Described herein is a crystalline fat comprising a powder density ranging from about 0.04 g/mL to about 0.40 g/mL at room temperature and at least 50% of particles have a particle size ranging from 10 to 50 μm in diameter. Also described herein is a shortening comprising crystalline fat having a powder density ranging from about 0.04 g/mL to about 0.40 g/mL at room temperature and at least 50% of particles have a particle size ranging from 3 to 60 μm in diameter and a liquid oil; wherein the crystalline fat ranges from about 25 wt % to about 99.9 wt % and the liquid oil ranges from about 0.1 wt % to about 75 wt %.

Process for manufacturing edible fat continuous emulsions comprising 10 to 85 wt. % of a dispersed water-phase and 15 to 90 wt. % of total fat, said process comprising the steps of: a. providing a water-phase; b. providing liquid oil; c. providing fat powder comprising hardstock fat; d. providing hardstock fat in liquid form; e. mixing fat powder comprising hardstock fat, hardstock fat in liquid form and liquid oil to provide an oil-slurry; f. mixing the oil-slurry provided at step ‘e’ with the water-phase to provide a water-in-oil emulsion, wherein the fat powder is not subjected to temperatures at which a substantial part of the fat powder melts. An edible fat continuous emulsion comprising 10 to 85 wt. % of a dispersed water-phase and 15 to 90 wt. % of total fat, comprising at least 2 wt. %, based on the weight of total fat, of a first hardstock fat with the following solid fat profile: N20 from 65 to 95; N35 from 25 to 55; and further comprising at least 2 wt. %, based on the weight of total fat, of a second hardstock fat with the following solid fat profile: N20 from 5 to 95; N30 below 60, wherein the Quotient-A is from 0.95 to 0.2, and wherein the emulsion has a glossiness-value of at least 4 and a Stevens-value of at least 75, wherein Quotient-A is the FWHM value of an emulsion divided by the FWHM value of the emulsion after rework using a votator process.

Process for manufacturing edible fat continuous emulsions comprising 10 to 85 wt. % of a dispersed water-phase and 15 to 90 wt. % of total fat, said process comprising the steps of: a. providing a water-phase; b. providing liquid oil; c. providing fat powder comprising hardstock fat; d. providing hardstock fat in liquid form; e. mixing fat powder comprising hardstock fat, hardstock fat in liquid form and liquid oil to provide an oil-slurry; f. mixing the oil-slurry provided at step ‘e’ with the water-phase to provide a water-in-oil emulsion, wherein the fat powder is not subjected to temperatures at which a substantial part of the fat powder melts. An edible fat continuous emulsion comprising 10 to 85 wt. % of a dispersed water-phase and 15 to 90 wt. % of total fat, comprising at least 2 wt. %, based on the weight of total fat, of a first hardstock fat with the following solid fat profile: N20 from 65 to 95; N35 from 25 to 55; and further comprising at least 2 wt. %, based on the weight of total fat, of a second hardstock fat with the following solid fat profile: N20 from 5 to 95; N30 below 60, wherein the Quotient-A is from 0.95 to 0.2, and wherein the emulsion has a glossiness-value of at least 4 and a Stevens-value of at least 75, wherein Quotient-A is the FWHM value of an emulsion divided by the FWHM value of the emulsion after rework using a votator process.

A device for automatic extraction, storage and encapsulation of fatty compounds, the device may include: an extraction unit configured to provide a liquid mixture comprising fatty compounds extracted from biological material and a liquid solvent; an evaporation and reaction unit; a storage unit comprising one or more storage outlet ports; and a controller configured to: control delivery of the liquid mixture from the extraction unit to the evaporation and reaction unit; control evaporation of the solvent from the liquid mixture in the evaporation and reaction unit; control delivery of the liquid mixture from the evaporation and reaction unit to the storage unit; detect safe connection of each of at least one of one or more capsules to one of the one or more storage outlet ports of the storage unit; and control filling of at least one of the one or more connected capsules with the liquid mixture.

A process for producing a fat-encapsulated ingredient. A fat is metered into an extruder, the fat having a melting point of at least 50° C. The fat is heated in in the extruder during rotation of at least one screw. At least one ingredient is metered into a barrel of the extruder to produce a flowable mixture. The flowable mixture is cooled in a a downstream adjacent section of the extruder barrel. The mixture is subsequently discharged through an extruder die. After discharge, the mixture is comminuted.

A process for the production of fat-encapsulated follistatin. The process includes metering fat having a melting point of at least 40° C. into an extruder, heating the fat in the extruder during rotation of the at least one screw, metering the follistatin into the extruder barrel to produce a flowable mixture, cooling the flowable mixture in a downstream adjacent section of the extruder barrel, subsequently discharging the mixture through an extruder die, and comminuting the mixture after it discharges from the extruder die.

Provided is an edible material having an exceptional sweetness-enhancing effect. This oxidized product of a palm-based oil and fat has a total content of α-carotene and β-carotene of 50 mass ppm or more and 2000 mass ppm or less, and a peroxide value of the oxidized product of 3 or more and 250 or less.

Provided is means of powderizing a liquid component, wherein the powderizing agent contains an oil and/or fat composition, and when a total triglyceride content is set to 100% by mass, the oil and/or fat composition contains 65 to 99% by mass of one or more types of XXX-type triglycerides having fatty acid residues X, each with x carbon atoms, at positions 1 to 3 and 35 to 1% by mass of one or more types of X2Y-type triglycerides each having a fatty acid residue Y with y carbon atoms in place of one of the fatty acid residues X of the XXX-type triglyceride, x, the number of carbon atoms, is an integer selected from 8 to 20, and y, the number of carbon atoms, is each independently an integer selected from x+2 to x+12 and satisfies y≤22.

Provided is means of powderizing a liquid component, wherein the powderizing agent contains an oil and/or fat composition, and when a total triglyceride content is set to 100% by mass, the oil and/or fat composition contains 65 to 99% by mass of one or more types of XXX-type triglycerides having fatty acid residues X, each with x carbon atoms, at positions 1 to 3 and 35 to 1% by mass of one or more types of X2Y-type triglycerides each having a fatty acid residue Y with y carbon atoms in place of one of the fatty acid residues X of the XXX-type triglyceride, x, the number of carbon atoms, is an integer selected from 8 to 20, and y, the number of carbon atoms, is each independently an integer selected from x+2 to x+12 and satisfies y≤22.

A device for automatic extraction, storage and encapsulation of fatty compounds, the device may include: an extraction unit configured to provide a liquid mixture comprising fatty compounds extracted from biological material and a liquid solvent; an evaporation and reaction unit; a storage unit comprising one or more storage outlet ports; and a controller configured to: control delivery of the liquid mixture from the extraction unit to the evaporation and reaction unit; control evaporation of the solvent from the liquid mixture in the evaporation and reaction unit; control delivery of the liquid mixture from the evaporation and reaction unit to the storage unit; detect safe connection of each of at least one of one or more capsules to one of the one or more storage outlet ports of the storage unit; and control filling of at least one of the one or more connected capsules with the liquid mixture.