Abstract: A reverse hydrocyclone cleaner for removing light contaminants from pulp slurry has a housing defining a hydrocyclone separating chamber. Pulp slurry is fed into the separating chamber adjacent an upper end thereof to form an outer helically and downwardly moving slurry stream relatively free from light contaminants, an inner pulp stream containing a substantial amount of the light contaminants and an air core within the inner stream. An overflow orifice is located adjacent an upper end of the separating chamber, and an underflow orifice is located adjacent a lower end of the separating chamber to remove the outer pulp stream relatively free from light contaminants. A centrally located blocking finger is located in the underflow orifice.

Abstract: An apparatus and method embodied in a TRC system for rapidly separating particulate solids from a mixed phase solids-gas stream which may be at velocities up to 150 ft./sec. and at high temperature. Specifically, the device is designed for incorporation at the discharge of solid-gas reacting TRC systems having low residence time requirements and carried out in tubular type reactors. Separation is effected by projecting solids by centrifugal force against a bed of solids as the gas phase makes a 180.degree. directional change, said solids changing direction only 90.degree. relative to the incoming stream.

Abstract: An air cleaning device having a chamber receiving an incoming air stream wherein the improvement consists of the chamber progressively confining the incoming air stream to increase its linear and angular velocity and having an exhaust chamber receiving contaminants and isolating the same from the turbulence of the incoming air stream and a shield adjacent the dome of the device restricting the vertical clearance of the chamber receiving the incoming air stream.

Abstract: This invention relates to an apparatus and method embodied in a TRC system for rapidly separating particulate solids from a mixed phase solids-gas stream which may be at velocities up to 150 ft./sec. and at high temperature. Specifically, the device is designed for incorporation at the discharge of solid-gas reacting TRC systems having low residence time requirements and carried out in tubular type reactors. Separation is effected by projecting solids by centrifugal force against a bed of solids as the gas phase makes a 180.degree. directional change, said solids changing direction only 90.degree. relative to the incoming stream.

Abstract: An ambient aerosol sampling device according to the disclosure herein includes a cyclonic fractionator comprised of an inner tube positioned partially inside a larger diameter middle tube that is plugged at the bottom. A still larger sized outer tube is positioned over the middle tube to receive air flow out of the middle tube and direct it to a conventional filter substrate. A plurality of vanes are positioned at the inlet of the inner tube to impart a vertical motion to an air stream flowing therein. A protective cover is positioned over the vanes and cyclonic fractionator, and an aerodynamic deflector at the bottom of the cover and air ramp inside the cover provides an omni-directional inlet pathway to draw air into the sampling device and to guide the airstream into the vanes.

Abstract: This invention relates to an apparatus and method for rapidly separating particulate solids from a mixed phase solids-gas stream which may be at velocities up to 150 ft./sec. and at high temperature. Specifically, the device is designed for incorporation at the discharge of solid-gas reacting systems having low residence time requirements and carried out in tubular type reactors. Separation is effected by projecting solids by centrifugal force against a bed of solids as the gas phase makes a 180.degree. directional change, said solids changing direction only 90.degree. relative to the incoming stream.

Abstract: An apparatus for removing particulate matter from gases includes an outer tube having an apertured bottom member, a plurality of stationary vanes for guiding gases into a vortical path through the outer tube, and an inner tube. The inner tube has a smaller diameter than the outer tube and fits partially inside the outer tube. Since the inner tube is arranged coaxially with respect to the outer tube, an annular passageway is defined between them. The passageway end of the outer tube is flared out forming a bell-mouth-shaped lip. A plurality of separate airfoil-shaped vanes, disposed across the passageway have their leading edges above the passageway. The bell-mouth-shaped lip and airfoil-shaped vanes, with their thicker leading edges extending above the passageway, both contribute to a more laminar flow through the passageway, thereby minimizing the pressure drop through the passageway.

Abstract: The present invention relates to improvements in centrifugal separators of the cyclone type, in which the liquid or gaseous fluid to be purified passes through an inlet blading which is shaped so as to cause the fluid to whirl rapidly in so-called irrotational flow with uniform longitudinal lamellar components, around a high voltage electrode. An outlet device firstly comprises a convergent portion which partly converts the energy of whirling into energy of longitudinal translation, then a blading which completes the conversion, and finally a divergent portion in which the excess of dynamic energy of flow is converted into static pressure in order to recover as much as possible of the whirling energy applied to the fluid upstream of the inlet of the cyclone device. The separated particles are evacuated through a tangential outlet. The invention is more particularly applicable to the purification of fluids.

Abstract: The invention relates to vacuum cleaning appliances.The appliance of the invention includes a cyclone unit which is operable to extract dust and other dirt from the air flow therethrough and to deposit the extracted dust and other dirt in a chamber outside the cyclone and separate from the air flow through the casing of the appliance. The extracted dirt is removed from the appliance by separation of the cyclone unit from the casing.The appliance is convertible to act both as an upright type cleaner or a cylinder type cleaner.

Abstract: This invention relates to an apparatus and method embodied in a TRC system for rapidly separating particulate solids from a mixed phase solids-gas stream which may be at velocities up to 150 ft./sec. and at high temperature. Specifically, the device is designed for incorporation at the discharge of solid-gas reacting TRC systems having low residence time requirements and carried out in tubular type reactors. Separation is effected by projecting solids by centrifugal force against a bed of solids as the gas phase makes a 180.degree. directional change, said solids changing direction only 90.degree. relative to the incoming stream.

Abstract: This invention relates to an apparatus and method for rapidly separating particulate solids from a mixed phase solids-gas stream which may be at velocities up to 150 ft./sec. and at high temperature. Specifically, the device is designed for incorporation at the discharge of solid-gas reacting systems having low residence time requirements and carried out in tubular type reactors. Separation is effected by projecting solids by centrifugal force against a bed of solids as the gas phase makes a 180.degree. directional change, said solids changing direction only 90.degree. relative to the incoming stream.

Abstract: A vortical-type separator for removing from the gas stream suspended particulates present in the gas stream has an internally generated scavenging gas flow and a pulse jet system for cleaning scavenging gas filter elements. The separator has two or more conduits that are coaxially positioned with an annular clearance at their ends. A gas swirl device creates a swirling motion, causing heavier particulates to be discharged out the annular clearance or ejection port into a scavenging gas plenum. A flow path is created between the scavenging gas plenum and the outlet of the separator, with the pressure differential between the outlet and the ejection port causing scavenging gas to flow to the outlet. A frame is mounted in the flow path over which a bag filter is secured. The dust-laden scavenging gas flows through the bag filter and out the outlet. A nozzle is positioned at the mouth of the bag filter for periodically discharging a pulse of clean gas into the bag filter reverse to the flow of the scavenging gas.

Abstract: An air pre-cleaner of the centrifugal type has a cylindrical housing with an annular louvred air entry structure at a first end thereof and coaxial therewith, and has an inner cylinder forming with the housing and the entry structure an annular separation chamber coaxial with, adjacent to, and axially inward of the entry structure. The inner cylinder forms with the housing a short cylindrical transfer chamber coaxial with, adjacent to, and axially outward of the separation chamber. A ring flange is disposed at the inner end of the inner cylinder along the inner ring of the annular separation chamber lying in a plane normal to the axis of the chambers. A dirt discharge slot is disposed in the side wall of the housing with one end of the slot substantially radially outward from the ring flange, the slot extending along a major portion of the axial length of the separation chamber.

Abstract: In a process for the centrifugal treatment of liquid of liquid or gaseous fluids containing impurities in suspension, of the type in which the fluid to be treated is injected tangentially in a first end of an apparatus of circular transverse section in which this fluid forms a first, substantially cylindrical rotating layer, while at the other end, and starting from the periphery, a fraction containing heavy impurities is collected, then cleared fluid, then possibly a fraction containing impurities lighter than the fluid, it being provided to recycle at least one fraction of the fluid leaving the apparatus by tangential injection into the first end thereof, the fraction to be recycled independently of the initial fluid to be treated is injected at a point located at a radial distance different from that of the point of injection of said fluid, so as to create in the apparatus at least one second, substantially cylindrical layer concentric to the first, in contact therewith and rotating in the same direction s

Abstract: Improved apparatus for carrying out catalytic chemical conversion and restoring the catalytic activity of solid particles previously used to promote chemical conversion involve improved devices to at least partially separate solid particles-vapor mixtures. These improved devices include, for example, properly positioned arresting vanes, flow reversal systems and/or plates, and provide for reduced attrition of the solid catalyst particles.Improved methods employing such apparatus are also disclosed.

Abstract: The disclosure concerns a separator for removing broken engine parts and other debris from the hot gases passing fro the exhaust manifold of an engine to the inlet of an associated turbocharger. The separator includes an annular separation chamber in which the gases are swirled by stationary vanes to effect centrifugal separation of the debris, and a cylindrical screen which filters the gases as they leave the separation chamber. The screen is mounted in cantilever fashion within the separator casing and carries, at its free end, the vanes and a deflector which directs inlet flow radially outward to the separation chamber. The vanes are freely mounted in slots formed in the screen, where they are held captive by the slot margins and the deflector, and the tips of the vanes are spaced radially from the surrounding casing of the separator.

Abstract: The inlet assembly is mounted within a separator vessel and comprises a housing similar in shape to that of a snail shell. This housing has a generally spiral side wall closed in by top and bottom end walls. A feed pipe delivers pressurized crude oil tangentially to the inner end of the spiral side wall so that it rotates outwardly, following the length of said wall, to an outlet communicating with the interior of the separator vessel. Gas is separated by centrifugation in the smaller radius central portion of the housing and then the liquid flow velocity is reduced by expansion of the stream in the larger radius outer portion. Improvements in gas separation and emulsion reduction have been observed from use of the assembly.

Abstract: An intake air system for an internal combustion engine having an upright stack mounted on vehicle structure, as a hood, with a stack connecting assembly. An air precleaner is mounted on the upper end of the stack. The lower end of the stack is connected to tubular members which leads to the air cleaner of the engine. The precleaner has a cylindrical housing surrounding a separation chamber. A vane assembly has a plurality of circumferentially spaced vanes providing an inlet passage open to the chamber for directing the air and particles into the chamber in a circular motion. A sleeve is centrally attached to the vane assembly and has a central outlet passage for carrying cleaned air from the chamber. An impeller assembly is rotatably mounted in the chamber and has a plurality of rotors having paddles located in contiguous relationship with respect to the walls of the chamber and a discharge opening in the housing.

Abstract: A cyclone separator having a central fluid conduit. An interceptor ring is externally attached to the end of the fluid conduit and has a surface which intercepts fluid flowing longitudinally along the outer surface of the fluid conduit and directs the fluid outwardly toward the interior wall of the container. Circumferential and longitudinal slots are located in the container in proximity to the interceptor ring to enhance the outward direction flow of fluid from the ring. A diffuser collar having a central opening therein is connected to the interceptor ring in a manner leaving an annular space or circumferential slots between the ring and the collar through which space unwanted materials.In an alternate version the diffuser collar is larger in diameter than the fluid conduit and the conduit extends into the diffuser collar forming a space therebetween by which an outer layer of fluid is skimmed from the spiraling column of fluid entering the fluid conduit to further cleanse the fluid of unwanted substances.