Disclosed is a process for de-acidification of fats and oils, to obtain micronutrients, to obtain a fatty acid product, and recovery of refined oils, comprising: feeding pre-treated oil feed stream to a vacuum steam stripping section, stripping off volatile phases. Feeding the stripped off the volatile phases to a condensing stage providing a condensed phase and a vapour phase. Sending the condensed phase to a vacuum distillation operation and sending the vapour phase to a cold condensation stage. Subjecting the condensed phase to a vacuum distillation operation, and obtaining a high temperature distillate and a stream of volatiles. Feeding the vapour phase from the high temperature condensing stage along with the stream of volatiles from the vacuum distillation operation to the cold condensation stage obtaining a stream of non-condensable gases and a cold temperature distillate, letting the stream of non-condensable gases continue to a vacuum system, and recovering from the vacuum steam stripping section a stream of refined oil.

The present invention relates to a process for removing metal from metal-containing glyceride oil comprising the steps of: (i) contacting a glyceride oil, comprising chromium, manganese, iron, cobalt, nickel and/or copper in a total amount of from 10 mg/kg to 10,000 mg/kg, with a liquid comprising a basic quaternary ammonium salt to form a treated glyceride oil; wherein the basic quaternary ammonium salt comprises a basic anion selected from hydroxide, alkoxide, alkylcarbonate, hydrogen carbonate, carbonate, serinate, prolinate, histidinate, threoninate, valinate, asparaginate, taurinate and lysinate; and (ii) separating the treated glyceride oil from a salt comprising the quaternary ammonium cation, providing a treated glyceride oil containing a reduced amount of metals.

The present invention relates to a process for removing metal from metal-containing glyceride oil comprising the steps of: (i) contacting a glyceride oil, comprising chromium, manganese, iron, cobalt, nickel and/or copper in a total amount of from 10 mg/kg to 10,000 mg/kg, with a liquid comprising a basic quaternary ammonium salt to form a treated glyceride oil; wherein the basic quaternary ammonium salt comprises a basic anion selected from hydroxide, alkoxide, alkylcarbonate, hydrogen carbonate, carbonate, serinate, prolinate, histidinate, threoninate, valinate, asparaginate, taurinate and lysinate; and (ii) separating the treated glyceride oil from a salt comprising the quaternary ammonium cation, providing a treated glyceride oil containing a reduced amount of metals.

In a process for purifying fatty acid alkyl esters, particularly methyl and ethyl esters, by means of vacuum distillation in a distillation column, water or steam is introduced into the distillation column and, during distillation, brought into contact with the fatty acid alkyl esters in the gas phase. This results in a significant reduction in the sulphur content and in the acid number of the fatty acid alkyl ester.

In a process for purifying fatty acid alkyl esters, particularly methyl and ethyl esters, by means of vacuum distillation in a distillation column, water or steam is introduced into the distillation column and, during distillation, brought into contact with the fatty acid alkyl esters in the gas phase. This results in a significant reduction in the sulphur content and in the acid number of the fatty acid alkyl ester.

The present disclosure relates to methods and systems for injecting a gas (e.g., air) into a grain oil recovered from a grain process so as to remove an amount of one or more materials (e.g., moisture, unsaponifiables, insolubles, free fatty acids, and the like) from the grain oil.

The present disclosure relates to methods and systems for injecting a gas (e.g., air) into a grain oil recovered from a grain process so as to remove an amount of one or more materials (e.g., moisture, unsaponifiables, insolubles, free fatty acids, and the like) from the grain oil.

The present invention relates to a process for increasing the oxidative stability of short path evaporated oils, by adding to short-path evaporated treated oil at least one other oil. It further relates to a composition comprising short-path evaporated treated palm oil and, at least one other oil. Furthermore, it relates to the food products comprising these oils with improved oxidative stability.

Disclosed is a VE Enrichment System, comprising a falling film heat exchanger, a deodorization tower (deodorizer), a deodorizer transfer pump, a post-stripping deodorization tower (post-stripper), a high pressure steam heater and fatty acid collection unit. The falling film heat exchanger comprises of 2 shell heat exchange section of which the bottom section is connected to the deodorizer and the upper section is connected to the high pressure steam heater which is then connected to the post stripper; the post stripper bottom outlet is connected back to the falling film heat exchanger at it tube side. The post stripper top outlet (vapour outlet) is connected to the fatty acid collection unit. The upper shell section of the falling film heat exchanger and the high pressure steam heater forms a loop with the post stripper, while another loop is formed for the bottom of shell section of the falling film heat exchanger and the deodorizer and its transfer pump. Depending on operation needs, a vacuum ejector can be added. This VE enrichment system is used to produce more fatty acid distillate with higher VE content during the deodorization process of vegetable oil.

A hollow vessel operated under vacuum receives whole orange peel delivered by a conveyor. The peel is heated indirectly by steam. Oil and water present in the peel evaporates and is drawn off to be condensed, captured and separated. Separation is by decantation. Operation under vacuum lowers the boiling point of the oil. Steam condensate is collected for reuse. The exiting peel discharges from the vessel and is conveyed away for further processing.