A process that provides for the reuse of yeast biomass used in the alcoholic fermentation of both sugarcane and corn in independent or integrated processes with steps of separation and reuse of solids prior to distillation and which are used in the process itself and in other industrial applications such as the production of high protein content (DDG/DDGS) ration, due to the alcohol recovery of the process, biodiesel, cell wall and yeast extract, as well as energy generation. The process also includes a drying step using indirect contact dryers operating with low pressure, non-noble vapors, such as plant vapor and exhaust vapor, and with the recovery of the ethanol contained in the wet cake.

A fortifier for growth and flowering in horticulture, trees and ornamental plants, aromatic plants and fruit trees, from wastewater from brewer's yeast with a very low protein concentration. Its attainment is comprised of the previous stages: filtered by 80 m; magnetic treatment of the liquid; addition of 0.1 to 20 g/l phosphate and 10 to 20 g/l glycose. Fermentation is carried out keeping the free amino acid content greater than 0.1%, the content of Mg.sup.+2 greater than 0.1%, total nitrogen, phosphate, and potassium below 3.0%, the content of protein from 0.5% to 1.0% and EDTA from 0.02% to 0.2%, all by dry matter weight; addition of microbes from the environment; at temperatures of 15 C. to 40 C. with gentle agitation, for 24 hours to 30 days; subsequent filtering and pH adjustment. It has been found to be effective in various crops.

A fortifier for growth and flowering in horticulture, trees and ornamental plants, aromatic plants and fruit trees, from wastewater from brewer's yeast with a very low protein concentration. Its attainment is comprised of the previous stages: filtered by 80 m; magnetic treatment of the liquid; addition of 0.1 to 20 g/l phosphate and 10 to 20 g/l glycose. Fermentation is carried out keeping the free amino acid content greater than 0.1%, the content of Mg.sup.+2 greater than 0.1%, total nitrogen, phosphate, and potassium below 3.0%, the content of protein from 0.5% to 1.0% and EDTA from 0.02% to 0.2%, all by dry matter weight; addition of microbes from the environment; at temperatures of 15 C. to 40 C. with gentle agitation, for 24 hours to 30 days; subsequent filtering and pH adjustment. It has been found to be effective in various crops.

Described herein is a system, methods, processes and nutrient-rich products-by-process, which are generated by the conversion of winery derivatives into nutrient-rich products in an ecological manner. Integration of this system into a winery assists the winery to manage its previously-considered waste nutrient-rich products in an ecological manner, which can also optionally provide them with a novel revenue stream. The system, methods, and processes are used to convert winemaking derivatives into bioactive nutrient-rich products comprising antioxidants and other bioactive molecules that reside within the marc and lees. These nutrient-rich products can be used as natural flavour, texture and color enhancers, in addition to nutritional ingredients to fortify processed foods and consumer recipes. They can also be used as health supplements and in the cosmetic industry.

Described herein is a system, methods, processes and nutrient-rich products-by-process, which are generated by the conversion of winery derivatives into nutrient-rich products in an ecological manner. Integration of this system into a winery assists the winery to manage its previously-considered waste nutrient-rich products in an ecological manner, which can also optionally provide them with a novel revenue stream. The system, methods, and processes are used to convert winemaking derivatives into bioactive nutrient-rich products comprising antioxidants and other bioactive molecules that reside within the marc and lees. These nutrient-rich products can be used as natural flavour, texture and color enhancers, in addition to nutritional ingredients to fortify processed foods and consumer recipes. They can also be used as health supplements and in the cosmetic industry.

Provided are methods and systems for remediating toxins present in feedstock that are used in processes to produce ethanol and other products.

A device is provided having a fermentation chamber having one or more inlets to receive a mixed stream to be fermented and an outlet to release fermented product; a distillation vessel surrounding the fermentation chamber having communication with the fermentation chamber outlet to receive fermented product to be distilled and a turbine located within the outlet of the fermentation chamber, the turbine having a rotor rotatable by force of flow of fermented product from the fermentation chamber to the distillation vessel, to generate electricity. A sidewall common to both the fermentation chamber and distillation vessel allows for heat transfer of heat generated from fermentation to the distillation vessel to heat the product to be distilled. A method of fermenting and distilling a product is also provided. The method involves receiving in a fermentation chamber a mixed stream to be fermented; transferring heat energy generated by fermentation to a distillation vessel surrounding the fermentation chamber; allowing pressurized fermented product to flow from the fermentation chamber into the distillation vessel via a turbine and rotating a rotor of the turbine by a force of flow of the fermented product to the distiller to generate electricity.

A device is provided having a fermentation chamber having one or more inlets to receive a mixed stream to be fermented and an outlet to release fermented product; a distillation vessel surrounding the fermentation chamber having communication with the fermentation chamber outlet to receive fermented product to be distilled and a turbine located within the outlet of the fermentation chamber, the turbine having a rotor rotatable by force of flow of fermented product from the fermentation chamber to the distillation vessel, to generate electricity. A sidewall common to both the fermentation chamber and distillation vessel allows for heat transfer of heat generated from fermentation to the distillation vessel to heat the product to be distilled. A method of fermenting and distilling a product is also provided. The method involves receiving in a fermentation chamber a mixed stream to be fermented; transferring heat energy generated by fermentation to a distillation vessel surrounding the fermentation chamber; allowing pressurized fermented product to flow from the fermentation chamber into the distillation vessel via a turbine and rotating a rotor of the turbine by a force of flow of the fermented product to the distiller to generate electricity.

A process for the manufacture of butanol, acetone and/or other renewable chemicals is provided wherein the process utilises one or more of the group comprising by-products of the manufacture of malt whisky, such as draff, pot ale and/or spent lees, biomass substrates, such as paper, sludge from paper manufacture and spent grains from distillers and brewers, and diluents, such as water and spent liquid from other fermentations. The process comprises treating a substrate to hydrolyse it and fermenting the treated substrate at an initial pH in the range of 5.0 to 6.0. Also provided is a biofuel comprising butanol manufactured according to the process of the invention.

A process for the manufacture of butanol, acetone and/or other renewable chemicals is provided wherein the process utilises one or more of the group comprising by-products of the manufacture of malt whisky, such as draff, pot ale and/or spent lees, biomass substrates, such as paper, sludge from paper manufacture and spent grains from distillers and brewers, and diluents, such as water and spent liquid from other fermentations. The process comprises treating a substrate to hydrolyse it and fermenting the treated substrate at an initial pH in the range of 5.0 to 6.0. Also provided is a biofuel comprising butanol manufactured according to the process of the invention.