Abstract: Specific-site extraction unit 24 extracts specific sites from microscopy images that are obtained by staining or fluorescence labeling of specific sites in a specimen 4. Based on the similarity between MS imaging data and the spatial distribution of the specific sites, cluster analysis unit 25 and division count determination processing unit 26 evaluate the similarity with the spatial distribution of all pixels that belong to one cluster when each of the pixels are categorized into a plurality of clusters. Since the specific sites are sites that include the same characteristic substance, clustering is judged to be appropriate if the similarity in spatial distribution is high. Hence, based on the correlation between spatial distributions, an appropriate division count for the cluster analysis is determined, and the result of the cluster analysis using the division count is output on a display unit 31.

Abstract: A germicidal method and apparatus for destroying airborne pathogenic bacteria such as tuberculosis bacteria using ultraviolet light. Air is drawn through a filter and into a sterilization chamber that is irradiated with ultraviolet light, and out through an exhaust opening. Consideration for the characteristics of the room in which the apparatus is installed and the positioning of the installation allows effective prevention of transmission of disease through expectoration and inhalation of airborne microdroplets of bacteria-containing sputum. The filter is of the low-density type which traps large particulates, but not small particulates of the size of the microdroplets, so that the filter does not become a bacteria colonization site. Baffles on the air intake opening and air exhaust opening to prevent ultraviolet light from escaping into the environment. The sterilization chamber is constructed such that the air passes the ultraviolet light bulbs twice as it circulates therethrough.

Abstract: A process for producing a synthetic and/or fuel gas from an organic containing material by utilizing a thermal pretreatment operation and a gasification reactor. The organic containing material is passed through a thermal pre-treatment operation to produce a gas fraction and a solid fraction. The solid fraction is processed in gasification reactor whereby product gas is produced, and contaminated products are processed for safe disposal. The thermal pre-treatment of the organic containing material produces a solid fraction which can be directly supplied to the gasification reactor without a need to supply a high quality coke to the gasification reactor thereby simplifying the process. The gas fraction and product gas produced from the thermal pre-treatment operation and/or gasification reaction, respectively, can be recycled so as to supply energy and/or processing gas for the various other processes.

Abstract: Process for radial distribution of fluid into a fluid mass wherein fluid is radially conveyed within and isolated from the fluid mass and discharged via a plurality of distribution points located radially in the fluid mass.

Abstract: A fluidized-bed reactor is suitable for uniformly oxidizing, i.e. combusting or gasifying, solid material containing combustible material and incombustible material, and for stably recovering thermal energy from the oxidized combustible material while smoothly discharging the incombustible material. The fluidized-bed reactor comprises a plurality of fluidizing gas diffusion devices disposed at a bottom of a fluidized-bed furnace for imparting different fluidizing speeds to the fluidized medium in a fluidized bed in the fluidized-bed furnace to form an upward flow of the fluidized medium in a fluidizing region with a substantially high fluidizing speed of the fluidized medium and a descending flow of the fluidized medium in a fluidizing region with a substantially low fluidizing speed of the fluidized medium. A plate-like thermal energy recovery device is disposed in the fluidizing region with the substantially low fluidizing speed of the fluidized medium and has a heat recovery surface extending vertically.

Abstract: A process for producing a polyoxymethylene using a reactor having a discharging port having a weir, which process comprises introducing trioxane or a mixture of trioxane and a compound reactive therewith into the reactor from its feeding port and continuously recovering the powdery polyoxymethylene formed, from said discharging port having a weir. Owing to the presence of the weir, the residence time of reaction mixture in reactor is long, making high the conversion of the monomer.

Abstract: A process in which a high-purity, high-pressure hydrogen-rich gas stream and a high-purity, high-pressure carbon monoxide-rich gas stream are simultaneously produced separately and continuously using a molten metal gasifier that contains at least two zones, thereby avoiding the need to separate or compress the gases in down-stream equipment.

Abstract: Apparatus for use in the rectification of liquid mixtures (separation of liquid mixtures into their constituents) and other processes requiring equilibration of liquid and gaseous phases in which mechanical energy is used to create and repeatedly regenerate free flying liquid structures that facilitate the intimate interaction and equilibration of said phases beyond standard practice and thereby allow smaller, more compact, more efficient, and more accessible apparatus and make practical lower operating temperatures and the use of inert carrier gases and otherwise increase the engineering options available to designers of rectification equipment and other equipment requiring liquid/vapor equilibration.

Abstract: In a method for treating a combustion exhaust gas from a waste burning facility, the exhaust gas has its temperature lowered to 180-230.degree. C., in a temperature lowering unit, is freed of dust in a dry dust collector, passed through a dioxin and NOx removing unit using a vanadium oxide-based catalyst and, thereafter, the exhaust gas at 180-230.degree. C. is further passed through a heat exchanger to effect heat recovery. The vanadium oxide-based catalyst is a vanadium oxide alone or the combination thereof either with an oxide of at least one element selected from the group consisting of molybdenum, tin, yttrium, boron and lead or with gold. In addition, a tungsten oxide may be used. These catalysts are preferably carried on titania for use. The method and an apparatus for implementing it require a simple system configuration and yet assure high thermal efficiency while achieving efficient removal of dioxins and nitrogen oxides.

Abstract: The invention is directed to an apparatus for contacting in a reactor solids in the form of free-flowing lumps with liquids or for contacting solids with liquids and gases by bringing the reactants into contact with each other, said reactor comprising a housing containing a screen in the area of which contacting takes place whereinthe screen is a rotary screen drum 5,the screen drum 5 rotates in a bottom vat during the operation, said vat holding a gaseous or liquid medium reacting with the solids, andthe bottom vat 10 can be lowered such that the solids in the screen drum 5 and the medium in the bottom vat 10 can be separated from each other whenever it is desired to alter or interrupt the chemical reaction or physical process.

Abstract: A method for repairing and restoring the functionality of equipment subjected to internal corrosion during its operation at high or medium pressure in a plant for the synthesis of urea. The method includes the cleaning of the corroded area, the formation of suitable supporting and/or holding surfaces for the placement of a new metallic lining, the formation of a new anticorrosive sealed off lining, obtained by positioning and welding flat elements and metallic plates which are suitably shaped and placed next to each other to become adapted to the internal profile of the equipment. The spaces and interstices below this new lining all communicate with at least one weep-hole present in the pressure resistant body. The entire repair is carried out through the manhole of the equipment and enables the restoring of its functionality for times similar to the normal duration of corresponding newly constructed equipment.

Abstract: A shaft reactor for treating bulk material, including granular bulk material, in particular for the continuous post-condensation of PET, PEN or PA in the solid phase. A uniform product flow without significant decrease of the usable contents of the reactor and a decrease of the bulk pressure in the reactor is achieved by use of internals which are uncomplicated to fabricate. Internals are arranged in the reactor which comprise at least one ring and a plurality or ribs.

Abstract: The invention relates to a device, in particular for the treatment of low-viscosity polymer melts, containing a vessel (1) with a stirrer element, the stirrer element (6) essentially comprising a support structure which passes through the vessel and on which surface formers (8) are arranged. According to the invention, the support structure is designed as a cage-like rod frame (7).This results in the following advantages:1. Owing to the now possible continuous wetting or wiping of the surfaces, encrustations and inhomogeneities are avoided.2. Due to enhanced cascading with weir plates, the residence time spectrum can be controlled, which likewise improves the product quality.3. The flexing of the stirrer element is reduced.

Abstract: A fluid delivery device (10) operated by a first gas delivery device (12) (e.g. electrochemical pump) that takes advantage of sequential gas production methods. The fluid delivery device includes a container (14) with an interior surface. An first gas delivery device for producing or delivering a first gas is placed in one end of the container. A moveable member (e.g. piston, bladder (18) or membrane) is positioned within the container, which moveable member, together with the container's interior surface and the electrochemical cell, structurally define a fluid-tight chamber. The moveable member may abut a first reactive material. Unreacted material (34), chemically reactive with the either the first gas or the first reactive material to generate a second gas, is contained within the container.

Abstract: A reactor for catalytic dehydrogenation of dehydrogenatable hydrocarbons, in particular C.sub.3 and/or C.sub.4 hydrocarbons, in a hydrocarbon-containing stream, with selective oxidation of hydrogen. The reactor comprises serially connected in the flow direction of the hydrocarbon-containing stream: a first catalyst zone (2), an oxygen admixing zone (3) provided with a means (5) for separate feeding of an oxygen-containing gas into the hydrocarbon-containing stream, and a second catalyst zone (4). The oxygen admixing zone (3) has a cross section area in the flow direction of the hydrocarbon-containing stream which is from 0.5% to 75% of the cross section area of each of the two catalysts zones (2, 4), so as to obtain a higher flow velocity in the oxygen-admixing zone (3) than in the catalyst zones.

Abstract: An integrated micro-ceramic chemical plant having a unitary ceramic body formed from multiple ceramic layers in the green state which are sintered together including the unitary ceramic body defining a mixing chamber and passage means for providing communication with the mixing chamber so that two or more fluids may be delivered to such mixing chamber for mixing or reacting chemicals in the fluids; and the unitary ceramic body including means for delivering the mixed chemicals to exit from the unitary ceramic body.

Abstract: In a reactor of the type having a vessel, an agitator for agitating the contents of the vessel, and a heat exchange system within the vessel, the improvement wherein the heat exchange system comprises: a first substantially annular header which comprises pipe; a second substantially annular header comprising pipe and being spaced from the first header; a third substantially annular header comprising pipe and being spaced from the first header and adjacent to the second header; a first set of tubes extending between and connecting the first header and the second header; and a second set of tubes extending between and connecting the first header and the third header.

Abstract: Sterile interconnection between disassociated segments of thermostable, compressible fluid conduit tubing is achieved by arranging within the bore of the free end of each segment a conductive hollow metal tube so as to establish a connected fluid flow path from one segment to the other, through the metal tube, and then sterilizing the connection by induction heating.

Abstract: The device serves to meter at least two free-flowing components and to convey metered quantities of the components into a mixer in which a reactive compound is formed from the metered quantities. For each component the device contains, as metering and conveying means, in each case at least one pump, a flow meter and a pressure vessel. The pressure vessel is subdivided by a flexible diaphragm into a first part-volume, which in each case receives one of the components, and a second part-volume which can be acted upon by incompressible fluid. When a starting component containing abrasive substances is used, to avoid sedimentation of the abrasive substances during metering and conveying, the pressure vessel which receives the abrasive component is designed and arranged in such a way that the abrasive component fed into its first part-volume rests on the flexible diaphragm.

Abstract: A process for discharging a reactor characterized by reducing the volume of a powder without compacting it, including treating the powder in a densification zone including at least one Archimedes' screw arranged in a barrel. The Archimedes' screw may also have both a reduction in pitch and an increase in diameter of the shaft. The densification zone may also contain two co- or counterrotating screws arranged in a barrel and exhibiting a reduction in the pitch of the screws. Densification zones consisting of two co-rotating screws give particularly good results.