| Class / Patent application number | Description | Number of patent applications / Date published |
|---|
| 203021000 | AND RECOVERING HEAT BY INDIRECT HEAT EXCHANGE | 28 |
| 20090032389 | PROCESS FOR THE MILD DISTILLATIVE SEPARATION OF MIXTURES - The invention relates to a semibatchwise process for the mild distillative separation of mixtures, in a first stage a column being supplied continuously with a feed and the feed being separated at least into different fractions, one of the fractions being removed continuously into a container, and, in a second step, the fraction removed into the container being recycled to the column and being separated again batchwise into different fractions. | 02-05-2009 |
| 20100307910 | TILTED MULTI EFFECT DISTILLATION MODULE WITH MEANS FOR HEATING AND COOLING - A tilted multi effect distillation module comprising a plurality of distillation stages, each stage defined by a first and a second sheet member arranged in parallel to each other, the second sheet member above the first sheet member, and by one or more frame members ( | 12-09-2010 |
| 20110132740 | METHOD FOR EVAPORATION AND POSSIBLE DISTILLATION OF FLUIDS USING A HEAT PUMP. - The invention concerns a method for evaporation and possibly distillation of liquids by means of a heat pump. By using a heat pump ( | 06-09-2011 |
| 20120255852 | REACTION PROCESS USING SUPERCRITICAL WATER - When obtaining a target substance by gradually cooling the reaction liquid by cooling in a plurality of stages divided in series, and then distilling the cooled reaction liquid by distillation in a plurality of stages divided in series, this method and this apparatus include: circulating a heating medium to be used for cooling in the plurality of the stages by way of; sequentially passing the heating medium toward the most upstream cooling stage from the most downstream cooling stage of the reaction liquid; cooling the heating medium which has been discharged from the most upstream cooling stage by using the heating medium for keeping or raising the temperature of the liquid which has been discharged from the distillation in the plurality of the stages; and returning the cooled heating medium back to the most downstream cooling stage of the reaction liquid. | 10-11-2012 |
| 203022000 | Utilizing recovered heat for heating feed | 13 |
| 20130075245 | METHODS AND SYSTEMS FOR HEATING AND MANIPULATING FLUIDS - Systems and methods are provided for heating and manipulating a fluid to heat the fluid, evaporate water from the fluid, concentrate the fluid, separate the fluid into fractions; and/or pasteurize the fluid, comprising a closed-loop heating subsystem coupled to a primary fluid-to-fluid heat exchanger, and one or more fluid manipulation subsystems also coupled to the primary fluid-to-fluid heat exchanger. | 03-28-2013 |
| 20090218210 | ENERGY-EFFICIENT DISTILLATION SYSTEM - Methods and devices are provided for an energy-efficient distillation system ( | 09-03-2009 |
| 20110031101 | FLUID FRACTIONATION PROCESS AND APPARATUS - The present invention relates to a fractionation process for producing at least two concentration fractions of a fluid including a solute, suspended or dissolved content using at least two fluidly connected evaporator units. The process includes the steps of: feeding a feed fluid including a solute, suspended or dissolved content into at least a first evaporator unit; evaporating a first amount of fluid from the feed fluid in at least the first evaporator unit to produce a first concentrated fluid; feeding at least a portion of the first concentrated fluid into at least a second evaporator unit; and evaporating a second amount of fluid from the first concentrated fluid in at least the second evaporator unit to produce a second concentrated fluid. | 02-10-2011 |
| 20100288622 | METHOD AND APPARATUS FOR CATALYTICALLY PROCESSING SLURRY - In a method and apparatus for thermal processing of slurry, slurry is combined with a bio-mass to produce a mixture. The mixture is subjected in a heated mixer pump to a cracking temperature, thereby allowing the mixture to catalytically undergo a cracking reaction to produce a reaction mixture which is directly outgased in the mixer pump to produce an outgased portion and a solid portion. The outgased portion and the solid portion are separately discharged from the mixer pump; with the low boiling fraction of the outgased portion allowed to cool down for further processing, and the solid portion collected in a residual matter container for further processing. | 11-18-2010 |
| 20110180383 | MEMBRANE DISTILLATION SYSTEM AND METHOD - A membrane distillation system includes a distillation vessel, an array of hollow fiber membranes pervious to distillate vapor but impervious to feed solution and an array of hollow tubes impervious to distillate vapor and feed solution but which allow thermal energy transmission. The system further includes a pump, a heat exchanger for heating the feed solution before it enters the hollow fiber membranes, and an outlet for removing distillate from the distillation vessel. A method for removing distillate from a feed solution includes delivering the feed solution through hollow tubes spanning a distillation vessel, heating the feed solution, delivering the feed solution through hollow fiber membranes spanning the distillation vessel to create a vapor pressure differential between the hollow fiber membranes and a distillation volume within the distillation vessel, and removing distillate from the distillation vessel. | 07-28-2011 |
| 203023000 | Distillation residue as heat source | 5 |
| 20120097520 | PROCESS AND APPARATUS FOR SEPARATION OF HYDROCARBONS AND NITROGEN - The invention provides a process and apparatus for the separation of a gaseous feed comprising a mixture of hydrocarbons and nitrogen gas, the process comprising the steps of: (i) cooling and at least partially condensing the gaseous feed; (ii) feeding the cooled and at least partially condensed feed from step (i) to a fractionation column comprising reboil to produce an overhead hydrocarbon vapour stream enriched in nitrogen and a condensed hydrocarbon product stream low in nitrogen, wherein prior to the fractionation, the feed stream is divided into at least two streams including: a) a first stream which is expanded and fed to the fractionation column; b) a second stream which is expanded, heated and fed to a lower stage of the fractionation column than the first stream, (iii) removing a hydrocarbon product stream low in nitrogen from the fractionation column; and (iv) removing a hydrocarbon vapour stream enriched in nitrogen from the fractionation column. | 04-26-2012 |
| 20110132741 | Thermal-Separation Process With Absorption Heat Pump - The invention comprises an absorption heat pump to supply energy to a distillation process or an outside process. The streams used to effect the absorption heat pump are to be combined in any case as a feedstream to a conversion process, and energy thus is conserved by avoiding the necessity of reseparating the streams. | 06-09-2011 |
| 20120145530 | METHOD AND APPARATUS FOR PURIFICATION OF TRICHLOROSILANE - There is provided a method for a purification of trichlorosilane, the method including: performing a pretreatment for separating a chlorosilane mixture from reaction products of a trichlorosilane production reaction; performing a first purification for separating the chlorosilane mixture into a first top stream and a first bottom stream; performing a second purification for separating the first top stream into a second top stream and a second bottom stream; and performing a third purification for separating the second bottom stream into a third top stream and a third bottom stream, wherein the performing of the third purification is carried out under pressure conditions higher than those of the performing of the second purification, and a heat exchange is generated between the second bottom stream and the third top stream. | 06-14-2012 |
| 20120145529 | APPARATUS, PROCESS AND SYSTEM FOR DELIVERING FLUID TO A DISTILLATION COLUMN OR REACTOR - A fluid delivery apparatus is provided for supplying a fluid mixture to a distillation column or reactor. The apparatus can be used to enhance the heat duty, the flow and/or the flow stability of an existing thermosiphon reboiler which supplies a heated fluid to the column or reactor. The apparatus includes an integrated eductor which receives and increases the fluid velocity of a supplemental fluid into which the heated fluid is aspirated to form a fluid mixture then delivered to the column or reactor. A process and a system utilizing the apparatus are also disclosed, as well as a method of retrofitting an existing system with the apparatus. | 06-14-2012 |
| 20100288623 | METHOD AND DEVICE FOR PRODUCING VACUUM IN A PETROLEUM DISTILLATION COLUMN - The invention relates to the oil processing industry and can be used for producing vacuum in a vacuum petroleum distillation column. The inventive method involves pumping out a vapour-gas medium from the column by means of a gas-gas ejector in such a way that a vapour-gas mixture is formed at the entry thereof and supplying said mixture to a condenser for producing a gas mixture and a vapour phase condensate. The gas mixture is supplied from the condenser to a liquid-gas jet apparatus and the condensate is delivered to an additional separator. A hydrocarbon-containing condensate is removed from the additional separator for the intended use thereof and a water-containing condensate is fed to a steam generator for producing steam by supplying heat of a hot distillate evacuated from the vacuum column. The thus obtained steam is used in the gas-gas ejector as a high-pressure gas. The device comprises a line for supplying a distillate of petroleum distillation, a line for removing a distillate of petroleum refining, the steam generator and the additional separator. The invention makes it possible to reduce energy consumption, increase vacuum depth and to exclude the use of a water vapour delivered from an external source. | 11-18-2010 |
| 203024000 | Compressed vapor as heat source | 3 |
| 20100175983 | Mutual Remediation of Effluents of Petroleum Production - Petroleous production is associated with effluents well known to foul lines, nozzles, and containers while consuming substantial energy to assist in both production and remediation. A heat exchanger and manifold system maximizes flows, minimizes changes in flow cross-section, and maximizes heat transfer area, while recycling both water and heat between processes. Dirty regions and clean regions result from scrubbing horizontal exhaust stacks and evaporation of production water in concert to remediate one another, while recycling a significant portion of the energy consumed by each. The heat exchanger relies on a manifold having many layered conduits, each connected to a single layer level of one or more cylindrical conduits in the exchanger. The cylinders of the exchanger themselves are arranged in multiple layers, each layer of a heat exchanger element being connected to a single layer of the manifold. Any shape of cylinder may work, but a right circular cylinder having corrugated sheets spacing the layers may be simple to construct. | 07-15-2010 |
| 20090294272 | METHOD FOR THE PURIFICATION OF WASTEWATERS FROM MELAMINE SYSTEMS - The invention relates to a method for purifying wastewaters of melamine systems. The method is characterized in that triazine-containing wastewater is subjected to a thermal pretreatment stage, whereupon the vapors are condensed from the gas phase of the thermal pretreatment stage, and the liquid phase of the thermal pretreatment stage is subjected to a thermal hydrolysis stage while NH | 12-03-2009 |
| 20120037489 | APPARATUS AND METHOD FOR PURIFYING A LIQUID - For purifying a liquid, the liquid is caused to evaporate in a cyclone in a recirculation circuit. Vapor is discharged via a discharge channel in which a compressor is included. In a heat exchanger downstream of the compressor, supplied vapor condenses and heat thereby released is transferred to liquid in the recirculation circuit. A liquid inlet of the cyclone is placed and directed for delivering a jet having a directional component tangential with respect to an inner surface of the cyclone. The liquid inlet has a section shaped such that in operation the delivered jet is a flat jet having a cross section which in a direction parallel to a nearest generatrix of the inner surface of the cyclone is greater than in a direction perpendicular thereto. The jet contacts the inner surface of the cyclone before drop formation occurs in the jet. A method for purifying a liquid is also described. | 02-16-2012 |
| 203025000 | Utilizing recovered heat for heating the distillation zone | 5 |
| 20080302650 | Process to recover low grade heat from a fractionation system - This invention relates to methods and apparatus for the energy efficient separation of ethane and propane from any hydrocarbon feed, i.e., from natural gas, natural gas liquids, liquid natural gas, or from gases from refinery or petroleum plants. | 12-11-2008 |
| 20090314624 | ENERGY EFFICIENT DISTILLATION SYSTEM AND METHOD - A new distillation process of simultaneous evaporation and condensation distillation that enables efficient transfer of heat energy and allows binary fluids to attain different concentrations and temperatures in the stripper and rectifier stages is disclosed. The process utilizes preferential evaporation of the more volatile component in the stripper while in the rectifier the less volatile component condenses first allowing for concentration of the more volatile component in subsequent stages. The rectifier operates at correspondingly hotter temperatures than the stripper allowing energy transfer from the rectifier to the stripper. | 12-24-2009 |
| 20120031747 | PROCESS AND SYSTEM FOR SEPARATING HEAVY AND LIGHT COMPONENTS CONTAINED IN A VAPOR MIXTURE - Herein disclosed is a method of separating heavy and light components from a vapor mixture. The method comprises a. distilling the vapor mixture into a first vapor phase and a first liquid phase; and b. condensing at least a portion of the first vapor phase into a second liquid phase and a second vapor phase; wherein the distilling utilizes the internal energy of the vapor mixture. In an embodiment, the method further comprises c. utilizing at least a portion of the first liquid phase to absorb at least a portion of the second vapor phase. In some cases, the method further comprises cooling the at least a portion of the first liquid phase prior to utilizing it to absorb the at least a portion of the second vapor phase. | 02-09-2012 |
| 203026000 | Compressed vapor as heat source | 2 |
| 20100108487 | DIVIDING WALL COLUMN WITH A HEAT PUMP - Systems and methods for separating a multi-component fluid are provided. The method can include introducing a multi-component fluid to a dividing wall column. The multi-component fluid can be heated to provide a first product, a second product, an intermediate distillate, and a process fluid. At lest a portion of the first product can be compressed to provide a compressed first product. Heat can be indirectly transferred from the compressed first product to at least a portion of the intermediate distillate to provide a heated intermediate distillate. The heated intermediate distillate can be recycled to the dividing wall column. The compressed first product can be expanded. | 05-06-2010 |
| 20100025218 | HIGH ENERGY REDUCTION IN A PROPANE DEHYDROGENATION UNIT BY UTILIZING A HIGH PRESSURE PRODUCT SPLITTER COLUMN - An improved process for the production of olefins, and in particular for separation of olefins produced by a dehydrogenation process from paraffin feed stocks, is provided. A high pressure product splitter is used to separate olefins produced in a dehydrogenation plant from residual paraffin feed stocks. The use of a high pressure splitter to separate olefin products from paraffin feed stocks allows for recovery of a high purity olefin product with lower energy consumption compared to prior art processes. The process is particularly suited to separation of propylene from propane. | 02-04-2010 |
| 203027000 | Utilizing recovered heat in subsequent step in process | 6 |
| 20130037404 | DISTILLATION PROCESS AND MULTI-COLUMN HEAT-INTEGRATED DISTILLATION SYSTEM - The invention relates to a process for separating a multi-component feed mixture in a distillation system comprising a first distillation column having a first fired reboiler, and at least a second distillation column having a second heat-exchange reboiler, comprising the steps of a) introducing the feed mixture to the first column, and separating into at least a first top and a first bottom product; b) taking part of the first bottom product for providing heat to the second reboiler as a utility stream; and c) feeding part of said utility stream after heat-exchange as main feed to the second column for further separation. This process allows significant energy savings, by reduction of the amount of external heat required for the fired reboiler and omission of a conventionally used heat-exhanger. The invention also relates to such distillation system suitable for separating a multi-component mixture with the process of the invention. | 02-14-2013 |
| 20120228118 | METHOD AND EQUIPMENT FOR TREATMENT OF BLACK LIQUOR AT PULP MILL - The invention relates to a method and equipment for treating pulp mill black liquor so as to recover the energy in chemicals therein. In the invention the black liquor is pyrolysed in a pyrolysis reactor ( | 09-13-2012 |
| 20100101930 | Heat Pump for High Purity Bottom Product - A process for reducing the energy consumption of a distillation column is disclosed. The process includes drawing off an intermediate vapor stream from the rectification section of the distillation column. The vapor stream is compressed and the heat in the vapor stream is exchanged with a portion of the liquid bottoms stream. The heat transfer condenses a portion of the vapor stream, while vaporizing the liquid bottoms stream. | 04-29-2010 |
| 20100025219 | System and method for membrane distillation with low reynolds numbers - A distillation system and method includes open reservoirs and pluralities of hollow fiber membranes and hollow tubes extending through portions of separate open reservoirs. The hollow fiber membranes are configured to allow vapor transmission, and the hollow tubes are configured to substantially prevent vapor transmission but allow transmission of thermal energy. Feed solution is circulated through the open reservoirs. Distillate is separated from the feed solution by the hollow fiber membranes and thermal energy is recouped through the hollow tubes. | 02-04-2010 |
| 20090173618 | Method of an apparatus for generating a vacuum and for separating volatile compounds in polycondensation reactions - The invention relates to a method for generating a vacuum and for separating volatile compounds during esterification, transesterification and/or polycondensation reactions. One or several jets of steam comprising a spray condenser, which is arranged up or downstream, are connected to the suction side of a reactor which is to be evacuated and phenol or steam containing phenol is used as propellant steam at a pressure of 0.5 hPa to approximately 1.5 MPa and liquid phenol or a liquid containing phenol is used as a spraying agent. | 07-09-2009 |
| 20110272267 | Heat Pump Distillation - A distillation column is disclosed. The column includes a plurality of rectification zones and corresponding stripping zones. Each rectification zone is linked to a heat pump or a stage of a heat pump. Overhead material from the top rectification zone is compressed and used to heat bottoms liquid from the bottom stripping zone. Similarly, overhead material from a lower rectification zone is compressed and used to heat liquid taken from the uppermost or top stripping zone. Optionally, overhead material from a middle rectification zone is compressed and used to heat liquid from a middle stripping zone. A single multiple stage heat pump compressor may be utilized as opposed to a plurality of heat pumps. Because the heat exchanger from each rectification-stripping zone pair has a lower duty, economical stab-in heat exchangers may be utilized. | 11-10-2011 |
