C08K5/057

Soluble corrosion resistant sol-gel

Aspects described herein generally relate to a sol-gel that is the reaction product of an organosilane, a metal alkoxide, an acid, and a thio-lanthanide salt having a solubility of about 1 gram or greater per gram of sol-gel at 23° C. The thio-lanthanide salt includes a cation and a thio-ligand. The cation can be lanthanum, cerium, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, scandium, yttrium, cobalt, calcium, strontium, barium, and zirconium. In another aspect, a component, such as a vehicle component, includes a metal substrate and a sol-gel disposed on the metal substrate. Methods can include forming a sol-gel by mixing a metal alkoxide and an acid to form a first mixture; mixing with the first mixture an organosilane to form a second mixture; and mixing with the second mixture a lanthanide salt to form a third mixture.

SILICONE-BASED THERMOPLASTIC MATERIALS FOR 3D-PRINTING

The invention relates to a process for preparing a polyurea or a polyurethane organopolysiloxane block copolymer having a silicone content of at least 90% in weight relative to the total weight of the organosiloxane block copolymer. The invention further relates to a polyurea or a polyurethane organopolysiloxane block copolymer obtained according to this process and its use in a method for manufacturing a 3D article by an additive technique.

SILICONE-BASED THERMOPLASTIC MATERIALS FOR 3D-PRINTING

The invention relates to a process for preparing a polyurea or a polyurethane organopolysiloxane block copolymer having a silicone content of at least 90% in weight relative to the total weight of the organosiloxane block copolymer. The invention further relates to a polyurea or a polyurethane organopolysiloxane block copolymer obtained according to this process and its use in a method for manufacturing a 3D article by an additive technique.

Nucleating agents, methods for their production, and associated polymer compositions

A method of manufacture of zinc monoglycerolate containing an incorporated modifier, and the product, the zinc monoglycerolate being in the form of agglomerates of crystallites, wherein the crystallite size based on the average coherence domain length is not more than 30 nm in the <100> direction, and not more than 60 nm in the <011> direction, as determined by the Scherrer equation via powder X-ray diffraction; and the aspect ratio computed by <100>/<011> coherent domain lengths is less than 0.65, preferably less than 0.56, in particular less than 0.44. Polymers containing this nucleating agent and methods for their production are also described. The zinc monoglycerolate is useful as a nucleating agent, and is very effective at low loading levels in polymers such as polypropylene.

Nucleating agents, methods for their production, and associated polymer compositions

A method of manufacture of zinc monoglycerolate containing an incorporated modifier, and the product, the zinc monoglycerolate being in the form of agglomerates of crystallites, wherein the crystallite size based on the average coherence domain length is not more than 30 nm in the <100> direction, and not more than 60 nm in the <011> direction, as determined by the Scherrer equation via powder X-ray diffraction; and the aspect ratio computed by <100>/<011> coherent domain lengths is less than 0.65, preferably less than 0.56, in particular less than 0.44. Polymers containing this nucleating agent and methods for their production are also described. The zinc monoglycerolate is useful as a nucleating agent, and is very effective at low loading levels in polymers such as polypropylene.

Nucleating agents, methods for their production, and associated polymer compositions

A method of manufacture of zinc monoglycerolate containing an incorporated modifier, and the product, the zinc monoglycerolate being in the form of agglomerates of crystallites, wherein the crystallite size based on the average coherence domain length is not more than 30 nm in the <100> direction, and not more than 60 nm in the <011> direction, as determined by the Scherrer equation via powder X-ray diffraction; and the aspect ratio computed by <100>/<011> coherent domain lengths is less than 0.65, preferably less than 0.56, in particular less than 0.44. Polymers containing this nucleating agent and methods for their production are also described. The zinc monoglycerolate is useful as a nucleating agent, and is very effective at low loading levels in polymers such as polypropylene.

METHOD OF MAKING AN ACID NEUTRALIZING POLYMER THROUGH REACTIVE COMPOUNDING

A method of making an acid neutralizing polymer includes: a) preparing a first reaction mixture by blending of a polyamide material, a solid strongly basic material, and a halogenated-dimethylalkylamine; b) adding the first reaction mixture to a first compounding machine; c) reacting the first reaction mixture for a time and at a temperature sufficient to produce a first reaction product; d) preparing a second reaction mixture including the polyamide material; e) adding the second reaction mixture to a second compounding machine; f) reacting the second reaction mixture for a time and at a temperature sufficient to produce a second reaction product; g) preparing a third reaction mixture by blending the first reaction mixture and the second reaction mixture; h) adding the third reaction mixture to a third compounding machine; and i) reacting the third reaction mixture for a time and at a temperature sufficient to produce the acid neutralizing polymer.

METHOD OF MAKING AN ACID NEUTRALIZING POLYMER THROUGH REACTIVE COMPOUNDING

A method of making an acid neutralizing polymer includes: a) preparing a first reaction mixture by blending of a polyamide material, a solid strongly basic material, and a halogenated-dimethylalkylamine; b) adding the first reaction mixture to a first compounding machine; c) reacting the first reaction mixture for a time and at a temperature sufficient to produce a first reaction product; d) preparing a second reaction mixture including the polyamide material; e) adding the second reaction mixture to a second compounding machine; f) reacting the second reaction mixture for a time and at a temperature sufficient to produce a second reaction product; g) preparing a third reaction mixture by blending the first reaction mixture and the second reaction mixture; h) adding the third reaction mixture to a third compounding machine; and i) reacting the third reaction mixture for a time and at a temperature sufficient to produce the acid neutralizing polymer.

COMPOSITION FOR ACOUSTIC LENSES, ACOUSTIC LENS, ACOUSTIC WAVE PROBE, ULTRASOUND PROBE, ACOUSTIC WAVE MEASUREMENT APPARATUS, ULTRASOUND DIAGNOSTIC APPARATUS, PHOTOACOUSTIC WAVE MEASUREMENT APPARATUS AND ULTRASONIC ENDOSCOPE, AND METHOD FOR MANUFACTURING ACOUSTIC WAVE PROBE
20220289937 · 2022-09-15 · ·

A composition for an acoustic lens contains the following components (A) to (C): (A) a polysiloxane having a vinyl group, (B) a polysiloxane having two or more Si—H groups in a molecular chain thereof, and (C) alumina particles surface-treated with at least one surface treatment agent of an aminosilane compound, a mercaptosilane compound, an isocyanatosilane compound, a thiocyanatosilane compound, an aluminum alkoxide compound, a zirconium alkoxide compound, or a titanium alkoxide compound.

Air exhaust or air-and-smoke exhaust pipe for clean room and manufacturing method therefor

The present invention provides an air exhaust or air-and-smoke exhaust pipe for a clean room and a manufacturing method thereof. The air exhaust or air-and-smoke exhaust pipe is a pipe that satisfies FM4922, FM4910, or another equivalent standard and that is used for exhausting nonflammable chemical gas and corrosive vapor or nonflammable chemical gas, corrosive vapor and smoke in fire. The manufacturing method for the air exhaust or air-and-smoke exhaust pipe is: coating an inner part of a pre-manufactured metal pipe with a liquid coating that can be initially dried at normal temperature or low temperature to obtain an inner coating pipe; and baking the inner coating pipe at a temperature not exceeding 250° C. after the coating is initially dried, thus the coating is completely dried to obtain a finished product.