| Class / Patent application number | Description | Number of patent applications / Date published |
|---|
| 422630000 |
Discrete sequential reaction stages
| 43 |
| 422625000 |
Including reformer reactor
| 20 |
| 422608000 |
With separation or purification means (e.g., rectification, evaporation, ion exchanger, extraction, settler, absorption, recrystallization, etc.)
| 15 |
| 422650000 |
Including plural parallel reaction stages with each stage in the form of a reaction tube
| 11 |
| 422603000 |
Microscale reactor | 5 |
| 20110150727 | Micro-Reactor System Assembly - A micro-reactor system assembly comprises a stack of at least n process modules ( | 06-23-2011 |
| 20110300039 | Integrated Combustion Reactors And Methods Of Conducting Simultaneous Endothermic and Exothermic Reactions - Integrated Combustion Reactors (ICRs) and methods of making ICRs are described in which combustion chambers (or channels) are in direct thermal contact to reaction chambers for an endothermic reaction. Particular reactor designs are also described. Processes of conducting reactions in integrated combustion reactors are described and results presented. Some of these processes are characterized by unexpected and superior results, and/or results that can not be achieved with any prior art devices. | 12-08-2011 |
| 20120045377 | Modular Reactor and System - In one aspect the invention relates to reactors and a reactor system that include multiple microstructures each having a first edge and a second edge and an entrance side ( | 02-23-2012 |
| 20130129584 | MICRO-CHANNEL REACTOR FOR PRODUCING SYNTHETIC NATURAL GAS - The present invention relates to a micro-channel reactor for producing synthetic natural gas, and more particularly, to a micro-channel reactor for producing synthetic natural gas containing methane gas from synthetic gas, including a porous nickel plate catalyst part. | 05-23-2013 |
| 20140322105 | Micro-Reactor System Assembly - A micro-reactor system assembly comprises a stack of at least n process modules ( | 10-30-2014 |
| 422601000 |
Including plural parallel reaction stages with each stage in the form of a plate | 5 |
| 20120039775 | CATALYST-COATED SUPPORT, METHOD FOR PRODUCING THE SAME, REACTOR COMPRISING THE SAME AND USE THEREOF - Supports having a catalytic coating comprising at least one porous and cavity-containing catalyst layer are described, cavities being irregular spaces having dimensions greater than 5 μm in at least two dimensions or having cross-sectional areas of at least 10 μm | 02-16-2012 |
| 20120177550 | CATALYTIC REACTOR - A catalytic reactor includes a pair of plates arranged in parallel at a predetermined interval so as to form a path in which fluid flows; a channel member bonded to the plates in the path to divide the path into channels; and a catalyst carrier inserted into each of the channels and extending along the each of the channels. At least one of the pair of plates serves as a first heat-transfer surface when contacting a temperature medium having a temperature zone different from a temperature zone in the path and exchanging heat with the temperature medium. Each of the channels has a cross section for which an aspect ratio (W/H) of a width to a height is equal to or less than 1, and the catalyst carrier includes a wave-shaped base having a single piece structure, and a catalyst formed on a surface of the base. | 07-12-2012 |
| 20130149218 | INSULATOR UNIT - An insulator unit for a multipurpose flow module, such as a plate reactor, comprising a plurality of thermally insulating layers arranged in a sandwich structure with a plurality of plates, to provide thermal insulation across the sandwich structure. | 06-13-2013 |
| 20140369902 | FLUIDIC MODULE PERMANENT STACK ASSEMBLIES AND METHODS - The present disclosure provides an assembled stack of fluidic modules comprising at least first and second fluidic modules assembled in a stacked configuration. The first fluidic module has first and second major planar surfaces and encloses a first fluidic passage extending therethrough from a first passage entrance to a first passage exit with the first passage exit located on the second major planar surface of the first fluidic module. The second fluidic module also has first and second major planar surfaces and encloses a second fluidic passage extending therethrough from a second passage entrance to a second passage exit, with the second passage entrance located on the first major planar surface of the second fluidic module. The second major planar surface of the first fluidic module and the first major planar surface of the second fluidic module are spaced apart and physically joined together by at least three separate glass or glass-ceramic pads fused therebetween, and the at least three pads include at least one pad having no through-hole and at least one pad having a through-hole, with the through-hole forming a sealed fluidic interconnection between the first fluidic passage and the second fluidic passage. A method of forming the assembled stack is also disclosed. | 12-18-2014 |
| 20160144336 | REACTOR - Provided is a reactor in which a catalyst to accelerate reaction of a reactant is allowed to act on a reaction fluid having the reactant. The reactor has a partition that defines, in a parallel form, a plurality of reaction flow passages through which the reaction fluid flows, and a plurality of catalyst structures, each having a catalyst and being respectively provided in each of the plurality of reaction flow passages. The partition has a communicating portion allowing the plurality of reaction flow passages to communicate mutually. | 05-26-2016 |
| 422606000 |
With multiphase mixing means | 5 |
| 20120100048 | HIGH PERFORMANCE CHIMNEY TRAY FOR A FIXED BED REACTOR - A chimney tray for a reactor, wherein a gas reactant and a liquid reactant are mixed in chimneys to improve the dispersion performance of the liquid reactant on the catalyst bed of a fixed bed reactor thereby increasing the contact efficiency between the liquid reactant and the catalyst depending on the uniformity of flow of the liquid reactant, resulting in increased reaction efficiency, and which includes a tray having a plurality of through-holes, and a plurality of chimneys perpendicularly inserted into the through-holes of the tray and having one or more outlets penetrating there through and facing each other, wherein each of the plurality of chimneys includes a conical lower end which is formed such that it extends from the lower surface of the tray to make an angle of 10˜40° with respect to the direction of the normal line of the tray. | 04-26-2012 |
| 20130243671 | HIGH SHEAR HYDROGENATION OF WAX AND OIL MIXTURES - A system for producing enhanced wax alternatives, including a high shear device comprising a rotor and a stator, and configured to process petroleum wax and base oil with a hydrogen-containing gas under shearing conditions to form a feedstock, wherein at least one of the rotor and the stator comprises a toothed surface; and a reactor comprising a reactor inlet and a reactor outlet, and configured for hydrogenation of the feedstock for a time sufficient to produce enhanced hydrogenated products, wherein the high shear device is in fluid communication with the reactor, whereby the feedstock is transferable therebetween. | 09-19-2013 |
| 20140271413 | Reactor Vessel for Complexecelle Formation - A reactor vessel for complexecelle formation is described. The reactor vessel has a vessel for containing a first reactant wherein the vessel comprises an open top. A lid is provided for attachment to the vessel which is adapted for sealing the open top. An impeller shaft extends through the lid and into the vessel wherein the impeller comprises at least one stirrer blade extending from the impeller shaft and the impeller shaft is adapted to rotate in the first reactant. A gas diffuser extends into the first reactant. A gas source is provided which is capable of providing gas to the gas diffuser for dispersing the gas into the first reactant. The rotating impeller shaft and gas source are capable of simultaneously acting to form bubble surfaces of the first reactant. A metering device is provided for introducing a second reactant to the vessel onto the bubble surfaces. | 09-18-2014 |
| 20150071834 | INTER-BED MIXING IN FIXED BED REACTORS - A stator-type mixing device is used as a mixing device between fixed catalyst beds in a reactor. The mixing device includes a plurality of blades or surfaces arranged around a central hub. The blades are arranged at an angle relative to vertical so that a fluid cannot pass vertically through the mixing device without contacting at least one blade or surface. The blades or surfaces allow the stator-type mixing device to span the full cross-sectional surface area of the reactor, so that concentration of liquids in a localized portion of the reactor cross-sectional area is reduced or minimized. For reactors where at least part of the process fluid is a liquid under reaction conditions, a distributor tray can be included below the stator-type mixing device. | 03-12-2015 |
| 20160167007 | INTER-BED MIXING IN FIXED BED REACTORS | 06-16-2016 |
| 422607000 |
With distributor or collection tray | 5 |
| 20110081282 | Flow distribution device for downflow catalytic reactors - The invention is a fluid distribution device for coupling with a fluid distribution conduit or chimney for improving the distribution of downwardly flowing poly-phase mixture including at least one gas phase and at least one liquid phase, above at least one catalyst bed of granular solid catalytic material. The fluid distribution device for receiving the liquid and gas phases has one or more openings in the top and/or upper portion of its height through which a gas phase can enter and has a gas conduit that opens to a mixing cavity within the device. The fluid distribution device further comprises one or more lateral openings for liquid ingress. The lateral opening or openings allow the liquid to enter a liquid conduit that opens to the internal mixing cavity. The mixing cavity allows intimate contact between the liquid and gas phases. Therefore the flow distribution device of the invention provides improved tolerance for tray out of levelness. | 04-07-2011 |
| 20120014849 | MULTIPHASE CONTACT AND DISTRIBUTION APPARATUS FOR HYDROPROCESSING - Systems and apparatus for mixing, cooling, and distributing multiphase fluid mixtures within a reactor, wherein reactor internal apparatus of the present invention provides not only improved fluid mixing and distribution to each underlying catalyst bed surface, but also offers other advantages including: decreased mixing tray height; easier maintenance, assembly and disassembly; and decreased amounts of fabrication material. In an embodiment, fluid may be evenly distributed to a catalyst bed from a fluid distribution unit comprising a nozzle tray including a plurality of nozzles, wherein the nozzles include at least one liquid inlet disposed tangentially to an inner surface of the nozzle. | 01-19-2012 |
| 20130259774 | COLUMN CONTACT APPARATUS AND METHOD FOR OPERATING THE SAME - The invention is a column contact apparatus for contacting gas with liquid in an upflow in a column container, containing two or more stages of honeycomb structural bodies in the column container in a vertical direction, a space portion formed between the respective stages of the honeycomb structural bodies and a flow-aligning portion as back-flow prevention means provided in the space portion between the respective stages such that the flow-aligning portion is not brought into contact with the honeycomb structural bodies, the flow-aligning portion including a plurality of holes with hole diameters of 0.5 mm to 8 mm. | 10-03-2013 |
| 20140154154 | APPARATUS AND METHODS FOR PRODUCING CHLORINE DIOXIDE - Chlorine dioxide (ClO | 06-05-2014 |
| 20140271414 | GAS DISTRIBUTOR NOZZLES - Systems and methods for injecting gas into a fluidized bed of particles are provided. The system can include a gas distribution system. The gas distribution system can include a header having a flow passage and a nozzle body coupled to the header. The nozzle body can have an inlet end in fluid communication with the flow passage and an outlet end positioned outside of the header. The nozzle body can have a longitudinal axis that is substantially perpendicular to a direction of flow through the flow passage. The nozzle body can have an orifice positioned between the inlet end and the outlet end. | 09-18-2014 |
| 422619000 |
Combined with contact material regenerating means (e.g., regenerating catalyst, etc.) | 2 |
| 20130142712 | AIR POLLUTION CONTROL SYSTEM AND METHOD | 06-06-2013 |
| 20130251608 | Reactor Components - The present disclosure relates to insulation components and their use, e.g., in regenerative reactors. Specifically, a process and apparatus for managing temperatures from oxidation and pyrolysis reactions in a reactor, e.g., a thermally regeneratating reactor, such as a regenerative, reverse-flow reactor is described in relation to the various reactor components. | 09-26-2013 |
| 422602000 |
Plate-type laminated reactor | 2 |
| 20120189511 | Micro-Reactor System Assembly - A micro-reactor system assembly comprises a stack of at least n process modules ( | 07-26-2012 |
| 20140301917 | APPARATUS FOR A HYDROCARBON REFORMING USING A MICRO-CHANNEL HEATER - The present invention relates to an apparatus for reforming a hydrocarbon using a micro-channel heater, which can utilize the combustion heat of a fuel as an energy source needed for reforming a hydrocarbon. A plurality of thin metal plates having micro-channels may be laminated in a multilayered structure so as to manufacture a small to medium compact hydrogen-producing apparatus. In particular, a reforming unit may be designed to have a multilayered structure so as to improve the capacity of a reformer up to a level desired by a user. | 10-09-2014 |
| 422624000 |
Including a mechanical means for transportation of material (e.g., conveyor, turntable, truck, etc.) | 1 |
| 20110116995 | APPARATUS AND METHOD FOR PRODUCING ALIGNED CARBON-NANOTUBE AGGREGATES - An apparatus of the present invention for producing an aligned carbon-nanotube aggregate is an apparatus for producing an aligned carbon-nanotube aggregate by synthesizing the aligned carbon-nanotube aggregate on a base material having a catalyst on a surface thereof, the apparatus including: a formation unit that processes a formation step of causing an environment surrounding the catalyst to be an environment of a reducing gas and heating at least either the catalyst or the reducing gas; a growth unit that processes a growth step of synthesizing the aligned carbon-nanotube aggregate by causing the environment surrounding the catalyst to be an environment of a raw material gas and by heating at least either the catalyst or the raw material gas; and a transfer unit that transfers the base material at least from the formation unit to the growth unit. Thus provided is a production apparatus and a production method that are capable of improving efficiency in the production of aligned CNT aggregates by preventing a decrease in production volume and deterioration in quality of aligned CNT aggregates in serial production and by making it easy to increase the size of the apparatus. | 05-19-2011 |
| 422623000 |
Including a boiler | 1 |
| 20110020197 | PORTABLE FUEL PROCESSOR - Described herein is a fuel processor that produces hydrogen from a fuel source. The fuel processor comprises a reformer and burner. The reformer includes a catalyst that facilitates the production of hydrogen from the fuel source. Voluminous reformer chamber designs are provided that increase the amount of catalyst that can be used in a reformer and increase hydrogen output for a given fuel processor size. The burner provides heat to the reformer. One or more burners may be configured to surround a reformer on multiple sides to increase thermal transfer to the reformer. Dewars are also described that increase thermal management of a fuel processor and increase burner efficiency. A dewar includes one or more dewar chambers that receive inlet air before a burner receives the air. The dewar is arranged such that air passing through the dewar chamber intercepts heat generated in the burner before the heat escapes the fuel processor. | 01-27-2011 |
| 422620000 |
Combined with recycling means (e.g., recycling products, reactants, etc.) | 1 |
| 20110229382 | SYSTEM FOR HEAT INTEGRATION WITH METHANATION SYSTEM - In an embodiment, a system includes a methanation section generally including a fuel inlet configured to receive a first fuel, a fuel outlet configured to output methane, and a first fuel path configured to route a first flow of the first fuel from the fuel inlet to the fuel outlet. The first fuel path includes a first methanator configured to generate the methane from the first fuel in an exothermic methanation region. The system also includes a second fuel path configured to route a second flow of a second fuel without conversion to methane. The second fuel path is also configured to receive heat from the exothermic methanation region. | 09-22-2011 |
| 422604000 |
With gas contact means for degassing or agitating (e.g., sparging, etc.) | 1 |
| 20130243670 | Apparatus and Methods for the Automated Synthesis of Small Molecules - Provided are methods for purifying N-methyliminodiacetic acid (MIDA) boronates from solution. Also provided are methods for deprotection of boronic acids from their MIDA ligands. The purification and deprotection methods can be used in conjunction with methods for coupling or otherwise reacting boronic acids. Iterative cycles of deprotection, coupling, and purification can be performed to synthesize chemical compounds of interest. The methods are suitable for use in an automated chemical synthesis process. Also provided is an automated small molecule synthesizer apparatus for performing automated synthesis of small molecules using iterative cycles of deprotection, coupling, and purification in accordance with methods of the invention. Coupling and other reactions embraced by the invention include, without limitation, Suzuki-Miyaura coupling, oxidation, Swern oxidation, “Jones reagents” oxidation, reduction, Evans' aldol reaction, HWE olefination, Takai olefination, alcohol silylation, desilylation, p-methoxybenzylation, iodination, Negishi cross-coupling, Heck coupling, Miyaura borylation, Stille coupling, and Sonogashira coupling. | 09-19-2013 |
| Entries |
| Document | Title | Date |
|---|
| 20100303690 | THERMAL CONTROL APPARATUS FOR CHEMICAL AND BIOCHEMICAL REACTIONS - An apparatus ( | 12-02-2010 |
| 20100329952 | REACTION DEVICE, HEAT-INSULATING CONTAINER, FUEL CELL DEVICE, AND ELECTRONIC APPARATUS - Disclosed is a reaction device that includes a reaction device main body that includes a first reaction unit and a second reaction unit, a container to house the reaction device main body and a first region that corresponds to at least the first reaction unit and a second region that corresponds to the second reaction unit, the first and second regions being provided to the container or internal side of the container. The first reaction unit is set to a temperature higher than that of the second reaction unit, and the first region has a higher reflectivity than that of the second region, with respect to a heat ray that is radiated from the reaction device main body. | 12-30-2010 |
| 20110150725 | IN SITU HEAT INDUCED ANTIGEN RECOVERY AND STAINING APPARATUS AND METHOD - Contemplated herein is an automated microscope slide antigen recovery and staining apparatus and method that features a plurality of individually operable miniaturized pressurizable reaction compartments for individually and independently processing a plurality of individual microscope slides. The apparatus preferably features independently movable slide support elements each having an individually heatable heating plate. Each slide support element preferably supports a single microscope slide. Each microscope slide can be enclosed within an individual pressurizable reaction compartment. Pressures exceeding 1 atm or below 1 atm can be created and maintained in the reaction compartment prior to, during or after heating of the slide begins. Because of the ability to pressurize and regulate pressure within the reaction compartment, and to individually heat each slide, each slide and a liquid solution or reagent thereon can be heated to temperatures that could not be obtained without the enclosed pressurized environment of the reaction compartment. A reagent dispensing strip having a plurality of reconfigurable reagent modules may also be used. | 06-23-2011 |
| 20110150726 | AUTOTHERMIC CATALYTIC REACTOR WITH FLAT TEMPERATURE PROFILE FOR THE PRODUCTION OF HYDROGEN FROM LIGHT HYDROCARBONS - The present invention relates to the make of a heterogeneous gas-solid catalytic reactor operated in autothermic conditions, characterised by a flat temperature profile. This invention concurrently uses three actions to optimise the operation of the ATR reactor both in terms of energy and of catalytic activity: the adoption of a specifically formulated catalyst so as to favour a “direct type” reaction mechanism, the use and the make of the catalyst on a structured support with a high porosity and tortuosity, and characterised by high thermal conductivity and the adoption of a radial flow geometry catalytic bed. | 06-23-2011 |
| 20110194997 | Catalytic Reactor - A compact catalytic reactor defines a multiplicity of first and second flow channels arranged alternately, for an endothermic reaction and for an exothermic reaction respectively, and each containing a removable fluid-permeable catalytic insert to catalyze the reaction. The flow channels have a straight portion extending from one end face of the reactor and a linking portion that communicates between the end of the straight portion and at least one side face of the reactor, wherein the straight portion and the linking portion are defined at least in part by fin structures. The fm structures of the linking portion may be perforated, so that there are perforations aligned with each straight portion, but at the end of the reactor each line of perforations is obstructed. Removal of the obstructions enables the catalytic inserts to be pushed out of the flow channels when they are spent. | 08-11-2011 |
| 20110212003 | REACTOR AND REACTOR SYSTEM FOR HIGH TEMPERATURE AND HIGH PRESSURE REACTIONS - A reactor and a reactor system for carrying out high temperature and high pressure reactions is disclosed herein. The reactor has an isolatable inner vessel for allowing for heat energy efficient cooling and heating of the reactor. The reactor comprises an outer reactor adapted for withstanding a reaction pressure and a reaction temperature, the outer reactor having a sealable reactor lid; an inner vessel within the outer reactor for containing a reaction solution and at least one reaction vessel, the inner vessel being open to the outer reactor such that the reaction pressure of the inner vessel and the outer reactor are substantially equalized and vapour in the inner vessel passes to the outer vessel, the inner vessel having a splatter shield for substantially preventing spillage of the reaction solution from the inner vessel into the outer reactor; a vapour injector in communication with the inner vessel for injecting vapour into the inner vessel for heating the reaction solution; an outlet in the outer vessel for exhausting vapour from the outer reactor and the inner vessel; and an outer reactor outlet for draining a liquid contained between the outer reactor and the inner vessel. | 09-01-2011 |
| 20110212004 | SYSTEM FOR MAKING RENEWABLE FUELS - Multiple catalytic processing stations couple with a system which produces volatile gas streams from biomass decomposition at discrete increasing temperatures. These catalytic processing stations can be programmed to maximize conversion of biomass to useful renewable fuel components based on input feedstock and desired outputs. | 09-01-2011 |
| 20110236279 | INTEGRATED REACTORS, METHODS OF MAKING SAME, AND METHODS OF CONDUCTING SIMULTANEOUS EXOTHERMIC AND ENDOTHERMIC REACTIONS - Integrated Combustion Reactors (ICRs) and methods of making ICRs are described in which combustion chambers (or channels) are in direct thermal contact to reaction chambers for an endothermic reaction. Superior results were achieved for combustion chambers which contained a gap for free flow through the chamber. Particular reactor designs are also described. Processes of conducting reactions in integrated combustion reactors are described and results presented. Some of these processes are characterized by unexpected and superior results. | 09-29-2011 |
| 20110274596 | MICRO-MACRO CHANNEL REACTOR - Disclosed is a micro-macro channel reactor comprising: a top end plate and a bottom end plate assembled on the outskirts of the micro-macro channel reactor; a heat exchanging plate by which a heat exchanging material passes through passages thereof so that heat is transferred between the heat exchanging material and such a fluid as a reactant, a product, or a mixture thereof that passes through a catalyst plate; a catalyst plate stacked and assembled together with the heat exchanging plate and including a catalyst section containing a reaction catalyst necessary to perform a catalytic reaction of the reactant while the reactant is passing through the catalyst section; and a support plate stacked and assembled together with the catalyst plate and configured to provide passages that allows the reactant to pass through the catalyst section of the catalyst plate. | 11-10-2011 |
| 20120039774 | SAMPLE SOLUTION INTRODUCTION KIT AND SAMPLE SOLUTION INJECTOR - A sample solution introduction kit and a sample solution injector capable of introducing sample solution while reducing the rate of occurrence of an air bubble and having a simplified structure are proposed. | 02-16-2012 |
| 20120045376 | METHOD OF MANUFACTURING A REACTOR AND SET OF REACTORS - A method of manufacturing a target reactor having a flow-channel system in which a plurality of reactants continuously flowing into said target reactor are mixed and interconvert to form a target volumetric flow-rate (f | 02-23-2012 |
| 20120093701 | APPARATUS FOR BIOMASS TORREFACTION, MANUFACTURING A STORABLE FUEL FROM BIOMASS AND PRODUCING OFFSETS FOR THE COMBUSTION PRODUCTS OF FOSSIL FUELS - Apparatus for biomass torrefaction which includes a serpentine elongated housing, the housing having three generally U-shaped axial portions having first and second axial extremities and an intermediate section, the first and second axial extremities are disposed in normal use at a higher elevation than the first and second axial extremities, the intermediate section being configured for holding a liquid. Other forms of the invention include the method for biomass torrefaction which includes providing a quantity of biomass, providing a liquid heat transfer fluid, providing at least a first housing for holding the heat transfer liquid, elevating the temperature of the liquid heat transfer liquid, heat treating the biomass by passing it through the heat transfer liquid in the first housing at a temperature and duration sufficient to accomplish torrefaction of the wood. In some forms of the method, the process further includes the step of pelletizing the biomass prior to performing the treating step. | 04-19-2012 |
| 20120275974 | High Temperature Platformer - An apparatus for reforming a hydrocarbon stream is presented. The apparatus involves changing the design of reformers and associated equipment to allow for increasing the processing temperatures in the reformers and heaters. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking. | 11-01-2012 |
| 20120328491 | COMPOSITIONS, DEVICES AND METHODS FOR HYDROGEN GENERATION - Methods and systems for hydrogen generation from solid hydrogen storage compositions which generate hydrogen in an exothermic reaction wherein the heat released can be absorbed by solid endothermic compositions are disclosed. The solid hydrogen storage compositions comprise mixtures of chemical hydrides and water surrogate compounds. Fuel cartridges suitable for use with compositions which generate hydrogen upon the application of thermal initiation and methods for operating the fuel cartridges are also disclosed. | 12-27-2012 |
| 20130064740 | VORTEX-TYPE MIXING DEVICE FOR A DOWN-FLOW HYDROPROCESSING REACTOR - The present invention is directed to a vortex-type mixing device for a down-flow hydroprocessing reactor. In particular, the device improves the effectiveness of an existing mixing volume in mixing the gas phase and liquid phase of two-phase systems. According to the present invention, the mixing device helps create a highly arcuate flow to incoming effluents and a high degree of mixing within a constrained interbed space of a hydroprocessing reactor. | 03-14-2013 |
| 20130302222 | Synthetic Gas Generator - The invention relates to an apparatus for generating synthetic gas, comprising a POX reactor with a first reaction chamber, into which a carbon-containing gaseous feedstock, as well as an oxidizing agent, can be introduced via a feeding system, and a discharge system, whereby a gasification product can be withdrawn from the reaction chamber. The apparatus further contains at least one further, i.e., a second, reaction chamber with a second feeding system, which is connected to the first reaction chamber via the discharge system. | 11-14-2013 |
| 20140044612 | After-Treatment System - An after-treatment system includes a Selective Catalytic Reduction (SCR) catalyst or a similar aftertreatment unit or brick that may be inserted into the opened end of a sleeve. The aftertreatment brick includes a substrate matrix with catalytic material that extends between a first face and a second face. A mantle is disposed around the substrate matrix and extends between a first rim proximate the first face and a second rim proximate the second face. The mantel may include a overhang extension that extends the first rim of the mantle beyond the first face of the substrate matrix. To enable retrieval of the SCR catalyst from the sleeve, a retrieval feature is disposed on a readily accessible, inner surface of the overhang extension. | 02-13-2014 |
| 20140086809 | DUAL VESSEL REACTOR - A dual vessel reactor and a method of carrying out a reaction using a dual vessel reactor are provided using a non-condensable gas to substantially isolate the inner vessel from the outer vessel during the reaction and limit the heating of the outer vessel when steam from the inner vessel condenses on the interior surface of the outer vessel. By limiting the heating of the outer vessel through the condensation of the steam or other vapour from the inner vessel, the operating temperature of the outer vessel is kept below an upper threshold of the operating temperature of a seal used to seal the door in the outer vessel. | 03-27-2014 |
| 20140147350 | Cleaner for Reactor Component Cleaning - A reactor assembly includes a first block having an array of reactors defined therein and a second block having an array of openings defined within a surface of the second block. Each opening of he array of openings is substantially aligned with a corresponding opening of the array of reactors so that that each reactor is associated with at least one corresponding opening defined within the surface of the second block when the surface of the second block is placed on a surface of the first block. The first block is removably sealed against each surface defining the array of openings. A network of channels is defined within the second block. The network of channels is in fluid communication with a fluid source. | 05-29-2014 |
| 20150104360 | Combinatorial Flow System and Method - A reactor assembly having a plurality of reaction chambers defined therein is provided. The reactor assembly includes a fluid flow module that provides a pressurized control flow of fluid from an open container. In another embodiment, the reactor block includes a plurality of passageways defined over a surface of a substrate to accommodate the combinatorial processing in order to obtain multiple data points from a single substrate. | 04-16-2015 |
| 20160129418 | HYDRATION APPARATUS AND METHOD - Vessels including an enclosure having an outer perimeter and an interior space, a channel disposed in the interior space, a first port disposed on a surface of the first enclosure at or proximate to a first end of the channel, and a second port disposed on a surface of the first enclosure at or proximate to a second end of the channel, where the channel has a length greater than the shortest distance between the first port and the second port, and where the first port and the second port are in fluid communication with one another. In some cases, the length of the channel is greater than a length of the outer perimeter. Optionally, the vessel may have a second enclosure having an outer perimeter and an interior space with a second channel disposed in the interior space, a third port disposed on a surface of the second enclosure at or proximate to a first end of the second channel, and a fourth port disposed on a surface of the second enclosure at or proximate to a second end of the second channel, where the second port, the third port and fourth port are in fluid communication. In yet some other optional variations, the vessel further includes a plurality of enclosures each having an outer perimeter and an interior space, a channel disposed in the interior space, a port disposed on a surface of the enclosure at or proximate to a first end of the channel, and a port disposed on a surface of the enclosure at or proximate to a second end of the channel, where the channel has a length greater than a shortest distance between the ports, and the second port and the ports disposed on the surface of the plurality of enclosures are in fluid communication. The perimeter shape of the enclosure(s) may be any suitable shape, including, but not limited to, substantially circular, ovate or rectangular. | 05-12-2016 |
| 20160194203 | DEVICE FOR CREATING OXYGEN | 07-07-2016 |
