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And subsequent handling of evolved gas, stripping gas, or residue liquid

Subclass of:

095 - Gas separation: processes

095241000 - DEGASIFICATION OF LIQUID

Patent class list (only not empty are listed)

Deeper subclasses:

Class / Patent application numberDescriptionNumber of patent applications / Date published
095254000 And subsequent handling of evolved gas, stripping gas, or residue liquid 26
20100064892GAS/LIQUID SEPARATOR FOR HYDROGEN GENERATING APPARATUS - A gas liquid separator system for a hydrogen generating apparatus includes a collection area for collecting liquid from the generated gases. To empty the collection area occasionally so that liquid does not build up and become entrained again in the dried gas, a vent solenoid is provided in communication with the collection area and a pump is used to create a vacuum periodically on the electrolysis cells. Such arrangement is used to open the liquid gas filter and possibly just the sump to atmosphere occasionally and vacuum generated to draw the liquid from the sump back to the electrolysis cells.03-18-2010
20150059574Vented Gas Drilling Fluid Catch Apparatus - The present invention is directed to a catch tank for drilling operations. The catch tank is located between a mud-gas separator and a flare. The catch tank has an inlet port with a closed end baffle which allows a drilling fluid-gas mixture to be separated and gas to proceed to the flare without entrained drilling fluid.03-05-2015
095255000 Evolved gas removed by sweep gas 1
20160068421METHODS AND APPARATUS FOR CONTROLLED SCRUBBING AND AERATION OF LIQUID MEDIUM - An apparatus and method for controlled ventilation and aeration of liquid medium includes a dome supported by a flotation device, a lower housing supported by the flotation device, the lower housing connected to the dome, wherein a sealed space is defined under the dome and above the flotation liquid, one or more orifices, the orifices configured in the dome, and an aeration apparatus positioned within the sealed space and partially submerged in the flotation liquid, wherein the aeration apparatus comprises one or more parallel shafts, at least one first disc positioned axially on one of the shafts, at least one second disc positioned axially on another of the shafts, wherein the second disc is interleaved relative to the first disc, and wherein a surface of the first disc rotates in a direction opposite a surface of the second disc relative to each other resulting in a mixing area therebetween.03-10-2016
095256000 For indirect heat exchange 7
20120090467SEPARATION SYSTEM COMPRISING A SWIRL VALVE - The invention relates to a separation system comprising a flow inlet (04-19-2012
095257000 Gas condensed 6
20130087043Device and Method for Removing Volatile Substances From a Liquid Mixture - A device comprises a desorber unit having a carrier arrangement with an inlet and an outlet for the liquid mixture, wherein the cant-lien arrangement is designed such that the liquid mixture can be guided between inlet and outlet via a number of carriers, e.g., profiles, tubes or pipes, and form a flowing liquid film on the surface of the carriers, and a gas control with a gas inlet and a gas outlet, between which the gas can sweep past the liquid film, such that the at least one volatile substance can pass over from the liquid mixture into the gas. A condensation unit with a gas inlet connects to the gas outlet of the desorber unit. A heat exchanger cools gas passed through it, which comes from the desorber unit, such that the at least one volatile substance can be condensed from the gas. A fan is incorporated into a gas connection between the desorber unit and the condensation unit such that a gas stream through the device can be produced.04-11-2013
20130145934APPARATUS AND METHODS FOR REGENERATION OF PRECIPITATING SOLVENT - A regenerator that can handle rich loaded chemical solvent containing precipitated absorption reaction products is disclosed. The invention is particularly suitable for separating CO06-13-2013
20140190351SYSTEMS AND METHODS FOR REDUCING THE ENERGY REQUIREMENTS OF A CARBON DIOXIDE CAPTURE PLANT - Systems and methods for reducing the energy requirements for carbon dioxide capture are described. Heat from system processes, such as steam condensation and hot flue gas, is utilized to heat reflux liquid utilized in release of carbon dioxide from absorbent solvent.07-10-2014
20140251139METHOD FOR PROCESSING WASTEWATER AND EXHAUST GAS CONDENSATES FROM THE POLYMERIZATION OF VINYL ACETATE AND ETHYLENE IN AN AQUEOUS MEDIUM - A method for processing wastewater and exhaust gas condensates from the polymerization of vinyl acetate and ethylene and optionally other comonomers in an aqueous medium by suspension or emulsion polymerization employs relieving pressure after completion of the polymerization of the polymerization batch and discharging the polymer dispersion. During the relieving, the gaseous phase is removed by means of a compressor. Optionally, the gaseous phase occurring during stripping is removed by the compressor and cooled by one or more heat exchangers before entry into the compressor. The liquid phases occurring in the compressor and optionally in the heat exchanger are separated from the gaseous phase and the liquid phases are given to a rectification column, and separated into a vinyl acetate monomer phase and a wastewater phase, and the vinyl acetate monomer phase is resupplied to polymerization.09-11-2014
20160144295ENERGY EFFICIENT SOLVENT REGENERATION PROCESS FOR CARBON DIOXIDE CAPTURE - A process for removing carbon dioxide from a carbon dioxide-loaded solvent uses two stages of flash apparatus. Carbon dioxide is flashed from the solvent at a higher temperature and pressure in the first stage, and a lower temperature and pressure in the second stage, and is fed to a multi-stage compression train for high pressure liquefaction. Because some of the carbon dioxide fed to the compression train is already under pressure, less energy is required to further compress the carbon dioxide to a liquid state, compared to conventional processes.05-26-2016
20160193561SYSTEMS AND METHODS FOR REDUCING THE ENERGY REQUIREMENTS OF A CARBON DIOXIDE CAPTURE PLANT07-07-2016
095258000 Gas recycled or further separated 6
20120180661COMPACT INERTIAL GAS-LIQUID SEPARATION SYSTEM - A compact inertial gas-liquid separator including: a stratification mechanism including a first horizontal pipe and a second pipe having a larger diameter possibly slightly tilted with respect to the horizontal, for example of ≦10°, connected to each other by a suitable connection gate; a cylindrical body with a vertical development, on which the stratification mechanism is tangentially inserted, wherein the inertial gas-liquid separation is performed, in whose upper part an arrangement of finishing elements can be optionally inserted for further separation of drops of liquid entrapped in the gaseous stream; two outlets for the liquid stream and for the gaseous stream.07-19-2012
20120199000APPARATUS AND METHOD FOR GAS-LIQUID SEPARATION - A two phase gas-liquid separation apparatus is provided that shapes the flow in a flow shaping line. Shaping the two-phase flow allows centrifugal force to send the heavier, denser liquid to the outside wall of the flow shaping line and allows the lighter, less dense vapor or gas to occupy the inner wall of the flow shaping line. With the gas positioned on the inner wall of the flow shaping line, an exit port on the inner wall will allow for the majority, if not all, of the gas, along with a low amount of liquid, to be sent to a conventional separator. A high ratio of vapor/liquid at a flow rate much lower than the total flow rate within the flow shaping line is sent to the conventional separator. This allows for efficient separation of the vapor from the liquid with the use of a smaller conventional separator.08-09-2012
20140352538Spherical Separation Device and Method for Separation - The present invention relates to an apparatus for separation of high volume flows of mixtures provided with at least two immiscible phases, especially for the first separation steps of flows of water/oil/gas/sand mixture that enter the apparatus as a wellstream mixture. The invention also relates to a method for separation of high volume flows of mixtures provided with at least immiscible phases.12-04-2014
20150306522INLINE GAS LIQUID SEPARATION SYSTEM WITH A SHARED REJECT VESSEL - The present invention concerns a gas-liquid separation system and a method for operating a gas-liquid separation the system.10-29-2015
20160032720COLLECTING AND REMOVING CONDENSATE FROM A GAS EXTRACTION SYSTEM - A gas extraction system for gas analysis is provided. The gas extraction system includes the use of a peristaltic pump for moving condensates to a liquid trap assembly. An improved fluid flow is thus provided, which includes delivering condensate from a condensate separator to a peristaltic pump and delivering the condensate from the peristaltic pump to a liquid trap assembly.02-04-2016
20160082377DESANDING APPARATUS AND A METHOD OF USING SAME - An apparatus and method for removing particulates from a multiple-phase fluid stream is disclosed. The apparatus comprises a treatment chamber having a fluid inlet for receiving the multiple-phase fluid stream. The apparatus also comprises a recovery chamber having a gas channel and a liquid channel in fluid communication with the treatment chamber at a gas and a liquid port, respectively. The gas and liquid channels converge at an intake port of a fluid outlet for discharging particulate-removed gas and liquid.03-24-2016
095259000 Liquid further separated 10
20090133578METHOD FOR RECEIVING FLUID FROM A NATURAL GAS PIPELINE - A method for receiving fluid from a natural gas pipeline, the fluid comprising gaseous hydrocarbons, liquid hydrocarbons, water and optionally solids, the method comprising: (a) in a slug catcher (05-28-2009
20110023715METHOD FOR TREATING WASTEWATER OR PRODUCED WATER - A method or process for treating wastewater containing high organics, silica, boron, hardness, and suspended and dissolved solids. The method includes degasifying the wastewater for the removal of dissolved gases and thereafter chemically softening the wastewater. After the chemical softening step, the wastewater is directed through a media filter or membrane which removes additional solids and precipitants. Thereafter the wastewater is directed through a sodium ion exchange that further softens the wastewater. The effluent from the ion exchange is directed through a cartridge filter and the effluent from the cartridge filter is directed through one or more reverse osmosis units. At a selected phase of the process, prior to the wastewater reaching the reverse osmosis unit or units, the pH of the wastewater is raised and maintained such that the pH of the wastewater reaching a reverse osmosis unit is at a pH greater than 10.5.02-03-2011
20110168021SETTLING DEVICE, PURIFIER COMPRISING A SETTLING DEVICE AND METHODS FOR ANAEROBIC OR AEROBIC PURIFICATION OF WASTE WATER - A three phase separator or settling device (07-14-2011
20120085236TREATMENT OF WATER FOR USE IN HYDRAULIC FRACTURE STIMULATION - A process and process line for treating water containing hydrogen sulfide for use as a hydraulic fracturing fluid is provided, to practice the following steps: separating a gaseous portion containing hydrogen sulfide from the water to form a first degassed water product; introducing the first degassed water product into a mechanical gas stripping unit and treating the first degassed water product with a stripper gas; recovering from the mechanical gas stripping unit at least one overhead vapor stream containing hydrogen sulfide and a stripped water stream as a bottom stream; degassing the stripped water stream in a degassing tank to produce a second degassed water product; and treating the second degassed water product with a hydrogen sulfide scavenger to produce a sweet water product having substantially reduced hydrogen sulfide.04-12-2012
20120137883METHOD FOR RECOVERING GAS FROM SHALE RESERVOIRS AND PURIFYING RESULTING PRODUCED WATER TO ALLOW THE PRODUCED WATER TO BE USED AS DRILLING OR FRAC WATER, OR DISCHARGED TO THE ENVIRONMENT - A system and method for removing gas from a gas producing subterranean formation and removing contaminants from the produced water is provided. The method includes providing a mixture of gas and water gathered from a gas producing well. Thereafter the method entails separating the gas from the mixture to produce a gas product and the produced water which includes organics, suspended solids and dissolved solids including silica. Thereafter, suspended solids are removed from the produced water. After removing some of the suspended solids, the produced water is directed to a micro porous polymer extraction (MPPE) unit. In the MPPE unit aromatic organic compounds are removed from the produced water. Thereafter the produced water is treated in a membrane bioreactor to remove additional organics. Thereafter the produced water is directed to at least one RO unit that produces a high dissolved solids containing reject stream and a low dissolved solids permeate stream. The method or process described reduces the concentration of certain contaminants in the produced water such that the output or permeate stream from at least one RO unit can be used for frac fluid, drilling mud, or discharged to the environment.06-07-2012
20140102299AIR TRAP FOR A MEDICAL INFUSION DEVICE - An air trap for a blood circuit and method for removing air from blood in a dialysis unit. The air trap may include a blood inlet supply line, a blood outlet supply line, and a container having an approximately spherical internal wall, an inlet at a top end of the container connected to the blood inlet supply line, and an outlet at a bottom end of the container connected to the blood outlet supply line. The inlet may be offset from a vertical axis of the approximately spherical internal wall such that blood entering the container is directed to flow in a spiral-like path. The inlet port may be arranged to introduce blood into the container in a direction that is approximately tangential to the approximately spherical inner wall of the container and/or in a direction that is approximately perpendicular to the vertical axis of the container.04-17-2014
20140116253CLOSED GAS BUSTER SEPARATION SYSTEM AND METHOD - A separation system including a horizontal separation vessel having a gas separation chamber defined by an upper wall of the separation vessel, a gas dome extending above the upper wall, a baffle plate disposed within the separation vessel, and a level of a lower surface of the baffle plate. The lower surface of the baffle plate is disposed below a level of an upper surface of a liquid weir disposed within the separation vessel. The upper surface of the liquid weir may set a liquid level within the separation vessel. The gas separation chamber may include a hydrostatic pressure seal zone between the level of the upper surface of the liquid weir and the level of the lower surface of the baffle plate. Liquid within the hydrostatic pressure seal zone may prevent a gas disposed within the gas separation chamber from escaping into a remainder of the separation vessel.05-01-2014
20140238238A METHOD AND DEVICE FOR BLOWING OFF GASEOUS CONTAMINANTS FROM CRUDE WATER IN THE PRODUCTION OF DRINKING WATER - The invention relates to a method for blowing off gaseous contaminants from crude water in the production of drinking water, comprising the step of introducing the water to be treated to the top of a shielded aerator and letting it pass through stacks of tubular elements interspersed with perforated sheets, while subjected to counter current suction. In a second aspect a device is provided for blowing off gaseous contaminants from crude water according to said method.08-28-2014
20140290484System and Method For Treating A Saline Feed Stream To An Electro-Chlorination Unit - A system to reduce scaling within or downstream of an electrolytic cell includes sulfate removal membranes located upstream of one or more electrolytic cells which are arranged to receive a permeate feed stream from the sulfate removal membranes. The membranes can be nanofiltration membranes. The saline feed stream, permeate feed stream, or both may be de-aerated streams. The electrolytic cells may be part of an electro-chlorination unit and can be divided electrolytic cells.10-02-2014
20150096441BUBBLE REMOVING METHOD, BUBBLE REMOVING APPARATUS, DEGASSING APPARATUS, AND COMPUTER-READABLE RECORDING MEDIUM - Disclosed is a bubble removing method in which fine bubbles are removed from a filter to improve the performance of the filter. The bubble removing method includes a step of degassing a processing liquid supplied from a supply source to prepare a highly degassed liquid (highly degassed liquid preparation), a step of supplying the prepared highly degassed liquid at a first processing liquid from a pump device to a filter device (temporary liquid permeation), a step of supplying the highly degassed liquid at a second processing liquid flow rate higher than the first processing liquid flow rate from the pump device to the filter device (initial liquid permeation), and a step of causing the highly degassed liquid to flow from the pump device to the filter device for a predetermined length of time (liquid permeation).04-09-2015
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