Bio-based ethanol, such as ethanol produced from lignocellulosic materials, for example, is processed to produce bio-based ethylene, which can then be processed further to produce other bio-based materials including bio-based polymers and copolymers, including bio-based polyethylene, bio-based α-olefins, bio-based 1,2-diols, as well as other compounds.

A method for decomposing a phenolic by-product generated in a phenol preparation process, the method including: adding a phenolic by-product stream, a decomposition apparatus side discharge stream, and process water to a mixing apparatus and mixing the phenolic by-product stream, the decomposition apparatus side discharge stream, and the process water; adding a mixing apparatus discharge stream discharged from the mixing apparatus to a phase separation apparatus and phase-separating the mixing apparatus discharge stream into an oil phase and an aqueous phase; feeding an oil phase stream discharged from the phase-separation apparatus and discharged to a decomposition apparatus and decomposing the oil phase stream; and circulating the decomposition apparatus side discharge stream discharged from the decomposition apparatus to the mixing apparatus.

A method for decomposing a phenolic by-product generated in a phenol preparation process, the method including: adding a phenolic by-product stream, a decomposition apparatus side discharge stream, and process water to a mixing apparatus and mixing the phenolic by-product stream, the decomposition apparatus side discharge stream, and the process water; adding a mixing apparatus discharge stream discharged from the mixing apparatus to a phase separation apparatus and phase-separating the mixing apparatus discharge stream into an oil phase and an aqueous phase; feeding an oil phase stream discharged from the phase-separation apparatus and discharged to a decomposition apparatus and decomposing the oil phase stream; and circulating the decomposition apparatus side discharge stream discharged from the decomposition apparatus to the mixing apparatus.

The present invention is directed toward an article of footwear with an improved eyelet system independent of the upper. The article of footwear includes an upper and a sole structure, where the sole structure includes a top surface, a bottom surface, a lateral side and a medial side. The article of footwear further includes an eyelet system coupled to the top surface of the sole structure. The eyelet system includes a base structure and a plurality of looped strand portions coupled to the base structure. The base structure is coupled to the top surface of the sole structure such that the plurality of looped strand portions extend outwardly from the sole structure, enabling the looped strand portions to receive a fastening element.

The present invention is directed toward an article of footwear with an improved eyelet system independent of the upper. The article of footwear includes an upper and a sole structure, where the sole structure includes a top surface, a bottom surface, a lateral side and a medial side. The article of footwear further includes an eyelet system coupled to the top surface of the sole structure. The eyelet system includes a base structure and a plurality of looped strand portions coupled to the base structure. The base structure is coupled to the top surface of the sole structure such that the plurality of looped strand portions extend outwardly from the sole structure, enabling the looped strand portions to receive a fastening element.

Methods and systems for preparing acetone from cumene hydroperoxide (CHP) are disclosed. The disclosed methods involve cleaving CHP to form a cleavage product stream. In some embodiments, the cleavage product stream is separated into an overhead stream and a bottoms stream. The bottoms stream is neutralized, washed and then treated in a crude acetone column to provide a crude acetone stream. The overhead stream of the cleavage product is flashed forward in the process, bypassing the neutralization, washing, and crude acetone column and is then combined with the crude acetone stream. The combined acetone streams are provided to an acetone product column. According to some embodiments, the acetone product column comprises a side draw for obtaining a recycle acetone stream, which is recycled to the cleavage reactor(s). The recycle acetone side draw may be located lower on the acetone product column than the point from which product acetone is obtained. The disclosed methods increase the efficiency of the process.

Methods and systems for preparing acetone from cumene hydroperoxide (CHP) are disclosed. The disclosed methods involve cleaving CHP to form a cleavage product stream. In some embodiments, the cleavage product stream is separated into an overhead stream and a bottoms stream. The bottoms stream is neutralized, washed and then treated in a crude acetone column to provide a crude acetone stream. The overhead stream of the cleavage product is flashed forward in the process, bypassing the neutralization, washing, and crude acetone column and is then combined with the crude acetone stream. The combined acetone streams are provided to an acetone product column. According to some embodiments, the acetone product column comprises a side draw for obtaining a recycle acetone stream, which is recycled to the cleavage reactor(s). The recycle acetone side draw may be located lower on the acetone product column than the point from which product acetone is obtained. The disclosed methods increase the efficiency of the process.

A solidification or crystallization method is disclosed, which includes providing at least a first organic compound and at least one volatile co-former organic compound. A mixture of at least the first organic compound and the co-former organic compound is formed, wherein either the first organic compound or the volatile co-former organic compound includes a hydrogen acceptor moiety and the other includes a hydrogen donor moiety, thereby allowing the formation of hydrogen bonds between the first organic compound and the volatile co-former organic compound. The mixture is allowed to stand for sufficient time for the mixture to liquify at a temperature below that of the melting points of the components, thereby forming a liquid mixture. The volatile co-former organic compound is allowed to evaporate, thereby resulting in crystallization of at least the first organic compound. The method can be a co-crystallization method if there are two organic compounds.

The invention relates to a process for preparing a specific hydroxy compound by means of decarboxylation of a specific carboxylic acid compound or a salt of said carboxylic acid compound, to a method for preparing a diaryl carbonate, a bisphenol or a polycarbonate, a diaryl carbonate or bisphenol, a polycarbonate, and to a method for adjusting the isotope ratio of C14 to C12 in a polymer. A specific solvent is used during decarboxylation.

The invention relates to a process for preparing a specific hydroxy compound by means of decarboxylation of a specific carboxylic acid compound or a salt of said carboxylic acid compound, to a method for preparing a diaryl carbonate, a bisphenol or a polycarbonate, a diaryl carbonate or bisphenol, a polycarbonate, and to a method for adjusting the isotope ratio of C14 to C12 in a polymer. A specific solvent is used during decarboxylation.