JP3397806B2 - Method for producing refrigeration cycle using second generation refrigerant - Google Patents
Method for producing refrigeration cycle using second generation refrigerantInfo
- Publication number
- JP3397806B2 JP3397806B2 JP19656592A JP19656592A JP3397806B2 JP 3397806 B2 JP3397806 B2 JP 3397806B2 JP 19656592 A JP19656592 A JP 19656592A JP 19656592 A JP19656592 A JP 19656592A JP 3397806 B2 JP3397806 B2 JP 3397806B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigeration cycle
- compressor
- refrigerant
- oil
- gas
- 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 - Fee Related
Links
- 238000005057 refrigeration Methods 0.000 title claims description 28
- 239000003507 refrigerant Substances 0.000 title claims description 21
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 239000010696 ester oil Substances 0.000 claims description 10
- 239000003921 oil Substances 0.000 claims description 7
- 238000007664 blowing Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 17
- 239000010721 machine oil Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 7
- 229910001873 dinitrogen Inorganic materials 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 238000005219 brazing Methods 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- -1 -125 Chemical compound 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- XPDWGBQVDMORPB-UHFFFAOYSA-N Fluoroform Chemical compound FC(F)F XPDWGBQVDMORPB-UHFFFAOYSA-N 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 239000002480 mineral oil Substances 0.000 description 2
- 235000010446 mineral oil Nutrition 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000013557 residual solvent Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000005437 stratosphere Substances 0.000 description 1
Landscapes
- Compressor (AREA)
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は、冷凍サイクルの製造方
法に関し、特に詳しくは第二世代の冷媒を使用した冷凍
サイクルの製造方法に関するものである。
【0002】
【従来の技術】冷媒の圧縮/膨張を繰り返して、冷/暖
房運転や冷凍などを行うタイプの冷凍サイクルでは、昔
はアンモニアが、近年はフロンが広く冷媒として使用さ
れている。フロンは周知のように燃性、爆発性、毒性が
なく、また、通常の状態では金属を腐食することがない
など、極めて使用特性に優れている。
【0003】しかし、化学的に極めて安定であるとして
広く使用されてきたフロンも、大気中に放出されると成
層圏に入り、紫外線によって分解されるまで極めて長期
間に渡って滞留し、紫外線を遮って地上の人間を含む生
物を保護しているオゾン層を破壊するとして、その使用
が国際的に制限されて来ている。このため、従来使用の
フロンに代替し得る無害なフロンの開発が鋭意進められ
ており、一部には既に第二世代冷媒と呼ばれているHC
FC−22、−123、−141b、HFC−134a
などのフロンが開発されている。
【0004】しかし、新規に開発されたこれら第二世代
のフロンは、何れも従来使用のフロンCFC−11、−
12、−502、−131b1などに比べると、冷凍機
油として従来使用してきた鉱油や合成油との相性が悪
く、二液に分離するので駆動部が摩耗したり、スラッジ
を生成し易いと云った問題点がある。
【0005】このため、第二世代フロンと相性の良い冷
凍機油の開発・改良も鋭意進められており、例えば新規
に開発したヒンダードエステルなどの特殊エステル油を
使用することにより、この問題を解決しようとする試み
があるが、この特殊エステル油には水分吸着性が大凡2
000ppmと従来の鉱油の水分吸着性50ppm程度
より極めて高いと云った性質があり、従来と同様にシス
テムを組み上げたのでは、システム内に多量の水分が残
留することになり、この水分が冷媒の断熱膨張時に氷結
して膨張弁を詰まらせ、冷凍作用が行われなくなる。ま
た、水分がHFCと特殊エステル油に作用して加水分解
して有機酸を生じ、金属部を腐食すると云った問題点も
あった。
【0006】
【発明が解決しようとする課題】したがって、現在開発
されているHCFC−22、−123、−141b、H
FC−134aなどの第二世代冷媒と、ヒンダードエス
テルなどの特殊エステル油を冷凍機油として使用しなが
ら、冷凍サイクル内に残留する水分量を可能な限り減少
させ、実用可能な冷凍サイクルの製造方法を開発する必
要があった。
【0007】
【課題を解決するための手段】本発明は上記従来技術の
課題を解決するための具体的手段として、第二世代冷媒
を使用すると共に冷凍機油として特殊エステル油を使用
する冷凍サイクルの製造方法であって、冷凍機油を注入
した圧縮機を加熱し、該圧縮機の下部側に設けたチャー
ジ口から水分が20ppm以下の低水分ガスを吹き込む
と同時に、上部側に設けた排気口から吸引排気し、内部
を減圧状態に保ってガス置換と水分排出とを行い、前記
吸引排気を終了し、前記低水分ガスの吹き込みを継続し
て内圧を大気圧を越える状態に保持し、該圧縮機を配管
接続することを特徴とする第二世代冷媒使用冷凍サイク
ルの製造方法を提供することにより、前記した従来技術
の課題を解決するものである。
【0008】
【作用】圧縮機は上部の排気口から吸引排気されて減圧
状態になっており、しかも、加熱されているため内部に
残留している水分や溶剤などは容易に蒸発する。そし
て、下部のチャージ口から水分量が20ppm以下(好
ましくは10ppm以下)の低水分ガスが吹き込まれて
いるので、下部から上部に向かう気流が生じており、こ
の気流に乗って前記蒸発した水や溶剤の蒸気が容易に排
出される。
【0009】圧縮機の内部が低水分ガスに置換された
後、前記吸引排気のみを停止し、前記低水分ガスの吹き
込みは続けて、内圧を大気圧より大きい状態に保って配
管接続するため、冷凍機油による水分の吸収が効果的に
防止される。
【0010】
【実施例】以下、図面に基づいて本発明の一実施例を説
明すると、符号1は冷凍サイクルの圧縮機であり、下部
側に設けたチャージパイプ口11に接続したゴムホース
2Aを介して、例えば水分量が20ppm以下(好まし
くは10ppm以下)の窒素ガスが充填された窒素ガス
ボンベ3を連結し、ゲージ圧0.2〜0.5Kgf/c
m2 gの圧力に減圧して注入可能となっている。
【0011】また、圧縮機1の上部側の排気口12に、
真空排気用のゴムホース2Bを介して排気能力が、例え
ば100〜300l/分、0.01〜0.04torr程度
の真空ポンプ4を接続し、内部に存するガスを吸引・排
気することができるようになっている。
【0012】なお、符号5は圧縮機1を、例えば70〜
90℃程度に加熱するための加熱手段であり、熱量を調
節して所定の温度に保持できるようになっている。
【0013】そして、組み立てと有機溶剤(例えば、塩
素系の1.1.1トリクロロエタンなど)による洗浄お
よび乾燥が終了した圧縮機に冷凍機油としての特殊エス
テル油を封入し、加熱手段5により例えば大略80℃に
加熱・保持し、
【0014】続いて、真空ポンプ4を駆動して、例えば
300l/分の吸引排気を行いながら、窒素ガスボンベ
3の圧力をレギュレータ31を介して、例えばゲージ圧
0.4Kgf/cm2 gに減圧して、チャージ口11か
ら窒素ガスを1〜15ml/分の割合で注入し、15分
間に渡ってガス置換と水分排出とを行った。
【0015】そして、真空ポンプ4による吸引排気のみ
を中止し、別のラインに移し、冷凍サイクル組み付け時
に圧縮機1の冷媒吸入口13と冷媒吐出口14とに、銅
製の冷媒管(図示せず)を、銀ろう付けにより冷媒管を
ろう付け接続した。このろう付け時の酸化スケール生成
防止に、前記低水分の窒素ガスを利用することで作業効
率も向上する。さらに、冷媒に第二世代冷媒の一つであ
るフロンR−134aを封入して、冷凍サイクルを製造
した。
【0016】上記ガス置換中の圧縮機1の内部は、40
0〜500mmHgに減圧されており、しかも、圧縮機
1は上記したように大略80℃に加熱されているため、
内部に残留していた水分や溶剤は容易に蒸発してガス置
換のために注入された低水分窒素ガスと共に排出され
る。
【0017】表1は、冷凍機油としての特殊エステル油
に平衡水分量が10ppmのA(共同石油社製、品番α
−32S−C)と、B(ICI社製、品番106)とを
使用して冷凍サイクルを製造し、大略3ケ月の冷凍運転
を行った後に、冷媒蒸気を分析した結果である。
【0018】
【表1】
【0019】表1から明らかなように、本発明の方法に
よって製造した冷凍サイクルでは、従来法により製造し
た場合より、HFC−134aの純成分が増加してい
る。また、水分量に関係するHFC−23、−125、
反応生成物と見られるC3 HF5 、C3 H2 F6 、C4
H2 F6 、その他のF化合物、それに毒性のあるCFC
−1123などが従来法では検出されたが、本発明の方
法で製造したときには、これら何れの化合物は全く検出
されなかった。
【0020】したがって、本発明によれば、第二世代冷
媒としてHFC−134a、−32、−125、−14
3aなどを単独、あるいは2種・3種などの組合せ物と
し、これと特殊エステル油を冷凍機油として使用するこ
とにより、実用可能な冷凍サイクルを製造することがで
きる。
【0021】なお、本発明は上記実施例に限定されるも
のではないので、特許請求の範囲に記載の趣旨から逸脱
しない範囲で各種の変形実施が可能である。例えば圧縮
機1に注入する低水分ガスとしては、内部の水分や残留
溶剤などを排出するものであり、また、銀ろうや銅ろう
などによって配管接続する際に、金属が酸化しないよう
に保護する機能持つものであれば良いので、水分量が2
0ppm以下のアルゴンガス、ヘリウムガス、二酸化炭
素であっても良い。
【0022】
【発明の効果】以上説明したように本発明は、第二世代
冷媒を使用すると共に冷凍機油として特殊エステル油を
使用する冷凍サイクルの製造方法であって、冷凍機油を
注入した圧縮機を加熱し、該圧縮機の下部側に設けたチ
ャージ口から水分が20ppm以下の低水分ガスを吹き
込むと同時に、上部側に設けた排気口から吸引排気し、
内部を減圧状態に保ってガス置換と水分排出とを行い、
前記吸引排気を終了し、前記低水分ガスの吹き込みを継
続して内圧を大気圧を越える状態に保持し、該圧縮機を
配管接続することを特徴とする第二世代冷媒使用冷凍サ
イクルの製造方法であるので、圧縮機内に残留していた
水分や溶剤をある限度以下に保つことが可能である。
【0023】このため、冷媒の圧縮/膨張を繰り返して
も氷結して膨張弁を詰まらせることがないし、フロンが
加水分解して酸を生じることもないので、金属部を腐食
することがないから、脂肪酸鉄塩とその重合物の生成も
抑制できることで、長期に渡って正常に機能する冷凍サ
イクルが製造できる。
【0024】特に、冷凍サイクルの組立工程に浄油機や
注油機がなく、油封入済みの圧縮機を用いて組み立てる
冷凍サイクルの組み立てに顕著な効果を奏する。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a refrigeration cycle, and more particularly to a method for manufacturing a refrigeration cycle using a second generation refrigerant. 2. Description of the Related Art In a refrigeration cycle of a type in which a refrigerant is repeatedly compressed / expanded to perform a cooling / heating operation or refrigeration, ammonia has been widely used in the past, and in recent years, chlorofluorocarbon has been widely used as a refrigerant. As is well known, chlorofluorocarbon has extremely excellent use characteristics, such as being nonflammable, explosive, and toxic, and not corroding metals under normal conditions. However, CFCs, which have been widely used because they are extremely stable chemically, enter the stratosphere when released into the atmosphere, stay there for a very long time until they are decomposed by ultraviolet rays, and block ultraviolet rays. Its use has been restricted internationally as it destroys the ozone layer that protects living organisms, including humans on the ground. For this reason, harmless chlorofluorocarbons that can be used in place of conventional chlorofluorocarbons are being developed intensively.
FC-22, -123, -141b, HFC-134a
CFCs have been developed. However, these newly-developed CFCs of the second generation are both CFC-11 and CFC-11, which are conventionally used.
Compared with 12, -502, -131b1, etc., it has poor compatibility with mineral oil or synthetic oil conventionally used as a refrigerating machine oil, and is separated into two liquids, so that the drive part is worn or sludge is easily generated. There is a problem. [0005] For this reason, the development and improvement of refrigerating machine oils compatible with the second-generation Freon are also being actively pursued. For example, the use of newly developed special ester oils such as hindered esters solves this problem. Attempts have been made, but this special ester oil has a water absorption
000 ppm, which is much higher than the conventional water absorption of mineral oil of about 50 ppm. If the system is assembled in the same manner as before, a large amount of water will remain in the system, and this water will During the adiabatic expansion, it freezes and clogs the expansion valve, so that the refrigeration operation is not performed. There is also a problem that water acts on HFC and special ester oil to hydrolyze to generate organic acids, thereby corroding metal parts. [0006] Therefore, the currently developed HCFC-22, -123, -141b, H
Using a second-generation refrigerant such as FC-134a and a special ester oil such as a hindered ester as a refrigerating machine oil, reducing the amount of water remaining in the refrigeration cycle as much as possible, and producing a practical refrigeration cycle. Had to be developed. SUMMARY OF THE INVENTION The present invention is directed to a refrigeration cycle using a second-generation refrigerant and a special ester oil as a refrigerating machine oil. A method of manufacturing, comprising heating a compressor into which refrigerating machine oil has been injected, blowing low-moisture gas having a water content of 20 ppm or less from a charge port provided on a lower side of the compressor, and simultaneously discharging a low-moisture gas from an exhaust port provided on an upper side. Suction and exhaust are performed, and gas replacement and moisture discharge are performed while maintaining the inside in a reduced pressure state.The suction and exhaust is terminated, the blowing of the low moisture gas is continued, and the internal pressure is maintained at a level exceeding atmospheric pressure. An object of the present invention is to solve the above-mentioned problem of the related art by providing a method for manufacturing a refrigeration cycle using a second generation refrigerant, which is characterized by connecting a machine with a pipe. The compressor is sucked and evacuated from the upper exhaust port to be in a decompressed state. Further, since the compressor is heated, moisture and solvent remaining in the compressor easily evaporate. Since a low-moisture gas having a water content of 20 ppm or less (preferably 10 ppm or less) is blown from the lower charging port, an air current is generated from the lower portion to the upper portion. Solvent vapors are easily discharged. After the inside of the compressor is replaced with low-moisture gas, only the suction and exhaust are stopped, and the blowing of the low-moisture gas is continued to connect the pipes while maintaining the internal pressure at a level higher than the atmospheric pressure. Moisture absorption by the refrigerating machine oil is effectively prevented. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. Reference numeral 1 denotes a compressor of a refrigeration cycle, which is connected via a rubber hose 2A connected to a charge pipe port 11 provided on the lower side. Then, for example, a nitrogen gas cylinder 3 filled with nitrogen gas having a water content of 20 ppm or less (preferably 10 ppm or less) is connected, and the gauge pressure is 0.2 to 0.5 kgf / c.
The pressure can be reduced to a pressure of m 2 g and injection is possible. Also, an exhaust port 12 on the upper side of the compressor 1
A vacuum pump 4 having an evacuation capacity of, for example, about 100 to 300 l / min and about 0.01 to 0.04 torr is connected via a vacuum evacuation rubber hose 2B so that gas existing inside can be sucked and exhausted. Has become. Reference numeral 5 denotes the compressor 1, for example, 70 to
It is a heating means for heating to about 90 ° C., and is capable of adjusting the amount of heat and maintaining a predetermined temperature. Then, a special ester oil as a refrigerating machine oil is sealed in a compressor which has been assembled and washed and dried with an organic solvent (for example, chlorine-based 1.1.1 trichloroethane). Subsequently, the pressure of the nitrogen gas cylinder 3 is adjusted to, for example, a gauge pressure of 0. 0 through the regulator 31 while the vacuum pump 4 is driven to perform suction and exhaust at, for example, 300 l / min. The pressure was reduced to 4 kgf / cm 2 g, nitrogen gas was injected from the charge port 11 at a rate of 1 to 15 ml / min, and gas replacement and water discharge were performed for 15 minutes. Then, only the suction and evacuation by the vacuum pump 4 is stopped, the system is moved to another line, and a copper refrigerant pipe (not shown) is connected to the refrigerant suction port 13 and the refrigerant discharge port 14 of the compressor 1 when the refrigeration cycle is assembled. ) Was connected to the refrigerant tube by silver brazing. By using the low-moisture nitrogen gas to prevent the formation of oxide scale during the brazing, the working efficiency is also improved. Further, a refrigeration cycle was manufactured by enclosing Freon R-134a, one of the second generation refrigerants, in the refrigerant. The interior of the compressor 1 during the gas replacement is 40
Since the pressure is reduced to 0 to 500 mmHg and the compressor 1 is heated to approximately 80 ° C. as described above,
The water and solvent remaining inside are easily evaporated and discharged together with the low-moisture nitrogen gas injected for gas replacement. Table 1 shows that a special ester oil as a refrigerating machine oil having an equilibrium water content of 10 ppm A (manufactured by Kyodo Sekiyu, part number α)
-32S-C) and B (manufactured by ICI, part number 106), a refrigeration cycle was manufactured, and after performing a refrigeration operation for approximately three months, the results of analysis of refrigerant vapor are shown. [Table 1] As is evident from Table 1, the refrigeration cycle manufactured by the method of the present invention has an increased pure component of HFC-134a as compared with the case of manufacturing by the conventional method. Further, HFC-23, -125,
C 3 HF 5 , C 3 H 2 F 6 , C 4
H 2 F 6 , other F compounds, and toxic CFCs
Although -1123 and the like were detected by the conventional method, none of these compounds were detected at all when produced by the method of the present invention. Therefore, according to the present invention, HFC-134a, -32, -125, -14
A practical refrigeration cycle can be manufactured by using 3a alone or in combination of two or three types and using a special ester oil as a refrigerating machine oil. Since the present invention is not limited to the above embodiment, various modifications can be made without departing from the spirit of the appended claims. For example, the low-moisture gas to be injected into the compressor 1 is for discharging internal water, residual solvent, and the like, and protects the metal from being oxidized when the pipe is connected with silver brazing or copper brazing. As long as it has a function, the water content is 2
0 ppm or less of argon gas, helium gas, and carbon dioxide may be used. As described above, the present invention relates to a method for producing a refrigeration cycle using a second-generation refrigerant and using a special ester oil as a refrigeration oil, wherein the compressor is provided with a refrigeration oil. Is heated, and a low moisture gas having a water content of 20 ppm or less is blown from a charge port provided on a lower side of the compressor, and, at the same time, suction and exhaust is performed from an exhaust port provided on an upper side,
Perform gas replacement and moisture discharge while keeping the inside under reduced pressure,
A method for producing a refrigeration cycle using a second generation refrigerant, wherein the suction / exhaust is terminated, the blowing of the low moisture gas is continued, the internal pressure is maintained at a level exceeding atmospheric pressure, and the compressor is connected to a pipe. Therefore, it is possible to keep the moisture and solvent remaining in the compressor below a certain limit. For this reason, even if the refrigerant is repeatedly compressed / expanded, it does not freeze and clog the expansion valve, and since hydrofluorocarbon is not hydrolyzed to generate an acid, it does not corrode metal parts. In addition, since the production of fatty acid iron salt and its polymer can be suppressed, a refrigeration cycle that functions normally for a long period of time can be manufactured. In particular, there is a remarkable effect in assembling a refrigeration cycle using an oil-filled compressor without an oil purifier or a lubricator in the refrigeration cycle assembly process.
【図面の簡単な説明】 【図1】一実施例の装置構成図である。 【符号の説明】 1 圧縮機 11 チャージ口 12 排気口 13 冷媒吸入口 14 冷媒吐出口 2A、2B ゴムホース 3 窒素ガスボンベ 31 レギュレータ 4 真空ポンプ 5 加熱手段[Brief description of the drawings] FIG. 1 is an apparatus configuration diagram of an embodiment. [Explanation of symbols] 1 compressor 11 Charge port 12 exhaust port 13 Refrigerant inlet 14 Refrigerant outlet 2A, 2B rubber hose 3 Nitrogen gas cylinder 31 Regulator 4 Vacuum pump 5 heating means
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F25B 49/02 F04B 39/16 F25B 1/00 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) F25B 49/02 F04B 39/16 F25B 1/00
Claims (1)
として特殊エステル油を使用する冷凍サイクルの製造方
法であって、冷凍機油を注入した圧縮機を加熱し、該圧
縮機の下部側に設けたチャージ口から水分が20ppm
以下の低水分ガスを吹き込むと同時に、上部側に設けた
排気口から吸引排気し、内部を減圧状態に保ってガス置
換と水分排出とを行い、前記吸引排気を終了し、前記低
水分ガスの吹き込みを継続して内圧を大気圧を越える状
態に保持し、該圧縮機を配管接続することを特徴とする
第二世代冷媒使用冷凍サイクルの製造方法。(57) [Claim 1] A method for producing a refrigeration cycle using a second-generation refrigerant and using a special ester oil as a refrigeration oil, wherein a compressor into which the refrigeration oil is injected is heated. 20 ppm of water from a charge port provided on the lower side of the compressor
Simultaneously with blowing in the following low moisture gas, suction and exhaust are performed through an exhaust port provided on the upper side, gas replacement and moisture discharge are performed while maintaining the inside under reduced pressure, and the suction and exhaust is completed, and the low moisture gas is discharged. A method for producing a refrigeration cycle using a second generation refrigerant, wherein blowing is continued to maintain the internal pressure above atmospheric pressure, and the compressor is connected to a pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19656592A JP3397806B2 (en) | 1992-06-30 | 1992-06-30 | Method for producing refrigeration cycle using second generation refrigerant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19656592A JP3397806B2 (en) | 1992-06-30 | 1992-06-30 | Method for producing refrigeration cycle using second generation refrigerant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0618129A JPH0618129A (en) | 1994-01-25 |
| JP3397806B2 true JP3397806B2 (en) | 2003-04-21 |
Family
ID=16359853
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19656592A Expired - Fee Related JP3397806B2 (en) | 1992-06-30 | 1992-06-30 | Method for producing refrigeration cycle using second generation refrigerant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3397806B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4187020B2 (en) | 2006-08-08 | 2008-11-26 | ダイキン工業株式会社 | Air conditioner and cleaning method thereof |
-
1992
- 1992-06-30 JP JP19656592A patent/JP3397806B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0618129A (en) | 1994-01-25 |
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