CN1210368C - Halogenated hydrocarbon refrigerant compositions containing hydrocarbon oil-reture agents - Google Patents
Halogenated hydrocarbon refrigerant compositions containing hydrocarbon oil-reture agents Download PDFInfo
- Publication number
- CN1210368C CN1210368C CN 99815670 CN99815670A CN1210368C CN 1210368 C CN1210368 C CN 1210368C CN 99815670 CN99815670 CN 99815670 CN 99815670 A CN99815670 A CN 99815670A CN 1210368 C CN1210368 C CN 1210368C
- Authority
- CN
- China
- Prior art keywords
- oil
- agents
- reture
- hydrocarbon
- hfc
- 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
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 85
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 82
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 81
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 72
- 239000000203 mixture Substances 0.000 title claims abstract description 49
- 239000003507 refrigerant Substances 0.000 title claims abstract description 33
- 150000008282 halocarbons Chemical class 0.000 title description 3
- 238000005057 refrigeration Methods 0.000 claims abstract description 54
- 239000000314 lubricant Substances 0.000 claims abstract description 22
- 150000005826 halohydrocarbons Chemical class 0.000 claims description 42
- RSJKGSCJYJTIGS-UHFFFAOYSA-N undecane Chemical compound CCCCCCCCCCC RSJKGSCJYJTIGS-UHFFFAOYSA-N 0.000 claims description 21
- SNRUBQQJIBEYMU-UHFFFAOYSA-N dodecane Chemical compound CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 claims description 19
- IIYFAKIEWZDVMP-UHFFFAOYSA-N tridecane Chemical compound CCCCCCCCCCCCC IIYFAKIEWZDVMP-UHFFFAOYSA-N 0.000 claims description 18
- 229910052799 carbon Inorganic materials 0.000 claims description 16
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 14
- YCOZIPAWZNQLMR-UHFFFAOYSA-N pentadecane Chemical compound CCCCCCCCCCCCCCC YCOZIPAWZNQLMR-UHFFFAOYSA-N 0.000 claims description 13
- BGHCVCJVXZWKCC-UHFFFAOYSA-N tetradecane Chemical compound CCCCCCCCCCCCCC BGHCVCJVXZWKCC-UHFFFAOYSA-N 0.000 claims description 13
- DCAYPVUWAIABOU-UHFFFAOYSA-N hexadecane Chemical compound CCCCCCCCCCCCCCCC DCAYPVUWAIABOU-UHFFFAOYSA-N 0.000 claims description 11
- 230000006835 compression Effects 0.000 claims description 9
- 238000007906 compression Methods 0.000 claims description 9
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 5
- 229920013639 polyalphaolefin Polymers 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 238000009833 condensation Methods 0.000 claims description 2
- 230000005494 condensation Effects 0.000 claims description 2
- PFNXDLYOYLRRNH-UHFFFAOYSA-N [C].FCl Chemical compound [C].FCl PFNXDLYOYLRRNH-UHFFFAOYSA-N 0.000 claims 2
- 239000003921 oil Substances 0.000 abstract description 113
- 125000004432 carbon atom Chemical group C* 0.000 abstract description 13
- OHMHBGPWCHTMQE-UHFFFAOYSA-N 2,2-dichloro-1,1,1-trifluoroethane Chemical compound FC(F)(F)C(Cl)Cl OHMHBGPWCHTMQE-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract 2
- 239000011707 mineral Substances 0.000 abstract 2
- 239000002480 mineral oil Substances 0.000 description 28
- 235000010446 mineral oil Nutrition 0.000 description 28
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 16
- 229910052731 fluorine Inorganic materials 0.000 description 14
- 150000001721 carbon Chemical group 0.000 description 12
- 125000001153 fluoro group Chemical group F* 0.000 description 12
- 150000004996 alkyl benzenes Chemical class 0.000 description 11
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 10
- GTLACDSXYULKMZ-UHFFFAOYSA-N pentafluoroethane Chemical compound FC(F)C(F)(F)F GTLACDSXYULKMZ-UHFFFAOYSA-N 0.000 description 9
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 8
- UJPMYEOUBPIPHQ-UHFFFAOYSA-N 1,1,1-trifluoroethane Chemical compound CC(F)(F)F UJPMYEOUBPIPHQ-UHFFFAOYSA-N 0.000 description 8
- RWRIWBAIICGTTQ-UHFFFAOYSA-N difluoromethane Chemical compound FCF RWRIWBAIICGTTQ-UHFFFAOYSA-N 0.000 description 8
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 7
- 239000006200 vaporizer Substances 0.000 description 7
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 6
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 5
- 229910052802 copper Inorganic materials 0.000 description 5
- 239000010949 copper Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000010687 lubricating oil Substances 0.000 description 5
- BKIMMITUMNQMOS-UHFFFAOYSA-N nonane Chemical compound CCCCCCCCC BKIMMITUMNQMOS-UHFFFAOYSA-N 0.000 description 5
- 239000001294 propane Substances 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- NPNPZTNLOVBDOC-UHFFFAOYSA-N 1,1-difluoroethane Chemical compound CC(F)F NPNPZTNLOVBDOC-UHFFFAOYSA-N 0.000 description 4
- BOUGCJDAQLKBQH-UHFFFAOYSA-N 1-chloro-1,2,2,2-tetrafluoroethane Chemical compound FC(Cl)C(F)(F)F BOUGCJDAQLKBQH-UHFFFAOYSA-N 0.000 description 4
- XPDWGBQVDMORPB-UHFFFAOYSA-N Fluoroform Chemical compound FC(F)F XPDWGBQVDMORPB-UHFFFAOYSA-N 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 4
- 229920001515 polyalkylene glycol Polymers 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- FKCNNGCHQHSYCE-UHFFFAOYSA-N difluoromethane;1,1,1,2,2-pentafluoroethane;1,1,1,2-tetrafluoroethane Chemical compound FCF.FCC(F)(F)F.FC(F)C(F)(F)F FKCNNGCHQHSYCE-UHFFFAOYSA-N 0.000 description 3
- 239000004519 grease Substances 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- IJDNQMDRQITEOD-UHFFFAOYSA-N sec-butylidene Natural products CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- RIQRGMUSBYGDBL-UHFFFAOYSA-N 1,1,1,2,2,3,4,5,5,5-decafluoropentane Chemical compound FC(F)(F)C(F)C(F)C(F)(F)C(F)(F)F RIQRGMUSBYGDBL-UHFFFAOYSA-N 0.000 description 2
- 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 2
- 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
- LKLFXAVIFCLZQS-UHFFFAOYSA-N 1,1,2,2,3,3,4,4-octafluorobutane Chemical compound FC(F)C(F)(F)C(F)(F)C(F)F LKLFXAVIFCLZQS-UHFFFAOYSA-N 0.000 description 2
- WXGNWUVNYMJENI-UHFFFAOYSA-N 1,1,2,2-tetrafluoroethane Chemical compound FC(F)C(F)F WXGNWUVNYMJENI-UHFFFAOYSA-N 0.000 description 2
- RFCAUADVODFSLZ-UHFFFAOYSA-N 1-Chloro-1,1,2,2,2-pentafluoroethane Chemical compound FC(F)(F)C(F)(F)Cl RFCAUADVODFSLZ-UHFFFAOYSA-N 0.000 description 2
- BHNZEZWIUMJCGF-UHFFFAOYSA-N 1-chloro-1,1-difluoroethane Chemical compound CC(F)(F)Cl BHNZEZWIUMJCGF-UHFFFAOYSA-N 0.000 description 2
- JYNCTFQDWJMJDI-UHFFFAOYSA-N 2-chloro-1,1,1,3,3-pentafluoropropane Chemical compound FC(F)C(Cl)C(F)(F)F JYNCTFQDWJMJDI-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 description 2
- 239000001273 butane Substances 0.000 description 2
- 125000004773 chlorofluoromethyl group Chemical group [H]C(F)(Cl)* 0.000 description 2
- 235000019406 chloropentafluoroethane Nutrition 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 235000013611 frozen food Nutrition 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- UKACHOXRXFQJFN-UHFFFAOYSA-N heptafluoropropane Chemical compound FC(F)C(F)(F)C(F)(F)F UKACHOXRXFQJFN-UHFFFAOYSA-N 0.000 description 2
- 238000006317 isomerization reaction Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 235000015927 pasta Nutrition 0.000 description 2
- MSSNHSVIGIHOJA-UHFFFAOYSA-N pentafluoropropane Chemical compound FC(F)CC(F)(F)F MSSNHSVIGIHOJA-UHFFFAOYSA-N 0.000 description 2
- -1 polyol ester Chemical class 0.000 description 2
- 230000007928 solubilization Effects 0.000 description 2
- 238000005063 solubilization Methods 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- ZQTIKDIHRRLSRV-UHFFFAOYSA-N 1,1,1,2,2,3,3,4,4-nonafluorobutane Chemical compound FC(F)C(F)(F)C(F)(F)C(F)(F)F ZQTIKDIHRRLSRV-UHFFFAOYSA-N 0.000 description 1
- SUAMPXQALWYDBK-UHFFFAOYSA-N 1,1,1,2,2,3-hexafluoropropane Chemical compound FCC(F)(F)C(F)(F)F SUAMPXQALWYDBK-UHFFFAOYSA-N 0.000 description 1
- FDOPVENYMZRARC-UHFFFAOYSA-N 1,1,1,2,2-pentafluoropropane Chemical compound CC(F)(F)C(F)(F)F FDOPVENYMZRARC-UHFFFAOYSA-N 0.000 description 1
- FYIRUPZTYPILDH-UHFFFAOYSA-N 1,1,1,2,3,3-hexafluoropropane Chemical compound FC(F)C(F)C(F)(F)F FYIRUPZTYPILDH-UHFFFAOYSA-N 0.000 description 1
- ZDCWZRQSHBQRGN-UHFFFAOYSA-N 1,1,1,2,3-pentafluoropropane Chemical compound FCC(F)C(F)(F)F ZDCWZRQSHBQRGN-UHFFFAOYSA-N 0.000 description 1
- AWTOFSDLNREIFS-UHFFFAOYSA-N 1,1,2,2,3-pentafluoropropane Chemical compound FCC(F)(F)C(F)F AWTOFSDLNREIFS-UHFFFAOYSA-N 0.000 description 1
- MWDWMQNTNBHJEI-UHFFFAOYSA-N 1,1,2,3,3-pentafluoropropane Chemical compound FC(F)C(F)C(F)F MWDWMQNTNBHJEI-UHFFFAOYSA-N 0.000 description 1
- WGZYQOSEVSXDNI-UHFFFAOYSA-N 1,1,2-trifluoroethane Chemical compound FCC(F)F WGZYQOSEVSXDNI-UHFFFAOYSA-N 0.000 description 1
- JXMGZLBGSDLPKN-UHFFFAOYSA-N 1,1-dichloro-1,2,2,3,3-pentafluoropropane Chemical compound FC(F)C(F)(F)C(F)(Cl)Cl JXMGZLBGSDLPKN-UHFFFAOYSA-N 0.000 description 1
- YERASKROMPMIBM-UHFFFAOYSA-N 1,1-dichloro-1,2,3,3,3-pentafluoropropane Chemical compound FC(F)(F)C(F)C(F)(Cl)Cl YERASKROMPMIBM-UHFFFAOYSA-N 0.000 description 1
- GDSQRBLILFKERU-UHFFFAOYSA-N 1,2-dichloro-1,1,2,3,3-pentafluoropropane Chemical compound FC(F)C(F)(Cl)C(F)(F)Cl GDSQRBLILFKERU-UHFFFAOYSA-N 0.000 description 1
- YMRMDGSNYHCUCL-UHFFFAOYSA-N 1,2-dichloro-1,1,2-trifluoroethane Chemical compound FC(Cl)C(F)(F)Cl YMRMDGSNYHCUCL-UHFFFAOYSA-N 0.000 description 1
- XAHBEACGJQDUPF-UHFFFAOYSA-N 1,2-dichloro-1,1,3,3,3-pentafluoropropane Chemical compound FC(F)(F)C(Cl)C(F)(F)Cl XAHBEACGJQDUPF-UHFFFAOYSA-N 0.000 description 1
- UJIGKESMIPTWJH-UHFFFAOYSA-N 1,3-dichloro-1,1,2,2,3-pentafluoropropane Chemical compound FC(Cl)C(F)(F)C(F)(F)Cl UJIGKESMIPTWJH-UHFFFAOYSA-N 0.000 description 1
- IDGBOLGHJQQORA-UHFFFAOYSA-N 1,3-dichloro-1,1,2,3,3-pentafluoropropane Chemical compound FC(Cl)(F)C(F)C(F)(F)Cl IDGBOLGHJQQORA-UHFFFAOYSA-N 0.000 description 1
- UHMWWIKRVZTBBR-UHFFFAOYSA-N 1-chloro-1,1,2,2,3-pentafluoropropane Chemical compound FCC(F)(F)C(F)(F)Cl UHMWWIKRVZTBBR-UHFFFAOYSA-N 0.000 description 1
- JQZFYIGAYWLRCC-UHFFFAOYSA-N 1-chloro-1,1,2,2-tetrafluoroethane Chemical compound FC(F)C(F)(F)Cl JQZFYIGAYWLRCC-UHFFFAOYSA-N 0.000 description 1
- JODPGPKOJGDHSV-UHFFFAOYSA-N 1-chloro-1,1,2,3,3,3-hexafluoropropane Chemical compound FC(F)(F)C(F)C(F)(F)Cl JODPGPKOJGDHSV-UHFFFAOYSA-N 0.000 description 1
- PYVLQNDYKVUJKC-UHFFFAOYSA-N 1-chloro-1,1,2,3,3-pentafluoropropane Chemical compound FC(F)C(F)C(F)(F)Cl PYVLQNDYKVUJKC-UHFFFAOYSA-N 0.000 description 1
- FXSNEEBOGAOVIM-UHFFFAOYSA-N 1-chloro-1,2,2,3,3-pentafluoropropane Chemical compound FC(F)C(F)(F)C(F)Cl FXSNEEBOGAOVIM-UHFFFAOYSA-N 0.000 description 1
- JEWUXLHWYRSHJK-UHFFFAOYSA-N 2,2-dichloro-1,1,1,3,3-pentafluoropropane Chemical compound FC(F)C(Cl)(Cl)C(F)(F)F JEWUXLHWYRSHJK-UHFFFAOYSA-N 0.000 description 1
- YGFIGGVCQHKDOL-UHFFFAOYSA-N 2,3-dichloro-1,1,1,2,3-pentafluoropropane Chemical compound FC(Cl)C(F)(Cl)C(F)(F)F YGFIGGVCQHKDOL-UHFFFAOYSA-N 0.000 description 1
- CYXIKYKBLDZZNW-UHFFFAOYSA-N 2-Chloro-1,1,1-trifluoroethane Chemical compound FC(F)(F)CCl CYXIKYKBLDZZNW-UHFFFAOYSA-N 0.000 description 1
- SCDLWHGUKGDYQD-UHFFFAOYSA-N 2-chloro-1,1,1,2,3,3-hexafluoropropane Chemical compound FC(F)C(F)(Cl)C(F)(F)F SCDLWHGUKGDYQD-UHFFFAOYSA-N 0.000 description 1
- LDMYCECIGXPKDO-UHFFFAOYSA-N 2-chloro-1,1,1,2,3-pentafluoropropane Chemical compound FCC(F)(Cl)C(F)(F)F LDMYCECIGXPKDO-UHFFFAOYSA-N 0.000 description 1
- BKWAVXQSZLEURV-UHFFFAOYSA-N 2-chloro-1,1,1,3,3,3-hexafluoropropane Chemical compound FC(F)(F)C(Cl)C(F)(F)F BKWAVXQSZLEURV-UHFFFAOYSA-N 0.000 description 1
- WQFDUYPAWUTJPA-UHFFFAOYSA-N 2-chloro-1,1,2,3,3-pentafluoropropane Chemical compound FC(F)C(F)(Cl)C(F)F WQFDUYPAWUTJPA-UHFFFAOYSA-N 0.000 description 1
- COAUHYBSXMIJDK-UHFFFAOYSA-N 3,3-dichloro-1,1,1,2,2-pentafluoropropane Chemical compound FC(F)(F)C(F)(F)C(Cl)Cl COAUHYBSXMIJDK-UHFFFAOYSA-N 0.000 description 1
- PUFSJRPTJJPPJP-UHFFFAOYSA-N 3-chloro-1,1,1,2,2,3-hexafluoropropane Chemical compound FC(Cl)C(F)(F)C(F)(F)F PUFSJRPTJJPPJP-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- XWCDCDSDNJVCLO-UHFFFAOYSA-N Chlorofluoromethane Chemical compound FCCl XWCDCDSDNJVCLO-UHFFFAOYSA-N 0.000 description 1
- 239000004340 Chloropentafluoroethane Substances 0.000 description 1
- LVZWSLJZHVFIQJ-UHFFFAOYSA-N Cyclopropane Chemical compound C1CC1 LVZWSLJZHVFIQJ-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 1
- 101100484930 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) VPS41 gene Proteins 0.000 description 1
- 240000006394 Sorghum bicolor Species 0.000 description 1
- 235000011684 Sorghum saccharatum Nutrition 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 235000009430 Thespesia populnea Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 125000002877 alkyl aryl group Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 125000000753 cycloalkyl group Chemical group 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- UMNKXPULIDJLSU-UHFFFAOYSA-N dichlorofluoromethane Chemical compound FC(Cl)Cl UMNKXPULIDJLSU-UHFFFAOYSA-N 0.000 description 1
- 239000010696 ester oil Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- QYSGYZVSCZSLHT-UHFFFAOYSA-N octafluoropropane Chemical compound FC(F)(F)C(F)(F)C(F)(F)F QYSGYZVSCZSLHT-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 229960004065 perflutren Drugs 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 230000001737 promoting effect Effects 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
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000010189 synthetic method Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/02—Materials undergoing a change of physical state when used
- C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
- C09K5/041—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
- C09K5/044—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds
- C09K5/045—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds containing only fluorine as halogen
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/10—Components
- C09K2205/12—Hydrocarbons
- C09K2205/122—Halogenated hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/22—All components of a mixture being fluoro compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Thermal Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
Abstract
Refrigerant compositions containing hydrocarbon oil-return agents which solubilize mineral and synthetic oil lubricants with hydrofluorocarbon and hydrofluorocarbon/hydrochlorofluorocarbon-based refrigerants are disclosed. These hydrocarbon oil-return agents, having seven through sixteen carbon atoms, as a small proportion of an overall refrigerant composition, permit efficient return of mineral and synthetic oil lubricants from non-compressor zones back to a compressor zone in a refrigeration system operating with hydrofluorocarbon and hydrofluorocarbon/hydrochlorofluorocarbon-based refrigerants.
Description
Invention field
The present invention relates to the refrigerant composition of hydrocarbonaceous oil-reture agents (oil-return), this oil-reture agents can make mineral oil and synthetic oil lubricant and halogenate hydrocarbon refrigerant solubilization, thereby makes lubricant turn back to compressor section from the non-compressor section of refrigeration system effectively.
Background of invention
Mineral oil and alkylbenzene (CFC) are used as lubricant in the refrigeration system at cfc-Ji (chlorofluorocarbon-based) usually.But these lubricants are in non-ozone-depleting substitute, hydrogen-containing carbon fluorochemical (hydrofluorocarbon) (HFC) in the refrigeration agent solubleness very low, this has just hindered their use, needs exploitation and uses the alternative lubricant based on polyalkylene glycol (PAG) and polyol ester (POE) that is suitable for the HFC refrigeration system.Though PAG and POE are the lubricants that is applicable to the HFC-base refrigeration system, their water absorbability is extremely strong, can absorb the water of thousands of ppm (1,000,000/) when being exposed to wet air.The moisture that is absorbed can make refrigeration system go wrong, for example the acid that generates the corrosion refrigeration system and produce difficult sludge.In contrast, the water absorbability of mineral oil and alkylbenzene is little a lot, and very little to the solubleness of water, is lower than 100ppm.In addition, PAG and POE lubricant are expensive more a lot of than hydro carbons lubricant, general expensive 3~6 times.Therefore, be necessary also to have an opportunity to solve this solubility so that make refrigerating industry mineral oil and alkyl benzene lubricants can be used for HFC-base refrigeration agent.
Hydrogeneous cfc (hydrochlorofluorocarbon) (HCFC) refrigeration agent is also replacing CFC, and usually replaces CFC with the form of mixtures with HFC.For example the solubleness in the mineral oil is littler than CFC at common refrigeration lubricant for these HCFC-base refrigerant compositions.When replacing pure CFC base refrigeration agent with HCFC or HCFC/HFC mixture, usually need lubricant is become alkylbenzene by mineral oil, cause the more cost of refrigerating industry.Therefore, be necessary also to have an opportunity to solve the low problem of this solubleness, so that refrigerating industry can be used HCFC and HCFC/HFC-base refrigeration agent with mineral oil lubricant.
For these reasons, being necessary for refrigerating industry provides and can make lubricating oil (disperse phase) be dissolved in the oil-reture agents of HFC-and/or HCFC-base refrigeration agent (external phase), so as to improve lubricating oil in refrigeration system conveying and lubricating oil by other refrigeration system district returning to refrigeration system compressor.
Summary of the invention
Target of the present invention relates to satisfy the refrigerant composition of above-mentioned requirements.This refrigerant composition contains: the halohydrocarbon that (a) contains at least one carbon atom and a fluorine atom; (b) be selected from the oil of mineral oil and synthetic oil; (c) contain the hydrocarbon oil-reture agents of 10~16 carbon atoms.
The invention still further relates to a kind of refrigerant composition, wherein contain: the halohydrocarbon that (a) contains at least one carbon atom and a fluorine atom; (b) contain the hydrocarbon oil-reture agents of 10~16 carbon atoms.
The invention still further relates to a kind of lubricant compositions that in compression refrigeration equipment, uses, wherein contain: the oil that (a) is selected from mineral oil and synthetic oil with halogenate hydrocarbon refrigerant; (b) contain the hydrocarbon oil-reture agents of 10~16 carbon atoms.
In addition, the invention still further relates to a kind of method that makes oil return compressor section by the non-compressor section in the compression refrigerating system, comprise: (a) containing in the presence of the hydrocarbon oil-reture agents of 6~16 carbon atoms, the oil that is selected from mineral oil and synthetic oil is contacted with containing the halohydrocarbon of at least one carbon atom with a fluorine atom at non-compressor section, to form the solution of a kind of oil-containing, halohydrocarbon and hydrocarbon oil-reture agents; (b) this solution is transported to compressor section by the non-compressor section of refrigeration system.
Detailed Description Of The Invention
The present invention relates to refrigerant composition, wherein contain: the halohydrocarbon that (a) contains at least one carbon atom and a fluorine atom; (b) be selected from the oil of mineral oil and synthetic oil; (c) contain the hydrocarbon oil-reture agents of 10~16 carbon atoms, wherein said hydrocarbon oil-reture agents makes said halohydrocarbon and said oil form solution.
The invention still further relates to refrigerant composition, wherein contain: the halohydrocarbon that (a) contains at least one carbon atom and a fluorine atom; (b) contain the hydrocarbon oil-reture agents of 10~16 carbon atoms, the oil that wherein said hydrocarbon oil-reture agents makes said halohydrocarbon and is selected from mineral oil and synthetic oil forms solution.
The invention still further relates to the lubricant mixture that in compression refrigeration equipment, uses with halogenate hydrocarbon refrigerant, wherein contain: the oil that (a) is selected from mineral oil and synthetic oil; (b) contain the hydrocarbon oil-reture agents of 10~16 carbon atoms, wherein said oil-reture agents makes said oil and halogenate hydrocarbon refrigerant form solution.
In addition, the invention still further relates to a kind of method that in compression refrigerating system, makes oil return compressor section by non-compressor section, comprise: (a) containing in the presence of the hydrocarbon oil-reture agents of 6~16 carbon atoms, the oil that is selected from mineral oil and synthetic oil is contacted with containing the halohydrocarbon of at least one carbon atom with a fluorine atom at non-compressor section, to form the solution of oil-containing, halohydrocarbon and hydrocarbon oil-reture agents; (b) this solution is transported to compressor section by the non-compressor section of refrigeration system.
Halohydrocarbon of the present invention contains at least one carbon atom and a fluorine atom, particularly suitable be to contain 1-6 carbon atom and at least one fluorine atom, randomly also chloride and normal boiling point Sauerstoffatom are-90 ℃~80 ℃ halohydrocarbon.So-called normal boiling point is meant the temperature the when vapour pressure of liquid mixture equals 1 normal atmosphere.These halohydrocarbon can be used general formula C
wF
2w+2-x-yH
xCl
yO
zExpression, wherein w is 1~6, and x is 1~9, and y is 0~3, and z is 0~2.Preferred those w are 1~6, and x is 1~5, and y is 0~1, and z is 0~1 halohydrocarbon.These halohydrocarbon are commerical prods, can be by a lot of channels, and E.I.du Pont de Nemours ﹠amp for example; Co., Fluoroproducts, Wilmington, DE, 19898, the U.S. obtains, and perhaps by the PCR Inc. for example of Synesis Company customized, P.O.Box 1466, Gainesville, the Florida, 32602, the U.S. obtains, in addition, can also use for example " fluorine chemistry magazine " (The Journalof Fluorine Chemistry), perhaps " organofluorine compound chemistry " (Chemistryof Oganic Fluorine Compounds), Milos Hudicky compiles, The MacMillanCompany publishes, New York, N.Y., the disclosed synthetic method of technology is produced in 1962..The example of halohydrocarbon has:
CCl
2F
2(CFC-12),
CHCl
2F(HCFC-21),CHClF
2(HCFC-22),CHF
3(HFC-23),CH
2ClF(HCFC-31),
CH
2F
2(HFC-32),CH
3F(HFC-41),CF
3CF
3(FC-116),CHCl
2CF
3(HCFC-123),
CHClFCClF
2(HCFC-123a),CHClFCF
3(HCFC-124),CHF
2CClF
2(HCFC-124a),
CHF
2CF
3(HFC-125),CH
2ClCF
3(HCFC-133a),CHF
2CHF
2(HFC-134),
CH
2FCF
3(HFC-134a),CClF
2CH
3(HCFC-142b),CHF
2CH
2F(HFC-143),
CF
3CH
3(HFC-143a),CHClFCH
3(HCFC-151a),CHF
2CH
3(HFC-152a),
CHF
2CCl
2CF
3(HCFC-225aa),CHClFCClFCF
3(HCFC-225ba),CHF
2CClFCClF
2(HCFC-225bb),CHCl
2CF
2CF
3(HCFC-225ca),CHClFCF
2CClF
2(HCFC-225cb),
CHF
2CF
2CCl
2F(HCFC-225cc),CClF
2CHClCF
3(HCFC-225da),
CClF
2CHFCClF
2(HCFC-225ea),CF
3CHFCCl
2F(HCFC-225eb),CHF
2CClFCF
3(HCFC-226ba),CHClFCF
2CF
3(HCFC-226ca),CHF
2CF
2CClF
2(HCFC-226cb),
CF
3CHClCF
3(HCFC-226da),CClF
2CHFCF
3(HCFC-226ea),CHF
2CF
2CF
3(HFC-227ca),
CF
3CFHCF
3(HFC-227ea),CHF
2CClFCHF
2(HCFC-235ba),
CH
2FCClFCF
3(HCFC-235bb),CHClFCF
2CHF
2(HCFC-235ca),CH
2ClCF
2CF
2(HCFC-235cb),
CH
2FCF
2CClF
2(HCFC-235cc),CHF
2CHClCF
3(HCFC-235da),
CHClFCHFCF
3(HCFC-235ea),CHF
2CHFCClF
2(HCFC-235eb),CClF
2CH
2CF
3(HCFC-235fa),
CHF
2CF
2CHF
2(HFC-236ca),CH
2FCF
2CF
3(HFC-236cb),
CHF
2CHFCF
3(HFC-236ea),CF
3CH
2CF
3(HFC-236fa),CH
2FCF
2CHF
2(HFC-245ca)
CH
3CF
2CF
3(HFC-245cb),CHF
2CHFCHF
2(HFC-245ea),CH
2FCHFCF
3(HFC-245eb),
CHF
2CH
2CF
3(HFC-245fa),CH
2FCF
2CH
2F(HFC-254ca),
CH
2CF
2CHF
2(HFC-254cb),CH
2FCHFCHF
2(HFC-254ea),CH
3CHFCF
3(HFC-254eb),
CHF
2CH
2CHF
2(HFC-254fa),CH
2FCH
2CF
3(HFC-254fb),CH
3CF
2CH
3(HFC-272ca),
CH
3CHFCH
2F(HFC-272ea),CH
2FCH
2CH
2F(HFC-272fa),
CH
3CH
2CF
2H(HFC-272fb),CH
3CHFCH
3(HFC-281ea),CH
3CH
2CH
2F(HFC-281fa),
CF
3CF
2CF
2CF
2H(HFC-329p),CF
3CF
2CFHCF
3(HFC-329me),
CF
3CF
2CF
2CFH
2(HFC-338q),CF
3CF
2CH
2CF
3(HFC-338mf),CF
3CF
2CFHCF
2H(HFC-338pe),
CF
3CFHCF
2CF
2H(HFC-338pce),CHF
2CF
2CF
2CF
2H(HFC-338pcc),
CF
3CFHCFHCF
3(HFC-338mee),CF
3CF
2CF
2CF
2CF
2H(HFC-42-11p),
CF
3CF
2CFHCF
2CF
3(HFC-42-11mce),CF
3CF
2CF
2CFHCF
3(HFC-42-11me),
CF
3CF
2CH
2CF
2CF
3(HFC-43-10mcf),CF
3CF
2CF
2CH
2CF
3(HFC-43-10mf),
CF
3CF
2CF
2CF
2CFH
2(HFC-43-10q),CF
3CF
2CF
2CFHCF
2H(HFC-43-10pe),
CF
3CF
2CFHCF
2CF
2H(HFC-43-10pce),CF
3CHFCHFCF
2CF
3(HFC-43-10mee),
CF
2HCF
2CF
2CF
2CF
2H(HFC-43-10pccc),CF
3CFHCF
2CF
2CF
2H(HFC-43-10pcce),
CF
3CFHCF
2CFHCF
3(HFC-43-10mece),CF
3CF
2CF
2CF
2CF
2CF
2H(HFC-52-13p),
C
4F
9OCH
3, and C4F
9OC
2H
5, preferred halogenated hydrocarbons is:
CHClF
2(HCFC-22),CHF
3(HFC-23),CH
2F
2(HFC-32),CHClFCF
3(HCFC-124),CHF
2CF
3(HFC-125),CHF
2CHF
2(HFC-134),CH
2FCF
3(HFC-134a),CF
3CH
3(HFC-143a),CHF
2CH
3(HFC-152a),CHF
2CF
2CF
3(HFC-227ca),CF
3CFHCF
3(HFC-227ea),CF
3CH
2CF
3(HFC-236fa),CHF
2CH
2CF
3(HFC-245fa),CHF
2CF
2CF
2CF
2H(HFC-338pcc),CF
3CHFCHFCF
2CF
3(HFC-43-10mee),
With azeotropic and class azeotropic Halocarbon blends for example:
HCFC-22/HFC-152a/HCFC-124 (R-401A, R-401B, R-401C), HFC-125/HFC-143a/HFC-134a (R-404A), HFC-32/HFC-125/HFC-134a (R-407A, R-407B, R-407C), HCFC-22/HFC-143a/HFC-125 (R-408A), HCFC-22/HCFC-124/HCFC-142b (R-409A), HFC-32/HFC-125 (R-410A), and HFC-125/HFC-143a (R-507).
Halohydrocarbon of the present invention also can contain at least a C of as many as 10 weight %
3-C
5Hydrocarbon, for example propane, propylene, cyclopropane, normal butane, Trimethylmethane and Skellysolve A.Contain these C
3-C
5The example of the halohydrocarbon of hydrocarbon is that (R-402A is R-402B) with HCFC-22/ octafluoropropane/propane (R-403A, class constant boiling mixture R-403B) for HCFC-22/HFC-125/ propane.
Oil of the present invention is to be used as the oil that lubricant and CFC-base refrigeration agent uses together usually in refrigeration equipment.These oil and character thereof are in 1990 " ASHRAE handbook (ASHRAEHandbook), refrigeration system and application the 8th chapter, title " lubricant in the refrigeration system " (" Lubricants in Refrigeration Systems ") is discussed in the 8.1-8.21 page or leaf.Oil of the present invention is included in the class oil that this area is called as mineral oil.Mineral oil comprises paraffinic hydrocarbons (straight chain and branched-chain saturated hydrocarbon), naphthenic hydrocarbon (ring chain hydrocarbon), aromatic hydrocarbons (the unsaturated cyclic hydrocarbon that contains one or more rings is characterized in that having the two keys of alternative), with non-hydrocarbons compound (outside de-carbon and the hydrogen, going back the equiatomic molecule of sulfur-bearing, nitrogen or oxygen).Oil of the present invention also is included in the class oil that this area is called as synthetic oil.Synthetic oil comprises alkylaromatic hydrocarbon (alkylaryls) (for example straight chain and branched alkylbenzene), synthetic paraffinic hydrocarbons and poly-alpha olefins.The example of commercially available lubricating oil of the present invention has Suniso 3GS, Sontex 372LT and Calumet RO-30 (above three kinds are naphthenic hydrocarbon), Zerol 150 (a kind of alkylbenzene) and " BVM 100 N " (a kind of paraffinic hydrocarbons).
The effective level of hydrocarbon oil-reture agents of the present invention in the present composition should be able to make halohydrocarbon and lubricating oil form a kind of solution.So-called " solution " is to say in the presence of the hydrocarbon oil-reture agents, it is easier to be miscible that halohydrocarbon and oil become, so that make oil as and the form of the homogeneous solution of halohydrocarbon get back to compressor section by the non-compressor section of refrigeration system, the amount of oil can be kept the operation of the normally lubricated and whole refrigeration system of compressor.The present invention contain at least one carbon atom and a fluorine atom the mixture of halohydrocarbon, the oil that is selected from mineral oil and synthetic oil and hydrocarbon oil-reture agents in, the preferred hydrocarbons oil-reture agents is less than total composition about 10 weight % of (comprising halohydrocarbon, oil and hydrocarbon oil-reture agents).More preferably the hydrocarbon oil-reture agents is less than total composition about 5 weight % of (comprising halohydrocarbon, oil and hydrocarbon oil-reture agents).About 10 weight % that the general concentration that does not need to make the hydrocarbon oil-reture agents surpasses total composition just can obtain enough oil and reflux, and find, the oil-reture agents that concentration surpasses about 10 weight % of total composition has disadvantageous effect to oil body, this can cause lubricated undesired, refrigeration equipment is produced pressure, even make refrigeration equipment produce mechanical fault.Find that also the oil-reture agents that concentration surpasses about 10 weight % of total composition has disadvantageous effect to the ability (capacity) and the performance of refrigerant composition.The effective content of hydrocarbon oil-reture agents can make halohydrocarbon and oil reach suitable miscible degree in the mixture of the present invention, to such an extent as to the oil in the compression refrigerating system can fully be got back to compressor section by non-compressor section (for example vaporizer).
The hydrocarbon oil-reture agents of the present composition comprises aliphatics straight chain, side chain or the ring chain hydrocarbon that contains at least 7 to 16 or be less than 16 carbon atoms.For example, heptane, octane, nonane, decane, undecane, kerosene and their mixture, particularly sulphur content are lower than the kerosene raffinate of 0.2 weight %.In the hydrocarbon oil-reture agents, preferably those are classified as flammable (combustible) ((flammable) is different with inflammableness) by ASTMD-93.So the flammable hydrocarbon of classification is preferably used as the hydrocarbon oil-reture agents, because how many consumptions can not make refrigerant compositions produce inflammableness.Preferred hydrocarbon oil-reture agents contains 7~16 carbon atoms.Preferred hydrocarbon oil-reture agents contains 11~13 carbon atoms.Most preferred commercially available energy is that Isopar H.Isopar H is a kind of high purity that U.S. Exxon Chemical sells as the compound of hydrocarbon oil-reture agents, the C of low arene content
11~C
12Isomerization alkanes.
Flash-point is lower than 37 ℃ compound and is generally considered to be flammable.Though the flash-point in the following table may be to measure with the method for difference slightly, still have flash-point with the increase of carbon chain lengths trend of rising.Chain length can begin to become flammable less than 10 carbon atoms.Compare with the technology of disclosed use propane, butane, Trimethylmethane and pentane as promoting oil to reflux, a kind of non-flammable hydrocarbons oil-reture agents or carrier can reduce the inflammableness in refrigeration or the air-conditioning system.And can use the inflammableness that is unlikely to the system that influences than inflammableness hydrocarbon amount more non-flammable hydrocarbon oil-reture agents.
Hydrocarbon | Molecular formula | Flash-point (℃) | Boiling point (℃) | Inflammableness |
Propane | CH 3CH 2CH 3 | -104 | -42 | Inflammable |
Trimethylmethane | (CH 3) 3CH | -84 | -12 | Inflammable |
Butane | CH 3(CH 2) 2CH 3 | -60 | -1 | Inflammable |
Pentane | CH 3(CH 2) 3CH 3 | -40 | 36~38 | Inflammable |
Hexane | CH 3(CH 2) 4CH 3 | -22~-26 | 65~69 | Inflammable |
Heptane | CH 3(CH 2) 5CH 3 | -8 | 92~100 | Inflammable |
Octane | CH 3(CH 2) 6CH 3 | 16 | 125~127 | Inflammable |
Nonane | CH 3(CH 2) 7CH 3 | 31 | 151 | Inflammable |
Decane | CH 3(CH 2) 8CH 3 | 46 | 174 | Flammable |
Kerosene | The HC mixture | 43~82 | 151~301 | Flammable |
IsoparH | C 11~C 12Isomerization alkanes | 57 | 182 | Flammable |
Undecane | CH 3(CH 2) 9CH 3 | 60 | 196 | Flammable |
Dodecane | CH 3(CH 2) 10CH 3 | 71 | 215~217 | Flammable |
Tridecane | CH 3(CH 2) 11CH 3 | 79 | 234 | Flammable |
The tetradecane | CH 3(CH 2) 12CH 3 | 100 | 252 | Flammable |
Pentadecane | CH 3(CH 2) 13CH 3 | 132 | 270 | Flammable |
N-Hexadecane | CH 3(CH 2) 14CH 3 | 135 | 287 | Flammable |
Mineral oil | Paraffin oils | 199 | 260~360 | Flammable |
Gross weight with mixture is a benchmark, and the refrigerant composition that the present invention contains halohydrocarbon, oil and hydrocarbon oil-reture agents contains the halohydrocarbon of 40~99 weight %, the oil of 1~60 weight % and the hydrocarbon oil-reture agents of 0.01~10 weight % usually.Said composition more preferably contains the halohydrocarbon of 50~90 weight %, the hydrocarbon oil-reture agents of the oil of 10~50 weight % and 0.01~5 weight %.
The present invention comprises: halohydrocarbon and hydrocarbon oil-reture agents; And the weight ratio between each composition and the present invention contain identical in the composition of halohydrocarbon, oil and hydrocarbon oil-reture agents in the other composition of oil and hydrocarbon oil-reture agents.That is to say that in composition of the present invention, the weight ratio of halohydrocarbon and oil is about 0.6 (40/60) to about 99 (99/1), oil is about 0.1 (1/10) to about 6000 (60/.01) with the weight ratio of hydrocarbon oil-reture agents.
The present invention also comprises refrigerating method, and promptly near evaporation refrigerant compositions of the present invention needs refrigerative object also comprises heating means, i.e. near the condensation refrigerant compositions of the present invention object of needs heating.
The invention still further relates to the method for halohydrocarbon being carried out solubilization in oil, being included in a kind of hydrocarbon oil-reture agents that can make this halohydrocarbon and this oil form the effective level of solution exists down, allow halohydrocarbon contact with oil, wherein said halohydrocarbon contains at least one carbon atom and a fluorine atom, and said grease separation is from mineral oil and synthetic oil.
The invention still further relates to and make oil return the method for compressor section, comprising by the non-compressor section of refrigeration system:
(a) in the presence of a kind of hydrocarbon oil-reture agents of effective level, allow said oil non-compressor section contact with at least a halohydrocarbon and
(b) said oil is delivered to compressor section from the non-compressor section of refrigeration system, wherein said halohydrocarbon contains at least one carbon atom and a fluorine atom, and said grease separation is from mineral oil and synthetic oil.
The invention still further relates to a kind of oil is delivered to the method for compressor section from the low pressure area of refrigeration system, comprising:
(a) in the presence of a kind of hydrocarbon oil-reture agents of effective level, allow said oil the refrigeration system low pressure area contact with at least a halohydrocarbon and
(b) said oil is delivered to compressor section from the low pressure area of refrigeration system, wherein said halohydrocarbon contains at least one carbon atom and a fluorine atom, and said grease separation is from mineral oil and synthetic oil.
Embodiment
In following examples, as not indicating, then percentage ratio (%) is represented the weight percentage of a certain material in said total composition.The oil backflow measuring error of being given is ± 0.5 weight %.
Embodiment 1
Measuring oil in oily refluxing unit as described below refluxes.Liquid refrigerant is delivered to a well heater by a pressure-pot through copper pipe to be evaporated.Allow refrigerant vapour by a pressure-regulator and metering valve flow and pressure are controlled at fixed value 1,000~1 respectively, 100cc/min and 1 normal atmosphere then.Refrigerant vapour is sent to the long 180cm of another root, the U-shaped copper pipe of inserting a thermostatic bath of external diameter 0.635cm.This U-shaped copper pipe starts from the long vertical straight tube of one section 37cm, bends to the long horizontal section that is positioned at the thermostatic bath bottom of 27cm then.This pipe is then with the zigzag vertical uplift, and this section zigzag has 4 23cm length, then is the long vertical straight tube of another section 23cm.The 10g oil of packing in this U-shaped pipe, hydrocarbonaceous oil-reture agents randomly, this oil-reture agents adds the U-shaped pipe by the vertical pipe end of 37cm.Allow refrigerant vapour slowly by the U-shaped pipe.Refrigeration agent that will come out from the U-shaped pipe and oil are collected in the susceptor and allow the refrigeration agent evaporation.Weighing oil is heavy then takes the U-shaped pipe out of for cooled dose to define how many oil.
Refrigeration agent R404A (44 weight %HFC-125,52 weight %HFC-143a and 4 weight %HFC-134a) is put into refrigerant tank.HAB 22 oil (HAB-22 is a kind of branched alkylbenzene oil that NipponOil sells) or HAB are added that hydrocarbon oil-reture agents Isopar H puts into copper U-shaped pipe, and wherein oil and oil-reture agents total amount are 10g.Thermostatic bath remains on-20 ℃.Refrigerant vapour is with 1,100cm
3The flow velocity of/min is by the U-shaped pipe and with 6,10, the weight of oil in 20 and 30 minutes the time interval measurement receptor.With POE 22 polyvalent alcohol ester oils is that benchmark and HAB 22 contrast.Data are shown in following table 1.
Table 1
The weight % of withdrawing oil | |||
Oil component in the U-shaped pipe | 6min | 10min | 20min |
POE | 1.0 | 10.6 | 18.9 |
HAB 22 | 0 | 6.1 | 16.2 |
Contain 3%Isopar H among the HAB 22 | 0 | 9.6 | 19.2 |
The result shows that when Isopar H was added hard alkylbenzene oil (HAB 22), oil refluxed suitable with POE.
Embodiment 2
Equipment and program test refrigeration agent R401A (53 weight %HCFC-22,13 weight %HFC-152a and 34 weight %HFC-124) with embodiment 1.To contain and not contain Suniso 3GS mineral oil and the contrast of benchmark Zerol 150 alkylbenzenes of Isopar H.The results are shown in table 2.
Table 2
The weight % of withdrawing oil | |||
Oil component in the U-shaped pipe | 6min | 10min | 20min |
3GS | 0 | 1.2 | 19.7 |
Zerol150 | 0 | 9.6 | 31.2 |
Contain 3%Isopar H among the 3GS | 0.4 | 14.0 | 30.6 |
The result shows, Isopar H is joined 3GS mineral oil can obtain the oil backflow suitable with Zerol 150 alkylbenzenes.
Embodiment 3
Except following said difference, with equipment and the program test refrigeration agent R407C (23 weight %HFC-32,25 weight %HFC-125 and 52 weight %HFC-134a) of embodiment 1.To contain and not Suniso 3GS mineral oil and the POE contrast of hydrocarbonaceous oil-reture agents Isopar H.Thermostatic bath remains on-20 ℃.The results are shown in table 3.
Table 3
The weight % of withdrawing oil | |||
Oil component in the U-shaped pipe | 6min | 10min | 20min |
POE | 3.1 | 14.1 | 26.5 |
3GS | 0 | 0 | 0 |
Contain 3%Isopar H among the 3GS | 0 | 0 | 0.3 |
Contain 6%Isopar H among the 3GS | 0 | 0 | 6.7 |
Contain 15%Isopar H among the 3GS | 10.0 | 18.7 | 27.3 |
The result shows, Isopar H is joined improved oily backflow in the 3GS oil, and the 3GS that adds 15%Isopar H has the oil backflow performance suitable with POE.
Embodiment 4
Except following said difference, with equipment and the program test R404A (44 weight %HFC-125,52 weight %HFC-143a and 4 weight %HFC-134a) of embodiment 1.To contain and not Suniso 3GS mineral oil and the POE contrast of hydrocarbonaceous oil-reture agents Isopar H.Thermostatic bath remains on-20 ℃.The results are shown in table 4.
Table 4
The weight % of withdrawing oil | |||
Oil component in the U-shaped pipe | 6min | 10min | 20min |
POE | 0 | 6.2 | 18.9 |
Contain 12%Isopar H among the 3GS | 4.2 | 13.3 | 23.3 |
Contain 15%Isopar H among the 3GS | 9.6 | 16.3 | 25.0 |
Contain 18%Isopar H among the 3GS | 17.1 | 24.3 | 33.8 |
The result shows, Isopar H is joined improved oily backflow in the 3GS oil, add 12,15 and the oil backflow performance of the 3GS of 18%Isopar H than POE lubricant improvement is arranged.
Embodiment 5
Following table 5 is listed in the Isopar H in 3GS mineral oil that represents with centistoke and the kinematic viscosity under-15 ℃ of pentane and the contrast of POE 22 oil phases.The used test method is ASTM method D446.
Table 5
Kinematic viscosity under-15 ℃, centistoke | |
POE | 589.5 |
3GS | 2936.7 |
3GS+6%IsoparH | 1277.3 |
3GS+12%IsoparH | 611.4 |
The 3GS+3% pentane | 971.6 |
Data show that under-15 ℃, viscosity and the POE of the 12%Isopar H in 3GS mineral oil are approaching.It is less that the pentane of adding 3% makes the viscosity reduction among the 3GS.When using pentane, inflammableness increases, and Isopar H is nonflammable.
Embodiment 6
When determining to use plain oil Suniso 3GS with test, whether R404A (44 weight %HFC-125,52 weight %HFC-143a and 4 weight %HFC-134a) can be used for the frozen food display case (HICA-0146-PLK type) in Hussmann supermarket.Showcase is equipped with a Copeland semitight reciprocation compressor (KAL-016L type), in its oil groove visor is housed.The frozen product cabinet is installed in the room in the environmental chamber, and condensing unit is installed in the outer room of environmental chamber.Two unit connect with copper pipe, and the suction tube external diameter is 5/8 inch, and the liquid line external diameter is 1/2 inch.The sample pot of a 300cc is installed between two valves on the liquid line.Oil circulation for measuring, in the system operation process with valve closes so that catch refrigeration agent/oil samples.Sample pot is taken off and weigh, refrigeration agent is slowly evaporated, and then the weighing sample pot is to determine the amount of refrigeration agent.Calculate the per-cent or the turning oil per-cent of oil in the refrigeration agent with the weight of surplus oil.The refrigeration agent R502 (48.8 weight %HCFC-22,51.2 weight %CFC-115 (chloropentafluoroethane)) that contains 3GS oil is as benchmark.Ability (capacity) is meant the enthalpy change of every pound of circulating refrigerant in the vaporizer, i.e. the heat at every turn removed of refrigeration agent in the vaporizer.Coefficient of refrigerating performance (COP) is meant the ratio of ability and the merit of compressor.It is measuring of refrigeration agent energy efficiency.The results are shown in table 6.
Table 6
Refrigeration agent/oil combination | Oil circulation (wt%) | Ability (Kbtu/H) | COP |
R502/3GS | 0.16 | 3.26 | 1.67 |
R404A/3GS* | 0.12 | 3.31 | 1.70 |
R404A/ contains 6%Isopar H** in 3GS | 0.15 | 3.26 | 1.65 |
* pasta drops to below the viewpoint in the visor
* is based on refrigeration agent and oily 0.3%Isopar H
Data show that the Isopar H that adds 6 weight % can obtain and the similar COP of benchmark R502/3GS system, refrigeration capacity and oil circulation.If there is not Isopar H, pasta decline explanation oil refluxes not enough in visor.
Embodiment 7
The concentration distribution of frozen food display case research Isopar H when system is operated with the Hussmann supermarket of embodiment 6.The 3GS mineral oil that will contain 15%Isopar H is added in the oil groove and adds R407C in system.Operate after 48 hours, analyze in the oil groove behind the oil and condenser in the fluid pipeline oily with the percentage concentration that obtains Isopar H and calculate material balance, shown in following table 7.
Table 7
The position | Time (hour) | The weight % of Isopar H |
Oil groove | 0 | 15.0 |
Oil groove | 48 | 2.3 |
Liquid line | 48 | 3.2 |
Vaporizer | 48 | 9.5 |
Data show that Isopar H has enough volatility to be taken out of oil groove and to be deposited in the vaporizer.The existence of Isopar H has reduced oil viscosity in the vaporizer, thereby the oil in the vaporizer is got back in the compressor.Isopar H concentration is reduced to 2.3% by 15% in the oil groove, can make that oil viscosity keeps enough highly to reduce the influence to compressor lubrication to greatest extent in the oil groove.
Claims (9)
1. the application of lubricant compositions in containing the compression refrigeration equipment of halogenate hydrocarbon refrigerant, described lubricant compositions contains:
(a) aromatic hydrocarbons refrigeration oil; With
(b) be selected from least a hydrocarbon oil-reture agents of decane, undecane, dodecane, tridecane, the tetradecane, pentadecane and n-Hexadecane.
2. refrigerant composition, it contains:
(a) be selected from least a halohydrocarbon of hydrogen-containing carbon fluorochemical and hydrogen-containing carbon fluorochloride;
(b) be selected from least a oil of paraffinic hydrocarbons, naphthenic hydrocarbon, aromatic hydrocarbons and poly-alpha olefins; With
(c) be selected from least a hydrocarbon oil-reture agents of decane, undecane, dodecane, tridecane, the tetradecane, pentadecane and n-Hexadecane.
3. one kind makes oil turn back to the method for compressor section from the non-compressor section of compression refrigerating system, comprising:
(a) be selected from the presence of the hydrocarbon oil-reture agents of decane, undecane, dodecane, tridecane, the tetradecane, pentadecane and n-Hexadecane, the oil that is selected from paraffinic hydrocarbons, naphthenic hydrocarbon, aromatic hydrocarbons and poly-alpha olefins is contacted with being selected from the halohydrocarbon of hydrogen-containing carbon fluorochemical with the hydrogen-containing carbon fluorochloride at non-compressor section, to form the solution of a kind of oil-containing, halohydrocarbon and hydrocarbon oil-reture agents; With
(b) solution is transported to compressor section by the non-compressor section of refrigeration system.
4. the application of claim 1, wherein said hydrocarbon oil-reture agents is selected from undecane, dodecane and tridecane.
5. the composition of claim 2, wherein said hydrocarbon oil-reture agents is selected from undecane, dodecane and tridecane.
6. the method for claim 3, wherein said hydrocarbon oil-reture agents is selected from undecane, dodecane and tridecane.
7. the method for the compressor in the lubricated compression refrigerating system that contains halogenate hydrocarbon refrigerant, it comprises the step that adds the composition that comprises following component in described compressor:
(a) be selected from least a oil of paraffinic hydrocarbons, naphthenic hydrocarbon, aromatic hydrocarbons and poly-alpha olefins; With
(b) be selected from least a hydrocarbon oil-reture agents of decane, undecane, dodecane, tridecane, the tetradecane, pentadecane and n-Hexadecane.
8. one kind makes oily non-compressor section from the compression refrigerating system that contains halogenate hydrocarbon refrigerant be transported to the method for compressor section, comprises the step that adds the composition that comprises following component:
(a) be selected from least a oil of paraffinic hydrocarbons, naphthenic hydrocarbon, aromatic hydrocarbons and poly-alpha olefins; With
(b) be selected from least a hydrocarbon oil-reture agents of decane, undecane, dodecane, tridecane, the tetradecane, pentadecane and n-Hexadecane.
9. a refrigerating method is included near the composition that evaporates claim 2 of object to be cooled, then the described composition of condensation.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/231,847 US6299792B1 (en) | 1998-01-16 | 1999-01-15 | Halogenated hydrocarbon refrigerant compositions containing polymeric oil-return agents |
US09/231847 | 1999-01-15 | ||
US35171099A | 1999-07-12 | 1999-07-12 | |
US09/351710 | 1999-07-12 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1333806A CN1333806A (en) | 2002-01-30 |
CN1210368C true CN1210368C (en) | 2005-07-13 |
Family
ID=26925485
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 99815670 Expired - Fee Related CN1210368C (en) | 1999-01-15 | 1999-07-14 | Halogenated hydrocarbon refrigerant compositions containing hydrocarbon oil-reture agents |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP1151054A1 (en) |
JP (1) | JP2002534578A (en) |
CN (1) | CN1210368C (en) |
AU (1) | AU772143B2 (en) |
BR (1) | BR9917321A (en) |
CA (1) | CA2359090A1 (en) |
WO (1) | WO2000042118A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB0105065D0 (en) * | 2001-03-01 | 2001-04-18 | Ici Plc | Lubricant compositions |
US6759374B2 (en) | 2001-09-19 | 2004-07-06 | 3M Innovative Properties Company | Composition comprising lubricious additive for cutting or abrasive working and a method therefor |
US8999191B2 (en) | 2013-03-15 | 2015-04-07 | National Refrigerants, Inc. | R22 replacement refrigerant |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5072067A (en) * | 1988-11-15 | 1991-12-10 | Idemitsu Kosan Company Limited | Lubricating oil composition |
CA2021916A1 (en) * | 1989-09-07 | 1991-03-08 | Harry N. Cripps | Compositions and process of using in refrigeration |
WO1993015168A1 (en) * | 1992-01-23 | 1993-08-05 | Pieter Jan Dirk Muntz | Lubricating oil composition |
EP1028152A3 (en) * | 1993-02-05 | 2005-06-15 | E.I. Du Pont De Nemours And Company | Compositions of a hydrofluorocarbon and a hydrocarbon |
US5611210A (en) * | 1993-03-05 | 1997-03-18 | Ikon Corporation | Fluoroiodocarbon blends as CFC and halon replacements |
CN1184501A (en) * | 1995-05-16 | 1998-06-10 | 美国3M公司 | Azeotrope-like compositions and their use |
-
1999
- 1999-07-14 BR BR9917321-2A patent/BR9917321A/en not_active IP Right Cessation
- 1999-07-14 AU AU49942/99A patent/AU772143B2/en not_active Expired - Fee Related
- 1999-07-14 EP EP99934019A patent/EP1151054A1/en not_active Withdrawn
- 1999-07-14 CA CA002359090A patent/CA2359090A1/en not_active Abandoned
- 1999-07-14 WO PCT/US1999/015935 patent/WO2000042118A1/en not_active Application Discontinuation
- 1999-07-14 JP JP2000593677A patent/JP2002534578A/en active Pending
- 1999-07-14 CN CN 99815670 patent/CN1210368C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP1151054A1 (en) | 2001-11-07 |
JP2002534578A (en) | 2002-10-15 |
CA2359090A1 (en) | 2000-07-20 |
WO2000042118A1 (en) | 2000-07-20 |
AU4994299A (en) | 2000-08-01 |
BR9917321A (en) | 2002-04-23 |
CN1333806A (en) | 2002-01-30 |
AU772143B2 (en) | 2004-04-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8765006B2 (en) | Refrigerant compositions having a siloxane solubilizing agent | |
US9303900B2 (en) | Halogenated alkene heat transfer compositions with improved oil return | |
US20210253925A1 (en) | Hydrofluorocarbon/trifluoroiodomethane/hydrocarbons refrigerant compositions | |
EP3263671B1 (en) | Compositions comprising carbon dioxide and a fluoroolefin | |
EP1047747B1 (en) | Halogenated hydrocarbon refrigerant compositions containing polymeric oil-return agents | |
WO2004031318A1 (en) | Refrigerant blend | |
CN1210368C (en) | Halogenated hydrocarbon refrigerant compositions containing hydrocarbon oil-reture agents | |
AU2022370363A1 (en) | Compositions comprising 2,3,3,3-tetrafluoropropene | |
MXPA01007102A (en) | Halogenated hydrocarbon refrigerant compositions containing hydrocarbon oil-return agents | |
KR20010101544A (en) | Halogenated Hydrocarbon Refrigerant Compositions Containing Hydrocarbon Oil-Return Agents | |
ZA200104870B (en) | Halogenated hydrocarbon refrigerant compositions containing hydrocarbon oil-return agents. | |
AU2022368749A1 (en) | Stabilized compositions comprising 2,3,3,3-tetrafluoropropene | |
MXPA00006543A (en) | Halogenated hydrocarbon refrigerant compositions containing polymeric oil-return agents |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
C10 | Entry into substantive examination | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |