JP2003285633A - Air conditioning apparatus for vehicle - Google Patents
Air conditioning apparatus for vehicleInfo
- Publication number
- JP2003285633A JP2003285633A JP2002093768A JP2002093768A JP2003285633A JP 2003285633 A JP2003285633 A JP 2003285633A JP 2002093768 A JP2002093768 A JP 2002093768A JP 2002093768 A JP2002093768 A JP 2002093768A JP 2003285633 A JP2003285633 A JP 2003285633A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- evaporator
- compressor
- cold storage
- heat exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000004378 air conditioning Methods 0.000 title claims abstract description 42
- 239000003507 refrigerant Substances 0.000 claims abstract description 422
- 239000007788 liquid Substances 0.000 claims abstract description 88
- 239000011232 storage material Substances 0.000 claims description 42
- 239000012808 vapor phase Substances 0.000 claims description 17
- 239000012071 phase Substances 0.000 claims description 16
- 230000006837 decompression Effects 0.000 claims description 7
- 238000001704 evaporation Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 abstract description 163
- 239000000463 material Substances 0.000 abstract description 27
- 230000005855 radiation Effects 0.000 abstract description 2
- 238000009423 ventilation Methods 0.000 abstract 1
- 238000005057 refrigeration Methods 0.000 description 27
- 238000010586 diagram Methods 0.000 description 12
- 238000007711 solidification Methods 0.000 description 11
- 230000008023 solidification Effects 0.000 description 11
- 230000009471 action Effects 0.000 description 10
- 230000007423 decrease Effects 0.000 description 10
- 230000008014 freezing Effects 0.000 description 10
- 238000007710 freezing Methods 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 239000007791 liquid phase Substances 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000004781 supercooling Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 239000013526 supercooled liquid Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Landscapes
- Air-Conditioning For Vehicles (AREA)
- Air Conditioning Control Device (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、停車時等に圧縮機
の駆動源である車両エンジンを一時的に停止させる車両
に適用される蓄冷式の車両用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 a cold storage type air conditioner for a vehicle which is applied to a vehicle in which a vehicle engine, which is a drive source of a compressor, is temporarily stopped when the vehicle is stopped.
【0002】[0002]
【従来の技術】近年、環境保護、車両エンジンの燃費向
上等を目的にして、信号待ち等の停車時に車両エンジン
を自動的に停止する車両(ハイブリッド車等のエコラン
車)が実用化されており、今後、停車時に車両エンジン
を停止する車両が増加する傾向にある。2. Description of the Related Art In recent years, a vehicle (eco-run vehicle such as a hybrid vehicle) in which a vehicle engine is automatically stopped when a vehicle is stopped such as waiting for a signal has been put into practical use for the purpose of environmental protection and improvement of fuel consumption of the vehicle engine. , In the future, the number of vehicles that stop the vehicle engine when the vehicle is stopped tends to increase.
【0003】ところで、車両用空調装置においては、冷
凍サイクルの圧縮機を車両エンジンにより駆動している
ので、上記エコラン車においては信号待ち等で停車し
て、車両エンジンが停止される毎に、圧縮機も停止して
冷房用蒸発器の温度が上昇し、車室内への吹出空気温度
が上昇するので、乗員の冷房フィーリングを損なうとい
う不具合が発生する。By the way, in the vehicle air conditioner, the compressor of the refrigeration cycle is driven by the vehicle engine. Therefore, in the above eco-run vehicle, the vehicle is stopped by waiting for a signal or the like and is compressed every time the vehicle engine is stopped. The air conditioner also stops, the temperature of the cooling evaporator rises, and the temperature of the air blown into the passenger compartment rises, which impairs the cooling feeling of the passengers.
【0004】そこで、車両エンジン(圧縮機)の稼働時
に蓄冷される蓄冷手段を備え、車両エンジン(圧縮機)
が停止して蒸発器の冷却作用が停止したときには蓄冷手
段の蓄冷熱量を使用して車室内への吹出空気を冷却でき
る蓄冷式の車両用空調装置の必要性が高まっている。Therefore, the vehicle engine (compressor) is provided with a cool storage means for storing cold when the vehicle engine (compressor) is operating.
There is a growing need for a regenerative vehicle air conditioner that can cool the air blown into the vehicle compartment by using the amount of stored heat of the regenerator when the cooling action of the evaporator is stopped.
【0005】この種の蓄冷式の車両用空調装置として、
従来、特開2000−313226号公報に記載された
ものが知られている。この従来技術では、図13に示す
ように車両エンジンにより駆動される圧縮機1を有する
空調用冷凍サイクルRにおいて、車室内への吹出空気を
冷却する蒸発器8と並列に蓄冷材40aを内蔵する蓄冷
熱交換器40を設けている。As a cold storage type vehicle air conditioner of this type,
Conventionally, the one described in Japanese Patent Laid-Open No. 2000-313226 is known. In this conventional technique, in a refrigeration cycle for air conditioning R having a compressor 1 driven by a vehicle engine as shown in FIG. 13, a cool storage material 40a is built in parallel with an evaporator 8 for cooling blown air into the vehicle interior. A cold storage heat exchanger 40 is provided.
【0006】そして、車両エンジン(圧縮機1)の稼働
時に蓄冷を行う時は電磁弁41を開弁して、膨張弁6に
より減圧された低圧冷媒を蒸発器8と蓄冷熱交換器40
に並列に流して蓄冷材40aを冷却し、蓄冷材40aへ
の蓄冷を行う。When cold storage is performed when the vehicle engine (compressor 1) is in operation, the solenoid valve 41 is opened, and the low-pressure refrigerant decompressed by the expansion valve 6 is cooled by the evaporator 8 and the cold storage heat exchanger 40.
In parallel to cool the regenerator material 40a to cool the regenerator material 40a.
【0007】そして、車両エンジンの停止により圧縮機
1が停止した時には電動ポンプ42を作動させて、蓄液
タンク43→電磁弁41→電動ポンプ42→蓄冷熱交換
器40→蒸発器8→蓄液タンク43の閉回路にて冷媒を
循環させる。蒸発器8で蒸発した気相冷媒を蓄冷熱交換
器40において蓄冷材40aの蓄冷熱量により凝縮し、
この凝縮後の液冷媒を蒸発器8に循環させる。これによ
り、蒸発器8の冷却作用を圧縮機1の停止時にも続行し
て車室内の冷房機能を発揮できるようにしている。When the compressor 1 is stopped due to the stop of the vehicle engine, the electric pump 42 is operated, and the liquid storage tank 43 → the solenoid valve 41 → the electric pump 42 → the cold storage heat exchanger 40 → the evaporator 8 → the liquid storage. The refrigerant is circulated in the closed circuit of the tank 43. The vapor-phase refrigerant evaporated in the evaporator 8 is condensed in the cold storage heat exchanger 40 by the amount of cold storage heat of the cold storage material 40a,
The condensed liquid refrigerant is circulated to the evaporator 8. As a result, the cooling action of the evaporator 8 is continued even when the compressor 1 is stopped so that the cooling function of the vehicle interior can be exhibited.
【0008】[0008]
【発明が解決しようとする課題】ところで、上記したよ
うに従来技術では、圧縮機1の稼働時には膨張弁7から
蓄液タンク43、蒸発器8を通過して圧縮機1の吸入側
へ向かう方向に冷媒が流れる。これに反し、圧縮機1の
停止時(放冷冷房時)には圧縮機1の吸入側から蒸発器
8を通過して蓄液タンク43側へ向かう方向、すなわ
ち、圧縮機稼働時と逆方向に冷媒が流れる。As described above, in the prior art, when the compressor 1 is in operation, the direction from the expansion valve 7 through the liquid storage tank 43 and the evaporator 8 toward the suction side of the compressor 1. Refrigerant flows into. On the contrary, when the compressor 1 is stopped (during cooling and cooling), the direction from the suction side of the compressor 1 to the liquid storage tank 43 side through the evaporator 8, that is, the direction opposite to the operation direction of the compressor. Refrigerant flows into.
【0009】このように、圧縮機1の稼働時と停止時と
で蒸発器8の冷媒流れ方向が逆転するので、蒸発器8に
おける熱交換性能が変動する。そのため、蒸発器熱交換
性能を圧縮機1の稼働時、圧縮機停止時の双方で高い状
態に維持できないという不具合が生じる。In this way, the refrigerant flow direction of the evaporator 8 is reversed when the compressor 1 is operating and when it is stopped, so that the heat exchange performance of the evaporator 8 varies. Therefore, the evaporator heat exchange performance cannot be maintained in a high state both when the compressor 1 is operating and when the compressor is stopped.
【0010】この不具合を図14に示す蒸発器8の具体
的な冷媒流路構成に基づいて説明する。図14は蒸発器
8の冷媒流路構成の具体的一例を示すものであり、特開
平9−170850号公報記載の冷媒流路構成である。
この公報記載のものは直交流と対向流とを組み合わせた
冷媒流路構成により蒸発器8の熱交換効率の向上を図っ
ている。This inconvenience will be described with reference to the concrete refrigerant flow path structure of the evaporator 8 shown in FIG. FIG. 14 shows a specific example of the refrigerant channel structure of the evaporator 8, which is the refrigerant channel structure described in JP-A-9-170850.
The one described in this publication is intended to improve the heat exchange efficiency of the evaporator 8 by a refrigerant flow path configuration in which a cross flow and a counter flow are combined.
【0011】すなわち、図14において、蒸発器8は空
気流れ方向Aの風下側に冷媒入口側熱交換部81を配置
し、空気流れ方向Aの風上側に冷媒出口側熱交換部82
を配置している。そして、冷媒入口側熱交換部81にお
いては、蒸発器8の左右両側の側面部のうち、一方(右
側)の側面部83aに冷媒入口84を配置し、この冷媒
入口84から冷媒を矢印B1のように下側タンク部85
の右側空間85a内に流入する。ここで、下側タンク部
85の内部空間は仕切り板86により右側空間85aと
左側空間85bとに仕切られている。That is, in FIG. 14, the evaporator 8 has a refrigerant inlet side heat exchange section 81 arranged on the lee side in the air flow direction A, and a refrigerant outlet side heat exchange section 82 on the windward side in the air flow direction A.
Are arranged. Then, in the refrigerant inlet side heat exchange section 81, the refrigerant inlet 84 is arranged on one (right) side surface portion 83a of the left and right side surfaces of the evaporator 8, and the refrigerant is fed from the refrigerant inlet 84 in the direction of the arrow B1. Lower tank part 85
Flows into the right side space 85a. Here, the inner space of the lower tank portion 85 is partitioned by a partition plate 86 into a right space 85a and a left space 85b.
【0012】冷媒は下側タンク部85の右側空間85a
から冷媒入口側熱交換部81の右側冷媒流路81aを上
昇して上側タンク部87に至る。この上側タンク部87
内には仕切り板が設けてないので、この上側タンク部8
7内を冷媒は矢印B2のように左側へ流れる。The refrigerant is the right space 85a of the lower tank portion 85.
From the upper side to the upper tank portion 87 by ascending in the right side refrigerant flow passage 81 a of the refrigerant inlet side heat exchange portion 81. This upper tank part 87
Since there is no partition plate inside, the upper tank 8
The refrigerant flows to the left in 7 as indicated by arrow B2.
【0013】次に、冷媒は冷媒入口側熱交換部81の左
側冷媒流路81bを下降して下側タンク部85の左側空
間85bに至り、この左側空間85bを矢印B3のよう
に左側へ冷媒が流れる。Next, the refrigerant descends through the left side refrigerant flow passage 81b of the refrigerant inlet side heat exchange section 81 to reach the left side space 85b of the lower tank section 85, and the left side space 85b is directed to the left side as indicated by arrow B3. Flows.
【0014】蒸発器8の左右両側の側面部のうち、他方
(左側)の側面部83bには側面冷媒流路88が形成し
てあり、下側タンク部85の左側端部はこの側面冷媒流
路88の下端部に連通している。そして、この側面冷媒
流路88の上端部は冷媒出口側熱交換部82の上側タン
ク部89の左側空間89aに連通しているので、冷媒は
は側面冷媒流路88を通過して左側空間89aに流入
し、左側空間89aを矢印B4のように右側へ流れる。Of the left and right side surfaces of the evaporator 8, a side surface refrigerant passage 88 is formed in the other (left side) side surface portion 83b, and the left side end portion of the lower tank portion 85 has this side surface refrigerant flow. It communicates with the lower end of the passage 88. Since the upper end portion of the side surface refrigerant passage 88 communicates with the left side space 89a of the upper tank portion 89 of the refrigerant outlet side heat exchange portion 82, the refrigerant passes through the side surface refrigerant passage 88 and the left side space 89a. And flows to the right through the left space 89a as indicated by arrow B4.
【0015】ここで、上側タンク部89の内部空間は仕
切り板90により左側空間89aと右側空間89bとに
仕切られている。このため、上側タンク部89の左側空
間89a内の冷媒は次に、冷媒出口側熱交換部82の左
側冷媒流路82aを下降して下側タンク部91内に至
る。Here, the inner space of the upper tank portion 89 is partitioned by a partition plate 90 into a left space 89a and a right space 89b. Therefore, the refrigerant in the left space 89a of the upper tank portion 89 next descends in the left refrigerant passage 82a of the refrigerant outlet side heat exchange portion 82 and reaches the lower tank portion 91.
【0016】この下側タンク部91内には仕切り板が設
けてないので、冷媒は下側タンク部91内を矢印B5の
ように右側へ流れる。下側タンク部91の右側領域から
冷媒は冷媒出口側熱交換部82の右側冷媒流路82bを
上昇して上側タンク部89の右側空間89bに至る。こ
の右側空間89bには蒸発器8の一方(右側)の側面部
83aに配置した冷媒出口92が連通しているので、右
側空間89bの冷媒は冷媒出口92から蒸発器8の外部
へ流出する。Since no partition plate is provided in the lower tank portion 91, the refrigerant flows rightward in the lower tank portion 91 as indicated by arrow B5. From the right side area of the lower tank section 91, the refrigerant rises in the right side refrigerant flow path 82b of the refrigerant outlet side heat exchange section 82 and reaches the right side space 89b of the upper tank section 89. Since the right side space 89b is communicated with the refrigerant outlet 92 arranged on one side surface (right side) 83a of the evaporator 8, the refrigerant in the right side space 89b flows out of the evaporator 8 through the refrigerant outlet 92.
【0017】なお、各冷媒流路81a、81b、82
a、82bは模式的に図示したが、実際にはいずれも並
列配置された複数のチューブにより構成される。このチ
ューブは周知のようにアルミニウム等の金属薄板の貼り
合わせ構造にて構成される。The respective refrigerant flow paths 81a, 81b, 82
Although a and 82b are shown schematically, in reality, each is composed of a plurality of tubes arranged in parallel. As is well known, this tube has a laminated structure of thin metal plates such as aluminum.
【0018】図14の蒸発器冷媒流路構成では、冷媒入
口側熱交換部81および冷媒出口側熱交換部82におけ
る冷媒流れ方向(蒸発器8の左右方向)に対して空気が
直交する方向Aに流れて、直交流の冷媒流路構成となっ
ている。そして、空気流れ方向Aの風下側に冷媒入口側
熱交換部81を配置し、空気流れ方向Aの風上側に冷媒
出口側熱交換部82を配置することにより、対向流の冷
媒流路構成となっている。In the evaporator refrigerant flow passage configuration of FIG. 14, air is orthogonal to the refrigerant flow direction in the refrigerant inlet side heat exchange section 81 and the refrigerant outlet side heat exchange section 82 (the lateral direction of the evaporator 8). And has a cross-flow refrigerant flow path configuration. Then, the refrigerant inlet side heat exchange section 81 is arranged on the leeward side in the air flow direction A, and the refrigerant outlet side heat exchange section 82 is arranged on the windward side in the air flow direction A, thereby forming a counterflow refrigerant flow path configuration. Has become.
【0019】蒸発器上流側に配置される減圧装置は、通
常、温度式膨張弁7(図13)で構成され、この温度式
膨張弁7により蒸発器出口冷媒が所定の過熱度となるよ
うにサイクル循環冷媒流量が調整される。そのため、蒸
発器8ではその冷媒出口側領域に冷媒の過熱域が形成さ
れ、蒸発器8の出口側冷媒温度が入口側冷媒温度よりも
高くなる。The pressure reducing device arranged on the upstream side of the evaporator is usually constituted by a temperature type expansion valve 7 (FIG. 13) so that the refrigerant at the outlet of the evaporator has a predetermined superheat degree. The cycle circulation refrigerant flow rate is adjusted. Therefore, in the evaporator 8, a refrigerant superheat region is formed in the refrigerant outlet side region thereof, and the outlet side refrigerant temperature of the evaporator 8 becomes higher than the inlet side refrigerant temperature.
【0020】従って、上記のように空気流れ方向Aに対
して対向流の冷媒流路を構成することにより、冷媒入口
側熱交換部81および冷媒出口側熱交換部82の双方に
おいて空気と冷媒との温度差を大きくして、蒸発器8の
熱交換性能を向上できる。Therefore, by constructing the counter-flow refrigerant passage in the air flow direction A as described above, the air and the refrigerant are exchanged in both the refrigerant inlet side heat exchange section 81 and the refrigerant outlet side heat exchange section 82. It is possible to improve the heat exchange performance of the evaporator 8 by increasing the temperature difference.
【0021】また、蒸発器8の冷媒流路構成では、冷媒
入口側から冷媒出口側へ向かうにつれて冷媒の蒸発が次
第に進行し、気相冷媒の比率(乾き度)が増大するの
で、冷媒出口側流路では冷媒流速の上昇による圧損の増
大が顕著となる。そこで、この圧損増大を低減するため
に、冷媒入口側熱交換部81の冷媒流路81a、81b
に比較して冷媒出口側熱交換部82の冷媒流路82a、
82bの流路断面積を大きくするように設計している。Further, in the refrigerant flow path configuration of the evaporator 8, the evaporation of the refrigerant gradually progresses from the refrigerant inlet side to the refrigerant outlet side, and the ratio (dryness) of the vapor phase refrigerant increases, so that the refrigerant outlet side. The increase in pressure loss due to the increase in the flow velocity of the refrigerant becomes remarkable in the flow passage. Therefore, in order to reduce this increase in pressure loss, the refrigerant flow paths 81a and 81b of the refrigerant inlet side heat exchange section 81 are reduced.
The refrigerant flow path 82a of the refrigerant outlet side heat exchange section 82,
It is designed to increase the flow passage cross-sectional area of 82b.
【0022】従って、圧縮機稼働時(通常冷房・蓄冷
時)において蒸発器8に冷媒が図14の冷媒流れ方向で
流れるように設定すると、図13の従来技術では圧縮機
停止時(放冷冷房時)に蒸発器8に冷媒が逆方向に流れ
るので、空気流れの風上側に入口側冷媒流路が位置し、
空気流れの風下側に出口側冷媒流路が位置して、並行流
の状態となる。そのため、出口側冷媒流路では空気と冷
媒との温度差が大幅に減少し、熱交換性能が大幅に低下
する。Therefore, if the refrigerant is set to flow in the evaporator 8 in the refrigerant flow direction shown in FIG. 14 when the compressor is operating (normal cooling / storage), in the prior art shown in FIG. 13, when the compressor is stopped (cooling and cooling). Since the refrigerant flows to the evaporator 8 in the opposite direction, the inlet-side refrigerant flow path is located on the windward side of the air flow,
The outlet side refrigerant flow path is located on the leeward side of the air flow, and a parallel flow state is established. Therefore, the temperature difference between the air and the refrigerant in the outlet-side refrigerant flow channel is significantly reduced, and the heat exchange performance is significantly reduced.
【0023】また、圧縮機停止時(放冷冷房時)には流
路断面積の大きい冷媒流路が冷媒入口側となり、流路断
面積の小さい冷媒流路が冷媒出口側となるので、蒸発器
8の圧損が圧縮機稼働時に比較して大幅に増大し、その
結果、蒸発器8への冷媒循環流量が減少し、熱交換性能
が更に低下する。Further, when the compressor is stopped (during cooling and cooling), the refrigerant flow passage having a large flow passage cross-sectional area is on the refrigerant inlet side, and the refrigerant flow passage having a small flow passage cross-sectional area is on the refrigerant outlet side. The pressure loss of the evaporator 8 is significantly increased as compared to when the compressor is in operation, and as a result, the refrigerant circulation flow rate to the evaporator 8 is reduced and the heat exchange performance is further reduced.
【0024】すなわち、図13の従来技術によると、圧
縮機停止時の蒸発器8への冷媒流れ方向が圧縮機稼働時
と逆方向になるため、圧縮機停止時には蒸発器8の本来
の熱交換性能を発揮できず、放冷冷房性能が著しく低下
する。That is, according to the conventional technique shown in FIG. 13, the direction of the refrigerant flow to the evaporator 8 when the compressor is stopped is opposite to that when the compressor is operating, so that the original heat exchange of the evaporator 8 is performed when the compressor is stopped. The performance cannot be exhibited, and the cooling and cooling performance is significantly reduced.
【0025】本発明は上記点に鑑みて、蓄冷式の車両用
空調装置において、圧縮機停止に伴う放冷冷房モード時
における蒸発器の熱交換性能を圧縮機稼働時と同様に良
好に発揮できるようにすることを目的とする。In view of the above points, the present invention can exhibit the heat exchange performance of the evaporator in the cold storage cooling air-conditioning mode accompanying the stop of the compressor in the same manner as when the compressor is operating, in the cold storage type air conditioner for a vehicle. The purpose is to do so.
【0026】[0026]
【課題を解決するための手段】上記目的を達成するた
め、請求項1に記載の発明では、少なくとも停車時に車
両エンジン(4)を停止する制御を行う車両に搭載され
る車両用空調装置であって、車両エンジン(4)により
駆動される圧縮機(1)と、圧縮機(1)から吐出され
た高圧冷媒の放熱を行う高圧側熱交換器(6)と、高圧
側熱交換器(6)を通過した冷媒を減圧する減圧手段
(7、70)と、減圧手段(7、70)により減圧され
た低圧冷媒を蒸発させて車室内へ送風される空気を冷却
する蒸発器(8)と、圧縮機(1)の稼働時に低圧冷媒
により冷却される蓄冷材(11a)を有する蓄冷熱交換
器(11)と、車両エンジン(4)が停止して圧縮機
(1)が停止したときに、蒸発器(8)と蓄冷熱交換器
(11)との間で冷媒を循環するポンプ手段(14)を
備え、圧縮機(1)の停止時に、蒸発器(8)で蒸発し
た気相冷媒を蓄冷材(11a)の蓄冷熱により冷却して
凝縮し、この凝縮後の液冷媒を蒸発器(8)に導入する
とともに、圧縮機(1)の停止時における蒸発器(8)
への冷媒流れ方向を圧縮機(1)の稼働時における蒸発
器(8)への冷媒流れ方向と同一にしたことを特徴とす
る。In order to achieve the above object, the invention as set forth in claim 1 is a vehicle air conditioner mounted on a vehicle for controlling to stop the vehicle engine (4) at least when the vehicle is stopped. The compressor (1) driven by the vehicle engine (4), the high pressure side heat exchanger (6) for radiating the high pressure refrigerant discharged from the compressor (1), and the high pressure side heat exchanger (6). ), A pressure reducing means (7, 70) for reducing the pressure of the refrigerant passing therethrough, and an evaporator (8) for evaporating the low pressure refrigerant reduced by the pressure reducing means (7, 70) to cool the air blown into the vehicle interior. A cold storage heat exchanger (11) having a cold storage material (11a) that is cooled by a low-pressure refrigerant when the compressor (1) is in operation, and when the vehicle engine (4) is stopped and the compressor (1) is stopped. , A refrigerant between the evaporator (8) and the cold storage heat exchanger (11) When the compressor (1) is stopped, the gas-phase refrigerant evaporated in the evaporator (8) is cooled and condensed by the cold storage heat of the cold storage material (11a), and condensed after the condensation. The liquid refrigerant is introduced into the evaporator (8), and the evaporator (8) when the compressor (1) is stopped
The refrigerant flow direction to the evaporator (8) is the same as the refrigerant flow direction to the evaporator (8) when the compressor (1) is in operation.
【0027】これにより、蓄冷式の車両用空調装置にお
いて、蒸発器(8)への冷媒流れが圧縮機停止時と圧縮
機稼働時とで同一方向であるため、圧縮機停止に伴う放
冷冷房時の蒸発器熱交換性能を圧縮機稼働時と同様に良
好に発揮できる請求項2に記載の発明のように、請求項
1において、蓄冷熱交換器(11)を圧縮機(1)の稼
働時における冷媒流れに対して蒸発器(8)と並列接続
する構成とすることができる。As a result, in the cold storage type vehicle air conditioner, the refrigerant flow to the evaporator (8) is in the same direction when the compressor is stopped and when the compressor is operating, so that the cooling and cooling is performed when the compressor is stopped. As in the invention according to claim 2, which can exhibit the evaporator heat exchange performance at the same time as when the compressor is in operation, in claim 1, the cold storage heat exchanger (11) is connected to the compressor (1) to operate. The evaporator (8) may be connected in parallel to the refrigerant flow at any time.
【0028】また、請求項3に記載の発明のように、請
求項1において、蓄冷熱交換器(11)を圧縮機(1)
の稼働時における冷媒流れに対して蒸発器(8)と直列
接続してもよい。Further, as in the invention described in claim 3, in claim 1, the cold storage heat exchanger (11) is replaced by a compressor (1).
The evaporator (8) may be connected in series with respect to the flow of the refrigerant during the operation.
【0029】これによると、圧縮機(1)の稼働時には
圧縮機(1)の作動により蓄冷熱交換器(11)と蒸発
器(8)との直列流路を通して常に冷媒を流して、蒸発
器(8)による冷房能力の発揮と、蓄冷熱交換器(1
1)の蓄冷材(11a)への蓄冷を行うことができる。According to this, when the compressor (1) is in operation, the refrigerant is constantly caused to flow through the series flow path of the cold storage heat exchanger (11) and the evaporator (8) by the operation of the compressor (1), and the evaporator (8) Demonstrate the cooling capacity and cool storage heat exchanger (1
It is possible to store cold in the cold storage material (11a) of 1).
【0030】そのため、蓄冷式の車両用空調装置におい
て、弁手段による冷媒流路の開閉機能を必要とすること
なく、簡単な流路構成にて冷房機能および蓄冷機能を良
好に発揮できる。Therefore, in the cold storage type air conditioner for a vehicle, the cooling function and the cold storage function can be satisfactorily exerted with a simple flow path configuration without requiring the opening / closing function of the refrigerant flow path by the valve means.
【0031】請求項4に記載の発明では、請求項3にお
いて、減圧手段は、蒸発器(8)の出口冷媒の過熱度に
応じて冷媒流量を調節する膨張弁(7)であり、蓄冷熱
交換器(11)を蒸発器(8)の冷媒入口側に設けるこ
とを特徴とする。According to a fourth aspect of the present invention, in the third aspect, the pressure reducing means is an expansion valve (7) for adjusting the refrigerant flow rate according to the degree of superheat of the outlet refrigerant of the evaporator (8). It is characterized in that the exchanger (11) is provided on the refrigerant inlet side of the evaporator (8).
【0032】ところで、蓄冷熱交換器(11)において
蓄冷材(11a)への蓄冷が完了すると、低圧冷媒は蓄
冷熱交換器(11)においてほとんど吸熱することなく
素通りするようになるが、もし、蓄冷熱交換器(11)
を蒸発器(8)の冷媒出口側に設けると、蒸発器出口冷
媒が蓄冷完了した蓄冷材(11a)により冷却されてし
まい、膨張弁(7)による冷媒流量調節を適切に行うこ
とができない事態が生じる。By the way, when the cold storage of the cold storage material (11a) is completed in the cold storage heat exchanger (11), the low-pressure refrigerant passes through the cold storage heat exchanger (11) with almost no heat absorption. Cold storage heat exchanger (11)
When the refrigerant is provided on the refrigerant outlet side of the evaporator (8), the evaporator outlet refrigerant is cooled by the regenerator material (11a) that has completed cold storage, and the expansion valve (7) cannot properly control the refrigerant flow rate. Occurs.
【0033】しかし、請求項4によると、蓄冷熱交換器
(11)を蒸発器(8)の冷媒入口側に設けているか
ら、膨張弁(7)は蓄冷熱交換器(11)を設けていな
い通常のサイクルと同様に蒸発器出口冷媒の過熱度に応
じて冷媒流量を適切に調節できる。However, according to claim 4, since the cold storage heat exchanger (11) is provided on the refrigerant inlet side of the evaporator (8), the expansion valve (7) is provided with the cold storage heat exchanger (11). The refrigerant flow rate can be appropriately adjusted according to the superheat degree of the refrigerant at the outlet of the evaporator as in the normal cycle.
【0034】請求項5に記載の発明では、請求項1にお
いて、蒸発器(8)の冷媒出口側に配置されるアキュム
レータタンク(120)を備え、アキュムレータタンク
(120)の内部にて蒸発器(8)出口の低圧冷媒の気
液を分離して、気相冷媒を圧縮機(1)の吸入側に導出
するようになっており、蓄冷熱交換器(11)を蒸発器
(8)の冷媒出口側とアキュムレータタンク(120)
との間に設け、圧縮機(1)の稼働時に蓄冷熱交換器
(11)を通過した低圧冷媒がアキュムレータタンク
(120)内部を通過して圧縮機(1)に吸入されるよ
うにし、圧縮機(1)の停止時に、アキュムレータタン
ク(120)内の液冷媒をポンプ手段(14)により蒸
発器(8)に導入することを特徴とする。According to a fifth aspect of the present invention, in the first aspect, an accumulator tank (120) arranged on the refrigerant outlet side of the evaporator (8) is provided, and the evaporator () is provided inside the accumulator tank (120). 8) The gas-liquid of the low-pressure refrigerant at the outlet is separated, and the gas-phase refrigerant is led to the suction side of the compressor (1). The cold storage heat exchanger (11) is used as the refrigerant of the evaporator (8). Outlet side and accumulator tank (120)
And a low-pressure refrigerant that has passed through the cold storage heat exchanger (11) during operation of the compressor (1) passes through the inside of the accumulator tank (120) and is sucked into the compressor (1). The liquid refrigerant in the accumulator tank (120) is introduced into the evaporator (8) by the pump means (14) when the machine (1) is stopped.
【0035】請求項5は、蒸発器出口側にアキュムレー
タタンク(120)を配置するアキュムレータに関する
ものであって、これにより、減圧手段として膨張弁
(7)を使用しなくても圧縮機(1)への液冷媒戻り、
ひいては液圧縮を防止できる。このように減圧手段とし
て膨張弁(7)を使用しない場合は、蓄冷熱交換器(1
1)を蒸発器(8)の冷媒出口側に設けてもサイクルの
冷媒流量調節作用に支障は生じない。Claim 5 relates to an accumulator in which an accumulator tank (120) is arranged on the evaporator outlet side, whereby a compressor (1) can be used without using an expansion valve (7) as a pressure reducing means. Liquid refrigerant return to,
As a result, liquid compression can be prevented. When the expansion valve (7) is not used as the pressure reducing means in this way, the cold storage heat exchanger (1
Even if (1) is provided on the refrigerant outlet side of the evaporator (8), it does not hinder the refrigerant flow rate adjusting action of the cycle.
【0036】また、蓄冷熱交換器(11)を通過した低
圧冷媒がアキュムレータタンク(120)内部を通過し
て圧縮機(1)に吸入されるから、蓄冷熱交換器(1
1)での冷却作用により低圧冷媒が液化しても、その液
冷媒はアキュムレータタンク(120)内に溜めること
ができる。従って、蓄冷熱交換器(11)のための液冷
媒貯留機能をアキュムレータタンク(120)に兼務さ
せることができる。Further, since the low-pressure refrigerant passing through the cold storage heat exchanger (11) passes through the inside of the accumulator tank (120) and is sucked into the compressor (1), the cold storage heat exchanger (1)
Even if the low-pressure refrigerant is liquefied by the cooling action in 1), the liquid refrigerant can be stored in the accumulator tank (120). Therefore, the accumulator tank (120) can also serve as the liquid refrigerant storage function for the cold storage heat exchanger (11).
【0037】そして、蒸発器(8)の冷媒流路での圧力
損失分だけ、蒸発器(8)の冷媒出口側の方が冷媒入口
側よりも低圧冷媒温度が低下するので、蒸発器出口側に
蓄冷熱交換器(11)を設けることにより、低圧冷媒温
度と蓄冷材(11a)との温度差が拡大して、蓄冷材
(11a)を効率よく冷却できる。Since the low pressure refrigerant temperature on the refrigerant outlet side of the evaporator (8) is lower than that on the refrigerant inlet side by the pressure loss in the refrigerant flow path of the evaporator (8), the evaporator outlet side is reduced. By providing the cold storage heat exchanger (11) in the above, the temperature difference between the low-pressure refrigerant temperature and the cold storage material (11a) increases, and the cold storage material (11a) can be efficiently cooled.
【0038】請求項6に記載の発明のように請求項5に
おいて、減圧手段(70)は、具体的には固定絞りもし
くは高圧冷媒状態に応動する可変絞りにて構成できる。According to the sixth aspect of the present invention, in the fifth aspect, the pressure reducing means (70) can be specifically constituted by a fixed throttle or a variable throttle that responds to a high pressure refrigerant state.
【0039】請求項7に記載の発明では、請求項1ない
し6のいずれか1つにおいて、圧縮機(1)の稼働時
に、低圧冷媒がポンプ手段(14)をバイパスして蓄冷
熱交換器(11)に流れるようになっていることを特徴
とする。In the invention according to claim 7, in any one of claims 1 to 6, when the compressor (1) is in operation, the low-pressure refrigerant bypasses the pump means (14) and the cold storage heat exchanger ( It is characterized in that it is adapted to flow to 11).
【0040】これにより、圧縮機稼働時にポンプ手段
(14)自体の存在により冷媒流量を減少させるといっ
た不具合が生じない。As a result, the problem that the flow rate of the refrigerant is reduced due to the presence of the pump means (14) itself when the compressor is operating does not occur.
【0041】なお、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も
のである。The reference numerals in parentheses of the above-mentioned means indicate the correspondence with the concrete means described in the embodiments described later.
【0042】[0042]
【発明の実施の形態】(第1実施形態)図1は第1実施
形態による車両用空調装置の冷凍サイクルRを示す。車
両用空調装置の冷凍サイクルRは冷媒を吸入、圧縮、吐
出する圧縮機1を有し、この圧縮機1には動力断続用の
電磁クラッチ2が備えられている。圧縮機1には電磁ク
ラッチ2およびベルト3を介して車両エンジン4の動力
が伝達されるので、電磁クラッチ2への通電を空調用制
御装置5により断続することにより圧縮機1の運転が断
続される。DESCRIPTION OF THE PREFERRED EMBODIMENTS (First Embodiment) FIG. 1 shows a refrigeration cycle R of a vehicle air conditioner according to a first embodiment. A refrigeration cycle R of a vehicle air conditioner has a compressor 1 that sucks, compresses, and discharges a refrigerant, and the compressor 1 is provided with an electromagnetic clutch 2 for connecting and disconnecting power. Since the power of the vehicle engine 4 is transmitted to the compressor 1 via the electromagnetic clutch 2 and the belt 3, the operation of the compressor 1 is interrupted by interrupting the power supply to the electromagnetic clutch 2 by the air conditioning controller 5. It
【0043】圧縮機1から吐出された高温、高圧の過熱
気相冷媒は高圧側熱交換器をなす凝縮器6に流入し、図
示しない冷却ファンより送風される外気と熱交換して冷
却され凝縮する。凝縮器6は凝縮部6aと、凝縮部6a
を通過後の冷媒の気液を分離して液冷媒を溜めるととも
に液冷媒を導出する受液器6bと、受液器6bからの液
冷媒を過冷却する過冷却部6cとを一体に構成した周知
のものである。The high-temperature, high-pressure superheated gas-phase refrigerant discharged from the compressor 1 flows into a condenser 6 which constitutes a high-pressure side heat exchanger, and is cooled by heat exchange with the outside air blown from a cooling fan (not shown) and condensed. To do. The condenser 6 includes a condenser section 6a and a condenser section 6a.
The liquid receiver 6b for separating the gas-liquid of the refrigerant after passing through the liquid refrigerant to collect the liquid refrigerant and for discharging the liquid refrigerant, and the supercooling unit 6c for supercooling the liquid refrigerant from the liquid receiver 6b are integrally configured. It is well known.
【0044】この過冷却部6cからの過冷却液冷媒は減
圧手段をなす膨張弁7により低圧に減圧され、低圧の気
液2相状態となる。膨張弁7は冷房用熱交換器をなす蒸
発器8の出口冷媒の過熱度を調節するように弁7aの開
度(冷媒流量)を調節する温度式膨張弁である。特に、
本例では、蒸発器8の出口冷媒が流れる蒸発器出口冷媒
流路7bをボックス型のハウジング7c内に構成して、
蒸発器8の出口冷媒の感温機構をハウジング7c内に一
体構成するタイプの温度式膨張弁7を用いている。The supercooled liquid refrigerant from the supercooling section 6c is depressurized to a low pressure by the expansion valve 7 which constitutes a depressurizing means, and becomes a low pressure gas-liquid two-phase state. The expansion valve 7 is a thermal expansion valve that adjusts the opening degree (refrigerant flow rate) of the valve 7a so as to adjust the degree of superheat of the outlet refrigerant of the evaporator 8 that constitutes the heat exchanger for cooling. In particular,
In this example, the evaporator outlet refrigerant flow path 7b through which the outlet refrigerant of the evaporator 8 flows is configured in the box-shaped housing 7c,
The thermal expansion valve 7 of the type in which the temperature-sensing mechanism for the outlet refrigerant of the evaporator 8 is integrally formed in the housing 7c is used.
【0045】蓄冷ユニット9は図1の2点鎖線枠内の機
器を1つの組立ユニットとして一体的に構成しているも
のであって、温度式膨張弁7の弁7aの出口流路を流路
切替弁10を介して蓄冷熱交換器11に接続している。
この蓄冷熱交換器11は、蓄冷材を封入した多数の蓄冷
材容器11aをタンク部材11bの内部に配置したもの
である。The cool storage unit 9 integrally comprises the devices within the chain double-dashed line frame in FIG. 1 as one assembly unit, and the flow path is the outlet flow path of the valve 7a of the thermal expansion valve 7. It is connected to the cold storage heat exchanger 11 via the switching valve 10.
This cold storage heat exchanger 11 is configured by arranging a large number of cold storage material containers 11a enclosing a cold storage material inside a tank member 11b.
【0046】より具体的には、多数の蓄冷材容器11a
をその容器相互間に冷媒が流通する隙間部を形成する状
態でタンク部材11b内に配置する。ここで、蓄冷材容
器11aの形態は具体的には図2(a)に示す冷媒流れ
方向に沿って細長く延びる円筒状からなるスティックタ
イプ、図2(b)に示すボールタイプ、図2(c)に示
すカプセルタイプのいずれでもよい。蓄冷材容器11a
は樹脂製の薄膜状パック部材、あるいはアルミニュウム
等の金属板材で形成することができる。More specifically, a large number of regenerator material containers 11a.
Are arranged in the tank member 11b in such a manner that a space for the refrigerant to flow between the containers is formed. Here, the form of the regenerator material container 11a is specifically a stick type having a cylindrical shape elongated in the refrigerant flow direction shown in FIG. 2 (a), a ball type shown in FIG. 2 (b), and FIG. ) Any of the capsule types shown in FIG. Cool storage material container 11a
Can be formed of a resin-made thin film pack member or a metal plate material such as aluminum.
【0047】蓄冷材容器11a内に封入する蓄冷材とし
ては、低圧冷媒により冷却されて相変化(液相→固相)
して凝固潜熱を蓄冷できる材料、すなわち、低圧冷媒温
度よりも高い温度で凝固する材料を選択する。The cold storage material sealed in the cold storage material container 11a is cooled by a low-pressure refrigerant and undergoes a phase change (liquid phase → solid phase).
Then, a material capable of storing latent heat of solidification is selected, that is, a material that solidifies at a temperature higher than the low-pressure refrigerant temperature is selected.
【0048】ここで、低圧冷媒温度は蒸発器8でのフロ
スト防止のために、通常3〜4℃程度の温度に制御さ
れ、また、冷房時における車室内吹出空気温度の目標上
限温度は冷房フィーリングの確保、蒸発器8からの悪臭
防止等のために、通常は12℃〜15°程度の温度に設
定される。Here, the low pressure refrigerant temperature is usually controlled to a temperature of about 3 to 4 ° C. in order to prevent frost in the evaporator 8, and the target upper limit temperature of the air blown into the vehicle compartment during cooling is the cooling fee. In order to secure the ring and prevent the bad odor from the evaporator 8, etc., the temperature is usually set to about 12 ° C to 15 °.
【0049】従って、蓄冷材としては、凝固点が上記低
圧冷媒温度と冷房時吹出空気温度の目標上限温度との間
に位置する材料が好ましく、具体的には、凝固点が6℃
〜8℃程度のパラフィンが最適である。もちろん、低圧
冷媒温度を0℃以下に制御すれば、蓄冷材として水
(氷)を使用することもできる。Therefore, as the regenerator material, a material having a freezing point located between the low-pressure refrigerant temperature and the target upper limit temperature of the blown air temperature during cooling is preferable. Specifically, the freezing point is 6 ° C.
Paraffin at about 8 ° C is most suitable. Of course, if the low-pressure refrigerant temperature is controlled to 0 ° C. or lower, water (ice) can be used as the cold storage material.
【0050】蓄冷材の蓄冷状態(凝固状態)を維持する
ためには、タンク部材11b内部を蓄冷材の凝固点以下
の低温状態に維持する必要があるため、タンク部材11
bは断熱タンクとして構成する必要がある。従って、タ
ンク部材11bは断熱性に優れた樹脂タンク、あるいは
金属タンク表面に断熱材を貼り付けたもの等を用いる。In order to maintain the cold storage state (solidified state) of the regenerator material, it is necessary to maintain the inside of the tank member 11b at a low temperature below the freezing point of the regenerator material.
b must be constructed as an insulating tank. Therefore, as the tank member 11b, a resin tank having an excellent heat insulating property, or a metal tank having a heat insulating material attached to the surface thereof is used.
【0051】なお、蓄冷熱交換器11をシェルアンドチ
ューブタイプの熱交換器として構成してもよく、その場
合はシェル(タンク部材)内部に配置されるチューブに
サイクル低圧冷媒を流通させ、そして、シェル内部にお
いてチューブの外側空間に蓄冷材を充填してサイクル低
圧冷媒により冷却すればよい。The cold storage heat exchanger 11 may be constructed as a shell-and-tube type heat exchanger. In that case, the cycle low-pressure refrigerant is passed through the tube arranged inside the shell (tank member), and Inside the shell, the outer space of the tube may be filled with a regenerator material and cooled by the cycle low-pressure refrigerant.
【0052】そして、蓄冷ユニット9において蓄冷熱交
換器11より下方部位に液冷媒タンク部12を配置し、
この液冷媒タンク部12は、後述の圧縮機停止に伴う放
冷冷房モード時(図6)に、蓄冷熱交換器11で凝縮し
た液冷媒を溜めるものである。なお、液冷媒タンク部1
2を蓄冷熱交換器11のタンク部材11bの下部に一体
に形成することが可能である。Then, in the cold storage unit 9, the liquid refrigerant tank portion 12 is arranged below the cold storage heat exchanger 11,
The liquid-refrigerant tank section 12 stores the liquid refrigerant condensed in the cold-storage heat exchanger 11 in a cooling / cooling mode (FIG. 6) associated with the stop of a compressor described later. The liquid refrigerant tank unit 1
It is possible to integrally form 2 in the lower part of the tank member 11b of the cold storage heat exchanger 11.
【0053】液冷媒タンク部12の上端部は流路切替弁
10と蓄冷熱交換器11との間の冷媒流路13に接続さ
れている。液冷媒タンク部12の下端部(底部)は、液
冷媒循環用ポンプ手段をなす電動ポンプ14に接続され
ている。The upper end portion of the liquid refrigerant tank portion 12 is connected to the refrigerant passage 13 between the passage switching valve 10 and the cold storage heat exchanger 11. The lower end portion (bottom portion) of the liquid refrigerant tank portion 12 is connected to an electric pump 14 that serves as liquid refrigerant circulation pump means.
【0054】この電動ポンプ14は放冷冷房モード時
に、液冷媒タンク部12内の液冷媒を吸入して逆止弁1
5→流路切替弁10→蒸発器8→蓄冷熱交換器11を経
て液冷媒タンク部12に至る閉回路にて循環する。すな
わち、蒸発器8には、後述の圧縮機稼働時(通常冷房時
・蓄冷冷房時)および圧縮機停止時(放冷冷房モード
時)の双方において常に同一方向Bに冷媒が流れるよう
にしてある。The electric pump 14 sucks the liquid refrigerant in the liquid refrigerant tank portion 12 in the cooling / cooling mode to check the valve 1.
It circulates in a closed circuit from 5 to the flow path switching valve 10 to the evaporator 8 to the cold storage heat exchanger 11 to the liquid refrigerant tank portion 12. That is, in the evaporator 8, the refrigerant always flows in the same direction B both when the compressor is in operation (normal cooling / cooling / cooling) and when the compressor is stopped (in the cooling / cooling mode), which will be described later. .
【0055】ここで、電動ポンプ14は、例えば、イン
ペラ(羽根車)を用いた遠心式のポンプにより構成され
る。また、流路切替弁10は具体的には、サーボモータ
のようなアクチュエータにより回転角が制御されるロー
タ式の弁体を有する電気制御弁であって、この弁体の回
転角制御により後述の図4〜図6に示すように、温度式
膨張弁7の出口流路を蓄冷熱交換器11の入口側冷媒流
路13又は逆止弁15側の冷媒流路に切り替える三方弁
タイプの流路切替作用を果たすものである。Here, the electric pump 14 is constituted by, for example, a centrifugal pump using an impeller (impeller). Further, the flow path switching valve 10 is specifically an electric control valve having a rotor type valve body whose rotation angle is controlled by an actuator such as a servomotor, and will be described later by controlling the rotation angle of this valve body. As shown in FIGS. 4 to 6, a three-way valve type flow passage that switches the outlet flow passage of the thermal expansion valve 7 to the inlet side refrigerant flow passage 13 of the cold storage heat exchanger 11 or the check valve 15 side refrigerant flow passage. It performs a switching function.
【0056】蒸発器8の出口冷媒流路16は膨張弁7内
部の蒸発器出口冷媒流路7bに接続される。この蒸発器
8の出口冷媒流路16の途中には蓄冷熱交換器11の冷
媒流路17が接続されている。この冷媒流路17は、圧
縮機稼働時には蓄冷熱交換器11にとって出口側流路と
なり、圧縮機停止時には蓄冷熱交換器11にとって入口
側流路となる。The outlet refrigerant flow passage 16 of the evaporator 8 is connected to the evaporator outlet refrigerant flow passage 7b inside the expansion valve 7. The refrigerant flow passage 17 of the cold storage heat exchanger 11 is connected in the middle of the outlet refrigerant flow passage 16 of the evaporator 8. The refrigerant passage 17 serves as an outlet-side passage for the cold storage heat exchanger 11 when the compressor is operating, and serves as an inlet-side passage for the cold storage heat exchanger 11 when the compressor is stopped.
【0057】また、蒸発器8内の具体的冷媒流路は、前
述の図14に例示する直交・対向流タイプの流路として
構成され、且つ、図14に示す冷媒入口側熱交換部81
の冷媒流路81a、81bに比較して冷媒出口側熱交換
部82の冷媒流路82a、82bの流路断面積を大きく
するように設計してある。これにより、蒸発器8の出口
側冷媒流路82a、82bにおいて気相冷媒の比率(乾
き度)の増大→冷媒流速の上昇による圧損の増大を低減
するようにしてある。Further, the specific refrigerant flow passage in the evaporator 8 is configured as a flow path of the orthogonal / counterflow type illustrated in the above-mentioned FIG. 14, and the refrigerant inlet side heat exchange section 81 shown in FIG.
It is designed to have a larger flow passage cross-sectional area of the refrigerant flow passages 82a and 82b of the refrigerant outlet side heat exchange section 82 than the refrigerant flow passages 81a and 81b. As a result, the increase of the ratio (dryness) of the vapor-phase refrigerant in the outlet-side refrigerant flow paths 82a and 82b of the evaporator 8 → the increase of the pressure loss due to the increase of the refrigerant flow velocity is reduced.
【0058】なお、図1の例では、膨張弁7を蓄冷ユニ
ット9と別体として図示しているが、膨張弁7も蓄冷ユ
ニット9の一部分として一体化し、膨張弁7と蓄冷ユニ
ット9を一体状態にて車両に搭載するようにしてもよ
い。In the example of FIG. 1, the expansion valve 7 is shown separately from the cold storage unit 9, but the expansion valve 7 is also integrated as a part of the cold storage unit 9, and the expansion valve 7 and the cold storage unit 9 are integrated. You may make it mount in a vehicle in the state.
【0059】蓄冷ユニット9は蓄冷熱交換器11内部の
低温状態を維持するためには蓄冷熱交換器11内への熱
の侵入をできるだけ抑制した方が良い。そのためには、
蓄冷ユニット9を車室内、例えば、車室内前部の計器盤
内側等に設置した方が良い。しかし、車室内のスペース
的制約から車室内に蓄冷ユニット9の搭載スペースを確
保できない場合は、蓄冷ユニット9を車室外、例えば、
エンジンルール等に設置することになる。In order to maintain the low temperature state inside the cold storage heat exchanger 11, it is preferable that the cold storage unit 9 suppress heat from entering the cold storage heat exchanger 11 as much as possible. for that purpose,
It is better to install the cool storage unit 9 inside the vehicle, for example, inside the instrument panel at the front of the vehicle. However, when it is not possible to secure a mounting space for the cool storage unit 9 in the passenger compartment due to space restrictions in the passenger compartment, the cool storage unit 9 is placed outside the passenger compartment, for example,
It will be installed in the engine rules etc.
【0060】図3は空調室内ユニット20を示すもので
あり、空調室内ユニット20は通常、車室内前部の計器
盤内側に搭載される。空調室内ユニット20の空調ケー
ス21は車室内へ向かって送風される空気の通路を構成
するものであり、この空調ケース21内に蒸発器8が設
置されている。FIG. 3 shows the air conditioning indoor unit 20, and the air conditioning indoor unit 20 is usually mounted inside the instrument panel in the front part of the vehicle interior. The air-conditioning case 21 of the air-conditioning indoor unit 20 constitutes a passage for air blown toward the vehicle interior, and the evaporator 8 is installed in the air-conditioning case 21.
【0061】空調ケース21において、蒸発器8の上流
側には送風機22が配置され、送風機22には遠心式送
風ファン22aと駆動用モータ22bが備えられてい
る。送風ファン22aの吸入側には内外気切替箱23が
配置され、この内外気切替箱23内の内外気切替ドア2
3aにより外気(車室外空気)または内気(車室内空
気)が切替導入される。In the air conditioning case 21, a blower 22 is arranged on the upstream side of the evaporator 8, and the blower 22 is provided with a centrifugal blower fan 22a and a drive motor 22b. The inside / outside air switching box 23 is arranged on the suction side of the blower fan 22a, and the inside / outside air switching door 2 in the inside / outside air switching box 23 is disposed.
The outside air (air outside the passenger compartment) or the inside air (air inside the passenger compartment) is switched and introduced by 3a.
【0062】空調ケース21内で、蒸発器8の下流側に
はエアミックスドア24が配置され、このエアミックス
ドア24の下流側には車両エンジン4の温水(冷却水)
を熱源として空気を加熱する温水式ヒータコア25が暖
房用熱交換器として設置されている。In the air conditioning case 21, an air mix door 24 is arranged on the downstream side of the evaporator 8, and hot water (cooling water) of the vehicle engine 4 is arranged on the downstream side of the air mix door 24.
A hot water type heater core 25 that heats air by using as a heat source is installed as a heating heat exchanger.
【0063】そして、この温水式ヒータコア25の側方
(上方部)には、温水式ヒータコア25をバイパスして
空気(冷風)を流すバイパス通路26が形成されてい
る。エアミックスドア24は回動可能な板状ドアであ
り、温水式ヒータコア25を通過する温風とバイパス通
路26を通過する冷風との風量割合を調節するものであ
って、この冷温風の風量割合の調節により車室内への吹
出空気温度を調節する。従って、本例においてはエアミ
ックスドア24により車室内への吹出空気の温度調節手
段が構成される。On the side (upper part) of the hot water heater core 25, there is formed a bypass passage 26 that bypasses the hot water heater core 25 and allows air (cool air) to flow. The air mix door 24 is a rotatable plate-like door, and is for adjusting the air flow rate ratio between the warm air passing through the hot water heater core 25 and the cool air passing through the bypass passage 26. The temperature of the air blown into the passenger compartment is adjusted by adjusting. Therefore, in this example, the air mix door 24 constitutes a temperature adjusting means for the air blown into the vehicle interior.
【0064】温水式ヒータコア25からの温風とバイパ
ス通路26からの冷風を空気混合部27で混合して、所
望温度の空気を作り出すことができる。さらに、空調ケ
ース21内で、空気混合部27の下流側に吹出モード切
替部が構成されている。すなわち、車両フロントガラス
内面に空気を吹き出すデフロスタ開口部28、車室内乗
員の上半身に向けて空気を吹き出すフェイス開口部2
9、および車室内乗員の足元に向けて空気を吹き出すフ
ット開口部30を吹出モードドア31〜33により開閉
するようになっている。The hot air from the hot water heater core 25 and the cold air from the bypass passage 26 can be mixed in the air mixing portion 27 to produce air at a desired temperature. Furthermore, in the air conditioning case 21, a blowout mode switching unit is configured on the downstream side of the air mixing unit 27. That is, the defroster opening 28 that blows air to the inner surface of the windshield of the vehicle, and the face opening 2 that blows air toward the upper half of the passenger in the passenger compartment.
9, and the foot opening 30 that blows air toward the feet of the passenger in the passenger compartment is opened and closed by the blowing mode doors 31 to 33.
【0065】蒸発器8の温度センサ34は空調ケース2
1内で蒸発器8の空気吹出直後の部位に配置され、蒸発
器吹出温度Teを検出する。ここで、蒸発器温度センサ
34により検出される蒸発器吹出温度Teは、通常の空
調装置と同様に、圧縮機1の電磁クラッチ2の断続制御
や、圧縮機1が可変容量型である場合はその吐出容量制
御に使用され、これらのクラッチ断続制御や吐出容量制
御により蒸発器8の冷却能力を調節して、蒸発器8の吹
出温度を制御する。The temperature sensor 34 of the evaporator 8 is the air conditioning case 2
It is arranged at a portion of the evaporator 8 immediately after the air is blown out, and detects the evaporator blowing temperature Te. Here, the evaporator outlet temperature Te detected by the evaporator temperature sensor 34 is the same as in a normal air conditioner when the electromagnetic clutch 2 of the compressor 1 is controlled to be intermittent or when the compressor 1 is of a variable capacity type. It is used for the discharge capacity control, and the cooling capacity of the evaporator 8 is adjusted by the clutch engagement / disengagement control and the discharge capacity control to control the blowout temperature of the evaporator 8.
【0066】空調用制御装置5には、上記の温度センサ
34の他に、空調制御のために、内気温Tr、外気温T
am、日射量Ts、温水温度Tw等を検出する周知のセ
ンサ群35から検出信号が入力される。また、車室内計
器盤近傍に設置される空調制御パネル36には乗員によ
り手動操作される温度設定スイッチ、風量切替スイッ
チ、吹出モードスイッチ、内外気切替スイッチ、圧縮機
1のオンオフ信号を発生するエアコンスイッチ等の種々
な操作スイッチ群(図示せず)が備えられ、この操作ス
イッチ群の操作信号も空調用制御装置5に入力される。In addition to the temperature sensor 34, the air-conditioning control device 5 has an inside air temperature Tr and an outside air temperature T for air-conditioning control.
A detection signal is input from a known sensor group 35 that detects am, the amount of solar radiation Ts, the hot water temperature Tw, and the like. An air conditioning control panel 36 installed near the instrument panel in the passenger compartment has a temperature setting switch manually operated by an occupant, an air volume changeover switch, a blowout mode switch, an inside / outside air changeover switch, and an air conditioner for generating an ON / OFF signal for the compressor 1. Various operation switch groups (not shown) such as switches are provided, and operation signals of these operation switch groups are also input to the air conditioning controller 5.
【0067】また、空調用制御装置5はエンジン用制御
装置37に接続されており、エンジン用制御装置37か
ら空調用制御装置5には車両エンジン4の回転数信号、
車速信号等が入力される。空調用制御装置5は上記の各
種入力信号に基づいて所定の演算処理を行って、電磁ク
ラッチ2、流路切替弁10、電動ポンプ14等の作動を
制御する。The air conditioning control device 5 is connected to the engine control device 37, and the engine control device 37 sends the air conditioning control device 5 a rotation speed signal of the vehicle engine 4.
A vehicle speed signal or the like is input. The air-conditioning control device 5 performs predetermined arithmetic processing based on the above various input signals to control the operation of the electromagnetic clutch 2, the flow path switching valve 10, the electric pump 14, and the like.
【0068】エンジン用制御装置37は周知のごとく車
両エンジン4の運転状況等を検出するセンサ群38から
の信号に基づいて車両エンジン4への燃料噴射量、点火
時期等を総合的に制御するものである。さらに、本実施
形態の対象とするエコラン車においては、車両エンジン
4の回転数信号、車速信号、ブレーキ信号等に基づいて
停車状態を判定すると、エンジン用制御装置37は、点
火装置の電源遮断、燃料噴射の停止等により車両エンジ
ン4を自動的に停止させる。As is well known, the engine control device 37 comprehensively controls the fuel injection amount to the vehicle engine 4, the ignition timing, etc. based on a signal from a sensor group 38 for detecting the operating condition of the vehicle engine 4. Is. Further, in the eco-run vehicle to which the present embodiment is applied, when the stop state is determined based on the rotation speed signal, the vehicle speed signal, the brake signal, etc. of the vehicle engine 4, the engine control device 37 shuts off the power of the ignition device. The vehicle engine 4 is automatically stopped by stopping fuel injection or the like.
【0069】また、エンジン停止後、運転者の運転操作
により車両が停車状態から発進状態に移行すると、エン
ジン用制御装置37は車両の発進状態をアクセル信号等
に基づいて判定して、車両エンジン4を自動的に始動さ
せる。なお、空調用制御装置5は、車両エンジン4停止
後の放冷冷房モードの時間が長時間に及び、蓄冷熱交換
器11の蓄冷熱量による冷房を持続できない状態になっ
た時はエンジン再稼働要求の信号をエンジン用制御装置
37に出力する。After the engine is stopped, when the vehicle is moved from the stopped state to the starting state by the driver's driving operation, the engine control unit 37 determines the starting state of the vehicle based on the accelerator signal or the like, and the vehicle engine 4 To start automatically. It should be noted that the air-conditioning control device 5 requests the engine restart when the time period of the cooling / cooling mode after the vehicle engine 4 is stopped is long and the cooling due to the amount of cold storage heat of the cold storage heat exchanger 11 cannot be continued. Is output to the engine control device 37.
【0070】空調用制御装置5およびエンジン用制御装
置37はCPU、ROM、RAM等からなる周知のマイ
クロコンピュータと、その周辺回路にて構成されるもの
である。なお、空調用制御装置5およびエンジン用制御
装置37を1つの制御装置として統合してもよい。The air-conditioning control device 5 and the engine control device 37 are composed of a well-known microcomputer including a CPU, a ROM, a RAM and the like, and its peripheral circuits. The air conditioning control device 5 and the engine control device 37 may be integrated as one control device.
【0071】次に、上記構成において第1実施形態の作
動を説明する。図4は車両走行時の通常冷房モード時の
作動を示すものであり、この通常冷房モード時では車両
エンジン4によって圧縮機1を駆動することにより冷凍
サイクルRが運転される。従って、圧縮機1から吐出さ
れた高圧気相冷媒が凝縮器6にて冷却され、過冷却状態
の液冷媒となって膨張弁7に流入する。この膨張弁7の
弁部7aで高圧液冷媒が減圧されて低温低圧の気液2相
状態となる。Next, the operation of the first embodiment having the above structure will be described. FIG. 4 shows the operation in the normal cooling mode during traveling of the vehicle. In the normal cooling mode, the refrigeration cycle R is operated by driving the compressor 1 by the vehicle engine 4. Therefore, the high-pressure gas-phase refrigerant discharged from the compressor 1 is cooled by the condenser 6 and becomes a supercooled liquid refrigerant and flows into the expansion valve 7. The high-pressure liquid refrigerant is decompressed by the valve portion 7a of the expansion valve 7 to become a low-temperature low-pressure gas-liquid two-phase state.
【0072】ここで、通常冷房モード時には空調制御装
置5の制御出力により流路切替弁10が、膨張弁7の出
口流路と蓄冷熱交換器11との間を遮断し、膨張弁7の
出口流路を電動ポンプ14側の流路に連通させる状態に
操作される。このとき、電動ポンプ14側の流路への冷
媒流入は逆止弁15の閉弁により阻止される。Here, in the normal cooling mode, the flow passage switching valve 10 shuts off between the outlet flow passage of the expansion valve 7 and the cold storage heat exchanger 11 by the control output of the air conditioning controller 5, and the outlet of the expansion valve 7 is closed. The flow passage is operated to communicate with the flow passage on the electric pump 14 side. At this time, the inflow of the refrigerant into the flow path on the electric pump 14 side is blocked by closing the check valve 15.
【0073】従って、膨張弁7を通過した低圧冷媒の全
量が図4の太線矢印に示すように蒸発器8に流入し、蒸
発器8において空調ケース21内の送風空気から低圧冷
媒が吸熱して蒸発し、気相冷媒となる。この気相冷媒
は、蒸発器8の出口冷媒流路16および膨張弁7内部の
蒸発器出口冷媒流路7bを経て圧縮機1に吸入され、再
度圧縮される。蒸発器8にて吸熱された冷風はフェイス
開口部29等から車室内へ吹き出して車室内を冷房す
る。Therefore, the entire amount of the low pressure refrigerant that has passed through the expansion valve 7 flows into the evaporator 8 as indicated by the thick arrow in FIG. 4, and the low pressure refrigerant absorbs heat from the blown air in the air conditioning case 21 in the evaporator 8. Evaporate and become a vapor phase refrigerant. This vapor-phase refrigerant is drawn into the compressor 1 through the outlet refrigerant flow path 16 of the evaporator 8 and the evaporator outlet refrigerant flow path 7b inside the expansion valve 7, and is compressed again. The cool air absorbed by the evaporator 8 is blown into the vehicle interior through the face opening 29 or the like to cool the vehicle interior.
【0074】次に、車両走行時において、冷房熱負荷が
所定量以下に低下して、冷房能力に余裕が生じたとき、
あるいは、車両減速時、すなわち、車両の慣性動力によ
り圧縮機1を駆動することができて、車両エンジン4に
よる圧縮機駆動動力を節減できる状態を空調制御装置5
にて判定したときは、通常冷房モードから蓄冷冷房モー
ドに切り替える。Next, when the cooling heat load is reduced to a predetermined amount or less while the vehicle is running, and there is a margin in the cooling capacity,
Alternatively, when the vehicle is decelerated, that is, in a state where the compressor 1 can be driven by the inertial power of the vehicle and the compressor driving power by the vehicle engine 4 can be saved, the air conditioning control device 5
When it is determined in, the normal cooling mode is switched to the cold storage cooling mode.
【0075】ここで、冷房熱負荷が所定量以下に低下し
た状態は、具体的には、例えば、蒸発器吹出温度Teが
所定温度以下に低下したこと等に基づいて判定できる。
車両減速時は車速等に基づいて判定できる。Here, the state in which the cooling heat load is reduced to a predetermined amount or less can be determined based on, for example, that the evaporator outlet temperature Te has decreased to a predetermined temperature or less.
When the vehicle decelerates, it can be determined based on the vehicle speed and the like.
【0076】蓄冷冷房モードにおいては空調制御装置5
の制御出力により流路切替弁10が図5に示すように膨
張弁7の出口流路と蓄冷熱交換器11との間を連通する
状態に操作される。従って、膨張弁7の出口流路に蒸発
器8と蓄冷熱交換器11が並列接続された状態となり、
膨張弁7を通過した低圧冷媒が図5の太線矢印のように
蒸発器8と蓄冷熱交換器11とに並列に流れる。In the cold storage / cooling mode, the air conditioning controller 5
By the control output of 1, the flow passage switching valve 10 is operated to communicate between the outlet flow passage of the expansion valve 7 and the cold storage heat exchanger 11, as shown in FIG. Therefore, the evaporator 8 and the cold storage heat exchanger 11 are connected in parallel to the outlet passage of the expansion valve 7,
The low-pressure refrigerant that has passed through the expansion valve 7 flows in parallel to the evaporator 8 and the cold storage heat exchanger 11 as indicated by the thick arrow in FIG.
【0077】これにより、蒸発器8においては空調ケー
ス21内の送風空気から低圧冷媒が吸熱して蒸発するこ
とにより送風空気が冷却され、蒸発器8通過後の冷風が
フェイス開口部29等から車室内へ吹き出して車室内を
冷房する。これと同時に、蓄冷熱交換器11においては
蓄冷材への蓄冷が行われる。As a result, in the evaporator 8, the low-pressure refrigerant absorbs heat from the air blown in the air-conditioning case 21 and evaporates, so that the air blown is cooled, and the cool air that has passed through the evaporator 8 passes through the face opening 29 or the like from the vehicle. It blows out into the room and cools the passenger compartment. At the same time, the cold storage heat exchanger 11 stores cold in the cold storage material.
【0078】すなわち、蒸発器8の冷房熱負荷が低下す
ると、膨張弁7の弁部7aの開度が減少し、冷凍サイク
ルの低圧圧力が低下し、低圧冷媒温度が蓄冷熱交換器1
1の蓄冷材の凝固点より低下するようになる。従って、
蓄冷熱交換器11では低圧冷媒の蒸発により蓄冷材の凝
固が開始され、蓄冷材に対して凝固潜熱が蓄冷される。
そして、蒸発器8および蓄冷熱交換器11で蒸発した気
相冷媒は、蒸発器8の出口冷媒流路16および膨張弁7
内部の蒸発器出口冷媒流路7bを経て圧縮機1に吸入さ
れ、再度圧縮される。That is, when the cooling heat load of the evaporator 8 decreases, the opening degree of the valve portion 7a of the expansion valve 7 decreases, the low-pressure pressure of the refrigeration cycle decreases, and the low-pressure refrigerant temperature changes to the cold-storage heat exchanger 1.
It becomes lower than the freezing point of the cold storage material of No. 1. Therefore,
In the cold storage heat exchanger 11, solidification of the cold storage material is started by evaporation of the low-pressure refrigerant, and latent heat of solidification is stored in the cold storage material.
Then, the vapor-phase refrigerant evaporated in the evaporator 8 and the cold storage heat exchanger 11 is the outlet refrigerant flow path 16 of the evaporator 8 and the expansion valve 7.
It is sucked into the compressor 1 through the evaporator outlet refrigerant flow path 7b and is compressed again.
【0079】ところで、液冷媒タンク部12は蓄冷熱交
換器11の入口側の冷媒流路13および蓄冷熱交換器1
1より下方位置に配置されているので、蓄冷冷房モード
において冷媒流路13から蓄冷熱交換器11に流入する
気液2相状態の低圧冷媒のうち、一部の液冷媒が気相冷
媒との密度差にて分離され、液冷媒タンク部12内に溜
まる。By the way, the liquid refrigerant tank portion 12 includes the refrigerant passage 13 on the inlet side of the cold storage heat exchanger 11 and the cold storage heat exchanger 1.
Since it is arranged at a position lower than 1, a part of the liquid refrigerant in the gas-liquid two-phase low-pressure refrigerant flowing from the refrigerant flow path 13 into the cold storage heat exchanger 11 in the cold storage cooling mode is the gas phase refrigerant. They are separated due to the difference in density and accumulated in the liquid refrigerant tank portion 12.
【0080】次に、信号待ち等の停車時に車両エンジン
4を自動的に停止する場合について説明すると、停車時
には空調作動状態(送風機22の作動状態)であって
も、車両エンジン4の停止に伴って冷凍サイクルRの圧
縮機1も強制的に停止状態となる。そこで、空調用制御
装置5ではこの停車時の車両エンジン(圧縮機)停止状
態を判定して、図6に示すように、空調制御装置5の制
御出力により流路切替弁10が通常冷房モード時と同じ
状態に操作される。Next, description will be made regarding a case where the vehicle engine 4 is automatically stopped when the vehicle is stopped such as waiting for a signal. Even when the vehicle engine 4 is stopped while the air conditioning is in operation (the blower 22 is in operation). As a result, the compressor 1 of the refrigeration cycle R is forcibly stopped. Therefore, the air conditioning control device 5 determines the vehicle engine (compressor) stop state when the vehicle is stopped, and as shown in FIG. 6, the flow path switching valve 10 is in the normal cooling mode by the control output of the air conditioning control device 5. It is operated in the same state as.
【0081】すなわち、流路切替弁10は、膨張弁7の
出口流路と蓄冷熱交換器11との間を遮断し、膨張弁7
の出口流路を電動ポンプ14側の流路に連通させる状態
に操作される。また、空調制御装置5の制御出力により
蓄冷ユニット9内の電動ポンプ14に給電し、電動ポン
プ14を作動させる。That is, the flow passage switching valve 10 shuts off the cold storage heat exchanger 11 from the outlet flow passage of the expansion valve 7, and the expansion valve 7
The outlet flow passage is operated to communicate with the flow passage on the electric pump 14 side. Moreover, the electric power is supplied to the electric pump 14 in the cold storage unit 9 by the control output of the air conditioning control device 5 to operate the electric pump 14.
【0082】これにより、冷凍サイクルRでは図6の太
線矢印に示すように、液冷媒タンク部12→電動ポンプ
14→逆止弁15→流路切替弁10→蒸発器8→冷媒流
路16、17→蓄冷熱交換器11→液冷媒タンク部12
からなる冷媒循環回路が形成されるとともに、液冷媒タ
ンク部12内の液冷媒が蒸発器8に導入される。As a result, in the refrigeration cycle R, as shown by the thick arrow in FIG. 6, the liquid refrigerant tank portion 12 → the electric pump 14 → the check valve 15 → the flow path switching valve 10 → the evaporator 8 → the refrigerant flow path 16, 17 → Cold heat exchanger 11 → Liquid refrigerant tank unit 12
And a liquid refrigerant in the liquid refrigerant tank portion 12 is introduced into the evaporator 8.
【0083】従って、蒸発器8では液冷媒タンク部12
からの液冷媒が送風機22の送風空気から吸熱して蒸発
するので、圧縮機停止後においても蒸発器8の冷却作用
を継続でき、車室内の冷房作用を継続できる。蒸発器8
で蒸発した気相冷媒の温度は蓄冷熱交換器11の蓄冷材
の凝固点より高いので、蓄冷材は気相冷媒から融解潜熱
を吸熱して固相から液相に相変化(融解)する。これに
より、気相冷媒は蓄冷材により冷却され液化する。この
液冷媒は重力により落下して液冷媒タンク部12に蓄え
られる。Therefore, in the evaporator 8, the liquid refrigerant tank portion 12
Since the liquid refrigerant from (1) absorbs heat from the blown air of the blower 22 and evaporates, the cooling action of the evaporator 8 can be continued even after the compressor is stopped, and the cooling action of the vehicle interior can be continued. Evaporator 8
Since the temperature of the vapor-phase refrigerant vaporized at is higher than the freezing point of the regenerator material of the regenerator 11, the regenerator material absorbs latent heat of fusion from the vapor-phase refrigerant and changes (melts) from the solid phase to the liquid phase. As a result, the vapor phase refrigerant is cooled and liquefied by the regenerator material. The liquid refrigerant falls due to gravity and is stored in the liquid refrigerant tank portion 12.
【0084】そして、蓄冷材が液相に相変化していくこ
とにより、液冷媒タンク部12内の液冷媒量が次第に減
少していくが、液冷媒タンク部12内の液冷媒が残存し
ている間、停車時(圧縮機停止時)の車室内冷房作用を
継続できる。As the regenerator material changes to the liquid phase, the amount of the liquid refrigerant in the liquid refrigerant tank portion 12 gradually decreases, but the liquid refrigerant in the liquid refrigerant tank portion 12 remains. While the vehicle is stopped, the vehicle interior cooling function can be continued when the vehicle is stopped (when the compressor is stopped).
【0085】なお、信号待ちによる停車時間は通常、1
〜2分程度の短時間であるから、蓄冷材として、凝固点
=6℃、凝固潜熱=229kJ/kgのパラフィンを、
420g程度用いることにより、1〜2分程度の停車時
の間、車室内冷房作用を継続できることを確認してい
る。The stop time for waiting for a signal is usually 1
Since it is a short time of about 2 minutes, paraffin with a freezing point = 6 ° C. and latent heat of solidification = 229 kJ / kg is used as a cold storage material.
It has been confirmed that by using about 420 g, the vehicle interior cooling function can be continued while the vehicle is stopped for about 1 to 2 minutes.
【0086】ところで、図4〜図6に示すように、通常
冷房モード、蓄冷冷房モード、および放冷冷房モードの
いずれにおいても、蒸発器8における冷媒流れ方向は、
膨張弁7の出口流路から蒸発器出口流路16へ向かう同
一方向Bである。従って、圧縮機停止に伴う放冷冷房モ
ード時における蒸発器8の熱交換性能を圧縮機稼働時と
同様に良好に発揮できる。By the way, as shown in FIGS. 4 to 6, in any of the normal cooling mode, the cold storage cooling mode, and the free-cooling cooling mode, the refrigerant flow direction in the evaporator 8 is
It is the same direction B from the outlet passage of the expansion valve 7 toward the evaporator outlet passage 16. Therefore, the heat exchange performance of the evaporator 8 in the cooling / cooling mode due to the stop of the compressor can be satisfactorily exhibited as in the compressor operation.
【0087】以下このことを具体的に説明すると、第1
実施形態の冷凍サイクルRでは、減圧装置として温度式
膨張弁7を用いて、この温度式膨張弁7により蒸発器出
口冷媒が所定の過熱度となるようにサイクル循環冷媒流
量が調整される。そのため、蒸発器8ではその冷媒出口
側領域に冷媒の過熱域が形成され、蒸発器8の出口側冷
媒温度が入口側冷媒温度よりも高くなる。The following is a specific description of this.
In the refrigeration cycle R of the embodiment, the thermal expansion valve 7 is used as a pressure reducing device, and the thermal expansion valve 7 adjusts the cycle circulation refrigerant flow rate so that the evaporator outlet refrigerant has a predetermined superheat degree. Therefore, in the evaporator 8, a refrigerant superheat region is formed in the refrigerant outlet side region thereof, and the outlet side refrigerant temperature of the evaporator 8 becomes higher than the inlet side refrigerant temperature.
【0088】従って、図14に示すように空気流れ方向
Aに対して対向流の冷媒流路を構成することにより、冷
媒入口側熱交換部81および冷媒出口側熱交換部82の
双方において空気と冷媒との温度差を大きくして、蒸発
器8の熱交換性能を向上できる。Therefore, as shown in FIG. 14, by forming a counterflow refrigerant passage in the air flow direction A, air is exchanged with air in both the refrigerant inlet side heat exchange section 81 and the refrigerant outlet side heat exchange section 82. The heat exchange performance of the evaporator 8 can be improved by increasing the temperature difference with the refrigerant.
【0089】また、蒸発器8の冷媒流路構成では、冷媒
入口側から冷媒出口側へ向かうにつれて冷媒の蒸発が次
第に進行し、気相冷媒の比率(乾き度)が増大するの
で、冷媒出口側流路では冷媒流速の上昇による圧損の増
大が顕著となる。そこで、第1実施形態の蒸発器8で
は、冷媒入口側熱交換部81の冷媒流路81a、81b
に比較して冷媒出口側熱交換部82の冷媒流路82a、
82bの流路断面積を大きくするように設計して、この
圧損増大を低減している。Further, in the refrigerant flow path configuration of the evaporator 8, the evaporation of the refrigerant gradually progresses from the refrigerant inlet side to the refrigerant outlet side, and the ratio (dryness) of the vapor phase refrigerant increases, so that the refrigerant outlet side The increase in pressure loss due to the increase in the flow velocity of the refrigerant becomes remarkable in the flow passage. Therefore, in the evaporator 8 of the first embodiment, the refrigerant flow paths 81a and 81b of the refrigerant inlet side heat exchange section 81 are provided.
The refrigerant flow path 82a of the refrigerant outlet side heat exchange section 82,
The increase in pressure loss is reduced by designing the flow passage cross-sectional area of 82b to be large.
【0090】そして、上記の3つの冷房モードにおける
蒸発器8での冷媒流れ方向がすべて同一方向Bであるた
め、対向流による熱交換性能の向上効果および冷媒出口
側流路82a、82bでの圧損増大の低減効果を放冷冷
房モード時にも他のモードと同様に発揮できる。Since all the refrigerant flow directions in the evaporator 8 in the above three cooling modes are the same direction B, the effect of improving heat exchange performance by the counter flow and the pressure loss in the refrigerant outlet side passages 82a, 82b are obtained. The effect of reducing the increase can be exhibited in the cooling / cooling mode as in the other modes.
【0091】なお、図13の従来技術において、放冷冷
房モード時に遠心式の電動ポンプ42の作動により、蓄
冷熱交換器40→電動ポンプ42→電磁弁41→蓄液タ
ンク43→蒸発器8の方向に冷媒を循環させれば、放冷
冷房モード時にも蒸発器8に対して圧縮機稼働時と同一
方向へ冷媒を流すことが可能となる。しかし、このよう
にすると、蓄冷冷房モード時に、電動ポンプ42のポン
プ機構部を正規の冷媒流れ方向と逆方向に冷媒が流れ、
この電動ポンプ42を通して蓄冷熱交換器40に冷媒が
流れるので、蓄冷熱交換器40への冷媒流れが電動ポン
プ42のポンプ機構部により著しく制限される。その結
果、蓄冷熱交換器11への冷媒流量が減少して蓄冷熱交
換器40における蓄冷能力が極端に低下するので、実際
はこのような対策を採用できない。In the prior art of FIG. 13, the operation of the centrifugal electric pump 42 in the cooling / cooling mode causes the cold storage heat exchanger 40 → the electric pump 42 → the solenoid valve 41 → the storage tank 43 → the evaporator 8 to operate. If the refrigerant is circulated in the same direction, it becomes possible to flow the refrigerant in the evaporator 8 in the same direction as when the compressor is operating, even in the cooling / cooling mode. However, with this configuration, the refrigerant flows through the pump mechanism portion of the electric pump 42 in the direction opposite to the normal refrigerant flow direction during the cold storage / cooling mode,
Since the refrigerant flows to the cold storage heat exchanger 40 through the electric pump 42, the flow of the refrigerant to the cold storage heat exchanger 40 is significantly limited by the pump mechanism portion of the electric pump 42. As a result, the flow rate of the refrigerant to the cold storage heat exchanger 11 is reduced and the cold storage capacity of the cold storage heat exchanger 40 is extremely reduced, so such a measure cannot be actually adopted.
【0092】これに対し、第1実施形態によると、蓄冷
冷房モード時に流路切替弁10から冷媒流路13を通過
して蓄冷熱交換器11に冷媒が流れ、電動ポンプ42を
バイパスして冷媒が流れるので、電動ポンプ42の存在
により蓄冷熱交換器11への冷媒流量が減少することは
全くない。On the other hand, according to the first embodiment, in the cold storage / cooling mode, the refrigerant flows from the flow path switching valve 10 through the refrigerant flow path 13 to the cold storage heat exchanger 11, and bypasses the electric pump 42 to carry the refrigerant. The flow rate of the refrigerant to the cold storage heat exchanger 11 never decreases due to the presence of the electric pump 42.
【0093】なお、第1実施形態では、図4の通常冷房
モード時に、流路切替弁10、電動ポンプ14、液冷媒
タンク部12を通過して蓄冷熱交換器11に冷媒が流れ
ることを防止するために、逆止弁15を用いているが、
通常冷房モード時に、停止状態にある電動ポンプ14自
身の流路抵抗により蓄冷熱交換器11への冷媒流入を僅
少量に制限できるのであれば、逆止弁15を廃止でき
る。In the first embodiment, the refrigerant is prevented from flowing to the cold storage heat exchanger 11 through the flow path switching valve 10, the electric pump 14 and the liquid refrigerant tank portion 12 in the normal cooling mode of FIG. The check valve 15 is used to
In the normal cooling mode, the check valve 15 can be omitted if the flow resistance of the electric pump 14 itself in the stopped state can restrict the refrigerant flow into the cold storage heat exchanger 11 to a small amount.
【0094】また、逆止弁15の機能を流路切替弁10
に一体化してもよい。つまり、流路切替弁10を、
(1)通常冷房モード時には蓄冷熱交換器11側および
電動ポンプ14側の流路を両方とも遮断し、(2)蓄冷
冷房モード時には蓄冷熱交換器11側の流路のみ連通状
態とし、電動ポンプ14側の流路は遮断状態とし、
(3)放冷冷房モード時には電動ポンプ14側の流路の
み連通状態とし、蓄冷熱交換器11側の流路は遮断状態
とするように構成してもよい。Further, the function of the check valve 15 is changed to the flow path switching valve 10
May be integrated with. That is, the flow path switching valve 10 is
(1) In the normal cooling mode, both the flow paths on the side of the cold storage heat exchanger 11 and the electric pump 14 are shut off, and (2) at the time of the cold storage cooling mode, only the flow path on the side of the cold storage heat exchanger 11 is in communication, and the electric pump The flow path on the 14 side is shut off,
(3) In the cooling / cooling mode, only the flow path on the electric pump 14 side may be in the communication state, and the flow path on the cold storage heat exchanger 11 side may be in the cutoff state.
【0095】(第2実施形態)上記の第1実施形態で
は、蓄冷冷房モード時に蓄冷熱交換器11側の流路を蒸
発器8の冷媒流路に対して並列接続し、蒸発器8と蓄冷
熱交換器11とに冷媒が並列に流れるように構成してい
るが、第2実施形態では蓄冷熱交換器11を蒸発器8の
入口側冷媒流路に直列に配置し、圧縮機稼働時には蓄冷
熱交換器11と蒸発器8との直列流路に常に冷媒が流れ
るようにし、それにより、第1実施形態の流路切替弁1
0を廃止する。(Second Embodiment) In the above-described first embodiment, the flow path on the cold storage heat exchanger 11 side is connected in parallel to the refrigerant flow path of the evaporator 8 in the cold storage cooling mode to cool the evaporator 8 and the cold storage. The refrigerant is configured to flow in parallel with the heat exchanger 11. However, in the second embodiment, the cold storage heat exchanger 11 is arranged in series in the refrigerant passage on the inlet side of the evaporator 8 and the cold storage is performed during operation of the compressor. Refrigerant is always allowed to flow in the serial flow path of the heat exchanger 11 and the evaporator 8, whereby the flow path switching valve 1 of the first embodiment is provided.
Abolish 0.
【0096】図7は第2実施形態による通常冷房・蓄冷
モードの状態を示し、図8は第2実施形態による放冷冷
房モードの状態を示す。なお、第2実施形態では圧縮機
稼働時に蓄冷熱交換器11と蒸発器8との直列流路に常
に冷媒が流れるので、第1実施形態の通常冷房モードと
蓄冷冷房モードとを合体した通常冷房・蓄冷モードが設
定されるだけとなる。FIG. 7 shows the state of the normal cooling / cooling storage mode according to the second embodiment, and FIG. 8 shows the state of the standing cooling / cooling mode according to the second embodiment. In the second embodiment, since the refrigerant always flows through the series flow path of the cold storage heat exchanger 11 and the evaporator 8 when the compressor is operating, the normal cooling mode in which the normal cooling mode and the cold storage cooling mode of the first embodiment are combined.・ Only the cold storage mode is set.
【0097】図7、図8において、第1実施形態と同等
部分には同一符号を付して説明を省略し、相違点のみを
以下具体的に説明する。膨張弁7の弁7aの出口部に接
続される蒸発器8の入口側冷媒流路18に蓄冷熱交換器
11を配置し、蓄冷熱交換器11を第1逆止弁15aを
介して蒸発器8の入口部に接続している。そして、蓄冷
熱交換器11の下方位置に配置される液冷媒タンク部1
2と電動ポンプ14とを、第1逆止弁15aと並列に設
けている。7 and 8, the same parts as those of the first embodiment are designated by the same reference numerals and the description thereof will be omitted. Only the different points will be specifically described below. The cold storage heat exchanger 11 is arranged in the inlet side refrigerant flow path 18 of the evaporator 8 connected to the outlet portion of the valve 7a of the expansion valve 7, and the cold storage heat exchanger 11 is connected to the evaporator via the first check valve 15a. It is connected to the entrance of 8. Then, the liquid refrigerant tank portion 1 arranged below the cold storage heat exchanger 11
2 and the electric pump 14 are provided in parallel with the first check valve 15a.
【0098】ここで、電動ポンプ14は液冷媒タンク部
12内の液冷媒を吸入して蒸発器8の入口部に向けて吐
出するように構成されている。第1逆止弁15aは電動
ポンプ14の作動時に閉弁して、ポンプ吐出冷媒が直
接、液冷媒タンク部12側へ向かうことを阻止する。Here, the electric pump 14 is configured to suck the liquid refrigerant in the liquid refrigerant tank portion 12 and discharge it toward the inlet portion of the evaporator 8. The first check valve 15a closes when the electric pump 14 operates, and blocks the pump discharge refrigerant from directly flowing toward the liquid refrigerant tank portion 12 side.
【0099】一方、蒸発器8の出口冷媒流路16は膨張
弁7内の蒸発器出口冷媒流路7bに接続されるととも
に、冷媒戻し流路19を経て蓄冷熱交換器11の冷媒入
口側に接続される。この冷媒戻し流路19には第2逆止
弁15bを設け、この第2逆止弁15bにより膨張弁7
の出口冷媒が直接、蒸発器8の出口冷媒流路16へ向か
うことを阻止するようになっている。On the other hand, the outlet refrigerant flow passage 16 of the evaporator 8 is connected to the evaporator outlet refrigerant flow passage 7b in the expansion valve 7, and passes through the refrigerant return flow passage 19 to the refrigerant inlet side of the cold storage heat exchanger 11. Connected. A second check valve 15b is provided in the refrigerant return passage 19, and the expansion valve 7 is provided by the second check valve 15b.
The outlet refrigerant is prevented from directly going to the outlet refrigerant passage 16 of the evaporator 8.
【0100】次に、第2実施形態の作動を説明する。図
7は車両走行時の通常冷房・蓄冷モード時の作動を示す
ものであり、この通常冷房・蓄冷モード時では車両エン
ジン4によって圧縮機1を駆動することにより冷凍サイ
クルRが運転され、図7の太線矢印に示すように、膨張
弁7通過後の低圧冷媒が蓄冷熱交換器11と蒸発器8と
の直列流路に常に流れる。Next, the operation of the second embodiment will be described. FIG. 7 shows the operation in the normal cooling / cooling storage mode while the vehicle is running. In this normal cooling / cooling storage mode, the refrigeration cycle R is operated by driving the compressor 1 by the vehicle engine 4. As indicated by the thick arrow, the low-pressure refrigerant after passing through the expansion valve 7 always flows in the series flow path of the cold storage heat exchanger 11 and the evaporator 8.
【0101】従って、膨張弁7通過後の低温の低圧冷媒
により先ず蓄冷熱交換器11の蓄冷材が冷却され、蓄冷
材への蓄冷を行う。そして、蓄冷熱交換器11を通過し
た低圧冷媒は次に蒸発器8において空調ケース21内の
送風空気から吸熱して蒸発し、気相冷媒となる。この気
相冷媒は、蒸発器8の出口冷媒流路16および膨張弁7
内部の蒸発器出口冷媒流路7bを経て圧縮機1に吸入さ
れ、再度圧縮される。蒸発器8にて冷却された冷風はフ
ェイス開口部29等から車室内へ吹き出して車室内を冷
房する。なお、蓄冷熱交換器11を通過した低圧冷媒中
の一部の液冷媒が重力にて下方の液冷媒タンク部12に
溜まる。Therefore, the cold storage material in the cold storage heat exchanger 11 is first cooled by the low-temperature low-pressure refrigerant after passing through the expansion valve 7, and the cold storage material stores cold energy. Then, the low-pressure refrigerant that has passed through the cold storage heat exchanger 11 then absorbs heat from the blown air in the air conditioning case 21 in the evaporator 8 and evaporates to become a vapor-phase refrigerant. This vapor-phase refrigerant is used in the outlet refrigerant flow path 16 of the evaporator 8 and the expansion valve 7.
It is sucked into the compressor 1 through the evaporator outlet refrigerant flow path 7b and is compressed again. The cool air cooled by the evaporator 8 is blown into the vehicle compartment through the face opening 29 or the like to cool the vehicle compartment. Note that a part of the liquid refrigerant in the low-pressure refrigerant that has passed through the cold storage heat exchanger 11 is collected in the lower liquid refrigerant tank portion 12 by gravity.
【0102】通常冷房・蓄冷モード時は液冷媒循環用の
電動ポンプ14の作動が不要であるため、空調制御装置
5の出力により電動ポンプ14が停止している。このた
め、電動ポンプ14が流通抵抗となるので、液冷媒タン
ク部12の液冷媒が電動ポンプ14を介して蒸発器8の
入口側に流入する量は僅少である。In the normal cooling / cooling storage mode, since the operation of the electric pump 14 for circulating the liquid refrigerant is unnecessary, the electric pump 14 is stopped by the output of the air conditioning controller 5. Therefore, since the electric pump 14 becomes a flow resistance, the amount of the liquid refrigerant in the liquid refrigerant tank portion 12 flowing into the inlet side of the evaporator 8 via the electric pump 14 is small.
【0103】次に、通常冷房・蓄冷モード時における蓄
冷ユニット9での冷媒の挙動をより具体的に説明する
と、夏期の高外気温時に冷房を始動する場合には蒸発器
8の吸い込み空気温度が40℃以上にも及ぶ高温とな
り、蒸発器8の冷房熱負荷が非常に大きくなる。このよ
うな冷房高負荷条件の下では、蒸発器8の出口冷媒の過
熱度が過大となり、膨張弁7の弁部7aの開度が全開と
なり、冷凍サイクルの低圧圧力が上昇する。Next, the behavior of the refrigerant in the cold storage unit 9 in the normal cooling / cooling mode will be described more specifically. When the cooling operation is started at the high outside air temperature in summer, the intake air temperature of the evaporator 8 is The temperature becomes as high as 40 ° C. or more, and the cooling heat load on the evaporator 8 becomes very large. Under such a cooling high load condition, the superheat degree of the outlet refrigerant of the evaporator 8 becomes excessive, the opening of the valve portion 7a of the expansion valve 7 is fully opened, and the low pressure of the refrigeration cycle rises.
【0104】そのため、蓄冷ユニット9の蓄冷熱交換器
11に流入する低圧冷媒の温度が蓄冷熱交換器11の蓄
冷材の凝固点(6〜8℃程度)より高い温度となる。従
って、蓄冷材は低圧冷媒との熱交換で凝固せず、蓄冷材
から顕熱分を吸熱するだけである。その結果、冷房高負
荷条件では低圧冷媒が蓄冷熱交換器11にて吸熱する熱
量は僅少量となる。そのため、低圧冷媒のほとんどは蓄
冷熱交換器11を持たない通常の空調装置と同様に蒸発
器8にて車室内吹出空気から吸熱して蒸発する。Therefore, the temperature of the low-pressure refrigerant flowing into the cold storage heat exchanger 11 of the cold storage unit 9 becomes higher than the freezing point (about 6 to 8 ° C.) of the cold storage material of the cold storage heat exchanger 11. Therefore, the regenerator material does not solidify due to heat exchange with the low-pressure refrigerant, and only absorbs sensible heat from the regenerator material. As a result, the amount of heat absorbed by the low-pressure refrigerant in the cold-storage heat exchanger 11 is very small under the cooling high-load condition. Therefore, most of the low-pressure refrigerant absorbs heat from the air blown into the passenger compartment in the evaporator 8 and evaporates, as in an ordinary air conditioner that does not have the cold storage heat exchanger 11.
【0105】なお、冷房高負荷時には、通常、図3の内
外気切替箱23から内気を吸入する内気モードが選択さ
れるから、冷房始動後の時間経過により蒸発器8の吸い
込み空気温度が低下し、冷房熱負荷が低下する。これに
より、蒸発器8の出口冷媒の過熱度が減少するので、膨
張弁7の弁部7aの開度が減少し、冷凍サイクルの低圧
圧力が低下し、低圧冷媒温度が低下する。When the cooling load is high, the inside air mode for sucking the inside air from the inside / outside air switching box 23 shown in FIG. 3 is usually selected. Therefore, the intake air temperature of the evaporator 8 decreases with the lapse of time after the start of cooling. , Cooling heat load decreases. As a result, the degree of superheat of the outlet refrigerant of the evaporator 8 is reduced, the opening degree of the valve portion 7a of the expansion valve 7 is reduced, the low pressure of the refrigeration cycle is reduced, and the low pressure refrigerant temperature is reduced.
【0106】そして、低圧冷媒温度が蓄冷熱交換器11
の蓄冷材の凝固点より低下すると、蓄冷材の凝固が開始
され、低圧冷媒は蓄冷材から凝固潜熱を吸熱するので、
蓄冷材からの吸熱量が増加する。しかし、蓄冷材がこの
ように凝固潜熱を蓄冷する段階に至った時点では、既
に、冷房熱負荷の低下により低圧冷媒温度が十分低下
し、車室内吹出空気が十分低下している。The low-pressure refrigerant temperature changes to the cold storage heat exchanger 11
When the temperature is lower than the freezing point of the cold storage material, solidification of the cold storage material is started and the low-pressure refrigerant absorbs latent heat of solidification from the cold storage material.
The amount of heat absorbed from the cold storage material increases. However, at the time when the cold storage material reaches the stage of storing the latent heat of solidification in this way, the low-pressure refrigerant temperature has already sufficiently decreased due to the reduction of the cooling heat load, and the air blown into the vehicle compartment has already sufficiently decreased.
【0107】従って、蓄冷材への凝固潜熱の蓄冷作用に
よって、冷房高負荷条件における急速冷房性能(クール
ダウン性能)が大きく阻害されることがない。換言する
と、蓄冷熱交換器11を冷房用蒸発器8の冷媒回路に直
列接続し、蓄冷熱交換器11に低圧冷媒が常に流れて
も、冷房高負荷条件における急速冷房性能を、僅少量低
下させるだけであり、良好に発揮できる。Therefore, the rapid cooling performance (cool down performance) under the cooling high load condition is not significantly hindered by the cold storage action of the solidification latent heat on the cold storage material. In other words, the cold storage heat exchanger 11 is connected in series to the refrigerant circuit of the cooling evaporator 8, and even if the low-pressure refrigerant always flows through the cold storage heat exchanger 11, the rapid cooling performance under the cooling high load condition is slightly reduced. Only, and can be demonstrated well.
【0108】次に、信号待ち等の停車時に車両エンジン
4を自動的に停止する場合について説明すると、停車時
には空調作動状態(送風機22の作動状態)であって
も、車両エンジン4の停止に伴って冷凍サイクルRの圧
縮機1も強制的に停止状態となる。そこで、空調用制御
装置5ではこの停車時の車両エンジン(圧縮機)停止状
態を判定して、蓄冷ユニット9内の電動ポンプ14に給
電し、電動ポンプ14を作動させる。Next, description will be made regarding a case where the vehicle engine 4 is automatically stopped when the vehicle is stopped such as waiting for a signal. Even when the vehicle engine 4 is stopped while the air conditioning is in operation (the blower 22 is in operation). As a result, the compressor 1 of the refrigeration cycle R is forcibly stopped. Therefore, the air conditioning control device 5 determines the vehicle engine (compressor) stop state when the vehicle is stopped, supplies power to the electric pump 14 in the cold storage unit 9, and operates the electric pump 14.
【0109】これにより、蓄冷熱交換器11タ下部の液
冷媒タンク部12に溜まっている液冷媒を電動ポンプ1
4が吸入して、蒸発器8の入口側に向かって液冷媒を吐
出する。この電動ポンプ14による液冷媒の吸入、吐出
作用によって、第1逆止弁15aには冷媒圧力が逆方向
に作用して第1逆止弁15aは閉弁する。これに反し、
第2逆止弁15bには冷媒圧力が順方向に作用して第2
逆止弁15bは開弁する。As a result, the liquid refrigerant accumulated in the liquid refrigerant tank portion 12 below the cold storage heat exchanger 11 is transferred to the electric pump 1
4 inhales and discharges the liquid refrigerant toward the inlet side of the evaporator 8. Due to the suction and discharge actions of the liquid refrigerant by the electric pump 14, the refrigerant pressure acts on the first check valve 15a in the opposite direction, and the first check valve 15a is closed. Contrary to this,
The refrigerant pressure acts on the second check valve 15b in the forward direction, and
The check valve 15b opens.
【0110】そのため、図8の太線矢印に示すように、
液冷媒タンク部12→電動ポンプ14→蒸発器8→出口
冷媒流路16→冷媒戻し流路19→第2逆止弁15b→
蓄冷熱交換器11→液冷媒タンク部12からなる冷媒循
環回路で冷媒が循環する。Therefore, as indicated by the thick arrow in FIG.
Liquid refrigerant tank portion 12 → electric pump 14 → evaporator 8 → outlet refrigerant flow path 16 → refrigerant return flow path 19 → second check valve 15b →
Refrigerant circulates in the refrigerant circulation circuit composed of the cold storage heat exchanger 11 → the liquid refrigerant tank portion 12.
【0111】従って、蒸発器8では液冷媒タンク部12
からの液冷媒が送風機22の送風空気から吸熱して蒸発
するので、圧縮機停止後においても蒸発器8の冷却作用
を継続でき、車室内の冷房作用を継続できる。Therefore, in the evaporator 8, the liquid refrigerant tank portion 12
Since the liquid refrigerant from (1) absorbs heat from the blown air of the blower 22 and evaporates, the cooling action of the evaporator 8 can be continued even after the compressor is stopped, and the cooling action of the vehicle interior can be continued.
【0112】蒸発器8で蒸発した気相冷媒は、蓄冷熱交
換器11を通過する際に蓄冷材の融解潜熱により冷却さ
れ凝縮する。この液冷媒は重力により落下して液冷媒タ
ンク部12に蓄えられる。The vapor-phase refrigerant evaporated in the evaporator 8 is cooled and condensed by the latent heat of fusion of the cold storage material when passing through the cold storage heat exchanger 11. The liquid refrigerant falls due to gravity and is stored in the liquid refrigerant tank portion 12.
【0113】そして、蓄冷材が凝固潜熱を気相冷媒から
吸熱して液相に相変化していくことにより、液冷媒タン
ク部12内の液冷媒量が減少していくが、液冷媒タンク
部12内の液冷媒が残存している間、停車時(圧縮機停
止時)の車室内冷房作用を継続できる。Then, the regenerator material absorbs latent heat of solidification from the vapor phase refrigerant and changes its phase to the liquid phase, whereby the amount of the liquid refrigerant in the liquid refrigerant tank section 12 decreases, but the liquid refrigerant tank section While the liquid refrigerant in 12 remains, the vehicle interior cooling operation at the time of vehicle stop (when the compressor is stopped) can be continued.
【0114】ところで、第2実施形態においても、通常
冷房・蓄冷モード時および放冷冷房モード時の双方にお
いて、蒸発器8には同一方向Bに冷媒が流れるから、第
1実施形態と同様に蒸発器8の熱交換性能を常に良好な
状態に維持できる。By the way, in the second embodiment as well, the refrigerant flows in the same direction B in the evaporator 8 in both the normal cooling / cooling mode and the cold cooling / cooling mode. The heat exchange performance of the vessel 8 can always be maintained in a good state.
【0115】また、第2実施形態では、第1実施形態と
異なり、「冷房用蒸発器8に対して蓄冷熱交換器11を
直列接続する」構成を備えているので、次に、この第2
実施形態に独自の構成による有利さを第1実施形態との
対比により詳述する。第1実施形態では、空調用冷凍サ
イクルRにおいて蓄冷材を内蔵する蓄冷熱交換器11を
圧縮機稼働時における冷媒流れに対して冷房用蒸発器8
と並列に設けているので、蓄冷熱交換器11の冷媒流路
を冷凍サイクルの運転状況に応じて流路切替弁10によ
り切り替えることが必須となる。このことは前述の従来
技術(特開2000−313226号公報)も同じであ
る。Further, unlike the first embodiment, the second embodiment has a configuration in which the cool storage heat exchanger 11 is connected in series to the cooling evaporator 8, so that the second embodiment will be described next.
The advantages of the configuration unique to the embodiment will be described in detail by comparison with the first embodiment. In the first embodiment, in the air conditioning refrigeration cycle R, the cool storage heat exchanger 11 having a built-in cool storage material is used for the cooling evaporator 8 with respect to the refrigerant flow when the compressor is operating.
Since it is provided in parallel with the above, it is essential to switch the refrigerant flow path of the cold storage heat exchanger 11 by the flow path switching valve 10 according to the operating condition of the refrigeration cycle. This also applies to the above-mentioned conventional technique (Japanese Patent Laid-Open No. 2000-313226).
【0116】これに反し、本実施形態によると、冷房用
蒸発器8に対して蓄冷熱交換器11を直列接続している
から、夏期の冷房始動時のように冷房熱負荷が非常に高
い条件においても、サイクル循環冷媒流量の全量が冷房
用蒸発器8を通過するから、蓄冷熱交換器11の追加に
より冷房用蒸発器8への循環冷媒流量が減少することは
ない。Contrary to this, according to the present embodiment, since the cold storage heat exchanger 11 is connected in series to the cooling evaporator 8, the condition that the cooling heat load is very high as in the start of cooling in the summer. Also in the above, since the entire amount of the cycle circulating refrigerant flow passes through the cooling evaporator 8, the addition of the cold storage heat exchanger 11 does not reduce the circulating refrigerant flow rate to the cooling evaporator 8.
【0117】しかも、蓄冷熱交換器11における蓄冷材
の凝固点を前述のように冷房時吹出空気温度の目標上限
温度(12〜15℃程度)よりも低い温度(6〜8℃程
度)に設定することにより、冷房高熱負荷条件における
低圧冷媒の温度よりも蓄冷材の凝固点が低い温度とな
る。このため、冷房高熱負荷条件では蓄冷材は低圧冷媒
との熱交換で凝固せず、顕熱分の吸熱が僅かに行われる
だけである。Moreover, the freezing point of the cold storage material in the cold storage heat exchanger 11 is set to a temperature (about 6 to 8 ° C.) lower than the target upper limit temperature (about 12 to 15 ° C.) of the blown air temperature during cooling as described above. As a result, the freezing point of the cold storage material becomes lower than the temperature of the low-pressure refrigerant under the cooling high heat load condition. Therefore, under the cooling high heat load condition, the regenerator material does not solidify due to heat exchange with the low-pressure refrigerant, and only a slight amount of sensible heat is absorbed.
【0118】そのため、低圧冷媒の大部分は蓄冷熱交換
器11を持たない通常の空調装置と同様に蒸発器8にて
車室内吹出空気から吸熱して蒸発する。つまり、蓄冷熱
交換器11への冷媒流れの切替のための特別の操作を行
わなくても、冷房高熱負荷条件における冷房用蒸発器8
の最大冷却能力を良好に発揮できる。Therefore, most of the low-pressure refrigerant absorbs heat from the air blown into the passenger compartment in the evaporator 8 and evaporates, as in the case of a normal air conditioner without the cold storage heat exchanger 11. That is, the evaporator 8 for cooling under the high heat load condition for cooling is performed without performing a special operation for switching the flow of the refrigerant to the cold storage heat exchanger 11.
The maximum cooling capacity of can be exhibited well.
【0119】また、蓄冷熱交換器11における蓄冷材の
凝固が完了し、蓄冷完了状態になると、蓄冷熱交換器1
1における低圧冷媒の吸熱はほとんどなくなるが、蓄冷
熱交換器11を冷房用蒸発器8の入口側に配置している
ため、膨張弁7は蒸発器8の出口冷媒の過熱度を感知し
て冷媒流量を調節できる。従って、蓄冷完了後において
も、蒸発器8の冷房熱負荷に応じた適切な冷媒流量を蒸
発器8に供給できる。When the cold storage material in the cold storage heat exchanger 11 is solidified and the cold storage is completed, the cold storage heat exchanger 1
Although the heat absorption of the low-pressure refrigerant in 1 is almost eliminated, the expansion valve 7 senses the degree of superheat of the refrigerant at the outlet of the evaporator 8 because the cold storage heat exchanger 11 is arranged at the inlet side of the cooling evaporator 8. The flow rate can be adjusted. Therefore, even after the cold storage is completed, an appropriate refrigerant flow rate according to the cooling heat load of the evaporator 8 can be supplied to the evaporator 8.
【0120】なお、図9は第2実施形態の比較例であ
り、この比較例のように、蓄冷熱交換器11をもし蒸発
器8の出口側冷媒流路16に配置すると、蒸発器8の出
口冷媒が過熱度を持っていても蓄冷材の蓄冷(凝固)完
了状態では蒸発器8の出口冷媒が蓄冷材により冷却され
て過熱度が小さくなってしまう。その結果、膨張弁7の
開度が減少して、蒸発器8の冷房熱負荷に対して冷媒流
量が過小になるという不具合が生じる。これに対し、第
2実施形態では蓄冷熱交換器11を冷房用蒸発器8の入
口側に配置することによりこのような不具合が生じな
い。FIG. 9 shows a comparative example of the second embodiment. If the cold storage heat exchanger 11 is arranged in the outlet side refrigerant passage 16 of the evaporator 8 as in this comparative example, the evaporator 8 Even if the outlet refrigerant has a superheat degree, the outlet refrigerant of the evaporator 8 is cooled by the cool storage material and the superheat degree becomes small in a state where the cool storage material has completed the cold storage (solidification). As a result, the opening degree of the expansion valve 7 decreases, and the refrigerant flow rate becomes too small with respect to the cooling heat load of the evaporator 8. On the other hand, in the second embodiment, such a problem does not occur by disposing the cold storage heat exchanger 11 on the inlet side of the cooling evaporator 8.
【0121】(第3実施形態)上記の第1、第2実施形
態では、減圧手段として膨張弁7を用い、膨張弁7によ
り蒸発器8の出口冷媒の過熱度を調節する冷凍サイクル
について説明したが、第2実施形態は蒸発器8の出口側
(圧縮機1の吸入側)にアキュムレータを配置し、この
アキュムレータにおいて蒸発器出口冷媒の気液を分離し
て液冷媒を溜めて、気相冷媒を圧縮機1に吸入させるア
キュムレータ式の冷凍サイクルに蓄冷熱交換器11を組
み合わせるものである。(Third Embodiment) In the above first and second embodiments, the refrigeration cycle in which the expansion valve 7 is used as the pressure reducing means and the expansion valve 7 adjusts the superheat degree of the refrigerant exiting the evaporator 8 has been described. However, in the second embodiment, an accumulator is arranged on the outlet side of the evaporator 8 (the suction side of the compressor 1), and in this accumulator, the vapor-liquid of the evaporator outlet refrigerant is separated to collect the liquid refrigerant, and the vapor-phase refrigerant. The cold-storage heat exchanger 11 is combined with an accumulator-type refrigeration cycle that allows the compressor 1 to be sucked into the compressor 1.
【0122】図10、図11は第3実施形態を示すもの
であり、第1、第2実施形態と同等部分には同一符号を
付して説明を省略する。また、制御装置5、37等の電
気制御部は第1、第2実施形態と同じであるので、図1
0、図11ではこの電気制御部の図示を省略している。FIGS. 10 and 11 show the third embodiment, and the same parts as those of the first and second embodiments are designated by the same reference numerals and the description thereof will be omitted. In addition, since the electric control units such as the control devices 5 and 37 are the same as those in the first and second embodiments,
0 and FIG. 11, the illustration of the electric control unit is omitted.
【0123】アキュムレータ式の冷凍サイクルにおいて
は、蒸発器8の出口側にアキュムレータタンク120を
配置するので、第3実施形態ではこのアキュムレータタ
ンク120に着目して蓄冷ユニット9をアキュムレータ
タンク120と一体に構成する。In the accumulator type refrigeration cycle, the accumulator tank 120 is arranged on the outlet side of the evaporator 8. Therefore, in the third embodiment, the regenerator unit 9 is constructed integrally with the accumulator tank 120 by paying attention to the accumulator tank 120. To do.
【0124】すなわち、第3実施形態では、蒸発器8の
出口側冷媒流路に蓄冷ユニット9の蓄冷熱交換器11を
配置するとともに、この蓄冷熱交換器11のタンク部材
11bをアキュムレータタンク120の上方側に一体に
構成する。従って、アキュムレータタンク120が第
1、第2実施形態の液冷媒タンク部12の役割を兼務す
る。That is, in the third embodiment, the cold storage heat exchanger 11 of the cold storage unit 9 is arranged in the outlet side refrigerant flow path of the evaporator 8, and the tank member 11b of the cold storage heat exchanger 11 is connected to the accumulator tank 120. It is integrally configured on the upper side. Therefore, the accumulator tank 120 also serves as the liquid refrigerant tank portion 12 of the first and second embodiments.
【0125】アキュムレータタンク120の内部にはU
状に曲げ形成された出口パイプ121が配置され、この
出口パイプ121のU状の底部にオイル戻し穴(図示せ
ず)を開口し、このオイル戻し穴から液冷媒中に含まれ
る圧縮機潤滑用オイルを吸い込むようになっている。ま
た、出口パイプ121のU状一端部に気相冷媒吸入口1
21aを設け、この気相冷媒吸入口121aをアキュム
レータタンク120内の下部に溜まる液冷媒よりも上方
の空間に開口することにより、アキュムレータタンク1
20内の上部の気相冷媒を吸入口121aから出口パイ
プ121内に吸入するようになっている。出口パイプ1
21の他端側はアキュムレータタンク120の上面部か
らタンク外部へ取り出して、圧縮機1の吸入側に接続す
るようになっている。The inside of the accumulator tank 120 is U
The outlet pipe 121 formed in a bent shape is arranged, and an oil return hole (not shown) is opened at the U-shaped bottom portion of the outlet pipe 121, and the oil return hole is used for lubricating the compressor contained in the liquid refrigerant. It is designed to suck in oil. In addition, the gas-phase refrigerant suction port 1 is provided at the U-shaped one end of the outlet pipe 121.
21a is provided, and this gas-phase refrigerant inlet 121a is opened in the space above the liquid refrigerant accumulated in the lower part of the accumulator tank 120, whereby the accumulator tank 1
The gas-phase refrigerant in the upper part of 20 is sucked into the outlet pipe 121 from the suction port 121a. Outlet pipe 1
The other end side of 21 is taken out from the upper surface of the accumulator tank 120 to the outside of the tank and connected to the suction side of the compressor 1.
【0126】そして、アキュムレータタンク120の底
面部と蒸発器8の入口側流路との間を連通する冷媒戻し
流路19を設け、この冷媒戻し流路19に液冷媒循環用
の電動ポンプ14および逆止弁15bを配置し、アキュ
ムレータタンク120内の液冷媒を電動ポンプ14によ
り吸入して蒸発器8の入口側へ向かって吐出する。逆止
弁15bは図7〜図9の第2逆止弁15bと同様のもの
である。A refrigerant return passage 19 is provided which connects the bottom surface of the accumulator tank 120 and the inlet side passage of the evaporator 8, and the refrigerant return passage 19 has an electric pump 14 for circulating liquid refrigerant and The check valve 15b is arranged so that the liquid refrigerant in the accumulator tank 120 is sucked by the electric pump 14 and discharged toward the inlet side of the evaporator 8. The check valve 15b is similar to the second check valve 15b in FIGS. 7 to 9.
【0127】なお、第3実施形態はアキュムレータ式の
冷凍サイクルに関するものであって、アキュムレータタ
ンク120にて蒸発器出口冷媒の気液を分離して液冷媒
を溜める。そして、出口パイプ121の気相冷媒吸入口
121aから気相冷媒を吸入して圧縮機1の吸入側に送
り込むことができる。The third embodiment relates to an accumulator type refrigeration cycle, in which the vapor-liquid of the evaporator outlet refrigerant is separated in the accumulator tank 120 to store the liquid refrigerant. Then, the gas-phase refrigerant can be sucked from the gas-phase refrigerant suction port 121 a of the outlet pipe 121 and sent to the suction side of the compressor 1.
【0128】従って、蒸発器出口冷媒の過熱度の調節を
行わなくても圧縮機1の液冷媒圧縮を防止できるので、
第3実施形態では減圧装置70としてキャピラリチュー
ブ、オリフィス等の固定絞り、あるいは高圧冷媒圧力に
応動する可変絞り等を使用することができる。これらの
減圧装置70は、過熱度制御機構を持つ温度式膨張弁7
に比して構成が簡素で、安価である。Therefore, the liquid refrigerant compression of the compressor 1 can be prevented without adjusting the superheat degree of the refrigerant at the evaporator outlet.
In the third embodiment, as the decompression device 70, a capillary tube, a fixed throttle such as an orifice, or a variable throttle that responds to the high pressure of the refrigerant can be used. These decompression devices 70 are temperature type expansion valves 7 having a superheat control mechanism.
The configuration is simpler and less expensive than the.
【0129】図10は第3実施形態による車両走行時の
通常冷房・蓄冷モードであり、車両エンジン4により圧
縮機1が駆動されることにより、図10の太線矢印で示
す回路、すなわち、圧縮機1の吐出側→凝縮器6→減圧
装置70→蒸発器8→蓄冷熱交換器11→アキュムレー
タタンク120→圧縮機1の吸入側に至る回路にて冷媒
が循環し、蒸発器8にて低圧冷媒が空調ケース21内の
送風空気から吸熱して蒸発することにより送風空気が冷
却され車室内の冷房を行うことができる。FIG. 10 shows a normal cooling / cooling mode when the vehicle is running according to the third embodiment. When the compressor 1 is driven by the vehicle engine 4, the circuit shown by the thick arrow in FIG. 10, that is, the compressor. Refrigerant circulates in the circuit from the discharge side of 1 to the condenser 6 to the decompression device 70 to the evaporator 8 to the cold storage heat exchanger 11 to the accumulator tank 120 to the suction side of the compressor 1, and the low pressure refrigerant in the evaporator 8 The heat is absorbed from the blown air in the air conditioning case 21 to evaporate, whereby the blown air is cooled and the vehicle interior can be cooled.
【0130】また、蓄冷熱交換器11において蓄冷材を
低圧冷媒により冷却して凝固させることにより蓄冷材へ
の蓄冷を行う。なお、通常冷房・蓄冷モードでは、電動
ポンプ14は第1、第2実施形態と同様に停止してお
り、また、逆止弁15bは閉弁している。Further, in the cold storage heat exchanger 11, the cold storage material is cooled and solidified by the low-pressure refrigerant to perform cold storage in the cold storage material. In the normal cooling / cooling storage mode, the electric pump 14 is stopped as in the first and second embodiments, and the check valve 15b is closed.
【0131】図11は第3実施形態による停車時の放冷
冷房モードであり、このときは電動ポンプ14を作動さ
せ、図11の太線矢印で示す回路により冷媒を循環させ
る。すなわち、アキュムレータタンク120内の液冷媒
を電動ポンプ14にて吸入、吐出することにより、電動
ポンプ14→逆止弁15b(開弁状態)→蒸発器8→蓄
冷熱交換器11→アキュムレータタンク120に至る回
路にて冷媒が循環する。FIG. 11 shows a cooling / cooling mode when the vehicle is stopped according to the third embodiment. At this time, the electric pump 14 is operated and the refrigerant is circulated by the circuit shown by the thick arrow in FIG. That is, by sucking and discharging the liquid refrigerant in the accumulator tank 120 with the electric pump 14, the electric pump 14 → the check valve 15b (open valve state) → the evaporator 8 → the cold storage heat exchanger 11 → the accumulator tank 120. Refrigerant circulates in every circuit.
【0132】これにより、アキュムレータタンク120
内の貯留液冷媒を蒸発器8に循環するとともに、蒸発器
8で蒸発した気相冷媒を蓄冷熱交換器11により冷却、
液化させることにより、第3実施形態においても停車時
の放冷冷房機能を良好に発揮できる。Thus, the accumulator tank 120
The stored liquid refrigerant therein is circulated to the evaporator 8, and the vapor-phase refrigerant evaporated in the evaporator 8 is cooled by the cold storage heat exchanger 11.
By liquefying, even in the third embodiment, the function of leaving and cooling air when the vehicle is stopped can be exhibited well.
【0133】ところで、第3実施形態はアキュムレータ
式の冷凍サイクルであるため、蒸発器8の出口側に蓄冷
熱交換器11を直列接続している。これは次の理由によ
る。すなわち、アキュムレータ式の冷凍サイクルでは、
減圧装置70をキャピラリチューブ、オリフィス等の固
定絞り、あるいは高圧冷媒圧力に応動する可変絞り等に
より構成することができ、膨張弁7を使用する必要がな
い。従って、蒸発器8の出口側に蓄冷熱交換器11を直
列接続しても、前述の蒸発器出口冷媒の過熱度調節の不
具合が生じない。By the way, since the third embodiment is an accumulator type refrigeration cycle, the cold storage heat exchanger 11 is connected in series to the outlet side of the evaporator 8. This is for the following reason. That is, in the accumulator type refrigeration cycle,
The decompression device 70 can be configured by a capillary tube, a fixed throttle such as an orifice, or a variable throttle that responds to the pressure of high-pressure refrigerant, and it is not necessary to use the expansion valve 7. Therefore, even if the cold storage heat exchanger 11 is connected in series to the outlet side of the evaporator 8, the above-mentioned problem of adjusting the superheat degree of the refrigerant at the outlet of the evaporator does not occur.
【0134】そして、蒸発器8の冷媒流路を流れる冷媒
流れには必ず圧力損失が発生するので、蒸発器8の入口
側に比して出口側の方が冷媒圧力(蒸発圧力)が低下す
る。ここで、アキュムレータ式の冷凍サイクルでは、ア
キュムレータタンク120内部に冷媒の気液界面が形成
され冷媒が飽和状態になっているので、蒸発器8内の冷
媒が過熱状態にならない。そのため、蒸発器8の出口側
では冷媒圧力の低下に伴って冷媒温度(蒸発温度)が必
ず入口側よりも低下する。Since a pressure loss is always generated in the refrigerant flow flowing through the refrigerant passage of the evaporator 8, the refrigerant pressure (evaporation pressure) on the outlet side of the evaporator 8 is lower than that on the outlet side. . Here, in the accumulator type refrigeration cycle, since the gas-liquid interface of the refrigerant is formed inside the accumulator tank 120 and the refrigerant is saturated, the refrigerant in the evaporator 8 does not become overheated. Therefore, the refrigerant temperature (evaporation temperature) on the outlet side of the evaporator 8 is always lower than that on the inlet side as the refrigerant pressure decreases.
【0135】従って、アキュムレータ式の冷凍サイクル
において、蒸発器8の出口側に蓄冷熱交換器11を直列
接続することにより、蓄冷材をより低温の冷媒にて冷却
でき、蓄冷材と冷媒との温度差を拡大して熱交換効率を
向上でき、蓄冷材の凝固をより短時間で完了できる。Therefore, in the accumulator type refrigeration cycle, by connecting the cold storage heat exchanger 11 in series to the outlet side of the evaporator 8, the cold storage material can be cooled by a lower temperature refrigerant, and the temperature of the cold storage material and the refrigerant can be reduced. The difference can be enlarged to improve the heat exchange efficiency, and the solidification of the regenerator material can be completed in a shorter time.
【0136】因みに、図12は第3実施形態の比較例で
あり、蒸発器8の入口側に蓄冷熱交換器11を直列接続
しているので、蓄冷材を冷却する低圧冷媒の温度が第3
実施形態より高くなり、蓄冷材の冷却能力が第3実施形
態より低下する。Incidentally, FIG. 12 is a comparative example of the third embodiment, and since the cold storage heat exchanger 11 is connected in series to the inlet side of the evaporator 8, the temperature of the low pressure refrigerant for cooling the cold storage material is the third.
It becomes higher than that of the embodiment, and the cooling capacity of the regenerator material becomes lower than that of the third embodiment.
【0137】なお、第3実施形態は、蒸発器8における
入口側冷媒温度よりも出口側冷媒温度の方が低下するア
キュムレータ式の冷凍サイクルであるから、蒸発器8に
おける冷媒流路構成は、図14の対向流ではなく並行流
とする。すなわち、図14において、空気流れ方向Aの
風上側に冷媒入口側熱交換部81を配置し、空気流れ方
向Aの風下側に冷媒出口側熱交換部82を配置してい
る。これにより、アキュムレータ式冷凍サイクルの蒸発
器8において、冷媒入口側熱交換部81および冷媒出口
側熱交換部82の双方において空気と冷媒との温度差を
大きくして、熱交換性能を向上できる。Since the third embodiment is an accumulator type refrigeration cycle in which the temperature of the refrigerant on the outlet side is lower than the temperature of the refrigerant on the outlet side in the evaporator 8, the structure of the refrigerant flow path in the evaporator 8 is as shown in FIG. It is not a counter flow of 14 but a parallel flow. That is, in FIG. 14, the refrigerant inlet side heat exchange section 81 is arranged on the windward side in the air flow direction A, and the refrigerant outlet side heat exchange section 82 is arranged on the leeward side in the air flow direction A. Thereby, in the evaporator 8 of the accumulator type refrigeration cycle, the temperature difference between the air and the refrigerant can be increased in both the refrigerant inlet side heat exchange section 81 and the refrigerant outlet side heat exchange section 82, and the heat exchange performance can be improved.
【0138】そして、第3実施形態においても、通常冷
房・蓄冷モード時および放冷冷房モード時の双方におい
て、蒸発器8には同一方向Bに冷媒が流れるから、第
1、第2実施形態と同様に蒸発器8の熱交換性能を常に
良好な状態に維持できる。Also in the third embodiment, since the refrigerant flows in the same direction B in the evaporator 8 in both the normal cooling / cooling mode and the cold cooling / cooling mode, it is different from the first and second embodiments. Similarly, the heat exchange performance of the evaporator 8 can always be maintained in a good state.
【0139】なお、第3実施形態において逆止弁15b
は電動ポンプ14の停止時、すなわち、通常冷房・蓄冷
モード時に閉弁することにより、減圧装置70出口側の
低圧冷媒が冷媒戻し流路19を経てアキュムレータタン
ク120に流入することを防止するものであるから、電
動ポンプ14自身の停止時の流通抵抗により低圧冷媒の
上記流れを実用上問題のないレベルに低下できるのであ
れば、逆止弁15bを廃止してもよい。In the third embodiment, the check valve 15b
Is to prevent the low-pressure refrigerant on the outlet side of the pressure reducing device 70 from flowing into the accumulator tank 120 through the refrigerant return passage 19 by closing the valve when the electric pump 14 is stopped, that is, in the normal cooling / cooling mode. Therefore, the check valve 15b may be omitted as long as the flow resistance of the electric pump 14 itself when stopped can reduce the flow of the low-pressure refrigerant to a level at which there is no practical problem.
【図1】本発明の第1実施形態を示す冷凍サイクルの回
路図である。FIG. 1 is a circuit diagram of a refrigeration cycle showing a first embodiment of the present invention.
【図2】図1の蓄冷材容器を例示する斜視図である。FIG. 2 is a perspective view illustrating the regenerator material container of FIG.
【図3】第1実施形態による空調室内ユニット部の概略
断面図である。FIG. 3 is a schematic cross-sectional view of an air conditioning indoor unit portion according to the first embodiment.
【図4】第1実施形態による通常冷房モード時の作動説
明用の回路図である。FIG. 4 is a circuit diagram for explaining an operation in a normal cooling mode according to the first embodiment.
【図5】第1実施形態による蓄冷冷房モード時の作動説
明用の回路図である。FIG. 5 is a circuit diagram for explaining an operation in the cold storage cooling mode according to the first embodiment.
【図6】第1実施形態による放冷冷房モード時の作動説
明用の回路図である。FIG. 6 is a circuit diagram for explaining an operation in a cooling / cooling mode according to the first embodiment.
【図7】第2実施形態による通常冷房・蓄冷モード時の
作動説明用の回路図である。FIG. 7 is a circuit diagram for explaining an operation in a normal cooling / cooling storage mode according to a second embodiment.
【図8】第2実施形態による放冷冷房モード時の作動説
明用の回路図である。FIG. 8 is a circuit diagram for explaining an operation in a cooling and cooling mode according to a second embodiment.
【図9】第2実施形態の比較例による通常冷房・蓄冷モ
ード時の作動説明用の回路図である。FIG. 9 is a circuit diagram for explaining an operation in a normal cooling / cooling storage mode according to a comparative example of the second embodiment.
【図10】第3実施形態による通常冷房・蓄冷モード時
の作動説明用の回路図である。FIG. 10 is a circuit diagram for explaining an operation in a normal cooling / cooling storage mode according to a third embodiment.
【図11】第3実施形態による放冷冷房モード時の作動
説明用の回路図である。FIG. 11 is a circuit diagram for explaining an operation in a cooling / cooling mode according to a third embodiment.
【図12】第3実施形態の比較例による通常冷房・蓄冷
モード時の作動説明用の回路図である。FIG. 12 is a circuit diagram for explaining an operation in a normal cooling / cooling storage mode according to a comparative example of the third embodiment.
【図13】従来装置の冷凍サイクルの回路図である。FIG. 13 is a circuit diagram of a refrigeration cycle of a conventional device.
【図14】従来装置および本発明の第1、第2実施形態
で用いる蒸発器の冷媒流路の概略説明図である。FIG. 14 is a schematic explanatory diagram of a refrigerant channel of an evaporator used in a conventional device and the first and second embodiments of the present invention.
1…圧縮機、4…車両エンジン、6…凝縮器(高圧側熱
交換器)、7…膨張弁(減圧手段)、70…固定絞り等
の減圧装置(減圧手段)、8…蒸発器、9…蓄冷ユニッ
ト、10…タンク部材、11…蓄冷熱交換器、11a…
蓄冷材容器、15…電動ポンプ。DESCRIPTION OF SYMBOLS 1 ... Compressor, 4 ... Vehicle engine, 6 ... Condenser (high pressure side heat exchanger), 7 ... Expansion valve (pressure reducing means), 70 ... Pressure reducing device (pressure reducing means) such as fixed throttle, 8 ... Evaporator, 9 ... Cool storage unit, 10 ... Tank member, 11 ... Cool storage heat exchanger, 11a ...
Cooling material container, 15 ... Electric pump.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F25B 5/00 F25B 5/00 A 43/00 43/00 E ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) F25B 5/00 F25B 5/00 A 43/00 43/00 E
Claims (7)
を停止する制御を行う車両に搭載される車両用空調装置
であって、 前記車両エンジン(4)により駆動される圧縮機(1)
と、 前記圧縮機(1)から吐出された高圧冷媒の放熱を行う
高圧側熱交換器(6)と、 前記高圧側熱交換器(6)を通過した冷媒を減圧する減
圧手段(7、70)と、 前記減圧手段(7、70)により減圧された低圧冷媒を
蒸発させて車室内へ送風される空気を冷却する蒸発器
(8)と、 前記圧縮機(1)の稼働時に前記低圧冷媒により冷却さ
れる蓄冷材(11a)を有する蓄冷熱交換器(11)
と、 前記車両エンジン(4)が停止して前記圧縮機(1)が
停止したときに、前記蒸発器(8)と前記蓄冷熱交換器
(11)との間で冷媒を循環するポンプ手段(14)を
備え、 前記圧縮機(1)の停止時に、前記蒸発器(8)で蒸発
した気相冷媒を前記蓄冷材(11a)の蓄冷熱により冷
却して凝縮し、この凝縮後の液冷媒を前記蒸発器(8)
に導入するとともに、 前記圧縮機(1)の停止時における前記蒸発器(8)へ
の冷媒流れ方向を前記圧縮機(1)の稼働時における前
記蒸発器(8)への冷媒流れ方向と同一にしたことを特
徴とする車両用空調装置。1. A vehicle engine (4) at least when the vehicle is stopped.
A vehicle air conditioner mounted on a vehicle for performing control for stopping a compressor, the compressor (1) driven by the vehicle engine (4).
A high pressure side heat exchanger (6) for radiating heat of the high pressure refrigerant discharged from the compressor (1), and a decompression means (7, 70) for decompressing the refrigerant having passed through the high pressure side heat exchanger (6). ), An evaporator (8) for evaporating the low-pressure refrigerant decompressed by the decompression means (7, 70) to cool the air blown into the passenger compartment, and the low-pressure refrigerant when the compressor (1) is in operation. Storage heat exchanger (11) having a storage material (11a) cooled by
Pump means for circulating a refrigerant between the evaporator (8) and the cold storage heat exchanger (11) when the vehicle engine (4) stops and the compressor (1) stops. 14), when the compressor (1) is stopped, the vapor-phase refrigerant evaporated in the evaporator (8) is cooled and condensed by the cold storage heat of the cold storage material (11a), and the condensed liquid refrigerant is provided. The evaporator (8)
And the flow direction of the refrigerant to the evaporator (8) when the compressor (1) is stopped is the same as the flow direction of the refrigerant to the evaporator (8) when the compressor (1) is in operation. A vehicle air conditioner characterized by the above.
(1)の稼働時における冷媒流れに対して前記蒸発器
(8)と並列接続することを特徴とする請求項1に記載
の車両用空調装置。2. The cold storage heat exchanger (11) is connected in parallel with the evaporator (8) with respect to the flow of refrigerant during operation of the compressor (1). Air conditioning system for vehicles.
(1)の稼働時における冷媒流れに対して前記蒸発器
(8)と直列接続することを特徴とする請求項1に記載
の車両用空調装置。3. The cold storage heat exchanger (11) according to claim 1, characterized in that it is connected in series with the evaporator (8) with respect to the flow of refrigerant during operation of the compressor (1). Air conditioning system for vehicles.
口冷媒の過熱度に応じて冷媒流量を調節する膨張弁
(7)であり、 前記蓄冷熱交換器(11)を前記蒸発器(8)の冷媒入
口側に設けることを特徴とする請求項3に記載の車両用
空調装置。4. The decompression means is an expansion valve (7) for adjusting the refrigerant flow rate according to the degree of superheat of the outlet refrigerant of the evaporator (8), and the cold storage heat exchanger (11) is connected to the evaporator. The vehicle air conditioner according to claim 3, wherein the air conditioner is provided on the refrigerant inlet side of (8).
れるアキュムレータタンク(120)を備え、 前記アキュムレータタンク(120)の内部にて前記蒸
発器(8)出口の低圧冷媒の気液を分離して、気相冷媒
を前記圧縮機(1)の吸入側に導出するようになってお
り、 前記蓄冷熱交換器(11)を前記蒸発器(8)の冷媒出
口側と前記アキュムレータタンク(120)との間に設
け、 前記圧縮機(1)の稼働時に前記蓄冷熱交換器(11)
を通過した低圧冷媒が前記アキュムレータタンク(12
0)内部を通過して前記圧縮機(1)に吸入されるよう
にし、 前記圧縮機(1)の停止時に、前記アキュムレータタン
ク(120)内の液冷媒を前記ポンプ手段(14)によ
り前記蒸発器(8)に導入することを特徴とする請求項
1に記載の車両用空調装置。5. An accumulator tank (120) arranged on a refrigerant outlet side of the evaporator (8), wherein a gas-liquid of a low pressure refrigerant at an outlet of the evaporator (8) is provided inside the accumulator tank (120). And the gas-phase refrigerant is led to the suction side of the compressor (1). The cold storage heat exchanger (11) is connected to the refrigerant outlet side of the evaporator (8) and the accumulator tank. (120) provided between the cold storage heat exchanger (11) and the compressor (1) during operation.
The low-pressure refrigerant passing through the accumulator tank (12
0) It passes through the inside and is sucked into the compressor (1), and when the compressor (1) is stopped, the liquid refrigerant in the accumulator tank (120) is evaporated by the pump means (14). The vehicle air conditioner according to claim 1, wherein the air conditioner is installed in the device (8).
くは高圧冷媒状態に応動する可変絞りにて構成されるこ
とを特徴とする請求項5に記載の車両用空調装置。6. The vehicle air conditioner according to claim 5, wherein the pressure reducing means (70) is composed of a fixed throttle or a variable throttle that responds to a high-pressure refrigerant state.
冷媒が前記ポンプ手段(14)をバイパスして前記蓄冷
熱交換器(11)に流れるようになっていることを特徴
とする請求項1ないし6のいずれか1つに記載の車両用
空調装置。7. The low-pressure refrigerant bypasses the pump means (14) and flows into the cold storage heat exchanger (11) when the compressor (1) is in operation. Item 7. The vehicle air conditioner according to any one of items 1 to 6.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002093768A JP3906724B2 (en) | 2002-03-29 | 2002-03-29 | Air conditioner for vehicles |
| DE10308542.4A DE10308542B4 (en) | 2002-02-28 | 2003-02-27 | Vehicle air conditioner with cold storage unit |
| FR0302401A FR2836421B1 (en) | 2002-02-28 | 2003-02-27 | AIR CONDITIONER FOR VEHICLE WITH COLD STORAGE UNIT |
| KR10-2003-0012476A KR100467361B1 (en) | 2002-02-28 | 2003-02-27 | Vehicle air conditioner with cold storage unit |
| US10/375,245 US6701731B2 (en) | 2002-02-28 | 2003-02-27 | Vehicle air conditioner with cold storage unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002093768A JP3906724B2 (en) | 2002-03-29 | 2002-03-29 | Air conditioner for vehicles |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2003285633A true JP2003285633A (en) | 2003-10-07 |
| JP3906724B2 JP3906724B2 (en) | 2007-04-18 |
Family
ID=29238073
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2002093768A Expired - Fee Related JP3906724B2 (en) | 2002-02-28 | 2002-03-29 | Air conditioner for vehicles |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3906724B2 (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006509678A (en) * | 2002-12-16 | 2006-03-23 | ダイムラークライスラー・アクチェンゲゼルシャフト | Air conditioners for automobiles in particular |
| JP2006256512A (en) * | 2005-03-17 | 2006-09-28 | Denso Corp | Regenerator, regenerator capsule, and vehicle air conditioner using the same |
| JP2009298390A (en) * | 2008-06-17 | 2009-12-24 | Denso Corp | Vehicular air conditioner |
| KR101170849B1 (en) | 2005-12-26 | 2012-08-02 | 한라공조주식회사 | Air conditioner for vehicle using thermal energy saving system |
| WO2012105676A1 (en) * | 2011-02-04 | 2012-08-09 | カルソニックカンセイ株式会社 | Refrigeration cycle device |
| WO2013017936A1 (en) | 2011-08-01 | 2013-02-07 | Toyota Jidosha Kabushiki Kaisha | Cooling system |
| WO2013030657A1 (en) | 2011-08-31 | 2013-03-07 | Toyota Jidosha Kabushiki Kaisha | Cooling system |
| KR101355689B1 (en) * | 2008-03-13 | 2014-01-27 | 아이신세이끼가부시끼가이샤 | Air conditioning system and accumulator thereof |
| WO2018037186A1 (en) * | 2016-08-26 | 2018-03-01 | Valeo Systemes Thermiques | Thermal system, in particular a motor vehicle air conditioning system |
| WO2018185841A1 (en) * | 2017-04-04 | 2018-10-11 | 三菱電機株式会社 | Refrigeration cycle device |
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| JP2006509678A (en) * | 2002-12-16 | 2006-03-23 | ダイムラークライスラー・アクチェンゲゼルシャフト | Air conditioners for automobiles in particular |
| JP2006256512A (en) * | 2005-03-17 | 2006-09-28 | Denso Corp | Regenerator, regenerator capsule, and vehicle air conditioner using the same |
| KR101170849B1 (en) | 2005-12-26 | 2012-08-02 | 한라공조주식회사 | Air conditioner for vehicle using thermal energy saving system |
| KR101355689B1 (en) * | 2008-03-13 | 2014-01-27 | 아이신세이끼가부시끼가이샤 | Air conditioning system and accumulator thereof |
| JP2009298390A (en) * | 2008-06-17 | 2009-12-24 | Denso Corp | Vehicular air conditioner |
| CN103328240A (en) * | 2011-02-04 | 2013-09-25 | 卡森尼可关精株式会社 | Refrigeration cycle device |
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| US9732663B2 (en) | 2011-08-01 | 2017-08-15 | Toyota Jidosha Kabushiki Kaisha | Cooling system |
| JP2013032870A (en) * | 2011-08-01 | 2013-02-14 | Toyota Motor Corp | Cooling system |
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| WO2013030657A1 (en) | 2011-08-31 | 2013-03-07 | Toyota Jidosha Kabushiki Kaisha | Cooling system |
| US9951973B2 (en) | 2011-08-31 | 2018-04-24 | Toyota Jidosha Kabushiki Kaisha | Cooling system utilizing a portion of the liquid refrigerant from the condenser |
| WO2018037186A1 (en) * | 2016-08-26 | 2018-03-01 | Valeo Systemes Thermiques | Thermal system, in particular a motor vehicle air conditioning system |
| FR3055251A1 (en) * | 2016-08-26 | 2018-03-02 | Valeo Systemes Thermiques | THERMAL SYSTEM, IN PARTICULAR A CLIMATE SYSTEM FOR A MOTOR VEHICLE |
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| JPWO2018185841A1 (en) * | 2017-04-04 | 2020-02-13 | 三菱電機株式会社 | Refrigeration cycle device |
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