C08G65/26

Processes for producing aromatic diamine-initiated polyether polyols

Processes are described for producing an aromatic diamine-initiated polyether polyol having a measured OH number of 300 to 500 mg KOH/g and a viscosity at 25° C. of 5000 to 50,000 mPas. The processes include a first alkoxylation step in which an alkylene oxide consisting essentially of propylene oxide is reacted with a starter consisting essentially of aromatic diamine at a molar ratio of propylene oxide to aromatic diamine of 1.4:1 to 2.0:1 to form an alkoxylated product; and a second alkoxylation step in which an alkylene oxide consisting essentially of propylene oxide is reacted with the alkoxylated product, in the presence of an added catalyst, until the ratio of moles of propylene oxide added in the process to the moles of aromatic diamine added in the process is 4:1 to 9:1.

Polymer with polyether polyester segment and polysiloxane segment

The invention relates to a polymer comprising: a) at least one polyether polyester copolymer segment, wherein the polyether polyester copolymer comprises ether units selected from the group consisting of the formula (II) —[CR.sup.1.sub.2].sub.n—O—, wherein n is an integer of 2 to 4, R.sup.1 represent independent of each other organic groups having 1 to 30 carbon atoms or hydrogen, and wherein in case n is equal to 2 at least one of the R.sup.1 represents an ether group having the formula —R.sup.2—O—R.sup.3, wherein R.sup.2 and R.sup.3 independent of each other represent organic groups having 1 to 30 carbon atoms, and b) at least one polysiloxane segment linked to the at least one polyether polyester copolymer segment.

Polymer with polyether polyester segment and polysiloxane segment

The invention relates to a polymer comprising: a) at least one polyether polyester copolymer segment, wherein the polyether polyester copolymer comprises ether units selected from the group consisting of the formula (II) —[CR.sup.1.sub.2].sub.n—O—, wherein n is an integer of 2 to 4, R.sup.1 represent independent of each other organic groups having 1 to 30 carbon atoms or hydrogen, and wherein in case n is equal to 2 at least one of the R.sup.1 represents an ether group having the formula —R.sup.2—O—R.sup.3, wherein R.sup.2 and R.sup.3 independent of each other represent organic groups having 1 to 30 carbon atoms, and b) at least one polysiloxane segment linked to the at least one polyether polyester copolymer segment.

HYDROPHILIC-HYDROPHOBIC COPOLYMER CARRYING SHORT CHAIN FATTY ACID ESTER

[Object]

To provide a derivative of a short chain fatty acid that can exhibit physiological functions inherent in the short chain fatty acid.

[Solution]

Provided is a block or graft copolymer including a hydrophobic segment of a repeat unit containing a short chain fatty acid ester that is hydrolyzable by esterase in vivo and a hydrophilic segment including a poly(ethylene glycol) chain. These copolymers are effective in the treatment or therapeutic treatment of various diseases or disorders, including cancer.

HYDROPHILIC-HYDROPHOBIC COPOLYMER CARRYING SHORT CHAIN FATTY ACID ESTER

[Object]

To provide a derivative of a short chain fatty acid that can exhibit physiological functions inherent in the short chain fatty acid.

[Solution]

Provided is a block or graft copolymer including a hydrophobic segment of a repeat unit containing a short chain fatty acid ester that is hydrolyzable by esterase in vivo and a hydrophilic segment including a poly(ethylene glycol) chain. These copolymers are effective in the treatment or therapeutic treatment of various diseases or disorders, including cancer.

METHOD FOR PRODUCING POLYETHER CARBONATE POLYOLS

A method for producing polyether carbonate polyols via the following steps: (i) accumulating alkylene oxide and carbon dioxide on a H-functional starter substance in the presence of a double metal cyanide catalyst or a metal complex catalyst based on the metals zinc and/or cobalt, wherein a reaction mixture containing the polyether carbonate polyol is obtained; and (ii) adding at least one component K to the reaction mixture containing the polyether carbonate polyol, wherein a buffer system suitable for buffering a pH value in the region of pH 3.0 to 9.0 is used as component K, wherein the component K is free from compounds containing P—OH— groups.

METHOD FOR PREPARING POLYETHER CARBONATE ALCOHOLS

A method for preparing polyether carbonate alcohols by attaching cyclic carbonate to an H-functional starter substance in the presence of a catalyst, characterized in that a tribasic alkali- or alkaline earth metal phosphate is used as the catalyst, the alkali metal being selected from potassium or cesium.

METHOD FOR PREPARING POLYETHER CARBONATE ALCOHOLS

A method for preparing polyether carbonate alcohols by attaching cyclic carbonate to an H-functional starter substance in the presence of a catalyst, characterized in that a tribasic alkali- or alkaline earth metal phosphate is used as the catalyst, the alkali metal being selected from potassium or cesium.

METHOD OF PREPARATION OF A POLYOL BLOCK COPOLYMER
20230147677 · 2023-05-11 ·

A processfor producing a (poly)ol block copolymer comprising the reaction of a DMC catalyst with a polycarbonate or polyester (poly)ol (co)polymer and ethylene oxide, and optionally one or more other alkylene oxides, to produce a (poly)ol block copolymer wherein > 70% of the copolymer chain ends are terminated by primary hydroxyl groups, and the copolymers and products incorporating such copolymers.

PROCESSES AND PRODUCTION PLANTS FOR PRODUCING POLYOLS
20230147479 · 2023-05-11 ·

Processes and production plants for preparing a polyol. The process includes continuously producing an intermediate polyol in a first reactor, b) continuously discharging the intermediate polyol from the first reactor, continuously mixing the intermediate polyol with an aqueous solutions of alkali metal to provide a mixture comprising the intermediate polyol, alkali metal, and water, continuously dehydrating the mixture comprising intermediate polyol, alkali metal, and water, thereby continuously producing a dehydrated mixture comprising the intermediate polyol and the alkali metal, transferring the dehydrated mixture to a second reactor, and producing the polyether polyol in the second reactor by feeding an alkylene oxide to the second reactor to thereby react the intermediate polyol with the alkylene oxide in the presence of the alkali metal.