The present disclosure provides methods of preparing a high color concentrate (HCC) wine. Aspects of the methods may include obtaining a grape fluid composition from one or more grapes, contacting the grape fluid composition with a reagent to modify the pH, adding an amount of distilled alcohol to the grape fluid composition to produce a fortified wine composition, and concentrating the fortified wine composition to produce an HCC wine. Aspects of the methods may further include obtaining a must from one or more grapes, fermenting the must to produce a grape fluid composition having a percent alcohol content, contacting the grape fluid composition with a reagent to modify the pH, and concentrating the grape fluid composition to produce an HCC wine. Also provided is a composition including the HCC wine produced according to the subject methods.

The present invention relates to a process for the concentration of a water-soluble organic peroxide, preferably an alkyl hydroperoxide, by reverse osmosis as well as to a process for the separation of a water-soluble organic peroxide and of a water-insoluble compound.

Provided are metal oxide ceramic materials and intermediate materials thereof (e.g., nanozirconia gels, nanozirconia green bodies, pre-sintered ceramic bodies, zirconia dental ceramic materials, and dental articles). The nanozirconia gels are formable gels. Also provided are methods of making and using the metal oxide materials and intermediate materials. The nanozirconia gels can be made using, for example, osmotic processing. The nanozirconia gels can be used to make nanozirconia green bodies, pre-sintered ceramic bodies, zirconia dental ceramic materials, and dental article. The nanozirconia green bodies, pre-sintered ceramic bodies, zirconia dental ceramic materials, and dental articles have desirable properties (e.g., optical properties and mechanical properties).

An organic solvent purification system that separates an organic solvent having a boiling point of more than 100 C. at 1 atm, such as N-methyl-2-pyrrolidone (NMP), from a liquid mixture containing the organic solvent and water and purifies the organic solvent includes: a heater that heats the liquid mixture; a pervaporation apparatus that includes a pervaporation membrane, and is provided at subsequent position of the heater, the pervaporation apparatus separating the organic solvent from the water; a vacuum evaporator to which the organic solvent collected from a concentration side of the pervaporation apparatus is supplied; and piping that supplies the heater with the organic solvent vaporized in the vacuum evaporator as a heat source of the heater. The heater heats the liquid mixture using concentration heat of the organic solvent vaporized by the vacuum evaporator.

The invention relates to the field of water purification, namely to methods and devices for water purification using the ultrafiltration method and is intended primarily for purifying water with organic contaminants. The method of purifying water with organic impurities by ultrafiltration consists of preliminary preparation of water for ultrafiltration, which consists of ozonation and mixing by recirculation in a contact container, as well as in the process of ultrafiltration itself utilizing membranes. In the near-membrane space of the ultrafiltration device there is formed a high-speed gas-liquid regime with a water-bubble flow flowing around the membrane surface. Wherein, water supplied to the ultrafiltration device is carried out simultaneously with the supply of ozone-air or ozone-oxygen mixture through at least one water-jet ejector. A second recirculation cycle is organized through the ultrafiltration device into the contact container and again into the ultrafiltration device. In the near-membrane space of the ultrafiltration device there is formed a high-speed gas-liquid regime with a water-bubble flow flowing around the membrane surface. Wherein the water flow through the water-jet ejector is set in the range from 0.5 to 45 m.sup.3/h, the ozone mixture flow is in the range from 0.3 to 30 m.sup.3/h, and pressure in the ejector discharge line is in the range from 0.2 to 1.6 MPa. The method is carried out using a system including an ozonation device, a contact tank, a recirculation line and an ultrafiltration device itself. At least one water-jet ejector is provided at the inlet to the ultrafiltration device, wherein the working diameter of the suction nozzle relates to the working diameter of the discharge line nozzle in the values between 0.35 and 1.0.

The present invention includes methods and systems for improving oil quality of a contaminated oil mixture by removing contaminants from a contaminated oil comprising the steps of: pretreating a membrane contactor system having a first and a second surface with an hydrophobic liquid, wherein the hydrophobic liquid is contacted to at least one of the first and second surfaces; obtaining a contaminated oil that comprises oil and lipophobic contaminants; contacting the contaminated oil onto a first surface of one or more membrane contactors to coalesce the oil on the first surface; and collecting the coalesced oil from the contaminated oil on the second surface of the membrane contactor.

The present invention includes methods and systems for improving oil quality of a contaminated oil mixture by removing contaminants from a contaminated oil comprising the steps of: pretreating a membrane contactor system having a first and a second surface with an hydrophobic liquid, wherein the hydrophobic liquid is contacted to at least one of the first and second surfaces; obtaining a contaminated oil that comprises oil and lipophobic contaminants; contacting the contaminated oil onto a first surface of one or more membrane contactors to coalesce the oil on the first surface; and collecting the coalesced oil from the contaminated oil on the second surface of the membrane contactor.

A series of multi-dimensional acoustic standing waves is set up inside a growth volume of a bioreactor. The acoustic standing waves are used to hold a cell culture in place as a nutrient fluid stream flows through the cell culture. The nutrient fluid stream dislodges some cells from the cell culture, which can then be recovered for cell therapy applications. The cell culture continues to expand and reproduce, permitting continuous recovery of cells from the bioreactor.

The present invention relates generally to processes for converting fructose-containing feedstocks to a product comprising 5-(hydroxymethyl)furfural (HMF) and water in the presence of water, solvent and an acid catalyst. In some embodiments, the conversion of fructose to HMF is controlled at a partial conversion endpoint characterized by a yield of HMF from fructose that does not exceed about 80 mol %. In these and other embodiments, the processes provide separation techniques for separating and recovering the product, unconverted fructose, solvent and acid catalyst to enable the effective recovery and reutilization of reaction components.

An organic solvent purification system that separates an organic solvent having a boiling point of more than 100 C. at 1 atm, such as N-methyl-2-pyrrolidone (NMP), from a liquid mixture containing the organic solvent and water and purifies the organic solvent includes: a heater that heats the liquid mixture; a pervaporation apparatus that includes a pervaporation membrane, and is provided at subsequent position of the heater, the pervaporation apparatus separating the organic solvent from the water; a vacuum evaporator to which the organic solvent collected from a concentration side of the pervaporation apparatus is supplied; and piping that supplies the heater with the organic solvent vaporized in the vacuum evaporator as a heat source of the heater. The heater heats the liquid mixture using concentration heat of the organic solvent vaporized by the vacuum evaporator.