Abstract: An in-treatment room dental vacuum system includes a vacuum producer and an operator tool including an evacuator tip. A separator is coupled with the vacuum producer and is disposed between the vacuum producer and the operator tool. A hose assembly connects the operator tool and the separator. In use, the separator receives material from the operator tool via the hose assembly and separates the material into wet phase material and dry phase material.

Abstract: An in-treatment room dental vacuum system includes a vacuum producer and an operator tool including an evacuator tip. A separator is coupled with the vacuum producer and is disposed between the vacuum producer and the operator tool. A hose assembly connects the operator tool and the separator. In use, the separator receives material from the operator tool via the hose assembly and separates the material into wet phase material and dry phase material.

Abstract: A vacuum-strength measurement device is utilized to determine vacuum producer system performance specifications and system parameters. A flow ability factor can be determined that represents the effect of system piping and usage area equipment on performance. With the flow ability factor, a vacuum strength requirement can be determined to effect a target vacuum performance. For system design, design parameters can be established based on a relationship between a desired flow ability factor and an amount of vacuum strength required to match target vacuum performance.

Abstract: A lighting assembly for use in direction and guidance systems includes an elongated insulating base upon which one or more light emitting diode strips, each supporting a plurality of light emitting diodes, are positioned. A terminal housing supporting operative power systems and control apparatus is coupled to one end of the lighting assembly while the remaining end may be coupled to an end cap or connected to a further lighting assembly to increase the array size. The light emitting diodes are covered by a light transmissive material that provides physical and weather protection for the light emitting diodes.

Abstract: A lighting strip for use in direction and guidance systems includes an elongated insulating base upon which one or more light emitting diode strips each supporting a plurality of light emitting diodes are positioned. A terminal housing supporting operative power systems and control apparatus is coupled to one end of the lighting strip while the remaining end may be coupled to an end cap or connected to a further lighting strip to increase the array size. The light emitting diodes are encapsulated within a light transmissive material top cover to provide physical protection and seal for the light emitting diodes.

Abstract: A lighting strip for use in direction and guidance systems includes an elongated insulating base upon which one or more light emitting diode strips each supporting a plurality of light emitting diodes are positioned. A terminal housing supporting operative power systems and control apparatus is coupled to one end of the lighting strip while the remaining end may be coupled to an end cap or connected to a further lighting strip to increase the array size. The light emitting diodes are encapsulated within a light transmissive material top cover to provide physical protection and seal for the light emitting diodes.

Abstract: Amalgam and other particles of four microns or more in size are removed with at least 95% efficiency from a particle-containing fluid line, preferably connected to a single dental operatory. Desirably a plurality of parallel centrifugal separators have their inlets connected to the fluid line, and gas outlets connected to a dental vacuum pump. The bottom liquid and particle outlet drains to a particle filter. The filtered water can be reintroduced into the gas flow to the vacuum pump, and the collected particles are disposed of in an environmentally sound manner.

Abstract: A method and apparatus provide for testing the useful vacuum of a dental vacuum system having at least one high volume evacuator valve (HVE) or hose. The vacuum tester is simple, inexpensive, can be used by non-technical personnel, is easily fabricated to test a wide range of performance standards, and evaluates useful vacuum performance during full flow (that is a real-life situation). The tester includes two simple components, an adaptor tube that is placed into contact with an HVE or hose, and a vacuum indicating weight which cooperates with the adaptor tube. With the dental vacuum system operating the weight is brought into position with respect to the tube so that gravity acts to move the weight away from the tube, and then the weight is released. If the weight moves away from the tube the useful vacuum conditions of the dental vacuum system are insufficient, whereas if the weight stays in operative position with respect to the tube the useful vacuum conditions are sufficient.

Abstract: An oil reclamation system flow meter for measuring the flow rate of a oil through the system wherein a housing forms a first chamber that leads through a constricted lower outlet into a second chamber and the second chamber. The first chamber also includes an intermediate outlet above the lower outlet and an upper outlet above the intermediate outlet. Both the intermediate and upper outlets flow into a duct that opens into the second chamber at a lower end. Oil flows through an inlet into the first chamber and through the lower outlet when the rate is below an ideal rate range, through both the lower outlet and the intermediate outlet when the rate is within the ideal range and through all three outlets when the rate exceeds the ideal range. A viewing conduit indicates the level of oil inside the first chamber and thereby indicates flow rate.

Abstract: A core plug apparatus includes an outer wall, an inner hub, a middle strengthening ring, and a plurality of interconnecting vanes. A vacuum seal wall covers one end of the plug to enable a vacuum lift force to be generated at one end of the roll of material. The vacuum seal wall includes a relatively thin central portion which can be displaced to allow the roll to be installed on a pair of mandrels, or to transport the roll using a rod extending from a lift device. The outer surface of the core plug may be textured to further increase frictional forces between the core plug and the inside wall of the core.

Abstract: A process for recovery of molybdenum from residual fractions derived from an epoxidation reaction of propylene with tertiary butyl hydroperoxide in liquid phase with tertiary butyl alcohol, in the presence of soluble molybdenum, which process comprises:Fractionating epoxidation reaction product for obtaining a liquid fraction containing essentially all molybdenum from the reaction product;Contacting the liquid fraction with anhydrous ammonia for forming a precipitate containing the major portion of the molybdenum and a liquid phase containing 500 ppm or less molybdenum;Separating the liquid phase from the precipitated solid;Evaporating the liquid phase under conditions of elevated temperatures and reduced pressure in the presence of 1 to 3% water for separation into an evaporator overhead vapor essentially free of molybdenum and an evaporator concentrate comprising essentially all of the molybdenum fed to the evaporator;Rapidly cooling evaporator concentrate from about evaporation temperature to about room te

Abstract: A process for recovery of molybdenum from residual fractions derived from an epoxidation reaction of propylene with tertiary butyl hydroperoxide in liquid phase with tertiary butyl alcohol, in the presence of soluble molybdenum, which process comprises:Fractionating epoxidation reaction product for obtaining a liquid fraction containing essentially all molybdenum from the reaction product;Contacting the liquid fraction with anhydrous ammonia for forming a precipitate containing the major portion of the molybdenum and a liquid phase containing 500 ppm or less molybdenum;Separating the liquid phase from the precipitated solid;Evaporating the liquid phase under conditions of elevated temperatures and reduced pressure in the presence of 1 to 3% water for separation into an evaporator overhead vapor essentially free of molybdenum and an evaporator concentrate comprising essentially all of the molybdenum fed to the evaporator;Rapidly cooling evaporator concentrate from about evaporation temperature to about room te

Abstract: A dental vacuum assembly utilizes a rotary vane vacuum pump. The pump is operatively connected to a vacuum reservoir and driven by an electric motor commonly mounted with the pump on a vibration-isolated platform. The vacuum reservoir is operatively connected to a number of different dental stations, each including a dental aspirator tip. The vacuum reservoir is supported by a support component which receives a drain valve in the bottom of the vacuum reservoir, and has a false bottom connected to a drain pipe section which extends through a side wall of the support component for easy connection to a sewer.

Abstract: Impure propylene oxide is purified by a distillation process wherein it is (a) extractively distilled in a first column using a C.sub.2 to C.sub.6 alkylene glycol extractive distillation agent to form a first overhead fraction comprising propylene oxide, C.sub.5 -C.sub.7 hydrocarbons methanol, water and oxygen-containing impurities, (b) wherein the first overhead fraction is separated in a second column into a second overhead fraction comprising most of the pentanes, pentenes and oxygen-containing impurities and a partially purified propylene oxide bottoms fraction comprising propylene oxide, hexenes, hexanes, and only residual quantities of pentenes and pentanes, (c) wherein the partially purified bottoms fraction is extracting distilled in a third column using a C.sub.7 -C.sub.

Abstract: An organic solution of a soluble molybdenum compound is ammonated with ammonia, ammonium hydroxide and/or an ammonium salt in order to significantly reduce the electrical resistance of the solution and a direct electric current is passed therethrough in order to collect a significant amount of the molybdenum in solid form at the negative electrode.

Abstract: In the preparation of tertiary butyl alcohol and a linear C.sub.3 -C.sub.12 mono epoxide by the epoxidation reaction of a linear C.sub.3 -C.sub.12 alpha mono olefin with tertiary butyl hydroperoxide in solution in tertiary butyl alcohol in the presence of a catalytic amount of a soluble complex of molybdenum with ethylene glycol, a portion of the catalyst that is used is a recycle (final) ethylene glycol solution of a complex of ethylene glycol with ammonium-containing molybdenum compounds prepared from ethylene glycol and a precipitate of solid ammonium-containing molybdenum compounds formed by saturating a heavy distillation fraction with ammonia to thereby form a liquid amination product containing a precipitate of solid ammonium-containing molybdenum compounds; the heavy distillation fraction being obtained by distillation of the epoxidation reaction product.

Abstract: The distillation product fraction obtained from an isobutane oxidation reaction product after the removal of unreacted isobutane will contain tertiary butyl hydroperoxide, tertiary butyl alcohol and carboxylic acid contaminants such as formic acid, acetic acid and isobutyric acid. It has been discovered that when the distillation product fraction is treated with about 1/2 to 1 equivalents of calcium oxide and/or calcium hydroxide based on the carboxylic acid content of the distillate product fraction, a portion of the carboxylic acid contaminants will precipitate thus partially purifying the distillation product fraction so that, thereafter, molybdenum precipitation will be substantially inhibited when the thus-treated distillation product fraction is used as a feedstock for an epoxidation reaction wherein tertiary butyl hydroperoxide is reacted with an olefin in the presence of a soluble molybdenum catalyst to provide an olefin epoxide and additional tertiary butyl hydroperoxide.

Abstract: Purified propylene oxide is recovered from an impure propylene oxide feedstock contaminated with more than 50 ppm of six carbon atom hydrocarbon impurities by a solvent extraction process wherein:an impure propylene oxide feedstock is charged to a liquid/liquid extraction zone and contacted therein with an extractant consisting essentially of water and a paraffinic hydrocarbon containing 8 to 10 carbon atoms, and resolved therein into a raffinate consisting essentially of an aqueous solution of propylene oxide and into an extract comprising the paraffinic hydrocarbon and the 6 carbon atom impurities initially present in the propylene oxide feedstock.

Abstract: An epoxidation reaction product formed by the molybdenum catalyzed reaction of propylene with tertiary butyl hydroperoxide to provide propylene oxide and tertiary butyl alcohol is separated by distillation into a propylene fraction, a propylene oxide fraction, a tertiary butyl alcohol fraction and a heavy liquid distillation fraction composed primarily of tertiary butyl hydroperoxide, tertiary butyl alcohol, dissolved molybdenum catalyst, and impurities including lower aliphatic C.sub.1 -C.sub.4 carboxylic acids, and the heavy liquid distillation fraction is saturated with hydrogen to precipitate the molybdenum therefrom for recovery.

Abstract: Methyl formate is removed from impure propylene oxide by contacting the impure propylene oxide in a treating zone with a basic ion exchange resin for a period of time sufficient to convert the methyl formate to formic acid and methanol, and by withdrawing a substantially methyl formate-free treated propylene oxide product from the treating zone.