Virdia, Inc.

Yissum Research Development Company of the Hebrew University of Jerusalem Ltd.

Asher Vitner Ltd.

Joma International As

Blue Tree Technologies Ltd.

A E Staley Manufacturing Company

Tate & Lyle Ingredients Americas LLC

Adama Makhteshim, Ltd.

Amylum Belgium N.v.

Tate & Lyle Ingredidents Americas, Inc.

N-drip Ltd.

Pigmentan Ltd.

Asher Vitner

Revital Mali

Robert P Jansen

Aharon Meir Eyal

Aharon Eyal

Avraham Baniel

Didier Toubia

Betty Hazan

Avraham M Baniel

Anthony Baiada

Zach Barnea

Matti Ben-Moshe

Pierre Cami

Gregory Pipko

Uri Shani

Tal Reuveni

Bruno Jarry

Sharon Dabach

David Heidel

Zvi Miller

Thomas Chattaway

Robert J Jansen

Emmanuel Mailly

Joelle More

David Gonen

Eran Segal

Boaz Rozengarten

Xiaohong Xia

Methods and systems are disclosed for selectively removing naturally-occurring sugars in beverages in an effective, affordable and scalable manner.

Methods and systems for producing low sugar beverages

Method and systems are disclosed for selectively removing naturally-occurring sugars in beverages in an effective, affordable and scalable manner.

A method comprising: (a) providing a partially processed sucrose crop product containing at least 2% optionally at least 5% of the sucrose content of said crop at harvest on a dry solids basis, cellulose and lignin; (b) hydrolyzing said partially processed crop product with HCl to produce an acid hydrolyzate stream and a lignin stream; and (c) de-acidifying said hydrolyzate stream to produce a de-acidified sugar solution and an HCl recovery stream. Additional, methods, systems and sugar mixtures are also disclosed.

Methods and systems for processing a sucrose crop and sugar mixtures

A sugar mixture comprising: monosaccharides; oligosaccharides in a ratio&#x2265;0.06 to total saccharides; disaccharides in a ratio to total saccharides&#x2265;0.05; pentose in a ratio to total saccharides&#x2265;0.05; at least one alpha-bonded di-glucose; and at least one beta-bonded di-glucose. Also disclosed are methods to make and/or use such mixtures.

Sugar mixtures and methods for production and use thereof

A sugar mixture comprising: monosaccharides; oligosaccharides in a ratio &#x2265;0.06 to total saccharides; disaccharides in a ratio to total saccharides &#x2265;0.05; pentose in a ratio to total saccharides &#x2265;0.05; at least one alpha-bonded di-glucose; and at least one beta-bonded di-glucose. Also disclosed are methods to make and/or use such mixtures.

The present invention provides a bead comprising: i) an external zone comprising a super absorbent polymer (SAP) that is capable of absorbing at least about 5 times its weight in water, surrounding ii) at least one internal zone comprising a core that contains at least one agrochemical, wherein the external zone is permeable to oxygen when hydrated, or the internal zone is formulated to release the at least one agrochemical into the external zone over a period of at least about one week when the hydrogel of the external zone is hydrated. The present invention also provides methods of using beads of the invention.

Microenvironment for efficient uptake of fertilizers and other agrochemicals in soil

A sugar mixture comprising: monosaccharides; oligosaccharides in a ratio &#x2267;0.06 to total saccharides; disaccharides in a ratio to total saccharides &#x2267;0.05; pentose in a ratio to total saccharides &#x2267;0.05; at least one alpha-bonded di-glucose; and at least one beta-bonded di-glucose. Also disclosed are methods to make and/or use such mixtures.

The present invention provides a method for the Industrial production of a titanium salt TP, said method comprising the steps of: i. Precipitation of titanic acid from a solution comprising titanium salt TP1; ii. Production of a titanium containing product TP2 from a medium comprising of said titanic acid and an acid; and iii. Thermal conversion of titanium containing product TP3 to a titanium salt TP at temperature higher than 170&#xb0; C.

Process for the production of titanium salts

The present invention provides a process for the purification and concentration of a partially water-soluble organic product from a source containing the same at concentration C0, which process comprises the steps of: (i) concentrating said product by means of a resin to form a first aqueous solution at concentration of C1; and (ii) fractionating an aqueous solution by temperature adjustment to form a second aqueous solution and a third aqueous solution with concentrations C2 and C3, respectively, wherein C2&#x3e;C3 and C2&#x3e;C1&#x3e;C0.

Process for the recovery of a fermentation product

The invention provides a method for the formation of small-size titanium oxide particles, comprising the steps of a) preparing a starting aqueous solution comprising at least one of titanic ions and complexes thereof, at a concentration of at least 0.1% w/w titanium; b) maintaining the solution at a temperature lower than 70&#xb0; C. for a retention time in which hydrolysis takes place, the extent of the hydrolysis being sufficient to produce O.i mmol protons per mmol of titanium present in solution, wherein the time does not exceed 14 days, to form a system containing a retained solution; and c) adjusting the conditions in the system by at least one of the steps of: i) heating the retained solution to elevate the temperature thereof by at least 1&#xb0; C.; ii) changing the pH of the retained solution by at least 0.1 units; and iii) diluting the retained solution by at least 20% whereby there are formed particles, wherein the majority of the particles formed are between about 2 nm and about 500 nm in size.

Methods for production of titanium oxide particles, and particles and preparations produced thereby

The invention provides a method for the Industrial purification of a titanium feed stream of purity P1, by the formation of a titanium-double-salt precipitate of purity P2 and a titanium solution with purity P3, wherein P2&#x3e;P1&#x3e;P3, the method comprising the steps of: i. forming, from the feed, a medium comprising water, titanium ion, a cation selected from the group consisting of ammonium, cations of alkali metals, protons and a combination thereof, and an anion selected from the group consisting of OH, SO4, HSO4, halides and a combination thereof, which formed medium is further characterized by the presence of (a) a double-salt precipitate comprising titanium ion, at least one of the cations and at least one of the anions; and (b) a titanium solution; and wherein the concentration of the anion in the titanium solution is higher than 15% and the ratio between the concentrations of the cation and the anion in the titanium solution is higher than 0.2 and lower than 1.6; and ii. separating at least a portion of the precipitate from the solution.

Process for the production of titanium products

Disclosed herein are processes for the recovery of 1,3-propanediol from an aqueous feed stream. The present invention involves contacting an aqueous feed stream that comprises water, 1,3-propanediol, and at least one contaminant with at least one solvent extractant to form a mixture. The mixture is separated into a first phase and a second phase. The second phase comprises a majority of the water from the aqueous feed stream. The first phase comprises solvent extractant and at least some of the 1,3-propanediol that was present in the aqueous feed stream. The weight ratio in the first phase of 1,3-propanediol to any one contaminant present is greater than the weight ratio of 1,3-propanediol to the same contaminant in the aqueous feed stream prior to the aqueous feed stream being contacted with the solvent extractant. The first phase can be removed from the separated second phase in order to recover the 1,3-propanediol.

Process for producing 1,3-propanediol

The invention provides a process for the recovery of citric acid from an aqueous solution feed stream originating in fermentation of carbohydrates and utilizing an amine solvent extraction step for separation of impurities comprising: subjecting said aqueous solution feed stream A to a treatment for partial recovery of citric acid, wherein said treatment is other than amine solvent extraction, to form a first portion of purified citric acid B and a secondary feed stream F; subjecting at least a portion G of said secondary feed stream F to a treatment consisting of amine solvent extraction to form a second portion of purified citric acid solution and to reject substantial of impurities initially present in said portion of said secondary feed stream; subjecting said second portion of purified citric acid solution to crystallization; and recycling mother liquor from said crystallization.

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Jerusalem, Israel

Asher Vitner