Abstract:
Die vorliegende Erfindung betrifft ein Verfahren zum Aufreinigen einer Polyol-Dispersion durch Strippen über mindestens einen rotierenden Körper, die durch das erfindungsgemäße Verfahren erhältliche Polyoldispersion sowie deren Verwendung zur Herstellung von Polyurethanen.
Abstract:
Herstellung von Isobutenhomopolymeren mit einem gewichtsgemittelten Molekulargewicht von 75.000 bis 10.000.000 durch Polymerisation von Isobuten in einer Polymerisationsvorrichtung in flüssiger Phase bei Temperaturen von -80°C bis -190°C in einem geeigneten inerten Lösungsmittel und in Gegenwart eines Polymerisationskatalysator-Komplexes auf Basis von Lewis-Säuren und Co-Katalysatoren,wobei man Isobuten,inertes Lösungsmittelund Polymerisationskatalysator-Komplex in mindestens drei Teilströmender Mischkammer einer Mischeinrichtung zuführt und dort vermischt, diese Mischung in den Flüssigphasenraum der Polymerisationsvorrichtung einspeist und dort die Polymerisation des Isobutens ablaufen lässt.
Abstract:
The invention relates to a process for a polyamide based on dicarboxylic acids and diamines, comprising the following stages: A) providing an aqueous monomer mixture composed of dicarboxylic acids and diamines; B) transferring the aqueous mixture from stage A) into a continuous evaporator reactor in which diamines and dicarboxylic acids are converted at a temperature in the range from 100 to 370°C and a pressure in the range from 2 to 51 bar (abs), the evaporator reactor being a vertical tube bundle reactor through which the flow is from the top downward; C) transferring the mixture from stage B) into a separator which is operated at a temperature in the range from 100 to 370°C and a pressure in the range from 1 to 50 bar with removal of gaseous components; wherein the tubes of the evaporator reactor have internals which direct the flow of the liquid phase of the mixture close to the wall towards the middle of the tubes and have free flow paths for the gas phase produced in the evaporator reactor over their axial length along the inner wall of the tubes.
Abstract:
Provided is a process of producing polymers of a N-vinyl carboxamide comprising the steps of flowing a reaction mixture comprising an aqueous liquid containing at least one polymerisation initiator, N-vinyl carboxamide monomer or a monomer mixture which comprises N-vinyl carboxamide into a reactor system,polymerising the monomer or monomer mixture to produce the polymer of a N-vinyl carboxamide, in which the reactor system comprises a series of reactor units comprising a combination of at least one mixed flow reactor and at least one single pass tubular reactor,wherein i) the at least one mixed flow reactor comprises at least one vessel containing internal and/or external means of mixing; and ii) the at least one single pass tubular reactor comprises a tubular section disposed between two ends,at least one inlet and at least one outlet in which the reaction mixture flows through the single pass tubular reactor only once, wherein substantially none of the reaction mixture exits the single pass tubular reactor less than 0.5 of the mean residence time of the reaction mixture in a single pass tubular reactor. The polymers resulting therefrom may be hydrolysed to provide polymers containing vinyl amine units. Also provided are the apparatus suitable for producing said polymers.
Abstract:
Disclosed herein is a process for producing polymers of an N-vinyl carboxamide, including the steps of flowing a reaction mixture containing an aqueous liquid containing at least one polymerisation initiator, N-vinyl carboxamide monomer or a monomer mixture containing N-vinyl carboxamide into a reactor system, and polymerising the monomer or monomer mixture to produce the polymer of a N-vinyl carboxamide. The polymers resulting therefrom may be hydrolysed to provide polymers containing vinyl amine units. Also disclosed herein is an apparatus suitable for producing the polymers.