The present invention relates to a process of compacting a microporous fat powder, notably a microporous fat powder that can suitably be used as an oil structuring agent.

One aspect of the invention relates to a process for compacting a microporous fat powder, said process comprising: feeding the fat powder into the feed zone of an extruder having a forwarding screw and a barrel within which said screw is centrally positioned; rotating said forwarding screw to advance said fat powder feed through a compacting zone of the extruder where the barrel comprises a plurality of venting openings having a shorter dimension that exceeds the volume weighted average diameter of the fat powder feed and that is less than 10 mm; and expelling the compacted fat powder from the extruder;
wherein the temperature of the fat powder during passage through the extruder is maintained below 40 C. and wherein the compaction factor achieved exceeds 1.5

Another aspect of the invention relates to a compacted microporous fat powder having the following characteristics: a freely settled density in the range of 90-600 g/l; a particle size distribution with at least 90 vol. % of the particles having a diameter in the range of 20 to 600 m; a maximum G.sub.i/G.sub.d ratio of more than 2.0, wherein G represents the elastic modulus at 10 C. of a dispersion of 2 wt. % of the compacted fat powder in glycerol, and wherein the maximum ratio is determined by recording G.sub.i whilst increasing the frequency from 0.1 to 15 s.sup.1, by subsequently recording G.sub.d whilst decreasing said frequency from 15 to 0.1 s.sup.1, and by calculating the ratio G.sub.i/G.sub.d at the frequency at which said ratio is highest.

The present invention provides an oil and fat having plasticity and excellent meltability in the mouth in a wide range of temperatures and a roll-in oil and fat composition using the plastic oil and fat having excellent extensibility and excellent meltability in the mouth in a wide range of temperatures. This roll-in oil and fat composition that has a stiff texture and exhibits excellent extensibility and superior intraoral solubility over a wide range of temperature is obtained by using a transesterified oil and fat which contains, with respect to the total amount of all constituent fatty acids, 5-25 wt % of lauric acid, 5-25 wt % of palmitic acid, and 10-35 wt % of stearic acid, and in which the weight ratio of stearic acid to palmitic acid (stearic acid/palmitic acid) is 0.5-7.

A hardstock fat composition for use in making edible water-in-oil emulsions such as spreads, in particular (but not exclusively) when produced using the hardstock in the form of micronized fat powder, and process to use such hardstock fat to make a fat slurry and to make a water-in-oil emulsion (like spreads) using such hardstock fat. The hardstock fat may give improved properties of the resulting emulsion.

The present technology is directed generally to compositions for inducing a color and/or chemical and/or physical change to a foodstuff, such as a previously baked bread or other starches and proteins, and associated methods and systems. In some embodiments, the compositions are browning butters and include Maillose as a browning agent. Some embodiments further include an additive such as a protein, a reducing sugar, or an alkaline agent.

A composition and method for supplementing food, nutrition, and diet systems with omega-6 to omega-3 balanced oils comprising a synergistic blend of at least two oils. The composition further comprises a synergistic blend of long chain omega-3 oil as a means to further increase the nutritional value. The composition provides an effective increase in therapeutic and pharmacological properties in nutrition and diet systems.

Hardstock fat having an amount of saturated fatty acids of at least 80 wt %, wherein the amount of H3mixed triglycerides is between 45 and 60 wt %, H3mixed being a group of triglycerides consisting of triglycerol esters of 3 H fatty acids wherein H is a saturated fatty acids having a length of C16 and/or C18, wherein the triglycerol ester is composed of two different fatty acids; and wherein the amount of H2Xmixed triglycerides is at least 10 wt %, H2Xmixed being a group of triglycerides consisting of H2M triglycerides and H2O triglycerides, wherein H2M triglycerides are triglycerol esters with two H fatty acid and one M fatty acid wherein M is a saturated fatty acid of a length of C12 and/or C14, and wherein H2O triglycerides are triglycerol esters with two H fatty acid and one O fatty acid wherein O is a unsaturated fatty acid of a length of C18, wherein the H2M and H2O triglycerides are composed of three different fatty acids.

A process for preparing a slurry of edible oil and fat powder, and to a process of preparing an edible fat-continuous spread out of such. The process for preparing said slurry has at least two different regimes of reduced pressure.

The invention relates to a process for the manufacture of an edible water-in-oil emulsion comprising 10 to 85 wt. % of liquid oil, 0.5 to 50 wt. % of hardstock fat, 10 to 85 wt. % of a dispersed water-phase; comprising the steps of: a) providing a first water-in-oil emulsion; b) providing a second water-in-oil emulsion; and c) mixing said first and second emulsion to provide a finished edible water-in-oil emulsion. The invention further relates to water-in-oil emulsions having a distinct water-phase release profile.

The present invention relates to a composition containing first oleosomes having a first distribution D50(1) and second oleosomes having a second size distribution D50(2).

Provided are edible emulsions that can be used as smoothies, creamers, syrups or other products to be used in food or consumed directly. The emulsions contain relatively high amounts, such as 10%-50% by weight of a protein composition, such as one or more of nut butters, whey, and, optionally, collagen, and very low amounts of a surfactant, typically less than 2%, such as less than 1.5%. The resulting emulsions are stable and have large particles in the range of about 3 m, 4 m or 5 m to 10 m or 15 m. As a result, the emulsions have a creamy consistency.