Abstract: The process for pairing a fat continuous spread having from about 30 about 80% fat and having a trans fatty acid level of less than about 10% is described. An interesterified hardstock as described herein is combined with liquid oil to form a fat phase. The fat phase and an aqueous phase are combined to form an emulsion which is crystallized to form substantially beta prime crystals in the C-unit. The beta prime containing crystal containing emulsion is the emulsion exiting the initial A-unit at a throughput of the emulsion through the entire production line of x kilograms per hour, a residence time of the emulsion in the crystallizing (C-unit) of y minutes and the recirculation flow rate of the emulsion recirculated into the cooled partially crystallized emulsion of 0.2 x to 10 x to form the fat continuous product.

Abstract: The present invention pertains to a process for the production of polyol fatty acid polyesters by reacting a reactant mixture of polyol, a fatty acid lower alkyl ester, a transesterification catalyst and an alkali metal soap emulsifier. The process comprises removing non-dissolved alkali metal soap from the reaction mixture at a degree of transesterification of more than 60%, preferably 65-90%, and recycling the alkali metal soap that is removed during the transesterification to the starting reactant mixture. The invention is applicable both to a batch-wise polyol polyester synthesis and to a continuous synthesis.

Abstract: In a process of preparing a tea extract, the extract is adjusted to 20.degree.-80.degree. C., treated with tannase at pH=4-7 and then subjected to ultrafiltration at 2.degree.-90.degree. C. using a membrane with an average molecular weight exclusion point of at least 5000 Daltons (preferably at least 30,000 Daltons). The extract may finally be subjected to an additional filtration, preferably microfiltration. Also an instant a cold-water soluble tea powder or granulate is claimed.

Abstract: A process for refining soap-containing crude polyol fatty-acid polyester reaction product, the process including one or more high-temperature refining treatments and as the first step in the refining process, contacting the crude reaction product with an acid to substantially convert the soap into its corresponding free fatty acids, and the subsequent step of substantially removing from the crude reaction product any salts therein prior to said one or more high-temperature refining treatments.

Abstract: The present invention pertains to a process for refining soap-containing crude polyol fatty-acid polyester reaction product, comprising the step of contacting the crude reaction product with an aqueous acid solution to substantially convert the soap into its corresponding free fatty acids, the subsequent step of drying said crude reaction product to substantially remove any free-water therein, and the step of substantially removing from the dried crude reaction product any salts therein.

Abstract: A process for refining organic-solvent containing crude polyol fatty-acid polyester reaction product, including the steps of distilling the crude reaction product to substantially remove the organic solvent, and subsequently subjecting the distilled reaction product to a bleaching treatment. The process allows an economic use of bleaching agents while achieving good color and color stability of the refined product.

Abstract: A method of preparing a water-in-oil emulsion spread by mixing a wet gelatin retentate wherein the off flavor has been reduced by membrane filtration to remove a low molecular weight fraction, with a fat phase.