揮し、かつ、その蒸発し
た冷媒を吸着するとともに、加熱されることにより吸着
していた冷媒を脱離する吸着剤(Si)が収納された吸
着器(21)を有する吸着式冷凍機(20)と、 熱を回収する熱回収手段(30)とを備え、 冷房運転時には、前記熱回収手段(30)により回収し
た熱を前記吸着式冷凍機(20)に投入して、前記吸着
式冷凍機(20)及び前記蒸気圧縮式ヒートポンプ(1
0)により冷房を行い、 暖房運転時には、前記熱回収手段(30)により回収し
た熱を前記蒸気圧縮式ヒートポンプ(10)に与えて、
その与えた熱及び前記室外熱交換器(12)にて回収し
た熱により暖房を行うことを特徴とする空調装置。
2. A compressor (11) and an outdoor heat exchanger (1).
2) a vapor compression heat pump (10) having a decompressor (13) and an indoor heat exchanger (14); exhibits a refrigerating ability by evaporating the refrigerant, adsorbs the evaporated refrigerant, and is heated. An adsorbent refrigerator (20) having an adsorber (21) containing an adsorbent (Si) for desorbing a refrigerant adsorbed by the heat exchanger, and a heat recovery means (30) for recovering heat. During the cooling operation, the heat recovered by the heat recovery means (30) is supplied to the adsorption refrigerator (20), and the adsorption refrigerator (20) and the vapor compression heat pump (1) are supplied.
0), cooling is performed, and during the heating operation, the heat recovered by the heat recovery means (30) is given to the vapor compression heat pump (10),
An air conditioner characterized by heating by the applied heat and the heat recovered by the outdoor heat exchanger (12).
【請求項3】 圧縮機(11)、室外熱交換器(1
2)、減圧器(13)及び室内熱交換器(14)を有す
る蒸気圧縮式ヒートポンプ(10)と、 冷媒の蒸発により冷凍能力を発揮し、かつ、その蒸発し
た冷媒を吸着するとともに、加熱されることにより吸着
していた冷媒を脱離する吸着剤(Si)が収納された吸
着器(21)を有する吸着式冷凍機(20)と、 熱を回収する熱回収手段(30)とを備え、 冷房運転時には、前記熱回収手段(30)により回収し
た熱を前記吸着式冷凍機(20)に投入して前記吸着式
冷凍機(20)にて前記蒸気圧縮式ヒートポンプ(1
0)の高圧側冷媒を冷却し、 暖房運転時には、前記熱回収手段(30)により回収し
た熱にて前記蒸気圧縮式ヒートポンプ(10)の低圧側
の冷媒を加熱しながら、蒸気圧縮式ヒートポンプ(1
0)にて暖房を行うことを特徴とする空調装置。
3. A compressor (11), an outdoor heat exchanger (1).
2) a vapor compression heat pump (10) having a decompressor (13) and an indoor heat exchanger (14); exhibits a refrigerating ability by evaporating the refrigerant, adsorbs the evaporated refrigerant, and is heated. An adsorbent refrigerator (20) having an adsorber (21) containing an adsorbent (Si) for desorbing a refrigerant adsorbed by the heat exchanger, and a heat recovery means (30) for recovering heat. During the cooling operation, the heat recovered by the heat recovery means (30) is supplied to the adsorption refrigerator (20), and the vapor compression heat pump (1) is supplied to the adsorption refrigerator (20).
0), the high-pressure side refrigerant is cooled. During the heating operation, the low-pressure side refrigerant of the vapor compression heat pump (10) is heated by the heat recovered by the heat recovery means (30). 1
An air conditioner characterized by performing heating in 0).
【請求項4】 前記熱回収手段(30)は、太陽熱を回
収する太陽熱集熱器であることを特徴とする請求項1な
いし3のいずれか1つに記載の空調装置。
4. An air conditioner according to claim 1, wherein said heat recovery means is a solar heat collector for recovering solar heat.
JP2001048708A 2001-02-23 2001-02-23 Air conditioner Withdrawn JP2002250573A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001048708A JP2002250573A (en) 2001-02-23 2001-02-23 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001048708A JP2002250573A (en) 2001-02-23 2001-02-23 Air conditioner

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Publication Number Publication Date
JP2002250573A true JP2002250573A (en) 2002-09-06

Family

ID=18909931

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002250573A (en)

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CN102003830A (en) * 2010-11-05 2011-04-06 中国科学院广州能源研究所 Adsorption type refrigerator and compression type air-conditioner combined system
CN102116539A (en) * 2011-03-31 2011-07-06 中国科学院广州能源研究所 Adsorption and compression composite heat pump system driven by multiple heat sources
CN101776349B (en) * 2010-02-02 2011-11-16 浙江大学 Continuous solar pump-free auto-cascade absorption type refrigerating system
CN102252480A (en) * 2011-05-19 2011-11-23 河南新飞电器有限公司 Solar energy refrigerator
CN102635975A (en) * 2012-05-14 2012-08-15 上海理工大学 Household cold and hot integrated machine with auxiliary power generating and heating by solar photovoltaic battery
CN102788446A (en) * 2012-08-30 2012-11-21 华北电力大学(保定) Adsorption type auxiliary heat pump refrigerating system driven by condensation heat
US8479529B2 (en) 2007-08-09 2013-07-09 Millennium Energy Industries, Incorporated Two-stage low temperature air cooled adsorption cooling unit
JP2016148475A (en) * 2015-02-12 2016-08-18 株式会社 大阪テクノクラート Hybrid air conditioning system

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