Abstract: A membrane oxygenator includes an upper nested arrangement of a hard shell venous reservoir, a bowl-like defoamer within the reservoir and a heat exchanger coil vertically supported within the defoamer, and includes a membrane oxygenator unit mounted on the bottom of the upper arrangement. The oxygenator unit includes an inlet chamber with a tangential inlet providing swirling blood flow to dislodge air bubbles and centrifuge air to an upper center region of an inlet chamber where gas is exhausted through a vent. A bottom blood outlet chamber of the blood oxygenator unit has a relatively thin vertical cross-sectional area such that priming flow velocity therein discharges all air from the outlet chamber.

Abstract: A blood oxygenator which independently controls the rate of oxygen and carbon dioxide exchange between an oxygen enriched gas and the blood. The oxygenator of the invention includes a gas inlet mechanism for diverting oxygen enriched gas between two different pathways. The first flow pathway feeds the oxygen bearing gas to a diffusion plate or sparger for the purpose of forming bubbles which diffuse into the blood to facilitate the exchange of oxygen and carbon dioxide between the gas and blood. The second flow pathway feeds oxygen down into the interior of the oxygenator as a substantially continuous stream which creates a substantially single gas bubble, or is simple a substantially continuous flow of gas with the oxygenator. This continuous flow of gas affects a gas exchange across the blood-gas interface, with carbon dioxide diffusing into the gas at substantially the same diffusion rate as occurs with the microbubbles diffusing into the blood, but with a lower diffusion rate for the oxygen.

Abstract: Improved methods and apparatus for removing unwanted pollutants from flue gases are disclosed. A sequence of at least three vertical beds of particulates is disposed in the flue gas exhaust duct. A first bed comprises boiler ash or sand. Lime in the fly ash and sulfuric acid and water in the flue gas react with the particulates to form gypsum, removing the fly ash from the flue gas. In the second bed, the remaining sulfuric acid is condensed and removed on a further bed of boiler ash. In the third bed, a catalyst, typically an activated aluminous particulate with an alkali coating thereon, provided by adding ammonia to the flue gas stream, condenses out the remaining sulphur dioxide, which can then be removed from the catalyst particles in a regenerative step. A scrubber embodying these principles is readily retrofittable to pre-existing power plants burning sulphur-containing coal.

Abstract: A sample handling unit for centrifugation apparatus, especially for cytocentrifugation to produce cell monolayers is disclosed. The sample handling unit is adapted for automated protective processing, e.g. fixation, of matter deposited on a slide during the centrifugation operation. For this purpose the unit has a body defining a deposition chamber, and a treatment fluid reservoir communicating with the deposition chamber via a buffer chamber and a flow path including a weir so arranged that in the position for centrifugation, treatment fluid such as fixative placed in the reservoir is retained therein until centrifugation produces an artificial gravitational field that causes the fluid to flow to the buffer chamber in which it is then retained by the weir for so long as the artificial gravitational field is maintained. Upon decay of that field the fluid flows over the weir towards the deposition chamber.

Abstract: A bubble cap assembly and distributor plate is revealed uniquely suited for a reactor in an ebullated bed process. In the riser of the bubble cap assembly a ball check valve is mounted on a valve seat. An orifice mixer below the valve seat delivers a homogeneous vapor-liquid mixture to the orifice in the valve seat thereby minimizing slug flow which causes destructive valve chatter. The fluid outlet port is positioned in the riser to hydraulically limit ball travel between the valve seat and the cap, eliminating the need for pins or other restraints.

Abstract: A method of preparing an integral multilayer analytical element such as for analysis of calcium comprising a water-impermeable light-transmissive support, a reagent layer containing a water-soluble indicator capable of reacting with an analyte to produce an optically detectable change, and a porous spreading layer containing a spreading action controller and/or an acid capable of decomposing the calcium compounds in a sample, superposed in this order, wherein the spreading action controller and/or the acid is dissolved in an organic solvent which does not dissolve the above water-soluble indicator, this solution is incorporated into the porous spreading layer, and this superposed material is dried. In the method of the present invention, the migration of the water-soluble indicator in the reagent layer at the time of incorporating the spreading action controller or the acid into the spreading layer is inhibited by using a particular organic solvent.

Abstract: A storage container of samples for analysis is disclosed, having a cylindrical tube and two fittings adapted for connection with a syringe, mutual connection of containers in series, or closing and manufactured from a suitable plastic or glass. A column of sorbent is closed at both ends with a porous partition, screen, paper filter, or a layer of silicate or glass wool. The size of sorbent particles is 20-150 um (micrometers). The content of the storage container is protected during storage and/or transportation by closures from both sides. The sorbents which are packed into the storage container are selected from silica gel or organic copolymeric carriers of specific or nonspecific functional groups, which are purposefully chosen.

Abstract: A process for economically converting carbo-metallic oils to lighter products. The carbo-metallic oils contain 650.degree. F.+ material which is characterized by a carbon residue on pyrolysis of at least about 1 and a Nickel Equivalents of heavy metals content of at least about 4 parts per million. This process comprises flowing the carbo-metallic oil together with particulate cracking catalyst through a progressive flow type reactor having an elongated reaction chamber, which is at least in part vertical or inclined, for a predetermined vapor riser residence time in the range of about 0.5 to about 10 seconds, at a temperature of about 900.degree. to about 1400.degree. F., and under a pressure of about 10 to about 50 pounds per square inch absolute sufficient for causing a conversion per pass in the range of about 40% to 90% while producing coke in amounts in the range of about 6 to about 14% by weight based on fresh feed, and laying down coke on the catalyst in amounts in the range of about 0.

Abstract: An apparatus for separating solids and vapors from a suspension of the two materials is disclosed. The solids are directed through a conoid element to enhance directional flow and to prevent return of solids to the separation apparatus.

Abstract: A moving belt interface for real-time, high-performance liquid chromatograph (HPLC)/mass spectrometer (MS) analysis which strips away the HPLC solvent as it emerges from the end of the HPLC column and leaves a residue suitable for mass-spectral analysis. The interface includes a portable, stand-alone apparatus having a plural stage vacuum station, a continuous ribbon or belt, a drive train magnetically coupled to an external drive motor, a calibrated HPLC delivery system, a heated probe tip and means located adjacent the probe tip for direct ionization of the residue on the belt. The interface is also capable of being readily adapted to fit any mass spectrometer.

Abstract: In the device for evaluating test strips having individual test sections, which consist of a terminal, a work platform with holder for the test strips and a sensing head, a position mark 5 is arranged for each test section 9 on the side of the holder 13. On the work platform 15, the sensing head 14 is arranged so as to be capable of of traversing the test sections 9 and the position marks 5. The sensing head 14 is provided with light sources 6, which are directed towards the test sections 9, of different wavelength and with a light receiver and with at least one position detector 10 which is directed towards the position marks.

Abstract: Apparatus for regenerating zeolite-type catalyst used in fixed bed hydrocarbon conversion processes, such as the conversion of olefins to gasoline and diesel fuel. Regeneration is achieved using a portion of a flue gas stream to regenerate catalyst and preheat feedstock. Economies in equipment and operation are realized by employing a once-through configuration for the regenerator gas stream.

Abstract: A gas mixer and distributor for a reactor has first and second inlet chambers with the second inlet chamber being interposed between the first inlet chamber and an entrance to a reaction chamber. Walls form tubular or slit-like passageways extending from the first chamber to the entrance of the reaction chamber through the second chamber. Upper portions of the passageways have uniform cross-sections selected to produce gas velocities above the flashback velocity, as well as producing turbulence to completely mix gas passing from the second chamber through orifices in the walls of the passageways. Lower sections of the passageways gradually increase in cross-section to reduce velocity and minimize vortexing and recirculation at the entrance to the reactor chamber.

Abstract: A centrifuge for performing biological and medical analyses for samples in test packs mounted in holders peripherally disposed on the centrifuge rotor. The test pack holders are also rotated relative to the rotor by means of a mechanical spinning portion fitted below the rotor. Analyses are made with a spectrophotometric measuring device, whose optical path is perpendicular to the plane of the rotor.

Abstract: A microprocessor controls a heater which generates steam inside the sealed chamber of a sterilizer. During that portion of the sterilizer cycle wherein sterilizing conditions are trying to be attained, the microprocessor monitors both the temperature and pressure levels inside the chamber by controlling the heater and waits until both variables reach predetermined levels before starting a sterilize timer. Once the timer is started, it is stopped if the level of either one of the temperature or pressure variables drops below a predetermined minimum value which, in the preferred embodiment, air their optimum values. While the sterilize timer is timing, the pressure level rather than the temperature level is used by the microprocessor to control the heater. These features allow a more reliable and accurate control of the generation and maintenance of sterilizing conditions inside the chamber, resulting in greater assurance of complete sterilization while minimizing the expenditure of time and energy.

Abstract: A sample duct in a carrier line is isolated by three-way valves blocking the flow of carrier or flushing liquid from reservoirs. The sample duct may be connected to a loading syringe and to a sample reservoir respectively by the valves. When the sample duct is connected into the carrier line, pressurized carrier fluid may convey the sample for analysis through a manifold comprising valves through which reagents may be introduced from reservoirs. The sample then passes through a thermostatically controlled reaction tube to a valve which switches it between waste and an outlet leading to a detector for analysis. The carrier and flushing fluids and the reagents are pressurized by gas from an inlet which is conveyed via an overpressure vent to the reservoir by lines. Rigid inert tubing is used throughout the carrier line, sample duct, manifold and reaction tube.

Abstract: A continuous process for alkylating an alkylatable hydrocarbon in the presence of a acid-type catalyst in which the alkylatable hydrocarbon is contacted with an alkylating agent in the presence of a catalyst in a reaction zone so as to alkylate the alkylatable hydrocarbon. The reaction product is separated in an acid settler vessel into an alkylate product phase, located in the upper portion of the first separation zone, and a catalyst phase located in the lower portion of the first separation zone. The catalyst phase is further separated into a first portion and second portion, such that the first portion is cooled and recycled for use in the alkylation reaction zone as a catalyst recycle, and the second portion is passed into a second separation zone, wherein the catalyst phase is further separated into a rerun catalyst stream containing acid-type catalyst and an acid soluble oil stream. The rerun catalyst stream is passed into the hydrocarbon phase of the acid settler vessel.

Abstract: A pipette assembly for automatic pipetting machines including a pipette tip and a pipette tip holder having a mandrel and a seal. The mandrel includes a plug portion which is adapted to engage a top end portion of the pipette tip, and a cylindrical seat portion proximate its bottom end. The seal is a unitary, resilient member having a cylindrical base portion, an upwardly flaring skirt portion, and an opening receptive to the seat portion of the mandrel. An inner surface of the base portion of the seal is provided with a pair of sealing ribs, one of which serves as a pivot for the skirt portion.

Abstract: A device suitable for use as a catalytic converter for purification of the exhaust gases from an internal combustion engine at continuous operating temperatures in excess of 1600.degree. F. and up to 2500.degree. F. includes a frangible ceramic monolith catalyst element resiliently mounted in a metallic housing. The monolith is wrapped in a thermally insulating layer of ceramic fibers capable of withstanding continuous exposure to temperatures of at least 2000.degree. F. A layer of intumescent material disposed between the housing and the ceramic fiber layer resiliently secures the monolith in the housing. A method of manufacture of such a device is also described.

Abstract: An analyte in solution is made to react with a specific reactant coated on the wave-guide thus modifying the optical properties thereof. The index of refraction of the wave-guide material is higher than that of the reaction medium which ensures that a light signal injected into said guide be carried by multiple total reflection, the distance of penetration of the evanescent wave associated with the totally reflected signal being of the same order of magnitude or greater than the thickness of the analyte-reactant product layer.