Patents
Sitemap › B01 - Physical or chemical processes or apparatus in general › B01J - Chemical or physical processes, e.g. catalysis, colloid chemistry; Their relevant apparatus › B01J 8 - Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
Patents for B01J 8 - Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes (34,406)
06/2010
06/08/2010US7731923 Method for simultaneously producing hydrogen and carbon monoxide
06/08/2010US7731918 Microreactor for generating hydrogen gas by decomposing or reforming a hydrocarbon fuel; plurality of spaced apart catalyst coated strips within at least one of the reaction chamber and combustion chamber with inlet and outlet ports
06/08/2010US7731917 Heat exchange reactor
06/08/2010US7731916 Method of charging catalyst tubes of a bundle of catalyst tubes in a structured fashion
06/08/2010CA2506760C Distillation system
06/03/2010WO2010061920A1 Regeneration tower for apparatus for dry discharge-gas treatment
06/03/2010WO2010061690A1 Reaction method using heat-exchange type reactor, and method for charging fillers in plate reactor
06/03/2010WO2010024935A3 Methods and devices for fluid handling
06/03/2010US20100137653 Process and apparatus for recovery of dichlorohydrins via codistillation
06/03/2010US20100137459 Multi-zone reforming methods and apparatus for conversion of devolatilized biomass to syngas
06/03/2010US20100135891 Process for production of pcc
06/03/2010US20100135872 Reformer module
06/03/2010US20100135871 Isothermal Reactor
06/03/2010US20100133473 Simultaneous Warm Gas Desulfurization and Complete CO-Shift for Improved Syngas Cleanup
06/03/2010US20100132633 Biomass gasification reactor
06/02/2010EP2191889A1 Catalyst loading system
06/02/2010EP2190568A2 Continuous-flow dual-bed reactor for production of liquid-phase hydrocarbon mixture on fischer-tropsch catalysis using synthetic gas
06/02/2010CN201493101U Heating device of melamine fluidized bed reactor
06/02/2010CN201493100U hydrogenation reactor
06/02/2010CN201493099U Cooling hydrogen spraying pan
06/02/2010CN201493098U Multi-directional side-stream radial fixed bed reactor
06/02/2010CN201493097U Spiral grooved gas-liquid distributor
06/02/2010CN201493096U Collector for outlet
06/02/2010CN201493095U Catalyst support disc
06/02/2010CN201493094U Central tube of reformation and isomerization reactor
06/02/2010CN201493093U Gas-liquid partition tray
06/02/2010CN201493092U Inlet diffuser
06/02/2010CN1642630B Reaction apparatus and reaction method applying the device
06/02/2010CN101716481A Hypergravity fluidization vapor deposition reaction device
06/02/2010CN101318654B Method for preparing high purity polysilicon particle with fluidized bed and bed fluidizing reactor
06/02/2010CN101312779B Hydrogen generator and fuel cell using same
06/02/2010CN101279227B Membrane type wall reactor
06/02/2010CN101229498B Reactor with framework fortified aperture plate
06/01/2010US7727931 Catalysts, activating agents, support media, and related methodologies useful for making catalyst systems especially when the catalyst is deposited onto the support media using physical vapor deposition
06/01/2010US7727509 Reducing interaction between carbon monoxide and shell side of reactor; extending lifetime, minimizing maintenance; adding protective element or compound to stream
06/01/2010US7727495 for catalytic reactor of turbine combustor, conduit comprising tube including an inlet and an outlet, tube contains a variation in its cross sectional area along at least a portion of its length to change a property of a fluid flowing adjacent wall of tube; oxidation catalyst is deposited on tube
06/01/2010US7727493 plate-shaped heat exchanger for a heat exchange unit of a chemical reactor in which thermal insulation is obtained in an unusually simple and reliable manner; uses ellipse-shaped cross-section tubes
06/01/2010US7727491 Pseudo-isothermal chemical reactor for heterogeneous chemical reactions
06/01/2010US7727490 flexibility in manufacturing; increasing the production of para-xylene, benzene, toluene, or an aromatic gasoline blend depending on market conditions; contains naphtha hydrotreating zone, reforming zone, extraction zone, para-xylene-separation zone, transalkylation zone, first and second fractionation
06/01/2010US7727485 compact reactor for making calcium nitrate spherical in a fluidized bed granulator, spherical in shape, hard and dry and do not break down easily during handling
06/01/2010US7727484 Fluid bed apparatus module and method of changing a first module for a second module in a fluid bed apparatus
06/01/2010US7727482 Method for carrying out chemical reactions in pseudo-isothermal conditions
06/01/2010US7727311 Installation and method for mixing and distributing a liquid phase and a gaseous phase
05/2010
05/27/2010WO2010058408A1 A process and an apparatus for converting solid organic materials into carbon or activated carbon
05/27/2010WO2010058257A1 Catalyst loading system
05/27/2010WO2010058164A1 Slurry bubble column reactor
05/27/2010WO2010057919A1 Device for generating combustible product gas from carbonaceous feedstocks
05/27/2010WO2010057915A1 Method for improving flowability of heterophasic polypropylene powder
05/27/2010WO2010037653A9 Apparatus and process for gas phase fluidised bed polymerisation reaction
05/27/2010WO2010022232A3 Chemical reactors
05/27/2010US20100130776 Process and reactor for the thermoneutral conversion of ethanol to acetic acid
05/27/2010US20100130648 Process for preparation of methyl methacrylate by esterification during oxidation
05/27/2010US20100129284 Method and apparatus for producing hydrogen and recovering carbon dioxide
05/27/2010US20100129283 Chemical Reactor
05/27/2010US20100129276 Gas mixing device and synthesis gas producing device
05/27/2010US20100129270 Catalyst Housing
05/27/2010US20100126908 Novel steam reforming furnace using porous burners
05/27/2010US20100126590 Particulate flow control process
05/27/2010US20100126060 Improvement involves concentrating the spent water stream to provide an aqueous fraction and a glycerin-containing fraction; low water emissions can prevent expensive sewage treatment equipment
05/27/2010CA2743960A1 A process and an apparatus for converting solid organic materials into carbon or activated carbon
05/27/2010CA2743563A1 Catalyst loading system
05/27/2010CA2743075A1 Device for generating combustible product gas from carbonaceous feedstocks
05/26/2010EP2189478A1 Process for producing water-absorbing resin
05/26/2010EP2188316A1 Chemical process optimization method that considers chemical process plant safety
05/26/2010EP1284815B1 An apparatus for the controlled optimized addition of reactants in continuous flow reaction systems and methods of using the same
05/26/2010CN201482478U Photocatalytic reaction apparatus using ultrasonic waves to prevent and remove scale
05/26/2010CN201482468U Distribution plate of fluidized bed reactor in ammoxidation
05/26/2010CN201482467U Fluidized bed distributing plate for producing chlorothalonil
05/26/2010CN201482466U Tube array fluidized bed reactor in chlorothalonil production
05/26/2010CN201482465U Device for removing impurities from mixed gas
05/26/2010CN201482464U Reforming catalyst stripper
05/26/2010CN1946928B Fuel reformer
05/26/2010CN1898361B Method of converting oxygen-containing compound to olefin product
05/26/2010CN1524623B External separator and cyclone separator for fluidic catalytic cracking process
05/26/2010CN101712412A Catalyst unloading device
05/26/2010CN101711965A Systems and methods for continuous multiphase reaction and separation
05/26/2010CN101711964A Multi-catalyst injection system
05/26/2010CN101711963A transmission mechanism of dense-phase loader
05/26/2010CN101711962A Catalytic conversion stripper
05/26/2010CN101314120B Slurry bed reactor and uses thereof
05/26/2010CN101304803B Isothermal chemical reactor
05/25/2010US7723259 capable of continuously oxidizing or combusting particulate matter from a relatively low temperature during a diesel engine operation; includes cerium, praseodymium, gallium, other oxides
05/25/2010US7723258 fabricating substance for catalytic combustion by providing salt precursor of a noble metal, providing a h-boron nitride as an inorganic combustion promoter, mixing salt precursor of noble metal and h-boron nitride with solvent to to form paste, dispersing paste on support, calcining
05/25/2010US7722844 improves reliability of an exhaust gas circulating ammonia injection unit, also allows reducing the problem of nozzle clogging even with a sulfur oxide-containing exhaust gas, and reduces production of dioxins in terms of a treatment of an exhaust gas from a municipal incinerator
05/25/2010US7722834 Recombiner system
05/25/2010US7722832 Separation method and assembly for process streams in component separation units
05/25/2010US7722831 an energy balanced reaction cycle converts gasoline, a liquid mixture of hydrocarbons and water into hydrogen enriched synthesis gas fuel for powering fuel cells
05/25/2010US7722690 Methods for producing synthesis gas
05/25/2010US7722689 Device for supplying fuel to a burner in a fuel cell system comprising a reformer
05/25/2010CA2557218C Bromine addition for the improved removal of mercury from flue gas
05/25/2010CA2557159C Dynamic halogenation of sorbents for the removal of mercury from flue gases
05/25/2010CA2548194C Process for the removal of heavy metals from gases, and compositions therefor and therewith
05/25/2010CA2438589C Method for manufacturing a hydrogen and nitrogen containing gas mixture
05/25/2010CA2362839C Method and apparatus for gas phase polymerisation of alpha-olefins
05/20/2010WO2010056461A2 Vertical shaft reactor systems
05/20/2010WO2010055618A1 Fluidized bed device
05/20/2010WO2010054464A1 Process for upgrading heavy oil and bitumen products
05/20/2010WO2010022830A3 Catalyst for the catalytic gas phase oxidation of aromatic hydrocarbons to form aldehydes, carboxylic acids and/or carboxylic acid anhydrides, in particular phthalic acid anhydride, and method for producing said type of catalyst
05/20/2010US20100125157 High shear process for producing micronized waxes
05/20/2010US20100125145 Quantity of the alcohol to be purified can be greatly reduced to significantly decrease the energy consumption and hence cost of biodiesel production
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