Class / Patent application number | Description | Number of patent applications / Date published |
095022000 | Gas flow rate modified | 40 |
20080196580 | Portable Oxygen Concentrator - A portable oxygen concentrator includes a reservoir adapted to store oxygen-enriched gas, a delivery valve adapted to communicate with the reservoir, a pressure sensor adapted to measure a reservoir pressure within the reservoir and to measure a pressure drop across the delivery valve, and an input device adapted to receive a pulse does setting. A controller coupled to the pressure sensor and monitors the reservoir pressure and the pressure drop across the delivery valve. The controller is also coupled to the delivery valve to selectively open the delivery valve for pulse durations based on the pulse dose setting to deliver pulses of gas from the reservoir to a user. The controller further adjusts the pulse durations based at least partially upon the reservoir pressure and the pressure drop across the delivery valve. | 08-21-2008 |
20080257145 | PRODUCT GAS CONCENTRATOR AND METHOD ASSOCIATED THEREWITH - Various equipment and methods associated with providing a concentrated product gas are provided. In one embodiment, the equipment includes an input device first and second sieve tanks, a variable restrictor, and a controller. In one embodiment, the method includes: a) selecting a desired output setting for the concentrated product gas from a plurality of output settings, b) separating one or more adsorbable components from a pressurized source gaseous mixture via first and second sieve tanks in alternating and opposing pressurization and purging cycles to form the concentrated product gas, and c) selectively controlling a variable restrictor based at least in part on the desired output setting to selectively provide flow between the first and second sieve tanks such that the flow for at least one output setting is different from the flow for at least one other output setting in relation to corresponding pressurization cycles. | 10-23-2008 |
20080271599 | Device and Method for Oxidizing, Reducing, Calcining, Sintering, or Melting Dusts - In a device for oxidizing, reducing, calcining, sintering or melting dusts such as, e.g., furnace or steel dusts, marl and lime dust mixtures, shredder light fractions, mineral dusts such as, e.g., glass dusts, cement kiln bypass dusts, dry sewage sludge, paper slurries or oil-containing grinding dust suspensions, using a dosing cyclone into which the dusts are charged and to which a tangential connector for feeding carrier gases is connected, and a combustion chamber following the dosing cyclone in the axial direction, wherein fuel and optionally additional carrier gas are injected into the combustion chamber coaxially with the discharge opening of the cyclone, a lance is arranged in the interior of the dosing cyclone, coaxially with the discharge opening of the dosing cyclone, for the introduction of liquid substances, substances dissolved in liquids or suspended in gases, or gaseous oxidizable substances and, in particular, fuels. According to the proposed method, the dosing cyclone is operated at a pressure reduced relative to the pressure prevailing in the fuel lance. | 11-06-2008 |
20090071327 | Filter System of an Electronic Equipment Enclosure - A filter system including a method for self cleaning the filter system of an electronic equipment enclosure where air flow is monitored either by monitoring fan performance of air flow velocity through the enclosure. The system includes two filters elements, an upstream ASHRAE or HEPA filter element to block particulate matter and a downstream PTFE filter element to block water vapor. The ASHRAE or HEPA filter element is relatively inexpensive and easy to clean. The PTFE filter element is more expensive and difficult to clean. Thus, the cheaper filter is used to protect the more expensive filter from contaminants and to increase its useful life. The method of self cleaning includes stopping the fan when a signal is received indicating a predetermined resistance to air flow which is a function of blockage of the filter elements, thereafter operating the fan at an increased rotational velocity to determine whether the fan itself is malfunctioning, thereafter slowing and stopping the fan to allow the fan to be reversed, rotating the fan in reverse for a predetermined period of time, such as five minutes, thereafter slowing and stopping the fan and returning the fan to its usual rotational velocity and direction. If the resistance to air flow is still above a predetermined level, the fan is again slowed, stopped and reversed and then returned to normal operation. The reversal operation can be conducted a multiple number of times, however, after a predetermined number, a signal is sent requesting maintenance | 03-19-2009 |
20090078116 | Adaptable dual-directional, differential pressure assembly - An adaptable dual direction, differential pressure assembly is disclosed. Solenoid valves release controlled bursts of air into a top of a container. A rate of the controlled bursts of air is partially responsive to a pressure differential between atmospheric pressure and that of compressed air in the reservoir. A pleated filter is fitted inside of the container. The pleated filter has an inner wall and an outer wall and has pleatings separated using hot melt glue beads there between. The controlled bursts of air are programmed to be substantially automatically responsive to one or more pressure differentials between an inner wall and an outer wall. In one embodiment, air is drawn from the blower through the pleated filter from the inner wall to the outer wall until a desired pressure differential is achieved. In yet another embodiment, air is drawn through the pleated filter from the outer wall into the inner wall and to draw upwardly out of the top of the container through the blower until a first pressure differential is achieved. | 03-26-2009 |
20090084261 | System for Controlling Flow Into Chromatographic Column Using Transfer Line Impedance - A system for controlling the flow rate into a chromatographic column is disclosed generally comprising communicating a fluid to the column through a transfer line, measuring the inlet pressure, determining the outlet pressure, and adjusting the applied pressure until the inlet and outlet pressures produce a desired flow rate for the transfer line outlet. In certain embodiments, the applied pressure is adjusted by controlling a proportional valve. In some embodiments, the outlet pressure is determined by measuring the pressure drop across the transfer line and calculating the outlet pressure from the measured inlet pressure and the pressure drop. | 04-02-2009 |
20090107329 | JET HOPPER - Apparatus for use in injecting powder materials into the flue gasses flowing through a baghouse compartment in conjunction with the performance of selected operating processes on the compartment fabric filters first entrains the powdered material into a pressurized fluid column to create a gaseous powder material plume that is injected into the flue gasses, thereby providing a more uniform entrainment of the powder materials into the flue gasses. | 04-30-2009 |
20090114088 | Inertial Gas-Liquid Separator with Variable Flow Actuator - An inertial gas-liquid separator has a variable flow actuator movable to open and close a variable number of accelerating flow nozzles. | 05-07-2009 |
20090126564 | DIAPHRAGM ACTUATED BLOW-BACK VALVE AND RESERVOIR - An accumulator having an internal valve opened by applying air pressure to a diaphragm with a small solenoid to apply air to the diaphragm where the air is supplied from a pilot air supply. When the internal valve operated by the diaphragm opens, it snaps to a fully open position thereby opening the valve and uncovering a passageway leading to a filter for cleaning. The passageway is sufficiently wide that the resulting flow of air through the passageway is so explosive that air pressure on the filter is distributed over the surface area of the filter for a brief moment, blowing the dust on the filter free. | 05-21-2009 |
20090211438 | Method of determining the purity of oxygen present in an oxygen-enriched gas produced from an oxygen delivery system - A method of determining the purity of oxygen present in an oxygen-enriched gas produced from an oxygen delivery system is disclosed. The oxygen delivery system includes at least one sieve bed having a nitrogen-adsorbing material disposed therein and configured to adsorb nitrogen from a feed gas introduced into the at least two sieve beds via a pressure-swing adsorption cycle. The method includes determining a quantity of nitrogen adsorbed by the nitrogen-adsorbing material by inferring an effective volume of the at least one sieve bed based on a pressure change of the at least one sieve bed. | 08-27-2009 |
20090293717 | METHOD AND APPARATUS FOR PRODUCING AND STORING OZONE USING ADSORBENT - The present invention provides a low-cost ozone production method and apparatus for carrying out ozone/oxygen separation using an ozone adsorbent, that re-uses the recovered oxygen as a feed for ozone production, and that desorbs and recovers the adsorbed ozone using dry air. In the method and apparatus, a gas containing an ozone and oxygen two-component gas supplied from an ozone generator is pressurized, introduced into an ozone adsorbent-packed adsorption column, and brought into contact with the adsorbent to adsorb the ozone to the adsorbent. Using dry air as a counterflow purge gas for the adsorbed ozone, the ozone is desorbed from the ozone adsorbent-packed adsorption column loaded with adsorbed ozone by depressurizing the adsorption column or air is introduced as a purge gas from the rear of the column into the adsorbent bed, whereby an ozone and air two-component gas is recovered. The method and apparatus use, as the ozone adsorbent, at least one selected from the group consisting of (1) pentasil-type zeolites, (2) acid-treated pentasil-type zeolites, (3) mesoporous silica, and (4) acid-treated mesoporous silica. | 12-03-2009 |
20100018390 | FUEL STORAGE TANK PRESSURE MANAGEMENT SYSTEM AND METHOD EMPLOYING A CARBON CANISTER - A carbon canister to adsorb hydrocarbons from a hydrocarbon air mixture in a UST system to prevent fugitive emissions due to overpressurization. The carbon canister has an inlet port at one end coupled to the UST system. An outlet port on the opposite end of the canister is connected to a flow-limiting orifice with a known calibrated flow rate that vents in a controlled fashion to the atmosphere. When UST pressure rises slightly above ambient pressure, fuel vapors and air from the UST system enters, via the inlet port, into the canister, where hydrocarbons are adsorbed onto the surface of the activated carbon. The cleansed air vents through the controlled flow outlet port to atmosphere, thereby preventing excessive positive pressure from occurring in the UST system. The activated carbon is purged of hydrocarbons by means of reverse air flow caused by negative UST pressures that occur during periods of ORVR vehicle refueling. | 01-28-2010 |
20100050867 | GAS TREATMENT APPARATUS, GAS TREATMENT METHOD, AND STORAGE MEDIUM - Disclosed is a gas treatment apparatus which can reduce the useless liquid quantity without using an expensive device, such as the evaporator or the mass flowmeter. The control mechanism performs control for exhausting the raw material storage container to make the raw material storage container have a predetermined vacuum pressure, stopping exhaustion to make the raw material storage container be in a sealed state, making the inside of the raw material storage container have the treatment gas atmosphere formed by gasifying the liquid raw material by the vacuum pressure within the raw material storage container, exhausting the chamber to make the chamber have a predetermined vacuum pressure in a state where the target substrate is received in the chamber, stopping the exhaustion to make the inside of the chamber be in a sealed state, opening the opening/closing valve to introduce the treatment gas from the raw material storage container to the chamber, and closing the opening/closing valve when the inside pressure of the chamber reaches a treatment pressure that is higher than the vacuum pressure and lower than a vapor pressure of the liquid raw material to make the chamber have the treatment gas atmosphere of the treatment pressure. | 03-04-2010 |
20100212492 | Horizontal Liquid/Gas Separation Device and Separation Method, Intended in Particular for the Liquid and Gas Phases of Crude Oil - A liquid/gas separator device for separating liquid and gaseous phases of a fluid, in particular crude oil, the device comprising a network of first and second separator pipes disposed horizontally, said first and second separator pipes being connected together by vertical link third pipes. The first separator pipes are fed from and connected upstream to a horizontal cylindrical diffuser and are connected downstream to a first horizontal cylindrical manifold. The second separator pipes are connected upstream to the same diffuser and downstream to a second horizontal cylindrical manifold. | 08-26-2010 |
20110017062 | FILTER WITH MEMORY, COMMUNICATION AND PRESSURE SENSOR - The present invention describes a system and method for accurately measuring the pressure within a filter housing. A pressure sensor and a communications device are coupled so as to be able to measure and transmit the pressure within the filter housing while in use. This system can comprise a single component, integrating both the communication device and the pressure sensor. Alternatively, the system can comprise separate sensor and transmitter components, in communication with one another. In yet another embodiment, a storage element can be added to the system, thereby allowing the device to store a set of pressure values. The use of this device is beneficial to many applications. For example, the ability to read pressure values in situ allows integrity tests to be performed without additional equipment. In addition, integrity testing for individual filters within multi-filter configurations is possible. | 01-27-2011 |
20110146485 | PROCESS GAS PURIFICATION DEVICE FOR A MELT REDUCTION SYSTEM FOR EXTRACTING PIG IRON - Process gas purification device ( | 06-23-2011 |
20110168017 | DEVICE AND METHOD FOR DEGASSING A LIQUID - Method and device for degassing a liquid of a substantially closed liquid circulation system at a working pressure. The method comprises passing at least a partial flow of the liquid through a restriction into a chamber in which a degassing pressure is maintained, the degassing pressure being higher than atmospheric pressure and lower than the working pressure, separating gas withdrawn from the partial flow of liquid from the partial flow, removing the gas from the chamber, and pumping the degassed partial flow of the liquid back into the substantially closed circulation system. The restriction comprises a nozzle, and the step of passing at least the partial flow of the liquid through the restriction into the chamber comprises spraying at least the partial flow of the liquid through the nozzle into the chamber for obtaining a jet and/or mist of the liquid in the chamber. | 07-14-2011 |
20110239860 | APPARATUS AND METHOD FOR CONTROLLING CONSTANT MASS FLOW TO GAS CHROMATOGRAPHY COLUMN - A device for providing a constant mass flow rate to a downstream column system of a gas chromatograph includes a small full scale mass flow controller that controls carrier gas to flow at a first mass flow rate and a flow resistance element, including an inlet port connected to a sample inlet, an outlet port connected to the downstream column system, and a pressure sensing port in fluid communication with the outlet port and the mass flow controller. A sample inlet pressure controller controls the sample inlet at a first pressure, and a pressure sensor measures a second pressure of the carrier gas at the pressure sensing port. A set point of the first pressure is determined as a function of the second pressure, flow resistance of the flow resistance element, and a second mass flow rate from the inlet port to the outlet port of the flow resistance element. | 10-06-2011 |
20110265644 | OXYGEN SUPPLY METHOD AND APPARATUS - A method and apparatus for supplying oxygen to meet a user demand in which oxygen is separated from air by an electrically driven oxygen separation device to supply oxygen to meet the user demand and to charge an adsorbent bed with all or part of the separated oxygen. When a user demand exists, oxygen can be supplied from both the electrically driven oxygen separation device and from oxygen desorbed from the adsorbent bed. | 11-03-2011 |
20110277630 | SYSTEMS AND METHODS FOR STARTING UP PRESSURE SWING ADSORPTION ASSEMBLIES AND HYDROGEN-PRODUCING FUEL PROCESSING SYSTEMS INCLUDING THE SAME - Systems and methods for initiating startup of PSA assemblies in hydrogen-processing assemblies, which may include a hydrogen-generation assembly and/or a fuel cell stack. The systems and methods include startup procedures that provide for pressurization of the adsorbent beds of the PSA assembly without the need for a stored quantity or other supply of purified hydrogen gas. The systems and methods additionally or alternatively include startup procedures that restrict or even prevent contamination of portions of the PSA assembly, hydrogen storage devices and/or accumulator tanks with an impure gas stream and/or decrease accumulation of the impure gas stream therein. This impure gas stream may be the mixed gas, reformate, or other gas stream that is intended to be purified by the PSA assembly when the PSA assembly is in its hydrogen-purifying operating state. | 11-17-2011 |
20120036997 | METHOD AND APPARATUS FOR SEPARATING A GASEOUS COMPONENT - In a method and an apparatus for separating at least one gaseous component from a waste gas of an installation for producing liquid pig iron, liquid primary steel products or sponge iron, in a first step, a stream of the waste gas passes through at least one adsorption separator at a first pressure, whereby the gaseous component is largely separated from the waste gas and, in a second step, the gaseous component is largely removed from the adsorption separator at a second pressure, which is lower than the first pressure. The method and apparatus are maintenance-free, cause low investment and energy costs and has a lower space requirement by a method in which the second pressure or the desorption pressure is generated by at least one jet pump, which is fed a stream of a propellant gas at a third pressure, which is higher than the second pressure. | 02-16-2012 |
20120227581 | Air Sampling Apparatus and Method - A sampling system includes a collection module including a gas handler, and a flow controller in communication with the gas handler of the collection module. The flow controller controls the gas handler to move a selected volume of gas through the collection module. | 09-13-2012 |
20130032028 | METHOD FOR OPERATING GAS SEPARATION DEVICE - Provided are a method for operating a gas separation device capable of performing gas separation with high separation capability and treatment amount in a small membrane area or in a small number of separation membrane modules, and a method for recovering a residual gas capable of performing more suitable detoxifying treatment or recycling by efficiently separating and recovering a mixed gas remaining in a cylinder, using the operating method. Two or more separation membrane modules are connected with each other in parallel. One separation membrane module is continuously and repeatedly operated in an operation cycle including: a first process for supplying a mixed gas into an airtight container and filling the airtight container with pressure; a second process for, when a predetermined time has elapsed or a predetermined pressure has been reached, stopping the supply of the mixed gas and retaining the supplied mixed gas; a third process for, when a predetermined time has elapsed or a predetermined pressure has been reached, recovering the mixed gas from a non-permeated gas discharge port; and a fourth process for, when a predetermined time has elapsed or a predetermined pressure has been reached, closing the non-permeated gas discharge port. The other separation membrane modules are operated in operation cycles shifted by respective predetermined intervals. | 02-07-2013 |
20130239803 | System and Method For Air Replacement and Positive Air Pressure Isolation - A method for reducing airborne contamination within a home includes installing an air-pressure control system within a window of the home, and drawing air from outside the home through the system inlet and an airflow path through the system. As it passes through the airflow path, a germicidal radiation chamber with a UV light source sterilizes the air. Additionally, filter(s) may clean the drawn air by removing particulates from the air as it passes through the filter. The method may then introduce the sterilized/cleaned air into the home through the system outlet. The sterilized/cleaned air may displace an equal volume of contaminated air within the home. | 09-19-2013 |
20130291718 | APPARATUS FOR CONCENTRATING AND DILUTING SPECIFIC GAS AND METHOD FOR CONCENTRATING AND DILUTING SPECIFIC GAS - One ozone concentrating chamber is provided therein with a part of a cooling temperature range where ozone can be selectively condensed or an oxygen gas can be selectively removed by transmission from an ozonized oxygen gas, and a part of a temperature range where condensed ozone can be vaporized, and condensed ozone is vaporized by moving condensed ozone with flow of a fluid or by gravitation to the part where condensed ozone can be vaporized, whereby the ozonized oxygen gas can be increased in concentration. Such a constitution is provided that a particle material | 11-07-2013 |
20140130666 | PURIFICATION ARRANGEMENTS AND METHODS FOR GAS PIPELINE SYSTEMS - A purification arrangement for a gas pipeline system includes a pressure vessel and at least first and second purification assemblies in the interior of the pressure vessel. An openable/closable barrier is positioned in the pressure vessel between the first and second purification assemblies. A gas flow may be established through the pressure vessel, and the gas may pass through the first purification assembly, the open barrier, and the second purification assembly to remove liquid and/or solid particulates from the gas. | 05-15-2014 |
20140216250 | DEGASSING MODULE FOR A CONTROLLED COMPLIANT FLOW PATH - A degassing module for removal of air and other gases during operation of a medical therapy device that delivers any one of hemodialysis, hemodiafiltration and hemofiltration. The degassing module has a flow-through first chamber that has a hydrophobic vent membrane that has an exterior and interior side forming a portion of the flow-through chamber. The hydrophobic vent membrane is positioned at a higher elevation on the flow-through chamber than a fluid outlet. Fluid flows through the flow-through chamber in a downward direction relative to the hydrophobic vent membrane. A flow-through chamber has a cross sectional area configured to provide for a downward flow velocity of the fluid to be less than the upward rise velocity of a smallest bubble to be removed from the fluid. | 08-07-2014 |
20140251130 | PRODUCT GAS CONCENTRATOR AND METHOD ASSOCIATED THEREWITH - Various equipment and methods associated with providing a concentrated product gas are provided. In one embodiment, the equipment includes an input device first and second sieve tanks, a variable restrictor, and a controller. In one embodiment, the method includes: a) selecting a desired output setting for the concentrated product gas from a plurality of output settings, b) separating one or more adsorbable components from a pressurized source gaseous mixture via first and second sieve tanks in alternating and opposing pressurization and purging cycles to form the concentrated product gas, and c) selectively controlling a variable restrictor based at least in part on the desired output setting to selectively provide flow between the first and second sieve tanks such that the flow for at least one output setting is different from the flow for at least one other output setting in relation to corresponding pressurization cycles. | 09-11-2014 |
20140366721 | SELF-REGULATING FILTRATION SYSTEM FOR WELD SMOKE - A process and system for ventilation of welding smoke including an air passage configured to receive smoke from a welding environment, wherein said air passage has an inlet and an outlet and said inlet is positioned adjacent to said welding environment. The system also includes a filter coupled to the air passage, wherein the filter comprises filter media that exhibits a burst strength of up to 20″ w.g., an initial resistance in the range of 0.3″ w.g. to 1.5″ w.g., an air flow in the range of 1,000 cubic feet per minute to 2,500 cubic feet per minute and a removal efficiency of greater than 50% for particles having a diameter of 0.3 μm to 10.0 μm. | 12-18-2014 |
20140373711 | Fluid Trap and Method of Separating Fluids - A fluid trap apparatus includes an inlet configured to receive a flow of composite fluid into the apparatus. The composite fluid contains at least a first fluid and a second fluid. An outer wall defines an interior chamber. A flow diffuser is interposed within the interior chamber. The flow diffuser directs the flow of the composite fluid to circulate through the interior chamber. The first fluid and the second fluid separate as the composite fluid circulates through the interior chamber. A method of separating a first fluid from a second fluid includes introducing a flow of composite fluid into a separate chamber. A pressure gradient is created within the separation chamber. A flow diffuser is interposed in a flow path between an inlet and an outlet. The flow diffuser directs the flow of the composite fluid within the separation chamber. The first fluid and the second fluid are separated. | 12-25-2014 |
20150040757 | AIRFLOW MANAGEMENT FOR LOW PARTICULATE COUNT IN A PROCESS TOOL - A method of providing airflow management in a substrate production tool includes providing a first mechanism coupling the substrate production tool to a fan filter unit. The fan filter unit provides filtered air to the substrate production tool. A second mechanism couples the substrate production tool to a reduced pressure exhaust mechanism. The reduced pressure exhaust mechanism provides an exhaust for excess gas flow within the substrate production tool. A substrate process area of the substrate production tool is maintained at a lower pressure than a pressure of a substrate transfer section of the substrate production tool. The substrate process area maintains a higher pressure than a pressure of the reduced pressure exhaust mechanism. The substrate transfer section maintains a higher pressure than the pressure of the reduced pressure exhaust mechanism. | 02-12-2015 |
20150047502 | Device and Method for Separating Gases - A device for separating gases comprises the following components: a source for the gases and flow adjustment means; a membrane unit for the production of a permeate gas and a retentate gas, one of which is the product gas; purity determining means for the product gas; a first control unit for the device; a retentate control system and a product gas pressure measurement, whereby the source has a second control unit for the flow adjustment means as a function of a target value of the gases and the first control unit is connected to the second control unit and to the retentate control system, whereby the first control unit can determine the target value and can control the retentate control system. | 02-19-2015 |
20150068396 | SYSTEM AND METHODS FOR REMOVING CONTAMINANTS FROM GAS EFFLUENTS - The present invention is directed to apparatuses and methods for pollution abatement. One embodiment provide methods of eliminating pollutants from an incoming optionally high temperature gaseous effluent stream, each method comprising directing the gaseous effluent stream sequentially through: (a) a sufficient volume of an aqueous liquid in a thermal shock vessel, such that the temperature of the gaseous effluent stream exiting the volume of liquid is in a range of about 5° C. to about 30° C., said liquid acting as filter to remove water, particles, soluble organic species, or a combination thereof from the gaseous stream; and one or more of: (b) an electronic bombardment module wherein the gaseous stream is ionized, forms molecular agglomerates, or both; (c) a magnetic rearrangement module, operating with a magnetic field in a range of about 0.5 to about 3 milliteslas; and (d) an electrostatic filter; so as to provide a pollution-reduced gas stream; wherein the optionally high temperature gaseous effluent stream initially contains impurities which include aromatic and non-aromatic hydrocarbons, carbon dioxide, carbon monoxide, oxides of nitrogen, oxides of sulfur, fluorocarbons or fluoroethers, or any combination thereof, along with high levels of humidity, solid or liquid particles, soluble or non-soluble organic species, or a combination thereof. | 03-12-2015 |
20150290560 | METHOD AND SYSTEM FOR FLUID SEPARATION WITH AN INTEGRATED CONTROL SYSTEM - A system for separating an input fluid flow comprising gas and liquid into separate gas and liquid flows, the system comprising: a primary inline separator configured to receive said input fluid flow and to separate said input fluid flow into a primary separator liquid output flow and a primary separator gas output flow; at least one secondary inline separator connected downstream from said primary inline separator to receive at least one of said primary separator output flows and to separate said received primary separator output flow into a secondary separator liquid output flow and a secondary separator gas output flow; a system gas outlet connected to at least one of said primary and secondary separators to output said respective gas output flow; a system liquid outlet connected to at least one of said primary and secondary separators to output said respective liquid output flow; and a control system configured to regulate flow through said primary and secondary separators to ensure a flow of gas from said gas output with a maximum amount of liquid carry-over and a flow of liquid from said liquid outlet with a maximum amount of entrained gas. | 10-15-2015 |
20160023155 | Apparatus and System Having a Valve Assembly and Swing Adsorption Processes Related Thereto - Provided are apparatus and systems having a lessened pulsation through the use of a pulse flow control mechanism. In performing a cyclical swing adsorption process, various streams are passed through adsorbent bed units during various steps in the swing adsorption process. The pulse flow control mechanism is utilized within a manifold of one of the streams to lessen pulsation within the manifold that results from performing the various steps. | 01-28-2016 |
20160096131 | REGULATED VACUUM OFF-GASSING OF GAS FILTER FOR FLUID PROCESSING SYSTEM AND RELATED METHODS - A method for filtering a gas includes sparging a gas through a liquid within a compartment of a container. In one embodiment the container can comprise a flexible bag. The sparged gas is passed from the container through a gas filter of a filter assembly. A partial vacuum is applied to the gas filter so that the partial vacuum assists in drawing the gas through the gas filter. | 04-07-2016 |
20160151741 | WATER REMOVAL DEVICE FOR GAS SAMPLING, AND METHOD AND SYSTEM | 06-02-2016 |
20160175740 | PURGE SYSTEM FOR CHILLER SYSTEM | 06-23-2016 |
20160184762 | LOAD FOLLOWING SINGLE BED REVERSING BLOWER ADSORPTION AIR SEPARATION SYSTEM - An exemplary single bed reversing blower adsorption based air separation unit is configured to follow the O | 06-30-2016 |
20160184763 | METHOD AND SYSTEM FOR HIGH RELIABILITY OXYGEN SUPPLY FROM MULTIPLE UNITS - A multi-unit system combines multiple single bed reversing blower vacuum swing adsorption air separation units together. The units feed a common O | 06-30-2016 |