WO2003037512A2 - Systeme de confinement a chambres multiples - Google Patents
Systeme de confinement a chambres multiples Download PDFInfo
- Publication number
- WO2003037512A2 WO2003037512A2 PCT/US2002/034649 US0234649W WO03037512A2 WO 2003037512 A2 WO2003037512 A2 WO 2003037512A2 US 0234649 W US0234649 W US 0234649W WO 03037512 A2 WO03037512 A2 WO 03037512A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- substance
- fluid communication
- electrochemical cell
- cell
- fuel
- Prior art date
Links
- 239000000126 substance Substances 0.000 claims abstract description 237
- 238000000034 method Methods 0.000 claims abstract description 93
- 230000008569 process Effects 0.000 claims abstract description 91
- 239000006227 byproduct Substances 0.000 claims abstract description 40
- 239000000446 fuel Substances 0.000 claims description 61
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 51
- 239000012530 fluid Substances 0.000 claims description 28
- 239000001257 hydrogen Substances 0.000 claims description 25
- 229910052739 hydrogen Inorganic materials 0.000 claims description 25
- 238000012545 processing Methods 0.000 claims description 25
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 24
- 229910052751 metal Inorganic materials 0.000 claims description 24
- 239000002184 metal Substances 0.000 claims description 24
- 239000000376 reactant Substances 0.000 claims description 22
- 238000004891 communication Methods 0.000 claims description 20
- 230000004888 barrier function Effects 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 13
- 239000007787 solid Substances 0.000 claims description 12
- 238000001311 chemical methods and process Methods 0.000 claims description 9
- 238000003786 synthesis reaction Methods 0.000 claims description 9
- 244000025254 Cannabis sativa Species 0.000 claims description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 8
- 239000003502 gasoline Substances 0.000 claims description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 230000015572 biosynthetic process Effects 0.000 claims description 6
- 239000003792 electrolyte Substances 0.000 claims description 6
- 239000002699 waste material Substances 0.000 claims description 6
- 238000005520 cutting process Methods 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 239000012279 sodium borohydride Substances 0.000 claims description 5
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 5
- 230000007246 mechanism Effects 0.000 claims description 4
- 150000002894 organic compounds Chemical class 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 239000002028 Biomass Substances 0.000 claims description 3
- 239000007795 chemical reaction product Substances 0.000 claims description 3
- 239000008213 purified water Substances 0.000 claims description 3
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims description 2
- 238000002242 deionisation method Methods 0.000 claims description 2
- 230000003197 catalytic effect Effects 0.000 claims 3
- 230000003292 diminished effect Effects 0.000 claims 2
- 239000002915 spent fuel radioactive waste Substances 0.000 claims 2
- 239000002283 diesel fuel Substances 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 239000003208 petroleum Substances 0.000 claims 1
- 239000003209 petroleum derivative Substances 0.000 claims 1
- 230000026676 system process Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 24
- 239000000047 product Substances 0.000 description 17
- 239000000463 material Substances 0.000 description 13
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- 238000002485 combustion reaction Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 9
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 8
- 239000008103 glucose Substances 0.000 description 8
- 230000005611 electricity Effects 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- 230000007423 decrease Effects 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 239000001569 carbon dioxide Substances 0.000 description 5
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 230000003247 decreasing effect Effects 0.000 description 4
- 229910044991 metal oxide Inorganic materials 0.000 description 4
- 150000004706 metal oxides Chemical class 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 230000032258 transport Effects 0.000 description 4
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 239000011701 zinc Substances 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- -1 for example Substances 0.000 description 3
- 239000002828 fuel tank Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 229910052720 vanadium Inorganic materials 0.000 description 3
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000010923 batch production Methods 0.000 description 2
- MOOAHMCRPCTRLV-UHFFFAOYSA-N boron sodium Chemical compound [B].[Na] MOOAHMCRPCTRLV-UHFFFAOYSA-N 0.000 description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 2
- 229910052794 bromium Inorganic materials 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 238000003487 electrochemical reaction Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000036647 reaction Effects 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- SJRJJKPEHAURKC-UHFFFAOYSA-O 4-methylmorpholin-4-ium Chemical compound C[NH+]1CCOCC1 SJRJJKPEHAURKC-UHFFFAOYSA-O 0.000 description 1
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 241001481828 Glyptocephalus cynoglossus Species 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- UQGFMSUEHSUPRD-UHFFFAOYSA-N disodium;3,7-dioxido-2,4,6,8,9-pentaoxa-1,3,5,7-tetraborabicyclo[3.3.1]nonane Chemical compound [Na+].[Na+].O1B([O-])OB2OB([O-])OB1O2 UQGFMSUEHSUPRD-UHFFFAOYSA-N 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 125000001841 imino group Chemical group [H]N=* 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical group C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000011369 resultant mixture Substances 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- YYMBJDOZVAITBP-UHFFFAOYSA-N rubrene Chemical compound C1=CC=CC=C1C(C1=C(C=2C=CC=CC=2)C2=CC=CC=C2C(C=2C=CC=CC=2)=C11)=C(C=CC=C2)C2=C1C1=CC=CC=C1 YYMBJDOZVAITBP-UHFFFAOYSA-N 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- NVIFVTYDZMXWGX-UHFFFAOYSA-N sodium metaborate Chemical compound [Na+].[O-]B=O NVIFVTYDZMXWGX-UHFFFAOYSA-N 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- ITMCEJHCFYSIIV-UHFFFAOYSA-M triflate Chemical compound [O-]S(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-M 0.000 description 1
- 125000001889 triflyl group Chemical group FC(F)(F)S(*)(=O)=O 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 229920003169 water-soluble polymer Polymers 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/065—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents from a hydride
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M12/00—Hybrid cells; Manufacture thereof
- H01M12/04—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
- H01M12/06—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/065—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dissolution of metals or alloys; by dehydriding metallic substances
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/16—Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
- H01M8/184—Regeneration by electrochemical means
- H01M8/188—Regeneration by electrochemical means by recharging of redox couples containing fluids; Redox flow type batteries
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Definitions
- the present invention relates generally to containment systems, and particularly containment systems configured for delivering and collecting substances. Description Of The Prior Art
- Figures 9A and 9B show a further embodiment of a structure for a multiple chamber containment system; and Figures 10A and 10B show still another embodiment of a structure for a multiple chamber containment system;.
- Figure 7 A shows a container 710 having a first portion 712 and a second portion 714 separated by a movable barrier 716, e.g., movable with assistance of a structure 722, which may comprise a helical screw, a linearly actuated device, or the like.
- Figure 7B shows container 710 having a larger volume in the second portion 714, due to movement of the barrier 716.
- Figure 9A shows a container 910 having a second portion 914 and a first portion 912, wherein the volume of the first portion 912 is defined by the space between the inner walls of the container 910 and the outer walls of the second portion 914.
- Figure 9B shows container 910 having a larger volume in the second portion 914, due to filling with a substance, and accordingly the volume of the portion 912 is decreased.
- Figure 10A shows a container 1010 having a first portion 1012 and a second portion 1014 in inversely variable volume relationship within the container 1010.
- Figure 10B shows container 1010 having a larger volume in the first portion 1014, due to filling with a substance, and accordingly the volume of the portion 1014 is decreased.
- the substances in the first and second portions may be the same or different.
- the container 110 may be a portable device, for example, suitable for laptop computers, cellular phones, power tools, other handheld devices, small transports devices such as scooters, etc. Further, container 110 may be integral with a system such as a land, water, or air vessel. Additionally, container 110 may be integral within an on-site power generation system. In a further embodiment, the process 120 may actually comprise several electrochemical cells.
- the connection between the portion 112 of the container 110 may have plural branches, that are separately connected to the plural electrochemical cells. Using suitable mechanical or fluid flow controls, such as valves, the metal fuel may be selectively transported to one or more of the connected plural electrochemical cells, forming cell systems of varying voltage and/or current.
- the partially used fuel from portion 513b may be circulated through the process 520 repeatedly, until it is determined (e.g., via an associated controller, voltage sensor, or the like) that the capacity is minimized. This will ensure the highest possible depth of discharge of the metal fuel. When the capacity of the metal fuel is minimized, then it may be outputted as final exhaust to portion 514.
- the catholyte may comprise the first substance, such as a bromine solution.
- the bromine is generally converted to bromide ions and is stored to in the second portion 114 as the second substance.
- the catholyte reacts at cell 320 according to the following half-cell reaction:
- the anolyte reacts at cell 320 according to the following half-cell reaction:
- MULTIPLE CHAMBER SYSTEM 500a Referring now to Figure 5A, a system 500a using a container 510 coupled to a process
- the container 510 comprises the first portion 512 having a first substance, and the second portion 513a having a second substance, which both generally provide input substances to process 520.
- the first and second inputs substance may be released to the process 520 at various rates and intervals, which may be the same or different from each other.
- the output of the process 520, a third substance, is provided to a portion 514 of the container 510.
- a specific embodiment of a chemical synthesis using system 500a include water gas shift reactions.
- carbon monoxide plus water react to produce carbon dioxide and hydrogen.
- the first portion 512 includes carbon monoxide and the second portion 513a includes water.
- the contents of the first portion 512 and the second portion 513a are fed to the process 520.
- the process 520 is typically at elevated temperatures, and over one or more catalysts.
- the resultant mixture of carbon dioxide and hydrogen is then stored in the third portion 514. Accordingly, as the reactants (carbon monoxide and water) form the products (carbon dioxide and hydrogen), the volume of the container 510 may remain constant, since portions 512 and 513 contract, and portion 514 expands.
- the useful byproduct may be light, wherein the process 520 comprises a transparent mixing chamber for mixing the first and second substances.
- the first and second substances are chemicals that, when combined, produce light.
- U.S. Patent No. 4,859,369 (the '"369 patent"), incorporated by reference herein, describes the use of water-soluble polymers in aqueous chemical light formulations.
- an aqueous solution of 4,4'- oxalylbis[(trifluoromethylsulfonyl)imino]ethylene]-bis[4-methylmorpholinium trifluoromethane-sulfonate], referred to as METQ, is mixed with poly(vinylpyrrolidone) and fluorescer rubrene sulfonate.
- Aqueous hydrogen peroxide is then added, which, when mixed, is capable of producing a bioluminescent material.
- any or all of the reactants may be stored as the first substance and the second substance in the container 500, or a similar container having additional portions for holding more than two reactants.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Manufacturing & Machinery (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Energy (AREA)
- Sustainable Development (AREA)
- Organic Chemistry (AREA)
- Biochemistry (AREA)
- Microbiology (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Fuel Cell (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Medical Preparation Storing Or Oral Administration Devices (AREA)
Abstract
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR10-2004-7006402A KR20040060956A (ko) | 2001-10-29 | 2002-10-29 | 다중챔버 보관장치 |
EP02784325A EP1565958A2 (fr) | 2001-10-29 | 2002-10-29 | Systeme de confinement a chambres multiples |
JP2003539844A JP2005512275A (ja) | 2001-10-29 | 2002-10-29 | 複数チャンバー式格納システム |
AU2002348108A AU2002348108A1 (en) | 2001-10-29 | 2002-10-29 | Multiple chamber containment system |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US34059201P | 2001-10-29 | 2001-10-29 | |
US60/340,592 | 2001-10-29 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2003037512A2 true WO2003037512A2 (fr) | 2003-05-08 |
WO2003037512A3 WO2003037512A3 (fr) | 2005-06-02 |
Family
ID=23334064
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2002/034649 WO2003037512A2 (fr) | 2001-10-29 | 2002-10-29 | Systeme de confinement a chambres multiples |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP1565958A2 (fr) |
JP (1) | JP2005512275A (fr) |
KR (1) | KR20040060956A (fr) |
CN (1) | CN1636251A (fr) |
AU (1) | AU2002348108A1 (fr) |
TW (2) | TWI253202B (fr) |
WO (1) | WO2003037512A2 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101210841B1 (ko) * | 2011-04-12 | 2012-12-11 | 부산대학교 산학협력단 | 비폭기 유기물 제거장치 |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102007034700A1 (de) * | 2007-07-16 | 2009-01-22 | Rennebeck, Klaus, Dr. | Redox-Batterie |
WO2024175589A1 (fr) * | 2023-02-24 | 2024-08-29 | Litricity Gmbh | Système de batterie redox |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3414437A (en) * | 1963-05-13 | 1968-12-03 | Electromechanical Devices Inc | Fluid circulating battery system |
US3551208A (en) * | 1966-12-12 | 1970-12-29 | Yardney International Corp | Cell with displaceable electrode |
JPS62229665A (ja) * | 1986-03-29 | 1987-10-08 | Sumitomo Electric Ind Ltd | 電解液流通型2次電池 |
JPS62271360A (ja) * | 1986-05-16 | 1987-11-25 | Sumitomo Electric Ind Ltd | 電解液流通型2次電池 |
AU7326096A (en) * | 1996-10-16 | 1998-05-11 | Kinga Paczolay | Electric vehicle |
HU221405B1 (en) * | 1996-10-16 | 2002-09-28 | Gyoergy Pintz | Electric currentless arrangement and method for charging accumulators |
JP3915334B2 (ja) * | 1999-08-30 | 2007-05-16 | 株式会社豊田自動織機 | 燃料電池用水素供給システム、燃料リサイクル方法、液体運搬用移動体、給油設備及び燃料リサイクルシステム |
-
2002
- 2002-10-29 WO PCT/US2002/034649 patent/WO2003037512A2/fr not_active Application Discontinuation
- 2002-10-29 TW TW093111788A patent/TWI253202B/zh not_active IP Right Cessation
- 2002-10-29 EP EP02784325A patent/EP1565958A2/fr not_active Withdrawn
- 2002-10-29 AU AU2002348108A patent/AU2002348108A1/en not_active Abandoned
- 2002-10-29 CN CNA028260252A patent/CN1636251A/zh active Pending
- 2002-10-29 TW TW091132100A patent/TWI226720B/zh not_active IP Right Cessation
- 2002-10-29 JP JP2003539844A patent/JP2005512275A/ja active Pending
- 2002-10-29 KR KR10-2004-7006402A patent/KR20040060956A/ko not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101210841B1 (ko) * | 2011-04-12 | 2012-12-11 | 부산대학교 산학협력단 | 비폭기 유기물 제거장치 |
Also Published As
Publication number | Publication date |
---|---|
TWI226720B (en) | 2005-01-11 |
AU2002348108A1 (en) | 2003-05-12 |
CN1636251A (zh) | 2005-07-06 |
TW200301978A (en) | 2003-07-16 |
EP1565958A2 (fr) | 2005-08-24 |
TW200423462A (en) | 2004-11-01 |
AU2002348108A8 (en) | 2005-11-17 |
JP2005512275A (ja) | 2005-04-28 |
WO2003037512A3 (fr) | 2005-06-02 |
TWI253202B (en) | 2006-04-11 |
KR20040060956A (ko) | 2004-07-06 |
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