US20120192856A1 - Ionic liquid solar ponds - Google Patents
Ionic liquid solar ponds Download PDFInfo
- Publication number
- US20120192856A1 US20120192856A1 US13/145,687 US201113145687A US2012192856A1 US 20120192856 A1 US20120192856 A1 US 20120192856A1 US 201113145687 A US201113145687 A US 201113145687A US 2012192856 A1 US2012192856 A1 US 2012192856A1
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- US
- United States
- Prior art keywords
- methyl
- imidazolium
- hexyl
- bis
- octyl
- 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.)
- Abandoned
Links
- 239000002608 ionic liquid Substances 0.000 title claims abstract description 72
- -1 phosphonium ion Chemical class 0.000 claims description 61
- 235000002639 sodium chloride Nutrition 0.000 claims description 16
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 12
- 230000005855 radiation Effects 0.000 claims description 12
- NJMWOUFKYKNWDW-UHFFFAOYSA-N 1-ethyl-3-methylimidazolium Chemical compound CCN1C=C[N+](C)=C1 NJMWOUFKYKNWDW-UHFFFAOYSA-N 0.000 claims description 11
- QWJNFFYFEKXZBF-UHFFFAOYSA-N cyanocyanamide Chemical compound N#CNC#N QWJNFFYFEKXZBF-UHFFFAOYSA-N 0.000 claims description 9
- 239000012266 salt solution Substances 0.000 claims description 9
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 8
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 claims description 8
- RAXXELZNTBOGNW-UHFFFAOYSA-O Imidazolium Chemical compound C1=C[NH+]=CN1 RAXXELZNTBOGNW-UHFFFAOYSA-O 0.000 claims description 7
- YGSDEFSMJLZEOE-UHFFFAOYSA-M salicylate Chemical compound OC1=CC=CC=C1C([O-])=O YGSDEFSMJLZEOE-UHFFFAOYSA-M 0.000 claims description 7
- 229960001860 salicylate Drugs 0.000 claims description 7
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 5
- 239000011780 sodium chloride Substances 0.000 claims description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 4
- 150000002500 ions Chemical class 0.000 claims description 4
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 4
- JUJWROOIHBZHMG-UHFFFAOYSA-O pyridinium Chemical compound C1=CC=[NH+]C=C1 JUJWROOIHBZHMG-UHFFFAOYSA-O 0.000 claims description 4
- 235000010344 sodium nitrate Nutrition 0.000 claims description 4
- 239000004317 sodium nitrate Substances 0.000 claims description 4
- DTIFFPXSSXFQCJ-UHFFFAOYSA-N tetrahexylazanium Chemical compound CCCCCC[N+](CCCCCC)(CCCCCC)CCCCCC DTIFFPXSSXFQCJ-UHFFFAOYSA-N 0.000 claims description 4
- HVVRUQBMAZRKPJ-UHFFFAOYSA-N 1,3-dimethylimidazolium Chemical compound CN1C=C[N+](C)=C1 HVVRUQBMAZRKPJ-UHFFFAOYSA-N 0.000 claims description 3
- FHDQNOXQSTVAIC-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;chloride Chemical compound [Cl-].CCCCN1C=C[N+](C)=C1 FHDQNOXQSTVAIC-UHFFFAOYSA-M 0.000 claims description 3
- KIDIBVPFLKLKAH-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;octyl sulfate Chemical compound CCCCN1C=C[N+](C)=C1.CCCCCCCCOS([O-])(=O)=O KIDIBVPFLKLKAH-UHFFFAOYSA-M 0.000 claims description 3
- IQQRAVYLUAZUGX-UHFFFAOYSA-N 1-butyl-3-methylimidazolium Chemical compound CCCCN1C=C[N+](C)=C1 IQQRAVYLUAZUGX-UHFFFAOYSA-N 0.000 claims description 3
- FQWUDBZGMGXIAR-UHFFFAOYSA-N 1-dodecylimidazole;2-hydroxybenzoic acid Chemical compound OC(=O)C1=CC=CC=C1[O-].CCCCCCCCCCCC[NH+]1C=CN=C1 FQWUDBZGMGXIAR-UHFFFAOYSA-N 0.000 claims description 3
- CAVPTISELCJZGX-UHFFFAOYSA-N 1-ethyl-3-methylimidazol-3-ium;methanetricarbonitrile Chemical compound N#CC(C#N)C#N.CCN1C=C[N+](C)=C1 CAVPTISELCJZGX-UHFFFAOYSA-N 0.000 claims description 3
- RVEJOWGVUQQIIZ-UHFFFAOYSA-N 1-hexyl-3-methylimidazolium Chemical compound CCCCCCN1C=C[N+](C)=C1 RVEJOWGVUQQIIZ-UHFFFAOYSA-N 0.000 claims description 3
- NKRASMXHSQKLHA-UHFFFAOYSA-M 1-hexyl-3-methylimidazolium chloride Chemical compound [Cl-].CCCCCCN1C=C[N+](C)=C1 NKRASMXHSQKLHA-UHFFFAOYSA-M 0.000 claims description 3
- WGHMGICKLQSEIA-UHFFFAOYSA-M 1-methyl-3-octylimidazol-1-ium;trifluoroborane;fluoride Chemical compound [F-].FB(F)F.CCCCCCCCN1C=C[N+](C)=C1 WGHMGICKLQSEIA-UHFFFAOYSA-M 0.000 claims description 3
- LSFWFJFDPRFPBK-UHFFFAOYSA-N 1-methyl-3-pentylimidazol-1-ium Chemical compound CCCCCN1C=C[N+](C)=C1 LSFWFJFDPRFPBK-UHFFFAOYSA-N 0.000 claims description 3
- WVDDUSFOSWWJJH-UHFFFAOYSA-N 1-methyl-3-propylimidazol-1-ium Chemical compound CCCN1C=C[N+](C)=C1 WVDDUSFOSWWJJH-UHFFFAOYSA-N 0.000 claims description 3
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims description 3
- OXFHNKYFIVWAAT-UHFFFAOYSA-N 2-ethyl-1,3-dimethylimidazol-1-ium Chemical compound CCC=1N(C)C=C[N+]=1C OXFHNKYFIVWAAT-UHFFFAOYSA-N 0.000 claims description 3
- FLVCCOBLYCNTDS-UHFFFAOYSA-N 2-hydroxybenzoic acid;1-nonylimidazole Chemical compound OC(=O)C1=CC=CC=C1[O-].CCCCCCCCC[NH+]1C=CN=C1 FLVCCOBLYCNTDS-UHFFFAOYSA-N 0.000 claims description 3
- OXFBEEDAZHXDHB-UHFFFAOYSA-M 3-methyl-1-octylimidazolium chloride Chemical compound [Cl-].CCCCCCCCN1C=C[N+](C)=C1 OXFBEEDAZHXDHB-UHFFFAOYSA-M 0.000 claims description 3
- YMGJQBWOTAGHGX-UHFFFAOYSA-M 4-methylbenzenesulfonate;methyl(tripropyl)phosphanium Chemical compound CCC[P+](C)(CCC)CCC.CC1=CC=C(S([O-])(=O)=O)C=C1 YMGJQBWOTAGHGX-UHFFFAOYSA-M 0.000 claims description 3
- FOZHLSIBKHFJBR-UHFFFAOYSA-M 4-methylbenzenesulfonate;methyl-bis(2-methylpropyl)-octylphosphanium Chemical compound CC1=CC=C(S([O-])(=O)=O)C=C1.CCCCCCCC[P+](C)(CC(C)C)CC(C)C FOZHLSIBKHFJBR-UHFFFAOYSA-M 0.000 claims description 3
- WYBDAYBFOCKDRR-UHFFFAOYSA-M 4-methylbenzenesulfonate;methyl-bis(2-methylpropyl)-tetradecylphosphanium Chemical compound CC1=CC=C(S([O-])(=O)=O)C=C1.CCCCCCCCCCCCCC[P+](C)(CC(C)C)CC(C)C WYBDAYBFOCKDRR-UHFFFAOYSA-M 0.000 claims description 3
- SNXTZFCNWIVLKZ-UHFFFAOYSA-M 4-methylbenzenesulfonate;methyl-tris(2-methylpropyl)phosphanium Chemical compound CC1=CC=C(S([O-])(=O)=O)C=C1.CC(C)C[P+](C)(CC(C)C)CC(C)C SNXTZFCNWIVLKZ-UHFFFAOYSA-M 0.000 claims description 3
- ZZAZFRIZOXHKGA-UHFFFAOYSA-M 4-methylbenzenesulfonate;tritert-butyl(methyl)phosphanium Chemical compound CC1=CC=C(S([O-])(=O)=O)C=C1.CC(C)(C)[P+](C)(C(C)(C)C)C(C)(C)C ZZAZFRIZOXHKGA-UHFFFAOYSA-M 0.000 claims description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 3
- 239000005696 Diammonium phosphate Substances 0.000 claims description 3
- XTELRELDJGQKND-UHFFFAOYSA-N FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCCC)[N+](CCCC)(CCCC)CCCC Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCCC)[N+](CCCC)(CCCC)CCCC XTELRELDJGQKND-UHFFFAOYSA-N 0.000 claims description 3
- YWLUMNWUIHOAFB-UHFFFAOYSA-N FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCCCCCCCC)[N+](CCCCCCCCCCCC)(CCCCCCCCCCCC)CCCCCCCCCCCC Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCCCCCCCC)[N+](CCCCCCCCCCCC)(CCCCCCCCCCCC)CCCCCCCCCCCC YWLUMNWUIHOAFB-UHFFFAOYSA-N 0.000 claims description 3
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 3
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims description 3
- FEESKOXAZUKOOM-UHFFFAOYSA-N bis(dihexylamino)methylidene-dimethylazanium trifluoromethanesulfonamide Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCC)N(CCCCCC)C(N(CCCCCC)CCCCCC)=[N+](C)C FEESKOXAZUKOOM-UHFFFAOYSA-N 0.000 claims description 3
- UHILXEAXHSCVON-UHFFFAOYSA-M bis(dihexylamino)methylidene-dimethylazanium;chloride Chemical compound [Cl-].CCCCCCN(CCCCCC)C(=[N+](C)C)N(CCCCCC)CCCCCC UHILXEAXHSCVON-UHFFFAOYSA-M 0.000 claims description 3
- OMMLVGFDYVJZPD-UHFFFAOYSA-M bis(dioctylamino)methylidene-dimethylazanium;chloride Chemical compound [Cl-].CCCCCCCCN(CCCCCCCC)C(=[N+](C)C)N(CCCCCCCC)CCCCCCCC OMMLVGFDYVJZPD-UHFFFAOYSA-M 0.000 claims description 3
- 229910021538 borax Inorganic materials 0.000 claims description 3
- 239000001110 calcium chloride Substances 0.000 claims description 3
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 3
- 235000011148 calcium chloride Nutrition 0.000 claims description 3
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims description 3
- 229910000388 diammonium phosphate Inorganic materials 0.000 claims description 3
- 235000019838 diammonium phosphate Nutrition 0.000 claims description 3
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 claims description 3
- 229910000397 disodium phosphate Inorganic materials 0.000 claims description 3
- 235000019800 disodium phosphate Nutrition 0.000 claims description 3
- 235000011147 magnesium chloride Nutrition 0.000 claims description 3
- 239000001103 potassium chloride Substances 0.000 claims description 3
- 235000011164 potassium chloride Nutrition 0.000 claims description 3
- 235000010333 potassium nitrate Nutrition 0.000 claims description 3
- 239000004323 potassium nitrate Substances 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- 235000017550 sodium carbonate Nutrition 0.000 claims description 3
- 239000001488 sodium phosphate Substances 0.000 claims description 3
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 3
- 235000011152 sodium sulphate Nutrition 0.000 claims description 3
- 239000004328 sodium tetraborate Substances 0.000 claims description 3
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 3
- DZLFLBLQUQXARW-UHFFFAOYSA-N tetrabutylammonium Chemical compound CCCC[N+](CCCC)(CCCC)CCCC DZLFLBLQUQXARW-UHFFFAOYSA-N 0.000 claims description 3
- CBXCPBUEXACCNR-UHFFFAOYSA-N tetraethylammonium Chemical compound CC[N+](CC)(CC)CC CBXCPBUEXACCNR-UHFFFAOYSA-N 0.000 claims description 3
- LQYWIIQPCKDKFI-UHFFFAOYSA-N tetraheptylazanium trifluoromethanesulfonamide Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCCC)[N+](CCCCCCC)(CCCCCCC)CCCCCCC LQYWIIQPCKDKFI-UHFFFAOYSA-N 0.000 claims description 3
- ZBHGPIBVMLWJIK-UHFFFAOYSA-N tetraoctylazanium trifluoromethanesulfonamide Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCCCC)[N+](CCCCCCCC)(CCCCCCCC)CCCCCCCC ZBHGPIBVMLWJIK-UHFFFAOYSA-N 0.000 claims description 3
- VYIBWJHMEWSFNP-UHFFFAOYSA-N tetrapentylazanium trifluoromethanesulfonamide Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCC)[N+](CCCCC)(CCCCC)CCCCC VYIBWJHMEWSFNP-UHFFFAOYSA-N 0.000 claims description 3
- OSBSFAARYOCBHB-UHFFFAOYSA-N tetrapropylammonium Chemical compound CCC[N+](CCC)(CCC)CCC OSBSFAARYOCBHB-UHFFFAOYSA-N 0.000 claims description 3
- FJAPXHMQWAFWMW-UHFFFAOYSA-N tributyl(hexyl)azanium Chemical compound CCCCCC[N+](CCCC)(CCCC)CCCC FJAPXHMQWAFWMW-UHFFFAOYSA-N 0.000 claims description 3
- LNCGLHZZOHORCK-UHFFFAOYSA-N tributyl(hexyl)azanium trifluoromethanesulfonamide Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCC)[N+](CCCC)(CCCC)CCCC LNCGLHZZOHORCK-UHFFFAOYSA-N 0.000 claims description 3
- MCUDRUWIQOZDKK-UHFFFAOYSA-N tributyl(octyl)azanium trifluoromethanesulfonamide Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCCCC)[N+](CCCC)(CCCC)CCCC MCUDRUWIQOZDKK-UHFFFAOYSA-N 0.000 claims description 3
- YWRSPDSZBLLBPN-UHFFFAOYSA-M tributyl(octyl)azanium;trifluoromethanesulfonate Chemical compound [O-]S(=O)(=O)C(F)(F)F.CCCCCCCC[N+](CCCC)(CCCC)CCCC YWRSPDSZBLLBPN-UHFFFAOYSA-M 0.000 claims description 3
- GCRCSLNXFKCFHB-UHFFFAOYSA-N triethyl(hexyl)azanium Chemical compound CCCCCC[N+](CC)(CC)CC GCRCSLNXFKCFHB-UHFFFAOYSA-N 0.000 claims description 3
- RJELOMHXBLDMDB-UHFFFAOYSA-M trihexyl(tetradecyl)phosphanium;bromide Chemical compound [Br-].CCCCCCCCCCCCCC[P+](CCCCCC)(CCCCCC)CCCCCC RJELOMHXBLDMDB-UHFFFAOYSA-M 0.000 claims description 3
- GTCDARUMAMVCRO-UHFFFAOYSA-M tetraethylazanium;acetate Chemical compound CC([O-])=O.CC[N+](CC)(CC)CC GTCDARUMAMVCRO-UHFFFAOYSA-M 0.000 claims description 2
- PIXJXYLHXVSDQA-UHFFFAOYSA-N FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCC)[N+](CCCCCC)(CCCCCC)CCCCCC Chemical compound FC(S(=O)(=O)N)(F)F.FC(S(=O)(=O)N)(F)F.C(CCCCC)[N+](CCCCCC)(CCCCCC)CCCCCC PIXJXYLHXVSDQA-UHFFFAOYSA-N 0.000 claims 2
- 230000005670 electromagnetic radiation Effects 0.000 claims 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims 1
- 150000003839 salts Chemical class 0.000 abstract description 12
- 150000003863 ammonium salts Chemical class 0.000 abstract description 2
- 150000004714 phosphonium salts Chemical class 0.000 abstract description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical class C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 abstract 1
- 150000004693 imidazolium salts Chemical class 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 238000005516 engineering process Methods 0.000 description 7
- 230000008020 evaporation Effects 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 6
- 238000009835 boiling Methods 0.000 description 5
- 238000007710 freezing Methods 0.000 description 5
- 230000008014 freezing Effects 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 238000012986 modification Methods 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- RWRDLPDLKQPQOW-UHFFFAOYSA-O Pyrrolidinium ion Chemical compound C1CC[NH2+]C1 RWRDLPDLKQPQOW-UHFFFAOYSA-O 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- 238000003306 harvesting Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000011800 void material Substances 0.000 description 2
- RWRDLPDLKQPQOW-UHFFFAOYSA-N Pyrrolidine Chemical class C1CCNC1 RWRDLPDLKQPQOW-UHFFFAOYSA-N 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- HLSFBFYQBSVXBS-UHFFFAOYSA-O bis(aminomethylidene)azanium Chemical class NC=[N+]=CN HLSFBFYQBSVXBS-UHFFFAOYSA-O 0.000 description 1
- 150000001642 boronic acid derivatives Chemical class 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000994 depressogenic effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- XYFCBTPGUUZFHI-UHFFFAOYSA-O phosphonium Chemical compound [PH4+] XYFCBTPGUUZFHI-UHFFFAOYSA-O 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 1
Images
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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S10/00—Solar heat collectors using working fluids
- F24S10/10—Solar heat collectors using working fluids the working fluids forming pools or ponds
- F24S10/13—Salt-gradient ponds
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S60/00—Arrangements for storing heat collected by solar heat collectors
- F24S60/30—Arrangements for storing heat collected by solar heat collectors storing heat in liquids
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/44—Heat exchange systems
Definitions
- a solar pond upper convection zone includes an ionic liquid.
- ionic liquids include phosphonium salts such as, but not limited to:
- the solutions included in the NCZ and the LCZ may use a variety of salt including, but not limited to, sodium chloride, potassium chloride, magnesium chloride, calcium chloride, sodium nitrate, potassium nitrate, ammonium nitrate, sodium sulfate, sodium carbonate, sodium bicarbonate, disodium phosphate, borax, and diammonium phosphate, and other fertilizer salts.
- salt including, but not limited to, sodium chloride, potassium chloride, magnesium chloride, calcium chloride, sodium nitrate, potassium nitrate, ammonium nitrate, sodium sulfate, sodium carbonate, sodium bicarbonate, disodium phosphate, borax, and diammonium phosphate, and other fertilizer salts.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Combustion & Propulsion (AREA)
- Thermal Sciences (AREA)
- Sustainable Energy (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
Description
- This technology is generally related to the use of ionic liquids in solar ponds.
- Solar ponds are used for collection and storage of solar energy. The energy can be extracted from the solar ponds for any suitable thermal application. In general, a solar pond has a structure of three or more layers of different density liquids. Typically, salts such as magnesium chloride, sodium chloride or sodium nitrate are dissolved in water in a concentration from 20% to 30% in the bottom layer, and the top layer is void, or nearly void of such salts. The top, i.e. least dense, layer is termed the upper convection zone (UCZ), with the middle zone being termed the non-convection zone (NCZ), and the lower, i.e. most dense, layer being termed the lower convection zone (LCZ).
- The salinity of the UCZ is typically very close to that of fresh water. In the NCZ, the salinity increases with the depth, with the salinity of the upper part of the NCZ being close to that of fresh water, and that of the lower part being close to that in the LCZ. There is little or no natural thermal convection in the NCZ, hence the name, “non-convection zone.” However, solar radiation is able to penetrate this zone and increase the temperature of the solar pond as a auction of the depth. The LCZ is the most dense layer and has a, high density of salt. The LCZ layer acts as an energy storage. Maintenance of the temperature gradient in the NCZ is essential for the efficient use of solar ponds.
- There are at least two major problems leading to the poor thermal efficiency of solar ponds. One of them relates to the stability of the salt gradient, and, the other, to the thickness of the upper convection zone. Generally, the upper convection zone is a thick layer to prevent water evaporation since the stability of the salt gradient is important for the thermal performance of the solar pond. However, a thicker UCZ may limit the solar energy reaching the LCZ.
- In one aspect, a solar pond is provided including a upper convection zone that includes an ionic liquid; a non-convection zone; and a lower convection zone. In some embodiments, the ionic liquid has a density that is less than a density of the non-convection zone and the lower convection zone, at an operating temperature of the upper convection zone of the solar pond. In other embodiments, the ionic liquid has a density that is greater than a density of the non-convection zone, at an operating temperature of the upper convection zone of the solar pond, where the surface tension of the non-convection zone is sufficient to retain the ionic liquid as the upper convection zone. In some embodiments, the density of the ionic liquid is from 0.80 g/ml to 1.25 g/ml, and the operating temperature of the upper convection zone is from about 0° C. to about 100° C.
- In some embodiments, the ionic liquid includes an imidazolium ion, an ammonium ion, a pyrrolidinium ion, a pyridinium ion, a piperidium ion, or a phosphonium ion. In other embodiments, the ionic liquid is a liquid at the operating temperature of the upper convection zone of the solar pond. In other embodiments, the ionic liquid is stable to IR, UV, and/or visible radiation for extended periods. In some embodiments, the ionic liquid is stable to IR, UV, and/or visible radiation for up to 6 months. In other embodiments, the ionic liquid is stable to IR, UV, and/or visible radiation for 6 months or longer. In yet other embodiments, the ionic liquid is stable to IR, UV, and/or visible radiation for from 6 months to 2 years. In some embodiments, the upper convention zone is from 0.1% to 10% of a total depth of the solar pond.
- In some embodiments, the non-convection zone is an aqueous salt solution. In some embodiments, the lower convection zone includes an aqueous salt solution, that is of a higher concentration than the non-convention zone. In such embodiments, the aqueous salt solutions include sodium chloride, potassium chloride, magnesium chloride, calcium chloride, sodium nitrate, potassium nitrate, ammonium nitrate, sodium sulfate, sodium carbonate, sodium bicarbonate, disodium phosphate, borax, and diammonium phosphate.
- In another aspect, a solar pond upper convection zone includes an ionic liquid.
- In another aspect, a geothermal system includes a solar pond including an upper convection zone including an ionic liquid.
-
FIG. 1 is a schematic drawing of a solar pond, according to one embodiment. - In the following detailed description, reference is made to the accompanying drawings, which form a part hereof. In the drawings, similar symbols typically identify similar components, unless context dictates otherwise. The illustrative embodiments described in the detailed description, drawings, and claims are not meant to be limiting. Other embodiments may be utilized, and other changes may be made, without departing from the spirit or scope of the subject matter presented here. The present technology is also illustrated by the examples herein, which should not be construed as limiting in any way.
- In one aspect, a solar pond is provided in which the UCZ includes an ionic liquid. In some embodiments the ionic liquid is non-volatile at atmospheric pressure and at a temperature of about 100° C. The zero, or near zero, evaporation of ionic liquids allows their application as a thin upper convection zone, which acts as a cap on the solar pond, preventing or diminishing evaporation of the water from the NCZ and LCZ, thereby maintaining a steady salt gradient in the system. This can improve the thermal performance of the solar pond in comparison to purely aqueous-based ponds.
- An illustration of an ionic liquid solar pond design is schematically shown in
FIG. 1 . Ionic liquids are used as the UCZ (120), while the NCZ (140) and the LCZ (160) are aqueous salt solutions as are blown in conventional solar ponds. Since there is a density gradient which increases from the top to the bottom layers, the layers tend not to mix to the extent that they maintain their separate identities. As a result, the ionic solar pond may simply be prepared by carefully layering the NCZ atop the LCZ and the UCZ atop the NCZ. Because of their zero or near zero evaporation pressure, ionic liquids act as a cover for the non-convection zone below it. Therefore, the water evaporation is decreased or avoided and the salt gradient remains more stable and consistent than in a conventional solar pond. Therefore thermal performance variations of the solar pond caused by fluctuations of the salt gradient of the non-convection zone will be reduced or eliminated. Also because of its diminished evaporation, the thickness of the ionic liquid containing upper convection zone can be very thin, so that the solar energy can be effectively transferred to the energy storage zone, with a minimum of losses due to absorption by the ionic liquid. - Ionic liquids are typically non-flammable, or are flame retardants, and have a high heat capacity of fusion. Consequently, the ionic liquid upper convection zone may improve the stability and the energy harvesting of the solar pond.
- Ionic liquids useful as the upper convection zone of solar ponds may be selected based on a variety of physical characteristics including but not limited to their stability to the sun's radiation; fluidity within the operating temperature of the solar pond; ability to remain the surface layer of the solar pond; and relative immiscibility with water.
- For example, the ionic liquid for use as an UCZ in a solar pond is stable to the sun's radiation for the period of time it is used in the solar pond. When exposed to the sun in a solar pond, such ionic liquids are stable, e.g., for 1-12 hours, 1-7 days, 1-4 weeks, 1-6 months, 6 months to 2 years, or longer than 6 months. In some embodiments, the ionic liquid is stable to infra-red, visible, and/or UV radiation for these periods of time. In some embodiments, the ionic liquid absorbs 10%, 20%, 30%, 40%, 50%, 60%, 70%, 80%, or 90% of UV radiation in the 400 nm-800 nm, 300 nm-400 nm, or the 150 nm-300 nm region, and the rest is allowed to pass through the UCZ to the NCL or LCZ. In other embodiments, the ionic liquid absorbs 10%, 20%, 30%, 40%, 50%, 60%, 70%, 80%, or 90% of infra-red radiation, and the rest is allowed to pass through the UCZ to the NCZ or LCZ. The UV and IR absorption properties of the ionic liquids can be easily determined by methods well-known to the skilled artisan, for example simply by using UV- or IR-absorption spectrometers.
- It is desirable that the ionic liquid exists in the fluid state when used in a solar pond to harvest solar energy. If the UCZ is a liquid, the transfer of energy via the UCZ to the NCZ may be supported by the convection within the UCZ. Generally the LCZ and the NCZ, are also fluids. The LCZ of the a solar pond relies on fluid movement in that zone to absorb and transfer heat within the pond. For mass balance and salinity balance in the pond, the NCZ of the solar pond is also typically a liquid.
- The ionic liquid will have a density so that the UCZ including the ionic liquid is maintained as a cap on the solar pond. This may be accomplished in at least two ways. First, the density of the ionic liquid may be lower that that of the least dense portion of the NCZ. Thus, based upon density alone, the ionic liquid will remain as the top layer and maintain it's position as a cap on the solar pond. Second, the density of the ionic liquid may be slightly greater than the least dense portion of the NCZ; however, in such situations, the UCZ layer may have to be sufficiently thin that the surface tension of the NCZ, is sufficient to retain the ionic liquid as a UCZ and not allow it to sink into the solar pond. If the density of the ionic liquid is much larger than that of the least dense portion of the NCZ, the ionic liquid may not be retained as a surface cap. The temperature of the UCZ may also impact its density. The ionic liquid should not be miscible with water solutions.
- Accordingly, in some embodiments, the ionic liquid has a density that is less than a density of the non-convection zone and the lower convection zone, at an operating temperature of the upper convection zone of the solar pond. In other embodiments, the density of the ionic liquid is from 0.80 g/ml to 1.25 g/ml, and the operating temperature of the upper convection zone is from about 0° C. to about 100° C. As used herein, the term about as applied to the temperature is a value that takes into account the phenomena of freezing point depression and boiling point elevation. When a solute such as a salt is dissolved in water, it may have a freezing point that is less than that of pure water (i.e. 0° C.), or it may have a boiling point that is higher than that of pure water (i.e. 100° C.). Therefore, where the saline solutions of the NCZ or the LCZ have freezing points lower than that of pure water, the operating temperature is from a temperature that is about equal to the temperature of the freezing point depressed saline solution to a temperature that is about equal to the temperature of the boiling point elevated saline solution. Or, in other words, from about 0° C. to about 100° C. If the temperature goes beyond the boiling point of the boiling point elevated saline solution, the solar pond will be disrupted. If the temperature is below the freezing point, there may not be efficient heat convection.
- It is also desirable that the ionic liquid is not miscible with aqueous salt solutions that form the NCZ layer or in some instances with water to the extent that it is not dispersed upon contact with the NCZ. This way, the water in the NCZ or the LCZ layers may not solubilize the ionic liquid and disperse it throughout the solar pond.
- There are a large number of known ionic liquids that may be included in the UCZ of a solar pond. For example, some ionic liquids generally include imidazolium ions, ammonium ions (including tetraalkylammonium ions), pyrrolidinium ions, pyridinium ions, piperidium ions, or phosphonium ions. A large number of ionic liquids and their properties have been reviewed by Handy (Current Organic Chemistry (2005) 9, 959-988), which may be used in accordance with the present technology. Illustrative examples ionic liquids include alkyl imidazolium salts, such as, but not limited to,:
- 3-methyl-1-(propan-ol)-imidazolium hexafluorophosphate;
- 3-methyl-1-(propan-2-ol)-imidazolium chloride;
- 3-methyl-1-(propan-2-ol)-imidazolium nitrate;
- 3-methyl-1-(ethoxyethoxy)-imidazolium hexafluorophosphate;
- 3-hexyl-1-(2-diethylphosphonato-ethyl)-imidazolium tetrafluoroborate;
- 3-hexyl-1-(3-diethylphosphonato-propyl)-imidazolium tetrafluoroborate;
- 3-octyl-1-(2-diethylphosphonato-ethyl)-imidazolium tetrafluoroborate;
- 3-methyl-1-butyl-imidazolium tetrafluoroborate;
- 3-methyl-1-butyl-imidazolium chloride;
- 3-methyl-1-butyl-imidazolium octyl sulfate;
- 3-methyl-1-butyl-imidazolium fluorohydrogenate;
- 3-methyl-1-ethyl-imidazolium tricyanomethane;
- 3-methyl-1-ethyl-imidazolium fluorohydrogenate;
- 3-methyl-1-ethyl-imidazolium carborane;
- 3-methyl-1-ethyl-imidazolium methylcarborane;
- 3-methyl-1-ethyl-imidazolium ethylcarborane;
- 3-methyl-1-methyl-imidazolium fluorohydrogenate;
- 3-methyl-1-propyl-imidazolium fluorohydrogenate;
- 3-methyl-1-pentyl-imidazolium fluorohydrogenate;
- 3-methyl-1-hexyl-imidazolium fluorohydrogenate;
- 3-methyl-1-hexyl-imidazolium chloride;
- 3-methyl-1-octyl-imidazolium chloride;
- 3-methyl-1-octyl-imidazolium tetrafluoroborate;
- 3-methyl-1-methyl-imidazolium tetrafluoroborate;
- 3-methyl-2-ethyl-1-methyl-imidazolium carborate;
- octylimidazolium salicylate;
- nonylimidazolium salicylate;
- dodecylimidazolium salicylate; or
- (butyoxymethyl)imidazolium salicylate.
- Other illustrative examples of ionic liquids include ammonium salts such as, but not limited to:
- tetraethylammonium tributyoctylborate;
- tetraethylammonium acetate;
- hexyl-triethyl-ammonium hexyl-triethylborate;
- hexyl-triethyl-ammonium tributyoctylborate;
- tetrapropylammonium tripropylhexylborate;
- tetrabutylammonium tributyhexylborate;
- hexyl-tri-butylammonium tributylhexylborate;
- hexyl-tri-butylammonium bis-trifluoromethanesulfonamide;
- heptyl-tri-butylammonium bis-trifluoromethanesulfonamide;
- tetrapentylammonium bis-trifluoromethanesulfonamide;
- octyl-tri-butylammonium bis-trifluoromethanesulfonamide;
- octyl-tri-butylammonium trifluoromethylsulfonate;
- tetrahexylammonium bis-tifluoromethanesulfonamide;
- tetrahexylammonium tributyhexylborate;
- tetraheptylammonium bis-trifluoromethanesulfonamide;
- tetraoctylammonium bis-trifluoromethanesulfonamide; or
- tetradodecylammonium bis-trifluoromethanesulfonamide.
- Yet other illustrative examples of ionic liquids include pyrrolidinium salts such as, but not limited to:
- N-methyl-N-propylpyrrolidine dicyanimide;
- N-methyl-N-butylpyrrolidine dicyanimide; or
- N-methyl-N-hexylpyrrolidine dicyanimide.
- Yet other illustrative examples of ionic liquids include bis-aminomethylene-ammonium salts such as, but not limited to:
- [bis-(N-butyl-N-ethyl-amino)-methylene]dimethyl-ammonium tetrafluoroborate;
- [bis-(N-hexyl-N-hexyl-amino)-methylene]-dimethyl-ammonium tetrafluoroborate;
- [bis-(N-hexyl-N-hexyl-amino)-methylene]-dimethyl-ammonium hexafluorophosphate;
- [bis-(N-hexyl-N-hexyl-amino)-methylene]-dimethyl-ammonium chloride;
- [bis-(N-hexyl-N-hexyl-amino)-methylene]-dimethyl-ammonium bis-trifluoromethanesulfonamide;
- [bis-(N-octyl-N-octyl-amino)-methylene]-dimethyl-ammonium tetrafluoroborate;
- [bis-(N-octyl-N-octyl-amino)-methylene]-dimethyl-ammonium hexafluorophosphate; or
- [bis-(N-octyl-N-octyl-amino)-methylene]-dimethyl-ammonium chloride.
- Yet other illustrative examples of ionic liquids include phosphonium salts such as, but not limited to:
- methyl-tripropylphosphonium tosylate;
- methyl-tri-(iso-butyl)phosphonium tosylate;
- methyl-tri-(tert-butyl)phosphonium tosylate;
- methyl-di-(iso-butyl)-octylphosphonium tosylate;
- methyl-di-(iso-butyl)-tetradecylphosphonium tosylate;
- tetradecyl-tri-(hexyl)-phosphonium bromide;
- tetradecyl-tri-(hexyl)-phosphonium tetrafluoroborate; or
- tetradecyl-tri-(hexyl)-phosphonium hexafluorophosphate.
- As will be understood, the density of the ionic liquids may vary as a function of both the cationic part (i.e. the imidazolium, ammonium, phosphonium, pyridinium, pyrrolidinium, etc) and the anionic part (i.e. the salicylate, tetrafluoroborate, other borates, carborane, tosylate, etc.). The structure-density variations of various ionic liquids and variations of their other properties relative to their structure are well known. See, e.g. Zhang et al., J. Phys. Chem. Ref. Data, Vol. 35, No. 4, 2006 (incorporated herein by reference).
- As noted above, the non-convection zone and the lower convection zone are aqueous salt solutions. These zones form a vertical salinity gradient, in which lower salinity solutions float on top of higher salinity solutions. Thus, near the interface between the ionic liquid and the NCZ, the salinity of the aqueous phase is lowest and near the bottom of the LCZ, the salinity is highest. Because of the higher salinity of the LCZ, solar radiation is more efficiently absorbed, thereby heating the water. According to various embodiments, the solutions included in the NCZ and the LCZ may use a variety of salt including, but not limited to, sodium chloride, potassium chloride, magnesium chloride, calcium chloride, sodium nitrate, potassium nitrate, ammonium nitrate, sodium sulfate, sodium carbonate, sodium bicarbonate, disodium phosphate, borax, and diammonium phosphate, and other fertilizer salts.
- The various layers may be of various thickness, as long as their relative layered structure and function remains intact. According to some embodiments, the UCZ is from 0.1% to 10% of a total depth of the solar pond; the NCZ is from 1% to 50% of a total depth of the solar pond; and the LCZ is from 10% to 90% of a total depth of the solar pond.
- Solar ponds including an ionic liquid may be used in a variety of thermal applications. For example, geothermal systems which extract energy from the ground or water for use in heating, may advantageously use such solar ponds. Other uses include electricity production, for example as produced by Rankine engines.
- While certain embodiments have been illustrated and described, it should be understood that changes and modifications can be made therein in accordance with ordinary skill in the art without departing from the technology in its broader aspects as defined in the following claims.
- All publications, patent applications, issued patents, and other documents referred to in this specification are herein incorporated by reference as if each individual publication, patent application, issued patent, or other document was specifically and individually indicated to be incorporated by reference in its entirety. Definitions that are contained in text incorporated by reference are excluded to the extent that they contradict definitions in this disclosure.
- The present disclosure is not to be limited in terms of the particular embodiments described in this application. Many modifications and variations can be made without departing from its spirit and scope, as will be apparent to those skilled in the art. Functionally equivalent methods and compositions within the scope of the disclosure, in addition to those enumerated herein, will be apparent to those skilled in the art from the foregoing descriptions. Such modifications and variations are intended to fall within the scope of the appended claims. The present disclosure is to be limited only by the terms of the appended claims, along with the full scope of equivalents to which such claims are entitled. It is to be understood that this disclosure is not limited to particular methods, reagents, compounds compositions or biological systems, which can of course vary. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting.
- The embodiments, illustratively described herein may suitably be practiced in the absence of any element or elements, limitation or limitations, not specifically disclosed herein. Thus, for example, the terms “comprising,” “including,” “containing,” etc. shall be read expansively and without limitation. Additionally, the terms and expressions employed herein have been used as terms of description and not of limitation, and there is no intention in the use of such terms and expressions of excluding any equivalents of the features shown and described or portions thereof, but it is recognized that various modifications are possible within the scope of the claimed technology. Additionally, the phrase “consisting essentially of” will be understood to include those elements specifically recited and those additional elements that do not materially affect the basic and novel characteristics of the claimed technology. The phrase “consisting of” excludes any element not specified.
- In addition, where features or aspects of the disclosure are described in terms of Markush groups, those skilled in the art will recognize that the disclosure is also thereby described in terms of any individual member or subgroup of members of the Markush group.
- As will be understood by one skilled in the art, for any and all purposes, particularly in terms of providing a written description, all ranges disclosed herein also encompass any and all possible subranges and combinations of subranges thereof. Any listed range can be easily recognized as sufficiently describing and enabling the same range being broken down into at least equal halves, thirds, quarters, fifths, tenths, etc. As a non-limiting example, each range discussed herein can be readily broken down into a lower third, middle third and upper third, etc. As will also be understood by one skilled in the art all language such as “up to,” “at least,” “greater than,” “less than,” and the like, include the number recited and refer to ranges which can be subsequently broken down into subranges as discussed above. Finally, as will be understood by one skilled in the art, a range includes each individual member.
- Other embodiments are set forth in the following claims.
Claims (20)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US2011/023317 WO2012105958A1 (en) | 2011-02-01 | 2011-02-01 | Ionic liquid solar ponds |
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| Publication Number | Publication Date |
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| US20120192856A1 true US20120192856A1 (en) | 2012-08-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| US13/145,687 Abandoned US20120192856A1 (en) | 2011-02-01 | 2011-02-01 | Ionic liquid solar ponds |
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| WO (1) | WO2012105958A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014063814A1 (en) * | 2012-10-24 | 2014-05-01 | Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. . | Method for thermochemically storing heat, and use of a composition for said method, containing a salt made of an organic base and an organic acid |
| CN113725378A (en) * | 2021-08-31 | 2021-11-30 | 苏州大学 | Perovskite light emitting diode |
| US11298326B2 (en) | 2015-03-24 | 2022-04-12 | Kyowa Kirin Co., Ltd. | Nucleic acid-containing lipid nanoparticles |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109539569B (en) * | 2018-11-12 | 2019-10-15 | 西安交通大学 | solar pool |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4063419A (en) * | 1976-11-12 | 1977-12-20 | Garrett Donald E | Energy production from solar ponds |
| US4244351A (en) * | 1978-11-06 | 1981-01-13 | Intertechnology/Solar Corporation | Solar collection system |
| US4249518A (en) * | 1979-10-22 | 1981-02-10 | Holt Rush D | Method for maintaining a correct density gradient in a non-convecting solar pond |
| US4326498A (en) * | 1980-11-05 | 1982-04-27 | Eckland John E | Solar canal |
| US4408459A (en) * | 1977-05-09 | 1983-10-11 | Amnon Yogev | Heat storage pond and power plant using same |
| US4541244A (en) * | 1980-03-27 | 1985-09-17 | Solmat Systems Ltd. | Method of and means for maintaining a halocline in an open body of salt water |
| US4744349A (en) * | 1986-07-28 | 1988-05-17 | Sorensen Jens Ole | Suppression of heat convection in aqueous insulation layer of solar pond |
| US20100099314A1 (en) * | 2004-11-01 | 2010-04-22 | Stacie Ellen Hecht | Ionic liquids derived from surfactants |
| US20100258251A1 (en) * | 2008-12-08 | 2010-10-14 | George Nitschke | System integration to produce concentrated brine and electricity from geopressured-geothermal reservoirs |
| US7828990B1 (en) * | 2008-02-14 | 2010-11-09 | Sandia Corporation | Low-melting point heat transfer fluid |
| US20110067690A1 (en) * | 2009-09-18 | 2011-03-24 | Massachusetts Institute Of Technology | Concentrated solar power system receiver |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62218766A (en) * | 1986-03-20 | 1987-09-26 | Toshiba Corp | Solar pond |
| JPS63210562A (en) * | 1987-02-26 | 1988-09-01 | Toshiba Corp | Solar pond |
| US5220792A (en) * | 1987-12-04 | 1993-06-22 | Ormat Turbines (1965) Ltd. | Method of and means for extracting heat from a hot fluid containing foreign material that interferes with heat transfer |
-
2011
- 2011-02-01 US US13/145,687 patent/US20120192856A1/en not_active Abandoned
- 2011-02-01 WO PCT/US2011/023317 patent/WO2012105958A1/en not_active Ceased
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4063419A (en) * | 1976-11-12 | 1977-12-20 | Garrett Donald E | Energy production from solar ponds |
| US4408459A (en) * | 1977-05-09 | 1983-10-11 | Amnon Yogev | Heat storage pond and power plant using same |
| US4244351A (en) * | 1978-11-06 | 1981-01-13 | Intertechnology/Solar Corporation | Solar collection system |
| US4249518A (en) * | 1979-10-22 | 1981-02-10 | Holt Rush D | Method for maintaining a correct density gradient in a non-convecting solar pond |
| US4541244A (en) * | 1980-03-27 | 1985-09-17 | Solmat Systems Ltd. | Method of and means for maintaining a halocline in an open body of salt water |
| US4326498A (en) * | 1980-11-05 | 1982-04-27 | Eckland John E | Solar canal |
| US4744349A (en) * | 1986-07-28 | 1988-05-17 | Sorensen Jens Ole | Suppression of heat convection in aqueous insulation layer of solar pond |
| US20100099314A1 (en) * | 2004-11-01 | 2010-04-22 | Stacie Ellen Hecht | Ionic liquids derived from surfactants |
| US7828990B1 (en) * | 2008-02-14 | 2010-11-09 | Sandia Corporation | Low-melting point heat transfer fluid |
| US20100258251A1 (en) * | 2008-12-08 | 2010-10-14 | George Nitschke | System integration to produce concentrated brine and electricity from geopressured-geothermal reservoirs |
| US20110067690A1 (en) * | 2009-09-18 | 2011-03-24 | Massachusetts Institute Of Technology | Concentrated solar power system receiver |
Non-Patent Citations (4)
| Title |
|---|
| Anderson, Jared et al., Ionic Liquids in Analytical Chemistry, May 1, 2006, Pages 2893-2894 * |
| Handy, S.T., "Room Temperature Ionic Liquids: Different Classes and Physical Properties," Current Organic Chemistry, 2005, Vol. 9 pp. 959-988. * |
| Kirchner, Barbara (Ed.), Ionic Liquids, Synthesis, Purification and Characterization of Ionic Liquids, 2010, Vol. 290, Page 7 * |
| Pimentel, D., Herz, M., Glickstein, M., Zimmerman, M., & al, e. (2002). Renewable energy: Current and potential issues. Bioscience, 52(12), 1111-1120. Retrieved from http://search.proquest.com/docview/216468480?accountid=14753 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014063814A1 (en) * | 2012-10-24 | 2014-05-01 | Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. . | Method for thermochemically storing heat, and use of a composition for said method, containing a salt made of an organic base and an organic acid |
| US11298326B2 (en) | 2015-03-24 | 2022-04-12 | Kyowa Kirin Co., Ltd. | Nucleic acid-containing lipid nanoparticles |
| CN113725378A (en) * | 2021-08-31 | 2021-11-30 | 苏州大学 | Perovskite light emitting diode |
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