The present invention relates to a foamed sintered polymeric material with improved mechanical properties and a process for the preparation thereof comprising the following steps: providing an expandable polymeric material in the form of granules, solubilizing with a time-varying pressure profile said one or more blowing agents in the expandable polymeric material, expanding said granules to form said expanded beads by instantly releasing the pressure or by pressure release and subsequent heating, and sintering together said expanded beads, preferably at a temperature higher than 30° C.

The present disclosure provides a process. The process includes (i) forming a composition containing a peroxide-modified ethylene-based polymer selected from the group consisting of a peroxide-modified ethylene/a-olefin multi-block copolymer, a peroxide-modified low density polyethylene, and combinations thereof; (ii) contacting the composition with a blowing agent to form a foam composition; and (iii) forming foam beads comprising the foam composition. The present disclosure also provides a foam bead produced by said process.

The present disclosure provides a process. The process includes (i) forming a composition containing a peroxide-modified ethylene-based polymer selected from the group consisting of a peroxide-modified ethylene/a-olefin multi-block copolymer, a peroxide-modified low density polyethylene, and combinations thereof; (ii) contacting the composition with a blowing agent to form a foam composition; and (iii) forming foam beads comprising the foam composition. The present disclosure also provides a foam bead produced by said process.

A method for producing expanded particles having a high expansion ratio by a pressure-release expansion with a simpler configuration and at a low facility cost is provided. A production device includes an expansion cylinder being provided with a connecting port that connects with open-system branch cylinder and having a space of a saturated steam atmosphere. The space of a saturated steam atmosphere may be a different space from a space inside the branch cylinder. A temperature (T1) inside the expansion chamber exceeds 102° C. and is not higher than a higher one of 108° C. and a temperature obtained by a melting point Tm of a thermoplastic resin minus 14° C. A temperature (T2) at a connecting port is not lower than 100° C., and the temperature (T1) is higher than the temperature (T2).

A method for producing expanded particles having a high expansion ratio by a pressure-release expansion with a simpler configuration and at a low facility cost is provided. A production device includes an expansion cylinder being provided with a connecting port that connects with open-system branch cylinder and having a space of a saturated steam atmosphere. The space of a saturated steam atmosphere may be a different space from a space inside the branch cylinder. A temperature (T1) inside the expansion chamber exceeds 102° C. and is not higher than a higher one of 108° C. and a temperature obtained by a melting point Tm of a thermoplastic resin minus 14° C. A temperature (T2) at a connecting port is not lower than 100° C., and the temperature (T1) is higher than the temperature (T2).

A method for producing an oxo-biodegradable expanded polystyrene (EPS) product is disclosed. In embodiments, the method includes: providing a volume of polystyrene; providing a volume of one or more chemical additives; combining the volumes of polystyrene and one or more chemical additives to form a mixture; and expanding the mixture into an oxo-biodegradable expanded polystyrene (EPS) product.

A method for producing an oxo-biodegradable expanded polystyrene (EPS) product is disclosed. In embodiments, the method includes: providing a volume of polystyrene; providing a volume of one or more chemical additives; combining the volumes of polystyrene and one or more chemical additives to form a mixture; and expanding the mixture into an oxo-biodegradable expanded polystyrene (EPS) product.

Expandable thermoplastic polyurethane comprising blowing agent, wherein the Shore hardness of the thermoplastic polyurethane is from A 44 to A 84.

Expandable thermoplastic polyurethane comprising blowing agent, wherein the Shore hardness of the thermoplastic polyurethane is from A 44 to A 84.

Expandable thermoplastic polyurethane comprising blowing agent, wherein the Shore hardness of the thermoplastic polyurethane is from A 44 to A 84.