Patent classifications
C08L97/005
Lignin-based polymers with enhanced melt extrusion ability
A solid polymer blend material comprising: (i) lignin; and (ii) a polyamide having a melting point of no more than 240° C. and which is below the decomposition temperature of the lignin; wherein said lignin is homogeneously dispersed in said polyamide. Methods for producing the blend material are also described. Methods for producing objects made of the blend material by melt extrusion are also described, comprising: (a) melt blending components (i) and (ii) to form a polymer blend in which components (i) and (ii) are homogeneously blended, wherein the polymer blend exhibits a melt viscosity of no more than 2000 Pa.Math.s at a shear rate of 100-1000 s.sup.−1 and when heated to a temperature of no more than 240° C.; and; (b) forming an object made of said polymer blend material.
Lignin-based polymers with enhanced melt extrusion ability
A solid polymer blend material comprising: (i) lignin; and (ii) a polyamide having a melting point of no more than 240° C. and which is below the decomposition temperature of the lignin; wherein said lignin is homogeneously dispersed in said polyamide. Methods for producing the blend material are also described. Methods for producing objects made of the blend material by melt extrusion are also described, comprising: (a) melt blending components (i) and (ii) to form a polymer blend in which components (i) and (ii) are homogeneously blended, wherein the polymer blend exhibits a melt viscosity of no more than 2000 Pa.Math.s at a shear rate of 100-1000 s.sup.−1 and when heated to a temperature of no more than 240° C.; and; (b) forming an object made of said polymer blend material.
POROUS CARBON STRUCTURE PRODUCTION
A process is provided for producing a structure into which blood or other bio-fluids can flow by capillary action, e.g. for a whole blood microsampling probe. The process comprises mixing particles of novolak resin and particles of hydrocarbon polymer, producing an uncarbonized structure from the mixture by pressurised moulding and carbonizing the moulded structure, the hydrocarbon resin being a polymer such as polystyrene that on pyrolysis has a zero carbon yield, and the particles of the hydrocarbon polymer leaving voids in the carbonized structure of sufficient size for flow of whole blood into and through the structure. The particles may be of partly cured and milled novolak resin, the novolak particles when in the moulded structure not exhibiting bulk flow during carbonization but sintering at inter-particle contact points during carbonization to provide a consolidated structure. In this variant, ethylene glycol may be used as a sintering aid. Alternatively, the particles may be of fully cured and milled novolak resin, and are mixed with the hydrocarbon polymer , the lubricant and with a binder such as lignin for providing a consolidated structure.
Process of making carbon fibers derived from lignin/carbon residue
A method of making a carbon fiber comprising esterification of a lignin precursor with an acid, acid anhydride, or acyl halide, thereby forming a reduced T.sub.g lignin. Mixing the reduced T.sub.g lignin with a carbon residue selected from the group of coal based raw material, petroleum based raw material and combinations thereof, thereby forming a fiber precursor mixture; and spinning the fiber precursor mixture into a fiber. A method of making a carbon fiber comprising esterification of a lignin with an acid derivative, thereby forming a reduced T.sub.g lignin. Mixing the reduced T.sub.g lignin with a pitch, thereby forming a fiber precursor mixture; and spinning the fiber precursor mixture into a fiber. A method of making a carbon fiber comprising lowering the T.sub.g of a lignin material, thereby forming a reduced T.sub.g lignin. Mixing the reduced T.sub.g lignin with a carbon residue, thereby forming a fiber precursor mixture and spinning the fiber precursor mixture into a fiber.
Process of making carbon fibers derived from lignin/carbon residue
A method of making a carbon fiber comprising esterification of a lignin precursor with an acid, acid anhydride, or acyl halide, thereby forming a reduced T.sub.g lignin. Mixing the reduced T.sub.g lignin with a carbon residue selected from the group of coal based raw material, petroleum based raw material and combinations thereof, thereby forming a fiber precursor mixture; and spinning the fiber precursor mixture into a fiber. A method of making a carbon fiber comprising esterification of a lignin with an acid derivative, thereby forming a reduced T.sub.g lignin. Mixing the reduced T.sub.g lignin with a pitch, thereby forming a fiber precursor mixture; and spinning the fiber precursor mixture into a fiber. A method of making a carbon fiber comprising lowering the T.sub.g of a lignin material, thereby forming a reduced T.sub.g lignin. Mixing the reduced T.sub.g lignin with a carbon residue, thereby forming a fiber precursor mixture and spinning the fiber precursor mixture into a fiber.
LIGNIN DERIVATIVE, LIGNIN RESIN COMPOSITION, RUBBER COMPOSITION, AND MOLDING MATERIAL
A lignin derivative that is extracted from biomass and is used for rubber reinforcement or for use in a molding material is provided. Such a lignin derivative has a number average molecular weight of 300 to 2,000, and contains a component that is soluble in a polar organic solvent, in an amount of 80% by mass or more. When such a lignin derivative is incorporated, a lignin resin composition, a rubber composition, or a molding material, all of which have excellent low hysteresis loss characteristics, elastic modulus, or tensile properties, can be obtained. Furthermore, when a component that is thermofusible is used as the soluble component, a lignin resin composition, a rubber composition, or a molding material, all of which have superior aforementioned characteristics, can be obtained.
LIGNIN DERIVATIVE, LIGNIN RESIN COMPOSITION, RUBBER COMPOSITION, AND MOLDING MATERIAL
A lignin derivative that is extracted from biomass and is used for rubber reinforcement or for use in a molding material is provided. Such a lignin derivative has a number average molecular weight of 300 to 2,000, and contains a component that is soluble in a polar organic solvent, in an amount of 80% by mass or more. When such a lignin derivative is incorporated, a lignin resin composition, a rubber composition, or a molding material, all of which have excellent low hysteresis loss characteristics, elastic modulus, or tensile properties, can be obtained. Furthermore, when a component that is thermofusible is used as the soluble component, a lignin resin composition, a rubber composition, or a molding material, all of which have superior aforementioned characteristics, can be obtained.
LIGNIN-BASED CARBON FOAMS AND COMPOSITES AND RELATED METHODS
A method of making a carbon foam comprises subjecting a precursor composition comprising an amount of at least partially decomposed lignin to a first pressure for a first time, optionally, while heating the precursor composition to a first temperature; heating the compressed precursor composition to a second temperature for a second period of time while subjecting the compressed precursor composition to a second pressure to further decompose the at least partially decomposed lignin and to generate pores within the compressed precursor composition, thereby providing a porous, decomposed precursor composition; and heating the porous, decomposed precursor composition to a third temperature for a third time to carbonize, and optionally, to graphitize, the porous, decomposed precursor composition to provide the carbon foam. Also provided are the carbon foams and composites made from the carbon foams.
RUBBER COMPOSITIONS AND METHODS
A nanostructured porous catalyst for rubber vulcanization, the catalyst comprising a high surface area.
Method of Depolymerising Phenolic Polymers
The invention provides a method for depolymerising a phenolic polymer, the method comprising reacting the phenolic polymer with dimethylsulphoxide (DMSO) and a hydrogen halide. The phenolic polymer may be selected from the group consisting of lignin and derivatives thereof. The hydrogen halide may be HBr. The quantity of hydrogen halide per gram of phenolic polymer may be from 30 mmoles to 70 mmoles. The quantity of DMSO per gram of phenolic polymer may be from 0.1 mole to 1 mole. The reaction may be performed at a temperature of from 100 to 120° C. The reaction may be carried out for between 10 h and 14 h. The product of the reaction may comprise vanillin.