Ginseng-shaped turnip germ oil production and manufacturing device and technological method thereof

Abstract

The invention discloses a ginseng-shaped turnip germ oil production and manufacturing device and a technological method thereof, belongs to the technical field of edible vegetable oil production equipment and manufacturing technological methods, and solves the problems that turnip kernel germs obtained after a shelling procedure of an existing ginseng-shaped turnip germ oil production and manufacturing device and technological method are relatively high in skin content; and the refining of the crude oil is easy to cause the burning of the oil and the quality of the finished oil is damaged. An adopted programmable industrial personal computer is respectively connected with and controls an impurity-removing stone-removing screening unit, a turnip seed germ extracting unit, a turnip germ frying and steaming unit, a squeezing and oil filtering unit, a crude oil refining unit and a product inspecting and packaging unit through electric leads; the production process comprises the following steps: screening raw materials for stone removal and impurity removal in the first procedure, extracting the turnip germs, frying and steaming the turnip germs, squeezing oil and filtering oil, refining crude oil, and inspecting and packaging the product in the sixth procedure, and the production device is novel and practical in structure, reasonable and feasible in process method and suitable for industrial production and manufacturing of the ginseng-shaped turnip and other turnip germ oil and the like.

Description

Technical Field

[0001] The invention belongs to the technical field of edible vegetable oil production equipment and manufacturing process methods, and relates to a production and manufacturing device for ginseng-shaped turnip germ oil and a process method thereof. Background Art

[0002] Ginseng-shaped turnip (Brassicarapa L.) is a plant of the genus Brassica in the family Cruciferae. It is cone-shaped like ginseng and is a plant used for both medicine and food. Turnip seed oil has extremely valuable therapeutic effects and very rich medicinal value. With the continuous development and technological progress of the edible vegetable oil industry, the technical requirements for edible vegetable oil production equipment and manufacturing process methods also need to be continuously improved, especially for the rich ginseng-shaped turnip industry. The research and development and promotion of ginseng-shaped turnip oil product production equipment and manufacturing process methods have broad development prospects. In the known technology, the existing edible vegetable oil production equipment and manufacturing process methods are mainly small-particle plant seed production equipment and manufacturing process methods such as rapeseed oil, safflower seed oil, salacia oil, coriander seed oil and other edible vegetable oil production equipment and manufacturing process methods mainly adopt seed kernel cleaning, peeling, cold pressing, extrusion, leaching oil production, followed by hydration, deacidification, drying, decolorization and other steps of the crude oil. However, due to the uniqueness of the hard foreskin of the ginseng-shaped turnip seed shell, the actual application of the existing small-particle plant seed oil production device and its process method is limited. For example, Chinese Patent Publication No. CN1498952A discloses a technical solution of "rapeseed peeling, cold pressing, extrusion puffing, leaching oil production method", which is to clean the rapeseed raw material, dry it, and then The raw material after the drying treatment is subjected to a cooling treatment, and the raw material after the cooling treatment is subjected to a peeling treatment. The rapeseed kernel is subjected to a flaking treatment and then a cold pressing treatment, and cold pressed crude oil and cold pressed cake are obtained through the cold pressing treatment, and the cold pressed crude oil is processed into cold pressed rapeseed oil after precipitation and fine filtration; the cold pressed cake is subjected to a conditioning treatment, and the conditioned cold pressed cake is fed into a high-oil content oil extrusion puffing machine for extrusion puffing treatment, and extruded crude oil and puffed pellets are directly obtained through the extrusion puffing treatment, and the extruded crude oil is subjected to a hydration degumming treatment to obtain extruded rapeseed oil; the puffed pellets are subjected to a leaching treatment, and leached crude oil and dehulled rapeseed meal are obtained through the leaching treatment, and the leached crude oil is refined to obtain finished rapeseed oil.However, it is limited by its process oil production method, which involves peeling the cooled raw materials, extruding the crude oil and then degumming it through hydration, etc., and mainly uses a single peeling machine for peeling, as well as subsequent separation technology and processes, but lacks specific processing technical measures. It can be inferred that if this solution is applied to the production and manufacturing process of ginseng-shaped turnip germ oil, the turnip seed kernel germ has a higher skin content after the shelling process. Since some undesirable components in turnip seeds are mainly contained in the husk, too high a skin content in the turnip seed kernel germ will reduce the quality of the turnip seed kernel germ oil and oil cake formed after oil production, and will also make the utilization rate of turnip seed oil cake low, including a direct impact on the subsequent livestock and poultry The amount of application in feed has greatly reduced the comprehensive utilization value of ginseng-shaped turnip seeds; the hydration degumming and refining of crude oil also has the following problems: first, during the hydration and deacidification process, the surface temperature of the electric heating tube in the hydration tank is too high, and it is in direct contact with the oil, which easily causes the oil to burn, and the quality of the finished oil is damaged; second, during the dehydration operation, due to the need to ensure the complete volatilization of the water in the oil, a higher temperature is set in the dehydration tank. Excessive temperature will cause oil oxidation, increase the peroxide value, and deepen the color of the oil, thereby damaging the quality of the finished oil; at the same time, the existing small-particle plant seed oil-making device and its process method cannot be used for the industrial production of ginseng-shaped turnip germ oil.

[0003] In view of this, in order to adapt to the development and technological progress of small-particle plant seed oil and oil cake production equipment and process methods, it is necessary to further improve and develop a new type of ginseng-shaped turnip germ oil production equipment and process methods. Summary of the invention

[0004] In order to overcome the shortcomings of the prior art, solve the problem that the turnip kernel germ after the shelling process in the existing ginseng-shaped turnip germ oil production and manufacturing device and its process method is high in skin content, and the crude oil refining easily causes the scorch of the oil, which damages the quality of the finished oil. The purpose of the present invention is to provide a production and manufacturing device with a novel and practical structure, a reasonable and feasible process method, a low skin content in the turnip kernel germ after the shelling process, a good dehydration, decolorization and degumming effect in the subsequent refining and refining of the crude oil, which can effectively avoid oil oxidation, ensure that the quality of the finished oil is not damaged, and maintain the performance of high-quality original juice finished oil, which is suitable for the industrial production of ginseng-shaped turnip germ oil. A new type of ginseng-shaped turnip germ oil production and manufacturing device and its process method.

[0005] The technical solution adopted by the present invention to solve the above problems is:

[0006] A ginseng-shaped turnip germ oil production and manufacturing device comprises: an impurity-removing and stone-removing screening unit, a turnip seed and germ extraction unit, a turnip germ frying and steaming unit, an oil pressing and filtering unit, a crude oil refining and refining unit, a product inspection and packaging unit, and a programmable microcomputer industrial control computer. The programmable industrial control computer is respectively connected and controlled by electric wires to the impurity-removing and stone-removing screening unit, the turnip seed and germ extraction unit, the turnip germ frying and steaming unit, the oil pressing and filtering unit, the crude oil refining and refining unit, and the product inspection and packaging unit. The impurity-removing and stone-removing screening unit is connected to the turnip seed and germ extraction unit at the rear, the turnip seed and germ extraction unit is connected to the turnip germ frying and steaming unit at the rear, and then connected to the oil pressing and filtering unit, and the oil pressing and filtering unit is connected to the crude oil refining and refining unit at the rear, and then connected to the product inspection and packaging unit; specifically:

[0007] (1) The impurity and stone removal screening unit A comprises a raw material ginseng-shaped turnip seed storage tank, a primary screening feeder, a first material elevator, and a vibrating screening machine. The conical bottom of the raw material ginseng-shaped turnip seed storage tank is equipped with a discharge control valve, a discharge conveying pipe connected to the primary screening feeder, and a discharge nozzle pipe of the primary screening feeder is connected to the vibrating screening machine by the first material elevator connected thereto, and the rear of the vibrating screening machine is connected to a turnip seed germ extraction unit;

[0008] (2) The turnip seed and germ extraction unit comprises a second material elevator, a high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine, a wall-breaking vibrating rotary screen, and a turnip germ collection and feeding bin. The feed receiving bucket of the second material elevator is connected to the vibrating screening machine, and the discharge pipe is connected to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine. The vibrating screening machine is also equipped with a dust removal and induced draft fan. The rear of the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine is connected to the wall-breaking vibrating rotary screen, and the rear of the wall-breaking vibrating rotary screen is connected to the turnip germ collection and feeding bin. The rear of the turnip germ collection and feeding bin is connected to the turnip germ frying and steaming unit;

[0009] ⑶, the turnip germ frying and steaming unit comprises a third material hoist and a drum-type electromagnetic frying and steaming pot, the feed receiving bucket of the third material hoist is connected to the turnip germ collection and feeding bin, the discharge interface pipe is connected to the drum-type electromagnetic frying and steaming pot, and the discharge port pipe of the drum-type electromagnetic frying and steaming pot is connected to the oil pressing and filtering unit;

[0010] (4) The oil pressing and filtering unit comprises a fourth material hoist, a screw oil press, a closed primary filter oil tank, and a double-cylinder air pressure filter. The feed receiving bucket of the fourth material hoist is connected to a drum-type electromagnetic frying steamer, and the discharge interface pipe is connected to the screw oil press. The squeezed oil outlet connecting pipe of the screw oil press is connected to the closed primary filter oil tank, and the squeezed oil cake discharge hopper is connected to the oil cake crushing machine. The output oil pipe of the closed primary filter oil tank is connected to the first oil delivery pump connected to the double-cylinder air pressure filter, and the filtered crude oil delivery pipe of the double-cylinder air pressure filter is connected to the turnip germ crude oil refining unit;

[0011] (5) The refining unit of the crude oil of turnip germ comprises a refined oil tank frame, a hydrated refined oil tank, a negative pressure dehydration and degumming refined oil tank, a secondary oil filter, a filtered crude oil delivery pump, and a hydration liquid storage tank. The hydrated refined oil tank is one or 2-3 hydrated refined oil tanks connected in parallel by an oil pipeline. The hydrated refined oil tank, the negative pressure dehydration and degumming refined oil tank, and the secondary refined oil filter are installed in parallel on the refined oil tank frame. The oil inlet pipe of the hydrated refined oil tank is connected to the oil inlet pipe installed on the refined oil tank. The bottom bracket of the refined oil tank frame is provided with an output oil pipe of the filtered crude oil delivery pump, and the input oil pipe of the filtered crude oil delivery pump is connected to the filtered crude oil delivery pipe of the double-cylinder air pressure filter. A hydrated liquid agent storage tank is installed on the upper part of the hydrated refined oil tank, and a metering control valve is installed on the infusion pipe of the hydrated liquid agent storage tank. A spray head installed on the top of the inner cavity of the hydrated refined oil tank is installed on the end of the infusion pipe. The tank cavity of the hydrated refined oil tank is located on the longitudinal central axis and is connected to a stirrer. The output of the hydrated refined oil tank The oil pipe is connected to the negative pressure dehydration and degumming refined oil tank, and the output oil pipe of the negative pressure dehydration and degumming refined oil tank is connected to the secondary refined oil filter. The inner wall of the tank cavity of the dehydration and degumming decolorization oil tank and the hydration refined oil tank is circumferentially connected with a spiral heating oil coil from bottom to top. The input oil pipe and the return oil pipe of the spiral heating oil coil are respectively connected to the circulating oil heating oil tank and the heating oil circulating pump installed at the bottom support of the refined oil tank seat. The negative pressure dehydration and degumming refined oil tank is also respectively equipped with a heating oil heating oil tank installed on the refined oil tank seat. The vacuum pump and the pneumatic booster pump of the bottom bracket of the frame, the top of the negative pressure dehydration and degumming refined oil tank is connected to the steam condenser by the steam delivery pipe in the tank, the steam condenser is connected to the oil-water separator, the oil-water separator is respectively connected to the vacuum pump and the dewatered water and impurity collection tank, the oil delivery pipe of the negative pressure dehydration and degumming refined oil tank is connected to the secondary refined oil filter, the refined oil delivery pipe of the secondary refined oil filter is respectively connected to the finished oil inspection table and the product inspection and packaging unit of turnip germ oil connected to the rear of the delivery oil pump;

[0012] (6) The product inspection and packaging unit of the turnip germ oil comprises: a mechanical one-piece frame of the product inspection and packaging unit, a finished oil storage tank, a finished oil delivery pump, a finished oil delivery pipe, a fully automatic oil filling machine, a light box, a bottle capping machine, a bottle capping machine, a heat shrinking machine, a fully automatic labeling machine, a product inspection table, an automatic cartoning machine, a conveying track, boxes of finished oil, a bottle washing machine, a packaging bottle drying and disinfecting machine, and a finished oil tank. The mechanical one-piece frame of the product inspection and packaging unit is equipped with a conveying track and is sequentially connected to the fully automatic oil filling machine, the light box, the bottle capping machine, the bottle capping machine, Heat shrink machine, full-automatic labeling machine, product inspection table, automatic cartoning machine, the input oil pipe of the finished oil stable quality storage tank is connected to the essential oil pipeline, and the finished oil output pipe is connected to the full-automatic oil filling machine at the rear through the installed finished oil delivery pump, the rear of the full-automatic oil filling machine is sequentially connected with a light box, a bottle capping machine, a bottle capping machine, a heat shrink machine and a full-automatic labeling machine, the front of the full-automatic oil filling machine is also sequentially connected with a packaging bottle drying and disinfecting machine and a bottle washing machine, the rear of the labeling machine is connected to the product inspection table and then to the automatic cartoning machine, and the rear output of the cartoning machine is connected to the finished oil tank.

[0013] The above-mentioned ginseng-shaped turnip germ oil production and manufacturing device, the high-speed centrifugal seed throwing, wall breaking, shelling and peeling machine is a double-connected high-speed centrifugal seed throwing, wall breaking, shelling and peeling machine, each single high-speed centrifugal seed throwing, wall breaking, shelling and peeling machine includes a wall breaking machine body, a feed receiving bucket, a power motor, a centrifugal wall breaking rotary screen, and a discharge hopper. The wall breaking machine body is composed of a U-shaped basin-shaped body seat with a sealed machine cover connected to the upper mouth, a centrifugal wall breaking rotary screen is installed in the inner cavity of the wall breaking machine body and is connected to a feed receiving bucket, and a discharge hopper is connected to the bottom of the U-shaped basin-shaped body seat, the feed receiving bucket is connected to the discharge connecting pipe of the second material elevator, and the bottom of the discharge hopper is connected to the wall breaking vibrating rotary screen.

[0014] The above-mentioned ginseng-shaped turnip germ oil production and manufacturing device, the wall-breaking vibrating rotary screen is a quadruple reciprocating wall-breaking vibrating rotary screen, and a cyclonic dust suction and removal device is installed on the quadruple reciprocating wall-breaking vibrating rotary screen, and the dust conveying pipe of the cyclonic dust suction and removal device is connected to the dust collecting box, and the lower part of the quadruple reciprocating wall-breaking vibrating rotary screen is connected to the second material elevator of the high-speed centrifugal seed-throwing wall-breaking shelling and peeling machine. The first wall-breaking vibrating rotary screen in the quadruple reciprocating wall-breaking vibrating rotary screen has a screen mesh with a low front and high rear inclination angle of 8-16°. The screen surfaces of the second to fourth wall-breaking vibrating rotary screens have an inclination angle of 12-22°, with the front being low and the back being high, and the inclination angle of the second to fourth wall-breaking vibrating rotary screens gradually increases from the front to the back; the front material receiving screen opening of the first wall-breaking vibrating rotary screen is connected to the discharge hopper of the high-speed centrifugal seed-breaking, shelling and peeling machine, the rear material discharging screen opening of the fourth wall-breaking vibrating rotary screen is connected to the turnip germ collection and feeding bin, and the return material screen opening behind the front screen of the vibrating rotary screen is connected to the return material conveying chute, which is connected to the second material elevator of the high-speed centrifugal seed-breaking, shelling and peeling machine.

[0015] The above-mentioned ginseng-shaped turnip germ oil production and manufacturing device, the drum-type electromagnetic frying steamer includes an electromagnetic frying steamer main body frame, a water spraying pipe, a spray head, a stirring fan wheel, a feed hopper, a discharge hopper, an electric heating drum, an outer insulation jacket of the electric heating drum, a stirring fan wheel power motor, and an electromagnetic pulse heater. The outer insulation jacket of the electric heating drum, the stirring fan wheel power motor, and the electromagnetic pulse heater are respectively installed on the electromagnetic frying steamer main body frame, and the electric heating drum connected to the electromagnetic pulse heater is installed inside the outer insulation jacket of the electric heating drum. The stirring fan wheel is installed in the inner cavity of the electric heating drum. The wheel shaft of the stirring fan wheel is connected to the power output shaft of the stirring fan wheel power motor by a transmission mechanism composed of a transmission wheel and a transmission belt or a transmission chain, and a plurality of spray heads connected to the water spraying pipe are installed on the circumferential drum wall of the inner cavity of the electric heating drum. The feed inlet of the electric heating drum is connected to the feed hopper, and the discharge inlet is connected to the discharge hopper. The discharge hopper is connected to the fourth material elevator, and the feed hopper is connected to the third material elevator.

[0016] In the above-mentioned ginseng-shaped turnip germ oil production and manufacturing device, the circulating oil heating tank and the hydrating liquid agent storage tank are both equipped with heating mechanisms and sensor temperature controllers; the rear of the oil cake crushing machine is equipped with a crushed oil cake conveying pipe or a conveyor connected to an oil cake turnover and recycling container.

[0017] In the above-mentioned ginseng-shaped turnip germ oil production and manufacturing device, 1-3 filter layers are embedded in the inner cavity of the closed primary filter oil tank and the inner cavity of the secondary fine oil filter, and the filter layer is any one of a filter cloth filter layer, a filter paper filter layer, and a filter mesh filter layer.

[0018] The above-mentioned ginseng-shaped turnip germ oil production and manufacturing device, the double-cylinder air pressure filter includes a filter body, a cover, a safety valve, a pressure control meter, a fine filter layer, an oil inlet pipe joint, an air inlet pipe joint, and an air outlet pipe joint. The filter body is a double-cylinder concave filter body. The filter body and the cover body are covered with a sealing ring at the mouth and are sealed and connected. The oil inlet pipe joint and the pipe joint of the filtered crude oil delivery pipe are respectively installed on the upper and lower side bodies of the filter body. The oil inlet pipe The joint is connected to the oil delivery pipe of the first oil delivery pump, and a safety valve and a pressure control gauge are respectively installed on the machine cover. The air inlet pipe joint and the air outlet pipe joint are connected to the air pressure pump. The air inlet pipe joint and the oil inlet pipe joint are installed on the filter body located on the upper part of the fine filter layer, and the air outlet pipe joint and the pipe joint of the filtered crude oil delivery pipe are installed on the filter body located on the lower part of the fine filter layer. 1-3 layers of fine filter layers are embedded in the inner cavity of the filter body, and the fine filter layer is any one of a filter cloth layer, a filter paper layer, and a filter mesh layer.

[0019] The above-mentioned ginseng-shaped turnip germ oil production and manufacturing device, the vibration screening machine includes a feed pipe joint, a screening box, an observation window, a support spring, a screening machine base, a vibration motor, a vibration screen layer, a discharge pipe joint, and a discharge pipe port for light floating impurities on the screen. The screening box is installed on the screening machine base, and 1-2 layers of vibration screen layers are embedded in the inner cavity of the screening box. The lower box of the screening box is respectively equipped with 3 support springs and a vibration motor connected to the screening machine base, and the top, bottom and side of the screening box are respectively equipped with a feed pipe joint, a discharge pipe joint and a discharge pipe port for light floating impurities on the screen, and an observation window is also installed on the screening box.

[0020] The above-mentioned ginseng-shaped turnip germ oil production and manufacturing device, based on the ginseng-shaped turnip germ oil production and manufacturing device, the process method of ginseng-shaped turnip germ oil production and manufacturing is:

[0021] ⑴. The first process is the process of raw material screening, stone removal and impurity removal: select raw materials containing more than 98% of full-fledged ginseng turnip seeds and store them in raw material ginseng turnip seed storage tanks; the ginseng turnip seeds are sent from the reduction tank to the primary screening feeder through the discharge control valve to control the discharge flow rate, and then are transported to the vibration screening machine through the first material elevator for raw material screening, stone removal and impurity removal; the screening time of the raw materials entering the vibration screen is 3 to 6 minutes, and the heavier impurities such as sand and gravel screened under the screen during the screening process are sent to the collection box through the outflow pipe, and the light impurities such as weeds and leaves screened above the screen are sucked out by the 32 to 40kw dust removal fan connected to the vibration screening machine;

[0022] (2) The second process is the process of extracting turnip germ: after the raw materials are screened and de-stoned and impurities are removed through the above process, they are transported by the second material elevator to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine and the four-unit reciprocating wall-breaking and vibrating rotary screen, the turnip seeds are shelled and the wall-breaking and vibrating rotary screen core is used to extract the turnip germ and transport it to the turnip germ collection and feeding bin; the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine adopts a high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine with a design speed of 1800-3200 rpm, the seed material peeled by the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine enters the first wall-breaking and vibrating rotary screen of the four-unit reciprocating wall-breaking and vibrating rotary screen, the cleaned germ peeled by the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine slides upward along the inclined screen surface of the vibrating rotary screen, and is collected and flows into the turnip germ collection and feeding bin, and the seeds that have not been peeled are The material slides downward along the inclined screen surface of the vibrating rotary screen, and returns to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine through the material elevator. The connection structure and mechanical properties of the second to fourth paths are the same as those of the first wall-breaking vibrating rotary screen. After repeated vibration and screening by four wall-breaking vibrating rotary screens, the peeled germs slide upward along the inclined screen surface of the vibrating rotary screen and are collected and flow into the turnip germ collection bin, and the unpeeled seed material slides downward along the inclined screen surface of the vibrating rotary screen and is transported back to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine by the vibrating rotary screen return material conveying pipe. In this way, the material is returned and peeled back and forth, and finally the turnip shell is removed to obtain the turnip germ; and a cyclone dust suction and removal device is installed on the upper part of the four wall-breaking vibrating rotary screens to discharge and collect the dust generated by the four wall-breaking vibrating rotary screens into a dust collecting box;

[0023] ⑶. The third process is the process of frying and steaming turnip germs: the turnip germs prepared by the above process are transported from the turnip germ collection and feeding bin to the drum-type electromagnetic frying steamer through the third material hoist, and the turnip germs are fried, steamed and cooked. The main points are: the drum-type electromagnetic frying steamer is designed to have a frying temperature of 110°C to 150°C and a frying time of 25 to 40 minutes. The specific frying time depends on the temperature setting. After the frying work in the frying steamer is completed, the water mist is transported to the spray head installed on the inner wall of the drum through a water pipe in the drum of the drum-type electromagnetic frying steamer for spraying for 3 to 6 seconds. The drum is rotated and steamed with water vapor for 5 to 10 minutes, so as to achieve the purpose of enhancing the flavor and nutrition of the oil.

[0024] ⑷、The fourth process is oil pressing and filtering: the turnip germs fried and steamed in the above process are transported to the screw oil press through the fourth material elevator for oil pressing, cake taking and filtering. The technical points are: ①. The pressing temperature of the screw oil press is set at 140℃~180℃, and the pressing temperature is adjusted according to the oil output; ②. The oil cake squeezed out of the screw oil press is crushed by the cake crusher and then transported to the cake turnover container or cake storage warehouse. The smoke generated during the pressing process The gas is discharged through the closed smoke exhaust fan; ③. The crude oil squeezed by the screw oil press is first filtered in a closed primary filter oil tank, and then transported by the first oil pump to the double-cylinder air pressure filter for further fine filtration. The air pressure of the double-cylinder air pressure filter is designed to be 0.4MPa, and the fine filter layer embedded in the inner cavity of the double-cylinder air pressure filter tank is 580-660 mesh. After fine filtration by the double-cylinder air pressure filter, the turnip germ crude oil enters the oil collection buffer box and is then transported to the next process by the filtered crude oil delivery pipe;

[0025] (5) The fifth process is the crude oil refining process: the turnip germ crude oil after fine filtration in the above process is transported to one or two to three parallel hydration refined oil tanks through the filtered crude oil delivery pipe and the filtered crude oil delivery pump, and then the input into the tank is sprayed by a spray head installed on the top of the tank connected to the hydration liquid storage tank through a metering control valve and a liquid delivery pipe to spray a hydration liquid with a weight of 2% to 5% of the filtered crude oil in the hydration refined oil tank. The hydration liquid includes salt water with a concentration of 1.8-4% or alkaline water with a concentration of 2% to 4%. The temperature of the hydration liquid is set to 80°C to 100°C. The oil temperature in the hydrated refined oil tank is set to be controlled at 60℃-100℃, the set control temperature of the heating oil in the circulating heating oil tank connected to the heating oil coil installed on the inner wall of the hydrated refined oil tank is 125~130℃, the set control stirring time of the agitator in the hydrated refined oil tank is 1.5~3 hours, the agitator stirs the heated crude oil in the tank and the injected brine and other hydrating liquids to promote the hydration expansion and condensation of the colloid in the turnip crude oil into a large piece of colloid, and after the stirring is completed, the static precipitation is set to be controlled for 5~8 hours. After degumming, the turnip crude oil in the hydrated refined oil tank is removed. The colloid flows from the control valve and the rubber discharge pipe at the bottom of the tank into the colloid storage tank for reuse; the degummed turnip oil after hydration and degumming in the hydration refining tank is transported to the negative pressure dehydration and degumming refining tank. The negative pressure dehydration and degumming refining tank is controlled by the vacuum pump installed. The negative pressure value in the refined oil tank is -0.1MPa~-0.3MPa, and the oil temperature in the tank is set to 80℃~120℃. The oil tank is heated and vacuumed under the stirring of the agitator. The negative pressure dehydration and decolorization time is set to 1~2 hours. The water in the oil boils at low temperature under negative pressure to precipitate water vapor, which is extracted through the connected steam condenser. The steam is cooled to become water and air, and then the water and impurities are separated from the air through the connected oil-water separator. The water and impurities flow into the dewatered water and impurity collection tank, and the air is discharged through the vacuum pump. After the dehydrated and degummed refined oil is statically precipitated in the tank for 3 to 6 hours, the oil temperature in the tank is set to 66 to 72°C, and the pneumatic pressure pump connected to the negative pressure dehydration and degumming refined oil tank is used to increase the pressure in the tank and discharge the oil to the secondary refined oil filter. After secondary filtration, it is refined into finished oil, and then it is transported to the finished oil storage tank through the refined oil pipeline and the finished oil inspection station after inspection by the refined oil delivery pump;

[0026] ⑹. The sixth process is the product inspection and packaging process: the ginseng-shaped turnip germ finished oil in the finished oil storage tank of the above process is transported to the fully automatic oil filling machine through the finished oil delivery pump, and at the same time, the oil filling bottles are cleaned by the bottle washing machine and dried and disinfected by the packaging bottle drying and disinfecting machine, and then transported to the fully automatic oil filling machine. After filling, the oil filling bottles are transported by the transmission track through the light box, bottle capping machine, bottle capping machine, heat shrink machine melting cap and fully automatic labeling machine in turn for capping, coding and labeling, and then sent to the product inspection station for inspection according to national standards and enterprise standards. After passing the inspection, it is sent to the automatic cartoning machine for product packing into a finished oil box, that is, the ginseng-shaped turnip germ finished oil of this application is made.

[0027] ⑺. In the production process of the ginseng-shaped turnip germ oil of the present application product, a programmable microcomputer industrial control machine is used to automatically control the entire process, including a de-impurity and stone removal screening unit A, a turnip seed germ extraction unit B, a turnip germ frying and steaming unit C, a pressing and oil filtering unit D, a crude oil refining unit E, and a product inspection and packaging unit F, which are connected by electrical wires.

[0028] The above-mentioned process for producing ginseng-shaped turnip germ oil comprises the following steps: in the crude oil refining process, after the dehydration and degumming of the negative pressure dehydration and degumming refined oil tank, an edible oil decolorant is added, and the weight ratio of the edible oil decolorant to the oil is 0.05-0.1:1, and the room temperature oil is stirred and mixed, so that the edible oil decolorant and the oil are in a paste-like flow state. The negative pressure value in the refined oil tank is controlled by a vacuum pump to be -0.1MPa--0.3MPa, and the oil temperature in the tank is set to be 80℃-120℃. The oil tank is heated and vacuum pumped under stirring by a stirrer. The vacuum setting controls the negative pressure decolorization time to be 30 to 60 minutes. The oil boils at low temperature under negative pressure to precipitate water vapor. The water and impurities are separated from the air through the connected steam condenser and oil-water separator. The water and impurities flow into the dewatered water and impurity collection tank, and the air is discharged through the vacuum pump. After the dehydrated, degummed and refined oil is allowed to settle in the tank for 1 to 2 hours, the temperature of the oil in the tank is set to 66 to 72°C. The pneumatic pressure pump connected to the negative pressure dehydration, degumming and refined oil tank is used to pressurize the tank and discharge the oil to the secondary fine oil filter to complete the dehydration, degumming and decolorization process.

[0029] When the present invention is used, the ginseng-shaped turnip germ oil production and manufacturing device of the present invention is installed in a production workshop or other suitable places according to design requirements and actual needs, raw materials are prepared, power, water and air sources are connected, and the designed programmable microcomputer industrial control computer is adjusted, and the ginseng-shaped turnip germ oil product is produced according to the ginseng-shaped turnip germ oil production and manufacturing process method of the present application.

[0030] Since the present invention adopts the above technical solution, the beneficial effects are:

[0031] 1. The raw materials of ginseng-shaped turnip seeds are first screened by a primary screening feeder and then screened by a vibrating screening machine to remove heavier debris such as sand and gravel and lighter debris such as weed leaves;

[0032] 2. In the extraction process of turnip germ, a high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine is used, which is connected to a four-joint reciprocating wall-breaking and vibrating rotary screen. The wall-breaking and screening are repeated four times, and the skin content of the obtained turnip germ is extremely low;

[0033] 3. The key to the oil pressing and filtering process is to use a drum-type electromagnetic frying steamer for frying and steaming, and then enter the temperature-controlled screw oil press to squeeze out the oil and take the cake. The squeezed oil cake is broken into cakes by a cake crusher, and the squeezed crude oil is first filtered in a closed primary filter oil tank, and then further finely filtered by a double-cylinder air pressure filter;

[0034] ㈣. The refining process of crude oil is as follows: first, a circulating heating oil coil is installed in the hydration refining tank. The spiral coil increases the surface area for heat transfer and heat dissipation. The heat transfer and heat dissipation are uniform, the surface temperature is low, and it is not easy to cause oil oxidation. It can also avoid the burning of oil, and can ensure that the quality of finished oil is not damaged. The hydration refining tank is equipped with a stirrer to fully stir the heated oil and water injection, promote the hydration expansion of the colloid in the oil and fat to condense into a large piece of colloid, so that the colloid is discharged from the discharge port; second, a negative pressure dehydration and degumming refining tank is designed, and a vacuum pump is provided to form a vacuum environment for dehydration process operation. Oxygen is isolated in the vacuum environment to avoid oil oxidation and color deepening; and an electric heating pipe is provided to prevent the steam in the dehydration process from contacting the inner wall of the tank cavity for condensation, thereby improving the dehydration and decolorization effect. The dehydrated and decolorized oil is pumped into the duplex secondary fine oil filter by a pressurized air pump for fine filtration. After filtering the impurities in the oil, it is refined into finished oil;

[0035] ㈤、Product inspection and automated packaging process: After the ginseng-shaped turnip germ finished oil is transported to the fully automatic oil filling machine through the finished oil delivery pump for filling, the oil filling bottle is then transported by the conveyor track and sequentially passes through the light box, bottle capping machine, bottle capping machine, heat shrinking machine cap melting machine and fully automatic labeling machine for capping, coding and labeling, and then sent to the product inspection station for inspection according to national standards and enterprise standards. After passing the inspection, it is sent to the automatic box packing machine for product box packing into finished oil boxes. It effectively solves the problem that the turnip seed kernel germ after the shelling process in the existing ginseng-shaped turnip germ oil production and manufacturing device and its process method has a high skin content, and the crude oil refining easily causes the oil to burn and the quality of the finished oil is damaged.

[0036] The results of actual operation tests have shown that it has the advantages of a novel and practical production device structure, a reasonable and feasible process method, a low skin content in the turnip kernel germ after the shelling process, and a good dehydration, decolorization and degumming effect in the subsequent refining of the crude oil. It can effectively avoid oil oxidation, ensure the quality of the finished oil from damage, maintain high-quality original juice finished oil performance, and be suitable for industrial production. It is suitable for the industrial production of ginseng-shaped turnip and other turnip germ oils and other small-particle plant seed oils.

[0037] Other features and advantages of the present application will be described in the following description, and partly become apparent from the description, or understood by implementing the present invention. The purpose and other advantages of the present application can be realized and obtained by the structures indicated in the description and the drawings. BRIEF DESCRIPTION OF THE DRAWINGS

[0038] In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following briefly introduces the drawings required for use in the description of the embodiments. Obviously, the drawings described are some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without creative work.

[0039] Figure 1 It is a schematic diagram of the specific structure of an embodiment of the manufacturing device for producing ginseng-shaped turnip germ oil of the present applicant.

[0040] Figure 2 yes Figure 1 Schematic diagram of the equipment connection structure of the impurity and stone removal screening unit and the turnip seed germ extraction unit in the embodiment.

[0041] Figure 3 yes Figure 1 Schematic diagram of the equipment connection structure of the turnip germ frying and steaming unit and the oil pressing and filtering unit in the embodiment.

[0042] Figure 4 yes Figure 1 Schematic diagram of the equipment connection structure of the crude oil refining unit in the embodiment.

[0043] Figure 5 yes Figure 1 Schematic diagram of the equipment connection structure between the product inspection and packaging unit and the programmable microcomputer industrial computer in the embodiment.

[0044] Figure 6 yes Figure 1 and Figure 2 A schematic diagram of the enlarged structure of the left view of the medium vibration screening machine body (excluding the dust removal fan).

[0045] Figure 7 yes Figure 1 and Figure 2 An enlarged cross-sectional structural schematic diagram of a single high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine in an embodiment.

[0046] Figure 8 yes Figure 1 and Figure 2 A schematic diagram of a partially enlarged cross-section structure of the first wall-breaking vibrating rotary screen in the embodiment.

[0047] Fig. 9 yes Figure 1 A schematic diagram of a partially enlarged cross-sectional structure of a drum-type electromagnetic frying and steaming pot in an embodiment.

[0048] Fig.10 yes Fig. 9 A schematic diagram of the cross-sectional structure of the embodiment from the right.

[0049] Fig.11 yes Fig. 9 A rear structural schematic diagram of an embodiment.

[0050] Fig.12 yes Figure 1 and Figure 3 A schematic diagram of the partially enlarged cross-section structure of the enclosed primary filter oil tank in the embodiment.

[0051] Fig.13 yes Figure 1 and Figure 3 A schematic diagram of the partially enlarged cross-section structure of the double-cylinder air pressure filter in the embodiment.

[0052] Fig.14 The invention discloses a process flow diagram of a method for producing ginseng-shaped turnip germ oil of the present invention.

[0053] The numbers in the attached drawings are: A-impurity and stone removal screening unit; B-turnip seed germ extraction unit; C-turnip germ frying and steaming unit; D-pressing and oil filtering unit; E-crude oil refining unit; F-product inspection and packaging unit F; 1-raw material ginseng-shaped turnip seed storage tank; 101-discharge control valve; 2-primary screening feeder; 3-first material elevator; 4-vibration screening machine; 401-dust removal fan; 402 feed pipe joint; 403-screening box; 404-observation window; 405-support spring; 406-screening machine frame; 407-vibration motor; 408-vibration screen layer; 409-discharge pipe joint; 410-discharge pipe outlet for light floating impurities on the screen; 5-second material elevator; 6-high-speed centrifugal seed throwing, wall breaking, shelling and peeling machine; 7- Wall-breaking vibration rotary screen; 701-cyclone dust suction and removal device; 702-dust conveying pipe; 703-return material conveying chute; 704-screen surface; 8-turnip germ collection and feeding bin; 9-third material elevator; 10-drum electromagnetic frying steamer; 101-electromagnetic frying steamer main frame; 102-water spraying pipe; 103-spray head; 104-stirring fan wheel; 105-feeding hopper; 106-discharging hopper; 107-electric heating drum; 108-electric heating drum outer insulation jacket; 109-stirring fan wheel power motor; 110-electromagnetic pulse heater; 11-fourth material elevator; 12-screw oil press; 121-crushing oil cake machine; 122-oil cake turnover and recycling container; 123-enclosed smoke exhaust fan; 13-enclosed Pre-filter oil tank; 131-inlet pipe joint; 132-oil tank cover; 133-mailbox body; 134-filter screen; 135-outlet pipe joint; 14-first oil delivery pump; 15-double-cylinder air pressure filter; 151-filter crude oil delivery pipe; 152-outlet pipe joint; 153-fine filter layer; 154-inlet pipe joint; 155-filter body; 156-machine cover; 157-safety valve; 158-pressure control gauge; 159-inlet pipe joint; 16-refined refined oil tank stand; 17-hydration refined oil tank; 171-filtered crude oil delivery pump; 172-circulating oil heating oil tank; 173-heating oil circulation pump; 174-spiral heating oil coil; 175-agitator; 176-hydration liquid agent storage tank; 177-meter Quantity control valve; 178-infusion tube; 179-spray head; 18-negative pressure dehydration and degumming refined oil tank; 181-vacuum pump; 182-pneumatic pressure pump; 183-steam condenser; 184-oil-water separator; 185-water and impurity collection tank; 19-secondary refined oil filter; 191-essence oil delivery pump; 192-essence oil delivery pipeline; 20-finished oil inspection table; 21-finished oil storage tank; 22-finished oil delivery pump; 23-finished oil output pipe; 24-fully automatic oil filling machine; 25-light box; 26-bottle capping machine; 27-bottle capping machine; 28-heat shrinking machine; 29-fully automatic labeling machine; 30-product inspection table; 31-automatic cartoning machine; 32-transmission track; 33-finished oil tank; 34-bottle washing machine;35-Packaging bottle drying and sterilizing machine; 36-Programmable microcomputer industrial control computer; 37-Product inspection and packaging machinery integrated stand. ; DETAILED DESCRIPTION

[0054] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0055] In the description of the present invention, it should be noted that the terms "upper", "lower", "left", "right", "inside", "outside", "top", "bottom", "front end", "rear end", "head", "tail", etc. indicate orientations or positional relationships based on the orientations or positional relationships shown in the accompanying drawings. They are only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation. Therefore, they cannot be understood as limiting the present invention.

[0056] Embodiment 1: As attached Figure 1-Figure 5 As shown, this embodiment includes: impurity removal and stone removal screening unit A, turnip seed germ extraction unit B, turnip germ frying and steaming unit C, pressing and filtering oil unit D, crude oil refining unit E, product inspection and packaging unit F, and programmable microcomputer industrial control computer 36. The programmable industrial control computer 36 is respectively connected and controlled by electric wires to the impurity removal and stone removal screening unit A, turnip seed germ extraction unit B, turnip germ frying and steaming unit C, pressing and filtering oil unit D, crude oil refining unit E and product inspection and packaging unit F. The impurity removal and stone removal screening unit A is connected to the turnip seed germ extraction unit B at the rear, the turnip seed germ extraction unit B is connected to the turnip germ frying and steaming unit C at the rear and then connected to the pressing and filtering oil unit D, and the pressing and filtering oil unit D is connected to the crude oil refining unit E at the rear and then connected to the product inspection and packaging unit F; specifically:

[0057] (1) The impurity and stone removal screening unit A comprises: a raw material ginseng-shaped turnip seed storage tank 1, a primary screening feeder 2, a first material elevator 3, and a vibrating screening machine 4. The conical bottom of the raw material ginseng-shaped turnip seed storage tank 1 is equipped with a discharge control valve 101, a discharge conveying pipe is connected to the primary screening feeder 2, and the discharge nozzle of the primary screening feeder 2 is connected to the vibrating screening machine 4 by the connected first material elevator 3, and the rear of the vibrating screening machine 4 is connected to a turnip seed germ extraction unit;

[0058] (2) The turnip seed and germ extraction unit B comprises: a second material elevator 5, a high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine 6, a wall-breaking vibrating rotary screen 7, and a turnip germ collection and delivery bin 8. The feed receiving bucket of the second material elevator 5 is connected to the vibrating screening machine 4, and the discharge pipe is connected to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine 6. The vibrating screening machine 4 is also equipped with a dust removal and induced draft fan 401. The rear part of the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine 6 is connected to the wall-breaking vibrating rotary screen 7. The rear part of the wall-breaking vibrating rotary screen 7 is connected to the turnip germ collection and delivery bin 8. The rear part of the turnip germ collection and delivery bin 8 is connected to the turnip germ frying and steaming unit;

[0059] ⑶, the turnip germ frying and steaming unit C comprises a third material hoist 9 and a drum-type electromagnetic frying steamer 10, the feed receiving bucket of the third material hoist 9 is connected to the turnip germ collection and feeding bin 8, the discharge interface pipe is connected to the drum-type electromagnetic frying steamer 10, and the discharge port pipe of the drum-type electromagnetic frying steamer 10 is connected to the oil pressing and filtering unit;

[0060] (4) The oil pressing and filtering unit D comprises: a fourth material hoist 11, a screw oil press 12, a closed primary filter oil tank 13, and a double-cylinder air pressure filter 14. The feed receiving bucket of the fourth material hoist 11 is connected to the drum-type electromagnetic frying steamer 10, and the discharge interface pipe is connected to the screw oil press 12. The squeezed oil outlet connecting pipe of the screw oil press 12 is connected to the closed primary filter oil tank 13, and the squeezed oil cake discharge hopper is connected to the oil cake crushing machine 121. The output oil pipe of the closed primary filter oil tank 13 is equipped with a first oil pump 14 connected to the double-cylinder air pressure filter 15, and the filtered crude oil delivery pipe 151 of the double-cylinder air pressure filter 15 is connected to the turnip germ crude oil refining unit;

[0061] (5) The turnip germ crude oil refining unit E comprises: a refined oil tank frame 16, a hydrated refined oil tank 17, a negative pressure dehydration and degumming refined oil tank 18, a secondary oil filter 19, a filtered crude oil delivery pump 171, and a hydration liquid agent storage tank 176. The hydrated refined oil tank 17 is one or 2-3 hydrated refined oil tanks connected in parallel by an oil pipeline. The hydrated refined oil tank 17, the negative pressure dehydration and degumming refined oil tank 18, and the secondary refined oil filter 19 are installed in parallel on the refined oil tank frame 16. The oil inlet pipe of the hydrated refined oil tank 17 is connected to the oil inlet pipe installed on the refined oil tank frame. The filtered crude oil delivery pump 171 outputs an oil pipe at the bottom bracket of 16, and the input oil pipe of the filtered crude oil delivery pump 171 is connected to the filtered crude oil delivery pipe 151 of the double-cylinder air pressure filter 15. A hydration liquid storage tank 176 is installed on the upper part of the hydrated refined oil tank 17, and a metering control valve 177 is installed on the infusion pipe 178 of the hydrated liquid storage tank 176. The pipe end of the infusion pipe 178 is equipped with a spray head 179 installed on the top of the inner cavity of the hydrated refined oil tank 17. The tank cavity of the hydrated refined oil tank 17 is located on the longitudinal central axis and is connected to a stirrer 175. The oil outlet pipe is connected to the negative pressure dehydration and degumming refined oil tank 18, and the output oil pipe of the negative pressure dehydration and degumming refined oil tank 18 is connected to the secondary refined oil filter 19. The inner wall of the tank cavity of the dehydration and degumming decolorization oil tank 18 and the hydration refined oil tank 17 is circumferentially connected with a spiral heating oil coil 174 from bottom to top. The input oil pipe and return oil pipe of the spiral heating oil coil 174 are respectively connected to the circulating oil heating oil tank 172 and the heating oil circulating pump 173 installed at the bottom support of the refined oil tank frame 16. The negative pressure dehydration and degumming refined oil tank 18 is also respectively installed with a A vacuum pump 181 and a pneumatic pressure pump 182, the top of the negative pressure dehydration and degumming refined oil tank 18 is connected to a steam condenser 183 by a steam delivery pipe in the tank, the steam condenser 183 is connected to an oil-water separator 184, the oil-water separator 184 is respectively connected to the vacuum pump 181 and a dewatered water and impurity collection tank 185, the oil delivery pipe of the negative pressure dehydration and degumming refined oil tank 18 is connected to a secondary refined oil filter 19, the refined oil delivery pipe 192 of the secondary refined oil filter 19 is respectively connected to a finished oil inspection table 20 and a product inspection and packaging unit of turnip germ oil connected to the rear of the delivery oil pump 191;

[0062] (6) The product inspection and packaging unit F of the turnip germ oil comprises: a product inspection and packaging unit mechanical one-piece frame 37, a finished oil storage tank 21, a finished oil delivery pump 22, a finished oil output pipe 23, a fully automatic oil filling machine 24, a light box 25, a bottle capping machine 26, a bottle capping machine 27, a heat shrinking machine 28, a fully automatic labeling machine 29, a product inspection table 30, an automatic box packing machine 31, a conveying track 32, a box of finished oil 33, a bottle washing machine 34, a packaging bottle drying and disinfecting machine 35, and a finished oil tank 33. The product inspection and packaging unit mechanical one-piece frame 37 is equipped with a conveying track 32 and is sequentially connected to the fully automatic oil filling machine 24, the light box 25, the bottle capping machine 26, the bottle capping machine 27, the heat shrinking machine 28, the fully automatic labeling machine 29, the product inspection table 30, the automatic box packing machine 31, the conveying track 32, the box of finished oil 33, the bottle washing machine 34, the packaging bottle drying and disinfecting machine 35, and the finished oil tank 33. 7. Heat shrink machine 28, full-automatic labeling machine 29, product inspection table 30, automatic case packing machine 31. The input oil pipe of the finished oil stable quality storage tank 21 is connected to the essential oil pipeline 192, and the finished oil output pipe 23 is connected to the full-automatic oil filling machine 24 at the rear through the installed finished oil delivery pump 22. The rear of the full-automatic oil filling machine 24 is sequentially connected with a light box 25, a bottle capping machine 26, a bottle capping machine 27, a heat shrink machine 28 and a full-automatic labeling machine 29. The front of the full-automatic oil filling machine 24 is also sequentially connected with a packaging bottle drying and disinfecting machine 35 and a bottle washing machine 34. The rear of the labeling machine is connected to the product inspection table 30 and then connected to the automatic case packing machine 31. The rear output of the case packing machine is connected to the finished oil tank 33.

[0063] The fully automatic oil filling machine in this embodiment is a YSGC-1 fully automatic filling machine.

[0064] Embodiment 2: Preferably, see attached Figure 1-Figure 2 , Figure 7 The high-speed centrifugal seed-breaking, shelling and peeling machine 6 described in this embodiment is a double-connected high-speed centrifugal seed-breaking, shelling and peeling machine. Each single high-speed centrifugal seed-breaking, shelling and peeling machine includes a wall-breaking machine body 602, a feed receiving bucket 601, a power motor 604, a centrifugal wall-breaking rotary screen 603, and a discharge hopper 605. The wall-breaking machine body 602 is composed of a U-shaped basin-shaped body seat with a sealed machine cover connected to the upper mouth. A centrifugal wall-breaking rotary screen 603 is installed in the inner cavity of the wall-breaking machine body 602 and is connected to the power motor 604. The sealing machine cover of the wall-breaking machine body 602 is connected to a feed receiving bucket 601, and a discharge hopper 605 is connected to the bottom of the U-shaped basin-shaped body seat. The feed receiving bucket 601 is connected to the discharge connecting pipe of the second material elevator 5, and the bottom of the discharge hopper 605 is connected to the wall-breaking vibrating rotary screen 7.

[0065] Example 3: Exemplary, see Appendix Figure 1-Figure 2 , Figure 8The wall-breaking vibration rotary screen 7 described in this embodiment is a quadruple reciprocating wall-breaking vibration rotary screen, and a cyclone dust suction and removal device 701 is installed on the quadruple reciprocating wall-breaking vibration rotary screen, and the dust conveying pipe 702 of the cyclone dust suction and removal device 701 is connected to the dust collecting box, and the lower part of the quadruple reciprocating wall-breaking vibration rotary screen is connected to the second material elevator 5 of the high-speed centrifugal seed-throwing wall-breaking shelling and peeling machine 6. The screen surface 704 of the first wall-breaking vibration rotary screen in the quadruple reciprocating wall-breaking vibration rotary screen described in this embodiment is low in front and high in the back. The inclined angle a is 8.2°, and the screen surfaces of the second to fourth wall-breaking vibrating rotary screens have low front and high rear inclination angles of 18°, 19°, 20°, and 22°, respectively; the front material receiving screen port of the first wall-breaking vibrating rotary screen is connected to the discharge hopper of the high-speed centrifugal seed-breaking, shelling and peeling machine 5, the rear material discharging screen port of the fourth wall-breaking vibrating rotary screen is connected to the turnip germ collection and feeding bin 8, and the return material screen port behind the front screen of the vibrating rotary screen is connected to the return material conveying chute 703 connected to the second material elevator 5 of the high-speed centrifugal seed-breaking, shelling and peeling machine 6.

[0066] Embodiment 4: For details, see the attached Figure 1 , Figure 3 , Figure 9-11 The drum-type electromagnetic frying steamer 10 of this embodiment comprises an electromagnetic frying steamer main body frame 101, a water spraying connecting pipe 102, a spray head 103, a stirring fan wheel 104, a feeding hopper 105, a discharging hopper 106, an electric heating drum 107, an electric heating drum outer insulation jacket 108, a stirring fan wheel power motor 109, and an electromagnetic pulse heater 110. The electromagnetic frying steamer main body frame 101 is respectively equipped with an electric heating drum outer insulation jacket 108, a stirring fan wheel power motor 109, and an electromagnetic pulse heater 110. The electric heating drum outer insulation jacket 108 is provided with a connection to the electromagnetic pulse heater 110. 0, a stirring impeller 104 is installed in the inner cavity of the electric heating roller 107, the wheel shaft of the stirring impeller 104 is connected to the power output shaft of the stirring impeller power motor 109 by a transmission mechanism consisting of a transmission wheel and a transmission belt or a transmission chain, and a plurality of spray heads 103 connected to a water spray pipe 102 are installed on the circumferential drum wall of the inner cavity of the electric heating roller 107, a feeding hopper 105 is connected to the feeding port of the electric heating roller 107, and a discharging hopper 106 is connected to the discharging port, the discharging hopper 106 is connected to the fourth material elevator 11, and the feeding hopper 105 is connected to the third material elevator 9.

[0067] Example 5: For further illustration, see the attached Figure 1 , Figure 4 In this embodiment, the circulating oil heating tank 172 and the hydrating liquid agent storage tank 176 are both equipped with a heating mechanism and a sensor temperature controller.

[0068] Embodiment 6: For more details, see the attached Figure 3In this embodiment, the rear of the oil cake crushing machine 121 is connected to a crushed oil cake conveying pipe or a conveyor connected to the oil cake turnover and recycling container 122.

[0069] Embodiment 7: Preferably, see attached Figure 1 , Figure 3-Figure 4 , Fig.12 In this embodiment, two filter layers are embedded in the inner cavity of the closed primary filter oil box 13 and the inner cavity of the secondary fine oil filter 19, and the filter layers are filter cloth filter layers.

[0070] Embodiment 8: For further details, see the attached Figure 1 , Figure 3 , Fig.13 The double-cylinder air pressure filter 15 of this embodiment includes a filter body 155, a cover 156, a safety valve 157, a pressure control gauge 158, a fine filter layer 153, an oil inlet pipe joint 159, an air inlet pipe joint 154, and an air outlet pipe joint 152. The filter body 155 is a double-cylinder concave filter body. The filter body 155 and the cover 156 with a sealing ring embedded in the mouth of the cover body cover each other and are sealed. The oil inlet pipe joint 159 and the pipe joint of the filtered crude oil delivery pipe 151 are respectively installed on the upper and lower side bodies of the filter body 155. The oil inlet pipe joint 159 is connected to the first oil delivery pipe 151. The oil delivery pipe of the pump 14 and the machine cover 156 are respectively installed with a safety valve 157 and a pressure control gauge 158, the air inlet pipe joint 154 and the air outlet pipe joint 152 are connected to the air pressure pump, the air inlet pipe joint 154 and the oil inlet pipe joint 159 are installed on the filter body 155 located on the upper part of the fine filter layer 153, the air outlet pipe joint 152 and the pipe joint of the filtered crude oil delivery pipe 151 are installed on the filter body 155 located on the lower part of the fine filter layer 153, and 1-3 layers of fine filter layers 153 are embedded in the inner cavity of the filter body 155, and the fine filter layer 153 is any one of a filter cloth layer, a filter paper layer, and a filter mesh layer.

[0071] Embodiment 9: Preferably, see attached Figure 1-Figure 2 , Figure 6 The vibration screening machine 4 described in this embodiment includes a feed pipe joint 402, a screening box 403, an observation window 404, a support spring 405, a screening machine frame 406, a vibration motor 407, a vibration screen layer 408, a discharge pipe joint 409, and a discharge pipe port 410 for light floating impurities on the screen. The screening box 403 is installed on the screening machine frame 406, and 1-2 layers of vibration screen layers 408 are embedded in the inner cavity of the screening box 403. Three support springs 405 and a vibration motor 407 are respectively installed on the lower box of the screening box 403, which are connected to the screening machine frame 406, and a feed pipe joint 402, a discharge pipe joint 409 and a discharge pipe port 410 for light floating impurities on the screen are respectively installed on the top, bottom and side body of the screening box 403, and an observation window 404 is also installed on the screening box 403.

[0072] Embodiment 10: The process for producing ginseng-shaped turnip germ oil in this embodiment is:

[0073] ⑴. The first process is the process of raw material screening, stone removal and impurity removal: select ginseng turnip seeds with more than 98% full fruit and store them in the raw material ginseng turnip seed storage tank; the ginseng turnip seeds are sent from the reduction tank to the primary screening feeder through the discharge control valve to control the discharge flow, and then transported to the vibration screening machine through the first material elevator for raw material screening, stone removal and impurity removal; the screening time of the raw material entering the vibration screen is 6 minutes, and the heavier impurities such as sand and gravel screened under the screen during the screening process are sent to the collection box through the outflow pipe, and the light impurities such as weeds and leaves screened above the screen are sucked out by the 32kw ​​dust removal fan connected to the vibration screening machine;

[0074] (2) The second process is the process of extracting turnip germ: after the raw materials are screened and de-stoned and impurities are removed through the above process, they are transported by the second material elevator to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine and the four-unit reciprocating wall-breaking and vibrating rotary screen, the turnip seeds are shelled and the wall-breaking and vibrating rotary screen core is used to extract the turnip germ and transport it to the turnip germ collection and feeding bin; the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine adopts a high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine with a design speed of 1800-3200 rpm, the seed material peeled by the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine enters the first wall-breaking and vibrating rotary screen of the four-unit reciprocating wall-breaking and vibrating rotary screen, and the clean germ peeled by the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine slides upward along the inclined screen surface of the vibrating rotary screen and is collected and flows into the turnip germ collection and feeding bin. The unpeeled seed material slides downward along the inclined screen surface of the vibrating rotary screen, and returns to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine through the material elevator. The connection structure and mechanical properties of the second to fourth paths are the same as those of the first wall-breaking vibrating rotary screen. After repeated vibration and screening by four wall-breaking vibrating rotary screens, the peeled germ slides upward along the inclined screen surface of the vibrating rotary screen and is collected and flows into the turnip germ collection bin. The unpeeled seed material slides downward along the inclined screen surface of the vibrating rotary screen and returns to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine. In this way, the peeling is repeated and the turnip shell is finally removed to obtain the turnip germ; and a cyclone dust suction and removal duster is installed on the upper part of the four wall-breaking vibrating rotary screens to discharge the dust generated by the four wall-breaking vibrating rotary screens and collect them into the dust collecting box;

[0075] ⑶. The third process is the process of frying and steaming turnip germs: the turnip germs prepared by the above process are transported from the turnip germ collection and feeding bin to the drum-type electromagnetic frying steamer through the third material elevator to fry and steam the turnip germs. The main points are: the drum-type electromagnetic frying steamer is designed to have a frying temperature of 120°C to 130°C and a frying time of 30 minutes. The specific frying time depends on the temperature setting. After the frying work in the frying steamer is completed, the water mist is transported to the drum of the drum-type electromagnetic frying steamer through a water pipe to a spray head installed on the inner wall of the drum for spraying for 5 seconds. The drum is rotated and steamed with water vapor for 10 minutes, so as to achieve the purpose of enhancing the flavor and nutrition of the oil.

[0076] ⑷. The fourth process is the oil pressing and filtering process: the turnip germs fried and steamed in the above process are transported to the screw oil press through the fourth material elevator for oil pressing, cake taking and filtering. The technical points are: ①. The pressing temperature of the screw oil press is set to 160°C, and the pressing temperature is adjusted according to the oil output; ②. The oil cakes pressed by the screw oil press are crushed by the cake crusher and then transported to the cake turnover and recycling container or cake storage warehouse. The smoke generated during the pressing process is discharged through the closed smoke exhaust fan; ③. The crude oil pressed by the screw oil press is first filtered in a closed primary filter oil tank, and then transported by the first oil pump to the double-cylinder air pressure filter for further fine filtering. The air pressure of the double-cylinder air pressure filter is designed to be 0.4MPa, and the fine filter layer embedded in the inner cavity of the double-cylinder air pressure filter tank is 600 mesh. The turnip germ crude oil after fine filtration by the double-cylinder air pressure filter enters the oil collecting buffer box, and then is transported to the next process by the filtered crude oil delivery pipe;

[0077] ⑸. The fifth process is the crude oil refining process: the turnip germ crude oil after fine filtration in the above process is transported to three parallel hydration refined oil tanks through the filtered crude oil delivery pipe and the filtered crude oil delivery pump, and then the input into the tank is sprayed by the spray head installed on the top of the tank connected to the hydration liquid storage tank through the metering control valve and the infusion pipe to spray the hydration liquid with a weight of 3.5% of the filtered crude oil in the hydration refined oil tank. The hydration liquid includes salt water with a concentration of 2.0% or alkaline water with a concentration of 2%-4%. The temperature of the hydration liquid is set to 90°C. The oil temperature in the tank is set to control 90°C, the set control temperature of the heating oil in the circulating heating oil tank connected to the heating oil coil installed on the inner wall of the hydrated refined oil tank is 1130°C, and the stirrer in the hydrated refined oil tank is set to control the stirring time to 2 hours. The stirrer stirs the heated crude oil in the tank and the injected brine and other hydrating liquids to promote the hydration, expansion and condensation of the colloid in the turnip crude oil into large pieces of colloid. After the stirring is completed, the static sedimentation is set to control the time for 7 hours. After degumming, the colloid released from the turnip crude oil in the hydrated refined oil tank is controlled from the bottom of the tank. The oil in the negative pressure dehydration and degumming refining tank is controlled by a vacuum pump. The negative pressure in the refining tank is -0.1MPa~-0.3MPa. The oil temperature in the tank is set to 110℃. The oil tank is heated and vacuumed under the stirring of the agitator. The negative pressure dehydration and decolorization time is set to 1.5 hours. The water in the oil boils at low temperature under negative pressure to precipitate water vapor, and the extracted steam is cooled through the connected steam condenser. But it turns into water and air, and the water and impurities are separated from the air by the connected oil-water separator. The water and impurities flow into the dewatered water and impurity collection tank, and the air is discharged through the vacuum pump. After the dehydrated and degummed refined oil is statically precipitated in the tank for 5 hours, the oil temperature in the tank is set to 70°C, and the pneumatic pressure pump connected to the negative pressure dehydration and degumming refined oil tank is used to increase the pressure in the tank and discharge the oil to the secondary refined oil filter. After secondary filtration, it is refined into finished oil, and then it is transported to the finished oil storage tank through the refined oil pipeline and the finished oil inspection station after inspection by the refined oil delivery pump;

[0078] ⑹. The sixth process is the product inspection and packaging process: the ginseng-shaped turnip germ finished oil in the finished oil storage tank of the above process is transported to the full-automatic oil filling machine through the finished oil delivery pump and filled with 500 ml per bottle. At the same time, the oil filling bottles are cleaned by the bottle washing machine and dried and disinfected by the packaging bottle drying and disinfecting machine, and then transported to the full-automatic oil filling machine. After filling, the oil filling bottles are transported by the transmission track through the light box, bottle capping machine, bottle capping machine, heat shrink machine melting cap and full-automatic labeling machine in turn for capping, coding and labeling, and then sent to the product inspection station for inspection according to national standards and enterprise standards. After passing the inspection, they are sent to the automatic cartoning machine for product packing into finished oil boxes, that is, the ginseng-shaped turnip germ finished oil of this application is made.

[0079] The trial product of this application, ginseng-shaped turnip germ finished oil, was tested by a national legal testing unit, and the main indicators of the test results are:

[0080]

[0081]

[0082] ⑺. In the production and manufacturing process of the ginseng-shaped turnip germ oil of the present application product, a programmable microcomputer industrial control machine is used to automatically control the entire process, including a de-impurity and stone removal screening unit A, a turnip seed germ extraction unit B, a turnip germ frying and steaming unit C, a pressing and oil filtering unit D, a crude oil refining unit E, and a product inspection and packaging unit F, which are connected by electrical wires.

[0083] Embodiment 11: In the crude oil refining process of embodiment 10 described in this embodiment, after the dehydration and degumming of the negative pressure dehydration and degumming refining tank, an edible oil decolorant is added, and the weight ratio of edible oil decolorant: oil is 0.06:1 at room temperature oil and fat is stirred and mixed, so that the edible oil decolorant and oil are in a paste-like flow state. The negative pressure value in the refined oil tank is controlled by a vacuum pump to be -0.1MPa to -0.3MPa, and the oil temperature in the tank is set to 80℃ to 120℃. The oil tank is heated and vacuumed under stirring with a stirrer. The negative pressure decolorization time is set to be 40 minutes. Water vapor is precipitated by low-temperature boiling in the oil under negative pressure. Water, impurities and air are separated through the connected steam condenser and oil-water separator. Water and impurities flow into the dewatered water and impurity collection tank, and the air is discharged through the vacuum pump. After the dehydrated, degummed and refined oil is allowed to settle in the tank for 1.5 hours, the temperature of the oil in the tank is set to 70°C. The pneumatic pressure pump connected to the negative pressure dehydration, degumming and refined oil tank is used to pressurize the tank and discharge the oil to the secondary fine oil filter to complete the dehydration, degumming and decolorization process.

[0084] The above is only one embodiment. On this basis, other technical features and technical solutions derived by adding components, equivalent substitutions and local improvements without creative work by technicians in this field are all within the scope of protection of the patent of this invention.

Claims

1. A manufacturing device for ginseng-shaped turnip germ oil, characterized in that: It comprises a dirt-removing and stone-removing screening unit (A), a turnip seed and germ extraction unit (B), a turnip germ frying and steaming unit (C), an oil pressing and filtering unit (D), a crude oil refining and refining unit (E), a product inspection and packaging unit (F), and a programmable microcomputer industrial control computer (36). The programmable industrial control computer is connected to and controls the dirt-removing and stone-removing screening unit, the turnip seed and germ extraction unit, the turnip germ frying and steaming unit, the oil pressing and filtering unit, the crude oil refining and refining unit and the product inspection and packaging unit respectively through electric wires. The rear part of the dirt-removing and stone-removing screening unit is connected to the turnip seed and germ extraction unit, the rear part of the turnip seed and germ extraction unit is connected to the turnip germ frying and steaming unit and then to the oil pressing and filtering unit, and the rear part of the oil pressing and filtering unit is connected to the crude oil refining and refining unit and then to the product inspection and packaging unit. Specifically: (1) The impurity and stone removal screening unit (A) comprises a raw material ginseng-shaped turnip seed storage tank (1), a primary screening feeder (2), a first material elevator (3), and a vibration screening machine (4); a discharge control valve (101) is installed at the conical bottom of the raw material ginseng-shaped turnip seed storage tank (1); a discharge conveying pipe is connected to the primary screening feeder (2); a discharge nozzle pipe of the primary screening feeder (2) is connected to the vibration screening machine (4) through the first material elevator (3); and a turnip seed germ extraction unit is connected to the rear of the vibration screening machine (4); (2) The turnip seed and germ extraction unit (B) comprises a second material elevator (5), a high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine (6), a wall-breaking vibrating rotary screen (7), and a turnip germ collection and delivery bin (8); the feed receiving hopper of the second material elevator (5) is connected to a vibrating screening machine (4), and the discharge pipe is connected to a high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine (6); the vibrating screening machine (4) is also equipped with a dust removal and induced draft fan (401); the rear of the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine (6) is connected to a wall-breaking vibrating rotary screen (7); the rear of the wall-breaking vibrating rotary screen (7) is connected to a turnip germ collection and delivery bin (8); and the rear of the turnip germ collection and delivery bin (8) is connected to a turnip germ frying and steaming unit; (3) The turnip germ frying and steaming unit (C) comprises a third material elevator (9) and a drum-type electromagnetic frying and steaming pot (10); the feed receiving bucket of the third material elevator (9) is connected to the turnip germ collection and feeding bin (8), the discharge interface pipe is connected to the drum-type electromagnetic frying and steaming pot (10), and the discharge port pipe of the drum-type electromagnetic frying and steaming pot (10) is connected to the oil pressing and filtering unit; (4) The oil pressing and filtering unit (D) comprises a fourth material elevator (11), a screw oil press (12), a closed primary filter oil tank (13), and a double-cylinder air pressure filter (14); the feed receiving hopper of the fourth material elevator (11) is connected to the drum-type electromagnetic frying steamer (10), the discharge interface pipe is connected to the screw oil press (12), the squeezed oil outlet connecting pipe of the screw oil press (12) is connected to the closed primary filter oil tank (13), the squeezed oil cake discharge hopper is connected to the oil cake crushing machine (121), the output oil pipe of the closed primary filter oil tank (13) is connected to the first oil delivery pump (14) connected to the double-cylinder air pressure filter (15), and the filtered crude oil delivery pipe (151) of the double-cylinder air pressure filter (15) is connected to the turnip germ crude oil refining unit; (5) The turnip germ crude oil refining unit (E) comprises a refined oil tank frame (16), a hydrated refined oil tank (17), a negative pressure dehydration and degumming refined oil tank (18), a secondary oil filter (19), a filtered crude oil delivery pump (171), and a hydration liquid agent storage tank (176). The hydrated refined oil tank (17) is one or two to three hydrated refined oil tanks connected in parallel by an oil delivery pipeline. The hydrated refined oil tank (17), the negative pressure dehydration and degumming refined oil tank (18), and the secondary refined oil filter (19) are installed in parallel on the refined oil tank frame (16). The oil inlet pipe of the hydrated refined oil tank (17) is connected to the oil inlet pipe installed on the refined oil tank frame (17). 6) an output oil pipe of a filtered crude oil delivery pump (171) of the bottom support, an input oil pipe of the filtered crude oil delivery pump (171) connected to a filtered crude oil delivery pipe (151) of a double-cylinder air pressure filter (15), a hydration liquid agent storage tank (176) installed on the upper part of the hydrated refined oil tank (17), a metering control valve (177) installed on a liquid delivery pipe (178) of the hydrated liquid agent storage tank (176), a spray head (179) installed on the top of the inner cavity of the hydrated refined oil tank (17) installed on the pipe end of the liquid delivery pipe (178), a stirrer (175) installed on the tank cavity of the hydrated refined oil tank (17) located on the longitudinal central axis, and a hydrated refined oil tank (17) The output oil pipe of the negative pressure dehydration and degumming refined oil tank (18) is connected to the secondary refined oil filter (19); the inner wall of the tank cavity of the dehydration and degumming refined oil tank (18) and the hydration refined oil tank (17) is connected with a spiral heating oil coil (174) from bottom to top in the circumferential direction; the input oil pipe and the return oil pipe of the spiral heating oil coil (174) are respectively connected to the circulating oil heating oil tank (172) and the heating oil circulating pump (173) installed at the bottom support of the refined oil tank frame (16); the negative pressure dehydration and degumming refined oil tank (18) is also respectively installed with a vacuum pump (172) installed at the bottom support of the refined oil tank frame (16); The negative pressure dehydration and degumming refined oil tank (18) is connected to a steam condenser (183) through a steam delivery pipe in the tank, and the steam condenser (183) is connected to an oil-water separator (184). The oil-water separator (184) is respectively connected to a vacuum pump (181) and a dewatered water and impurity collection tank (185). The oil delivery pipe of the negative pressure dehydration and degumming refined oil tank (18) is connected to a secondary refined oil filter (19). The refined oil delivery pipe (192) of the secondary refined oil filter (19) is respectively connected to a finished oil inspection table (20) and a product inspection and packaging unit for turnip germ oil connected to the rear of the delivery oil pump (191); (6) The product inspection and packaging unit (F) of the turnip germ oil comprises a product inspection and packaging unit mechanical integrated frame (37), a finished oil storage tank (21), a finished oil delivery pump (22), a finished oil delivery pipe (23), a fully automatic oil filling machine (24), a light box (25), a bottle capping machine (26), a bottle capping machine (27), a heat shrinking machine (28), a fully automatic labeling machine (29), a product inspection table (30), an automatic box packing machine (31), a conveying track (32), boxed finished oil (33), a bottle washing machine (34), a packaging bottle drying and disinfecting machine (35), and a finished oil tank (33). The conveying track (32) is installed on the product inspection and packaging unit mechanical integrated frame (37) and is sequentially connected to the fully automatic oil filling machine (24), the light box (25), the bottle capping machine (26), and the bottle capping machine (27). , a heat shrinking machine (28), a fully automatic labeling machine (29), a product inspection table (30), and an automatic case packing machine (31); the input oil pipe of the finished oil stable quality storage tank (21) is connected to the essential oil delivery pipe (192); the finished oil output pipe (23) is connected to the fully automatic oil filling machine (24) at the rear through the connected finished oil delivery pump (22); the rear of the fully automatic oil filling machine (24) is connected in sequence to a light box (25), a bottle capping machine (26), a bottle capping machine (27), a heat shrinking machine (28), and a fully automatic labeling machine (29); the front of the fully automatic oil filling machine (24) is also connected in sequence to a packaging bottle drying and disinfecting machine (35) and a bottle washing machine (34); the rear of the fully automatic labeling machine (29) is connected to the product inspection table (30) and then to the automatic case packing machine (31); the rear output of the case packing machine is connected to the finished oil tank (33).

2. The ginseng-shaped turnip germ oil production and manufacturing device according to claim 1, characterized in that: The high-speed centrifugal seed-throwing wall-breaking, shelling and peeling machine (6) is a double-connected high-speed centrifugal seed-throwing wall-breaking, shelling and peeling machine. Each single high-speed centrifugal seed-throwing wall-breaking, shelling and peeling machine comprises a wall-breaking machine body (602), a feed receiving bucket (601), a power motor (604), a centrifugal wall-breaking rotary screen (603), and a discharge bucket (605). The wall-breaking machine body (602) is composed of a U-shaped basin-shaped machine body seat with a sealing machine cover connected to the upper opening. A centrifugal wall-breaking rotary screen (603) connected to a power motor (604) is installed in the inner cavity of the wall-breaking machine body (602), and a feed hopper (601) is installed on the sealed machine cover of the wall-breaking machine body (602), and a discharge hopper (605) is connected to the bottom of the U-shaped basin-shaped body seat, the feed hopper (601) is connected to the discharge pipe of the second material elevator (5), and the bottom of the discharge hopper (605) is connected to the wall-breaking vibrating rotary screen (7).

3. The manufacturing device for producing ginseng-shaped turnip germ oil according to claim 1, characterized in that: The wall-breaking vibrating rotary screen (7) is a quadruple reciprocating wall-breaking vibrating rotary screen, and a cyclone dust suction and removal device (701) is installed on the quadruple reciprocating wall-breaking vibrating rotary screen. The dust conveying pipe (702) of the cyclone dust suction and removal device (701) is connected to the dust collecting box. The screen surface (704) of the first wall-breaking vibrating rotary screen in the quadruple reciprocating wall-breaking vibrating rotary screen has a front low and rear high inclination angle of 8-16°, and the screen surfaces of the second to fourth wall-breaking vibrating rotary screens have a front low and rear high inclination angle of 8-16°. The angle of inclination is 12-22°, and the inclination angles of the second to fourth wall-breaking vibrating rotary screens gradually increase from the front to the back; the front material receiving screen opening of the first wall-breaking vibrating rotary screen is connected to the discharge hopper of the high-speed centrifugal seed-throwing wall-breaking shelling and peeling machine (5), the rear material discharging screen opening of the fourth wall-breaking vibrating rotary screen is connected to the turnip germ collection and feeding bin (8), and the rear material return screen opening of the front screen of the vibrating rotary screen is connected to the return material conveying chute (703) connected to the second material elevator (5) of the high-speed centrifugal seed-throwing wall-breaking shelling and peeling machine (6).

4. The manufacturing device for producing ginseng-shaped turnip germ oil according to claim 1, characterized in that: The drum-type electromagnetic frying steamer (10) comprises an electromagnetic frying steamer main body frame (101), a water spraying connecting pipe (102), a spray head (103), a stirring fan wheel (104), a feeding hopper (105), a discharging hopper (106), an electric heating drum (107), an outer heat preservation jacket (108) of the electric heating drum, a power motor for the stirring fan wheel (109), and an electromagnetic pulse heater (110). The electromagnetic frying steamer main body frame (101) is respectively mounted with the outer heat preservation jacket (108) of the electric heating drum, the power motor for the stirring fan wheel (109), and the electromagnetic pulse heater (110). The outer heat preservation jacket (108) of the electric heating drum is equipped with a motor connected to the electromagnetic pulse heater (110). ) of an electric heating drum (107), wherein a stirring impeller (104) is installed in the inner cavity of the electric heating drum (107), the wheel shaft of the stirring impeller (104) is connected to the power output shaft of the stirring impeller power motor (109) by a transmission mechanism consisting of a transmission wheel and a transmission belt or a transmission chain, and a plurality of spray heads (103) connected to a water spray connecting pipe (102) are installed on the circumferential drum wall of the inner cavity of the electric heating drum (107), the feed inlet of the electric heating drum (107) is connected to a feed hopper (105), and the discharge inlet is connected to a discharge hopper (106), the discharge hopper (106) is connected to a fourth material elevator (11), and the feed inlet hopper (105) is connected to a third material elevator (9).

5. The manufacturing device for producing ginseng-shaped turnip germ oil according to claim 1, characterized in that: The circulating oil heating tank (172) and the hydrating liquid agent storage tank (176) are both equipped with a heating mechanism and a sensor temperature controller; the rear of the oil cake crushing machine (121) is connected to a crushed oil cake conveying pipe or a conveyor connected to the oil cake turnover and recycling container (122).

6. The manufacturing device for producing ginseng-shaped turnip germ oil according to claim 1, characterized in that: The inner cavity of the closed primary filter oil box (13) and the inner cavity of the secondary fine oil filter (19) are both embedded with 1-3 filter layers, wherein the filter layer is any one of a filter cloth filter layer, a filter paper filter layer and a filter mesh filter layer.

7. The manufacturing device for producing ginseng-shaped turnip germ oil according to claim 1, characterized in that: The double-cylinder air pressure filter (15) comprises a filter body (155), a cover (156), a safety valve (157), a pressure control gauge (158), a fine filter layer (153), an oil inlet pipe joint (159), an air inlet pipe joint (154), and an air outlet pipe joint (152). The filter body (155) is a double-cylinder concave filter body. The filter body (155) and the cover (156) with a sealing ring embedded at the mouth of the cover body are mutually covered and sealed. The oil inlet pipe joint (159) and the pipe joint of the filtered crude oil delivery pipe (151) are respectively installed on the upper and lower side bodies of the filter body (155). The oil inlet pipe joint (159) is connected to the first oil delivery pump (151). 4), a safety valve (157) and a pressure control gauge (158) are respectively installed on the cover (156), an air inlet pipe joint (154) and an air outlet pipe joint (152) are connected to an air pressure pump, the air inlet pipe joint (154) and the oil inlet pipe joint (159) are installed on a filter body (155) located on the upper part of the fine filter layer (153), and the air outlet pipe joint (152) and the pipe joint of the filtered crude oil delivery pipe (151) are installed on the filter body (155) located on the lower part of the fine filter layer (153), and 1-3 layers of fine filter layers (153) are embedded in the inner cavity of the filter body (155), and the fine filter layer (153) is any one of a filter cloth layer, a filter paper layer, and a filter mesh layer.

8. The manufacturing device for producing ginseng-shaped turnip germ oil according to claim 1, characterized in that: The vibrating screening machine (4) comprises a feed pipe joint (402), a screening box (403), an observation window (404), a support spring (405), a screening machine frame (406), a vibration motor (407), a vibrating screen layer (408), a discharge pipe joint (409), and a discharge pipe port (410) for light floating impurities on the screen. The screening box (403) is connected to the screening machine frame (406). A 1- The present invention relates to a two-layer vibrating screen layer (408), wherein three supporting springs (4050) and a vibration motor (407) are respectively installed on the lower box of the screening box (403) and connected to the screening machine frame (406), and a feed pipe joint (402), a discharge pipe joint (409) and a discharge pipe port (410) for light floating impurities on the screen are respectively installed on the top, bottom and side of the screening box (403), and an observation window (404) is also installed on the screening box (403).

9. The manufacturing device for producing ginseng-shaped turnip germ oil according to claim 1, characterized in that: Based on the ginseng-shaped turnip germ oil production and manufacturing device, the process method for producing the ginseng-shaped turnip germ oil is: ⑴. The first process is raw material screening, stone removal and impurity removal: select raw materials containing more than 98% of full-fledged ginseng turnip seeds and store them in raw material ginseng turnip seed storage tanks; the ginseng turnip seeds are sent from the reduction tank to the primary screening feeder through the discharge control valve to control the discharge flow rate, and then are transported to the vibration screening machine through the first material elevator for raw material screening, stone removal and impurity removal; the screening time of the raw materials entering the vibrating screen is 3 to 6 minutes, and the heavier impurities such as sand and gravel screened under the screen during the screening process are sent to the collection box through the outflow pipe, and the light impurities such as weeds and leaves screened above the screen are sucked out by the 32 to 40kw dust removal fan connected to the vibration screening machine; (2) The second process is to extract turnip germ: after the raw materials are screened and de-stoned and impurities are removed through the above process, they are transported by the second material elevator to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine and the four-unit reciprocating wall-breaking and vibrating rotary screen, the turnip seeds are shelled and the wall-breaking and vibrating rotary screen core is screened, and the turnip germ is extracted and transported to the turnip germ collection and feeding bin; the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine adopts a high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine with a design speed of 1800-3200 rpm, the seed material peeled by the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine enters the first wall-breaking and vibrating rotary screen of the four-unit reciprocating wall-breaking and vibrating rotary screen, the cleaned germ peeled by the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine slides upward along the inclined screen surface of the vibrating rotary screen and is collected and flows into the turnip germ collection and feeding bin, The unpeeled seed material slides downward along the inclined screen surface of the vibrating rotary screen, and returns to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine through the material elevator. The connection structure and mechanical properties of the second to fourth paths are the same as those of the first wall-breaking vibrating rotary screen. After repeated vibration and screening by four wall-breaking vibrating rotary screens, the peeled germ slides upward along the inclined screen surface of the vibrating rotary screen and is collected and flows into the turnip germ collection bin. The unpeeled seed material slides downward along the inclined screen surface of the vibrating rotary screen and returns to the high-speed centrifugal seed-throwing, wall-breaking, shelling and peeling machine. In this way, the peeling is repeated and the turnip shell is finally removed to obtain the turnip germ. A cyclone dust suction and removal device is correspondingly installed on the upper part of the four wall-breaking vibrating rotary screens to discharge and collect the dust generated by the four wall-breaking vibrating rotary screens into a dust collecting box. ⑶. The third process is frying and steaming turnip germ: the turnip germ prepared by the above process is transported from the turnip germ collection and feeding bin to the drum-type electromagnetic frying steamer through the third material hoist, and the turnip germ is fried, steamed and cooked. The main points are: the drum-type electromagnetic frying steamer is designed to have a frying temperature of 110°C to 150°C and a frying time of 25 to 40 minutes. The specific frying time depends on the temperature setting. After the frying work in the frying steamer is completed, the water mist is transported to the spray head installed on the inner wall of the drum through a water pipe in the drum of the drum-type electromagnetic frying steamer for spraying for 3 to 6 seconds. The drum is rotated and steamed with water vapor for 5 to 10 minutes, so as to achieve the purpose of enhancing the flavor and nutrition of the oil; ⑷、The fourth process is oil pressing and filtering: the turnip germs fried and steamed in the above process are transported to the screw oil press through the fourth material elevator for oil pressing, cake taking and filtering. The technical points are: ①. Set the pressing temperature of the screw oil press to 140℃~180℃, and adjust the pressing temperature according to the oil output; ②. The oil cake squeezed by the screw oil press is crushed by the cake crusher and then transported to the cake turnover container or cake storage warehouse. The smoke generated during the pressing process is discharged through a closed smoke exhaust fan; ③. The crude oil squeezed by the screw oil press is first filtered by a closed primary filter oil tank, and then transported by the first oil pump to the double-cylinder air pressure filter for further fine filtration. The air pressure of the double-cylinder air pressure filter is designed to be 0.4MPa, and the fine filtration layer embedded in the inner cavity of the double-cylinder air pressure filter tank is 580~660 mesh. The turnip germ crude oil after fine filtration by the double-cylinder air pressure filter enters the oil collection buffer box, and then is transported to the next process by the filtered crude oil delivery pipe; ⑸. The fifth process is crude oil refining: the turnip germ crude oil after fine filtration in the above process is transported to one or two to three parallel hydration refined oil tanks through the filtered crude oil delivery pipe and the filtered crude oil delivery pump, and then the input into the tank is sprayed by the spray head installed on the top of the tank connected to the hydration liquid storage tank through the metering control valve and the infusion pipe to spray the hydration liquid with a weight of 2% to 5% of the filtered crude oil in the hydration refined oil tank. The hydration liquid includes salt water with a concentration of 1.8-4% or alkaline water with a concentration of 2% to 4%. The temperature of the hydration liquid is set to 80℃ to 100℃. The oil temperature in the oil refining tank is set to control 60℃-100℃, the set control temperature of the heating oil in the circulating heating oil tank connected to the heating oil coil installed on the inner wall of the hydrated refined oil tank is 125~130℃, and the set control stirring time of the agitator in the hydrated refined oil tank is 1.5~3 hours. The agitator stirs the heated crude oil in the tank and the injected brine and other hydrating liquids to promote the hydration expansion and condensation of the colloid in the turnip crude oil into large pieces of colloid. After the stirring is completed, the static precipitation is set to control the time of 5~8 hours for degumming. The colloid flows from the control valve and the rubber discharge pipe at the bottom of the tank to the colloid storage tank for reuse; the degummed turnip oil after hydration and degumming in the hydration refining tank is transported to the negative pressure dehydration and degumming refining tank. The negative pressure dehydration and degumming refining tank is controlled by the vacuum pump installed in the refining tank. The negative pressure value in the refining tank is -0.1MPa~-0.3MPa, and the oil temperature in the tank is set to 80℃~120℃. The oil tank is heated and vacuumed under the stirring of the stirrer. The negative pressure dehydration and decolorization time is set to 1~2 hours. The water in the oil boils at low temperature under negative pressure to precipitate water vapor, which is extracted through the connected steam condenser. The steam is cooled to become water and air, and then the water and impurities are separated from the air by the connected oil-water separator. The water and impurities flow into the dewatered water and impurity collection tank, and the air is discharged through the vacuum pump. After the dehydrated and degummed refined oil is statically precipitated in the tank for 3 to 6 hours, the oil temperature in the tank is set to 66-72°C, and the pneumatic pressure pump connected to the negative pressure dehydration and degumming refined oil tank is used to increase the pressure in the tank and discharge the oil to the secondary refined oil filter. After the secondary filtration, it is refined into finished oil, and then it is transported to the finished oil storage tank through the refined oil pipeline and the finished oil inspection station after inspection by the refined oil delivery pump; ⑹. The sixth process is product inspection and packaging: the ginseng-shaped turnip germ finished oil in the finished oil storage tank of the above process is transported to the fully automatic oil filling machine through the finished oil delivery pump. At the same time, the oil filling bottles are washed by the bottle washing machine and dried and disinfected by the packaging bottle drying and disinfecting machine, and then transported to the fully automatic oil filling machine. After filling, the oil filling bottles are transported by the conveyor track to the light box, bottle capping machine, bottle capping machine, heat shrink machine melting cap and fully automatic labeling machine for capping, coding and labeling, and then sent to the product inspection station for inspection according to national standards and enterprise standards. After passing the inspection, it is sent to the automatic box packing machine for product box packing into a finished oil box, that is, the ginseng-shaped turnip germ finished oil of this application is made. . ⑺. In the production and manufacturing process of the ginseng-shaped turnip germ oil of the present application product, a programmable microcomputer industrial control machine is used to automatically control the entire process, including a de-impurity and stone removal screening unit A, a turnip seed germ extraction unit B, a turnip germ frying and steaming unit C, a pressing and oil filtering unit D, a crude oil refining unit E, and a product inspection and packaging unit F, which are connected by electrical wires.

10. The process for producing ginseng-shaped turnip germ oil according to claim 9, characterized in that: In the crude oil refining process, after the dehydration and degumming of the refined oil tank by negative pressure dehydration and degumming, an edible oil decolorant is added, and the room temperature grease is stirred and mixed in a weight ratio of edible oil decolorant: grease of 0.05-0.1:1, so that the edible oil decolorant and the grease are in a paste-like flow state. The negative pressure value in the refined oil tank is controlled by a vacuum pump to be -0.1MPa-0.3MPa, and the oil temperature in the tank is set to be controlled to be 80℃-120℃. The oil tank is heated and vacuumed under stirring by a stirrer to set and control the negative pressure decolorization time. The process is as follows: the process is carried out for 30 to 60 minutes, and the oil and fat boils at low temperature under negative pressure to precipitate water vapor, and the water and impurities are separated from the air through the connected steam condenser and oil-water separator, and the water and impurities flow into the dewatered water and impurity collection tank, and the air is discharged through the vacuum pump. After the dehydrated, degummed and refined oil is statically precipitated in the tank for 1 to 2 hours, the temperature of the oil and fat in the tank is set to 66 to 72°C, and the pneumatic pressure pump connected to the negative pressure dehydration, degumming and refined oil tank is used to increase the pressure in the tank and discharge the oil to the secondary fine oil filter, thereby completing the dehydration, degumming and decolorization process.

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