Processes for grinding corn, ground corn products, and processes for making ethanol from the ground corn products. In some examples, a process for making ethanol can include introducing a plurality of corn pieces into a mill. The process can also include milling the corn pieces in the mill to produce a ground corn product. Greater than 25 wt % of the ground corn product can have a particle size of greater than 105 μm, as measured according to AOAC 965.22-1966. Greater than 80 wt % of the ground corn product can have a particle size of 425 μm or less, as measured according to AOAC 965.22-1966. The process can also include processing the ground corn product to produce a fermentation mash that can include ethanol and separating at least a portion of the ethanol from the fermentation mash to produce a stillage.

The present disclosure includes systems and methods for hydrolyzing (e.g., pretreatment and/or enzymatic hydrolysis) lignocellulosic biomass into one or more sugars such as pentose and glucose sugars. The present disclosure includes configurations that incorporate flashing and/or liquid cooling so as to permit desirable throughput. The present disclosure also includes a liquefaction configuration so as to permit desirable (e.g., continuous high volume) throughput.

The present invention relates to an improved method and device for treating biomass in which thermally treated biomass is discharged from a pressurized reactor and introduced into a blow tank and then a flash tank, wherein the absolute pressure in the blow tank is maintained above atmospheric pressure and the absolute pressure in the flash tank is maintained below atmospheric pressure. The slurry of biomass separated in the flash tank is then enzymatically treated. The heat from the thermally treated biomass is recovered from the latent heat of a vaporous aqueous stream withdrawn from the blow tank.

Preparation of a product comprising stromal vascular traction cells includes washing human biological material comprising adipose in a container apparatus having an internal filter, which divides an internal containment volume of the container apparatus into a tissue retention volume on one side of the filter and a filtrate volume on an opposite side of the filter, and a mixing device with at least one rotatable mixing member disposed in the tissue retention volume. The washing includes operation of the mixing device to rotate the mixing member through the human biological material within the tissue retention volume, and the washing is followed by digesting washed material within the internal containment volume with added enzyme, centrifuging of the container apparatus to prepare a centrifuged pellet in the filtrate volume, selectively removing material of the pellet and preparing a product with a mixture of stromal vascular fraction cells of removed pellet material and an aqueous suspension liquid.

A tissue processing system for dissociation of and release of cellular components from adipose tissue to prepare stromal vascular fraction includes a portable tissue processing unit for containing biological material including adipose tissue during enzymatic digestion processing and a digestion drive unit configured to receive the tissue processing unit for rotational processing of the tissue processing unit about an axis of rotation. The unit has an upright orientation and a reclined orientation in which the axis of rotation is at a reclined angle to horizontal relative to the upright orientation. The digestion drive unit is configured to receive and drive rotation of the tissue processing unit in the reclined orientation. Methods for processing biological material including adipose tissue include enzymatically digesting adipose tissue with rotation of a tissue processing unit around an axis of rotation in a reclined orientation.

The invention relates to a method for controlling an enzymatic pre-treatment process, e.g. a mashing process. The method allows for accurate determination of specific sugar molecules as well as the average length of the sugar chains in real-time during e.g. a mashing process. Further information on e.g. the concentration of dissolved protein and free amino acids can also be obtained simultaneously. The method comprises the use of an infrared (IR) spectometer for continuously measuring attenuated total reflectance (ATR) IR spectra of samples obtained during pre-treatment of biomass.

The present invention relates to the use of warmers, or autonomous heat packs, for heating and maintaining a solution at a suitable temperature, for the period of time required to accomplish a chemical, biochemical or biological reaction, in particular in molecular biology or cell biology applications. Biology kits containing warmers are also part of this invention.

Methods of decellularization of tissue, such as mammalian tissue, are provided, along with methods of making an extracellular matrix (ECM) preparation. Systems and apparatus useful in performing the methods are also provided.

In some embodiments, a kit for preparing a cell suspension may include a device and a housing. The device may include a first label identifying a first reservoir of the device for use with a first portion of a tissue processing method and a second label identifying a second reservoir of the device for use with a second portion of the tissue processing method. The housing includes a first housing portion configured to store a first set of components associated with the first portion of the tissue processing method. The first housing portion includes a first visual indicator associated with the first label of the device. The second housing portion may be configured to store a second set of components associated with the second portion of the tissue processing method. The second housing portion may include a second visual indicator associated with the second label of the device.

A method and apparatus for enzymatic hydrolysis where a plant based feed is hydrolysed using an enzyme to form a hydrolysed product. An additive for preventing enzyme adsorption is fed to an enzymatic hydrolysis stage, the plant based feed, the hydrolysed product, a starting material, and/or a plant based material formed from the starting material. The hydrolysed product is supplied from the enzymatic hydrolysis stage to a first solid-liquid separation stage where a lignin fraction comprising the additive and a liquid composition comprising the enzyme are separated. The liquid composition is mixed with the plant based material in a mixing stage, forming a mixture. A solid and liquid fraction are separated from the mixture in a second solid-liquid separation stage. At least part of the solid fraction comprising the enzyme is fed as the plant based feed to the enzymatic hydrolysis stage.