A platform for research: civil engineering, architecture and urbanism
A platform for research: civil engineering, architecture and urbanism
KONTINUIERLICH BETRIEBENES VERFAHREN ZUR HERSTELLUNG VON COPOLYMEREN
Preparing a copolymer in a continuous mode of operation in a polymerization device containing a polymerization reactor having a feeder line and an outlet comprises: supplying a radical polymerization initiator, and an acid monomer and a polyether macromonomer as a monomer precursor into the reactor through feeder line, where the polymerization reactor at -20 to +120[deg] C contains initiator, monomer precursor, and copolymer containing reaction composition; and mixing the polyether macromonomer with initiator, monomer precursor and copolymer containing reaction composition, in the reactor. Preparation of a copolymer in a continuous mode of operation in a polymerization device containing a polymerization reactor having a feeder line and an outlet comprises: supplying a radical polymerization initiator, and an acid monomer and a polyether macromonomer as a monomer precursor into the reactor through feeder line, where the polymerization reactor at -20 to +120[deg] C contains initiator, monomer precursor, and copolymer containing reaction composition, the copolymer containing reaction composition is introduced into the reactor through the outlet, and the introduction of the polyether macromonomer and acid monomer is carried out in a separate manner; and mixing the polyether macromonomer with the initiator, monomer precursor and copolymer containing reaction composition, in the reactor. An independent claim is included for the copolymer obtained by the process.
KONTINUIERLICH BETRIEBENES VERFAHREN ZUR HERSTELLUNG VON COPOLYMEREN
Preparing a copolymer in a continuous mode of operation in a polymerization device containing a polymerization reactor having a feeder line and an outlet comprises: supplying a radical polymerization initiator, and an acid monomer and a polyether macromonomer as a monomer precursor into the reactor through feeder line, where the polymerization reactor at -20 to +120[deg] C contains initiator, monomer precursor, and copolymer containing reaction composition; and mixing the polyether macromonomer with initiator, monomer precursor and copolymer containing reaction composition, in the reactor. Preparation of a copolymer in a continuous mode of operation in a polymerization device containing a polymerization reactor having a feeder line and an outlet comprises: supplying a radical polymerization initiator, and an acid monomer and a polyether macromonomer as a monomer precursor into the reactor through feeder line, where the polymerization reactor at -20 to +120[deg] C contains initiator, monomer precursor, and copolymer containing reaction composition, the copolymer containing reaction composition is introduced into the reactor through the outlet, and the introduction of the polyether macromonomer and acid monomer is carried out in a separate manner; and mixing the polyether macromonomer with the initiator, monomer precursor and copolymer containing reaction composition, in the reactor. An independent claim is included for the copolymer obtained by the process.
KONTINUIERLICH BETRIEBENES VERFAHREN ZUR HERSTELLUNG VON COPOLYMEREN
CONTINUOUS METHOD FOR PRODUCING COPOLYMERS
PROCÉDÉ CONTINU DESTINÉ À LA FABRICATION DE COPOLYMÈRES
SCHWEDE CHRISTIAN (author) / VIERLE MARIO (author) / MANGEL TIMO (author) / ALBRECHT GERHARD (author) / HERZOG VOLKER (author) / ARLT KLAUS (author)
2018-08-15
Patent
Electronic Resource
German
IPC:
C04B
Kalk
,
LIME
/
C08F
MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
,
Makromolekulare Verbindungen, erhalten durch Reaktionen, an denen nur ungesättigte Kohlenstoff-Kohlenstoff-Bindungen beteiligt sind
/
C08L
COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
,
Massen auf Basis makromolekularer Verbindungen
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