| Document |
Document Title |
|
JPS51124857A |
PURPOSE: To provide easy continuous kneading and mixing device for powder and liquid materials.
|
|
JPS5138758B1 |
|
|
JPS5138757B1 |
|
|
JPS5138760B1 |
|
|
JPS51127969U |
|
|
JPS5136991Y1 |
|
|
JPS5129916B2 |
A continuous casting process and apparatus for a liquid polymerizable composition comprising a pair of endless belts which are arranged such that the lower run of the upper belt is disposed above the upper run of the lower belt and said ...
|
|
JPS51103035U |
|
|
JPS5193784A |
|
|
JPS5126899B2 |
|
|
JPS5129324Y1 |
|
|
JPS5187714U |
|
|
JPS5118903B1 |
|
|
JPS5155063A |
|
|
JPS5152553A |
|
|
JPS5150386A |
Polymerization reactor with agitator having axial action which circulates the reactor content substantially in a flow parallel to the reactor walls and parallel to the concentrically arranged interior coolers consisting of parallel U-sha...
|
|
JPS5149172A |
A method of heat treating a material, particularly for the despersion and firing of wet agglomerates, slurries, sludges and the like in fluidized bed, spouting bed or spouting/fluidised bed combustors, comprises extracting hot sold parti...
|
|
JPS5137177A |
Process for the continuous production of a polymer of an alpha -olefin monomer. The monomer is polymerized in bulk, employing a screw conveyor as the reactor. The monomer can be in liquid phase when introduced into the conveyor. By the p...
|
|
JPS518999B2 |
|
|
JPS5132521A |
|
|
JPS5127874A |
|
|
JPS5128846U |
|
|
JPS5116283A |
|
|
JPS512960B2 |
|
|
JPS516870A |
|
|
JPS512788A |
|
|
JPS511554U |
|
|
JPS50148282A |
|
|
JPS5035959B1 |
|
|
JPS5034508B1 |
1305461 Polymerizing in a multi-stage reactor TISZAI VEGYI KOMBINAT 7 Jan 1970 [7 Jan 1969] 882/70 Heading C3P [Also in Division B1] An acrylic copolymer is produced (see Example 2) by passing a homogenized and preheated starting mixture...
|
|
JPS50138089A |
|
|
JPS50125964A |
Starting a wet oxidation unit by initially supplying a small part of full power to start the compressor-expander train, the resultant low volume of low pressure air being by-passed around the unit to expander inlet, heating and saturatin...
|
|
JPS5030107B2 |
A vertical autoclave suitable for the bulk polymerization of vinyl chloride based polymers and copolymers embodying agitation means comprising at least one agitator (A) in the form of helicoidal ribbon about a rotatable shaft in the uppe...
|
|
JPS5028983B1 |
|
|
JPS5028984B1 |
|
|
JPS5028986B1 |
|
|
JPS5028985B1 |
|
|
JPS50115677A |
|
|
JPS50102957U |
|
|
JPS50106873A |
1453469 Mixing apparatus: vortex apparatus CHEM-TROL POLLUTION SERVICES INC 17 Dec 1973 58419/73 Headings B1C and B1F A mixer has an upper portion 16 and a lower portion 18 terminating in a reduced diameter outlet 20, a tangential inlet ...
|
|
JPS50101286A |
|
|
JPS5025711Y1 |
|
|
JPS5022027B1 |
Method by which an esterification precursor is continuously converted to an esterification reaction product liquid by admixing a feed stream of the precursor into and with a circulating stream of the product liquid, heating the admixture...
|
|
JPS5021514B2 |
A continuous reactor for viscous materials that give off volatile matter during operation has two rows of agitation rotors mounted staggeredly and with a phase angle of 90 DEG to each other on a parallel pair of shafts. Each of the agita...
|
|
JPS5089303A |
|
|
JPS5019600B1 |
Thermoplastic condensation polymers are prepared by feeding the viscous starting materials or solutions thereof into a heated tube, along the inner wall of which they are moved by a worm conveyer, to the exit point, w...
|
|
JPS5017192B1 |
1,273,514. Mixing apparatus; polycondensation apparatus. BAKER PERKINS Inc. 27 Oct., 1970 [30 Oct., 1969], No. 50983/70. Headings B1C and B1X. Apparatus for poly condensation and other reactions, evaporating and mixing comprises co-rotat...
|
|
JPS5016753B1 |
|
|
JPS5016755B1 |
|
|
JPS5016754B1 |
|
