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Subclass of:

202 - Distillation: apparatus

202081000 - APPARATUS

202082000 - Systems

202152000 - Separatory

Patent class list (only not empty are listed)

Deeper subclasses:

Class / Patent application numberDescriptionNumber of patent applications / Date published
202182000 With vapor-treating devices 78
202176000 With distilland treating devices 34
202172000 Plural 18
202175000 With agitator 14
202168000 Still and extractor 5
20140216915APPARATUS FOR REMOVING A CONTAMINANT FROM A SOLVENT SEPARATION PROCESS - The invention is a process and apparatus for removing a contaminant from an aromatic selective solvent. A feed stream comprising an aromatic hydrocarbon and a non-aromatic hydrocarbon is contacted with the aromatic selective solvent in an extractive distillation zone to produce a raffinate stream comprising the non-aromatic hydrocarbon, and a rich solvent stream comprising the aromatic hydrocarbon and the solvent. The rich solvent stream is separated in a second distillation zone to produce an extract stream comprising the aromatic hydrocarbon, and a lean solvent stream comprising the contaminant and the aromatic selective solvent. At least a portion of the lean solvent stream is washed with a non-aromatic hydrocarbon to produce a clean solvent stream, at least a portion of which is passed to at least one of the extractive distillation zone and the second distillation zone.08-07-2014
20100170776MULTI-PHASE SELECTIVE MASS TRANSFER THROUGH A MEMBRANE - Disclosed herein are embodiments relating to particular systems comprising a selective transfer membrane that can be utilized in material separation. In certain embodiments, the membrane assembly comprises part of a desalination, distillation, liquid purification, and/or heating and cooling system. Other particular embodiments allow for a high rate of thermal capture by way of the system utilizing a selective transfer membrane. Certain preferred embodiments include a selective transfer membrane comprising an ionomeric polymer that is permeable to high dipole materials.07-08-2010
20130233693Apparatus for Recovering Products Using Adsorption Separation and Fractionation - An apparatus according to various approaches includes separating a component from a feed stream using adsorption separation. The process further includes directing one of the extract stream and the raffinate stream to a high pressure distillation column. In addition, the process includes pumping the one of the extract stream and the raffinate stream to increase the pressure in the stream to flow the one of the extract stream and the raffinate stream into an inlet of the distillation column.09-12-2013
20150360144SYSTEMS FOR EXTRACTING SOLUTE FROM A SOURCE MATERIAL - Systems for extracting solute from a source material are shown and described. Each of the systems includes: a solvent source container configured to store a cooled solvent, a canister configured to contain the source material and receive solvent to produce an extract solution, and one or more extract containers in communication configured to receive and distill the extract solution, the solvent source container being configured to receive a post-extraction portion of the solvent. In some examples, the one or more extract containers are first and second extract containers that are each selectively coupleable to the canister and are selectively removable for storage of the extract mixture or the solute. In some other examples, the system further includes a cooling mechanism coupled to the solvent source container for cooling the recycled solvent within the solvent collection container.12-17-2015
20160184732BUTADIENE EXTRACTION PROCESS - A process for recovering 1,3-butadiene from a C06-30-2016
202166000 Still and stand boiler 4
20090101490Water Purification System - Devices and methods for water purification are provided. An improved demister (04-23-2009
20140166466Desalination System Using a Filter Press - A filter press system for water desalination may comprise: a frame; a plurality of filter plates configured to form a stack of parallel plates, each of filter plates being movably attached to the frame, the filter plates further being configured to form a multiplicity of chambers, each of the chambers being formed by adjacent filter plates, each of the chambers being lined by filter cloths and substantially filled with beads, wherein the plurality of filter plates, the multiplicity of chambers and the filter cloths are configured to allow water vapor to escape from the chambers while retaining salts from the water to form a filter cake; a heater, for heating the water in the chambers; a condenser for condensing the water vapor; and a separator for separating the beads from the filter cake after the filter cake is released from the chambers.06-19-2014
20140209448STRIPPING SYSTEM - A stripping system includes: a boiler which generates steam by heating water; a first heat exchanger (latent heat exchanger) which collects latent heat of the steam generated by the boiler, and thereby condenses the steam into condensed water; a second heat exchanger (sensible heat exchanger) which collects sensible heat of the condensed water, and thereby heats untreated water absorbing ammonia; and a stripping tower which receives the heated untreated water introduced therein, and vaporizes the ammonia from the heated untreated water.07-31-2014
20160051905Water Distiller Apparatus - A water distiller apparatus includes a boiler, a first condenser unit, a connector tube, a second condenser unit and an exhaust chimney. The boiler that contains unpurified water is exposed to an external heat source so that water vapor can be produced and condensed within the first condenser unit. Then the apparatus is able to discharge clean liquid water into a collection vessel. The excess water vapor is then discharged and condensed within the connector tube and the second condenser unit, where the apparatus once again discharges clean liquid water into another collection vessel. Then the remaining water vapor is discharged into the exhaust chimney as the apparatus creates a third collection point for clean liquid water at the end of the exhaust chimney as cooling fins of the exhaust chimney cool down water vapor into clean liquid water.02-25-2016
202202000 With condensate-treating devices 3
20110108405GASIFICATION PLANT WITH TOTAL ZERO DISCHARGE OF PLANT PROCESS WATERS - In certain embodiments, a system includes a gasification system configured to output grey water. The system also includes a grey water zero liquid discharge (ZLD) system configured to receive the grey water and to generate a first stream of distillate. The grey water ZLD system comprises an ammonia stripping system. An amount of water into and out of the grey water ZLD system is approximately equal.05-12-2011
20090242379REGENERATED SULFUR RECOVERY APPARATUS - A regenerated sulfur recovery apparatus positioned in a sulfur recovery plant, which apparatus contains a sulfur purifier that cools gaseous sulfur and condensates it, forming liquid sulfur while removing impurities contained therein; the apparatus containing a steam supplying means for melting solid sulfur deposited on an inner wall of the sulfur purifier, a molten sulfur reservoir that recovers and stores the melted sulfur, a reservoir heating means that heats the reservoir, an exhaust gas line that directs to the outside an exhaust gas formed in the reservoir when the reservoir is heated by the reservoir heating means, and an inert gas supply means that supplies an inert gas to the reservoir, such that the inert gas supplied into the reservoir flows to the outside through the exhaust gas line when molten sulfur stored in the reservoir is discharged from the reservoir.10-01-2009
20130206576MEMBRANE-BASED HYBRID PROCESS FOR SEPARATION OF MIXTURES OF ORGANICS, SOLIDS, AND WATER - A system and process that are a hybrid of distillation and membrane separations offers a highly efficient means of separating a fluid feed mixture into organic, solid, and aqueous components. The distillation section is followed by two membrane separation sections operated in parallel, with the distillation section separating the feed mixture into an organics-rich fraction and an organics-depleted and solids-rich fraction. One membrane section operates on the organics-rich fraction and separates it into a more organics-rich sub-fraction and a water-rich, organics-depleted sub-fraction, while the other membrane section operates on the organics-depleted, solids-rich fraction from the distillation section and separates it into a solids-rich sub-fraction and a solids-depleted, water-rich sub-fraction.08-15-2013
202167000 Still and feed-water heater 3
20100065414WATER HEATING AND DISTILLATION ARRANGEMENT - A water heating and distillation arrangement including a low-pressure steam generator boiler system including at least one boiler and adapted to produce steam at a pressure slightly above atmospheric pressure; a hot water tank; a composite, low-pressure condenser having condenser tubes for condensing steam into distilled water; the condenser being adapted to transfer heat of condensation of the steam to heat water in the hot water tank in which the condenser tubes are located; at least one steam pipe for transporting steam from the boiler system at low pressure loss to the condenser; means for processing, collecting and distributing the distilled water flowing out of the condenser; supply means for supplying the hot water tank and boiler system with feed water, and of distributing the hot water for use; and an integrated sensing, control, safety, and diagnostic system for controlling and integrating functions of the boiler system, the condenser and associated components.03-18-2010
20120000762Solar Thermal System for the Partial Desalination of Seawater and Electrical Energy - A solar thermal system for the partial desalination of sea water and for generating electricity includes a mass of black top material such as asphalt or the like used in paving roadways, parking lots and the like. The system also includes a network of interconnected conductive conduits such as a serpentine array of copper tubing and a pump for pumping seawater through the copper tubing that is in contact with or surrounded by the black top or asphalt portion of a roadway. The asphalt layer acts as a black body for absorbing heat from the sun and converts solar energy to thermal energy.01-05-2012
20150336807HYDROGEN-POWERED DESALINATION PLANT - The hydrogen-powered desalination plant is a multi-stage flash desalination system using hydrogen fuel to power the top brine heater of the plant. The hydrogen-powered desalination plant includes a plurality of flash distillation stages, which each include a flash chamber and a condenser. The top brine heater in the hydrogen-powered desalination plant is powered by the carbon-free combustion of hydrogen gas with oxygen gas. The combustion of the hydrogen gas with the oxygen gas creates a flame, which is used directly to generate steam from atomized seawater, any seawater not converted to steam being collected as preheated brine and passed to the multi-stage flash desalination system for successive stages of flash distillation. Preferably, the flame is generated as a vortex.11-26-2015
202170000 Still extractor 3
20140061021METHODS AND EXTRACTION UNITS EMPLOYING VAPOR DRAW COMPOSITIONAL ANALYSIS - Embodiments of extraction unit and an analysis method are provided. In one embodiment, the analysis method includes the steps of providing a feed stream and a species-selective solvent to the distillation column, drawing a vapor sample from the distillation column, condensing the vapor sample, and analyzing at least a portion of the condensed vapor sample.03-06-2014
20150367250SOLVENT EXTRACTION APPARATUS - A solvent extraction apparatus comprises a cooler for condensing solvent vapour and a funnel provided towards its lower end. The funnel has an upper surface at which terminates a central downwards directed elongate outlet having an internal exit port formed in a side wall. A vertically movable lifting rod passes through the cooler and the outlet. A section of the lifting rod is shaped to delimit a passage-way for condensate whilst simultaneously sealing the port. A liquid guide is provided at the upper surface to preferentially direct flow of condensate towards the passage-way.12-24-2015
20150375136ESSENTIAL OIL DISTILLATION SYSTEMS, DEVICES, AND METHODS - Essential oil distillation systems and methods for purifying an essential oil from plant material are shown and described. Each of the example essential oil distillation systems includes a material chamber configured to receive plant material and a solvent, a combination of the plant material and the solvent forming an essential oil, contaminant, and solvent mixture; a temperature regulating sleeve configured to be cooled to decrease a temperature of the mixture and freeze one or more contaminants in the mixture; at least one filter configured to filter the one or more contaminants from the mixture to separate a solvent and essential oil solution from the one or more contaminants; and a recovery chamber fluidly coupled to a downstream end of the material chamber, the recovery chamber configured to receive the solvent and essential oil solution.12-31-2015
202205000 Vacuum 3
20100012476APPARATUS FOR RECOVERING ACRYLIC ACID - Disclosed is a simplified apparatus for recovering acrylic acid from a mixture containing acrylic acid, acrylic acid dimer and impurities with high boiling point, in a stable and efficient manner. An apparatus for recovering an acrylic acid from a mixture containing acrylic acid, acrylic acid dimer and impurities with high boiling point, which comprises: an acrylic acid recovering device that comprises an acrylic acid distillation unit being present within an acrylic acid dimer pyrolysis tank, and is operated under reduced pressure; and a line for introducing the mixture into the acrylic acid recovering device, wherein decomposition of the acrylic acid dimer is carried out under reduced pressure at a lower part of the acrylic acid recovering device, while the acrylic acid is recovered by distillation under reduced pressure from a top of the acrylic acid recovering device.01-21-2010
20110031100COMPOSITE MEMBRANES FOR MEMBRANE DISTILLATION AND RELATED METHODS OF MANUFACTURE - The present invention provides composite membranes for membrane distillation and related methods of manufacture. In particular, there is provided a composite hydrophilic/hydrophobic membrane comprising a hydrophilic polymer layer and a hydrophobic polymer layer comprising fluorinated surface-modifying macromolecules, wherein said composite membrane has a high vapour flux. Also provided herein are methods of manufacturing and optimizing the composite membranes and a membrane distillation system comprising the composite membranes.02-10-2011
20150047964DEVICE FOR SEPARATING OIL FROM AN OIL-WATER MIXTURE - A device for separating oil from an oil-water mixture includes a first pump which is connected with a separation tank. The first pump pumps the oil-water mixture to the separation tank. A first valve is connected between the first pump and the separation tank. The separation tank has a heating unit and a cooler is connected to the top of the separation tank. The cooler is connected with a vacuum pump and a container. The oil is separated from the oil-water mixture effectively.02-19-2015
202164000 Recovery from containers 2
20090159419SOLVENT RECYCLER - In a solvent recycling system, a distillation vessel having an upper distillation zone and a lower waste collection zone and means whereby solvent waste falls into said waste collection zone before solvent enters said distillation zone. The system preferably has a solvent vapour outlet and a heating means, whereby solvent enters the vessel from above through the solvent feed inlet and solvent waste falls into said waste collection zone before distillation is commenced, and a shut-off means or filling tube extending below the distillation zone associated with the inlet to prevent solvent vapours exiting the vessel through the inlet during distillation.06-25-2009
20110155556LIQUID TREATMENT DEVICE AND METHOD - A buccal delivery system capable of being blended in a normal dry powder process and compressed using a standard tabletting machine, said buccal delivery system comprising a matrix of: (a) an effective amount of one or more active ingredients; (b) an amount of one or more polyethylene glycols or derivatives thereof having a molecular weight between 1000 to 8000 sufficient to provide the required hardness and time for dissolution of the matrix; (c) 0.05-2% by weight of the total matrix of one or more suspending agents; (d) 0.05-2% by weight of the total matrix of one or more flowing agents; and (e) 0.05-2% by weight of the total matrix of one or more sweeteners.06-30-2011
202206000 Automatic heat control 1
20090294271Device for Purification of a Liquid - The present invention refers to a device (12-03-2009
Entries
DocumentTitleDate
20130206573Steam Generation Apparatus - A steam generation apparatus 08-15-2013
20160129367THIN FILM SYSTEMS AND METHODS FOR USING AND MAKING SAME - Systems and methods for generating a thin film of a fluid are described. In an embodiment, a fluid support structure may be configured to receive a fluid, such as water, at a top surface and to support the fluid over at least a portion of the top surface. Channels may be formed in the top surface of the fluid support structure. Wiper blades may be configured to move over the top surface in contact with at least a portion of the fluid to form the fluid into a thin film. The wiper blades may include protrusions corresponding to the channels. As the wiper blades move over the top surface, the protrusions may move within the channels forming a thin film of the fluid within the channels. According to some embodiments, the fluid support structure may be configured as an evaporation surface configured to facilitate the evaporation of the fluid.05-12-2016
20190143243STILL05-16-2019

Patent applications in all subclasses Still

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