Dow Global Technolgoies LLC

Rohm and Haas Company

Dow Silicones Corporation

Parrot

Varioptic S.a.

Aveso, Inc.

Rohm & Haas Electronic Materials LLC

Parrot Drones

Daniel Lawrence Dermody

David L Malotky

Manesh Nadupparambil Sekharan

Aleksander Jozef Pyzik

Robert Scott Moglia

William J Harris

Timothy J Young

Colin Li Pi Shan

Liang Chen

Craig F Gorin

David H Bank

Scott T Matteucci

Bruce D Hook

Kaoru Aou

Nathan Wilmot

Mary Anne Leugers

Harpreet Singh

Sanjib Biswas

Sharon Allen

Scott T Burr

Mathieu Maillard

John B Cuthbert

Kevin J Bouck

Michael E Hus

Peter J Cate

Christopher John Tucker

Gary Lee Jialanella

Peng Gao

Felipe A Donate

Haiyang Yu

Susan J Babinec

Matthew James Kalinowski

Syed Zafar Mahdi

Matthias Stefan Ober

Liang Hong

Roland Bayer

Barry Alan Morris

Daniel P Sophiea

Jason A Reese

Zhifeng Bai

Kiran K Baikerikar

Matthew T Bishop

Thomas J Parsons

Bryan L McCulloch

Yunlong Guo

Kyle D Anderson

Jessica Ye Huang

Jake Joo

Stacey A Saba

Qinghao Meng

Yi Fan

Thomas L Tomczak

Hari Katepalli

Zhe Jia

Helge Braun

John Bryan Vincent

Adam L Grzesiak

Amit K Chaudhary

James R De Garavilla

Caroline Woelfle-Gupta

Sanjay C Solanki

Wanfu Ma

Christopher Thiede

Joshua M Katzenstein

James C Taylor

Kathleen Barnes

David A Hayes

Rebekah K Feist

An Kaga

Richard Tien Hua Chou

Matthew J Crimmins

Niranjan Malvadkar

Geraldine Malet

Kumar N Sanketh

Meagan Broadway

Mark D Fisher

Géraldine Malet

Yu Chen

Russell T Cooper

Jacob Milne

Liana Moreau

Thomas Tomczak

Yin Tang

Didem Oner-Deliormanh

Keith Harris

Van M Delk, Jr

An N Kaga

Chrisopher P Thiede

Kathleen M O'CONNELL

Didem Oner

The present disclosure provides an electrochemical cell. In an embodiment, the electrochemical cell includes a separator disposed between an optional anode and an optional cathode. The separator includes (A) a porous substrate and (B) a porous coating layer on the substrate. The porous substrate (A) is composed of an olefin-based polymer having a melting point, Tm, greater than 130° C. The porous coating layer (B) has a melting temperature from 80° C. to 110° C. The porous coating layer (B) is composed of a plurality of microparticles, and an optional binding agent. The microparticles have an average particle size from 0.3 microns to 1.5 microns. The microparticles are composed of (i) an ethylene-based polymer, having (a) a density from 0.90 g/cc to less than 0.94 g/cc, (b) a Tm from 90° C. to 120° C., (c) a melt index from 30 g/10 min to 600 g/10 min. The microparticles also include (ii) a dispersant composed of a C-Caliphatic fatty acid. The microparticles also include (iii) an optional acid functional wax.

Shutdown separator

A coating composition which comprises a dispersion which is a melt blended product of one or more olefinic base polymers; one or more dispersants; one or more compatibilizers; water; and optionally base; wherein the dispersion exhibits an average volume mean particle size diameter of less than or equal to 2 microns, a solids content of equal to or less than 70 wt %, and a pH of 8 or greater; one or more rheology modifiers; and optionally one or more neutralizing agents is provided. An article coated with the coating composition and a method of making the coated article are also provided.

Coating composition, a coated fabric, a method of making a coated fabric, and an article made from the coated fabric

The present disclosure provides a process. The process includes providing a blend containing (A) a first powder including (i) a polyolefin having a density from 0.860 g/cc to 0.910 g/cc, and a melt index from 1.5 g/10 min to 1,000 g/10 min; (ii) from 1 wt % to 15 wt % of a dispersant selected from an acrylic dispersant, a poloxamer, and combinations thereof; and (iii) optionally, a polyolefin wax, the first powder having a mean volume average particle size from 1 μm to 300 μm; and (B) a second powder including an ethylene/α-olefin copolymer having (i) a density from 0.920 g/cc to 0.955 g/cc; and (ii) a melt index from 1.0 g/10 min to 15 g/10 min, the second powder having a mean volume average particle size from 325 μm to 4,000 μm; and rotational molding the blend to form a rotational molded article.

Process for forming a rotational molded article

The present disclosure provides a process including providing a polyolefin aqueous dispersion having (50) to (90) wt % solids content of dispersion, the polyolefin aqueous dispersion containing solid particles containing a polyolefin including an ethylene-based polymer having a melting temperature from greater than (115)&#xb0; C. to (140)&#xb0; C., polyolefin wax, acrylic dispersant; and an aqueous phase including excess acrylic dispersant; adding diluting water to form a diluted polyolefin aqueous dispersion having (5) to less than (50) wt % solids content; collecting the solid particles; washing the solid particles with a washing agent to remove the excess acrylic dispersant; and removing the washing agent to form a powder having a mean volume average particle size from (10) to (300) &#x3bc;m, a sphericity from (0.92) to (1.0), a particle size distribution from (1) to less than (2), a particle density from (98)% to (100)%, and a flow rate in a large funnel from (1) to (5) seconds.

Process for forming a powder

A method of preparing a resin infused random fiber mat including the step of forming a liquid dispersion mat of polymeric resin and fiber on a porous substrate.

Manufacture of composite dispersion based resin-infused random fiber mat

A continuous process for producing a polyurea concentrate or powder. The process includes combing at least one amine and an isocayante in the presence of a liquid diluent or a base oil in a rotor stator mixer. The concentrate comprises a polyurea in a base oil wherein the concentration of from about 20 weight percent to about 50, or 40 or 35 or 30 weight percent of polyurea based on total weight of grease thickener. The powder has particle size of 2 to 400 microns. This concentrate or powder can then be formulated by grease manufacturers to the desired final properties without the need for handling of the isocyanate and amine raw materials.

Method of making a grease thickener and the thickener made by the method

An aqueous ionomer dispersion, and method of manufacturing thereof, comprising an ionomer composition and water, wherein the ionomer composition comprises: a) at least 20 wt. %, based on the total weight percent of the ionomer composition, of an ionomer; and b) up to 80 wt. %, based on the total weight percent of the ionomer composition, of a polyolefin.

Aqueous ionomeric dispersions, and methods thereof

Recovery times and/or airflow of flexible polyurethane foam is increased by including certain tackifiers in the foam formulation. The tackifiers are formed into an emulsion that includes a polyether containing oxyethylene groups, a nonionic surfactant and certain fumed silica, carbon black or talc particles.

Flexible polyurethane foam having prolonged recovery time

An additive manufactured article is comprised of at least two adhered layers of extrudates () comprised of a thermoset material having therein a phase change material, wherein the phase change material undergoes a phase change at a temperature less than where the thermoset material decomposes. The article may be made by dispensing a mixture comprised of an organic reactive material and phase change material forming extrudates that are 3D printed into an article having multiple layers of extrudates bound together and then allowing the organic reactive material to react forming a thermoset material having therein the phase change material to form the additive manufactured article. The shape of the article may be changed by heating to a temperature above the temperature where the phase change material undergoes a phase change while applying a force and then cooling below the phase change temperature. Likewise, the original shape may be returned by merely heating above the phase change temperature and then cooling in the absence of a force being applied.

Thermoset additive manufactured articles incorporating a phase change material and method to make them

A continuous process for producing a polyurea concentrate or powder. The process includes combing at least one amine and an isocyanate in the presence of a liquid diluent or a base oil in a rotor stator mixer. The concentrate comprises a polyurea in a base oil wherein the concentration of from about 20 weight percent to about 50, or 40 or 35 or 30 weight percent of polyurea based on total weight of grease thickener. The powder has particle size of 2 to 400 microns. This concentrate or powder can then be formulated by grease manufacturers to the desired final properties without the need for handling of the isocyanate and amine raw materials.

Recovery times and/or airflow of flexible polyurethane foam is increased by including certain tackifiers in the foam formulation. The tackifiers are characterized in being incompatible with polyol or polyol mixture used to make the foam, having a viscosity of at least 5,000 centipoise at 25 #C and having a glass transition temperature of at most 20 #C. The tackifier is pre-blended with certain monols to form a lower-viscosity blend that is combined with one or more other polyols and a polyisocyanate to form a reaction mixture for producing a polyurethane foam.

The present disclosure provides a process. The process includes (i) melt blending, in an extruder, (a) a polyolefin phase and (b) an aqueous phase in the presence of (c) at least one dispersant selected from an acrylic dispersant, a poloxamer dispersant, and combinations thereof; (ii) producing an interfacial tension from 0.1 dynes/cm to 25 dynes/cm; (iii) forming a polyolefin aqueous dispersion having from 25 wt % to 90 wt % solids content of dispersion; and (iv) removing the water from the polyolefin aqueous dispersion to form a powder. The powder has a mean volume average particle size from 10 &#x3bc;m to 300 &#x3bc;m, a sphericity from 0.92 to 1.0, a particle size distribution from 1 to less than 2, and a particle density from 98% to 100%.

An additive elastomeric manufactured part having an elongation at break of at least 50% may be made by a method comprising the following. A material comprising a prepolymer and filler is first dispensed through a nozzle to form an extrudate deposited on a base. The base, nozzle or combination thereof is moved while dispensing the material so that there is horizontal displacement between the base and nozzle in a predetermined pattern to form an initial layer of the material on the base. Subsequent layers are then formed on the initial layer by repeating the dispensing and movement on top of the initial layer and layers that follow.

Method for additive manufacturing

The inventions is directed to a method for recovering support materials used in an additive manufacturing process. The method comprises exposing a precursor additive manufactured article comprised of a water soluble support polymer and an insoluble material to water. The water soluble support polymer is dissolved in the water. The remaining article is then removed from the water. The dissolved water soluble polymer is precipitated from the water. The precipitated polymer is separated from the water and any remaining water removed to recover the water soluble support polymer. The recovered water soluble support polymer may then be re-used to make further additive manufactured articles.

Recovery of additive manufacturing support materials

The invention is directed at new process and systems for preparing composite materials that include a polymer phase and a fiber phase.

Pre-molding article from thermoset polymer dispersions

Growing community of inventors

Midland, MI, United States of America

Daniel Lawrence Dermody