Abstract: The present invention relates to a method for screening of polycondensation catalysts, wherein at least two polycondensation catalysis reactions are performed simultaneously under substantially equivalent conditions in at least two reaction cells which are present in one and the same room, using a sample comprising material to be polycondensated and a catalyst to be screened, and wherein the performances of the catalysts are analyzed. The present invention further relates to an apparatus suitable for performing the method.

Abstract: A microreactor includes a plurality of interconnected microstructures arranged in m process units with the process units configured to be operable together in parallel. Each of the m process units has a number n of respective process fluid inlets, wherein a number y of the n respective process fluid inlets are connected individually to respective non-manifolded fluid pumps, and wherein a number n minus y of the n respective process fluid inlets are connected to a respective manifolded fluid pump via a manifold, wherein y is an integer from 1 to n-1 inclusive.

Abstract: Synthesis of arrays of chain molecules, such as oligonucleotides, in large quantities can be carried out utilizing projection onto an active substrate of a magnified image of a light emitting object array having selectable regions of light and dark areas forming a pattern. Projection optics formed entirely of mirrors are used to receive the light emitted from the object array and image the pattern of the array onto the active surface of the substrate. The mirrors in the projection optics include a first, concave mirror, a second, convex mirror, a third, concave mirror, and a fourth, convex mirror, each receiving the beam of light in turn, with the light reflected from the fourth mirror being imaged onto the active surface of the substrate with an image area greater than that of the original light emitting array.

Abstract: The invention relates to an original experimental device for the study and the validation of processes in a reactive simulated moving bed, as well as the method that makes possible the exploitation of the results obtained from said device. This device consists of one or two columns and a number of storage tanks.

Abstract: Catalysts are described in which an active catalyst is disposed on a low surface area, oxide support. Methods of forming catalysts are described in which a Cr-containing metal is oxidized to form a chromium oxide layer and an active catalyst is applied directly on the chromium oxide layer. Methods of making new catalysts are described in which the surface is sonicated prior to depositing the catalyst. Catalyst systems and methods of oxidation are also described. The inventive systems, catalysts and methods are, in some instances, characterized by surprisingly superior results.

Abstract: The present invention relates to a method of manufacturing a micro reactor device that includes a tubular reactor (1) as a flow path, for allowing reaction species to react in the reactor (1). The micro reactor device is manufactured by forming a particle layer (2) on an inner wall of the reactor (1). The particle layer (2) can be formed by causing a dispersion liquid of particles to flow through the reactor (1) and drying. In this way, it is possible to provide a method of manufacturing a micro reactor device having an inner wall modified so that the reaction species can react more efficiently, and to provide the micro reactor device.

Abstract: In one embodiment, a parallel batch reactor generally includes a plurality of reactor vessels and a plurality of valves configured to allow flow into the reactor vessels when a gas is supplied to the reactor at a pressure higher than a pressure within the reactor vessels and restrict flow from the reactor vessels. A method includes inserting chemical components into the reactor vessels, supplying a first gas to the reactor vessels to pressurize the reactor vessels, stopping supply of the first gas, and supplying a second gas to the reactor at a lower pressure than a pressure within the reactor vessels. The second gas passes through the valves and into the reactor vessels when the pressure within the reactor vessels drops below the pressure of the second gas.

Abstract: A method and apparatus for improving air quality within an enclosed space. The apparatus provides at least three molecular sieves that contain zeolite material to treat the air to remove toxins such as suspended particles, carbon dioxide, carbon monoxide, nitrogen dioxide, bacteria, formaldehyde, total volatile organic compounds, radon, ozone, toxic mould and organic odor-causing compounds. The apparatus uses the sieves such that one of the sieves is locked and retaining air, substantially immobile within, for a period of not less than 2 seconds to allow the zeolite material to breakdown the compounds and release the individual natural elements.

Abstract: A fine channel device including a fine channel provided with at least two inlet ports for feeding fluid, inlet channels communicated with the inlet ports, a confluent portion communicated with the inlet channels, a branch portion communicated with the fine channel, from which at least two outlet channels are branched to feed predetermined amounts of fluid, and outlet ports communicated with the outlet channels. The fine channel is provided with a plurality of partition walls arranged along a boundary formed by at least two kinds of fluid fed from the inlet ports so as not to cause mutual contamination of fluid. Furthermore, the plurality of partition walls are spaced apart at intervals in a flowing direction of fluid.

Abstract: In a multi-station reaction apparatus (1) comprising an annular heat transfer block (30) formed with a plurality of cavities (31) for receiving respective reaction vessels (36), the upper surface of the heat transfer block (30) has a central recess (32) around which the said plurality of cavities (31) are arrayed. The apparatus further comprises a removable cooling module (4), the central recess (32) of the heat transfer block (30) being shaped so as to accommodate the removable cooling module (4) and corresponding surfaces of the central recess (32) of the heat transfer block (30) and the cooling module (4) being shaped such that there is a stepped interface between them. The cooling module (4) comprises a metal block having channels therein through which coolant circulates when the cooling module (4) is in use.

Abstract: The invention relates to a process for the continuous free-radical homogeneous solution polymerization or melt polymerization of (meth)acrylate monomer mixtures.

Abstract: Localized catalyst activity in an SCR unit for controlling emissions from a boiler, power plant, or any facility that generates NOx-containing flue gases is monitored by one or more modules that operate on-line without disrupting the normal operation of the facility. Each module is positioned over a designated lateral area of one of the catalyst beds in the SCR unit, and supplies ammonia, urea, or other suitable reductant to the catalyst in the designated area at a rate that produces an excess of the reductant over NOx on a molar basis through the designated area. Sampling probes upstream and downstream of the designated area draw samples of the gas stream for NOx analysis, and the catalyst activity is determined from the difference in NOx levels between the two probes.

Abstract: The microreactor is formed by a sandwich including a first body, an intermediate sealing layer and a second body. A buried channel extends in the first body and communicates with the surface of the first body through a first and a second apertures. A first and a second reservoirs are formed in the second body and are at least partially aligned with the first and second apertures. The sealing layer separates the first aperture from the first reservoir and the second aperture from the second reservoir, thereby avoiding contamination of liquids contained in the buried channel from the outside and from any adjacent buried channels. The sealing layer is perforated during use of the device, but a resilient plug can be used to reseal the device.

Abstract: A sample block for use in the polymerase chain reaction, DNA sequencing, and other procedures that involve the performance of simultaneous reactions in multiple samples with temperature control by heating or cooling elements contacting the bottom surface of the block is improved by the inclusion of hollows in the block that are positioned to decrease the mass of the block in the immediate vicinity of the wells.

Abstract: A microstructure includes first and second plates. The first plate defines a recess. The second plate is bonded to the first plate to block an opening of the recess to thereby form a closed vacuum space or a closed space filled with inert gas.

Abstract: A reactor assembly for analysing the effluent stream from at least one flow-through reactor, The reactor includes a flow-through reactor for performing at least one chemical reaction. The flow-through reactor includes a reaction chamber including a reaction zone, the reaction chamber being connected to a reactor inlet for a reactant, upstream of the reaction zone and a reactor outlet for the effluent stream from the reaction zone, downstream of the reaction zone; and an analyser for subjecting the effluent stream to an analysing procedure, each reactor outlet being connected to an analyser by an effluent conduit. The reactor assembly further includes a dilution fluid supply member for adding a dilution fluid to the effluent stream, downstream of the reaction zone.

Abstract: Disclosed herein is a microreactor capable of reducing a pressure drop in an entire system. The microreactor includes a mixer 103 having a mixing channel for mixing two kinds of raw materials 101 and 102, and a reactor 109 having a reaction channel connected to the downstream side of the mixing channel to receive the mixture flowing out from the mixing channel and cause chemical reactions of the mixture inside the reaction channel. The reactor 109 a first reactor unit 107 having a large surface-to-volume (S-V) ratio of the reaction channel at an upstream side, and a second reactor unit 108 having a small S-V ratio of the reaction channel at a downstream.

Abstract: The invention describes a laboratory reactor for the kinetic study of catalytic reactions calling for a gaseous reaction phase and a liquid reaction phase, characterized by a capillary shape, a substantially uniform arrangement of the catalyst grains along the reactor, with, on average, every cross-section of the reactor comprising a defined and constant number of catalyst grains, and this number of grains being between 1 and 4. The reactor that is the object of the invention is especially well suited for studying reactions of hydrogenation, hydrotreatment, and hydrocracking.

Abstract: When fluids A and B are caused to flow together from a fluid introduction portion into a microreactionchannel, they are divided into a plurality of fluid segments A and B in a diametral section of the microreactionchannel at the entrance side, and are mixed with each other by molecular diffusion to perform multiple reaction while being caused to flow as laminar flows.

Abstract: The present invention includes a removable microchannel unit including an inlet orifice and an outlet orifice in fluid communication with a plurality of microchannels distributed throughout the removable microchannel unit, and a pressurized vessel adapted have the removable microchannel unit mounted thereto, the pressurized vessel adapted to contain a pressurized fluid exerting a positive gauge pressure upon at least a portion of the exterior of the removable microchannel unit. The invention also includes a microchannel unit assembly comprising a microchannel unit operation carried out within a pressurized vessel, where pressurized vessel includes a pressurized fluid exerting a positive gauge pressure upon an exterior of the microchannel unit operation, and where the microchannel unit operation includes an outlet orifice in fluid communication with an interior of the pressurized vessel.

Abstract: A disposable reactor module, monitoring/optical detection system and related hardware for, inter alia, chemical reactions including Polymerase Chain Reactions.

Abstract: A Reactor (1) for solid phase synthesis comprises a vessel (2), a plurality of filters (3) arranged in the vessel (2) and a plurality of filtrate outlets (4) for evacuating the filtrate out of the filters (3). Each filter (3) is connected to one filtrate outlet (4). The reactor (1) comprises means (3, 4) for delivering a gas into the vessel (2) in a region of the vessel (2) near to the bottom (24) of the vessel (2) and beside the filters (3).

Abstract: A device (20) for manufacturing a carbon nanotube array (10) includes a reaction chamber (220), a gas introducing tube (228), and a quartz boat (240). The reaction chamber includes a first gas inlet (222), a second gas inlet (224), and a gas outlet (226). The first gas inlet is configured for introducing a reaction gas, and the second gas inlet is configured for introducing a disturbance gas. The quartz boat is disposed in the reaction chamber. The quartz boat is used to carry a substrate (12) from/upon which the carbon nanotube array grows. The gas introducing tube is connected to the second gas inlet and to the quartz boat. The gas introducing tube is used to transport the disturbance gas introduced from the second gas inlet to the quartz boat to disturb/interrupt nanotube growth.

Abstract: The invention provides microfluidic systems for altering the solution environment around a nanoscopic or microscopic object, such as a sensor, and methods for using the same. The invention can be applied in any sensor technology in which the sensing element needs to be exposed rapidly, sequentially, and controllably, to a large number of different solution environments whose characteristics may be known or unknown.

Abstract: A multi-well plate such as a microtiter plate is secured from its well side in a manner that corrects or compensates for any deviations of the plate base from a planar configuration. This is achieved by an apparatus that includes an array of posts with exposed tips that define a plane, a plurality of movable collets that, when appropriately actuated, seize the walls of selected wells, and a biasing means to urge the collets in a direction that forces the wells of the microtiter plate against the exposed tips of the posts.

Abstract: Synthesis of chain molecules such as DNA is carried out in a conduit having an interior channel with an inlet end and an outlet end. At least one wall of the conduit is substantially transparent to selected wavelengths of light. Solid carrier particles are contained within the interior channel of the conduit. A plurality of controllable light sources are mounted at spaced locations along the length of the transparent wall of the conduit to allow selective illumination of separated sections of the particles within the conduit. When a light source is turned on, a photodeprotecting group is removed from the carrier particles in the section that is illuminated by the light source. A reagent containing a selected base is flowed through the conduit so that the base will attach to the carrier particles in those sections which have been exposed to light and deprotected.

Abstract: The compact chemical reactor with a central axis includes at least two unit reactors disposed adjacent to each other to form front and back sides of the compact chemical reactor; a front and back reactant plenum communicating with the front and back side respectively; at least one of the plenums comprises a reactant; and unit reactors comprising: a front cavity between front and back process layers; a back cavity between back and front process layers of adjacent unit reactors; the process layers facilitate transport processes between reactant plenums; each cavity communicates with one side of the compact chemical reactor; a front and back perimeter barrier on the back and front process layers respectfully, substantially surrounding respective cavities. At least one of the unit reactors comprise at least one frame formed from one of the process layers, at least one of the perimeter barriers, and at least one of the cavities.

Abstract: A method for reacting a plurality of materials in parallel within a reactor vessel having a plurality of reaction wells formed therein. Each of the reaction wells has an open end exposed to a common pressure chamber defined by the reactor vessel. The method includes opening a cover of the reactor vessel, inserting components into the reaction wells, closing the cover of the reactor vessel to create a sealed chamber, supplying a gas substantially above atmospheric pressure that reacts with the components within the reaction wells, and releasing pressure from the reactor vessel.

Abstract: A manufacturing method for 123I-ADAM and an automatic manufacturing device thereof are disclosed. The manufacturing process for 123I-ADAM consists of four steps-add [123I] ammonium iodide solution, make oxidation reaction occur, terminate the reaction and neutralize the solution, filter and collect the filtrate. The automatic manufacturing device includes a plurality of units for taking each of the four steps that is disposed inside a chassis and is operated by automatic control. Users only need to put reactants into storage bottles respectively, turn on the power, and initiate the operation system, Then the preparation process of drugs for clinical diagnosis is finished within twenty minutes.

Abstract: A manufacturing method for 123I-ADAM and an automatic manufacturing device thereof are disclosed. The manufacturing process for 123I-ADAM consists of four steps-add [123I] ammonium iodide solution, make oxidation reaction occur, terminate the reaction and neutralize the solution, filter and collect the filtrate. The automatic manufacturing device includes a plurality of units for taking each of the four steps that is disposed inside a chassis and is operated by automatic control. Users only need to put reactants into storage bottles respectively, turn on the power, and initiate the operation system, Then the preparation process of drugs for clinical diagnosis is finished within twenty minutes.

Abstract: The present invention discloses the substrate and the micro reactor for mixing two kinds of fluids. The micro reactor of the present invention comprises a housing having first and second inlet ports and an outlet port formed thereon; and a plurality of substrates stacked in the housing, wherein the substrate has a space formed at a central portion thereof in one direction; a plurality of first channels extended from one side thereof to the space and corresponding to the first inlet port; and a plurality of second channels extended from the other side thereof to the space and corresponding to the second inlet port; wherein a portion between two neighboring first channels corresponds to the second channel and a portion between two neighboring second channels corresponds to the first channel to form sequentially reaction interfaces of the first and second fluids in the space.

Abstract: An M.times.N matrix microfluidic device for performing a matrix of reactions, the device having a plurality of reaction cells in communication with one of either a sample inlet or a reagent inlet through a via formed within an elastomeric block of the device. Methods provided include a method for forming vias in parallel in an elastomeric layer of an elastomeric block of a microfluidic device, the method comprising using patterned photoresist masks and etching reagents to etch away regions or portions of an elastomeric layer of the elastomeric block.

Abstract: The present invention relates to a method and a device for the parallel study of chemical reactions in at least two spatially separated reaction spaces. In particular, the invention is suitable for reactions which are not constant volume reactions and/or for reactions in which fluid flows through at least two spatially separated reaction spaces are intended to be controlled together for all the reaction spaces, or for related subsets of them, in the most straightforward way possible.

Abstract: Means for enabling plating on sites of complex configuration, etching for fine complex pattern, etc. through reduction of the viscosity resistance brought about by walls of fine liquid channel of microreactor. In particular, a microreactor comprising a liquid inlet, a fine liquid channel and a liquid discharge zone characterized in that the liquid channel is formed of a magnetic barrier of band ferromagnet so that a magnetic liquid introduced through the inlet undergoes at least one operation of chemical reaction, mixing, extraction and absorption in the liquid channel. Further, there is provided means for plating or etching performed by causing a plating solution or an etching solution to flow through the liquid channel.

Abstract: A system is provided wherein a plug flow reactor is used to make combinatorial libraries of materials. Examples of plug flow reactors include stirred tube reactors, extruders, and static mixers.

Abstract: Unexpected corrosion of downstream sections of a dialkyl carbonate manufacturing apparatus has been traced to alkyl chloroformate impurities, which slowly decompose to yield hydrochloric acid. An improved process and apparatus for dialkyl carbonate synthesis reduce corrosion by physically removing or chemically decomposing the alkyl chloroformate impurities within the corrosion-resistant upstream sections of the apparatus.

Abstract: A stack type reactor that can adjust a length of channel (reaction time) to react raw substances with each other for a sufficient time and mix completely raw substances to maximize the reaction efficiency. The stack type reactor comprises an upper block with at least two inlets that introduce different kinds of raw substances and a lower channel fluidly connected to the inlets and formed at a lower surface thereof; a unit block including an upper channel corresponding to the lower channel of the upper block and formed on an upper surface thereof, the unit block including a lower channel formed at a lower surface thereof and fluidly connected with the upper channel via a connecting flow passage. The upper block and unit block form a flow path for the raw substances by connecting to the lower channel of the upper block to the upper channel of the unit block.

Abstract: In a microreactor in which a plurality of fluids L1 and L2 are led through their respective feed channels to merge in one reaction channel and react with each other while circulating, a spiral reaction channel is formed by cutting a spiral screw thread on either the outer surface of a round-bar-shaped core member or the inner surface having a circular cross section of an outer cylindrical member and engaging the outer surface of the core member in close contact with the inner surface of the outer cylindrical member.

Abstract: Embodiments of an apparatus, system, and method for chemical synthesis and/or analysis are disclosed. One embodiment of a disclosed apparatus comprises a laminated, microfluidic structure defining a reactor and a separator. Such apparatuses, or portions thereof, generally have dimensions ranging from about 1 micrometer to about 100 micrometers. To implement synthetic processes, disclosed embodiments of the apparatus generally include at least one valve, and often plural, selectively actuatable valves. Detectors, including optical detectors, also can be used to detect product and other materials as they flow by, or are otherwise presented to, the detector. Individual apparatuses may be coupled both in series and in parallel to form a system for making chemical compounds. The apparatus is particularly useful for making compounds requiring iterative reaction schemes, and further can be used to make compounds having morphological structures that resemble the morphology of the apparatus itself, such as dendrimers.

Abstract: A device includes a support (1) and at least two seals (2), which are arranged in a row and are hermetically fitted into cavities, and protrude from the support laterally with respect to inlet and outlet openings, one end of the support being provided with an inlet opening (3) and one end being provided with an outlet opening (4), and the seals being provided with a least one inlet opening and one outlet opening, and the support containing at least one first channel (5) which starts at the inlet opening (3) and is continuous, and is arranged in such a way that it opens into the inlet openings in the side walls of the seals arranged in a row, and one second channel (6) which starts at the outlet opening and is continuous, and is arranged in such a way that it opens into the outlet openings in the side walls of the seals arranged in a row.

Abstract: Embodiments of the present invention are directed to an apparatus and method for performing parallel processes. One embodiment of the present invention is directed to an apparatus for performing a process having a plurality of steps in which each step is performed in a vessel by flowing a fluid through said vessel. The steps of the process comprise at least a first step and at least one subsequent step. At least one of the subsequent steps is a final step, and each step has a time associated with its performance, a step period. At least one step has a longest step period, and the total number of steps, times the longest step period equals a process period. The apparatus comprises a plurality of vessels. Each of the plurality of vessels is for performing sequentially all the steps of the process in the process period and each of the plurality of vessels is for performing each step of the process in the longest step period.

Abstract: An instrumentation interface that provides a standardized states of a plurality of devices to a control system. Coordinating the operation of the plurality of devices in an analytical system is simplified by allowing the control system to perform in terms of simplified standard states. Device specific states that vary for different types of devices are logically linked to the standardized states via a form of a translator. By having the control system not worry about the specifics of a device, its ability to coordinate large number of devices is improved.

Abstract: The present invention relates to a method of testing catalysts and catalyst systems via a plurality of stations in which each station can accommodate a common reactor module in order to accomplish unattended, automated, rapid serial experimentation.

Abstract: A multiport cofinger stopper and a device that includes a multiport cofinger stopper and a microreactor, wherein the stopper includes a main housing with a central orifice and a plurality of outer orifices located about the central orifice, and a sealing mechanism on the sidewall of the main housing. The cofinger is a concentric set of at least two tubes with at least one inner tube and an outer tube, the outer tube having a closed bottom. In some embodiments, the main housing has an upper section and a lower section, with the lower section of smaller diameter than the upper section.

Abstract: The present invention provides methods, systems and apparatus in which one fluid passes through an orifice or orifices and mixes with another fluid as it flows through a microchannel.

Abstract: The invention related to a microreactor system for the continuous synthesis, which provides defined reaction chambers and conditions for said synthesis, as well as to the uses of said microreactor in carrying out a chemical reaction. According to said invention, (a) said mircoreactor system (11) is of modular design, (b) a processing unit (10) is made up of processing modules which are connected to each other by frictional engagement and (c) the fluid connections in said processing unit (10) can be obtained by the frictional connection of said processing modules.

Abstract: Methods and apparatus for implementing microfluidic analysis devices are provided. A monolithic elastomer membrane associated with an integrated pneumatic manifold allows the placement and actuation of a variety of fluid control structures, such as structures for pumping, isolating, mixing, routing, merging, splitting, preparing, and storing volumes of fluid. The fluid control structures can be used to implement a variety of sample introduction, preparation, processing, and storage techniques.

Abstract: The present invention pertains to A cyclic process for testing FCC catalysts with resid feedstock on a small scale wherein in a first cycle: a) the feed to be cracked is heated to a temperature between 50 and 500° C., b) the heated feed is injected into a riser reactor containing the FCC catalyst to be tested having a temperature between 500 and 800° C., the injection time being less than 2 seconds, c) an inert gas is injected into the lower end of said reactor riser together in the vicinity of the feed injection in a volume ratio of inert gas to vaporized feed of about 0.03 and 10, the mixing of feed and inert gas occurring in said riser reactor; d) the feed is contacted with the FCC catalyst under fluidized conditions for a contact time of less than 8 seconds; e) the feed is stripped from the FCC catalyst and the properties of the product are analyzed; and in a second cycle a quench liquid is injected into said riser reactor in an amount of up to about 20 wt.

Abstract: A process is described in which an elastic fluid is contacted with a particulate solid. This comprises providing a substantially vertical elongate tubular containment zone (1) containing a charge of the particulate solid (5), the volume of the containment zone (1) being greater than the settled volume of the particulate solid (5). An upper retainer means (3) is mounted at the upper end of the containment zone (1), the upper retainer means (3) being permeable to the fluid but adapted to retain particulate solid (5) in the containment zone (1). A follower means (4) is movably mounted in the containment zone (1) beneath the charge of particulate solid (5) for movement upwardly from the lower end of the containment zone (1) upon upward flow of elastic fluid through the containment zone (1) at a rate beyond a threshold rate.

Abstract: A method of starting up and shutting down a microchannel process is provided. Included are the steps of providing a first multi-planar process unit, preferably adapted to process an endothermic reaction, a second multi-planar process unit, preferably adapted to process an exothermic reaction, providing a containment vessel, the containment vessel containing at least a portion of the first, and preferably the second, process unit. In startup, the microchannel process is first checked for pressure integrity by pressurizing and checking the important components of the process for leaks. Subsequently, the process units are heated by introducing a dilute low-thermal energy density material, preferably to the second process unit, followed by the introduction of a dilute high-thermal energy density material, and adjusting the proportion of high-thermal energy density material as required. In shutdown, a purge material from the containment vessel is introduced into the first, and preferably the second, process unit.