首页 / 国际专利分类库 / 作业;运输 / 一般的物理或化学的方法或装置 / 化学或物理方法,例如,催化作用,胶体化学;其有关设备 / 使原料颗粒化的一般方法或装置{如,肥料},(金属颗粒化入B22F 9/00,{熔渣颗粒化入C21B 3/06},矿石或废料颗粒化入C22B 1/14;塑料或可塑态物质的机械加工以制得颗粒入B29B 9/00;以其化学组成为特征的肥料颗粒化工艺见C05B至C05G有关组;大分子物质粉末化或颗粒化的化学部分入C08J 3/12);使颗粒材料总体上变得可自由流动,例如使它们成为疏水的
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 Preparation of ultrafine mixed metallic-oxide powders US3681010D 1970-09-14 US3681010A 1972-08-01 MESSIER DONALD R; GAZZA GEORGE E
A METHOD FOR THE PREPARATION OF ULTRAFINE MIXED METALLIC-OXIDE POWDERS COMPRISING THE STEPS OF: COMELTING STOICHIOMETRIC AMOUNTS OF HYDRATED NITRATES OF A LEAST TWO CATIONS, FREEZING THE MELT TO PRODUCE AN INTIMATE MIXTURE OF THE SOLID HYDRATED NITRATES, PARTIALLY DEHYDRATING THE SOLID MIXTURE AT A SUBLIQUIDUS TEMPERATURES AND HEATING THE DEHYDRATED MIXTURE IN ORDER TO DRIVE OFF THE NITROGEN AND DECOMPOSE THE MIXTURE TO THE OXIDE.
182 Hollow spherical articles US3674461D 1970-05-21 US3674461A 1972-07-04 FARNAND JOSEPH REDMOND; PUDDINGTON IRA EDWIN
HOLLOW ARTICLES FREE OF HOLES OR SEAMS OF A METAL SELECTED FROM ALUMINUM, MAGNESIUM, BORON, AND BERYLLIUM ARE PROVIDED BY COATING A SHAPED CORE OF A MATERIAL TRANSFORMABLE DIRECTLY INTO GAS WITH FLAKES OR PARTICLES OF THE METAL, SLOWLY REMOVING THE CORE MATERIAL THROUGH THE PARTICULATE COATING IN GASEOUS FORM, AND CONSOLIDATING THE COATING (E.G. BY FUSING OR SINTERING). COATINGS OF THESE METALS CANNOT BE SATISFACTORILY PREPARED BY REDUCTION OF THEIR SALTS IN SOLUTION. SMALL SPHERES OF A DIAMETER LESS THAN 0.2 INCH (ESPECIALLY 0.005 TO 0.06 INCH) ARE OF PARTICULAR INTEREST.
183 Solidified gas pellets US3660986D 1969-12-03 US3660986A 1972-05-09 HARDT ROBERT C; KOZLOW EDWARD
Carbon dioxide pellets of a high density formed in a manner to break easily into minute pieces yet not agglomerate during shipment, together with a head member for a pellet machine to form pellets of this kind.
184 Method of making spherules of a crystalline nuclear fuel carbide US27264D 1965-08-20 USRE27264E 1972-01-11
METHOD OF PRODUCING NUCLEAR CARBIDE SPHERULES WHEREIN NUCLEAR PARTICLES OF CARBIDE OR OTHER COMPOSITION, ARE HEATED IN AN ISOLATING MEDIUM SUCH AS CARBON TO THE FUSION TEMPERATURE TO PRODUCE SPHERULES. WHEN STARTING WITH NON-CARBIDE PARTICLES ENOUGH CARBON IS INCLUDED TO FORM THE CARBIDE. THE SPHERULES ARE THEN GIVEN A PYROLYTIC CARBON COATING.
185 Process of forming free-flowing, particulate mixtures of phosphates and silicates US3620979D 1968-04-24 US3620979A 1971-11-16 CORLISS DUNCAN SIMMONS; KEAST RUSSELL RAYMOND; LEWIS SAXMAN RICHARD
Free-flowing, fast-dissolving, completely soluble, strong, granular particles containing a mixture of a hydratable alkali metal phosphate and an alkali metal silicate wherein the SiO2 to said phosphate mole ratio is at least 1:1, were produced by maintaining the alkali metal phosphate at a temperature of 60* to 100* C., gradually adding an aqueous solution of alkali metal silicate to the alkali metal phosphate, continually evaporating water from the resulting mixture, controlling the rate of addition of the alkali metal silicate solution so that the resulting mixture is maintained in the form of discrete particles, continuing said alkali metal silicate addition until the discrete, granular particles have an SiO2 to said phosphate mole ratio of at least 1:1, and recovering dry-appearing, granular particles which yield a pH of at least 10.5 in an aqueous 1 percent solution.
186 Compacted pigment compositions US3615809D 1968-09-26 US3615809A 1971-10-26 NAGLE FLOYD B; HOCK KENNETH R; HAYNES WINFIELD SCOTT JR
The invention relates to pigmented or colored thermoplastic polymers and pertains especially to compacted pigment compositions that are readily dispersed in thermoplastic polymers to make uniformly colored or pigmented polymer articles.
187 Free-flowing fused beads of thermoplastic polymers US3592801D 1968-12-12 US3592801A 1971-07-13 ILAVSKY JERRY D; FORD RICHARD W
FREE-FLOWING FUSED BEADS OF NORMALLY SOLID, THERMOPLASTIC ORGANIC POLYMERS SUCH AS POLYETHYLENE ARE PREPARED BY (1) SUSPENDING A FINE POWDER OF THE THERMOPLASTIC POLYMER IN AN AQUEOUS MEDIUM CONTAINING A SMALL AMOUNT OF A NON-REACTIVE, INSOLUBLE SUSPENDING AGENT SUCH AS ZINC OXIDE, (2) HEATING THE RESULTING SUSPENSION TO A TEMPERATURE AT OR ABOVE THE MELTING POINT OF THE POLYMER WHILE SUBJECTING THE SUSPENSION TO AGITATION AND (3) COOLING THE SUSPENSION UNDER CONTINUED AGITATION.
188 Method for agglomerating suspended particles US3577489D 1968-04-26 US3577489A 1971-05-04 ROSENTHAL CHRISTIAN
A PLURALITY OF FINELY SUBDIVIDED SOLID PARTICLES IS CONVERTED INTO A MASS OF DISTINCT AGGLOMERATED BODIES BY SUSPENDING THE SOLID SUBDIVIDED PARTICLES IN WATER HEATED TO AT LEAST 80*C. THE PARTICLES MUST BE SUCH THAT WATER IS INERT THERETO AND WHICH ARE AT MOST SLIGHTLY SOLUBLE IN WATER. THE GRANULATING AGENT IS A SYNTHETIC ORGANIC PLASTIC WHICH IS DISSOLVED IN A LIQUID ORGANIC SOLVENT AT AT LEAST 80*C. THE GRANULATING SOLUTION IS THEN ADDED TO THE SUSPENSION AND THE THUS-FORMED MIXTURE IS MAINTAINED, PREFERABLY UNDER STIRRING, AT AN ELEVATED TEMPERATURE BELOW 100*C. AND SUFFICIENTLY HIGH TO FORM GRANULES OF THE FINELY SUBDIVIDED PARTICLES AND THE GRANULATING AGENT SO THAT A PLURALITY OF AGGLOMERATED BODIES EACH COMPRISING A PLURALITY OF THE FINELY SUBDIVIDED PARTICLES ADHERED TO EACH OTHER BY THE GRANULATING AGENT WILL BE OBTAINED.
189 Enzyme carrying detergent particles US3549541D 1968-05-31 US3549541A 1970-12-22 REINISH MARTIN DAVID
190 Agglomerating pulverulent material by contacting with a film of jetted liquid US3549336D 1966-11-29 US3549336A 1970-12-22 HODEL THEODORE
191 Agglomerated silica bodies and method US3538212D 1968-09-18 US3538212A 1970-11-03 BEAU RAYMOND; FOURNIGUET JEAN
192 Mineral grinding aids US3492138D 1967-05-15 US3492138A 1970-01-27 SERAFIN FRANK G
193 Ion exchange method for preparing metal oxide microspheres US3438749D 1966-10-25 US3438749A 1969-04-15 LONADIER FRANK D; BROWN WILLARD B; FUSHIMI FRED C; SILVER GARY L
194 Process for agglomeration of suspended particles in streaming gases US55314466 1966-05-26 US3410054A 1968-11-12 WILHELM DEITERS
195 Preparation of brittle inorganic polycrystalline powders by shock-wave techniques US47799765 1965-06-16 US3367766A 1968-02-06 JONATHAN BARRINGTON; BERGMANN OSWALD R
196 Cyanuric acid production US38335164 1964-07-17 US3318887A 1967-05-09 MOORE WILLIAM P; FITZ-WILLIAM JR CHARLES B R
197 Method for making metal oxide microspheres US44826065 1965-04-15 US3312631A 1967-04-04 SMITH JEAN G
198 Contacting apparatus and process for forming aggregates US33019463 1963-12-12 US3279924A 1966-10-18 PEEBLES DAVID D
199 Increasing the bulk density of sodium perborate tetrahydrate by mixing with molten perborate US22130362 1962-09-04 US3278276A 1966-10-11 LUDWIG PELLENS; HELMUT HONIG; WILHELM MOSER
200 Production of spheroidized particles US29763563 1963-07-25 US3272615A 1966-09-13 HOFFMAN DANIEL J N; BEETON THOMAS B
1,051,334. Spray-producers. SOUTH AFRICAN IRON & STEEL INDUSTRIAL CORPORATION Ltd. July 25, 1963 [Aug. 1, 1962], No. 29512/63. Heading B2F. [Also in Division C7]. Irregularly shaped particles are spheroidised by swirling them through a flame to melt them at least at their surfaces and then allowing them to pass into a cooling zone. The particles may be of Fe/Si (10 to 25% Si) and may contain Cu or Al. As shown, irregularly shaped particles are fed through a hopper 1 to a Venturi-tube 7 where they are dispersed in preheated air fed from a pipe 5. Combustible gas, supplied through a pipe 11, is fed into a chamber 12 tangentially and thereby swirled. This swirling gas then swirls the air and dispersed particles as they issue from an outlet 9 of a discharge tube 4. The particles swirl through oxidising and reducing zones 14 and 15 of a flame 13, are heated and spheroidised. They pass into a cooling chamber 23 and solidify. The nozzle is provided with a water cooling jacket 22 and reducing gas is fed through a surrounding passage 18 to provide an envelope to the flame. The amount of swirling of the particles can be adjusted by raising or lowering the discharge tube 4. A small proportion of combustible gas may be mixed with the air. Cooling medium for the cooling chamber 23 is supplied through an annular inlet 24 and may also be supplied tangentially to the chamber.
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