JP5519224B2 - Refrigeration circuit - Google Patents
Refrigeration circuit Download PDFInfo
- Publication number
- JP5519224B2 JP5519224B2 JP2009210260A JP2009210260A JP5519224B2 JP 5519224 B2 JP5519224 B2 JP 5519224B2 JP 2009210260 A JP2009210260 A JP 2009210260A JP 2009210260 A JP2009210260 A JP 2009210260A JP 5519224 B2 JP5519224 B2 JP 5519224B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- refrigeration circuit
- fluorinated hydrocarbon
- unsaturated fluorinated
- ether
- 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 50
- 239000003507 refrigerant Substances 0.000 claims description 82
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 38
- 239000004215 Carbon black (E152) Substances 0.000 claims description 37
- 229930195733 hydrocarbon Natural products 0.000 claims description 37
- 150000002430 hydrocarbons Chemical class 0.000 claims description 37
- 239000004593 Epoxy Substances 0.000 claims description 16
- 150000001335 aliphatic alkanes Chemical class 0.000 claims description 15
- 230000007246 mechanism Effects 0.000 claims description 9
- 239000000314 lubricant Substances 0.000 claims description 8
- 239000003921 oil Substances 0.000 claims description 7
- 230000006835 compression Effects 0.000 claims description 6
- 238000007906 compression Methods 0.000 claims description 6
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 5
- 229910045601 alloy Inorganic materials 0.000 claims description 5
- 239000000956 alloy Substances 0.000 claims description 5
- 229910052782 aluminium Inorganic materials 0.000 claims description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 5
- 239000010721 machine oil Substances 0.000 claims description 5
- 229910052749 magnesium Inorganic materials 0.000 claims description 5
- 239000011777 magnesium Substances 0.000 claims description 5
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 239000002826 coolant Substances 0.000 claims 1
- 239000012188 paraffin wax Substances 0.000 description 14
- 238000000354 decomposition reaction Methods 0.000 description 13
- 239000010687 lubricating oil Substances 0.000 description 13
- 239000007787 solid Substances 0.000 description 13
- 229910052751 metal Inorganic materials 0.000 description 12
- 239000002184 metal Substances 0.000 description 12
- 230000015572 biosynthetic process Effects 0.000 description 8
- 238000006116 polymerization reaction Methods 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 150000001336 alkenes Chemical class 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 239000007769 metal material Substances 0.000 description 6
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 6
- 229920001515 polyalkylene glycol Polymers 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- RWRIWBAIICGTTQ-UHFFFAOYSA-N difluoromethane Chemical compound FCF RWRIWBAIICGTTQ-UHFFFAOYSA-N 0.000 description 4
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 4
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 4
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 4
- 230000001050 lubricating effect Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 229920001451 polypropylene glycol Polymers 0.000 description 3
- 230000001737 promoting effect Effects 0.000 description 3
- 238000010792 warming Methods 0.000 description 3
- NSGXIBWMJZWTPY-UHFFFAOYSA-N 1,1,1,3,3,3-hexafluoropropane Chemical compound FC(F)(F)CC(F)(F)F NSGXIBWMJZWTPY-UHFFFAOYSA-N 0.000 description 2
- NPNPZTNLOVBDOC-UHFFFAOYSA-N 1,1-difluoroethane Chemical compound CC(F)F NPNPZTNLOVBDOC-UHFFFAOYSA-N 0.000 description 2
- HNRMPXKDFBEGFZ-UHFFFAOYSA-N 2,2-dimethylbutane Chemical compound CCC(C)(C)C HNRMPXKDFBEGFZ-UHFFFAOYSA-N 0.000 description 2
- FXRLMCRCYDHQFW-UHFFFAOYSA-N 2,3,3,3-tetrafluoropropene Chemical compound FC(=C)C(F)(F)F FXRLMCRCYDHQFW-UHFFFAOYSA-N 0.000 description 2
- ZFFMLCVRJBZUDZ-UHFFFAOYSA-N 2,3-dimethylbutane Chemical compound CC(C)C(C)C ZFFMLCVRJBZUDZ-UHFFFAOYSA-N 0.000 description 2
- WGECXQBGLLYSFP-UHFFFAOYSA-N 2,3-dimethylpentane Chemical compound CCC(C)C(C)C WGECXQBGLLYSFP-UHFFFAOYSA-N 0.000 description 2
- GVNVAWHJIKLAGL-UHFFFAOYSA-N 2-(cyclohexen-1-yl)cyclohexan-1-one Chemical compound O=C1CCCCC1C1=CCCCC1 GVNVAWHJIKLAGL-UHFFFAOYSA-N 0.000 description 2
- GXDHCNNESPLIKD-UHFFFAOYSA-N 2-methylhexane Chemical compound CCCCC(C)C GXDHCNNESPLIKD-UHFFFAOYSA-N 0.000 description 2
- FDMFUZHCIRHGRG-UHFFFAOYSA-N 3,3,3-trifluoroprop-1-ene Chemical compound FC(F)(F)C=C FDMFUZHCIRHGRG-UHFFFAOYSA-N 0.000 description 2
- AORMDLNPRGXHHL-UHFFFAOYSA-N 3-ethylpentane Chemical compound CCC(CC)CC AORMDLNPRGXHHL-UHFFFAOYSA-N 0.000 description 2
- VLJXXKKOSFGPHI-UHFFFAOYSA-N 3-methylhexane Chemical compound CCCC(C)CC VLJXXKKOSFGPHI-UHFFFAOYSA-N 0.000 description 2
- PFEOZHBOMNWTJB-UHFFFAOYSA-N 3-methylpentane Chemical compound CCC(C)CC PFEOZHBOMNWTJB-UHFFFAOYSA-N 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 2
- 101150065749 Churc1 gene Proteins 0.000 description 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 102100038239 Protein Churchill Human genes 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000003112 inhibitor Substances 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- CRSOQBOWXPBRES-UHFFFAOYSA-N neopentane Chemical compound CC(C)(C)C CRSOQBOWXPBRES-UHFFFAOYSA-N 0.000 description 2
- GTLACDSXYULKMZ-UHFFFAOYSA-N pentafluoroethane Chemical compound FC(F)C(F)(F)F GTLACDSXYULKMZ-UHFFFAOYSA-N 0.000 description 2
- MSSNHSVIGIHOJA-UHFFFAOYSA-N pentafluoropropane Chemical compound FC(F)CC(F)(F)F MSSNHSVIGIHOJA-UHFFFAOYSA-N 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- FFTOUVYEKNGDCM-OWOJBTEDSA-N (e)-1,3,3-trifluoroprop-1-ene Chemical compound F\C=C\C(F)F FFTOUVYEKNGDCM-OWOJBTEDSA-N 0.000 description 1
- YFMFNYKEUDLDTL-UHFFFAOYSA-N 1,1,1,2,3,3,3-heptafluoropropane Chemical compound FC(F)(F)C(F)C(F)(F)F YFMFNYKEUDLDTL-UHFFFAOYSA-N 0.000 description 1
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 1
- WZLFPVPRZGTCKP-UHFFFAOYSA-N 1,1,1,3,3-pentafluorobutane Chemical compound CC(F)(F)CC(F)(F)F WZLFPVPRZGTCKP-UHFFFAOYSA-N 0.000 description 1
- YCBCLGNNEUTCEC-UHFFFAOYSA-N 1,1,1,3,4-pentafluorobut-2-ene Chemical compound FCC(F)=CC(F)(F)F YCBCLGNNEUTCEC-UHFFFAOYSA-N 0.000 description 1
- UJPMYEOUBPIPHQ-UHFFFAOYSA-N 1,1,1-trifluoroethane Chemical compound CC(F)(F)F UJPMYEOUBPIPHQ-UHFFFAOYSA-N 0.000 description 1
- PGJHURKAWUJHLJ-UHFFFAOYSA-N 1,1,2,3-tetrafluoroprop-1-ene Chemical compound FCC(F)=C(F)F PGJHURKAWUJHLJ-UHFFFAOYSA-N 0.000 description 1
- LNGDLROYEAUMEQ-UHFFFAOYSA-N 1,1,2-trifluoroprop-1-ene Chemical compound CC(F)=C(F)F LNGDLROYEAUMEQ-UHFFFAOYSA-N 0.000 description 1
- BNYODXFAOQCIIO-UHFFFAOYSA-N 1,1,3,3-tetrafluoroprop-1-ene Chemical compound FC(F)C=C(F)F BNYODXFAOQCIIO-UHFFFAOYSA-N 0.000 description 1
- URZZGOOCQOQVOC-UHFFFAOYSA-N 1,1,3-trifluoroprop-1-ene Chemical compound FCC=C(F)F URZZGOOCQOQVOC-UHFFFAOYSA-N 0.000 description 1
- ZUAQTIHDWIHCSV-UHFFFAOYSA-N 1,2,3,3-tetrafluoroprop-1-ene Chemical compound FC=C(F)C(F)F ZUAQTIHDWIHCSV-UHFFFAOYSA-N 0.000 description 1
- DSZTYVZOIUIIGA-UHFFFAOYSA-N 1,2-Epoxyhexadecane Chemical compound CCCCCCCCCCCCCCC1CO1 DSZTYVZOIUIIGA-UHFFFAOYSA-N 0.000 description 1
- DDMOUSALMHHKOS-UHFFFAOYSA-N 1,2-dichloro-1,1,2,2-tetrafluoroethane Chemical compound FC(F)(Cl)C(F)(F)Cl DDMOUSALMHHKOS-UHFFFAOYSA-N 0.000 description 1
- CDOOAUSHHFGWSA-UHFFFAOYSA-N 1,3,3,3-tetrafluoropropene Chemical compound FC=CC(F)(F)F CDOOAUSHHFGWSA-UHFFFAOYSA-N 0.000 description 1
- FAOACLKUNWKVPH-UHFFFAOYSA-N 2,3,3,4,4,4-hexafluorobut-1-ene Chemical compound FC(=C)C(F)(F)C(F)(F)F FAOACLKUNWKVPH-UHFFFAOYSA-N 0.000 description 1
- ZHKVUSSHABANQG-UHFFFAOYSA-N 2,3,3,4,4,5,5-heptafluoropent-1-ene Chemical compound FC(F)C(F)(F)C(F)(F)C(F)=C ZHKVUSSHABANQG-UHFFFAOYSA-N 0.000 description 1
- WMNDUXWIOZPSJD-UHFFFAOYSA-N 2,3,3,4,4-pentafluorobut-1-ene Chemical compound FC(F)C(F)(F)C(F)=C WMNDUXWIOZPSJD-UHFFFAOYSA-N 0.000 description 1
- JMRIJKGIVGYIAD-UHFFFAOYSA-N 2,3,3-trifluoroprop-1-ene Chemical compound FC(F)C(F)=C JMRIJKGIVGYIAD-UHFFFAOYSA-N 0.000 description 1
- BZHMBWZPUJHVEE-UHFFFAOYSA-N 2,3-dimethylpentane Natural products CC(C)CC(C)C BZHMBWZPUJHVEE-UHFFFAOYSA-N 0.000 description 1
- NHGSUDHIUKAWHN-UHFFFAOYSA-N 2,4,4,4-tetrafluoro-3-(trifluoromethyl)but-1-ene Chemical compound FC(=C)C(C(F)(F)F)C(F)(F)F NHGSUDHIUKAWHN-UHFFFAOYSA-N 0.000 description 1
- IYOLYUNUVFIFIE-UHFFFAOYSA-N 2-(difluoromethyl)-3,3-difluoroprop-1-ene Chemical compound FC(F)C(=C)C(F)F IYOLYUNUVFIFIE-UHFFFAOYSA-N 0.000 description 1
- MPGABYXKKCLIRW-UHFFFAOYSA-N 2-decyloxirane Chemical compound CCCCCCCCCCC1CO1 MPGABYXKKCLIRW-UHFFFAOYSA-N 0.000 description 1
- IOHJQSFEAYDZGF-UHFFFAOYSA-N 2-dodecyloxirane Chemical compound CCCCCCCCCCCCC1CO1 IOHJQSFEAYDZGF-UHFFFAOYSA-N 0.000 description 1
- CEUXMUYHMURJFZ-UHFFFAOYSA-N 2-heptadecyloxirane Chemical compound CCCCCCCCCCCCCCCCCC1CO1 CEUXMUYHMURJFZ-UHFFFAOYSA-N 0.000 description 1
- GXOYTMXAKFMIRK-UHFFFAOYSA-N 2-heptyloxirane Chemical compound CCCCCCCC1CO1 GXOYTMXAKFMIRK-UHFFFAOYSA-N 0.000 description 1
- QBJWYMFTMJFGOL-UHFFFAOYSA-N 2-hexadecyloxirane Chemical compound CCCCCCCCCCCCCCCCC1CO1 QBJWYMFTMJFGOL-UHFFFAOYSA-N 0.000 description 1
- LXVAZSIZYQIZCR-UHFFFAOYSA-N 2-nonyloxirane Chemical compound CCCCCCCCCC1CO1 LXVAZSIZYQIZCR-UHFFFAOYSA-N 0.000 description 1
- AAMHBRRZYSORSH-UHFFFAOYSA-N 2-octyloxirane Chemical compound CCCCCCCCC1CO1 AAMHBRRZYSORSH-UHFFFAOYSA-N 0.000 description 1
- XSNXNMMWBCZUSS-UHFFFAOYSA-N 2-pentadecyloxirane Chemical compound CCCCCCCCCCCCCCCC1CO1 XSNXNMMWBCZUSS-UHFFFAOYSA-N 0.000 description 1
- QMIBIXKZPBEGTE-UHFFFAOYSA-N 2-tridecyloxirane Chemical compound CCCCCCCCCCCCCC1CO1 QMIBIXKZPBEGTE-UHFFFAOYSA-N 0.000 description 1
- QMIWYOZFFSLIAK-UHFFFAOYSA-N 3,3,3-trifluoro-2-(trifluoromethyl)prop-1-ene Chemical compound FC(F)(F)C(=C)C(F)(F)F QMIWYOZFFSLIAK-UHFFFAOYSA-N 0.000 description 1
- NTJPBRSQUATARU-UHFFFAOYSA-N 3,3,4,4,4-pentafluoro-2-(trifluoromethyl)but-1-ene Chemical compound FC(F)(F)C(=C)C(F)(F)C(F)(F)F NTJPBRSQUATARU-UHFFFAOYSA-N 0.000 description 1
- IZHPSCJEIFFRLN-UHFFFAOYSA-N 3,3,4,4,4-pentafluorobut-1-ene Chemical compound FC(F)(F)C(F)(F)C=C IZHPSCJEIFFRLN-UHFFFAOYSA-N 0.000 description 1
- LQAPOTKKMIZDGP-UHFFFAOYSA-N 3,3,4,4,5,5,5-heptafluoropent-1-ene Chemical compound FC(F)(F)C(F)(F)C(F)(F)C=C LQAPOTKKMIZDGP-UHFFFAOYSA-N 0.000 description 1
- GVEUEBXMTMZVSD-UHFFFAOYSA-N 3,3,4,4,5,5,6,6,6-nonafluorohex-1-ene Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C=C GVEUEBXMTMZVSD-UHFFFAOYSA-N 0.000 description 1
- RBMOVUILDUBRGH-UHFFFAOYSA-N 3,3,4,5,5,5-hexafluoropent-1-ene Chemical compound FC(F)(F)C(F)C(F)(F)C=C RBMOVUILDUBRGH-UHFFFAOYSA-N 0.000 description 1
- YOIHZDOLVJDWDY-UHFFFAOYSA-N 3,4,4,4-tetrafluoro-3-(trifluoromethyl)but-1-ene Chemical compound FC(F)(F)C(F)(C=C)C(F)(F)F YOIHZDOLVJDWDY-UHFFFAOYSA-N 0.000 description 1
- VJOOWZFVJAJKPV-UHFFFAOYSA-N 4,4,5,5,6,6,6-heptafluorohex-1-ene Chemical compound FC(F)(F)C(F)(F)C(F)(F)CC=C VJOOWZFVJAJKPV-UHFFFAOYSA-N 0.000 description 1
- DVQRFCKQKDQEER-UHFFFAOYSA-N 4,5,5,5-tetrafluoro-4-(trifluoromethyl)pent-1-ene Chemical compound FC(F)(F)C(F)(C(F)(F)F)CC=C DVQRFCKQKDQEER-UHFFFAOYSA-N 0.000 description 1
- PMPVIKIVABFJJI-UHFFFAOYSA-N Cyclobutane Chemical compound C1CCC1 PMPVIKIVABFJJI-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- LVZWSLJZHVFIQJ-UHFFFAOYSA-N Cyclopropane Chemical compound C1CC1 LVZWSLJZHVFIQJ-UHFFFAOYSA-N 0.000 description 1
- YSMRWXYRXBRSND-UHFFFAOYSA-N TOTP Chemical compound CC1=CC=CC=C1OP(=O)(OC=1C(=CC=CC=1)C)OC1=CC=CC=C1C YSMRWXYRXBRSND-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000002516 radical scavenger Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Images
Landscapes
- Lubricants (AREA)
Description
本発明は、冷媒の全部又は1部としてHFO1234yfに代表される不飽和フッ化炭化水素冷媒を含む冷媒が使用される冷凍回路に関する。 The present invention relates to a refrigeration circuit in which a refrigerant including an unsaturated fluorinated hydrocarbon refrigerant typified by HFO1234yf is used as all or part of the refrigerant.
車両用空調装置などに用いられる冷凍回路には現状では代表的な冷媒としてフルオロカーボンの一種であるHFC134aが使用されるとともに、代表的な冷凍機油としてポリアルキレングリコール(PAG)が使用されている。 Currently, HFC134a, which is a kind of fluorocarbon, is used as a typical refrigerant in a refrigeration circuit used for a vehicle air conditioner and the like, and polyalkylene glycol (PAG) is used as a typical refrigeration oil.
現在、世界規模で地球温暖化を防止する取り組みが盛んに進んでいる。特にEU諸国においてはフロンガス規制において、自動車用の代表的な冷媒HFC134aの高い地球温暖化係数(GWP1430)に対する規制を進め、2012年以降の新型車へのこの冷媒の使用の禁止を、また2017年以降には全ての車両へのこの冷媒の使用禁止を決定した。これを受け、世界各地域に同様の規制が波及している。この動向に対して冷媒メーカー、冷凍機油メーカー及び空調機器メーカーは、安全でありながら地球温暖化係数(GWP)などのさらなる低減と改善を目指して、新冷媒及び新冷媒用冷凍機油の研究・開発が行われている。このような改善を目指した新冷媒として現在、低GWP化を求めて分子内部に不飽和結合を導入し、蒸発温度が−50℃から−10℃の範囲にある不飽和フッ化炭化水素冷媒が次世代の冷媒として開発されている。特に、HFO1234yfやHFO1234zeなどの不飽和フッ化炭化水素冷媒が世界的に採用される見込みが有力である。これらの物質を車両用空調装置などの冷凍回路へ適用できるよう改良を目指した試験研究が盛んになってきた。 Currently, efforts are being made to prevent global warming on a global scale. In particular, in Freon gas regulation in the EU countries, promoting restrictions on high global warming potential of a typical refrigerant HFC134a for a motor vehicle (GWP1430), the prohibition of the use of the refrigerant to the new models since 2012, also 2017 Later, we decided to ban the use of this refrigerant in all vehicles. In response, similar regulations are spreading throughout the world. In response to this trend, refrigerant manufacturers, refrigeration oil manufacturers, and air conditioning equipment manufacturers are researching and developing new refrigerants and refrigeration oils for new refrigerants with the aim of further reducing and improving the Global Warming Potential (GWP) while being safe. Has been done. As a new refrigerant aiming at such improvement, an unsaturated fluorinated hydrocarbon refrigerant having an evaporating temperature in the range of −50 ° C. to −10 ° C. by introducing an unsaturated bond inside the molecule in search of low GWP is now available. Developed as the next generation refrigerant. In particular, it is probable that unsaturated fluorinated hydrocarbon refrigerants such as HFO1234yf and HFO1234ze will be adopted worldwide. Test research aimed at improving these materials so that they can be applied to refrigeration circuits such as air conditioners for vehicles has become popular.
ところが、不飽和フッ化炭化水素冷媒は低GWP値を特長のひとつとする反面、分子内に不飽和結合を有するためHFC134aをはじめとする従来の飽和フッ化炭化水素系冷媒と比較して反応性が高く熱・化学的安定性に乏しい。そこで、本発明者らは、不飽和フッ化炭化水素冷媒の代表例であるHFO1234yfについて、この冷媒を実際の冷凍回路に使用した場合の熱・化学的安定性を確認する実験を行ったところ、圧縮機としてスクロール圧縮機を使用し、冷媒としてHFO1234yfを使用し、且つ冷凍機油として代表的なポリアルキレングリコールを使用した実験系の冷凍回路では、特に高速高負荷条件下において、圧縮機内にワックス状の固形物が生成するのに対し、この実験系の冷凍回路においてスクロール圧縮機をレシプロ圧縮機に置換えた実験系の冷凍回路では、高速高負荷条件下においても、ワックス状の固形物は生成しないという事実を確認した。このワックス状の固形物は、冷凍回路の詰まりや冷凍性能の低下を引き起こすため、冷凍回路の著しい性能低下や故障などの致命的な欠陥になり得る。ワックス状の固形物の生成はHFO1234yfに限られず分子内に同様の不飽和結合を有する他の不飽和フッ化炭化水素冷媒においても生成するものと考えられる。従って、冷凍回路において不飽和フッ化炭化水素冷媒を使用する場合、特に高速高負荷条件下においてもかかるワックス状の固形物が圧縮機内や冷凍回路内に生成するのを防止する必要がある。 However, while unsaturated fluorocarbon refrigerants have a low GWP value, they have an unsaturated bond in the molecule, so they are more reactive than conventional saturated fluorocarbon refrigerants such as HFC134a. High and poor thermal and chemical stability. Therefore, the present inventors conducted an experiment to confirm the thermal and chemical stability when HFO1234yf, which is a representative example of an unsaturated fluorinated hydrocarbon refrigerant, is used in an actual refrigeration circuit. In the experimental refrigeration circuit using a scroll compressor as the compressor, HFO1234yf as the refrigerant, and a typical polyalkylene glycol as the refrigeration oil, a wax-like shape is formed in the compressor particularly under high speed and high load conditions. In contrast, the experimental refrigeration circuit in which the scroll compressor is replaced with a reciprocating compressor in this experimental refrigeration circuit does not produce a waxy solid even under high-speed and high-load conditions. Confirmed the fact. This wax-like solid causes clogging of the refrigeration circuit and deterioration of the refrigeration performance, so that it can be a fatal defect such as a significant performance reduction or failure of the refrigeration circuit. The formation of a wax-like solid is not limited to HFO1234yf, but may be generated in other unsaturated fluorinated hydrocarbon refrigerants having similar unsaturated bonds in the molecule. Therefore, when an unsaturated fluorinated hydrocarbon refrigerant is used in the refrigeration circuit, it is necessary to prevent such wax-like solids from being generated in the compressor or the refrigeration circuit even under high speed and high load conditions.
従って、本発明が解決しようとする課題は、圧縮機としてスクロール圧縮機を使用し、冷媒として不飽和フッ化炭化水素冷媒を使用し、且つ冷凍機油としてポリアルキレングリコールなどのエーテル系潤滑油を使用する冷凍回路において、冷凍回路の詰まりや冷凍性能の低下の原因となるワックス状の固形物が冷凍回路内に生成するのを防止することにある。 Accordingly, the problem to be solved by the present invention is that a scroll compressor is used as a compressor, an unsaturated fluorinated hydrocarbon refrigerant is used as a refrigerant, and an ether-based lubricating oil such as polyalkylene glycol is used as a refrigerator oil. An object of the present invention is to prevent the formation of waxy solids in the refrigeration circuit that cause clogging of the refrigeration circuit and a decrease in refrigeration performance.
本発明者らはワックス状の固形物の化学分析を行い、この固形物は融点が約50℃〜72℃の低分子量の重合パラフィンであることを確認した。本発明者らはこの分析結果に基づきワックス状の固形物の生成メカニズムを次のように推定している。すなわち、スクロール圧縮機では旋回スクロールの旋回運動に伴って旋回スクロールの渦巻体と固定スクロールの渦巻体とが高温高圧の冷媒ガスの作用に対抗するために相互に強く押圧された状態で摺動するため、使用する冷凍機油には高度の潤滑性能が要求されるところ、HFO1234yfなどの不飽和結合を有する冷媒に対するポリアルキレングリコールなどのエーテル系潤滑油の潤滑性能はスクロール圧縮機にとって必ずしも充分ではない。このため、高温高負荷条件下において、旋回スクロールの旋回運動に伴い圧縮機構部の摺動表面に局部的に金属活性表面が露出し易くなる。一方、不飽和フッ化炭化水素冷媒は反応性が高く熱・化学的安定性に乏しい。その結果、露出した金属活性表面が反応触媒として作用して、スクロール圧縮機の圧縮機構部内において高温高圧の冷媒ガス雰囲気下で不飽和フッ化炭化水素冷媒とエーテル系潤滑油のポリオキシアルキレン構造との反応を誘起し、その結果不飽和フッ化炭化水素冷媒の分解と分解物たる重合性オレフィンの生成が起こり、更にこの重合性オレフィンが圧縮機内部の圧力および熱のもとで金属活性表面の重合触媒作用を受けて重合して重合パラフィンを生成するものと推定される。また、不飽和フッ化炭化水素冷媒の分解により生成するフッ化水素は不飽和フッ化炭化水素冷媒の更なる分解を助長する触媒として作用するものと推定される。従って、ワックス状の固形物の生成を防止するためには、エーテル系潤滑油の潤滑性能の不足をポリオキシアルキレン構造を有しない他の潤滑油性成分の併用により補うことが有効な手段となり得る。また、不飽和フッ化炭化水素冷媒の分解により生成するフッ化水素を捕捉する酸捕捉剤を使用することも有効な手段となり得る。本発明者らはこの観点から各種化合物について検討し、長鎖脂肪族エポキシアルカンがワックス状の固形物の生成防止に非常に効果的である事実を見出した。本発明はかかる技術的知見と着想に基づいて完成されたものである。 The present inventors conducted a chemical analysis of a waxy solid, and confirmed that this solid was a low molecular weight polymerized paraffin having a melting point of about 50 ° C to 72 ° C. Based on this analysis result, the present inventors presume the formation mechanism of a waxy solid as follows. That is, in the scroll compressor, the swirl of the orbiting scroll and the swirl of the fixed scroll slide in a state where they are strongly pressed against each other in order to counteract the action of the high-temperature and high-pressure refrigerant gas. Therefore, the refrigerating machine oil to be used is required to have a high level of lubricating performance. However, the lubricating performance of the ether-based lubricating oil such as polyalkylene glycol with respect to the refrigerant having an unsaturated bond such as HFO1234yf is not always sufficient for the scroll compressor. For this reason, the metal active surface is likely to be locally exposed on the sliding surface of the compression mechanism part with the turning motion of the orbiting scroll under the high temperature and high load condition. On the other hand, unsaturated fluorinated hydrocarbon refrigerants are highly reactive and poor in thermal and chemical stability. As a result, the exposed metal active surface acts as a reaction catalyst, and the polyoxyalkylene structure of the unsaturated fluorinated hydrocarbon refrigerant and the ether-based lubricating oil in the compression mechanism portion of the scroll compressor under a high-temperature and high-pressure refrigerant gas atmosphere. As a result, decomposition of the unsaturated fluorohydrocarbon refrigerant and formation of a polymerizable olefin as a decomposition product occur, and this polymerizable olefin is further applied to the metal active surface under pressure and heat inside the compressor. It is presumed that polymerized paraffin is produced by polymerization under the reaction of polymerization catalyst. Further, it is presumed that hydrogen fluoride produced by the decomposition of the unsaturated fluorinated hydrocarbon refrigerant acts as a catalyst for promoting further decomposition of the unsaturated fluorinated hydrocarbon refrigerant. Therefore, in order to prevent the formation of a wax-like solid, it can be an effective means to supplement the lack of lubricating performance of the ether-based lubricating oil with the combined use of other lubricating oil components having no polyoxyalkylene structure. . It is also effective to use an acid scavenger that captures hydrogen fluoride produced by the decomposition of the unsaturated fluorinated hydrocarbon refrigerant. The present inventors have studied various compounds from this viewpoint, and have found that long-chain aliphatic epoxy alkanes are very effective in preventing the formation of waxy solids. The present invention has been completed based on such technical knowledge and ideas.
すなわち、本発明の冷凍回路は、少なくとも冷媒と冷凍機油とを充填し、当該冷媒を圧縮する圧縮機として圧縮機構部がアルミニウム又はマグネシウム若しくはその合金製のスクロール圧縮機を備える冷凍回路において、当該冷媒がその一部又は全部として不飽和フッ化炭化水素冷媒を含有し、当該冷凍機油が、ポリオキシアルキレン構造を有するエーテル系潤滑油と、炭素原子数が8〜25である長鎖脂肪族エポキシアルカンとを含有することを特徴としている。また、当該長鎖エポキシアルカンは、前記エーテル系潤滑油の充填量に対し、0.5重量%〜15重量%充填されることが好ましい。さらに、長鎖エポキシアルカンは、前記冷媒の充填量に対し、0.1重量%〜3重量%充填されることが好ましい。この発明によれば、前記エポキシアルカンが、圧縮機の運転に伴い引き起される不飽和フッ化炭化水素冷媒の分解と重合性分解物の重合に起因する重合パラフィンの生成とを防止する重合パラフィン防止剤として機能する。 That is, the refrigeration circuit of the present invention, by filling a refrigerating machine oil and at least a refrigerant, the refrigeration circuit compressor mechanism as a compressor for compressing the refrigerant comprises aluminum or magnesium or scroll compressor made its alloys, the refrigerant there containing unsaturated fluorinated hydrocarbon refrigerant as part or all of the refrigerating machine oil, the ether-based lubricant having a polyoxyalkylene structure, a long-chain aliphatic epoxy alkane carbon atoms is 8 to 25 It is characterized by containing and. Moreover, it is preferable that the said long-chain epoxy alkane is filled 0.5 to 15 weight% with respect to the filling amount of the said ether type lubricating oil. Furthermore, it is preferable that the long-chain epoxy alkane is filled in an amount of 0.1 to 3% by weight with respect to the amount of the refrigerant. According to the present invention, the epoxy alkane prevents the polymerization of the unsaturated fluorinated hydrocarbon refrigerant caused by the operation of the compressor and the generation of the polymerized paraffin resulting from the polymerization of the polymerizable decomposition product. Functions as an inhibitor.
上記構成において熱・化学的安定性が特に低い分子末端にCH 2 =CH−又はCH 2 =CF−の基を有する不飽和フッ化炭化水素冷媒が用いられる場合にも、重合パラフィンの生成を効果的に防止できる。また、上記構成において不飽和フッ化炭化水素冷媒として代表的なHFO1234yf及びHFO1234zeが用いられる場合にも、重合パラフィンの生成を効果的に防止できる。
Especially low molecular terminals thermal and chemical stability in the
本発明の冷凍回路は、家電、住宅空調、流通分野などに利用されるあらゆる冷凍回路に適用可能であり、特に車両空調装置用冷凍回路として好適である。車両空調装置用冷凍回路において本発明を適用することにより、HFO1234yfなどの不飽和フッ化炭化水素冷媒を使用して環境負荷を低減し且つ従来と同様の動作安定性を達成した冷凍回路を実現することが可能となる。 The refrigeration circuit of the present invention can be applied to any refrigeration circuit used in home appliances, residential air conditioning, distribution fields, and the like, and is particularly suitable as a refrigeration circuit for a vehicle air conditioner. By applying the present invention to a refrigeration circuit for a vehicle air conditioner, an refrigeration circuit is realized that uses an unsaturated fluorohydrocarbon refrigerant such as HFO1234yf to reduce the environmental load and achieve the same operational stability as before. It becomes possible.
本発明によれば、圧縮機として圧縮機構部がアルミニウム又はマグネシウム若しくはその合金製のスクロール圧縮機を使用し、冷媒として不飽和フッ化炭化水素冷媒を充填し、且つ冷凍機油としてポリオキシアルキレン構造を有するエーテル系潤滑油を充填する冷凍回路において、エーテル系潤滑油の潤滑性能の不足を長鎖エポキシアルカンの併用により補うとともに、不飽和フッ化炭化水素冷媒の分解により生成し冷媒の更なる分解を助長するフッ化水素を長鎖エポキシアルカンのエポキシ基で捕捉することにより、圧縮機構部の摺動に伴う金属活性表面の露出を防止して、これにより圧縮機構部内において高温高圧の冷媒ガス雰囲気下で不飽和フッ化炭化水素冷媒とエーテル系潤滑油のポリオキシアルキレン構造とが露出した金属活性表面の触媒作用を受けて反応することを防止でき、その結果冷凍回路の詰まりや冷凍性能の低下の原因となる重合パラフィンの生成を防止することができる。 According to the present invention, the compressor mechanism uses a scroll compressor made of aluminum, magnesium, or an alloy thereof as a compressor, is filled with an unsaturated fluorinated hydrocarbon refrigerant as a refrigerant, and has a polyoxyalkylene structure as a refrigerator oil. In a refrigeration circuit filled with ether-based lubricants, the lack of lubrication performance of ether-based lubricants is compensated by the combined use of long-chain epoxy alkanes, and the refrigerant is further decomposed by the decomposition of unsaturated fluorinated hydrocarbon refrigerants. By capturing the promoting hydrogen fluoride with the epoxy group of the long-chain epoxy alkane, the exposure of the metal active surface due to the sliding of the compression mechanism is prevented, so that the high temperature and high pressure refrigerant gas atmosphere is maintained in the compression mechanism. Of metal activity in which unsaturated fluorocarbon refrigerant and polyoxyalkylene structure of ether-based lubricant are exposed Of undergoing catalysis can be prevented from reacting, it is possible to prevent the generation of the result causes a reduction in clogging or freezing performance of the refrigeration circuit polymerization paraffin.
図1は車両用空調装置などに用いられる冷凍回路の基本的な構成を示している。図1において、冷凍回路1は、冷媒を圧縮する圧縮機2と、圧縮した冷媒を凝縮する凝縮器3と、凝縮した冷媒を減圧・膨張させる減圧・膨張手段としての膨張弁4と、減圧・膨張した冷媒を蒸発させる蒸発器5とを備えている。この冷凍回路1中には、冷媒と所定の混合物とが充填され、当該冷凍回路1中を冷媒がその状態を変化させながら循環される。
FIG. 1 shows a basic configuration of a refrigeration circuit used in a vehicle air conditioner or the like. In FIG. 1, a
本発明で使用するスクロール圧縮機には特に制限はない。圧縮機の構成材料として鉄系材料のほか、アルミニウム、マグネシウム又はその合金などの軽金属系材料が使用可能である。圧縮機構部において可動側のスクロールは慣性力を低減させるために鉄系材料よりも比重が小さなアルミニウム、マグネシウム又はその合金などの軽金属系材料が使用される場合が多い。これらの鉄系材料や軽金属系材料はいずれも純粋の金属素材の状態では高い反応性に富んでいるが、通常はその表面は酸化被膜で覆われて金属素材の活性が抑えられた状態にある。しかし、冷凍機油の潤滑性能が不充分であると、酸化被膜が旋回スクロールの旋回運動に伴う摩擦などにより失われて金属活性表面が露出する。金属活性表面が露出すると、その金属素材の高い反応性のために、この金属活性表面は極めて高い触媒作用を呈する。従って、高温高圧状態の冷媒雰囲気下でエーテル系潤滑油と不飽和フッ化炭化水素冷媒とがこの金属活性表面に接触すると、この金属活性表面の触媒作用を受けてエーテル系潤滑油のポリオキシアルキレン構造と不飽和フッ化炭化水素冷媒が反応する。この反応により不飽和フッ化炭化水素冷媒の分解と分解物たる重合性オレフィンの生成が起こり、更にこの重合性オレフィンが金属活性表面の重合触媒作用を受けて高温高圧の冷媒ガス雰囲気下で重合して重合パラフィンを生成することになる。しかしながら、本発明によれば、エーテル系潤滑油は長鎖エポキシアルカンを含有し、この長鎖エポキシアルカンは高温高圧の冷媒ガス雰囲気下でも不飽和フッ化炭化水素冷媒と反応することはないので、エーテル系潤滑油の潤滑性能の不足を補って金属活性表面の露出を防止する一方、不飽和フッ化炭化水素冷媒の分解により生成し冷媒の更なる分解を助長するフッ化水素と反応してこれを消失させ、これにより不飽和フッ化炭化水素冷媒の分解と分解物たる重合性オレフィンの生成を防止するとともに、重合性オレフィンの重合による重合パラフィンの生成を防止する。 There is no restriction | limiting in particular in the scroll compressor used by this invention. In addition to iron-based materials, light metal materials such as aluminum, magnesium, or alloys thereof can be used as the constituent material of the compressor. In order to reduce the inertial force, a light metal material such as aluminum, magnesium, or an alloy thereof having a smaller specific gravity than the iron material is often used for the scroll on the movable side in the compression mechanism. Although these iron-based materials and light metal-based materials are both highly reactive in the state of pure metal materials, their surfaces are usually covered with an oxide film and the activity of the metal materials is suppressed. . However, when the lubricating performance of the refrigerating machine oil is insufficient, the oxide film is lost due to friction accompanying the orbiting motion of the orbiting scroll and the metal active surface is exposed. When the metal active surface is exposed, the metal active surface exhibits a very high catalytic action due to the high reactivity of the metal material. Therefore, when an ether type lubricating oil and an unsaturated fluorinated hydrocarbon refrigerant come into contact with the metal active surface in a high-temperature and high-pressure refrigerant atmosphere, the metal active surface is catalyzed and the polyoxyalkylene of the ether type lubricating oil. The structure reacts with the unsaturated fluorinated hydrocarbon refrigerant. This reaction causes the decomposition of the unsaturated fluorinated hydrocarbon refrigerant and the production of a polymerizable olefin as a decomposition product, and this polymerizable olefin undergoes polymerization catalysis on the metal active surface and polymerizes in a high-temperature and high-pressure refrigerant gas atmosphere. As a result, polymerized paraffin is produced. However, according to the present invention, the ether-based lubricating oil contains a long-chain epoxy alkane, and this long-chain epoxy alkane does not react with the unsaturated fluorinated hydrocarbon refrigerant even in a high-temperature and high-pressure refrigerant gas atmosphere. This compensates for the lack of lubrication performance of ether-based lubricants and prevents exposure of the active metal surface, while reacting with hydrogen fluoride, which is generated by the decomposition of unsaturated fluorinated hydrocarbon refrigerant and promotes further decomposition of the refrigerant. As a result, the decomposition of the unsaturated fluorinated hydrocarbon refrigerant and the production of the polymerizable olefin as a decomposition product are prevented, and the production of polymerized paraffin due to the polymerization of the polymerizable olefin is prevented.
本発明で使用される不飽和フッ化炭化水素冷媒としては、例えば1,2,3,3−テトラフルオロ−1−プロペン(HFO1234ye);1,3,3,3−テトラフルオロ−1−プロペン(HFO1234ze);2,3,3,3−テトラフルオロ−1−プロペン(HFO1234yf);1,1,2,3−テトラフルオロ−1−プロペン(HFO1234yc);1,1,3,3−テトラフルオロ−1−プロペン(HFO1234zc);2,3,3−トリフルオロ−1−プロペン(HFO1243yf);3,3,3−トリフルオロ−1−プロペン(HFO1243zf);1,1,2−トリフルオロ−1−プロペン(HFO1243yc);1,1,3−トリフルオロ−1−プロペン(HFO1243zc);1,2,3−トリフルオロ−1−プロペン(HFO1243ye);1,3,3−トリフルオロ−1−プロペン(HFO1243ze);3,3,3−トリフルオロプロペン(HFO1243zf)などのハイドロフルオロプロペン:2,3,3,4,4,4−ヘキサフルオロ−1−ブテン(CF 3 CF 2 CF=CH 2 );3,3,3−トリフルオロ−2−(トリフルオロメチル)−1−プロペン(CH 2 =C(CF 3 ) 2 );1,1,1,3,4−ペンタフルオロ−2−ブテン(CF 3 CH=CFCH 2 F);3,3,4,4,4−ペンタフルオロ−1−ブテン(CF 3 CF 2 CH=CH 2 );2,3,3,4,4−ペンタフルオロ−1−ブテン(CH 2 =CFCF 2 CHF 2 );3,3,4,4−テトラフルオロ−1−ブテン(CH 2 =CHCF 2 CHF 2 );3,3−ジフルオロ−2−(ジフルオロメチル)−1−プロペン(CH 2 =C(CHF 2 ) 2 );3,3,4,4,4−ペンタフルオロ−2−(トリフルオロメチル)−1−ブテン(CH 2 =C(CF 3 )CF 2 CF 3 );3,4,4,4−テトラフルオロ−3−(トリフルオロメチル)−1−ブテン((CF 3 ) 2 CFCH=CH 2 );2,4,4,4−テトラフルオロ−3−(トリフルオロメチル)−1−ブテン(CH 2 =CFCH(CF 3 ) 2 );4,4,4−トリフルオロ−3−(トリフルオロメチル)−1−ブテン(CH 2 =C(CF 3 )CH 2 CF 3 )などのハイドロフルオロブテン:3,3,4,4,5,5,5−ヘプタフルオロ−1−ペンテン(CF 3 CF 2 CF 2 CH=CH 2 );2,3,3,4,4,5,5−ヘプタフルオロ−1−ペンテン(CH 2 =CFCF 2 CF 2 CHF 2 );3,3,4,5,5,5−ヘキサフルオロ−1−ペンテン(CH 2 =CHCF 2 CHFCF 3 );4,5,5,5−テトラフルオロ−4−(トリフルオロメチル)−1−ペンテン(CH 2 =CHCH 2 CF(CF 3 ) 2 )などのハイドロフルオロペンテン: 3,3,4,4,5,5,6,6,6−ノナフルオロ−1−ヘキセン(CF 3 CF 2 CF 2 CF 2 CH=CH 2 );4,4,5,5,6,6,6−ヘプタフルオロ−1−ヘキセン(CH 2 =CHCH 2 CF 2 CF 2 CF 3 )などのハイドロフルオロヘキセンが挙げられる。不飽和フッ化炭化水素冷媒の中でも特に分子末端にCH 2 =CH−又はCH 2 =CF−の基を有するものはポリオキシアルキレン構造を有するエーテル系潤滑油とスクロール圧縮機内で反応して重合パラフィンを生成させる程度が分子末端にこれらの基を有しないものよりも顕著である。従って、これらの基を有する不飽和フッ化炭化水素冷媒を使用する冷凍回路に対し本発明の適用は特に有効である。
Examples of the unsaturated fluorinated hydrocarbon refrigerant used in the present invention include 1,2,3,3-tetrafluoro-1-propene ( HFO 1234ye); 1,3,3,3-tetrafluoro-1-propene. ( HFO 1234ze); 2,3,3,3-tetrafluoro-1-propene ( HFO 1234yf); 1,1,2,3-tetrafluoro-1-propene ( HFO 1234yc); 1,1,3,3 -Tetrafluoro-1-propene ( HFO 1234zc); 2,3,3-trifluoro-1-propene ( HFO 1243yf); 3,3,3-trifluoro-1-propene ( HFO 1243zf); 1,1, 2-trifluoro-1-propene (HFO 1243yc); 1,1,3- trifluoro-1-propene (HFO 1243zc); 1,2, - trifluoro-1-propene (HFO 1243ye); 1,3,3- trifluoro-1-propene (HFO 1243ze); 3,3,3- trifluoropropene (HFO 1243zf) hydrofluoropropenes such: 2, 3,3,4,4,4-hexafluoro-1-butene (CF 3 CF 2 CF═CH 2 ); 3,3,3-trifluoro-2- (trifluoromethyl) -1-propene (CH 2 ) = C (CF 3 ) 2 ); 1,1,1,3,4-pentafluoro-2-butene (CF 3 CH═CFCH 2 F); 3,3,4,4,4-pentafluoro-1- butene (CF 3 CF 2 CH = CH 2); 2,3,3,4,4- pentafluoro-1-butene (CH 2 = CFCF 2 CHF 2 ); 3,3,4,4- tetrafluoro -1 -Bu Emissions (CH 2 = CHCF 2 CHF 2 ); 3,3- difluoro-2- (difluoromethyl) -1-propene (CH 2 = C (CHF 2 ) 2); 3,3,4,4,4- penta fluoro-2- (trifluoromethyl) -1-butene (CH 2 = C (CF 3 ) CF 2 CF 3); 3,4,4,4- tetrafluoro-3- (trifluoromethyl) -1-butene ((CF 3 ) 2 CFCH═CH 2 ); 2,4,4,4-tetrafluoro-3- (trifluoromethyl) -1-butene (CH 2 ═CFCH (CF 3 ) 2 ); Hydrofluorobutenes such as 4-trifluoro-3- (trifluoromethyl) -1-butene (CH 2 ═C (CF 3 ) CH 2 CF 3 ): 3,3,4,4,5,5,5- heptafluoro-1-pentene (CF 3 F 2 CF 2 CH = CH 2 ); 2,3,3,4,4,5,5- heptafluoro-1-pentene (CH 2 = CFCF 2 CF 2 CHF 2); 3,3,4,5, 5,5-hexafluoro-1-pentene (CH 2 ═CHCF 2 CHFCF 3 ); 4,5,5,5-tetrafluoro-4- (trifluoromethyl) -1-pentene (CH 2 ═CHCH 2 CF ( CF 3) 2) hydrofluoroether pentene like: 3,3,4,4,5,5,6,6,6-nonafluoro-1-hexene (CF 3 CF 2 CF 2 CF 2 CH = CH 2); 4 , 4, 5, 5, 6, 6, 6-heptafluoro-1-hexene (CH 2 ═CHCH 2 CF 2 CF 2 CF 3 ) and the like. Particularly the molecular terminal among unsaturated fluorinated
上記化合物は単独又は2種以上の混合物として使用される。また、上記化合物とともには飽和ハロゲン化炭化水素冷媒又は炭化水素冷媒を併用することも可能である。代表的な飽和フッ化炭化水素冷媒ならびに炭化水素系冷媒としては、例えば1,1,1,2−テトラフルオロエタン(HFC134a)、1,1−ジフルオロエタン(HFC152a)、ジフルオロメタン(HFC32)、ペンタフルオロエタン(HFC125)、1,1,1−トリフルオロエタン(HFC143a)、1,1,1,2,3,3,3−ヘプタフルオロプロパン(HFC227ea)、1,1,1,3,3−ペンタフルオロブタン(HFC365mfc)、2,2,−ジクロロ−1,1,1−トリフルオロエタン(HFC123)、1,1,1,3,3−ペンタフルオロプロパン(HFC245fa)、1,2−ジクロロ−1,1,2,2−テトラフルオロエタン(HFC124)、1,1,1,3,3,3−ヘキサフルオロプロパン(HFC236fa)が挙げられる。代表的な炭化水素冷媒としては、例えばプロパン、プロピレン、シクロプロパン、n−ブタン、イソブタン、n−ペンタン、2−メチルブタン(イソペンタン)、シクロブタン、シクロペンタン、2,2−ジメチルプロパン、2,2−ジメチルブタン、2,3−ジメチルブタン、2,3−ジメチルペンタン、2−メチルヘキサン、3−メチルヘキサン、2−メチルペンタン、3−エチルペンタン、3−メチルペンタン、シクロヘキサン、n−ヘプタン、メチルシクロペンタン、およびn−ヘキサンが挙げられる。 The said compound is used individually or in mixture of 2 or more types. In addition, a saturated halogenated hydrocarbon refrigerant or a hydrocarbon refrigerant can be used in combination with the above compound. Typical saturated fluorinated hydrocarbon refrigerants and hydrocarbon refrigerants include, for example, 1,1,1,2-tetrafluoroethane ( HFC 134a), 1,1-difluoroethane ( HFC 152a), difluoromethane ( HFC 32). , Pentafluoroethane ( HFC 125), 1,1,1-trifluoroethane ( HFC 143a), 1,1,1,2,3,3,3-heptafluoropropane ( HFC 227ea), 1,1,1 , 3,3-pentafluorobutane ( HFC 365mfc), 2,2, -dichloro-1,1,1-trifluoroethane ( HFC 123), 1,1,1,3,3-pentafluoropropane ( HFC 245fa) ), 1,2-dichloro-1,1,2,2-tetrafluoroethane (HFC 124), 1,1,1,3,3,3- Hexa fluoro propane (HFC 236fa) and the like. Typical hydrocarbon refrigerants include, for example, propane, propylene, cyclopropane, n-butane, isobutane, n-pentane, 2-methylbutane (isopentane), cyclobutane, cyclopentane, 2,2-dimethylpropane, 2,2- Dimethylbutane, 2,3-dimethylbutane, 2,3-dimethylpentane, 2-methylhexane, 3-methylhexane, 2-methylpentane, 3-ethylpentane, 3-methylpentane, cyclohexane, n-heptane, methylcyclo Examples include pentane and n-hexane.
本発明で使用される長鎖エポキシアルカンとしては、例えば1,2−エポキシノナン、1,2−エポキシデカン、1,2−エポキシウンデカン、1,2−エポキシドデカン、1,2−エポキシテトラデカン、1,2−エポキシペンタデカン、1,2−エポキシヘキサデカン、1,2−エポキシヘプタデカン、1,2−エポキシオクタデカン、1,2−エポキシノナデカンなどの炭素原子数8〜25のエポキシアルカンが好ましい。長鎖エポキシアルカンのエーテル系潤滑剤に対する添加量は0.5〜15重量%が好ましく、封入冷媒量に対する添加量は0.1〜3重量%が好ましい。 Examples of the long-chain epoxy alkane used in the present invention include 1,2-epoxynonane, 1,2-epoxydecane, 1,2-epoxyundecane, 1,2-epoxydodecane, 1,2-epoxytetradecane, Epoxyalkanes having 8 to 25 carbon atoms such as 1,2-epoxypentadecane, 1,2-epoxyhexadecane, 1,2-epoxyheptadecane, 1,2-epoxyoctadecane and 1,2-epoxynonadecane are preferred. The addition amount of the long-chain epoxy alkane with respect to the ether lubricant is preferably 0.5 to 15 % by weight, and the addition amount with respect to the amount of the enclosed refrigerant is preferably 0.1 to 3% by weight.
本発明による重合パラフィンの生成防止効果は以下の実施例及び比較例により確認することができる。実施例及び比較例において図1に示される冷凍回路が用いられる。冷凍回路のスクロール圧縮機はアルミニウム合金製の固定スクロールとアルミニウム合金製にアルマイト処理された旋回スクロールとを備えている。冷凍回路内にHFO1234yf冷媒を所定量充填し、スクロール圧縮機内に表1に記載の処方の混合物を所定量充填する。実施例及び比較例のエーテル系潤滑油には極圧剤としてリン酸トリクレシルを潤滑油に対し1.0%添加する。スクロール圧縮機の回転数を6000rpmに設定し、この回転速度で400時間に亘って冷凍回路を連続運転する。運転終了後に圧縮機内及び冷凍回路の配管内を点検してワックス状の固形物(重合パラフィン)の生成の有無を確認する。この確認実験により表1に記載の結果が得られる。表1の効果の欄における判定基準は次の通りである。
○:目視で確認できる固形物は存在しない。
×:目視で確認できる固形物が存在する。
The effect of preventing formation of polymerized paraffin according to the present invention can be confirmed by the following examples and comparative examples. In the examples and comparative examples, the refrigeration circuit shown in FIG. 1 is used. The scroll compressor of the refrigeration circuit includes a fixed scroll made of aluminum alloy and a turning scroll made of aluminum alloy and anodized. A predetermined amount of HFO1234yf refrigerant is filled in the refrigeration circuit, and a predetermined amount of the mixture of the formulations shown in Table 1 is filled in the scroll compressor. To the ether-based lubricating oils of Examples and Comparative Examples, tricresyl phosphate as an extreme pressure agent is added to 1.0% of the lubricating oil. The rotation speed of the scroll compressor is set to 6000 rpm, and the refrigeration circuit is continuously operated at this rotation speed for 400 hours. After completion of the operation, the inside of the compressor and the piping of the refrigeration circuit are inspected to confirm whether waxy solids (polymerized paraffin) are generated. The results shown in Table 1 are obtained by this confirmation experiment. The judgment criteria in the column of effect in Table 1 are as follows.
○: There is no solid matter that can be visually confirmed.
X: A solid substance that can be visually confirmed exists.
上表において、PPGはポリプロピレングリコールを主構造として分子末端をエーテル変性処理したポリアルキレングリコールを表し、%は封入冷媒量に対する重量%を表す。
In the above table, PPG represents polyalkylene glycol in which polypropylene glycol is the main structure and the molecular ends are ether-modified, and% represents weight% with respect to the amount of encapsulated refrigerant.
表1に示すように、実施例1〜2のようにエーテル系潤滑油(PPG)に重合パラフィン防止剤として長鎖エポキシアルカンを添加する場合には、回転数6000rpm、連続運転時間400時間の高温高負荷条件下においても、重合パラフィンは発生しないのに対し、比較例にように長鎖エポキシアルカンを添加しない場合には、同条件下において、重合パラフィンが発生する。 As shown in Table 1, when adding a long-chain epoxy alkane as a polymerized paraffin inhibitor to an ether-based lubricating oil (PPG) as in Examples 1 and 2 , the rotation speed was 6000 rpm and the continuous operation time was 400 hours. Polymerized paraffin is not generated even under high load conditions, whereas polymerized paraffin is generated under the same conditions when no long-chain epoxy alkane is added as in the comparative example.
本発明は家電、住宅空調、流通分野などに利用されるあらゆる冷凍回路に適用可能であり、特に車両空調装置用冷凍回路において、HFO1234yfなどの不飽和フッ化炭化水素冷媒を使用して環境負荷を低減し且つ従来と同様の動作安定性を達成した冷凍回路を実現することが可能である。 The present invention can be applied to any refrigeration circuit used in home appliances, residential air conditioning, distribution fields, etc., and particularly in a refrigeration circuit for a vehicle air conditioner, using an unsaturated fluorinated hydrocarbon refrigerant such as HFO1234yf to reduce environmental impact. It is possible to realize a refrigeration circuit that reduces and achieves the same operational stability as conventional ones.
1 冷凍回路
2 圧縮機
3 凝縮器
4 減圧・膨張手段としての膨張弁
5 蒸発器
DESCRIPTION OF
Claims (5)
当該冷媒が、その一部又は全部として不飽和フッ化炭化水素冷媒を含有し、
当該冷凍機油が、ポリオキシアルキレン構造を有するエーテル系潤滑油と、炭素原子数が8〜25である長鎖エポキシアルカンとを含有することを特徴とする冷凍回路。 In a refrigeration circuit that is filled with at least a refrigerant and refrigeration oil, and the compression mechanism includes a scroll compressor made of aluminum, magnesium, or an alloy thereof as a compressor that compresses the refrigerant.
The coolant, containing the unsaturated fluorinated hydrocarbon refrigerant as part or the whole,
Refrigeration circuit to which the refrigerating machine oil, to the ether-based lubricant having a polyoxyalkylene structure, characterized in that the number of carbon atoms contains a long-chain epoxy alkanes is 8-25.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009210260A JP5519224B2 (en) | 2009-09-11 | 2009-09-11 | Refrigeration circuit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009210260A JP5519224B2 (en) | 2009-09-11 | 2009-09-11 | Refrigeration circuit |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2011057886A JP2011057886A (en) | 2011-03-24 |
JP5519224B2 true JP5519224B2 (en) | 2014-06-11 |
Family
ID=43945880
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2009210260A Expired - Fee Related JP5519224B2 (en) | 2009-09-11 | 2009-09-11 | Refrigeration circuit |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP5519224B2 (en) |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2233553A4 (en) * | 2007-10-29 | 2011-08-31 | Nippon Oil Corp | Refrigerator oil and working fluid composition for refrigerating machine |
KR101578567B1 (en) * | 2007-11-22 | 2015-12-17 | 이데미쓰 고산 가부시키가이샤 | Lubricating oil composition for refrigerating machine |
-
2009
- 2009-09-11 JP JP2009210260A patent/JP5519224B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2011057886A (en) | 2011-03-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2577435C2 (en) | Compositions for heat transfer, possessing improved mixability with liquid lubricant | |
JP5936604B2 (en) | Heat transfer fluids and their use in countercurrent heat exchangers | |
JP5749188B2 (en) | Binary composition of 2,3,3,3-tetrafluoropropene and ammonia | |
JP5983671B2 (en) | Azeotropic or azeotrope-like compositions containing 1-chloro-3,3,3-trifluoropropene and 1,1,1,3,3-pentafluoropropane | |
JP2019032155A (en) | Heat transfer process | |
WO2010146841A1 (en) | Refrigeration circuit and method for improving same | |
JP2010203759A (en) | Freezer | |
US9845419B2 (en) | Low GWP heat transfer compositions containing difluoromethane and 1,3,3,3-tetrafluoropropene | |
JP2011057885A (en) | Freezing circuit and method for improving the same | |
CN107044739B (en) | Refrigerator, method for manufacturing refrigerator, and method for improving COP | |
JP7117537B2 (en) | Method for suppressing disproportionation reaction of working fluid for refrigerating cycle and method for manufacturing working fluid for refrigerating cycle | |
WO2010146842A1 (en) | Refrigeration circuit and method for improving same | |
JP5898300B2 (en) | Composition comprising 3,3,3-trifluoropropene and ammonia | |
JP5719105B2 (en) | Refrigeration circuit | |
JP5519224B2 (en) | Refrigeration circuit | |
JP2011058747A (en) | Refrigerating circuit and method of improving the same | |
JP7389373B2 (en) | A composition containing a refrigerant, its use, a refrigerator having the same, and a method of operating the refrigerator | |
AU2016231462B2 (en) | Heat-transfer compositions exhibiting improved miscibility with the lubricating oil | |
AU2015202362B2 (en) | Heat-transfer compositions exhibiting improved miscibility with the lubricating oil |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20120405 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20130905 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20131008 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20131206 |
|
RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20131206 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20131206 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20140117 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20140312 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20140403 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 5519224 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |