Producing a dealcoholized beverage from its alcoholic beverage starting product and plant for implementing the method, which comprises the following steps: separating the beverage starting product into an alcoholic and aromatic permeate and into an aromatic and almost alcohol-free retentate in a permeation module by non-thermal permeation, dealcoholizing the permeate in a module intended for that task, and finally mixing the dealcoholized permeate with the almost alcohol-free retentate in a final-mixing module. Prior to the dealcoholizing, aroma compounds are removed from the aromatic and alcoholic permeate by cold adsorption in an aroma adsorber, resulting both in an aroma phase and in an aroma-free but alcoholic permeate which, however, has the alcohol removed from it by alcohol separation, resulting in an aqueous, largely dearomatized and dealcoholized permeate water phase. Final mixing of aroma phase, permeate water phase and retentate takes place in the final-mixing module to give a dealcoholized beverage.

The disclosure relates to a device for fermentation integrated with separation and purification of acetone, butanol, and ethanol (ABE) or butanol alone, including a medium tank (1), used for supplying a medium into a bioreactor; a bioreactor (2), connected with the medium tank (1), used for fermentation; a gas distributor (9), used for supplying gas bubble to the fermentation broth; a membrane separation unit (4), with gas communication to the bioreactor (2), used for receiving a gas with ABE or butanol from the bioreactor and separating ABE or butanol; a condensation unit (5), used for recovering ABE or butanol; a vacuum manometer (6) and a vacuum pump (8), used for supplying a force for driving ABE or butanol in a vapor form; and product tank (7), used for receiving a product.

A method of and apparatus for recovering an alcohol solvent from a liquid mixture of the solvent and plant oil and decarboxylating the plant oil may include, pressurizing the liquid mixture to a super-atmospheric pressure, recirculating the pressurized liquid mixture a plurality of times through at least one membrane separator to separate some of the solvent from the mixture to provide a concentrated mixture of the plant oil with less solvent, reducing the pressure of the liquid concentrated mixture to less than 15 psig, heating it at a pressure of less than 15 psig to a temperature sufficient to vaporize the solvent in the concentrated mixture, removing sufficient heat from the vaporized solvent to condense it to a liquid solvent at atmospheric pressure and temperature conditions, and heating the plant oil to a temperature desirably of at least 215° F. to decarboxylate the plant oil.

The present invention is directed to improved systems and processes for clarifying a thin stillage stream in a biofuel production process, such as a dry grind alcohol production process, that removes desirable amounts of insoluble solids from at least a portion of the thin stillage stream, thereby realizing any number of process enhancements.

A system and method for washing and separating fiber in the processing of grains in between the steps of fermentation and distillation is disclosed. Also disclosed is a method for producing a high protein feed.

A method of and system for making at least four types of animal feed products for various types of animals to maximize and use all of the components found in the whole stillage in an alcohol producing plant. The method includes liquefying, fermenting, distilling, performing a selective particle size separating into three streams, wherein the three streams contain a first stream of a large particle stream that is used to form a first animal feed suitable for ruminant animals, a second stream of a coarse protein stream that is used to form a second animal feed suitable for chicken and pigs, and a third stream of a fine particle stream that is used to form a third animal feed suitable for fish and pet. The third stream is further concentrated and enriched to have a syrup with 35%-80% of dry solid.

The present disclosure provides processes and systems for ethanol production. In one embodiment, a first beer column receives a first portion of a feed mixture including ethanol and water to form a first beer column bottom stream and a first beer column vaporous overhead stream. A beer column receives a second portion of the feed mixture. A first portion of the first beer column bottom stream is forwarded to a first beer column reboiler. A second portion of the first beer column bottom stream is forwarded to a plurality of evaporators. A condensed portion of the first beer column vaporous overhead stream is forwarded to a stripper column. The stripper column forms a feed stream, which is contacted with a separation system, thereby forming a permeate and a retentate. The permeate is forwarded directly to at least one selected from the first beer column and the stripper column.

The present disclosure provides for organic solvent production via distillation and dehydration by: directing portions of a feed stream to a first and second distillation columns operating at a different pressures from each other, wherein the organic solvent is preferably an alcohol and more preferably ethanol; generating, in the first distillation column, a vaporous first overhead stream; directing the vaporous first overhead stream directly to a rectification system; generating, in the second distillation column, a vaporous second overhead stream; forming a condensed second overhead stream from the vaporous second overhead stream; directing, at least a portion of the condensed second overhead stream to the rectification system; generating, via the rectification system, a third overhead stream; directing at least a portion of the third overhead stream to a separation system; and generating, in the separation system, an enriched solvent stream.

Processes, systems and equipment are for treating a digestate resulting from the thin stillage of a bioethanol plant. They can include a decarbonizer system to reduce the carbon and water footprint in an ethanol plant and associated biogas plant by treating a digestate stream resulting from a thin stillage digester. The treatment includes heating the digestate stream to decompose ammonia bicarbonate contained in the digestate stream into ammonium and bicarbonate; and contacting the heated digestate stream with air so that a first portion of the ammonia is desorbed from the heated stream to mix with the air.

Disclosed is a process to produce a purified vapor comprising dialkyl-furan-2,5-dicarboxylate (DAFD). Furan-2,5-dicarboxylic acid (FDCA) and an alcohol in an esterification zone to generate a crude diester stream containing dialkyl furan dicarboxylate (DAFD), unreacted alcohol, 5-(alkoxycarbonyl)furan-2-carboxylic acid (ACFC), and alkyl furan-2-carboxylate (AFC). The esterification zone comprises at least one reactor that has been previously used in an DMT process.