141 |
Preparation of powdered resins |
US12999661 |
1961-08-08 |
US3259609A |
1966-07-05 |
SHOZO SATAKE; KENJI TATEBAYASHI |
|
142 |
Apparatus for the segmentation of polymer solutions |
US5892660 |
1960-09-28 |
US3208829A |
1965-09-28 |
TERENZI JOSEPH F |
|
143 |
Alcoholysis of cross-linked vinyl ester polymer |
US78923359 |
1959-01-27 |
US3082194A |
1963-03-19 |
PRIMO IMPERIALE; ADRIANO CELLA |
|
144 |
Method of making plastic pellets |
US71897558 |
1958-03-04 |
US2974135A |
1961-03-07 |
ANDREW EUGENE A |
|
145 |
Method and apparatus for forming pellets of thermoplastic material |
US72687658 |
1958-04-07 |
US2951262A |
1960-09-06 |
ISIDORE DORMAN; HOOS CURTIS G |
|
146 |
Treatment of plastics |
US47041254 |
1954-11-22 |
US2929107A |
1960-03-22 |
ANDREW EUGENE A |
|
147 |
Method for pelleting |
US45823154 |
1954-09-24 |
US2923033A |
1960-02-02 |
BALDWIN WARREN R; BOHN JAMES N |
|
148 |
Method and apparatus for producing regenerated cellulose pellets |
US23891451 |
1951-07-27 |
US2820984A |
1958-01-28 |
SPINA ANTHONY N; BROWN ALFRED S |
|
149 |
Fiber forming apparatus |
US45943654 |
1954-09-30 |
US2784451A |
1957-03-12 |
BOWEN WILLIAM V |
|
150 |
Apparatus for granulating chemical substances |
US24309151 |
1951-08-22 |
US2714224A |
1955-08-02 |
FRANZ SCHAUB |
|
151 |
Electric switch casing |
US1842848 |
1948-04-01 |
US2571859A |
1951-10-16 |
GATES FREDERIC P |
|
152 |
Production of dry powdery thermoplastic compositions |
US77213347 |
1947-09-04 |
US2530852A |
1950-11-21 |
BIXBY WILLARD F |
|
153 |
Process and apparatus for manufacture of shellac |
US73210247 |
1947-03-03 |
US2525970A |
1950-10-17 |
NATHAN SPIER NORMAN; EMANUEL PHILLIPS |
|
154 |
Powdered resin manufacture |
US33237840 |
1940-04-29 |
US2326539A |
1943-08-10 |
PAUL IRANY ERNEST |
|
155 |
Clothes-line clamp. |
US15805417 |
1917-03-28 |
US1249405A |
1917-12-11 |
HUNTLEY ERNEST R |
|
156 |
METHOD FOR PRODUCING POLYMER MICROPARTICLES |
EP15806734 |
2015-06-01 |
EP3153541A4 |
2018-01-10 |
KONDO YOSHINORI; ECHIGO YUJI; KITAMURA AKIRA; TAKEZAKI HIROSHI |
Provided is a method of producing polymer particles characterized in that, in a system in which a polymer A and a polymer B are dissolved in and mixed with an organic solvent to undergo phase separation into two phases which are a solution phase containing with the polymer A as a major component and a solution phase containing the polymer B as a major component, the polymer A, the polymer B, and the organic solvent are continuously supplied to a mixing apparatus to thereby allow an emulsion to be formed; the emulsion is supplied to a vessel and added continuously with a poor solvent for the polymer A in the vessel to allow the polymer A to precipitate ; and polymer A particles is continuously taken from the vessel. The present invention provides a method that allows for mass production by efficient processes of manufacturing and that continuously microparticulates and produces polymer particles with lower variability in the average particle diameter and a smaller particle diameter distribution index. |
157 |
MASTERBATCH PELLETS, PROCESS FOR PRODUCING SAME, AND POLYAMIDE RESIN COMPOSITION CONTAINING THE MASTERBATCH PELLETS |
EP11783662 |
2011-05-20 |
EP2573130A4 |
2017-09-06 |
TERADA KAZUNORI |
|
158 |
HIGH-TEMPERATURE SPRAY DRYING PROCESS AND APPARATUS |
EP11767526.4 |
2011-09-22 |
EP2618924A1 |
2013-07-31 |
FRIESEN, Dwayne, T.; NEWBOLD, David, D.; BAUMANN, John, M.; DUBOSE, Devon, B.; MILLARD, Douglas, L. |
The process comprises delivering a spray solution comprising at least one solute in a solvent to a spray-drying apparatus, using a flash nozzle to atomize the spray solution into droplets within the spray-drying apparatus to remove at least a portion of the solvent from the droplets to form a plurality of particles, and collecting the particles. The spray solution is directed to a heat exchanger, thereby increasing the temperature of the spray solution to a temperature T2, wherein T2 is greater than T\. The flash nozzle comprises a central tube through which the spray solution is delivered and an outer tube through which a sweep gas is delivered. The central tube may have a first outer diameter at an inlet and a second outer diameter at an outlet, wherein the first outer diameter is greater than the second outer diameter. |
159 |
PROCESS FOR PRODUCING BIOPOLYMER NANOPARTICLES |
EP07840927 |
2007-08-14 |
EP2069431A4 |
2013-07-17 |
WILDI ROBERT H; VAN EGDOM EDWARD; BLOEMBERGEN STEVEN |
|
160 |
VORRICHTUNG ZUR HERSTELLUNG VON GRANULAT |
EP04707900.9 |
2004-02-04 |
EP1592501B1 |
2012-05-30 |
GIERKE, Stephan; ROTH, Bernhard; NOCELLA, Roger; HÄFELE, Dietmar |
Disclosed is a device for the production of a granulate whereby a perforated rotating outer tube with a supply device for the dripping material arranged on the inside thereof is disposed on a rocker whereby the drive motor for the drum is disposed as a counterweight on the side opposite the pivoting axis of the rocker. The rocker is pressed against a stop for positioning and is provided with a pivoting arm part (6a) which bears the bearing for a side of the rotating drum and which can be pivoted laterally with the bearing for maintenance activities or similar in order to enable easy dismantling of the drum. |