Summary of the invention
The objective of the invention is to develop a kind of usefulness 1,3 optionally fixed lipase catalyzed edible oil and fat and DHA (being called for short DHA) grease carry out ester exchange, the edible vegetable oil and fat of the high added value of DHA (being called for short DHA) is rich in production, makes the production method of the edible oil and fat oxidation stability enhancing of adding DHA (being called for short DHA).
The present invention utilizes enzyme process to change composition or aliphatic acid a kind of triglycerides that the position prepares on glycerol backbone of triglycerides, changes the oxidation stability that the position distribution situation of DHA in triglycerides improves edible oil and fat by the Structured Lipids technology.
The method of the edible oil and fat that contain DHA is produced in enzyme process ester exchange of the present invention, and its step is as follows:
(1) in closed container, with the DHA grease in hybrid reaction after the ratio of required DHA content put in the edible oil and fat, enzyme-added by the 4-7% of total weight of oil percentage, DHA content is 1-50% in the DHA grease of described interpolation;
(2) closed container vacuumizes, and vacuum is-0.08~-0.1MPa, be warming up to 60-75 ℃, stir, stir speed (S.S.) is 50-300 rev/min, about time 3-6 hour;
(3) reaction is complete, fills nitrogen in closed container, filters, and obtains the edible oil and fat after the ester exchange, obtains product oil or with traditional alkali refining method removal free fatty, deodorization obtains product oil behind molecular clock.
Edible oil and fat include but not limited to palm oil, soybean salad oil, sunflower oil, tea oil, olive oil, siritch, peanut oil.
The advantage that the method for the edible oil and fat that contain DHA is produced in enzyme process ester exchange of the present invention is: with 1,3 optionally fixed lipase catalyzed edible oil and fat and DHA (being called for short DHA) grease carry out ester exchange, the edible vegetable oil and fat of the high added value of DHA (being called for short DHA) is rich in production, the edible oil and fat that are rich in DHA (being called for short DHA) are sealed in the proper packing container, placed 18 to 24 months in room temperature behind the vacuum nitrogen filling, peroxide value still remains on≤10meq/kg, and its oxidation stability significantly strengthens.
The specific embodiment
Embodiment one:
The method of the edible oil and fat that contain DHA is produced in a kind of enzyme process ester exchange, and its step is as follows:
(1) in closed container, after getting 0.4kgDHA grease and 100kg sunflower oil and mixing, add the 4kg enzyme, DHA content is 1% in the DHA grease of described interpolation;
(2) closed container vacuumizes, and vacuum is-0.08MPa, is warming up to 60 ℃, stirs, and stir speed (S.S.) is 50 rev/mins, 3 hours time;
(3) reaction is complete, fills nitrogen in closed container, is cooled to 50 ℃, filters, and obtains the sunflower oil after the ester exchange, obtains DHA content and be 0.004% product oil 96kg behind molecular clock.
Embodiment two:
The method of the edible oil and fat that contain DHA is produced in a kind of enzyme process ester exchange, and its step is as follows:
(1) in closed container, get 0.002kgDHA grease and 100kg mixed with olive oil after, add the 7kg enzyme, DHA content is 50% in the DHA grease of described interpolation;
(2) closed container vacuumizes, and vacuum is-0.1MPa, is warming up to 75 ℃, stirs, and stir speed (S.S.) is 300 rev/mins, 6 hours time;
(3) reaction is complete, fills nitrogen in closed container, is cooled to 60 ℃, filters, and obtains the palm oil after the ester exchange, removes free fatty behind alkali refining, and it is 0.001% product oil 93kg that deodorization obtains DHA content.
Embodiment three:
The method of the edible oil and fat that contain DHA is produced in a kind of enzyme process ester exchange, and its step is as follows:
(1) in closed container, after getting 0.008kgDHA grease and 100kg tea oil and mixing, add the 5.5kg enzyme, DHA content is 27% in the DHA grease of described interpolation;
(2) closed container vacuumizes, and vacuum is-0.09MPa, is warming up to 67 ℃, stirs, and stir speed (S.S.) is 175 rev/mins, 4.5 hours time;
(3) reaction is complete, fills nitrogen in closed container, is cooled to 55 ℃, filters, and obtains the tea oil after the ester exchange, obtains DHA content and be 0.002% product oil 94.5kg behind molecular clock.
Embodiment four:
The method of the edible oil and fat that contain DHA is produced in a kind of enzyme process ester exchange, and its step is as follows:
(1) 100kgDHA grease and 25kg palm oil are dropped in the closed container, add the 5kg enzyme, DHA content is 20% in the DHA grease of described interpolation;
(2) closed container vacuumizes, and vacuum is-0.08MPa, is warming up to 60 ℃, stirs, and stir speed (S.S.) is 50 rev/mins, 3 hours time;
(3) reaction is complete, fills nitrogen in closed container, is cooled to 50 ℃, filters, and obtains the DHA grease after the ester exchange, removes free fatty behind molecular clock, obtains DHA content and be 16% finished product DHA grease 121kg.
Embodiment five
The method of the edible oil and fat that contain DHA is produced in a kind of enzyme process ester exchange, and its step is as follows:
(1) 140kg DHA grease and 20kg olive oil are dropped in the closed container, add the 11.2kg enzyme, DHA content is 50% in the DHA grease of described interpolation;
(2) closed container vacuumizes, and vacuum is-0.1MPa, is warming up to 75 ℃, stirs, and stir speed (S.S.) is 300 rev/mins, 6 hours time;
(3) reaction is complete, fills nitrogen in closed container, is cooled to 60 ℃, filters, and obtains the DHA grease after the ester exchange, and with traditional alkali refining method removal free fatty, it is 43.75% finished product grease 152kg that deodorization obtains DHA content.
Embodiment six:
The method of the edible oil and fat that contain DHA is produced in a kind of enzyme process ester exchange, and its step is as follows:
(1) 110kg DHA grease and 20kg tea oil are dropped in the closed container, add the 7.15kg enzyme, DHA content is 35% in the DHA grease of described interpolation;
(2) closed container vacuumizes, and vacuum is-0.09MPa, is warming up to 67 ℃, stirs, and stir speed (S.S.) is 175 rev/mins, 4.5 hours time;
(3) reaction is complete, fills nitrogen in closed container, is cooled to 55 ℃, filters, and obtains the DHA grease after the ester exchange, removes free fatty behind molecular clock, and obtaining DHA content is 29.62% finished product grease 125kg.
In addition to the implementation, the present invention can form a plurality of embodiment, does not give unnecessary details one by one at this.