Abstract: A three-dimensional (3D)) object production process comprising providing a thermoset printing apparatus comprising a mixing chamber to receive and mix at least a first reactive component and a second reactive component to provide a thermosetting material, an extrusion nozzle to deliver the thermosetting material to form a 3D object, at least one actuator coupled to the extrusion nozzle to move the extrusion nozzle when delivering the thermosetting material to form the 3D object, and a controller comprising one or more processors and coupled to the extruded thermoset printing apparatus, and depositing the thermosetting material to form the 3D object, wherein the depositing comprises depositing a first layer of thermosetting material and depositing an at least second layer of thermosetting material, wherein the beads of thermosetting material in the at least second layer are offset from the beads of thermosetting material in the first layer.

Abstract: A process for the purification of levulinic acid including the following steps: a. providing a composition 1, comprising at least 75 wt. % of levulinic acid; b. cooling composition 1 to at least one temperature Tc, wherein Tc is a temperature in the range 1.23*(W1)?104.5?Tc (° C.)?1.23*(W1)?89.5, wherein W1 is the weight % of levulinic acid in composition 1, to obtain a cooled composition 1; c. performing melt crystallization of composition 1 including the steps of: i. bringing the cooled composition 1 into contact with levulinic acid crystal seeds, ii. allowing the levulinic acid in composition 1 to crystallize at at least one temperature Tc to obtain crystals 1 and liquid 1, and iii. draining of liquid 1; d. optionally, treating crystals 1, after draining of liquid 1, by sweating, according to the following steps: i. heating the crystals 1 at a temperature between 5 and 40° C. to obtain crystals 2 and liquid 2, and ii. draining of liquid 2; e.

Abstract: The invention relates to a continuous or repetitive batch process for the hydrogenation of levulinic acid (LA) or esters thereof to at least gamma valerolactone (GVL) in a reactor comprising a feed stream and an outlet stream, in the presence of a solid Ru catalyst, said process comprising (a) pretreating said solid Ru catalyst with a reductant; and (b) reacting levulinic acid with hydrogen and the pretreated solid Ru catalyst obtained in step (a) at a temperature and residence time suitable to form at least GVL, characterized in that the pretreatment is in the presence of a first solvent which comprises water. This process is stable and little or no Ru will leak form the support.

Abstract: A process for the purification of levulinic acid including the following steps: a. providing a composition 1, comprising at least 75 wt. % of levulinic acid; b. cooling composition 1 to at least one temperature Tc, wherein Tc is a temperature in the range 1.23*(W1)?104.5?Tc (° C.)?1.23*(W1)?89.5, wherein W1 is the weight % of levulinic acid in composition 1, to obtain a cooled composition 1; c. performing melt crystallization of composition 1 including the steps of: i. bringing the cooled composition 1 into contact with levulinic acid crystal seeds, ii. allowing the levulinic acid in composition 1 to crystallize at at least one temperature Tc to obtain crystals 1 and liquid 1, and iii. draining of liquid 1; d. optionally, treating crystals 1, after draining of liquid 1, by sweating, according to the following steps: i. heating the crystals 1 at a temperature between 5 and 40° C. to obtain crystals 2 and liquid 2, and ii. draining of liquid 2; e.

Abstract: The invention relates to a continuous or repetitive batch process for the hydrogenation of levulinic acid (LA) or esters thereof to at least gamma valerolactone (GVL) in a reactor comprising a feed stream and an outlet stream, in the presence of a solid Ru catalyst, said process comprising (a) pretreating said solid Ru catalyst with a reductant; and (b) reacting levulinic acid with hydrogen and the pretreated solid Ru catalyst obtained in step (a) at a temperature and residence time suitable to form at least GVL, characterized in that the pretreatment is in the presence of a first solvent which comprises water. This process is stable and little or no Ru will leak form the support.

Abstract: The invention relates to a process for the production of 5-formylvaleric acid and adipic acid or esters thereof from an isomeric mixture of pentenoic acid or esters thereof said mixture comprising at least 4-pentenoic acid or esters thereof, and further comprising 3-pentenoic acid and/or 2-pentenoic acid or esters thereof. The process allows for efficient production of two different intermediates for producing polyamide using a single process, with good selectivity, little waste, in an economically efficient fashion. The process is very suitable to use an isomeric pentenoic acid mixture obtained from valerolactone, and can be used to produce renewable polyamide intermediates using a single process.

Abstract: The invention relates to a process for the production of 5-formylvaleric acid and adipic acid or esters thereof from an isomeric mixture of pentenoic acid or esters thereof said mixture comprising at least 4-pentenoic acid or esters thereof, and further comprising 3-pentenoic acid and/or 2-pentenoic acid or esters thereof. The process allows for efficient production of two different intermediates for producing polyamide using a single process, with good selectivity, little waste, in an economically efficient fashion. The process is very suitable to use an isomeric pentenoic acid mixture obtained from valerolactone, and can be used to produce renewable polyamide intermediates using a single process.