序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
181 Forming shaped abrasive particles US13731771 2012-12-31 US08753558B2 2014-06-17 Michael D. Kavanaugh
A method of forming a shaped abrasive particle includes extruding a mixture into an opening in a screen within an application zone and translating the screen and belt to a release zone and separating the screen and belt to form a precursor shaped abrasive particle on the belt, wherein the screen and belt are separated at a release angle of at least about 15° and not greater than about 45°, wherein the release angle is defined as an angle between a surface of the screen and a surface of the belt.
182 HIGH-FLUIDITY NON-CAKING DIANHYDROHEXITOL PELLETS US13824613 2011-09-30 US20130281718A1 2013-10-24 Mathias Ibert; Jerome Saint Pol; Herve Wyart
Dianhydrohexitol pellets, whose fluidity is preserved even after lengthy storage, include between 90% and 100%, preferably between 95% and 100%, and more preferentially between 97% and 100% of dianhydrohexitols by weight, on a dry weight basis, and have the particularity of not being subject to caking. A process for preparing the dianhydrohexitol pellets is also described.
183 TRANSFER ASSISTED SCREEN PRINTING METHOD OF MAKING SHAPED ABRASIVE PARTICLES AND THE RESULTING SHAPED ABRASIVE PARTICLES US13908268 2013-06-03 US20130255162A1 2013-10-03 Dennis G. Welygan; Dwight D. Erickson; John T. Boden
Shaped ceramic articles can be obtained by screen printing the desired shapes from a dispersion of a precursor of the ceramic onto a receiving surface using a transfer assisted technique that applies a differential pressure, at least partially drying the screen printed shapes, and firing them to generate the shaped ceramic articles. Shaped abrasive particles made using lower viscosity sol gels that tended to flow or creep after the screen printing formation were found to have higher grinding performance over screen printed shaped abrasive particles made with higher viscosity sol gels.
184 Laser Method for Making Shaped Ceramic Abrasive Particles, Shaped Ceramic Abrasive Particles, and Abrasive Articles US13881601 2011-10-21 US20130212952A1 2013-08-22 Dennis G. Welygan; Charles J. Studiner, IV; Dwight D. Erickson; Scott A. Baum; Edward J. Woo; Pingfan Wu; Travis L. Potts
A method of making shaped ceramic abrasive particles includes cutting a layer of ceramic precursor material using a laser beam and forming shaped ceramic precursor particles. Further thermal processing provides shaped ceramic abrasive particles. Shaped ceramic abrasive particles producible by the methods and abrasive articles containing them are also disclosed.
185 FORMING SHAPED ABRASIVE PARTICLES US13731771 2012-12-31 US20130186005A1 2013-07-25 Michael D. Kavanaugh
A method of forming a shaped abrasive particle includes extruding a mixture into an opening in a screen within an application zone and translating the screen and belt to a release zone and separating the screen and belt to form a precursor shaped abrasive particle on the belt, wherein the screen and belt are separated at a release angle of at least about 15° and not greater than about 45°, wherein the release angle is defined as an angle between a surface of the screen and a surface of the belt.
186 Systems and Methods of Pelletizing Heavy Hydrocarbons US12699325 2010-02-03 US20110185631A1 2011-08-04 Anand Subramanian; Raymond H. Floyd; Vasant K. Patel
Systems and methods for pelletizing a molten heavy hydrocarbon that can be extruded from a drop former to create a plurality of droplets that are subsequently quenched in a cooling media to create asphaltenic pellets. The asphaltenic pellets can be solidified by transferring heat from the droplets to the cooling media to provide the solid asphaltenic pellets. The solid asphaltenic pellets can then be separated from the cooling media which can be recycled for use.
187 Pastillation of ammonium sulfate nitrate US12415312 2009-03-31 US07985393B2 2011-07-26 Michael R. Smith
A process is presented for the production of ammonium sulfate nitrate. The process provides for producing a highly uniform product and having a substantially uniform size. The process includes reacting ammonium sulfate and ammonium nitrate to form an FASN slurry melt. The slurry melt is continuously stirred and heated to keep the slurry melt under a shear thinned condition and at a uniform temperature until the slurry melt is extruded, cooled and solidified.
188 METHOD AND DROP FORMER FOR PRODUCING TABLETS AND METHOD FOR PRODUCING A SULFUROUS FERTILIZER US12734940 2008-12-03 US20100288005A1 2010-11-18 Hans-Kurt Schromm; Albert Baeder; Matthias Kleinhans
1.1 The invention relates to a method for producing tables made of mixtures of a plurality of materials, and a method for producing a sulfurous fertilizer. 2.1. The invention relates to a method for producing tablets made of mixtures of a plurality of materials, particularly urea mixtures, having the following steps:—producing a liquid melt of a first material,—adding at least one further material in solid or liquid form to the melt for producing a mixture,—output of drops of the mixture onto a steel belt by means of a drop former having a rotating, perforated outer drum,—solidification of the drops of the mixture on the steel belt into tablets, wherein the at least one additional material is mixed into the liquid melt in liquid form immediately before the drop former or into the liquid melt in solid form upstream of a two-stage heated grinding and mixing unit. 2.2. Use for producing fertilizer, for example.
189 Method and Installation for the Production of Pellets from Biomass in a Pelletizing Press for Use as Fuel in Furnaces US12758370 2010-04-12 US20100263268A1 2010-10-21 Gernot von Haas
A method and an installation for producing pellets from prepared biomass in a pelleting press for use as fuel in fireplaces. The biomass is made of fibers, shavings or chippings containing cellulose and/or lignocellulose, with or without a binding agent and/or additives, and after being prepared is stored in a biomass bunker. The method includes: biomass discharged from the biomass bunker into a scatter device, a mat made of the biomass having a substantially uniform weight per unit area formed by the scatter device on a molding belt, the mat produced on the molding belt examined by an examining device for defective spots and/or foreign substances, and the mat supplied to a pelleting press. At least parts of the mat or a section of the mat include defective regions and/or foreign substances separated from the method upstream of the pelleting press.
190 Pastillation of Ammonium Sulfate Nitrate US12415312 2009-03-31 US20100242556A1 2010-09-30 Michael R. Smith
A process is presented for the production of ammonium sulfate nitrate. The process provides for producing a highly uniform product and having a substantially uniform size. The process includes reacting ammonium sulfate and ammonium nitrate to form an FASN slurry melt. The slurry melt is continuously stirred and heated to keep the slurry melt under a shear thinned condition and at a uniform temperature until the slurry melt is extruded, cooled and solidified.
191 Process for the manufacture of chemical absorbents and chemical absorbent formulations US09284400 1999-07-02 US06562748B2 2003-05-13 Michael John Holder
A soda lime formulation comprises calcium hydroxide in admixture with sodium hydroxide and potassium hydroxide and water, and further comprises a zeolite such as sodium aluminium silicate. The formulation has improved mechanical strength and may be prepared in granular form by mixing its constituents with water to form a paste and passing the paste between a pair of rollers having hemispherical depressions therein.
192 Drop forming method and sulphur polymer concrete process US09298609 1999-04-26 US06228905B1 2001-05-08 Allan F. Soderberg; Paul Terness; Derril Locke Thomas
A method of transforming a molten material or melt into discrete solid particles comprises forming the melt into prills by passing the melt through a perforated member, dropping the prills onto a bed of powdered material, such as silica flour, to coat the prills with the material in the bed and permitting the prills to cool, thereby to solidify into discrete solid particles. In one embodiment, the melt comprises at least two components such as elemental sulphur and an olefinic hydrocarbon, which are subjected to a chemical reaction, such as the polymerization of the olefinic hydrocarbon with the sulphur to form a sulphur polymer stabilizer. A method of producing a sulphur concrete incorporating the sulphur polymer stabilizer is also provided.
193 Method and apparatus for purifying chemical substances US581594 1996-03-14 US5810892A 1998-09-22 Axel Konig; Joachim Ulrich
After being subjected to a melt crystallization operation, a crystal-containing melt is formed into particles of the same size and shape and then conducted in counter-flow relationship to washing liquid in a washing column. The crystal-containing melt can be formed into particles by a device which deposits the crystal-containing melt as identically sized drops onto a cooling belt. The particles can be completely hardened or only partially hardened when entering the washing column.
194 Process for forming crystalline polymer pellets US694084 1996-08-08 US5744074A 1998-04-28 Jan M. Stouffer; Elwood Neal Blanchard; Kenneth Wayne Leffew
This invention relates to a process and apparatus for forming a polyester polymer into particles. More particularly, this invention relates to a process and apparatus for forming crystalline, uniform pellets from an amorphous polyester melt. The polyester pellets have utility, for example, as feedstock for a process for producing higher molecular weight polyesters.
195 Extrusion apparatus having a nozzle-headed drum US693235 1991-04-26 US5286181A 1994-02-15 Jules Schwager
An apparatus for extruding a mass onto a moving support mechanism. A first cylinder for receiving the mass within its interior has an exit channel through which the mass is forced. A second cylinder is disposed about the first cylinder for relative rotation with respect to the first cylinder. The second cylinder includes a plurality of forming channels which repeatedly aligned with the exit channel of the first cylinder during relative rotation of the cylinders and through which the mass is forced. A plurality of nozzles are formed in the outer surface of the second cylinder and are shaped and arranged for guiding the excess mass away from the exit ends of the forming channels during at least a portion of the rotational movement of said second cylinder and for guiding the excess mass into the extruded mass at the extruding position of the apparatus.
196 Device for continuous production of ceramic superconductor US737682 1991-07-30 US5235158A 1993-08-10 Paolo Marini; Mario Tului; Stefano Fortunati
A device for the continuous production of ceramic conductors, for example, yttrium, barium and copper oxide type, which includes an endless belt and a tank and conduit for feeding solution from the tank onto the endless belt to form a liquid layer containing the desired proportion of metal ions on the endless belt. The endless belt passes through a furnace where the liquid is evaporated from the liquid layer and the residual metal salts are treated in an oxidizing atmosphere to produce ceramic oxides. A scraper is provided to remove the resulting ceramic oxides from the endless belt.
197 Apparatus for the production of granules from two-phase mixtures US547492 1983-11-01 US4578021A 1986-03-25 Konrad Schermutzki
An apparatus produces granules from two-phase mixtures wherein an initial substance is enriched with crystal nuclei in a temperature controlled precrystallizer and the resultant precrystallized melt is fully crystallized on a cooling surface. A droplet former is disposed over the cooling surface and includes inner and outer telescoping tubes. The inner tube communicates downstream with the precrystallizer and has a plurality of outlet orifices for conducting the precrystallized melt outwardly therethrough. The outer and inner tubes are arranged for relative rotation. The outer tube has a plurality of discharge orifices which are intermittently alignable with the outlet apertures in response to relative rotation between the tubes for discharging drops of precrystallized mass onto the cooling surface.
198 Apparatus for the production of molded bodies from filter cakes US69793 1979-08-27 US4283285A 1981-08-11 Peter Paschen; Chatty Rao; Helmut Preuss
An apparatus for producing agglomerates from a rotary filter such as a rotating filter drum, which includes a perforated filter member on the filter, a slotted member disposed on the filter member and a sludge or slurry storage means disposed above the slotted member, the storage means discharging solid particles of the sludge into the slotted member essentially in the direction of solid sedimentation.
199 Apparatus for preparing granular material by means of a strip caster US88115 1979-10-25 US4256581A 1981-03-17 Karl G. Boman; Konrad Schermutzki
An apparatus for the preparation of granulate from hot-melting mixes comprises a pourer connected by a filter-containing conduit to at least one mixing and melting device. The strip pourer is disposed above a cooling conveyor which feeds to a crushing device. The pourer comprises a heated tubular body provided on its under side with discharge nozzles arranged in at least one row. A filter is disposed within the tubular body across the discharge nozzles to prevent unwanted particles from reaching the nozzles.
200 Device for feeding a baking apparatus for green pellets US3630414D 1969-07-01 US3630414A 1971-12-28 PARMENTIER PAUL VICTOR
The invention relates to the feeding of baking apparatus with green pellets, for instance of iron ore, supplied by pelletizing apparatus the output of which may fluctuate. The green pellets coming from the pelletizing apparatus, optionally after screening, is fed to a movable belt conveyor discharging to a fixed belt conveyor which in turn discharges to the baking apparatus. Measuring apparatus measures the mass flow rates of the green pellets discharging from both conveyors. The movable conveyor is moved parallel to the conveying direction of the fixed conveyor at a velocity proportional to the difference between the mass flow rates so that the depth of the layer of green pellets on the fixed conveyor is approximately constant.
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