20 Hope Ave Suite 208, Waltham, MA 02453 (978)4531300 (Phone)
Certifications:
Allergy & Immunology, 1979 Pediatrics, 1973
Languages:
English Chinese Japanese
Hospitals:
20 Hope Ave Suite 208, Waltham, MA 02453
Newton - Wellesley Hospital 2014 Washington Street, Newton, MA 02462
Saints Medical Center 1 Hospital Drive, Lowell, MA 01852
Education:
Medical School National Taiwan University, College Of Medicine Graduated: 1962 Medical School Taiwan University Hospital Graduated: 1962 Medical School Chldns Hospital Med Center Graduated: 1971 Medical School Taiwan University Hospital Graduated: 1966 Medical School Chldns Hospital Med Center Graduated: 1966
Chi S. Wang - Woodridge IL 60517 J. Daniel Lyons - Wheaton IL
Assignee:
Chi S. Wang - Woodridge IL
International Classification:
H01M 804
US Classification:
429 17, 429 13, 429 22
Abstract:
An integrated process and system for producing electricity for stationary purposes or for electric-powered vehicle using any of multiple hydrocarbon input fuels, a fuel cell, and a thermoelectric reformer that allows quick response to transient loads. Optional high-temperature and low-temperature water-gas shift reactors are used to convert carbon monoxide to carbon dioxide in the reformate stream; a hydrogen separator is used to remove carbon dioxide, carbon monoxide, and trace hydrocarbons; and a condenser is used to remove moisture from the reformate stream. Hydrogen gas not consumed in the fuel cell is stored or recycled for subsequent input to the fuel cell. H O produced in the fuel cell is recycled for use in the reformer and water-gas shift reactors and is heated with waste heat from the fuel cell and carbon dioxide, carbon monoxide, and hydrocarbons from the hydrogen separator. A mixer is used to vaporize the input fuel prior to entering the thermoelectric reformer. Some of the electricity produced in the fuel cell is used for powering the thermoelectric reformer and is also stored for subsequent startup and peak load purposes.
Plasma Reformer For Hydrogen Production From Water And Fuel
A plasma reformer for the chemical reforming of gaseous mixtures of water and hydrocarbon fuels for producing hydrogen. The reformer contains a reaction chamber with outer lateral walls containing emitter electrodes and inner lateral walls containing collector electrodes. The emitter electrodes and collector electrodes form an electric circuit. There are a multiplicity of thin needle-like extrusions on the emitter electrode from which a profusion of high energy electrons are emitted. These high-energy electrons dissociate the hydrocarbon fuel through absorption and ionization emitting low energy electrons in the process. These low energy electrons cause dissociation of water. Thus, dissociation of hydrocarbon fuel acts to initiate dissociation of water. The molar ratio of water to hydrocarbon fuel in the input mixture for reactions, and therefor the production of hydrogen from water, increases with carbon number of the hydrocarbon fuel.
A process for producing hydrogen for direct use as a fuel or for input to a fuel cell from dissociating HO in a plasma reformer with hydrocarbon fuel acting as an initiator. The molar ratio of water to hydrocarbon fuel in the input mixture for reactions, and therefore the production of hydrogen from water, increases with the carbon number of the hydrocarbon fuel. Steps in the process include: mixing and vaporizing an HO and hydrocarbon fuel mixture in an atomization/evaporation chamber, further heating the mixture in a rotating-flow buffer chamber, dissociating HO and hydrocarbon fuel in a plasma reformer, converting carbon monoxide and HO to hydrogen and carbon dioxide in a water shift reactor and optionally conditioning the reformate stream by removing carbon dioxide and by purifying hydrogen.
Thermoelectric Reformer Unit For Hydrogen Production
A thermoelectric reformer unit-for dissociating fossil-based hydrocarbons, renewable hydrocarbons or hydrogen-containing inorganic compounds to produce hydrogen in a reactor using thermoelectric technology with thermoelectric materials to achieve very high conversion efficiencies. Thermoelectric reforming occurs in a reactor core containing a number of energy sources. These energy sources generate extremely high temperature heat that reacts with the fuels in its local surrounding areas. Since the heat is locally generated, it will not penetrate far within the reactor core that is surrounded by walls that act as a casing for the reformer. Synthetic gas produced in the reformer can be fed into internal combustion engines certain, types of fuel cells, or other energy conversion equipment without or with only limited levels of purification. Ancillary components are needed to produce high-purity hydrogen fuel for other types of fuel cells.
A hydraulic brake lever assembly includes a hollow lever mount accommodating therein a hydraulic pump. Two window openings are respectively formed in opposite sides of a middle section of the lever mount and in communication with an interior space of the lever mount. The hydraulic pump includes an outer cylinder member and an inner bore member arranged inside the outer cylinder member to define a hydraulic fluid chamber therebetween. An in-flow passage is defined in a wall of the inner bore member to communicate a bore defined in the inner bore member. A spring-biased piston is movably received in the bore of the inner bore member. The piston is driven by a driving bar coupled to a handgrip. The outer cylinder member forms in a wall thereof a hole receiving and in threading engagement with a transparent plug that is exposed through each of the window openings.
Energy Self-Sustainable Reactor For Gasifying Engine Particulates And Unburned Hydrocarbons
A reactor that can be attached to the exhaust manifold of an internal combustion engine to oxidize and burn carbon soot particles, carbon monoxide, and unburned hydrocarbons, and to dissociate nitrogen and sulfur oxides. The reactor has a reaction zone that contains porous heat-retaining foam cells and that is bounded by a porous heat-retaining zone, which in turn is surrounded by ceramic insulation materials to minimize energy losses. Engine exhaust at elevated temperatures and containing some oxygen (air) enters the reaction chamber. By means of impinging heat transfer, thermal radiation enhancement, energy trapping and combustion of engine emissions, temperatures sufficient to oxidize carbon soot particles, carbon monoxide, and unburned hydrocarbons are attained. Steam or atomized water droplets are introduced to improve the efficiency of the reactor through gasification, regasification, water shift reactions, methanation, and hydrocracking reactions. Harmless product of the oxidation reactions, H. sub.
Photocatalytic Reactor For Metal Recovery From Industrial Waste Streams
A photocatalytic reactor to recover precious metals, useful metals, and toxic metals from industrial waste streams using visible or ultraviolet light and semiconductor material as the photocatalyst. Seeds of metal in the same metal group as the metals being recovered are implanted in the reactor to create nucleation sites for the deposition, agglomeration, and growth of the metals being recovered. The reactor may have internally reflective surfaces to effectively multiply the light sources. The input waste stream may be mixed with reaction acceptor materials that reduce electron-hole recombination and that increase reaction rates.
Process For Hydrogen Production From Hydrogen Sulfide Dissociation
A process using high-temperature thermal dissociation to recover hydrogen and salable sulfur from industrial waste streams containing hydrogen sulfide (H. sub. 2 S) is disclosed. Thermal dissociation occurs in a thermoelectric reactor at temperatures up to 1900. degree. C. Waste energy from the high-temperature reactor is recovered and used to preheat the H. sub. 2 S-laden stream before entering the high-temperature reactor. Sulfur is separated out in a condenser. The process also includes a scrubber to eliminate the carryover of liquid sulfur mists or aerosols, and a membrane to separate the hydrogen from the dissociated product stream. Trace amounts of unconverted H. sub. 2 S are recycled through the process for further dissociation.
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