A method of converting polystyrene to diphenylmethane using either UV light and or heat and a Lewis acid is disclosed.

A method of converting polystyrene to diphenylmethane using either UV light and or heat and a Lewis acid is disclosed.

A method is provided for preparing a reprocessed rubber from thermoset rubber particles. The method includes providing a plurality of thermoset rubber particles, inducing dynamic swelling and dynamic compatibilization of the plurality of rubber particles, admixing at least one de-linking agent with the swelled and wetted rubber particles, and wherein the step of admixing the at least one de-linking agent is carried out under thermo-mechanical mixing.

A method is provided for preparing a reprocessed rubber from thermoset rubber particles. The method includes providing a plurality of thermoset rubber particles, inducing dynamic swelling and dynamic compatibilization of the plurality of rubber particles, admixing at least one de-linking agent with the swelled and wetted rubber particles, and wherein the step of admixing the at least one de-linking agent is carried out under thermo-mechanical mixing.

Methods of depolymerizing polyolefin-based material into useful petrochemical products using styrene oligomers or polymers, and heat are described. The styrene oligomers or polymers improve the depolymerization reaction by decreasing the halftime for the depolymerization, which results in a higher depolymerization rate and a shorter residence time in the depolymerization unit, allowing for a predictable depolymerization reaction, and decreasing the branching or aromatic formations in the product.

Methods of depolymerizing polyolefin-based material into useful petrochemical products using styrene oligomers or polymers, and heat are described. The styrene oligomers or polymers improve the depolymerization reaction by decreasing the halftime for the depolymerization, which results in a higher depolymerization rate and a shorter residence time in the depolymerization unit, allowing for a predictable depolymerization reaction, and decreasing the branching or aromatic formations in the product.

This invention provides an advanced process for converting plastic waste into base chemicals. In various embodiments, the process includes one or more of the following process steps, including cleaning, shredding, dissolving plastic waste in an aromatic solvent, pre-fractionation, catalytic decomposition, fractionation, and coking. This method effectively breaks down plastic waste into valuable chemicals and high-quality reusable plastic.

This invention provides an advanced process for converting plastic waste into base chemicals. In various embodiments, the process includes one or more of the following process steps, including cleaning, shredding, dissolving plastic waste in an aromatic solvent, pre-fractionation, catalytic decomposition, fractionation, and coking. This method effectively breaks down plastic waste into valuable chemicals and high-quality reusable plastic.

Processes for recovering dialkyl terephthalates. The processes can include exposing a polyester composition to one or more glycols to depolymerization conditions thereby providing one or more depolymerization products. The one or more glycols can include diethylene glycol (DEG), triethylene glycol (TEG), 1,4-cyclohexanedimethanol (CHDM), poly(ethylene glycol) (PEG), neopentyl glycol (NPG), propane diol (PDO), butanediol (BDO), 2-methyl-2,4-pentanediol (MP diol), poly(tetramethylene ether)glycol (PTMG), or a combination thereof. The one or more depolymerization products can be exposed to an alcoholysis process to recover dialkyl terephthalate. Optionally, ethylene glycol (EG) produced from the depolymerization process can be recovered and re-used in a subsequent dialkyl terephthalate recovery or other process.

Processes for recovering dialkyl terephthalates. The processes can include exposing a polyester composition to one or more glycols to depolymerization conditions thereby providing one or more depolymerization products. The one or more glycols can include diethylene glycol (DEG), triethylene glycol (TEG), 1,4-cyclohexanedimethanol (CHDM), poly(ethylene glycol) (PEG), neopentyl glycol (NPG), propane diol (PDO), butanediol (BDO), 2-methyl-2,4-pentanediol (MP diol), poly(tetramethylene ether)glycol (PTMG), or a combination thereof. The one or more depolymerization products can be exposed to an alcoholysis process to recover dialkyl terephthalate. Optionally, ethylene glycol (EG) produced from the depolymerization process can be recovered and re-used in a subsequent dialkyl terephthalate recovery or other process.