CN203597320U - Production system of lycopene health care oil - Google Patents
Production system of lycopene health care oil Download PDFInfo
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- CN203597320U CN203597320U CN201320630640.1U CN201320630640U CN203597320U CN 203597320 U CN203597320 U CN 203597320U CN 201320630640 U CN201320630640 U CN 201320630640U CN 203597320 U CN203597320 U CN 203597320U
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Abstract
The utility model discloses a production system of lycopene health care oil and belongs to the field of production of edible oil and fat. The production system provided by the utility model comprises a raw oil storage tank, a lycopene extract storage tank, a nitrogen tank, a filling line, a primary mixer, a pre-heating device, a vibration mixing tank, a pressure stirring tank, a separation device and a cooling device, wherein an inlet of the primary mixer is connected with the lycopene extract storage tank and the raw oil storage tank respectively; an outlet of the primary mixer is connected with the vibration mixing tank; the raw oil storage tank is connected with the vibration mixing tank through the pre-heating device; the vibration mixing tank is connected with the pressure stirring tank; the pressure stirring tank is connected with the separation device; the separation device is connected with the filling line through the cooling device; the vibration mixing tank and the pressure stirring tank are respectively connected with the nitrogen tank. The production system provided by the utility model has the advantages of simple process, high production efficiency, security and reliability; furthermore, the loss amount of lycopene in a processing process is reduced to the minimum level by sufficiently considering the physical characteristics of the lycopene of easiness in oxidation, need of being kept in a dark place and poor thermal stability.
Description
Technical field
The utility model relates to a kind of production system of health-care oil, more particularly, relates to a kind of production system of the health-care oil that contains lycopene.
Background technology
Lycopene is one of natural that occurring in nature oxidation resistance is the strongest, and the speed of its cancellation free radical is 1000 times of VC, 100 times of VE, 2～3 times of β-carrotene.As everyone knows, free radical is the source of ten thousand diseases, is hidden maximum enemy in human body.
Scientists finds that the oxygen carrier that the free radical of infringement health is nearly all stronger with those activity is relevant, and active oxygen radical is actual to the infringement of human body is a kind of oxidizing process, reduce the infringement from free radical, will do from anti-oxidant; Lycopene is exactly the natural enemy of free radical, is the most fruitful antioxidant.The World Food Programme (FAO) and the World Health Organization (WHO) have listed lycopene in food additives register, and the lycopene that is described as " plant gold " is just receiving the concern of each side aspect anti-oxidant, in emerging status.
Because the otherness in diet structure and west, compatriots take in lycopene amount every day not as good as occidentals's 1/4th, and according to the investigation of United States Department of Agriculture and statistics, calendar year 2001, the U.S. takes in lycopene amount every day per capita at 10.9mg.As can be seen here, improve lycopene intake, be related to and improve the national general level of the health, the large problem of benefiting compatriots, it is not only an economic problems, is also a social concern, is worth everybody to pay close attention to.
Mid-term in 20th century, United States Medicine man reported first lycopene and the anticancer effect that is related to, by epidemiology survey and repeatedly zoopery, prove that lycopene has the effect of pre-anti-cancer, find so a kind of inverse relation, namely lycopene concentration is negative relation in the incidence of prostate cancer, cancer of the esophagus, cancer of pancreas, intestinal cancer, breast cancer, cervix cancer, cutaneum carcinoma, carcinoma of urinary bladder, and the lycopene cancer morbidity that content is high is in vivo low, and the incidence of disease is high on the contrary.And the morbidity cause of cancer is how many relevant with free radical, how to make compatriots every day can be by most convenient, the most easily, the most simply, do not forget the method for taking in lycopene and reach by improving meals exactly, lycopene health-care oil is exactly the key addressing this problem, it is as carrier with edible oil, complete lycopene extract and edible oil are merged, produce the health-care oil that is rich in lycopene.Compatriots can obtain lycopene by modes such as, cookings cold and dressed with sauce with lycopene health-care oil, its benefit is to eat " medicine " (i.e. edible lycopene capsules), also can obtain lycopene by meals, improve compatriots' lycopene intake, thereby reach the general level of the health that improves compatriots.
Find through retrieval: in the patent application of " about the lycopene health-care oil " in the past declared, someone mentioned extraction temperature is 30 ℃ and 80～105 ℃, does not all reach the molten point of lycopene.The utility model thinks, in the time that lycopene does not also reach molten some temperature, its meltage is very little, and it is very long to dissolve the used time.As shown in Figure 5, extraction temperature at lycopene is selected 30 ℃, when solid-liquid ratio is 1:3, measure the curve map of the extracted amount of soybean oil lixiviate lycopene under different time, wherein, abscissa represents extraction time (h), ordinate represents lycopene extracted amount (μ g/ml), as we know from the figure: in the time that extraction time reaches 15h, the extracted amount of lycopene just can reach peak value, and the maximum that so-called peak value is also just issued to the situation of 30 ℃, according to the physical characteristic of lycopene, when 30 ℃ (comprising 80～105 ℃), lycopene can not be extracted completely, also there is a large amount of lycopenes in tomato material the inside.
Summary of the invention
1. the technical problem that utility model will solve
The purpose of this utility model is to solve the lycopene health-care oil problem that number of dropouts is large, production efficiency is low of lycopene in process of production in prior art, a kind of production system of lycopene health-care oil is provided, adopt the technical solution of the utility model, not only technique is simple, production efficiency is high, safe and reliable, and fully taken into account lycopene oxidizable, keep in dark place, the physical characteristic of poor heat stability, make the number of dropouts of lycopene in process drop to floor level.
2. technical scheme
For achieving the above object, the technical scheme that the utility model provides is:
The production system of a kind of lycopene health-care oil of the present utility model, comprise feedstock oil storage tank, lycopene extract storage tank, nitrogen pot and canning line, also comprise just mixed device, preheating device, vibration blending tank, pressure agitator tank, separator and cooling device, the import of described first mixed device respectively with lycopene extract storage tank, feedstock oil storage tank is connected, the outlet of described first mixed device is connected with vibration blending tank, described feedstock oil storage tank is connected with vibration blending tank by preheating device, described vibration blending tank is connected with pressure agitator tank, described pressure agitator tank is connected with separator, described separator is connected with canning line by cooling device, described vibration blending tank is connected with nitrogen pot respectively with pressure agitator tank.
Further, described preheating device comprises high temperature heat conductive oil storage tank and preheater, and the high temperature heat conductive oil in described high temperature heat conductive oil storage tank is flowed through after preheater and is back in high temperature heat conductive oil storage tank, forms loop; Described cooling device comprises cooling water tank, cooler and filter, and the cooling water flow in described cooling water tank is back in cooling water tank after cooler, forms loop, and described filter is arranged at the water outlet of cooling water tank.
Further, on described high temperature heat conductive oil storage tank, preheater, vibration blending tank, pressure agitator tank and cooler, be provided with temperature controller, on described vibration blending tank and pressure agitator tank, be provided with pressure controller, the exit of described feedstock oil storage tank and lycopene extract storage tank is provided with flow quantity control instrument, on described first mixed device, preheater, vibration blending tank, pressure agitator tank and cooler, is provided with time controller.
Further, on described vibration blending tank, be provided with the rearrangeable switch for regulating its vibration frequency, on described vibration blending tank and pressure agitator tank, be provided with oxygen escape valve; Described separator is decanter.
The production system of a kind of lycopene health-care oil of the present utility model, comprise feedstock oil storage tank, nitrogen pot and canning line, also comprise cleaning device, dewater unit, freeze-drying apparatus, micron ultra shifter, just mixed device, preheating device, vibration blending tank, pressure agitator tank, separator and cooling device, described cleaning device, dewater unit, freeze-drying apparatus and micron ultra shifter set gradually, the import of described first mixed device respectively with micron ultra shifter, feedstock oil storage tank is connected, the outlet of described first mixed device is connected with vibration blending tank, described feedstock oil storage tank is connected with vibration blending tank by preheating device, described vibration blending tank is connected with pressure agitator tank, described pressure agitator tank is connected with separator, described separator is connected with canning line by cooling device, described vibration blending tank is connected with nitrogen pot respectively with pressure agitator tank.
Further, described freeze-drying apparatus comprises low temperature conduction oil storage tank and lyophilizer, and the low temperature conduction oil in described low temperature conduction oil storage tank is flowed through after lyophilizer and is back in low temperature conduction oil storage tank, forms loop; Described preheating device comprises high temperature heat conductive oil storage tank and preheater, and the high temperature heat conductive oil in described high temperature heat conductive oil storage tank is flowed through after preheater and is back in high temperature heat conductive oil storage tank, forms loop; Described cooling device comprises cooling water tank, cooler and filter, and the cooling water flow in described cooling water tank is back in cooling water tank after cooler, forms loop, and described filter is arranged at the water outlet of cooling water tank.
Further, on described high temperature heat conductive oil storage tank, low temperature conduction oil storage tank, preheater, vibration blending tank, pressure agitator tank and cooler, be provided with temperature controller, on described vibration blending tank and pressure agitator tank, be provided with pressure controller, described feedstock oil storage tank and the exit of micron ultra shifter are provided with flow quantity control instrument, on described first mixed device, preheater, vibration blending tank, pressure agitator tank and cooler, are provided with time controller.
Further, on described vibration blending tank, be provided with the rearrangeable switch for regulating its vibration frequency, on described vibration blending tank and pressure agitator tank, be provided with oxygen escape valve; Described separator is centrifuge.
3. beneficial effect
The technical scheme that adopts the utility model to provide, compared with existing known technology, has following remarkable result:
(1) due to the poor heat stability of lycopene, for avoiding that lycopene is heated for a long time and causes lycopene to run off, the production system of a kind of lycopene health-care oil of the present utility model, first a part of feedstock oil is carried out to preheating, another part carries out just mixed without the feedstock oil of preheating and tomato powder or lycopene extract, compound by the feedstock oil after preheating and after just mixing mixes again again, greatly shorten the time that lycopene is detained in high temperature, prevented the loss of lycopene;
(2) production system of a kind of lycopene health-care oil of the present utility model, realizes the anaerobic state of process by being filled with nitrogen, avoid lycopene oxidized;
(3) production system of a kind of lycopene health-care oil of the present utility model, the compound of feedstock oil, lycopene extract or feedstock oil, tomato powder is carried out to pressure vibration and pressure stirring, being conducive to the lycopene degree of depth incorporates in feedstock oil, feedstock oil and lycopene are merged more fully with even, shorten extraction time, enhance productivity;
(4) production system of a kind of lycopene health-care oil of the present utility model, carries out coolingly to the lycopene health-care oil obtaining, make lycopene depart from as early as possible hot environment, reduces lycopene Yin Gaowen and the destruction that produces;
(5) production system of a kind of lycopene health-care oil of the present utility model, by high temperature heat conductive oil, feedstock oil is carried out to preheating, feedstock oil is stirred simultaneously, make it reach quickly and evenly the temperature of setting, pre-heat effect is better, preheat temperature is to set according to the molten point of lycopene, and feedstock oil and lycopene are merged more fully;
(6) production system of a kind of lycopene health-care oil of the present utility model, while adopting tomato skin or tomato material as raw materials for production, adopt deep cooling freeze-drying to be dried tomato skin or tomato material, there will not be the problem that lycopene is run off because of hyperthermia drying;
(7) production system of a kind of lycopene health-care oil of the present utility model, on high temperature heat conductive oil storage tank, low temperature conduction oil storage tank, preheater, vibration blending tank, pressure agitator tank and cooler, be provided with temperature controller, effectively control the variations in temperature of each process, accelerate on the one hand the fusion of feedstock oil and lycopene, prevent on the one hand the loss of lycopene; On vibration blending tank and pressure agitator tank, be provided with pressure controller, the pressure of being convenient to vibrate in blending tank and pressure agitator tank regulates; The exit of feedstock oil storage tank, lycopene extract storage tank and micron ultra shifter is provided with flow quantity control instrument, and the proportioning of lycopene and feedstock oil can be accurately set, and produces the lycopene health-care oil of different size; Just on mixed device, preheater, vibration blending tank, pressure agitator tank and cooler, be provided with time controller, be conducive to control the time of each process, on the basis that feedstock oil and lycopene fully merge, enhance productivity guaranteeing;
(8) production system of a kind of lycopene health-care oil of the present utility model, is provided with the rearrangeable switch for regulating its vibration frequency on its vibration blending tank, is convenient to vibrate frequency adjustment and control in blending tank; On vibration blending tank and pressure agitator tank, be provided with oxygen escape valve, make nitrogen be full of vibration blending tank and pressure agitator tank completely, oxygen is thoroughly discharged, reach anaerobic state, make to vibrate in blending tank and pressure agitator tank simultaneously and there is certain pressure.
Accompanying drawing explanation
Fig. 1 is the production system schematic diagram of a kind of lycopene health-care oil of embodiment 1;
Fig. 2 is the control system schematic diagram of the lycopene health-care oil production system in embodiment 1;
Fig. 3 is the production system schematic diagram of a kind of lycopene health-care oil of embodiment 2;
Fig. 4 is the control system schematic diagram of the lycopene health-care oil production system in embodiment 2;
Fig. 5 is in the time that extraction temperature is 30 ℃, and lycopene extracted amount is with the curve map of extraction time variation.
Label declaration in schematic diagram:
1, high temperature heat conductive oil storage tank; 2, lycopene extract storage tank; 3, just mix device; 4, preheater; 5, feedstock oil storage tank; 6, vibration blending tank; 7, nitrogen pot; 8, pressure agitator tank; 9, separator; 10, cooling water tank; 11, filter; 12, cooler; 13, canning line; 14, rearrangeable switch; 15, cleaning device; 16, dewater unit; 17, lyophilizer; 18, micron ultra shifter; 19, low temperature conduction oil storage tank.
The specific embodiment
For further understanding content of the present utility model, in conjunction with the accompanying drawings and embodiments the utility model is described in detail.
In the production process of existing lycopene health-care oil, the molten point of not noticing lycopene is 172 ℃～173 ℃ (in the situation that of 760mmHg), therefore, content of lycopene in the lycopene health-care oil of producing generally can seldom, be difficult to meet the picked-up requirement of people to lycopene.
In conjunction with Fig. 1, the production system of a kind of lycopene health-care oil of the present embodiment, the vegetable oil of employing refining and lycopene extract are as raw materials for production, contained lycopene is generally 5%～10% in lycopene extract, specifically comprises feedstock oil storage tank 5, lycopene extract storage tank 2, nitrogen pot 7, canning line 13, just mixed device 3, preheating device, vibration blending tank 6, pressure agitator tank 8, separator 9 and cooling device.The import of just mixed device 3 is connected with lycopene extract storage tank 2, feedstock oil storage tank 5 respectively, wherein, lycopene extract storage tank 2 is connected with just mixed device 3 by meter, feedstock oil storage tank 5 is connected with just mixed device 3 by flowmeter, for controlling the mixed proportion of feedstock oil and lycopene extract; The outlet of just mixed device 3 is connected with vibration blending tank 6, feedstock oil storage tank 5 is connected with vibration blending tank 6 by preheating device, compound for the feedstock oil after preheating and after just mixing mixes again, and carry out pressure vibration, greatly shorten the holdup time of lycopene in high temperature, prevented the loss of lycopene; Vibration blending tank 6 is connected with pressure agitator tank 8, stirs under acting in conjunction at pressure vibration and pressure, feedstock oil and lycopene is merged more fully and evenly, shorten extraction time, enhances productivity; On vibration blending tank 6 in the present embodiment, be also provided with the rearrangeable switch 14 for regulating its vibration frequency, be convenient to vibrate frequency adjustment and control in blending tank 6; Pressure agitator tank 8 is connected with separator 9, and for insoluble matter is separated with lycopene health-care oil, this separator 9 is decanter; Separator 9 is connected with canning line 13 by cooling device, and cooling object is to make lycopene depart from as early as possible hot environment, reduces lycopene Yin Gaowen and the destruction that produces; Vibration blending tank 6 is connected with nitrogen pot 7 respectively with pressure agitator tank 8, realizes the malleation anaerobic state of process by being filled with nitrogen, avoids lycopene oxidized, is conducive to the extraction of lycopene.In order to make nitrogen be full of vibration blending tank 6 and pressure agitator tank 8 completely, on vibration blending tank 6 and pressure agitator tank 8, be respectively arranged with oxygen escape valve, the principle of this oxygen escape valve is similar to the air bleeding valve of household pressure-cooker, in the time that nitrogen is filled with vibration blending tank 6 and pressure agitator tank 8, nitrogen is together with oxygen mix, when nitrogen constantly enters, nitrogen and oxygen proportion in vibration blending tank 6 and pressure agitator tank 8 constantly change, and constantly discharge by oxygen escape valve, finally reach anaerobic state, make to vibrate in blending tank 6 and pressure agitator tank 8 simultaneously and there is certain pressure.
Above-mentioned preheating device comprises high temperature heat conductive oil storage tank 1 and preheater 4, high temperature heat conductive oil storage tank 1 is connected with preheater 4, high temperature heat conductive oil in high temperature heat conductive oil storage tank 1 is flowed through after preheater 4 and is back in high temperature heat conductive oil storage tank 1, form closed circuit, by high temperature heat conductive oil, feedstock oil is carried out to preheating, feedstock oil is stirred simultaneously, make it reach quickly and evenly the temperature value of setting, pre-heat effect is better; Cooling device comprises cooling water tank 10, cooler 12 and filter 11, cooling water tank 10 is connected with cooler 12, cooling water flow in cooling water tank 10 is back in cooling water tank 10 after cooler 12, form closed circuit, filter 11 is arranged at the water outlet of cooling water tank 10, realizes the circulating cooling to lycopene health-care oil.
As shown in Figure 2, the production system of a kind of lycopene health-care oil of the present embodiment, also comprise control system, this control system comprises the control to temperature, pressure, flow and time, specifically on high temperature heat conductive oil storage tank 1, preheater 4, vibration blending tank 6, pressure agitator tank 8 and cooler 12, be provided with temperature controller, effectively control the variations in temperature of each process, accelerate on the one hand the fusion of feedstock oil and lycopene, prevent on the one hand the loss of lycopene; On vibration blending tank 6 and pressure agitator tank 8, pressure controller is set, the pressure of being convenient to vibrate in blending tank 6 and pressure agitator tank 8 regulates; Exit at feedstock oil storage tank 5 and lycopene extract storage tank 2 arranges flow quantity control instrument, and the proportioning of lycopene and vegetable oil can be accurately set, and produces the lycopene health-care oil of different size; Setup times controller on just mixed device 3, preheater 4, vibration blending tank 6, pressure agitator tank 8 and cooler 12, is conducive to control time of each process, on the basis that feedstock oil and lycopene fully merge, enhances productivity guaranteeing.
In conjunction with Fig. 3, the production system of a kind of lycopene health-care oil of the present embodiment, adopt the vegetable oil of refining and tomato skin or tomato material as raw materials for production, specifically comprise feedstock oil storage tank 5, nitrogen pot 7, canning line 13, cleaning device 15, dewater unit 16, freeze-drying apparatus, micron ultra shifter 18, just mixed device 3, preheating device, vibration blending tank 6, pressure agitator tank 8, separator 9 and cooling device.Cleaning device 15, dewater unit 16, freeze-drying apparatus and micron ultra shifter 18 set gradually, and are respectively used to tomato skin or tomato material clean, dewater, are dried and pulverize.The import of just mixed device 3 is connected with micron ultra shifter 18, feedstock oil storage tank 5 respectively, the outlet of just mixed device 3 is connected with vibration blending tank 6, feedstock oil storage tank 5 is connected with vibration blending tank 6 by preheating device, compound for the feedstock oil after preheating and after just mixing mixes again, and carry out pressure vibration, greatly shorten the holdup time of lycopene in high temperature, prevented the loss of lycopene; Vibration blending tank 6 is connected with pressure agitator tank 8, stirs under acting in conjunction at pressure vibration and pressure, feedstock oil and lycopene is merged more fully and evenly, shorten extraction time, enhances productivity; On vibration blending tank 6 in the present embodiment, be also provided with the rearrangeable switch 14 for regulating its vibration frequency, be convenient to vibrate frequency adjustment and control in blending tank 6; Pressure agitator tank 8 is connected with separator 9, and for insoluble matter is separated with lycopene health-care oil, this separator 9 is centrifuge; Separator 9 is connected with canning line 13 by cooling device, and cooling object is to make lycopene depart from as early as possible hot environment, reduces lycopene Yin Gaowen and the destruction that produces; Vibration blending tank 6 is connected with nitrogen pot 7 respectively with pressure agitator tank 8, realizes the malleation anaerobic state of process by being filled with nitrogen, avoids lycopene oxidized, is conducive to the extraction of lycopene.In order to make nitrogen be full of vibration blending tank 6 and pressure agitator tank 8 completely, on vibration blending tank 6 and pressure agitator tank 8, be respectively arranged with oxygen escape valve, the principle of this oxygen escape valve is similar to the air bleeding valve of household pressure-cooker, in the time that nitrogen is filled with vibration blending tank 6 and pressure agitator tank 8, nitrogen is together with oxygen mix, when nitrogen constantly enters, nitrogen and oxygen proportion in vibration blending tank 6 and pressure agitator tank 8 constantly change, and constantly discharge by oxygen escape valve, finally reach anaerobic state, make to vibrate in blending tank 6 and pressure agitator tank 8 simultaneously and there is certain pressure.
Above-mentioned freeze-drying apparatus comprises low temperature conduction oil storage tank 19 and lyophilizer 17, and the low temperature conduction oil in low temperature conduction oil storage tank 19 is flowed through after lyophilizer 17 and is back in low temperature conduction oil storage tank 19, forms circulation; Preheating device comprises high temperature heat conductive oil storage tank 1 and preheater 4, high temperature heat conductive oil storage tank 1 is connected with preheater 4, high temperature heat conductive oil in high temperature heat conductive oil storage tank 1 is flowed through after preheater 4 and is back in high temperature heat conductive oil storage tank 1, form closed circuit, by high temperature heat conductive oil, feedstock oil is carried out to preheating, feedstock oil is stirred simultaneously, make it reach quickly and evenly the temperature value of setting, pre-heat effect is better; Cooling device comprises cooling water tank 10, cooler 12 and filter 11, cooling water tank 10 is connected with cooler 12, cooling water flow in cooling water tank 10 is back in cooling water tank 10 after cooler 12, form closed circuit, filter 11 is arranged at the water outlet of cooling water tank 10, realizes the circulating cooling to lycopene health-care oil.
As shown in Figure 4, the production system of a kind of lycopene health-care oil of the present embodiment, also comprise control system, this control system comprises the control to temperature, pressure, flow and time, specifically on high temperature heat conductive oil storage tank 1, low temperature conduction oil storage tank 19, preheater 4, vibration blending tank 6, pressure agitator tank 8 and cooler 12, be provided with temperature controller, effectively control the variations in temperature of each process, accelerate on the one hand the fusion of feedstock oil and lycopene, prevent on the one hand the loss of lycopene; On vibration blending tank 6 and pressure agitator tank 8, be provided with pressure controller, the pressure of being convenient to vibrate in blending tank 6 and pressure agitator tank 8 regulates; Exit at feedstock oil storage tank 5 and micron ultra shifter 18 is provided with flow quantity control instrument, and the proportioning of lycopene and vegetable oil can be accurately set, and produces the lycopene health-care oil of different size; Being just provided with time controller on mixed device 3, preheater 4, vibration blending tank 6, pressure agitator tank 8 and cooler 12, be conducive to control the time of each process, on the basis that feedstock oil and lycopene fully merge, enhance productivity guaranteeing.
The production system of a kind of lycopene health-care oil of the present utility model, not only technique is simple, production efficiency is high, safe and reliable, and fully taken into account lycopene oxidizable, keep in dark place, the physical characteristic of poor heat stability, make the number of dropouts of lycopene in process drop to floor level.
Below schematically the utility model and embodiment thereof are described, this description does not have restricted, and shown in accompanying drawing is also one of embodiment of the present utility model, and actual structure is not limited to this.So, if those of ordinary skill in the art is enlightened by it, in the situation that not departing from the utility model creation aim, without the creationary frame mode similar to this technical scheme and the embodiment of designing, all should belong to protection domain of the present utility model.
Claims (8)
1. the production system of a lycopene health-care oil, comprise feedstock oil storage tank (5), lycopene extract storage tank (2), nitrogen pot (7) and canning line (13), it is characterized in that: also comprise just mixed device (3), preheating device, vibration blending tank (6), pressure agitator tank (8), separator (9) and cooling device, the import of described first mixed device (3) respectively with lycopene extract storage tank (2), feedstock oil storage tank (5) is connected, the outlet of described first mixed device (3) is connected with vibration blending tank (6), described feedstock oil storage tank (5) is connected with vibration blending tank (6) by preheating device, described vibration blending tank (6) is connected with pressure agitator tank (8), described pressure agitator tank (8) is connected with separator (9), described separator (9) is connected with canning line (13) by cooling device, described vibration blending tank (6) is connected with nitrogen pot (7) respectively with pressure agitator tank (8).
2. the production system of a kind of lycopene health-care oil according to claim 1, it is characterized in that: described preheating device comprises high temperature heat conductive oil storage tank (1) and preheater (4), high temperature heat conductive oil in described high temperature heat conductive oil storage tank (1) is flowed through after preheater (4) and is back in high temperature heat conductive oil storage tank (1), forms loop; Described cooling device comprises cooling water tank (10), cooler (12) and filter (11), cooling water flow in described cooling water tank (10) is back in cooling water tank (10) after cooler (12), form loop, described filter (11) is arranged at the water outlet of cooling water tank (10).
3. the production system of a kind of lycopene health-care oil according to claim 2, it is characterized in that: described high temperature heat conductive oil storage tank (1), preheater (4), vibration blending tank (6), on pressure agitator tank (8) and cooler (12), be provided with temperature controller, on described vibration blending tank (6) and pressure agitator tank (8), be provided with pressure controller, described feedstock oil storage tank (5) and the exit of lycopene extract storage tank (2) are provided with flow quantity control instrument, described first mixed device (3), preheater (4), vibration blending tank (6), on pressure agitator tank (8) and cooler (12), be provided with time controller.
4. the production system of a kind of lycopene health-care oil according to claim 3, it is characterized in that: on described vibration blending tank (6), be provided with the rearrangeable switch (14) for regulating its vibration frequency, on described vibration blending tank (6) and pressure agitator tank (8), be provided with oxygen escape valve; Described separator (9) is decanter.
5. a production system for lycopene health-care oil, comprises feedstock oil storage tank (5), nitrogen pot (7) and canning line (13), is characterized in that: also comprise cleaning device (15), dewater unit (16), freeze-drying apparatus, micron ultra shifter (18), just mixed device (3), preheating device, vibration blending tank (6), pressure agitator tank (8), separator (9) and cooling device, described cleaning device (15), dewater unit (16), freeze-drying apparatus and micron ultra shifter (18) set gradually, the import of described first mixed device (3) respectively with micron ultra shifter (18), feedstock oil storage tank (5) is connected, the outlet of described first mixed device (3) is connected with vibration blending tank (6), described feedstock oil storage tank (5) is connected with vibration blending tank (6) by preheating device, described vibration blending tank (6) is connected with pressure agitator tank (8), described pressure agitator tank (8) is connected with separator (9), described separator (9) is connected with canning line (13) by cooling device, and described vibration blending tank (6) is connected with nitrogen pot (7) respectively with pressure agitator tank (8).
6. the production system of a kind of lycopene health-care oil according to claim 5, it is characterized in that: described freeze-drying apparatus comprises low temperature conduction oil storage tank (19) and lyophilizer (17), low temperature conduction oil in described low temperature conduction oil storage tank (19) is flowed through after lyophilizer (17) and is back in low temperature conduction oil storage tank (19), forms loop; Described preheating device comprises high temperature heat conductive oil storage tank (1) and preheater (4), and the high temperature heat conductive oil in described high temperature heat conductive oil storage tank (1) is flowed through after preheater (4) and is back in high temperature heat conductive oil storage tank (1), forms loop; Described cooling device comprises cooling water tank (10), cooler (12) and filter (11), cooling water flow in described cooling water tank (10) is back in cooling water tank (10) after cooler (12), form loop, described filter (11) is arranged at the water outlet of cooling water tank (10).
7. the production system of a kind of lycopene health-care oil according to claim 6, it is characterized in that: described high temperature heat conductive oil storage tank (1), low temperature conduction oil storage tank (19), preheater (4), vibration blending tank (6), on pressure agitator tank (8) and cooler (12), be provided with temperature controller, on described vibration blending tank (6) and pressure agitator tank (8), be provided with pressure controller, described feedstock oil storage tank (5) and the exit of micron ultra shifter (18) are provided with flow quantity control instrument, described first mixed device (3), preheater (4), vibration blending tank (6), on pressure agitator tank (8) and cooler (12), be provided with time controller.
8. the production system of a kind of lycopene health-care oil according to claim 7, it is characterized in that: on described vibration blending tank (6), be provided with the rearrangeable switch (14) for regulating its vibration frequency, on described vibration blending tank (6) and pressure agitator tank (8), be provided with oxygen escape valve; Described separator (9) is centrifuge.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103518866A (en) * | 2013-10-14 | 2014-01-22 | 陈联伟 | Production method and production system for health-protection lycopene oil |
-
2013
- 2013-10-14 CN CN201320630640.1U patent/CN203597320U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103518866A (en) * | 2013-10-14 | 2014-01-22 | 陈联伟 | Production method and production system for health-protection lycopene oil |
| CN103518866B (en) * | 2013-10-14 | 2015-04-08 | 陈联伟 | Production method and production system for health-protection lycopene oil |
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