JPH0474628B2 - - Google Patents
Info
- Publication number
- JPH0474628B2 JPH0474628B2 JP19079085A JP19079085A JPH0474628B2 JP H0474628 B2 JPH0474628 B2 JP H0474628B2 JP 19079085 A JP19079085 A JP 19079085A JP 19079085 A JP19079085 A JP 19079085A JP H0474628 B2 JPH0474628 B2 JP H0474628B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- boiling point
- main circuit
- composition
- rich
- 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.)
- Expired
Links
- 239000003507 refrigerant Substances 0.000 claims description 60
- 239000000203 mixture Substances 0.000 claims description 35
- 238000009835 boiling Methods 0.000 claims description 33
- 230000007423 decrease Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 238000005057 refrigeration Methods 0.000 description 5
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 3
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Central Heating Systems (AREA)
Description
産業上の利用分野
本発明は、近年、特に注目を浴びるようになつ
た非共沸混合冷媒および回転数可変型圧縮機を用
いた空調装置等の熱ポンプ装置に関する。
従来の技術
従来、空調装置や給湯装置等に利用されている
非共沸混合冷媒および回転数可変型圧縮機を用い
た熱ポンプ装置の冷凍サイクルは、従来からよく
知られた第4図に示すようなものであつた。第4
図において、1は回転数可変型圧縮機、2は凝縮
器、3は絞り装置、4は蒸発器で順に配管接続し
て構成されている。また、圧縮機1を駆動するた
めに、交流電源5および、周波数変換器6が電気
回路として接続されている。また、従来こういう
冷凍サイクルを運転する場合の周波数変換器6か
ら出力される周波数および電圧の関係は、第3図
に示すように、比較的低周波数では、周波数と電
圧が比例するような関係に、また、比較的高周波
数では、電圧が一定となるような関係になつてい
た。また、非共混合冷媒の沸点が低い場合には、
高低圧、冷媒循環量とも増大してモータ負荷トル
クが増し、また、逆に沸点が高い場合には、高低
圧、冷媒循環量とも減少してモータ負荷トルクが
減るため、冷凍サイクル内に沸点の低い非共沸混
合冷媒を流す時には、入力電圧を若干高めにし、
全周波数で運転し逆に沸点の高い非共沸混合冷媒
を流す時には、入力電圧を若干低めにし、全周波
数で運転して常にその冷媒に対してモータ効率の
最適となる所で運転し、そうすることによつて、
非共沸混合冷媒を使用した時のEER(冷凍出力/
電気入力)の値を、単一冷媒使用時よりも上回る
ことが可能となつていた。
発明が解決しようとする問題点
一方、近年、熱ポンプ装置の年間消費電力をさ
らに減少させようという動きの中で、回転数可変
型圧縮機と、ある決まつた組成の非共沸混合冷媒
で熱ポンプ装置を運転しても、単一冷媒使用時よ
りも、その効果は上がるものの、熱ポンプ装置の
負荷に常に対応し、年間消費電力から見てその効
果を充分に発揮できる運転というものが困難にな
つてきている。すなわち、比較的沸点の低い非共
沸混合冷媒を用いて全周波数を運転する場合、圧
縮機の吸入比容積が減少して冷媒循環量が増加す
るため、高能力が出せ、高周波数運転時、すなわ
ち、負荷の大きいところでは、非常にEERも高
く維持できたが、低周波数運転時、すなわち負荷
の小さい所では、従来のように、圧縮機への入力
電圧を調節しても、冷媒のもつ能力が大きいた
め、負荷とのつり合いがとれにくい等の問題があ
つて、EERに対して、あまり大きな効果は得ら
れなかつた。また、比較的沸点の高い非共沸混合
冷媒を用いて全周波数を運転する場合には、逆
に、吸入比容積が増加して冷媒循環量が減少する
ため、低能力が出せ、低周波数運転時、すなわ
ち、負荷の小さいところでは、EERも高く維持
できたが、高周波数運転時、すなわち、負荷の大
きいところでは、従来のように圧縮機への入力電
圧を調節しても、冷媒のもつ能力が小さいため負
荷とつり合いがとれにくい等の問題があつて
EERに対して、あまり大きな効果は得られなか
つた。
すなわち、ある沸点の非共沸混合冷媒を回転数
可変型圧縮機で運転し、かつ、従来のように回転
数可変型圧縮機への入力電圧を調節しても、その
冷媒でEERが最適となるような負荷範囲(周波
数範囲)は限られており、実際に年間で負荷が大
きく変化するような熱ポンプ装置の場合、負荷が
大きく変化しても、やむを得ず、同じ沸点を持つ
た非共沸混合冷媒を使用してEERの最適となる
圧縮機入力電圧を調節して運転していたため、年
間消費電力から考えると、その効果はあまり大き
いとは言えなかつた。
そこで、本発明は、負荷のいかなる変化に対し
ても常に負荷に対応した能力が出せ、年間消費電
力をさらに減少することのできる熱ポンプ装置を
提供することを目的とする。
問題点を解決するための手段
本発明は上記目的を達成するために、非共沸混
合冷媒を用い、回転数可変型圧縮機、凝縮器、第
一絞り装置、蒸発器を配管接続して主回路とな
し、前記主回路内の冷媒組成を可変する手段を備
え、前記回転数可変型圧縮機の運転周波数(F)と前
記回転数可変型圧縮機のモータ入力電圧(V)との比
(V/F)を前記主回路内の組成が低沸点成分に
富む場合には高めに、高沸点成分に富む場合には
低めに設定したものである。
作 用
上記構成によれば、熱ポンプ装置の負荷が増大
した場合、副回路からなる冷媒組成可変手段詳し
しくは、冷媒精留作用によつて主回路内は、低沸
点成分に富み、その結果、高低圧、冷媒循環量が
増大するため、モータ負荷トルクが増す。したが
つて同一周波数で若干モータへの入力電圧を高め
ることによつてモータ効率の最適となるところで
運転することができ、冷媒として最適な負荷範囲
で運転し、かつ、その時回転数可変型圧縮機とし
ても最適な運転をすることができるものである。
また、負荷が減少した場合には逆に、高沸点成分
に富んだ組成として、モータ負荷トルクも減少す
るため、若干、入力電圧を下げることによつて同
様に最適な運転を保ち得るものである。
実施例
本発明になる熱ポンプ装置の一実施例を第1図
および第2図に基づいて説明する。ここにおい
て、7は回転数可変型圧縮機(以下圧縮機と呼
ぶ)、8は凝縮機、9は第一絞り装置、10は第
二絞り装置、11は蒸発器であり、冷凍サイクル
の主回路では7,8,9,11で構成されてい
る。12は冷媒精留塔、13は塔頂貯留器、14
は塔底貯留器、15a,bは電磁弁であり組成可
変手段の副回路は10,12,13,14,15
a,15bで構成されている。また、塔底貯留器
14内には加熱源16が、塔頂貯留器13内には
冷却源17が配置されている。また、圧縮機7を
駆動するために交流電源18が周波数変換器19
を通して供給されている。以上のように構成され
た熱ポンプ装置において、その作用は次のようで
あつた。圧縮機7より吐出された冷媒ガスは、実
線矢印の方向へ流れ、凝縮器8で液化し、分岐点
Aで二方向に分流され、一方は、絞り装置9に流
入して低圧まで膨張する。もう一方は、塔底貯留
器14に流入し、そこで加熱源16によつて流入
冷媒が加熱され沸騰する。主回路内を高沸点成分
に富んだものとするには電磁弁15aを閉、15
bを開とすることにより、いわゆる精留作用によ
り塔底貯留器14内で発生した低沸点冷媒ガスが
上昇し、下降する液と熱、物質交換しながら、非
常に低沸点成分に富んだガスとなつて上昇し、冷
却源17で冷却液化して塔頂貯留器13内に溜ま
る。一方、低沸点成分に富んだガスが気化して残
された高沸点成分に富んだ液は、電磁弁15bを
通つて第二絞り装置10に流入して合流点Bで、
先に述べた第一絞り装置9を出た冷媒と合流す
る。このようにして、主回路は、高沸点成分に富
んだ冷媒組成となつていく。また、逆に、主回路
内を低沸点成分に富んだものとするには、電磁弁
15aを開、15bを閉とすることにより、塔底
貯留器14内に高沸点成分に富んだ冷媒が貯留さ
れて、低沸点成分に富んだ冷媒が主回路内へ流入
していき達成される。
このように、電磁弁15aを開放、電磁弁15
bを閉止することにより、塔底貯留器14に高沸
点冷媒が貯留され、主回路はその結果低沸点組成
に富んだ冷媒となり、また、電磁弁15aを閉止
し、電磁弁15bを開放することにより、主回路
は高沸点成分に富んだ冷媒となる。したがつて、
組成そのものを検出しなくても、電磁弁15a、
電磁弁15bの開閉操作に応じて主回路内の冷媒
組成を変化させ、圧縮機7の運転周波数(F)とモー
タ入力電圧(V)との比(V/F)を変えるものであ
る。そして、
熱ポンプ装置の負荷が大きい場合には、能力が
大きく出る低沸点成分に富んだ成分で、かつ、周
波数の高い領域で運転することが、負荷との対
応、EER的にも良くその時には、前述の如く、
高低圧とも上昇し、冷媒循環量も増大するため、
モータの負荷トルクは増す。そこで、モータへの
入力電圧を若干高めにすることによつてモータ効
率の最適となる点で運転することが可能となる。
また逆に、熱ポンプ装置の負荷が小さい場合に
は、能力の少ない高沸点成分に富んだ成分で、か
つ、周波数の低い領域で運転するのが負荷対応
性、EER的にも良く、その時には、前述の如く、
高低圧ともに低下し冷媒循環量も減少するため、
モータ負荷トルクは減る。そこで、モータへの入
力電圧を若干低めにすることによつてモータ効率
の最適となる点で運転することが可能となる。
具体的には、第2図で示す如く、横に運転周波
数、縦にモータ入力電圧をとれば、図の実線で示
したような主回路組成、および周波数に対する電
圧で運転する方法が最良である。すなわち、熱ポ
ンプ装置の負荷、言いかえれば運転周波数(F)に応
じて、主回路内に流れる冷媒組成を可変にし、圧
縮機7の運転周波数(F)とモータ入力電圧(V)との比
(V/F)を主回路内の組成が低沸点成分に富む
場合には高めに、高沸点成分に富む場合には低め
に設定することによつて、その時の負荷に対応し
た最適な冷媒組成およびモータ入力電圧で運転で
き、EERは常に最適となる。
また、本発明を実験的に検証するために、非共
沸混合冷媒として低沸点成分のR22と高沸点成分
のR12を用い、一台の空冷の冷凍サイクル(エア
コン)を用い、組成を可変するバイパス回路を付
加せずに運転する。この場合、冷媒としては冷媒
R22を20%および冷媒R12を80%それぞれ混合し
た混合冷媒Aと、冷媒R22を60%および冷媒R12
を40%それぞれ混合した混合冷媒Bとを別々に封
入した。すなわち、組成を可変するバイパス回路
を付加して運転した場合に起こる主回路の組成変
化(AからB)を別々の混合冷媒を封入して確認
した結果を表に示している。表から明らかなよう
に、低負荷時(30Hz運転時)においては、混合冷
媒Aで運転すると電圧が51VでEERがその周波
数、その組成での最大値3.95になり、混合冷媒B
で運転すると電圧が58VでEERがその周波数、そ
の組成での最大値3.84となつた。すなわち、圧縮
機7の運転周波数(F)とモータ入力電圧(V)との比
(V/F)の値は、低沸点組成に富んだ混合冷媒
Bのときの方が混合冷媒Aのときよりも高めに設
定することによつてEERもそのときの最大値に
なることを示す。同様に高負荷時(75Hz運転時)
については、組成を可変するバイパス回路を付加
して運転した場合には、V/Fの値を高沸点組成
に富んでいる場合より高めに設定することによ
り、EERが最大となることを示す。ここでは、
周波数を一定にした実験で比較しているので、能
力は若干の差異が出るが、能力を合わせた実験を
行なつても同様の結果を得ており、本実験によ
り、本発明の効果が検証できた。
TECHNICAL FIELD The present invention relates to a heat pump device such as an air conditioner using a non-azeotropic mixed refrigerant and a variable rotation speed compressor, which has recently attracted particular attention. Conventional technology The refrigeration cycle of a heat pump device using a non-azeotropic mixed refrigerant and a variable speed compressor, which is conventionally used in air conditioners, water heaters, etc., is shown in Fig. 4, which is well known in the past. It was something like that. Fourth
In the figure, 1 is a variable rotation speed compressor, 2 is a condenser, 3 is a throttle device, and 4 is an evaporator, which are connected in order through piping. Further, in order to drive the compressor 1, an AC power source 5 and a frequency converter 6 are connected as an electric circuit. Furthermore, when operating this type of refrigeration cycle, the relationship between the frequency and voltage output from the frequency converter 6 is such that at relatively low frequencies, the frequency and voltage are proportional, as shown in Figure 3. Also, at relatively high frequencies, the relationship was such that the voltage was constant. In addition, if the boiling point of the non-comixed refrigerant is low,
Both high and low pressure and refrigerant circulation amount increase, resulting in an increase in motor load torque. Conversely, when the boiling point is high, both high and low pressure and refrigerant circulation amount decrease, reducing motor load torque. When flowing a low-temperature non-azeotropic refrigerant mixture, increase the input voltage slightly,
When operating at full frequency and flowing a non-azeotropic refrigerant mixture with a high boiling point, the input voltage is slightly lowered, and the motor is operated at full frequency to ensure optimum motor efficiency for that refrigerant. By doing,
EER (refrigeration output/
It became possible to exceed the value of electrical input (electrical input) compared to when using a single refrigerant. Problems to be Solved by the Invention On the other hand, in recent years, amidst the movement to further reduce the annual power consumption of heat pump equipment, there has been a trend towards variable speed compressors and non-azeotropic refrigerant mixtures with a certain fixed composition. Although operating a heat pump device is more effective than when using a single refrigerant, it is not possible to operate the heat pump device in such a way that it can always handle the load of the heat pump device and fully demonstrate its effectiveness in terms of annual power consumption. It's getting difficult. In other words, when operating at all frequencies using a non-azeotropic mixed refrigerant with a relatively low boiling point, the specific suction volume of the compressor decreases and the refrigerant circulation amount increases, so high capacity can be achieved, and during high frequency operation, In other words, the EER could be maintained at a very high level under heavy loads, but during low-frequency operation, that is, under low loads, even if the input voltage to the compressor was adjusted as in the past, the refrigerant's Due to the large capacity, there were problems such as difficulty in balancing the load, so it did not have much effect on EER. In addition, when operating at full frequency using a non-azeotropic mixed refrigerant with a relatively high boiling point, conversely, the suction specific volume increases and the refrigerant circulation amount decreases, making it possible to achieve low capacity and operate at low frequencies. However, during high frequency operation, that is, when the load is large, even if the input voltage to the compressor is adjusted as in the past, the EER of the refrigerant can be maintained high. Due to the small capacity, there are problems such as difficulty in balancing the load.
There was no significant effect on EER. In other words, even if a non-azeotropic refrigerant mixture with a certain boiling point is operated in a variable speed compressor and the input voltage to the variable speed compressor is adjusted as in the past, the EER will not be optimal for that refrigerant. The load range (frequency range) in which this occurs is limited, and in the case of heat pump equipment where the load changes greatly over the year, even if the load changes greatly, it is unavoidable to use non-azeotropic heat pumps with the same boiling point. Since the compressor was operated using a mixed refrigerant and adjusting the compressor input voltage to optimize EER, the effect could not be said to be very large in terms of annual power consumption. SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a heat pump device that can always provide a capacity corresponding to the load regardless of any changes in the load, and can further reduce annual power consumption. Means for Solving the Problems In order to achieve the above object, the present invention uses a non-azeotropic mixed refrigerant and connects a variable speed compressor, a condenser, a first throttling device, and an evaporator with piping. a circuit, comprising means for varying the refrigerant composition in the main circuit, and a ratio between the operating frequency (F) of the variable rotation speed compressor and the motor input voltage (V) of the variable rotation speed compressor ( V/F) is set higher when the composition in the main circuit is rich in low boiling point components, and set lower when the composition is rich in high boiling point components. Effect According to the above configuration, when the load on the heat pump device increases, the refrigerant composition variable means consisting of the sub-circuit specifically, the main circuit is enriched with low boiling point components due to the refrigerant rectification action, and as a result, , high and low pressure, and the amount of refrigerant circulation increase, so the motor load torque increases. Therefore, by slightly increasing the input voltage to the motor at the same frequency, it is possible to operate the motor at its optimum efficiency. However, it is possible to drive optimally.
In addition, when the load decreases, the motor load torque decreases as the composition is rich in high boiling point components, so it is possible to maintain optimal operation by slightly lowering the input voltage. . Embodiment An embodiment of a heat pump device according to the present invention will be described based on FIGS. 1 and 2. Here, 7 is a variable speed compressor (hereinafter referred to as a compressor), 8 is a condenser, 9 is a first throttle device, 10 is a second throttle device, and 11 is an evaporator, which is the main circuit of the refrigeration cycle. It is composed of 7, 8, 9, and 11. 12 is a refrigerant rectification column, 13 is a top reservoir, 14
15a and 15b are electromagnetic valves, and 10, 12, 13, 14, 15 are subcircuits of composition variable means.
It is composed of a and 15b. Further, a heating source 16 is arranged in the tower bottom reservoir 14 and a cooling source 17 is arranged in the tower top reservoir 13. Also, in order to drive the compressor 7, the AC power supply 18 is connected to a frequency converter 19.
is supplied through. In the heat pump device configured as described above, the operation was as follows. The refrigerant gas discharged from the compressor 7 flows in the direction of the solid arrow, is liquefied in the condenser 8, and is split into two directions at the branch point A, one of which flows into the expansion device 9 and expands to a low pressure. The other flows into the bottom reservoir 14 where the incoming refrigerant is heated by the heating source 16 to boiling. To make the main circuit rich in high boiling point components, close the solenoid valve 15a,
By opening b, the low boiling point refrigerant gas generated in the tower bottom reservoir 14 rises due to the so-called rectification effect, and while exchanging heat and material with the descending liquid, a gas rich in extremely low boiling point components is generated. It rises, is cooled and liquefied by the cooling source 17, and accumulates in the tower top reservoir 13. On the other hand, the gas rich in low boiling point components is vaporized and the liquid rich in high boiling point components left behind flows into the second throttle device 10 through the electromagnetic valve 15b, and at the confluence point B,
It joins with the refrigerant that has exited the first throttle device 9 mentioned earlier. In this way, the main circuit has a refrigerant composition rich in high boiling point components. Conversely, in order to make the main circuit rich in low boiling point components, by opening the solenoid valve 15a and closing the solenoid valve 15b, a refrigerant rich in high boiling point components is added to the bottom reservoir 14. This is achieved by the stored refrigerant rich in low boiling point components flowing into the main circuit. In this way, the solenoid valve 15a is opened and the solenoid valve 15a is opened.
By closing b, the high boiling point refrigerant is stored in the tower bottom reservoir 14, and as a result, the main circuit becomes a refrigerant rich in low boiling point composition, and the solenoid valve 15a is closed and the solenoid valve 15b is opened. As a result, the main circuit becomes a refrigerant rich in high boiling point components. Therefore,
Even if the composition itself is not detected, the solenoid valve 15a,
The refrigerant composition in the main circuit is changed according to the opening/closing operation of the solenoid valve 15b, and the ratio (V/F) between the operating frequency (F) of the compressor 7 and the motor input voltage (V) is changed. When the load on the heat pump equipment is large, it is recommended to use a component rich in low boiling point components that can increase the capacity and operate in a high frequency range, in order to cope with the load and improve EER. , as mentioned above,
Both high and low pressures rise and the amount of refrigerant circulation increases,
The motor load torque increases. Therefore, by increasing the input voltage to the motor a little higher, it becomes possible to operate the motor at a point where the motor efficiency is optimized.
On the other hand, when the load on the heat pump equipment is small, it is better to operate the heat pump in a low-frequency region with a high-boiling-point component with low capacity, and in terms of load response and EER. , as mentioned above,
As both high and low pressures decrease and the amount of refrigerant circulating decreases,
Motor load torque decreases. Therefore, by lowering the input voltage to the motor slightly, it becomes possible to operate the motor at a point where the motor efficiency is optimized. Specifically, as shown in Figure 2, if you take the operating frequency horizontally and the motor input voltage vertically, the best method is to operate with the main circuit composition and voltage versus frequency as shown by the solid line in the diagram. . In other words, the composition of the refrigerant flowing in the main circuit is varied according to the load of the heat pump device, in other words, the operating frequency (F), and the ratio between the operating frequency (F) of the compressor 7 and the motor input voltage (V) is changed. By setting (V/F) higher when the composition in the main circuit is rich in low-boiling point components and lower when it is rich in high-boiling point components, the optimal refrigerant composition corresponding to the load at that time can be set. and motor input voltage, and the EER is always optimal. In addition, in order to experimentally verify the present invention, we used R22, a low boiling point component, and R12, a high boiling point component, as a non-azeotropic mixed refrigerant, and used one air-cooled refrigeration cycle (air conditioner) to vary the composition. Operate without adding a bypass circuit. In this case, the refrigerant is
Mixed refrigerant A, which is a mixture of 20% R22 and 80% refrigerant R12, and 60% refrigerant R22 and refrigerant R12
and mixed refrigerant B, which was a mixture of 40% of each, were separately sealed. That is, the table shows the results of checking the composition change (from A to B) of the main circuit that occurs when the main circuit is operated with the addition of a bypass circuit that changes the composition by sealing different mixed refrigerants. As is clear from the table, at low load (30Hz operation), when operating with mixed refrigerant A, the voltage is 51V and the EER reaches the maximum value of 3.95 at that frequency and composition, and when mixed refrigerant B
When operated at a voltage of 58V, the EER reached the maximum value of 3.84 at that frequency and composition. In other words, the value of the ratio (V/F) between the operating frequency (F) of the compressor 7 and the motor input voltage (V) is higher when mixed refrigerant B is rich in low boiling point composition than when mixed refrigerant A is used. This shows that by setting EER to a high value, EER will also reach its maximum value at that time. Similarly, at high load (75Hz operation)
For this case, when a bypass circuit that changes the composition is added and the system is operated, the EER is maximized by setting the V/F value higher than when the fuel is rich in high-boiling point compositions. here,
Since the comparison was made using an experiment with a constant frequency, there will be some differences in performance, but similar results were obtained even when the performance was combined, and this experiment verified the effectiveness of the present invention. did it.
【表】
発明の効果
以上述べた如く、本発明は、非共沸混合冷媒を
用い、負荷に応じて主回路内を流れる冷媒組成を
可変し、その時の回転数可変型圧縮機の運転周波
数に応じて、入力電圧を可変することにより、常
にEERを最適に保つ効果がある。また、モータ
効率を高く維持することが可能となるので、モー
タの発熱の低下、振動の減少等、信頼性の向上に
寄与する効果も大となる。[Table] Effects of the Invention As described above, the present invention uses a non-azeotropic mixed refrigerant to vary the refrigerant composition flowing in the main circuit according to the load, and adjusts the operating frequency of the variable rotation speed compressor at that time. By varying the input voltage accordingly, it is effective to always keep the EER at the optimum level. Furthermore, since it is possible to maintain high motor efficiency, effects such as reduction in heat generation and vibration of the motor, which contribute to improvement in reliability, are also significant.
第1図は本発明の一実施例における熱ポンプ装
置の原理図、第2図は本発明の一実施例における
熱ポンプ装置の回転数可変型圧縮機への入力電圧
を周波数および主回路内を流れる冷媒組成に対し
て示した特性図、第3図は従来の回転数可変型圧
縮機への入力電圧を周波数および熱ポンプ装置内
冷媒組成に対して示した特性図、第4図は従来の
非共沸混合冷媒、および回転数可変型圧縮機を用
いた熱ポンプ装置の原理図である。
7……回転数可変型圧縮機、8……凝縮機、9
……第一絞り装置、10……第二絞り装置、11
……蒸発器、12……冷媒精留塔、13……塔頂
貯留器、14……塔底貯留器、15……電磁弁、
16……加熱源、17……冷却器、18……交流
電源、19……周波数変換器。
Fig. 1 is a principle diagram of a heat pump device according to an embodiment of the present invention, and Fig. 2 is a diagram showing the input voltage to the variable rotation speed compressor of the heat pump device according to an embodiment of the present invention. A characteristic diagram showing the flowing refrigerant composition; Figure 3 is a characteristic diagram showing the input voltage to a conventional variable speed compressor with respect to frequency and refrigerant composition in the heat pump device; FIG. 2 is a principle diagram of a heat pump device using a non-azeotropic mixed refrigerant and a variable rotation speed compressor. 7... variable speed compressor, 8... condenser, 9
...First squeezing device, 10...Second squeezing device, 11
...Evaporator, 12...Refrigerant rectification column, 13...Tower top reservoir, 14...Tower bottom reservoir, 15...Solenoid valve,
16... Heating source, 17... Cooler, 18... AC power supply, 19... Frequency converter.
Claims (1)
機、凝縮器、第一絞り装置、蒸発器を配管接続し
て主回路となし、前記主回路内の冷媒組成を可変
する手段を備え、前記回転数可変型圧縮機の運転
周波数(F)と前記回転数可変型圧縮機のモータ入力
電圧(V)との比(V/F)を前記主回路内の組成が
低沸点成分に富む場合には高めに、高沸点成分に
富む場合には低めに設定した熱ポンプ装置。 2 冷媒組成を可変する手段は、冷媒精留塔、塔
頂貯留器、第二絞り装置、電磁弁を配管接続する
とともに主回路の凝縮器の出口と蒸発器の入口と
をバイパスする回路からなる特許請求の範囲第1
項記載の熱ポンプ装置。[Claims] 1. Using a non-azeotropic mixed refrigerant, a variable rotation speed compressor, a condenser, a first throttling device, and an evaporator are connected via piping to form a main circuit, and the refrigerant composition in the main circuit is The ratio (V/F) between the operating frequency (F) of the variable rotation speed compressor and the motor input voltage (V) of the variable rotation speed compressor is controlled by the composition in the main circuit. The heat pump device is set at a higher temperature when it is rich in low boiling point components, and at a lower temperature when it is rich in high boiling point components. 2. The means for varying the refrigerant composition consists of a circuit that connects the refrigerant rectification column, the top reservoir, the second throttling device, and the solenoid valve with piping and bypasses the condenser outlet and evaporator inlet of the main circuit. Claim 1
Heat pump device as described in Section 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60190790A JPS6252368A (en) | 1985-08-29 | 1985-08-29 | heat pump equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60190790A JPS6252368A (en) | 1985-08-29 | 1985-08-29 | heat pump equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6252368A JPS6252368A (en) | 1987-03-07 |
| JPH0474628B2 true JPH0474628B2 (en) | 1992-11-26 |
Family
ID=16263781
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60190790A Granted JPS6252368A (en) | 1985-08-29 | 1985-08-29 | heat pump equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6252368A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5499508A (en) * | 1993-03-30 | 1996-03-19 | Kabushiki Kaisha Toshiba | Air conditioner |
| JP3341500B2 (en) * | 1994-11-25 | 2002-11-05 | 株式会社日立製作所 | Refrigeration apparatus and operating method thereof |
-
1985
- 1985-08-29 JP JP60190790A patent/JPS6252368A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6252368A (en) | 1987-03-07 |
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