Class / Patent application number | Description | Number of patent applications / Date published |
422131000 | Organic polymerization | 88 |
20080226512 | Gas distribution plate for fluidized-bed olefin polymerization reactors - A gas distribution plate for fluidized-bed, olefin polymerization reactors is provided. In addition to holes for distributing a fluidizing gas, the plate comprises a plurality of hollow projections for introducing a fluid into the fluidized-bed reactor. The hollow projections, which can be tubes or pipes, extend above the plate towards the fluidized bed and serve a number of purposes. The projections can break apart or penetrate fallen polymer agglomerates or sheets. They can be equipped with flow or pressure sensors to detect a decrease in flow rate or an increase in pressure drop across the projections, which is an indicator of the presence and/or size of fallen polymer agglomerates or sheets. The projections can also break apart the agglomerates or sheets into smaller pieces by delivering blasts of fluid directly into the agglomerates or sheets. The projections can also be used to inject a kill agent into the fallen agglomerates or sheets, or collapsed portions of the bed, to speed up penetration of the kill agent into the agglomerates, sheets, or collapsed portions. | 09-18-2008 |
20080253936 | Process for producing synthetic petroleum jelly - A method and system for producing petroleum jelly from hydrocarbons. The method converts the hydrocarbon source into a synthesis gas. The synthesis gas is converted into at least a light-hydrocarbons stream and a heavy-hydrocarbons stream, which both include a plurality of paraffins and a plurality of olefins. The plurality of paraffins is reacted with the plurality of olefins in the presence of a dialkyl peroxide initiator to form the petroleum jelly. A synthesis gas production system is adapted to produce a synthesis gas from at least a natural gas source. A hydrocarbon conversion system is adapted to produce heavier hydrocarbons from at least the synthesis gas, the heavier hydrocarbons containing at least a plurality of paraffins and a plurality of olefins. A petroleum-jelly production system is adapted to convert the produced heavier hydrocarbons into petrolatum. | 10-16-2008 |
20090016938 | SLOPED TUBULAR REACTOR WITH SPACED SEQUENTIAL TRAYS - A sloped tubular reactor operable to facilitate a chemical reaction in a reaction medium flowing therethrough. The reactor can include a plurality of spaced apart internal trays disposed at different elevations in a downwardly sloping elongated tubular member. | 01-15-2009 |
20090016939 | MULTI-LEVEL TUBULAR REACTOR WITH VERTICALLY SPACED SEGMENTS - A multi-level tubular reactor operable to facilitate a chemical reaction in a reaction medium flowing therethrough. The tubular reactor can include a plurality of horizontally elongated and vertically spaced reactor segments coupled to and extending outwardly from a common header. One or more of the reactor segments can contain a tray that divides the internal volume of the reactor segment into upper and lower chambers. The reaction medium can flow away from the header in the upper chambers and back to the header in the lower chambers. | 01-15-2009 |
20090016940 | SLOPED TUBULAR REACTOR WITH DIVIDED FLOW - A sloped tubular reactor operable to facilitate a chemical reaction in a reaction medium flowing therethrough. The reactor can include a downwardly sloped tubular member, a flow divider disposed in the tubular member, and one or more internal trays disposed in the tubular member. The flow divider divides flow of the reaction medium among the trays and the bottom of the tubular member. | 01-15-2009 |
20090081085 | APPARATUS FOR PRODUCING THREE-DIMENSIONAL STRUCTURE - A process for producing a periodic structure comprises the steps of preparing a working object, the property of which changes in view of a photoreaction caused by an exciting energy, generating a light having a photonic energy of intensity of one fraction of natural number divisions of the exciting energy by each of the light sources of light-source groups arranged regularly in a two-dimensional arrangement, and concentrating the light emitted from the light source group at each of the light-concentrating points arranged at regular intervals in the working object to cause a photoreaction at and around the light-concentrating point to form a periodic structure comprised of regions each of which has a changed property in the working object. | 03-26-2009 |
20090148353 | Polymer Synthesizer - The present invention provides a polymer synthesizer having a high efficiency production rate. The synthesis of the polymers, and more particularly of DNA and RNA, is done very quickly. Furthermore, it is possible to synthesize a plurality of polymers in the same batch without significantly increasing the time and the complexity of the process. | 06-11-2009 |
20100061897 | Microencapsulation of amines - A system for microencapsulation of an amine in a polymer shell in an aqueous environment. | 03-11-2010 |
20100209307 | METHOD FOR IMPROVING THE PREDICTION OF POLYMER PROPERTIES AND A SYSTEM HAVING IMPROVED POLYMER PROPERTY PREDICTION CAPABILITIES - The instant invention is a method for improving the prediction of polymer properties and a system having improved polymer property prediction capabilities. The method for improving the prediction of polymer properties according to instant invention comprises the following steps of: (1) providing a polymer; (2) providing a prediction model; (3) utilizing said prediction model to define an average polymer property prediction value; (4) determining a feasible range; (5) measuring one or more properties of said polymer; (6) determining whether said one or measured polymer properties are within said feasible range: (7) validating said one or more measured polymer properties if said one or more measured polymer properties fall within the feasible range or invalidating said one or more measured polymer properties if said one or more measured polymer properties fall outside of the feasible range; (8) optionally updating said prediction model; (9) repeating said previous steps at least one or more times; and (10) thereby improving the prediction of polymer properties. The polymerization system having improved polymer property prediction capabilities according to instant invention comprises at least one polymerization reactor; an automated prediction model; means for measuring one or more polymer properties; means for detecting one or more erroneous measured polymer properties; and means for updating said automated predication model. | 08-19-2010 |
20100247391 | Apparatus for Oligomerizing Dilute Ethylene - The process and apparatus converts ethylene in a dilute ethylene stream that may be derived from an FCC product to heavier hydrocarbons. The catalyst may be an amorphous silica-alumina base with a Group VIII and/or VIB metal. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, hydrogen and ammonia. At least 40 wt-% of the ethylene in the dilute ethylene stream can be converted to heavier hydrocarbons. | 09-30-2010 |
20100260647 | INTEGRATED PLANT FOR PRODUCING 2-ETHYL-HEXANOL AND METHACRYLIC ACID - An integrated facility is disclosed for simultaneous production of butanal and methacrylic acid products where the facility utilizes a mixed methacrolein and isobutanal stream to make methacrylic acid. The facility is also designed to utilize downstream n-butanal products such as n-butanol and/or 2-ethyl-hexanol to make butyl-methacrylates and 2-ethyl-hexyl-methacrylate. A method is also disclosed which integrates the production of butanal derived products and methacrylic acid derived products. | 10-14-2010 |
20100329934 | Slurry phase polymerisation process - A process comprising polymerising in a loop reactor an olefin monomer optionally together with an olefin commoner in the presence of a polymerisation catalyst in a diluent to produce a slurry comprising solid particulate olefin polymer and the diluent wherein the Fronde number is maintained at or below 20 is disclosed. | 12-30-2010 |
20110076201 | Overhung Axial Flow Compressor, Reactor and Method - Overhung axial compressor, chemical reactor and method for compressing a fluid. The overhung axial compressor includes a casing configured to be vertically split along a vertical axis for access to an inside of the casing and a removable cartridge. The removable cartridge is configured to fit inside the casing and to be detachably attached to the casing. The removable cartridge includes a shaft disposed along a horizontal axis, the shaft being configured to rotate about the horizontal axis, a bearing system attached to the removable cartridge and configured to rotationally support a first end of the shaft, and plural blades disposed toward a second end of the shaft such that the second end is overhung inside the casing. The compressor also includes a guide vane mechanism configured to connect to the removable cartridge, the guide vane mechanism being configured to adjust a flow of a fluid to the plural blades. | 03-31-2011 |
20110097243 | APPARATUS FOR THE RECOVERY OF ETHYLENE GLYCOL IN THE PRODUCTION OF POLYETHYLENE TEREPHTHALATE - In an apparatus for the recovery of ethylene glycol in a polyethylene terephthalate(PET) production process water accumulating in the esterification reaction is mixed with a process fluid containing 2-methyl-1,3-dioxolane (MDO). The mixing is carried out in a tank upstream of a rectification column. Through the increase in the water content in the fluid, a shift in the reaction equilibrium takes place and consequently a cleavage of the 2-methyl-1,3-dioxolane present into ethylene glycol and acetaldehyde takes place. Following the cleavage reaction, the mixture is fed from the tank into a rectification column, whereby the ethylene glycol produced from the cleavage reaction is returned to the PET production process. | 04-28-2011 |
20110165027 | METHOD AND APPARATUS FOR CURING WASTE CONTAINING PHOTOPOLYMERIC COMPONENTS - An Apparatus for polymerizing photoactive materials included in a liquid material by electromagnetic radiation, by dispensing the liquid material layer-wise into a container and irradiating the accumulated layers by a curing radiation, wherein a substantial part of the radiation is well transmitted through the photoactive material. | 07-07-2011 |
20110171078 | Apparatus For Humidification Of Hydrocarbon Mixtures - A humidification system (A) for humidifying a dry hydrocarbon stream includes a column ( | 07-14-2011 |
20110194984 | Polymerization Method - The invention relates to a process for continuously preparing water-absorbing polymer particles by mixing a monomer solution with a redox initiator consisting of at least one oxidizing agent and at least one reducing agent and polymerizing it, wherein the monomer solution is mixed with at least one oxidizing agent upstream of the polymerization reactor and the at least one reducing agent is metered into the polymerization reactor, and also to an apparatus for performing the process. | 08-11-2011 |
20110236270 | Wicking-based reagent-solution draining in an automated system - Embodiments of the present invention include processing steps and subsystems, within automated-biopolymer-synthesis systems and within other automated systems for organic-chemistry-based processing, for removing reagent solutions and solvents from reaction chambers following various synthetic reaction steps and washing steps undertaken during biopolymer synthesis. Embodiments of the present invention employ any of various different types of liquid-absorbing materials to wick, or remove by capillary action, liquids from reaction chambers. Wicking-based methods and subcomponents of the present invention remove significantly greater fractions of solutions from reaction chambers than conventional methods and subsystems and, in addition, are mechanically simpler and produce fewer deleterious side effects than currently used methods and subsystems. | 09-29-2011 |
20110256031 | Automated polymer-synthesis system - Embodiments of the present invention are directed to automated-polymer-synthesis systems that include discrete reagent-solution-addition, wait-time, and reagent-solution-draining sub-systems which together significantly increase throughput and decrease sub-system idle time. The automated-polymer-synthesis systems that represent embodiments of the present invention additionally include switches at points in which carriers can be received from multiple input paths or output to multiple different output paths. The automated-polymer-synthesis systems that represent embodiments of the present invention generally include an input spur and output spur in addition to a main loop, allowing carriers containing only completed polymers to be removed and new carriers input, so that carriers traverse the automated-polymer-synthesis systems independently from one another. | 10-20-2011 |
20110274589 | Gas-Phase Polymerization Of Alpha-Olefin - A method for preparing polyolefin from alpha-olefin with high productivity using an internal circulating fluidized bed polymerization reactor is disclosed. The method for gas-phase polymerization of alpha-olefin comprising the steps of: supplying circulation gas including one or more alpha-olefins and inert gas into a polymerization reactor; polymerizing the alpha-olefin to polyolefin in two separated polymerization areas in the polymerization reactor; and discharging produced polyolefin from the polymerization reactor. The polymerization reactor is divided into the two polymerization areas by a draft tube, and an inside of the draft tube forms a riser where growing polyolefin polymers move up in fast fluidization, and an outside of the draft tube forms an annulus where the polyolefin polymers passing the riser move down by gravity, and the polyolefin polymers passing the annulus are introduced to a lower part of the riser again, so that the polyolefin polymers are polymerized during circulating between the riser and the annulus. | 11-10-2011 |
20110300024 | SYSTEM AND PROCESS FOR PRODUCTION OF POLYETHYLENE AND POLYPROPYLENE - A system for production of a polymer that may include a first high shear mixing device configured for producing a nanodispersion comprising particles or bubbles having a mean diameter less than 1 micron dispersed in a monomer-containing liquid or gaseous phase; a pump configured for delivering a pressurized liquid stream comprising the monomer to the first high shear mixing device; and a vessel configured for receiving the nanodispersion and for maintaining a predetermined pressure and temperature. | 12-08-2011 |
20110318233 | SUPPORTED IONIC LIQUID REACTOR - A chemical reactor, comprising:
| 12-29-2011 |
20120039755 | Methods and Devices for Polymerization - A method of treating a gas phase fluidized bed reactor and a method of polymerizing olefins in a gas phase fluidized bed reactor in the presence of a catalyst prone to cause sheeting by introducing a chromium-containing compound into the reactor and forming a high molecular weight polymer coating on the walls of the reactor. Furthermore, a device for and method of introducing the chromium-containing compound into the fluidized bed reactor at a plurality of locations in proximity to a lower section of a bed section wall of the fluidized bed reactor, and forming a high molecular weight polymer coating on the bed section wall. | 02-16-2012 |
20120156104 | SYSTEM AND PROCESS FOR PRODUCTION OF POLYVINYL CHLORIDE - A system configured to produce polyvinyl chloride that includes a high shear mixing device comprising at least one rotor/stator set and configured to produce a polymerization mixture by high shear mixing a vinyl chloride solution with an initiator solution, wherein the polymerization mixture comprises an emulsion of droplets; a pump in fluid communication with an inlet of said high shear mixing device; and a vessel in fluid communication with an outlet of said high shear mixing device and configured for to maintain a predetermined pressure and temperature on the polymerization mixture, wherein the vessel comprises an outlet for a product comprising polyvinyl chloride and unconverted vinyl chloride and a vent gas outlet for at least one gas selected from the group consisting of gaseous vinyl chloride, volatile reaction products, and combinations thereof. | 06-21-2012 |
20120275961 | Fluid Separation Systems And Methods - Systems and methods for separating particles from fluids are provided. The system comprises a vessel with a fluid inlet and a fluid outlet and a baffle assembly located within the vessel. The baffle assembly has a plurality of baffles that can provide a change in direction to fluid entering the vessel thereby separating particles. During shut-down of a polymerization reactor, reaction mixture is discharged to a separation system where polymer particles are removed from the mixture prior to being released into the atmosphere. | 11-01-2012 |
20120308438 | OLIGOMERIZATION REACTOR AND CONTROL SYSTEM - A process unit, having:
| 12-06-2012 |
20130017124 | POLYMERIZATION APPARATUS FOR DENTAL TECHNOLOGYAANM NOGUCHI; YukieAACI TokyoAACO JPAAGP NOGUCHI; Yukie Tokyo JP - Polymerization apparatus for dental technology, having a housing; a partition wall disposed in the housing so as to form a polymerization space where polymerization is carried out; a rotating table, which is arranged on a lower side of the polymerization space and on which the dental prosthesis is disposed directly or via other members; and a plurality of LED light sources which irradiate a light for the curing to a polymerization region, which is formed on the upper side of the rotating table and where the dental prosthesis can be disposed, wherein at least one of the plurality of LED light sources is disposed such that a light axis thereof is inclined obliquely upward to be directed toward the polymerization region. | 01-17-2013 |
20130058837 | PROCESS FOR PRODUCING WATER-ABSORBING POLYMER PARTICLES - A process for producing water-absorbing polymer particles, wherein a polymer gel is removed from a polymerization reactor, stored intermediately as a particulate polymer gel in a delay vessel, removed by means of a first conveying device at the lower end of the delay vessel and dried, the intermediately stored particulate polymer gel being conveyed within the delay vessel by means of at least one second conveying device above the first conveying device in the direction of the first conveying device. | 03-07-2013 |
20130101469 | System and Method for Processing Reactor Polymerization Effluent - A method of treating a polymerization reactor effluent stream comprising recovering the reactor effluent stream from the polymerization reactor, flashing the reactor effluent stream to form a flash gas stream, separating the flash gas stream into a first top stream, a first bottom stream, and a side stream, wherein the side stream substantially comprises hexane, separating the first top stream into a second top stream and a second bottom stream, wherein the second bottom stream substantially comprises isobutane, and separating the second top stream into a third top stream and a third bottom stream; wherein the third top stream substantially comprises ethylene, and wherein the third bottom stream is substantially free of olefins. | 04-25-2013 |
20130236366 | CONDENSATION AND WASHING DEVICE, POLYMERISATION DEVICE AND METHOD FOR CLEANING PROCESS STEAM DURING THE PRODUCTION OF POLYLACTIDE - The present invention relates to a condensation and washing device with which in particular the process vapours which occur during the production of polylactide can be processed and cleaned. Furthermore, the present invention relates to a polymerisation device for the production of polylactide and also to a method for processing process vapours which occur during the production of polylactide; possibilities for use of both the condensation and washing devices and of the method are likewise mentioned. | 09-12-2013 |
20130280137 | System and Method for Processing Reactor Polymerization Effluent - A method of treating a polymerization reactor effluent stream comprising recovering the reactor effluent stream from the polymerization reactor, flashing the reactor effluent stream to form a flash gas stream, separating the flash gas stream into a first top stream, a first bottom stream, and a side stream, wherein the side stream substantially comprises hexane, separating the first top stream into a second top stream and a second bottom stream, wherein the second bottom stream substantially comprises isobutane, and separating the second top stream into a third top stream and a third bottom stream; wherein the third top stream substantially comprises ethylene, and wherein the third bottom stream is substantially free of olefins. | 10-24-2013 |
20140178256 | Serpentine Fluid Reactor Components - Some embodiments of the present invention provide components for a serpentine fluid reactor which is optimized for one or more objective functions of interest such as pressure drop, erosion rate, fouling, coke deposition and operating costs. The components are designed by computer modeling the components individually and collectively in which the cross section of flow path is substantially circular under industrial conditions to validate the model design and its operation. Then iteratively the component designs are deformed and the operation of the deformed part(s) is modeled and compared to values obtained with other deformed models until the value of the objective function is optimized (e.g. at an extreme) or the change in the objective function is approaching zero. | 06-26-2014 |
20140255260 | Catalyst Metering Device - The invention relates to a catalyst metering device with a valve formed of an iron-based alloy steel hardened to a Rockwell hardness C of at least 60. The device can be used for metering of a catalyst for an ethylene polymerization reaction. The invention further relates to ethylene polymerization wherein the catalyst is metered in a catalyst metering device with a iron-based alloy steel hardened valve, as well as to a ethylene polymerization reactor comprising such a catalyst metering device. | 09-11-2014 |
20150086429 | System and Process for Recovering Gas Emissions Generated in Producing Olefin Polymers - The present disclosure provides a system for recovering emissions generated from an olefin polymerization process, comprising: a devolatilizer for receiving a fresh sweep gas and emissions generated from the olefin polymerization process and outputting a first fluid and a polyolefin resin; a compression refrigeration unit including a compression device and a first heat exchange device, for receiving said first fluid and outputting a first gas-liquid mixture; a first gas-liquid separation device for separating the first gas-liquid mixture and outputting a first recovery product and a first gas phase composition; a first gas separation device for receiving the first gas phase composition, removing small molecular substances therefrom, and outputting a composition rich in small molecular gases and a second gas phase composition rich in hydrocarbons; and a second gas separation device having a second heat exchange device, a second gas-liquid separation device, and a first gas expansion device. | 03-26-2015 |
20160032022 | MICROPROCESSING FOR PREPARING A POLYCONDENSATE - The present invention relates to a process for preparing polydextrose by using a microdevice. It further relates to the use of a microdevice for the polycondesation reactions. | 02-04-2016 |
20160159950 | Novel High Clarity Low Haze Compositions - A first embodiment which is a bimodal polymer having a weight fraction of a lower molecular weight (LMW) component ranging from about 0.25 to about 0.45, a weight fraction of a higher molecular weight (HMW) component ranging from about 0.55 to about 0.75 and a density of from about 0.931 g/cc to about 0.955 g/cc which when tested in accordance with ASTM D1003 using a 1 mil test specimen displays a haze characterized by equation: % Haze=2145=2145−2216*Fraction | 06-09-2016 |
20170232418 | APPARATUS FOR INTRODUCTION OF DROPLETS OF A MONOMER SOLUTION INTO A REACTOR | 08-17-2017 |
422132000 | Closed loop | 13 |
20090081086 | Apparatus for Continuously Producing Polyisocyanate - An apparatus for continuously producing polyisocyanate is provided for quickly contacting polyamine and carbonyl chloride in order to suppress an undesirable reaction between polyamine and polyisocyanate so that a by-product can be reduced and the yield of polyisocyanate can be improved. In a circulatory line | 03-26-2009 |
20090148354 | OLEFIN POLYMERIZATION REACTION UNIT AND POLYOLEFIN PRODUCTION PROCESS - An olefin polymerization reaction unit includes a multistage gas phase polymerization reactor which is divided into two or more polymerization stages, in which polyolefin particles move from an initial stage to a final stage, and in which an olefin monomer-containing gas is fed from the final stage toward the initial stage. The reaction unit also includes first circulating means for feeding to the final stage a gas that is discharged from the initial stage and then cooled with a first heat exchanger, and second circulating means for feeding to one of the polymerization stages a condensate formed by condensing, with a second heat exchanger different from the first heat exchanger, a gas removed from one of the polymerization stages. | 06-11-2009 |
20090252657 | Slurry phase polymerisation process - A process comprising polymerising an olefin monomer optionally together with an olefin comonomer in the presence of a polymerisation catalyst in a diluent in a loop reactor which comprises at least 2 horizontal sections and at least 2 vertical sections to produce a slurry comprising solid particulate olefin polymer and the diluent wherein the Froude number in at least 20% of the length of the vertical sections of the reactor loop is less than 85% of the Froude number in at least 20% of the length of the horizontal sections of the loop is disclosed. | 10-08-2009 |
20100008829 | TRANSFER PIPE BETWEEN LOOP REACTORS - The present invention discloses a transfer system between the first and second reactors in a double loop reactor that is equipped to reduce clogging in the transfer lines by providing a regulation mechanism arranged to insure equivalent flushing in each transfer line. | 01-14-2010 |
20100215550 | PUMPING APPARATUS AND PROCESS FOR POLYMERIZATION IN LOOP REACTORS - An olefin polymerization process and apparatus wherein a fluid slurry comprising monomer, diluent and catalyst is circulated in a continuous loop reactor by two or more pumps. The process and apparatus allow operating the reaction at significantly higher solids content in the circulating fluid slurry. In a preferred embodiment, the fluid slurry is circulated by two impellers arranged so that the downstream impeller benefits from the rotational energy imparted by the upstream impeller. An olefin polymerization process operating at higher reactor solids by virtue of more aggressive circulation has improved efficiencies, particularly in larger-volume reactors. | 08-26-2010 |
20110002816 | POLYMERISATION REACTOR - A tubular reactor for use in polymerisation reactions is described, having a design pressure P | 01-06-2011 |
20110150711 | Loop Reactor for Emulsion Polymerisation - A polymerization reactor comprising a circulation loop, an inlet for raw material, an outlet, driving means for circulating a reactor charge within the circulation loop, and a pig station for storing, launching, and receiving cleaning pigs. The pig station comprises a lid to cover an opening enabling removal of the cleaning pig. The pig station is constructed as a box with a cylindrical bore connected at both ends to the circulation loop, the bore having a central part with a diameter which is larger than the inner diameter of the circulation loop. At a transitional part at the outer ends of the bore the bore diameter narrows down to be substantially equal to the inner tube diameter of the circulation loop. Over at least a part of the inner bore substantially half of the circular cross-section is formed in the removable lid. | 06-23-2011 |
20120070345 | METHODS AND SYSTEMS FOR CONTROLLING POLYMER PARTICLE SIZE - Techniques are provided for producing polymer particles of a size just slightly larger than the size of polymer fines. The technique may prevent or limit the occurrence of reactor fouls associated with large polymer particles. The technique also may provide a greater weight percentage of solids in the reactor. The desired polymer particle size may be achieved by employing a catalyst having particles of a size determined based on the expected catalyst productivity. In certain embodiments, the catalyst particle size may be determined based on the expected catalyst productivity, the polymer particle density, the catalyst particle density, and/or the polymer particle size. | 03-22-2012 |
20120093693 | Multiple Loop Reactor for Olefin Polymerization - The present invention provides a multiple loop reactor suitable for polymerizing olefins comprising at least two interconnected loop reactors, whereby said connection essentially consists of one or more transfer lines suitable for transferring polymer slurry from a reactor to another reactor and whereby said transfer line extends substantially horizontally. The invention further relates to a process for producing olefin polymers in a multiple loop react or according to the invention. The invention also relates to the use of a transfer line for transferring polymer slurry from a reactor to another reactor in a multiple loop reactor comprising at least two interconnected loop reactors, whereby said transfer line extends substantially horizontally. | 04-19-2012 |
20130022508 | SYSTEM FOR ENHANCED RECOVERY OF TANGENTIAL ENERGY FROM AN AXIAL PUMP IN A LOOP REACTOR - An axial pump system cooperative with an elbow or other pipe section improves conversion of tangential to axial flow of a slurry flowing through a loop reactor by including both primary and secondary outlet guide vanes in the pipe section. The secondary guide vanes have “see through” access from the outlet end of the pipe section, while the primary guide vanes have “see through” access from the inlet side of the pipe section. Pump energy efficiency is improved, and friction of polymer particles on the reactor loop and pump sidewalls is reduced, thereby reducing the amount of polymer decay and increasing the percentage of useable and saleable product obtained from the reactor. Guide vanes can be straight or curved. Curved guide vanes can have inlet angles approximating the absolute flow angle of the fluid, and/or outlet angles approximating 0 degrees relative to the meridianal axis of the pipe section. | 01-24-2013 |
20130095001 | Process for Improving the Polymerization of Ethylene and One or More Optional Comonomer(s) in a Polymerization Loop Reactor - The present invention relates to a process for improving the polymerization of ethylene and one or more optional co-monomer(s) in a polymerization loop reactor characterized in that said process comprises the step of controlling the hydrogen/monomer ratio along the path of the reactor by multiple, spatially separated, feeding of hydrogen along the path of the loop reactor. In particular, the invention provides a process for controlling, and preferably narrowing, the molecular weight distribution of the produced polymer particles. In another aspect, the invention relates to a polymerization loop reactor suitable for the polymerization process of ethylene and an optional olefin co-monomer, wherein the molecular weight distribution of the produced ethylene polymer can be controlled. | 04-18-2013 |
20140140894 | POLYOLEFIN PRODUCTION WITH MULTIPLE POLYMERIZATION REACTORS - A polyolefin production system including: a first reactor configured to produce a first discharge slurry having a first polyolefin; a second reactor configured to produce a second discharge slurry having a second polyolefin; and a post-reactor treatment zone having at least a separation vessel configured to receive the second discharge slurry or both the first discharge slurry and the second discharge slurry. | 05-22-2014 |
20140334984 | REACTOR FOR PREPARING POLYOLEFIN - The invention relates to a process for preparing polyolefin in a loop reactor. The polymer is prepared by polymerizing olefin monomers in the presence of a catalyst to produce a polyolefin slurry while pumping said slurry through said loop reactor by means of a pump. The present process is characterized in that the catalyst is fed in the loop reactor at a distance to the pump. The invention allows production of the polymer with advantageous properties while leading to fewer blockages of the reactor. | 11-13-2014 |
422133000 | Generating foamed plastic | 1 |
20100040509 | Method and plant for the manufacture of polymer particles - The method for the manufacture of foamed or foamable polymer particles employs a mixture of a polymer melt and a recycled polymer melt produced from recycled, propellant-containing polymer particles. The associated plant for the manufacture of the foamed or foamable polymer particles is provided with an apparatus for the processing of recycled, propellant-containing polymer particles. | 02-18-2010 |
422134000 | Including plural sequential reaction stages | 14 |
20090047186 | MODULAR DEVICE FOR THE CONTINUOUS DEGASSING AND PRODUCTION OF POLYMER PRECONDENSATE WITH HIGH REACTION PRODUCT SURFACE TO VOLUME RATIO WITH GENTLE TREATMENT OF THE REACTION PRODUCT MASS - A modular device for the continuous degassing of reaction products, such as of a carboxylic acid or a polycarboxylic acid with a multi-functional alcohol suitable for application in the production of precondensates (or also prepolymers), has a heated enclosure in which a plurality of modules are stacked one above the other, each said module having a base. There is a vapor inlet to the uppermost module and a discharge port at the lower most module with at least one module intermediate the uppermost and lowest modules to provide space for expansion of the vapor. The base of each module preferably is concave and there are conduits that provide flow communication between the modules. | 02-19-2009 |
20090208381 | REACTOR FOR THE CONTINUOUS AND SIMULTANEOUS PRODUCTION OF DIFFERENT POLYESTER PRODUCTS HAVING ADJUSTABLE VARIABLE VISCOSITY, THE PROGRESS OF THE PROCESS BEING REGULATED VIA THE HYDRAULIC DRIVE SYSTEM - A device for degassing a flowable, viscous and pasty product includes a reactor having a product inlet and a product discharge outlet. A plurality of rotors each defining a reaction zone are located side-by-side in the reactor and a separate driving system mounted outside of the reactor for rotating each rotor with each driving system being an hydraulic system. | 08-20-2009 |
20090232711 | Slurry phase polymerisation process - A process comprising polymerising in a loop reactor an olefin monomer optionally together with an olefin commoner in the presence of a polymerisation catalyst in a diluent to produce a slurry comprising solid particulate olefin polymer and the diluent wherein the Froude number is maintained at or below 20 is disclosed. | 09-17-2009 |
20090246092 | Flushing in a Multiple Loop Reactor - The present invention discloses multiple loop reactor wherein one of the settling legs transferring polymer product from one loop to a further loop can be taken out of service or re-opened without interfering with the operation of said multiple loop reactor. | 10-01-2009 |
20100158764 | Apparatus for Improving Flow Properties of Crude Petroleum - A process and apparatus for improving flow properties of crude may include processing a first crude stream, which may in turn include cracking the first crude stream with catalyst to form a cracked stream and spent catalyst, hydrotreating a portion of the cracked stream and then mixing the hydrotreated stream with an unprocessed second crude stream. | 06-24-2010 |
20100316536 | Process and Apparatus for Oligomerization in Multiple Stages with Single Fractionation Column - In an oligomerization process comprising at least two oligomerization reactors, at least portions of product streams from two reactors are separated in the same separator vessel. In an embodiment, a liquid product stream from the first oligomerization reactor is fed to a fractionation column and a side cut from the fractionation column feeds the second oligomerization reactor. | 12-16-2010 |
20110158856 | PROCESS FOR PRODUCTION OF AMPHOTERIC ELECTROLYTE RESIN BY CONTINUOUS BULK POLYMERIZATION AND APPARATUS FOR THE PRODUCTION - A continuous polymerization apparatus is provided for producing an amphoteric electrolyte resin by continuous bulk polymerization at low cost, which apparatus includes a reaction vessel, the reaction vessel including at least four polymerization zones adjacent to each other in series, each polymerization zone being separated by a partition plate, the partition plates admitting a stirring shaft with stirrers, each of the polymerization zones having a thermosensor for sensing temperature within the polymerization zone, a heating device for heating the polymerization zone and a cooling device for cooling the polymerization zone. | 06-30-2011 |
20110243797 | APPARATUS FOR OLIGOMERIZING DILUTE ETHYLENE - The apparatus converts ethylene in a dilute ethylene stream that may be derived from an FCC product to heavier hydrocarbons. The oligomerization reactor is in communication between a primary absorber column and a secondary absorber column in an FCC product recovery section. The oligomerization catalyst may have a low silica base with a Group VIIIB metal and operate at low pressure without excessive deactivation. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, hydrogen and ammonia. At least 40 wt-% of the ethylene in the dilute ethylene stream can be converted to heavier hydrocarbons. | 10-06-2011 |
20120076696 | Apparatus for hydrogenation and method for hydrogenating conjugated diene polymer by employing the apparatus - The present invention provides an apparatus and a method for continuous hydrogenation of conjugated diene polymer. By feeding the conjugated diene polymer, a catalyst composition and a hydrogen to the apparatus for hydrogenation. This apparatus for hydrogenation includes at least one hydrogenation reaction unit each comprising at least one a hydrogenation reactor with an outlet and at least one heat exchanger. In the hydrogenation reaction unit, the conjugated diene polymer, the catalyst composition and the hydrogen are mixed in a non-mechanical mixing mode and proceed hydrogenation with heat exchanger being connected to the outlet of the hydrogenation reactor. | 03-29-2012 |
20130142699 | METHOD AND DEVICE FOR THE DECONTAMINATION OF PLASTIC FLAKES - A method for preparing contaminated plastics ground into flakes, such as RPET or such polymers, having at least decontamination and SSP treatment steps, with at least one reactor, with heating to the process temperature taking place essentially outside the reactor. Also, a device for carrying out the method, and having at least one decontamination reactor and at least one SSP reactor, a device for heating plastic flakes to the process temperature being arranged upstream of the decontamination reactor. Also an SSP reactor having at least two individual reactors, and preferably between 3 and 7 individual reactors. | 06-06-2013 |
20130224078 | SYSTEM FOR PRODUCING STEAM USING HEAT RECOVERED FROM A POLYMERIZATION REACTION - The present invention relates to a process for producing steam using heat recovered from a polymerization reaction. In particular, the present invention relates to a process for producing steam using heat recovered from a polymerization reaction for producing polyolefin, comprising the steps of: thermally contacting said polymerization reaction with a cooling fluid such that the cooling fluid removes heat from said reaction, thermally contacting at least part of said cooling fluid with at least one absorption cycle thereby transferring heat from the cooling fluid to said absorption cycle, using said absorption cycle to produce steam from a condensate, wherein the cooling fluid is used as a hot source for heating at least one evaporator and at least one generator comprised in said at least one absorption cycle. The present invention also relates to a process for cooling a polymerization reaction using a process as described herein. Said invention also relates to a polyolefin producing unit. | 08-29-2013 |
20140170028 | PROCESS AND APPARATUS FOR RECOVERING PRODUCT - A process and apparatus are disclosed for recovering a product stream by fractionation perhaps with compression of a C | 06-19-2014 |
20140301903 | Plants and Processes for Forming Polymers - The present invention relates to a process of forming a polymer, the process comprising polymerizing olefin monomers to form a reaction mixture, treating the reaction mixture to form a first polymer-rich phase, treating the first polymer-rich phase to form a second polymer-rich phase, and devolatilizing the second polymer-rich phase, the process further comprising at least one step of adjusting the temperature of a first and/or the second polymer-rich phase before the devolatilization. The present invention also relates to a plant that is useful for the process provided above. | 10-09-2014 |
20140377137 | SYSTEM FOR RECYCLING PRODUCT STREAMS SEPARATED FROM A HYDROCARBON-CONTAINING FEED STREAM - The present invention relates to a process for recycling product streams that have been separated from a hydrocarbon-containing feed stream comprising olefin monomer, olefin co-monomer, hydrocarbon diluent and components such as H | 12-25-2014 |
422135000 | Including reactant agitating means in reaction chamber | 13 |
20080226513 | Rotating Stirring Device with Substantially Narrow Distribution of Energy Dissipation Rate - A rotating stirring device for generating substantially narrow distribution of energy dissipation rate and avoiding presence of Taylor vortices is disclosed. The device includes an outer member ( | 09-18-2008 |
20090041634 | Nucleic Acid Synthesizers - The present invention relates to nucleic acid synthesizers and methods of using and modifying nucleic acid synthesizers. For example, the present invention provides highly efficient, reliable, and safe synthesizers that find use, for example, in high throughput and automated nucleic acid synthesis, as well as methods of modifying pre-existing synthesizers to improve efficiency, reliability, and safety. | 02-12-2009 |
20090053114 | Reactor For The Treatment Of Highly Viscous Plastic Melts - The invention relates to a reactor for the treatment of highly viscous plastic melts, comprising a horizontal, cylindrical container ( | 02-26-2009 |
20090117013 | PROCESS FOR CONTINUOUS PREPARATION OF HIGH MOLECULAR WEIGHT POLYESTERS BY ESTERIFICATION OF DICARBOXYLIC ACIDS AND/OR TRANSESTERIFICATION OF DICARBOXYLIC ACIDS WITH DIOLS AND/OR MIXTURES THEREOF AND AN APPARATUS THEREFOR - The present invention relates to a method for the continuous production of high-molecular polyesters by esterification of dicarboxylic acids and/or transesterification of dicarboxylic acid esters with diols and/or mixtures thereof in the presence of catalysts with formation of a prepolymer in a tower reactor and polycondensation thereof to form a high-molecular polyester in a polycondensation reactor, a prepolymer with >40 to 70 repeat units (DP) being produced in the tower reactor and this prepolymer being polycondensed in only one further reactor to form a polyester with >150 to 205 DP. | 05-07-2009 |
20090208382 | SYSTEM AND PROCESS FOR PRODUCTION OF POLYVINYL CHLORIDE - A method is disclosed for producing polyvinyl chloride which includes mixing a vinyl chloride solution with an initiator solution in at least one high shear mixing device comprising at least one rotor/stator set producing a rotor tip speed of at least 5.1 m/sec (1000 ft/min), to form a polymerization mixture; and allowing the mixture to polymerize by free radical polymerization to form polyvinyl chloride. The polymerization mixture may be subjected to free radical polymerization conditions comprising a temperature in the range of about 20° C. to about 230° C. In some embodiments, the high shear mixing device produces a shear rate of at least 20,000 s | 08-20-2009 |
20090232712 | ORGANIC SYNTHESIZER - To provide an organic synthesizer that can conduct a pressure reaction and an atmospheric reaction in one organic synthesizer and can realize attachment of reaction vessels to the organic synthesizer and detachment of the reaction vessels from the organic synthesizer without applying any load to gas supply/discharge pipes. | 09-17-2009 |
20140086801 | POLYMERIZATION REACTOR FOR BUTYL RUBBER PRODUCTION - A low temperature polymerization reactor for the production of butyl rubber by catalytic polymerization of isobutylene with small amount of a conjugated diolefin such as isoprene includes: an extended upper head with fluid deflector fixed to the top tube-sheet, the shapes of the head and deflector being optimized in order to reach a very homogeneous slurry velocity in the rows of tubes and to minimize the pressure drop due to the inversion of flow from up-flow to down-flow and to the entrance of the slurry in the tubes; an hemispheric bottom head with fluid deflectors placed between the impeller and the bottom itself and designed to minimize the pressure drop due to the inversion of flow from down-flow to up-flow; and straightening baffles inside the draft tube, which shape and dimensions are optimized to turn the radial velocity components produced by the rotation of the impeller into axial velocity components. | 03-27-2014 |
20140328722 | METHOD AND APPARATUS FOR PREPARING POLYMER BEADS OF UNIFORM PARTICLE SIZE BY SUSPENSION POLYMERISATION - Monomer solution and liquid solution immiscible with the monomers in the monomer solution are cocurrently jetted upwardly in a pulsating manner in a reaction vessel. Monomer droplets are allowed to rise up in a controlled and smooth manner under the dynamic forces exerted by differential flow rate and differential pressure between the monomer and liquid solutions and the differential densities between the monomer and liquid solutions without causing coalescence, agglomeration and breakup of the monomer droplets and to stabilize by partial polymerization of the droplets at 50-60° C. The monomer droplets flow out horizontally into a polymerization reactor and get polymerized in the polymerization reactor under agitation at 80-85° C. The polymer beads are dried at 80-100° C. and sieved. | 11-06-2014 |
20150290616 | Process and Apparatus for Continuous Solution Polymerization - Provided are processes and apparatuses for continuous solution polymerization which can mitigate fouling during the production of propylene-based polymers. | 10-15-2015 |
20150290617 | APPARATUS AND METHOD OF REACTING POLYMERS PASSING THROUGH METAL ION CHELATED RESIN MATRIX TO PRODUCE INJECTABLE MEDICAL DEVICES - The present disclosure relates to an apparatus and process for forming medical devices from an injectable composition. The apparatus includes a supply assembly configured to maintain and selective dispense a first precursor and a second precursor, a mixing assembly configured to mix the first and second precursors, and at least one catalyzing element including a transition metal ion to aid in the polymerization of the first and second precursors. The process includes dispensing a volume of the first precursor and a volume of the second precursor into a mixing assembly and mixing the first and second precursors. The first and second precursors each possess a core and at least one functional group known to have click reactivity with each other. The mixed precursors are contacted with a transition metal catalyst to produce a flowable composition for use as a medical device. | 10-15-2015 |
20150353677 | POLYMER PRODUCTION APPARATUS - To provide a polymer production apparatus, which contains: a first supply unit configured to supply raw materials including a monomer; a second supply unit configured to supply a compressive fluid; a contact unit configured to bring the monomer into contact with the compressive fluid; and a reaction unit configured to allow the monomer, which has been brought into contact with the compressive fluid, to react in the presence of the compressive fluid, wherein the reaction unit contains one, or two or more extrusion devices, and one, or two or more stirring devices. | 12-10-2015 |
422136000 | And means rotatably mounting reaction chamber | 2 |
20100008830 | RADIAL MIXING DEVICES FOR ROTATING INCLINED REACTORS - Disclosed in this specification is the design for an internal mixing device which increases the plug flow like behaviour of the rotating inclined reactor. | 01-14-2010 |
20140328723 | PROCESS FOR CONTINUOUSLY PRODUCING WATER-ABSORBING POLYMER PARTICLES - A process for continuously producing water-absorbing polymer particles by polymerizing a monomer solution comprising acrylic acid and/or salts thereof, wherein the acrylic acid supplied has a dimeric acrylic acid content of at least 0.02% by weight and the dimeric acrylic acid content is kept essentially constant. | 11-06-2014 |
422138000 | With heat exchanger for reaction chamber or reactants located therein | 10 |
20090074628 | Thermal cycler - A thermalcycler includes a first thermalcycler body section having a first face and a second thermalcycler body section having a second face. A cavity is formed by the first face and the second face. A thermalcycling unit is positioned in the cavity. A heater trace unit is connected to a support section, to the first thermalcycler body section, to the second thermalcycler body section, and to the thermalcycling unit. The first thermalcycler body section and the second thermalcycler body section are positioned together against the support section to enclose the thermalcycling unit and the heater trace unit. | 03-19-2009 |
20110097244 | Bulk polymerization reactors for producing drag reducer - A polymerization reactor for creating drag-reducing polymer having a reservoir and at least one heat exchanger plate in fluid communication with a coolant source, wherein each heat exchanger plate may be disposed on a lid. The heat exchanger plates are treated and/or covered to provide that the exchanger plates can be readily disengaged from the drag-reducing polymer. The polymerization reactors of the present invention permit large amounts of polymer to be formed in each reactor batch. Preferably, polymers are formed in the polymerization reactor by bulk polymerization. Methods for forming drag-reducing polymers are also disclosed. | 04-28-2011 |
20110150712 | ISOOLEFIN-DIOLEFIN PRODUCTION PROCESS AND APPARATUS THEREFORE - In an isoolefin-diolefin rubber production process (e.g. a butyl rubber production process), the cold rubber slurry produced in the reaction vessel is transported from the reaction vessel to the flash tank during which time the cold slurry may be expressed to separate at least part of the cold liquid reaction medium from the isoolefin-diolefin rubber. The separated cold liquid reaction medium is transported off stream, for example by a mechanical filter, where it can be recycled back into the reaction vessel and/or where it can be used to cool a feed stream or streams of the reaction components. The isoolefin-diolefin rubber and the residual liquid reaction medium are transported to a flash tank for further processing. The ability to separate and recycle cold liquid reaction medium makes the process more economical. In one aspect, the slurry may be transported from the reaction vessel to the flash tank by a self-cleaning fully intermeshing co-rotating twin screw extruder, which helps overcome the problem of plugging due to rubber sticking to the surfaces of the slurry transfer apparatus. | 06-23-2011 |
20110300025 | ENERGY EFFICIENT POLYOLEFIN PROCESS - A manufacturing process for producing polyolefin, having a feed system, a reactor system including at least one polymerization reactor, a diluent/monomer recovery system, a fractionation system, and an extrusion/loadout system having an extruder. The manufacturing process is configured to consume less than 325 kilowatt-hours of electricity per metric ton of polyolefin produced. | 12-08-2011 |
20120219463 | Catalyst Feed Systems and Methods for Using the Same - Catalyst feed systems and processes utilizing such systems are described herein. Some embodiments disclosed herein relate to a process for improving the flowability of catalyst in a catalyst feed system, including providing a catalyst feed vessel with at least one heat exchange system for maintaining the catalyst system temperature below a critical flow temperature. Also disclosed is a catalyst feed system for the polymerization of olefins including a catalyst feed vessel; and a heat exchange system for maintaining a temperature of a catalyst within the catalyst feed vessel. Additionally disclosed is a process for polymerization of olefins including maintaining a supported catalyst in a catalyst feed vessel below a critical flow temperature of the catalyst; feeding the catalyst to a polymerization reactor; and contacting the catalyst with an olefin to form a polyolefin. | 08-30-2012 |
20140065024 | FLASHLINE HEATER SYSTEM AND METHOD - The present embodiments provide a system and method for separation within a polymer production process. Specifically, a flashline heater configured according to present embodiments may provide more time than is required for complete vaporization of liquid hydrocarbons that are not entrained within a polymer fluff produced within a polymerization reactor. Such extra time may allow for liquid hydrocarbons that are entrained within the polymer fluff to be vaporized. | 03-06-2014 |
20140134057 | CHEMICAL PRODUCTION SYSTEM - Systems and methods of producing chemical compounds are disclosed. An example chemical production system includes an intake chamber having intake ports for entry of a gas mixture. An igniter ignites the gas mixture in the intake chamber. A nozzle restricts exit of the ignited gas mixture from the intake chamber. An expansion chamber cools the ignited gas with a cooling agent. The expansion chamber has an exhaust where the cooled gas exits the expansion chamber. A chemical compound product is formed in the expansion chamber. | 05-15-2014 |
20140377138 | Method and Device for Producing Polyphosphoric Acid - A method and device for producing polyphosphoric acid burns a fuel in combustion air in a combustion chamber, sprays a spray fluid comprising substantially pure orthophosphoric acid and undertakes polymerization-condensation of the pure orthophosphoric acid. A polyphosphoric acid in the form of an acid mist accompanied by formation of gases which mix with combustion gases resulting from burning of the fuel is formed to reach a predetermined temperature, wherein the mixture causes sudden lowering of combustion gas temperature. The acid mix is separated from the gas mixture and the polyphosphoric acid is collected at a bottom of the combustion chamber and the gas mixture is outputted via a lower part of the combustion chamber separate from the collection of polyphosphoric acid. | 12-25-2014 |
20160038883 | POROUS FILM MANUFACTURING METHOD AND APPARATUS - A method of manufacturing a porous film includes a decomposition step of introducing a porous film precursor which is formed by coagulating an undiluted film forming solution containing a hydrophilic polymer and a hydrophobic polymer, into a decomposition container; bringing a heated chemical containing an oxidizing agent into contact with the porous film precursor in the decomposition container; warming the porous film precursor in contact with the chemical; and decomposing the hydrophilic polymer remaining inside the porous film precursor using the oxidizing agent. An apparatus for manufacturing a porous film includes a decomposition device provided with the decomposition container. | 02-11-2016 |
20160039950 | APPARATUS FOR PRODUCING WATER-ABSORBENT RESIN - In an apparatus for producing the water-absorbent resin, gas heated by the polymerization heat accompanied by a polymerization reaction in a reactor main body flows through a first pipe into a heat exchanging structure, and a cooled fluid obtained by the cooling flows through a second pipe into the reactor main body. In the apparatus, a first pipe temperature adjusting portion adjusts a temperature of the first pipe to fall within a predetermined temperature range, and a polymerization reactor temperature adjusting portion adjusts a temperature of an upper portion of the reactor main body to fall within a predetermined temperature range. | 02-11-2016 |