Abstract: A raw material gas supply apparatus is configured to obtain a difference between a set value and a measured value of a vaporized raw material, add the difference as a correction value to the set value of the flow rate of the carrier gas to maintain an amount of the vaporized raw material at the set value, and subtract a difference from a set value of a flow rate of the dilution gas to maintain a total flow rate of the carrier gas and the dilution gas at a constant level. The amount of the vaporized raw material is calculated by subtracting an integration value of a measured value of the flow rate of the inert gas in the supply period of the raw material gas from an integration value of the flow rate of the raw material gas which is measured in the supply period.

Abstract: A method comprises transporting a first stream of a carrier gas to a delivery device that contains a solid precursor compound. The first stream of carrier gas is at a temperature greater than or equal to 20° C. The method further comprises transporting a second stream of the carrier gas to a point downstream of the delivery device. The first stream and the second stream are combined to form a third stream, such that the dewpoint of the vapor of the solid precursor compound in the third stream is lower than the ambient temperature. The flow direction of the first stream, the flow direction of the second stream and the flow direction of the third stream are unidirectional and are not opposed to each other.

Abstract: A method comprises transporting a first stream of a carrier gas to a delivery device that contains a solid precursor compound. The first stream of carrier gas is at a temperature greater than or equal to 20° C. The method further comprises transporting a second stream of the carrier gas to a point downstream of the delivery device. The first stream and the second stream are combined to form a third stream, such that the dewpoint of the vapor of the solid precursor compound in the third stream is lower than the ambient temperature. The flow direction of the first stream, the flow direction of the second stream and the flow direction of the third stream are unidirectional and are not opposed to each other.

Abstract: A method of supplying and controlling the flow of a process gas to a process chamber. The method includes initiating a known flow rate of a process gas to a process chamber, dividing the known flow rate of the process gas into a first flow of the process gas at a first flow rate and a second flow of the process gas at a second flow rate, measuring a first pressure associated with the first flow of the process gas, measuring a second pressure associated with the second flow of the process gas, and controlling the first flow rate and the second flow rate according to a target flow condition by adjusting a first conductance of the first flow of the process gas and a second conductance of the second flow of the process gas and monitoring the first pressure and the second pressure.

Abstract: An embodiment of the present invention is a method for creating and maintaining a partial vapor pressure in a sample chamber of a sorption analyzer. A first dry gas flow is purged from a first mass flow controller through a saturator to produce a near-saturated gas flow. The near-saturated gas flow is mixed with a second dry gas flow from a second mass flow controller to produce a mixed gas flow with a predetermined partial vapor pressure. The mixed gas flow is directed into the sample chamber. If the lowest possible vapor pressure is required in the sample chamber, the first dry gas flow is directed around the saturator to the sample chamber and vapor migrating from the saturator is vented to the atmosphere.

Abstract: A method is provided for controlling superheating and temperature of a compressed natural gas stream and the addition of a corrision inhibitor composition for transmission through a pipeline that includes: a. dividing a stream of natural gas discharged from a high pressure gas compressor (106) into a first portion (108) and a second portion (202); b. passing the first portion (108) of the gas from the gas compressor to a heat exchanger (112) to heat the gas to a predetermined temperature; c. passing the first portion of gas (111) exiting the heat exchanger to an aftercooler (114); d. passing the second portion (202) of natural gas discharged from the gas compressor (106) to the aftercooler (114) without passing it through the heat exchanger (112), the second portion of gas and the first portion of gas being mixed at the aftercooler inlet and cooled by the aftercooler and discharged from the aftercooler as a cooled gas stream (116) having a temperature no greater than a first temperature; e.

Abstract: A fluid multiplexer includes a manifold having a plurality of fluid conduits formed therein, a fluid input and a plurality of fluid connection points located on the manifold and fluidically coupled together via the fluid conduits, and a flow control module coupled to the fluid connection points, the flow control module configured to provide a plurality of blocking flows to the manifold to control the flow of a primary fluid through the fluid conduits.

Abstract: The invention relates to a device and a method for distributing two liquids that cannot be mixed with each other for mass transfer and heat exchange columns, comprising at least one distributor channel or a distributor channel arrangement, the distributor channel being fed one or more liquids in different phases via at least one inflow from a collecting device arranged above said distributor channel, and said distributor channel having overflow and/or outflow openings for the distribution of the liquids. The device according to the invention is distinguished by the fact that the distributor channel has at least one internal means for the phase separation of the liquid and that separate outflow and/or overflow openings are provided for each of the phases to be separated, the cross section and/or elevation of which openings are arranged in dependence on the physical properties of the liquids in such a way that a homogeneous distribution of the liquids on the basis of predetermined phase components is achieved.

Abstract: Microfluidic devices capable of combining discrete fluid volumes generally include channels for supplying different fluids toward a sample chamber and means for establishing fluid communication between the fluids within the chamber. Discrete fluid plugs are defined from larger fluid volumes before being combined. Certain embodiments utilize adjacent chambers or subchambers divided by a rupture region such as a frangible seal. Further embodiments utilize one or more deformable membranes and/or porous regions to direct fluid flow. Certain devices may be pneumatically or magnetically actuated.

Abstract: Methods and devices for delivering fluids into microfluidic device body structures are described. The methods and devices include the use of fluid manifolds which are integrated or interchangeable with device body structures. Methods of fabricating manifolds are also provided.

Abstract: A method and system are shown for protecting the threaded ends of tubular goods such as oil field tubulars from physical damage and corrosion due to environmental factors. A thread protector is formed of a polymeric body having cylindrical wall portions which engage the threaded ends of the tubular goods. Instead of relying upon a separate thread compound or corrosion inhibitor applied to the exposed threads, the polymeric body has incorporated therein a corrosion inhibiting compound, which is blended within the polymeric body as a part of the manufacturing process used to mold the polymeric body. The thread protector of the present disclosure includes a weather barrier to minimize exposure of the threaded ends of the tubular goods to moisture and other contaminants. The weather barrier includes a weather barrier ring and an air vent.

Abstract: A solid chemical feed system, preferably including two feed bowls, comprises a quantity of solid chemicals that dissolve upon immersion in water to form a liquid solution. A sump is provided to receive liquid solution from the feed bowls, the liquid solution with additive chemicals being used as a treatment for cooling towers, boilers, or other industrial processes to inhibit corrosion and rust. The feed system comprises a valve system that is controlled by a sensor that detects the conductivity of the liquid solution to alternatingly switch the introduction of liquid solution from one feed bowl to the other feed bowl. As such, upon depletion of chemical feed in one bowl, desired treatment will continue and the empty bowl may be replaced without disruption of liquid solution supply.

Abstract: A bottom outlet valve for a tank car having a bottom is provided. The valve includes a nozzle projecting from the bottom of the tank car and defining an opening and having a locking member, an outlet cap shaped and dimensioned to cover the opening and moveable between open and closed positions, wherein in the closed position the cap forms a substantially liquid-tight seal with the opening. The valve also includes at least one moveable handle coupled to the cap and having a locking portion engageable with the locking member and a hand gripping portion formed by structure defining a closed loop. Movement of the hand gripping portion causes engagement of the locking portion with the locking member, wherein when the locking member and locking portion are engaged, the outlet cap is retained in a closed position.

Abstract: A method of controlling the amount of conductivity increasing substances, e.g., free available halogen, in particular free available chlorine, present in an aqueous medium is described. In accordance with the method of the present invention, an aqueous medium is provided and its conductivity determined. A source of at least one conductivity increasing substance is introduced controllably into the aqueous medium, and a second conductivity measurement is made. The determined conductivities are compared, and in response to this comparison, the amount of conductivity increasing substance added to the aqueous medium is adjusted. In a preferred embodiment of the present invention, the aqueous medium is an aqueous stream, and the source of conductivity increasing substance is calcium hypochlorite, which is introduced into the aqueous stream through the use of a feeder unit, i.e., a chlorination unit.

Abstract: An installation for lubricating, cleaning and/or disinfecting conveyor belts for containers, more particularly for foods, such as bottles, glasses, cans, bags and the like, comprising a central metering station connectable to a water pipe used to dilute a concentrated lubricant, cleaner or disinfectant, and several distributing pipes connected to the metering station lead to the points of use. At each point of use there is a mixing valve (13-19) connectable to distribution line (52) and the water pipe (23) and individually adjustable for each point of use and a pressure reducer (50, 51) fitted upstream of each mixing valve. Varying concentration can be provided for each point of use (31-37) with little technical complexity. In another embodiment, the invention is the process carried out by the installation.

Abstract: A system and method for treating a fluid flowing along a main fluid supply path in which a streaming current detector receives a sample flow of a main fluid supply following main dosing with a chemical under control of a streaming current detector output. A secondary chemical dosing is applied to the sample under the control of the streaming current detector output in a feedback loop.

Abstract: An apparatus and method for facilitating the attainment of thermodynamic equilibrium and for measurement of interfacial tension of mixtures. A fixed volume chamber is connected at an upper end face and lower wall portion of the chamber to a first variable volume chamber and at a lower end face and upper wall portion of the chamber to a second variable volume chamber. Conduit valves and a valve controller control the flow of mixtures between the first and second variable volume chambers and the fixed volume chamber to selectively cause more dense component of the mixture to flow through less dense component of the mixture and less dense component of the mixture to flow through more dense component of the mixture, the flow through occurring within the fixed volume chamber.

Abstract: A readily cleaned liquid transfer system is designed for use with an associated vessel or container, such as a barrel, having therein a liquid to be removed. The system comprises a recirculation loop, a transfer manifold, and a transfer hose for providing flow communication between the transfer manifold and the recirculation loop. The transfer manifold has an inlet port which is located at about the bottom of the barrel, and an outlet port. The recirculation loop which has water flowing therethrough which is used as a diluent, also includes an eductor pump. The eductor pump hydrodynamically drives or draws the liquid in the barrel, through the transfer manifold and the transfer hose, into the recirculation loop. The recirculation loop discharges a blended product to a product tank.

Abstract: Method and apparatus for including within a carrier fluid to be utilized in different areas at least one additive in a constant predetermined concentration and at least one other additive in varying concentration depending on the particular area of use. For example, this invention allows various concentrations of one chemical such as a lubricant in a carrier liquid such as water to be delivered to selected different areas while maintaining a constant concentration of other chemicals such as chelates and the like in the carrier liquid. Thus, the invention lends itself to an apparatus and method of treating a plurality of zones of a processing line with a liquid, the liquid comprising a treatment liquid and a stock liquid in combination such as to maintain the concentration of one or more constituents constant while varying the concentration of one or more other constituents. The invention particularly concerns the lubricating of conveyors as in bottling lines and the like.

Abstract: To prepare a flow of gas at a high temperature of operation, a flow of gas which has previously been heated to a temperature much lower than the operating temperature is divided into two elementary flows, which are thereafter individually heated at higher temperatures, one of which is higher than the operating temperature and the other being lower than the operating temperature. The two flows thus differently heated are each sent to a buffer container which is heat insulated and two elementary gas flows are withdrawn from the containers and are thereafter combined in regulated proportion by means of a mixing valve adjusted at a control mixing position by means of a correcting signal which differentiates between the effective temperature of the gas prepared and a control temperature. Application for example to the manufacture of articles made of expanded foam material utilizing carbon dioxide.

Abstract: The inlet and outlet passages communicating with a water-cooled engine oil cooler for a vehicle, such as a motorcycle, are arranged for bypass of a regulated amount of oil from the inlet passage to the outlet passage to enhance the flowability of the cooled oil. Provision is made for a replaceable flow control orifice between the oil inlet and outlet passages to regulate oil viscosity. Also described is an arrangement providing for mounting the cooler to the crankcase or oil pan surface whereby air flowing past the cooler during movement of the vehicle assists the effects of the cooling liquid.

Abstract: A method and apparatus for diverting into a branch line a portion of a gas-liquid flow stream from a two-phase flow trunk line. Each of two or more takeoff pipes withdraw a two-phase portion of the trunk line flow stream and transmit it to a single common branch line. The takeoff pipes are oriented to produce branch line flow of predetermined quality. The quality of branch line flow may be monitored and control valves positioned in one or more takeoff pipes and in the branch line to facilitate branch line flow of variable quality and rate.

Abstract: A method and apparatus for diverting into a branch line a portion of a gas-liquid flow stream from a two-phase flow trunk line. Each of two or more takeoff pipes withdraw a two-phase portion of the trunk line flow stream and transmit it to a single common branch line. The takeoff pipes are oriented to produce branch line flow of predetermined quality. The quality of branch line flow may be monitored and control valves positioned in one or more takeoff pipes and in the branch line to facilitate branch line flow of variable quality and rate.

Abstract: The invention is a system for controlling the mass flow rates of vapor and carrier gas in a flowing fluid mixture. A regulated flow of carrier gas is divided so that a fraction of the flow passes through a vaporizer to pick up the vapor while the balance bypasses the vaporizer. The streams are then recombined and the resulting mixture is passed through a dew point detector which gives an output signal which varies according to variations in the mass ratio of the vapor to the carrier gas. A controller responds to the detector signal to generate a control signal which modulates a valve to vary the fraction of the carrier gas passing through the vaporizer, thereby influencing the mass rate at which the vapor is introduced. The feedback control from the dew point detector to the valve is adapted to regulate the dew point, and thereby the mass ratio of vapor to carrier.

Abstract: A system for controlling the silver ion concentration of a silver halide emulsion made by mixing alkali halide and silver nitrate solutions which are delivered continuously to a vessel at primary addition rates. The silver ion concentration in the vessel is measured to establish the deviation from a desired concentration. Where the error is within a limited or normal range, a low signal selector circuit causes a pump in a secondary flow loop to deliver a secondary amount of whichever solution is needed to offset the deviation. Where the error is abnormal, a high signal selector circuit alters the primary addition rate of the alkali halide solution to offset the deviation.