Abstract:
The present invention relates to methods and systems of pitching yeast to fermentation reactors. More particularly, the present invention involves pitching yeast from one fermentation tank to at least one additional fermentation tank. Advantageously, yeast can be continuously pitched from fermentor to fermentor for as long as practically desirable.
Abstract:
A system for fermentation of biomass is disclosed. The system comprises a method for producing a fermentation product in a fermentation system from biomass that has been pre-treated and separated into a first component and a second component. The method comprises the steps of supplying the first component to the fermentation system; providing an ethanologen to the fermentation system; maintaining the first component and ethanologen in the fermentation system; and recovering the fermentation product from the fermentation system. A fermentation system configured to produce a fermentation product from biomass that has been pre-treated and separated into a first component and a second component is disclosed. The system comprises a first vessel configured to receive the first component and an ethanologen and a second vessel configured to propagate the ethanologen for supply to the first vessel. A biorefinery for producing a fermentation product from biomass is also disclosed. The biorefinery comprises a preparation system to prepare the biomass into prepared biomass; a pre-treatment system to pre-treat the prepared biomass with a dilute acid for separation into a first component from which pentose can accessed for fermentation and a second component from which hexose can be made available for fermentation; a first treatment system to treat the first component into a treated first component by removing removed components from the first component; a first fermentation system to produce a first fermentation product from the pentose; a distillation system to recover ethanol from the first fermentation product; and a treatment system to process removed components. The biomass comprises lignocellulosic material; the lignocellulosic material comprises at least one of corn cobs, corn plant husks, corn plant leaves and corn plant stalks. The first component comprises pentose; the pentose comprises xylose. The ethanologen is capable of fermenting xylose into ethanol.
Abstract:
A system and method for managing an ethanologen for use in biorefinery is disclosed. The method for propagating ethanologen for use in the production of a fermentation product from biomass comprises the steps of providing a medium for propagation of ethanologen; supplying a first cell mass of ethanologen to the medium; supplying xylose to the medium as a carbon source for the ethanologen; and maintaining the medium comprising the first cell mass of ethanologen at a pH of between about 5.0 and 6.0 and at a temperature of between about 26 and About 37 degrees Celsius so that the first cell mass of ethanologen is propagated into a second cell mass of ethanologen. The second cell mass of ethanologen is larger than the first cell mass of ethanologen. The system for propagating ethanologen for use in the production of a fermentation product from biomass comprises a first stage comprising a first vessel configured to maintain a medium comprising ethanologen; a second stage comprising a second vessel configured to maintain a medium supplied from the first stage; a source of xylose to be provided to the medium as a carbon source for ethanologen in the first stage; and a source of xylose to be provided to the medium as a carbon source for the ethanologen in the second stage. The ethanologen has a first cell mass when supplied to the first stage and the ethanologen has a second cell mass when supplied from the first stage to the second stage and the ethanologen has a third cell mass when supplied from the second stage. The second cell mass is at least 200 times larger than the first cell mass The third cell mass is at least 20 times larger than the second cell mass.
Abstract:
Systems and methods for improving ethanol yield are provided. A feedstock is ground suitably fine for use in fermentation. The feedstock may include corn or any other suitable material. In some cases, the feedstock undergoes a fractionation prior to grinding. The ground feedstock may be slurried with water and enzymes to facilitate conversion of the starch in the feedstock to sugars. The slurry may be about 35% solids. After being slurried, an ethanologen may be added. Additionally, the pH of the slurry may be adjusted to between 4.2 and 5.2 to facilitate the priming. A primer is added to the slurry. The primer may include any weak acid, and in some embodiments includes acetic acid. Acetic acid, when used as a primer, may be added at a concentration of between 1200 and 3600 parts per million. The slurry is fermented to produce improved yields of ethanol.
Abstract:
Systems and methods for increasing fermentation efficiency of a lignocellulosic hydrolysate are disclosed. The system comprises a filter configurable to remove matter having a particle size of larger than about 25 to 100 microns from the liquid component, and at least one nanofilter configurable to remove acids from the liquid component. An apparatus is used to adjust the pH of the nanofiltered liquid component using a calcium hydroxide composition to a pH of about 5.5 to 6.0. The calcium hydroxide composition includes calcium hydroxide alone or in combination with either ammonium hydroxide and/or potassium hydroxide. The biomass comprises lignocellulosic material including at least one of corncob, corn plant husk, corn plant leaves, and corn plant stalks.
Abstract:
The present invention relates to using high oil corn to make a biochemical such as ethanol. More particularly, the invention relates to methods of making a biochemical using relatively low temperature saccharification followed by fermentation or simultaneous saccharification and fermentation of high oil corn.
Abstract:
The present invention relates to systems and methods for propagating yeast using a feedstock material such as starch and one or more enzymes (e.g., an enzyme cocktail) to break down the feedstock material into one or more monosaccharides at a sufficient rate so that the yeast can use the monosaccharides as a carbon source for producing more yeast cells while not producing an undue amount of alcohol.
Abstract:
Disclosed are methods and systems for propagating microorganisms such as yeast using a carbon source that includes glycerol and a nutrient source that includes a stillage component.
Abstract:
Assessing quality of feedstock is provided and may be useful for determining quality of feed (such as corn kernels). The assessment determines endogenous enzyme activity within the feedstock, which correlates with total ethanol yields in raw starch hydrolysis (non-cooked) systems. In some embodiments, a sample containing flour (ground feedstock) is provided. In some cases, flour is diluted in water and buffered with a phosphate buffered solution. The buffered flour solution is contacted with a molecule, or fluorescent dye, such as fluorescein diacetate and/or difluorofluorescein that is altered by enzymatic (esterase) activity in a detectable fashion. Enzyme activity may be facilitated using an incubator. The detectible alteration may be measured using a fluorometer. In some embodiments, two incubations and fluorescence measurements can be performed. By subtracting the difference between the measured fluorescence, a fluorescence index may be found, which correlates with the endogenous enzyme activity in the feedstock sample.