The present document describes a system and a process for the extraction of several products from apple peel. There are several unit operations involved including an ultrafiltration unit, concentration unit, and a three stage counter current separator centrifuge wherein water is used as the solvent. The final products that are extracted from apple peel include pectin, syrup, fibers, as well as soluble and dried retenate fractions.

The present invention is directed to a process for the hydrolysis of biomass as well as the saccharide-containing permeate product and the protein-containing product produced by this process. In a further aspect, the present invention is directed to a process for the production of organic compounds from the saccharide-containing product. In an additional aspect the present invention is directed to the use of the protein-containing product for the production of a fermentation medium.

The present document describes a system and a process for the extraction of several products from apple peel. There are several unit operations involved including an ultrafiltration unit, concentration unit, and a three stage counter current separator centrifuge wherein water is used as the solvent. The final products that are extracted from apple peel include pectin, syrup, fibers, as well as soluble and dried retenate fractions.

Provided is a biomass hydrothermal decomposition system which includes: a biomass supply unit that supplies a biomass raw material; hydrothermally decomposing the biomass raw material using pressurized hot water; a hydrothermal decomposition unit that dissolves lignin components and hemicellulose components in the pressurized hot water; a biomass solid fraction discharge unit that discharges a biomass solid fraction from the hydrothermal decomposition unit; an enzymatic liquefaction tank that is in connection with the biomass solid fraction discharge unit, and in which the discharged biomass solid fraction is introduced, and an enzyme is supplied to the biomass solid fraction to liquefy the biomass solid fraction; and a discharge unit that discharges the liquefied biomass solid fraction.

A method of producing a sugar liquid includes filtering a cellulose-derived sugar liquid through one or more separation membranes selected from the group consisting of an ultrafiltration membrane, a nanofiltration membrane and a reverse osmosis membrane and washing the separation membrane(s) after filtration with washing water containing an alkaline substance and an aromatic compound at 10? C. or more and less than 50? C.

An apparatus for filtering a suspension has a housing with an inlet receiving the suspension to be filtered, an outlet for the clear filtered filtrate, and a drain for removal of filter cake. The housing has a cylindrical part centered on an axis. An output ring pipe is connected to the outlet and externally surrounds the cylindrical part. A plurality of segmental filter holders are fittable into the cylindrical part from above and together form a circular insert with each holder forming an inlet chamber having an outflow fitting connectable to the annular output pipe. Respective sets of filter elements each formed by a respective strip-shaped support and a mesh filter sock surrounding the support are carried on the holder and open into the respective inlet chambers. A removable cover upwardly closes the cylindrical part above the inserts.

A method of producing a sugar liquid includes filtering a cellulose-derived sugar liquid through one or more separation membranes selected from the group consisting of an ultrafiltration membrane, a nanofiltration membrane and a reverse osmosis membrane, and washing the separation membrane(s) after filtration with washing water containing an acidic substance and an aromatic compound.

A concentrator system is for processing maple sap for production of maple syrup. The concentrator system includes a fluid circuit for receiving maple sap to be processed from a given source of maple sap. At least one osmotic membrane is operatively disposed about the fluid circuit and in fluid connection with the maple sap to be processed, for passing the maple sap to be processed through the at least one osmotic membrane, at differential pressure of at least 600 PSI, in order to withdraw water content from the maple sap being processed and thus obtain a resulting concentrated maple sap in one single step.

A technology for material separation is provided. The technology enables an output of a first material from a rotary lifter. The technology enables a direction of a fluid stream onto the first material in flight based on the output of the first material such that the first material is separated into at least a second material and a third material. The technology enables a conveyance of the second material away from the rotary lifter. The technology enables a removal of the third material via a vacuum port.

A technology for material separation is provided. The technology enables an output of a first material from a rotary lifter. The technology enables a direction of a fluid stream onto the first material in flight based on the output of the first material such that the first material is separated into at least a second material and a third material. The technology enables a conveyance of the second material away from the rotary lifter. The technology enables a removal of the third material via a vacuum port.