| Document |
Document Title |
|
JPS5411151B2 |
|
|
JPS549875Y1 |
|
|
JPS548455Y2 |
|
|
JPS5444271A |
PURPOSE: To avoid the decreases of the polymerization speed of contents or the decreases of quality and to efficiently produce polymer of high quality by selecting the location of an outlet nozzle according to the revolving velocity of t...
|
|
JPS5437074A |
|
|
JPS545805Y1 |
|
|
JPS5420965A |
A fluid reaction mixt. is agitated in a vessel equipped with two eccentrically placed agitators mounted on vertical shafts of different lengths. The agitators induce an axial motion in the mixt. Each shaft is placed diametrically opposit...
|
|
JPS542616B1 |
|
|
JPS541685B1 |
|
|
JPS5346871B2 |
|
|
JPS5346791B2 |
|
|
JPS5344183B2 |
|
|
JPS5343986B2 |
|
|
JPS53143876U |
|
|
JPS5345092Y2 |
|
|
JPS5339918B2 |
|
|
JPS53121087A |
PURPOSE: To control the preliminary polymerization reaction accurately with a simple device, by detecting the viscosity change of reactants with power values supplied to the agitating motor.
|
|
JPS5339403B1 |
This invention is directed to the production, by synthesis, of tertiary aliphatic amines by amination of alkyl haloids, by means of secondary aliphatic amine, wherein a reaction mixture is prepared which consists of two fractions, one fr...
|
|
JPS53119277A |
|
|
JPS5335592B2 |
|
|
JPS53109875A |
|
|
JPS5334188B2 |
A distillation column reactor which provides a relatively long residence time with a minimum drop in pressure which comprises a distillation column containing standard trays with downcomers, a liquid reservoir between the trays, and vapo...
|
|
JPS5399290A |
Mixing and polymerisation reactor with continuous operation, comprises a cylindrical container with inlets and outlets for the continuously passing reactants, and >=1 rotary shafts arranged along the longitudinal axis of the reactor. Con...
|
|
JPS5399246A |
Mixing and polymerisation reactor with continuous operation, comprises a cylindrical container with inlets and outlets for the continuously passing reactants, and >=1 rotary shafts arranged along the longitudinal axis of the reactor. Con...
|
|
JPS5328952B2 |
|
|
JPS5390173A |
|
|
JPS5394939U |
|
|
JPS5372086A |
|
|
JPS5318554B2 |
|
|
JPS5322626Y2 |
|
|
JPS5317636B2 |
|
|
JPS5315915B2 |
|
|
JPS5312789Y2 |
|
|
JPS538596B2 |
|
|
JPS538316B2 |
|
|
JPS537953B2 |
|
|
JPS5310458Y2 |
|
|
JPS535907B2 |
|
|
JPS538076Y2 |
|
|
JPS534106B2 |
|
|
JPS535119Y2 |
|
|
JPS535098Y2 |
|
|
JPS535118Y2 |
|
|
JPS531797B2 |
|
|
JPS531396Y2 |
|
|
JPS5257192Y2 |
|
|
JPS52147692A |
PURPOSE: The use of a polumerizer equipped with two shafts having 8 -shaped blades thereon in the last polymerization step minimizes the dead space in the polymetizer and provides extremely high-vicosity polyethylene terephthalate.
|
|
JPS52144149A |
|
|
JPS52136887A |
|
|
JPS5246922Y2 |
|
