CN108576835A - One kind is for draining device and its working method in garden stuff processing - Google Patents

Abstract

A juicing device and working method for fruit and vegetable processing, the device includes a crushing mechanism, a grinding mechanism, a central controller and a stainless steel support, and the crushing mechanism includes a bludgeoning crushing chamber, a bludgeoning crusher, a crusher shaft and multiple crushing hammers The grinding mechanism includes a pellet feeding chamber, a juicing turntable, a fixed disc, a collection chamber, a filtrate separation chamber, a compression rotating shaft, and a grinding motor; Coordinated tooth grinding; method: start the blunt impact crusher, add materials and water, the extruded product is discharged, and the mixture of water and granular materials enters the filtrate separation chamber; automatically monitor the broken particle size of fruits and vegetables, and start grinding under suitable working conditions Motor; automatically monitor the height of the material level to control the speed of the bludgeon crusher and grinding motor; control the action of the transmission motor and stirring motor, and add water and chemicals to treat the mixture of water and pellets. The invention can conveniently and quickly complete the juice extraction operation.

Description

Juicing device and working method for fruit and vegetable processing

technical field

The invention relates to a juice extraction device used in fruit and vegetable processing and a working method thereof.

Background technique

With the improvement of living standards, more and more people begin to pay attention to the pursuit of health and health preservation. In the existing juicing process of fruit and vegetable processing, it is necessary to first chop the vegetables and fruits with a knife, and then use a juice extractor to squeeze the juice. A machine for crushing fruits and vegetables. The structure of these machines is mostly a motor drives a shaft to rotate. There are several cutters on the shaft. The shaft goes deep into the bottom of the mixing cup so that the ingredients can be broken and poured into the container. It is mostly mixed with the juice, and it is difficult to separate the juice separately.

Contents of the invention

Aiming at the problems existing in the above-mentioned prior art, the present invention provides a juicing device used in fruit and vegetable processing. The device is easy to operate, can conveniently complete the juicing operation of vegetables and fruits, and can directly separate the juice, which can effectively Improve the work efficiency of juicing.

The invention provides a juice extraction device used in fruit and vegetable processing, comprising a crushing mechanism, a grinding mechanism, a central controller and a stainless steel bracket arranged at the lower part of the grinding mechanism. The fruit and vegetable feeding port above one side of the chamber and connected with the inner cavity of the bludgeoning crushing chamber, the water inlet pipe arranged on the upper side of the bludgeoning crushing chamber, the bludgeoning crusher fixed on the top of the bludgeoning crushing chamber, and the rotatable The crusher shaft arranged in the center of the blunt crushing chamber, and the sieve plate fixedly arranged at the lower opening end of the blunt crushing chamber; the upper end of the crusher shaft is connected with the output shaft of the blunt crushing machine, and the crusher shaft is uniform The ground set has multiple crushing hammers;

The crushing mechanism also includes a crushing particle size detector fixedly installed under the inner wall of the bludgeoning crushing chamber;

The grinding mechanism includes a pellet feeding chamber connected through the lower opening end of the blunt crushing chamber, a juicing turntable rotatably arranged under the pellet feeding chamber, and a The fixed disc, the collection room fixedly connected to the lower periphery of the fixed disc, the fruit puree extrusion port arranged on one side of the collection room, the material level gauge arranged in the pellet feeding room, and the ground connected to the collection room The filtrate separation chamber arranged at the lower part of the material collection chamber, the compression rotating shaft arranged in the filtrate separation chamber, the slag water level gauge installed in the filtrate separation chamber, the slag discharge pipe arranged at the bottom of the filtrate separation chamber, and the bludgeoning Grinding motor on one side of the crushing chamber;

In the longitudinal direction of the juicing turntable, there is at least one discharge hole connected to its lower surface; The compression cover body and the support platform carrying the fixed disk and the compression cover body are composed of a gap fit between the compression cover body and the fixed grinding disc. The compression cover body is evenly arranged along its circumference with several compression chambers communicating with its inner cavity. holes; the feeding part of the collection chamber is located on its upper part and is arranged around the compression cover, and a filter screen is provided at the communication part between the collection chamber and the filtrate separation chamber; shaft; the upper end of the compression rotating shaft rotatably passes through the support platform and the fixed grinding disc and is installed in the juicing turntable; the bottom end of the compression rotating shaft is equipped with a slave transmission pulley; the output shaft of the grinding motor is equipped with The transmission pulley, the main transmission pulley is connected with the secondary transmission pulley through the transmission pulley; the lower surface of the juicing turntable and the upper surface of the fixed grinding disc are provided with mutually matching grinding teeth;

The crushing particle size detector, blunt impact crusher, material level gauge, slag water level gauge, grinding motor, solenoid valve on the slag discharge pipe, and control valve on the water inlet pipe are connected to the central controller through wires;

The pellet feeding chamber is a cylindrical structure; the stainless steel bracket is made of galvanized material; the grinding motor and the central controller are fixedly installed on the stainless steel bracket.

In this technical scheme, the fruits and vegetables crushed by the blunt impact crushing chamber can directly enter between the juicing turntable and the fixed millstone for grinding operation, and be extruded into strips under the action of the compression cover to be discharged directly for direct bagging . The juice produced during the crushing process and some unextruded pellets enter the filtrate separation chamber for separation treatment, thereby effectively avoiding environmental pollution. The device can process the crushed materials in a one-stop centralized manner. It does not require intermediate transportation links, can effectively save the transportation costs of intermediate links, can effectively reduce the labor load of workers, and can directly dispose of substances that may pollute the environment. It has good environmental protection performance. In addition, the device adopts automatic control, which can further reduce the labor workload of workers, and at the same time, can effectively ensure the treatment effect.

Further, in order to improve the separation effect, the interior of the filtrate separation chamber is sequentially provided with a liquid inlet buffer plate fixedly connected to the top, a mixing bucket fixedly connected to the upper part, and a muddy water buffer plate fixedly connected to the upper part of the middle part from top to bottom. , a through-hole plate fixedly connected in the middle, a stirring wheel rotatably arranged at the lower part and a sedimentation buffer plate fixedly connected at the lower end; the lower opening end of the filtrate separation chamber is fixedly connected with a funnel-shaped sedimentation chamber, The slag discharge pipe is connected through the bottom of the sedimentation chamber;

The stirring barrel is provided with a stirring shaft, the stirring shaft is equipped with stirring blades, and the stirring shaft is driven by a transmission motor; the stirring wheel is driven by a stirring motor;

The space between the mud-water buffer plate and the through-hole plate forms a buffer chamber; the liquid-inlet buffer plate, the mud-water buffer plate, the through-hole plate and the sedimentation buffer plate are all disc structures, and their surfaces are arranged with several through hole;

The transmission motor of the stirring motor is connected with the central controller by wires.

Further, in order to improve the treatment effect, the mixing tank is a cone with a large top and a small bottom, and its bottom and top are both open structures, and the inside of the bottom and the inside of the top are respectively provided with a medicament filling ring and a cleaning ring; The drug filling ring and the cleaning ring pipe are all hollow ring structures inside, and a number of spray heads are uniformly arranged at the lower end; the upper part of the buffer chamber is also connected with a clear water discharge pipe connected with its inner cavity;

The cleaning ring pipe and the medicament filling ring are respectively externally connected to the water adding pump and the drug adding pump; the water adding pump and the drug adding pump are connected to the central controller;

The stirring wheel is composed of several rectangular curved pipes, the number of which is not less than 6; the stirring blade is located on the inner central axis of the stirring barrel.

Further, in order to improve the connection strength and improve the treatment effect, the outer edge of the liquid inlet buffer plate, the outer edge of the top of the mixing bucket, the outer edge of the muddy water buffer plate, the outer edge of the through-hole plate, and the outer edge of the sedimentation chamber The edge and the inner wall of the filtrate separation chamber are seamlessly welded.

Further, in order to improve products with good extrusion degree and high compression output, the juice extracting turntable is composed of the following components in parts by weight:

Ultrasonic atomized gas-phase pure water 321.6~546.2 parts, methyl dodecyl siloxane 113.6~155.9 parts, 4-methoxy-α-methylphenylacetic acid methyl ester 116.0~225.9 parts, methyl n-hexane 112.2~ 129.1 parts, 115.8-172.9 parts of zymosan, 118.2-179.8 parts of 4,4'-(1-methylethylene) bisphenol and (chloromethyl) ethylene oxide and ethylene oxide polymer , 120.2-175.0 parts of sulfur nanoparticles, 113.5-155.3 parts of polysiloxane and silicone ether, 115.1-155.8 parts of polymers of formaldehyde, 1,3-dimethylbenzene and phenol, m-tert-butylphenylchlorothiomethyl 115.0-138.9 parts of acid ester, 104.7-140.8 parts of 2-[2-(2-methoxyethoxy)ethoxy]ethanol borate, 103.7-146.9 parts of 3-methyl-4-nitrobenzoic acid , 112.4-157.9 parts of N,N'-methyltetraylbis[4-[(4-isocyanatophenyl)methyl]-aniline, 122.1-166.1 parts of Pelargonium chrysanthemum extract, and the mass concentration is 112ppm-379ppm 145.5 to 199.3 parts of tert-butyl α-bromoisobutyrate.

Further, in order to improve products with good extrusion molding degree and high compression output, the manufacturing process of the juice extracting turntable includes the following steps:

Step 1: In the high-pressure stirred reactor, add ultrasonically atomized gas-phase pure water and methyl dodecyl siloxane, start the mixer in the high-pressure stirred reactor, set the speed at 114rpm-160rpm, and start the high-pressure Heating the oil temperature device in the stirring reactor to raise the temperature to 129.6°C~130.2°C, add 4-methoxy-α-methyl phenylacetate and stir evenly, carry out the reaction for 106.6~117.9 minutes, add methyl n-hexyl Alkanes, the flow rate of 105.8m ³ /min ~ 146.1m ³ /min hydrogen 106.6 ~ 117.9 minutes; then add zymosan in the high-pressure stirred reactor, start the heating oil temperature in the high-pressure stirred reactor again device, raise the temperature to 146.0°C~179.9°C, keep it warm for 106.2~117.1 minutes, add 4,4'-(1-methylethylene)bisphenol and (chloromethyl)oxirane and oxirane the polymer, adjust the pH value of the solution in the high-pressure stirred reactor to 4.8 to 8.9, and keep the temperature for 106.8 to 346.8 minutes;

Step 2: Take another sulfur nanoparticle, and after the sulfur nanoparticle is ultrasonically treated at a power of 6.46KW～11.9KW for 0.112～1.179 hours; add the sulfur nanoparticle into another high-pressure stirred reactor, and add a mass concentration of 116ppm～346ppm polysiloxane and silicone ether disperse sulfur nanoparticles, start the heating oil temperature device in the high-pressure stirred reactor, make the solution temperature between 48°C and 80°C, start the high-pressure stirred reactor Mixer, and stir at a speed of 4×10 ² rpm to 8×10 ² rpm, adjust the pH value between 4.7 and 8.8, keep stirring for 112 to 179 minutes; then stop the reaction and let stand for 6.46×10 to 11.9×10 minutes, Remove impurities; add formaldehyde, 1,3-dimethylbenzene and phenol polymer to the suspension, adjust the pH value between 1.7 and 2.8, and form a precipitate, which is eluted with ultrasonic atomized gas-phase pure water, and passed through a centrifuge in the The solids were obtained at a rotation speed of 4.620×10 ³ rpm to 9.936×10 ³ rpm, dried at a temperature of 2.761×10 ² ℃ to 3.510×10 ² ℃, ground and passed through a 0.620×10 ³ to 1.936×10 ³ mesh sieve, and used for later use;

Step 3: take m-tert-butylbenzene chlorothioformate and sulfur nanoparticles treated in step 2, mix them uniformly and irradiate with solar radiation reflection, the energy of solar radiation reflection irradiation is 103.7MeV～131.9MeV, The dosage is 151.7kGy～191.9kGy, and the irradiation time is 115.7～140.9 minutes, and the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles with changed properties is obtained; the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles The particle mixture is placed in another high-pressure stirred reactor, start the heating oil heater in the high-pressure stirred reactor, set the temperature at 114.4°C to 160.9°C, start the stirrer in the high-pressure stirred reactor, and rotate at a speed of 106rpm to 501rpm , adjust the pH to 4.1-8.1, dehydrate for 115.1-129.1 minutes, and set aside;

Step 4: Add the m-tert-butylbenzene chlorothioformate and sulfur nanoparticle mixture with the changed properties obtained in step 3 to 2-[2-(2-methoxyethane) with a mass concentration of 116ppm～346ppm Oxygen) ethoxy] ethanol borate, and flow into the high-pressure stirred reactor in the first step, the flow rate is 251mL/min～979mL/min; start the high-pressure stirred reactor mixer, set the speed 120rpm~160rpm; stir for 4~8 minutes; then add 3-methyl-4-nitrobenzoic acid, start the heating oil temperature device in the high-pressure stirred reactor, raise the temperature to 150.5°C~187.3°C, and adjust the pH to 4.5 Between ～8.3, the flow rate of hydrogen gas is 105.904m ³ /min～146.962m ³ /min, keep warm and stand for 140.6～170.2 minutes; start the high-pressure stirring reactor mixer again, the speed is 115rpm～160rpm, add N,N '-methyltetraylbis[4-[(4-isocyanatophenyl)methyl]-aniline, and adjust the pH to between 4.5 and 8.3, and keep the temperature for 139.6 to 179.9 minutes;

Step 5: Start the mixer in the high-pressure stirred reactor, set the rotating speed at 112rpm～179rpm, start the heating oil heater in the high-pressure stirred reactor, and set the temperature in the high-pressure stirred reactor to 1.603×10 ² ℃～2.118×10 ² ℃, add geranium chrysanthemum extract, react for 106.0～117.9 minutes; then add tert-butyl α-bromoisobutyrate, start the heating oil heater in the high-pressure stirring reactor, set high pressure The temperature in the stirred reactor is 190.2℃～246.1℃, the pH is adjusted to 4.8～8.8, the pressure is 1.12MPa～1.13MPa, and the reaction time is 0.4～0.9 hours; after that, the pressure is reduced to 0MPa, and the temperature is reduced to 106.0℃～117.9℃, the material is discharged into the compression molding machine, and the juicing turntable is obtained;

The particle size of the sulfur nanoparticles is 120 μm˜130 μm.

Aiming at the problems existing in the prior art, the present invention also provides a working method for a juicing device in fruit and vegetable processing, the method is simple in operation, high in automation, and can complete the crushing of materials to be crushed in a one-stop centralized manner. Processing work, and it will not pollute the environment.

In order to achieve the above object, the present invention provides a working method for a juice extraction device in fruit and vegetable processing, comprising the following steps:

Step 1: The staff presses the start button on the central controller, starts the control valve on the blunt impact crusher and the water inlet pipe, and puts the fruits and vegetables to be processed into the blunt impact crushing chamber through the fruit and vegetable feeding port for crushing, and at the same time Spray clean water in the bludgeoning crushing chamber, and the crushed fruits and vegetables enter the pellet feeding chamber under the action of the water body. Under the action, it is extruded into strips, and discharged from the compression hole on the side of the compression cover into the collection chamber, and finally enters the collection box through the fruit puree extrusion port. The mixture of uncompressed minced meat and juice often The filter screen flows down into the filtrate separation chamber;

Step 2: During the crushing process of fruits and vegetables to be broken in the bludgeoning crushing chamber, the crushing particle size detector located in the bludgeoning crushing chamber monitors the crushing particle size of fruits and vegetables in real time; when the crushing particle size detector detects that the crushing particle size of fruits and vegetables is less than 8cm, the broken particle size detector will feed back the detection signal to the central controller, and the central controller will reduce the speed of the blunt impact crusher and start the grinding motor at the same time;

Step 3: The material level gauge located in the pellet feeding chamber monitors the pellet material level height in real time; when the material level gauge detects that the pellet material level height is higher than the system set value L1, the material level gauge reports to the central controller After sending out an electric signal, the central controller reduces the speed of the blunt impact crusher after receiving the electric signal, and at the same time increases the speed of the grinding motor; The position meter sends an electric signal to the central controller 2, and the central controller increases the speed of the blunt impact crusher after receiving the electric signal, and at the same time reduces the speed of the grinding motor;

Step 4: The central controller starts the transmission motor, water pump and stirring motor at the same time, the mixture of uncompressed minced meat and juice enters the mixing tank through the liquid inlet buffer plate, and the clean water injected by the cleaning ring pipe The mixture enters the mixing barrel together, and rotates under the driving of the stirring blade, so as to achieve the purpose of centrifugation, so that the minced meat and juice are quickly separated once, and the separated juice quickly enters the buffer chamber through the mud buffer plate and is discharged through the clear water discharge pipe The separated minced meat is separated through the through-hole plate and rotated by the stirring wheel for secondary separation. After stirring, the sediment enters the sedimentation chamber through the sedimentation buffer plate for sedimentation;

Step 5: The slag water level gauge located in the filtrate separation chamber monitors the slag water level in the filtrate separation chamber in real time; when the slag water level gauge detects that the slag water level in the filtrate separation chamber is higher than the system set value, The slag water level gauge sends a feedback signal to the central controller, and the central controller opens the slag discharge pipe after receiving the electrical signal, and the slag water is discharged through the slag discharge pipeline.

The method has a simple operation process and a high degree of automation, can significantly improve production efficiency on the basis of effectively reducing labor intensity of workers, and will not pollute the environment.

Description of drawings

Fig. 1 is a structural representation of the present invention;

Fig. 2 is a schematic structural view of a bludgeoning crushing chamber in the present invention;

Fig. 3 is the structural representation of grinding mechanism among the present invention;

Fig. 4 is the structural representation of filtrate separation chamber among the present invention;

Fig. 5 is a graph showing the change of the corrosion resistance of the material of the juicing turntable according to the present invention with the use time.

In the figure: 1. Fruit and vegetable feeding port, 2. Crushing motor, 3. Blunt impact crushing chamber, 3-1, Crusher shaft, 3-2, Crushing hammer, 3-3, Crushing particle size detector, 3-4 , Water inlet pipe, 4, Grinding mechanism, 4-1, Pellet feed chamber, 4-2, Material level gauge, 4-3, Juicing turntable, 4-4, Collection chamber, 4-5, Filtrate separation chamber , 4-5-1, through-hole plate, 4-5-2, sedimentation chamber, 4-5-3, sedimentation buffer plate, 4-5-4, stirring wheel, 4-5-5, stirring Motor, 4-5-6, buffer chamber, 4-5-7, mud water buffer plate, 4-5-8, stirring blade, 4-5-9, cleaning ring pipe, 4-5-10, transmission motor, 4 -5-11, liquid inlet buffer plate, 4-5-12, mixing barrel, 4-5-13, clear water discharge pipe, 4-5-14, drug filling ring, 4-6, compression rotating shaft, 4- 7. Slag water level gauge, 4-8, slag discharge pipe, 4-9, fixed disc, 5, fruit puree extrusion port, 6, grinding motor, 7, transmission pulley, 8, stainless steel bracket, 9, central control device.

Detailed ways

The present invention will be further described below in conjunction with accompanying drawing.

As shown in Figures 1 to 3, a juicing device used in fruit and vegetable processing includes a crushing mechanism, a grinding mechanism 4, a central controller 9 and a stainless steel support 8 arranged at the bottom of the grinding mechanism 4, and the crushing mechanism includes a blunt The crushing chamber 3, the fruit and vegetable feeding port 1 arranged above one side of the bludgeoning chamber 3 and connected to the inner cavity of the bludgeoning chamber 3, the water inlet pipe 3-4 arranged on the upper side of the bludgeoning chamber 3 , the bludgeoning crusher 2 fixedly arranged on the top of the bludgeoning crushing chamber 3, the crusher rotating shaft 3-1 rotatably arranged at the center of the bludgeoning crushing chamber 3, the sieve plate fixedly arranged at the lower opening end of the bludgeoning crushing chamber 3; The upper end of the crusher rotating shaft 3-1 is connected to the output shaft of the blunt impact crusher 2, and the crusher rotating shaft 3-1 is evenly equipped with a plurality of crushing hammers 3-2 along its length direction;

The crushing mechanism also includes a crushing particle size detector 3-3 fixedly installed under the inner wall of the bludgeoning crushing chamber 3;

The grinding mechanism 4 includes a granular material feeding chamber 4-1 connected through the lower opening end of the blunt crushing chamber 3, a juicing turntable 4-3 rotatably arranged below the granular material feeding chamber 4-1, a fixed The fixed disc 4-9 that is arranged below the juicing turntable 4-3 and cooperates with it, is fixedly connected to the collection chamber 4-4 on the periphery of the bottom of the fixed disk 4-9, is arranged on the collection chamber 4-4- The fruit puree extrusion port 5 on the side, the material level gauge 4-2 arranged in the pellet feeding chamber 4-1, and the filtrate separation chamber 4 arranged at the bottom of the collecting chamber 4-4 in communication with the collecting chamber 4-4 -5, the compression rotating shaft 4-6 arranged in the filtrate separation chamber 4-5, the slag water level gauge 4-7 installed in the filtrate separation chamber 4-5, and the drain set at the bottom of the filtrate separation chamber 4-5 The slag pipe 4-8, the grinding motor 6 arranged on one side of the bludgeoning crushing chamber 3;

The juicing turntable 4-3 is longitudinally provided with at least one discharge hole connected to its lower surface; It consists of a fixed grinding disc, a compression cover surrounding the fixed grinding disc, and a support platform carrying the fixed discs 4-9 and the compression cover. There is a gap between the compression cover and the fixed grinding disc. Several compression holes communicated with its inner cavity are evenly arranged; the feeding part of the collection chamber 4-4 is located at its upper part and is arranged around the compression cover, the collection chamber 4-4 and the filtrate separation chamber 4-5 The connecting parts between are provided with a filter screen; the center of the juicing turntable 4-3 is disassembled and connected with a compression rotating shaft 4-6; Installed in the juicing turntable 4-3, the bottom end of the compression rotating shaft 4-6 is equipped with a slave transmission pulley; the output shaft of the grinding motor 6 is equipped with a main transmission pulley, and the main transmission pulley passes through the transmission pulley 7 and the slave transmission Belt pulley connection; the lower surface of the juicing turntable 4-3 and the upper surface of the fixed grinding disc are all provided with mutually matching grinding teeth;

The broken particle size detector 3-3, blunt impact crusher 2, material level gauge 4-2, slag water level gauge 4-7, grinding motor 6, electromagnetic valve on the slag discharge pipe 4-8, water inlet pipe The control valves on the 3-4 are respectively controlled and connected with the central controller 9 by wires.

As shown in Figure 4, the interior of the filtrate separation chamber 4-5 is sequentially provided with a liquid inlet buffer plate 4-5-11 fixedly connected to the top, and a mixing bucket 4-5-12 fixedly connected to the top. , the mud-water buffer plate 4-5-7 fixedly connected to the upper position of the middle part, the through-hole plate 4-5-1 fixedly connected to the middle part, the stirring wheel 4-5-4 rotatably arranged at the lower part and fixedly connected to the The sedimentation buffer plate 4-5-3 at the lower end; the lower opening end of the filtrate separation chamber 4-5 is fixedly connected with a funnel-shaped sedimentation chamber 4-5-2, and the slag discharge pipe 4-8 is connected to the bottom The bottom of the mud settling chamber 4-5-2 is connected throughly;

The mixing barrel 4-5-12 is provided with a stirring shaft, the stirring shaft is equipped with a stirring blade 4-5-8, and the stirring shaft is driven by a transmission motor 4-5-10; the stirring wheel 4-5- 4 Driven by stirring motor 4-5-5;

The space between the mud buffer plate 4-5-7 and the through-hole plate 4-5-1 forms a buffer chamber 4-5-6; the liquid inlet buffer plate 4-5-11, mud water buffer plate 4-5 -7. Both the through-hole plate 4-5-1 and the sedimentation buffer plate 4-5-3 are disc structures, and a number of through-holes are arranged on the surface;

The stirring motor 4-5-5 transmission motor 4-5-10 is connected with the central controller 9 wires.

The bludgeoning crushing chamber 3 is a stainless steel cylindrical structure; the bludgeoning crusher 2 is a frequency conversion motor; the angle between the fruit and vegetable feeding port 1 and the horizontal plane is 30°, and a slideway is provided inside the fruit and vegetable feeding port 1; The fruit paste extrusion port 5 is a bucket-shaped structure; the material of the crusher shaft 3-1 is manganese steel; the crushing hammer 3-2 is a trapezoidal thin plate structure; the crushing hammer 3-2 and the crusher shaft 3- 1 connected by bolts, the number of the broken hammers 3-2 is not less than 15 pieces.

The pellet feeding chamber 4-1 is a cylindrical structure; the stainless steel bracket 8 is made of galvanized material; the central controller 9 is fixedly installed on the stainless steel bracket 8 .

The mixing barrel 4-5-12 is a cone with a large top and a small bottom, and its bottom and top are open structures, and the inside of the bottom and the inside of the top are respectively provided with medicament filling rings 4-5-14, cleaning The ring pipe 4-5-9; the drug filling ring 4-5-14 and the cleaning ring pipe 4-5-9 are all hollow ring structures inside, and a number of spray heads are evenly arranged at the lower end; The upper part of the buffer chamber 4-5-6 is also communicated with a clear water discharge pipe 4-5-13 communicating with its inner cavity;

The cleaning ring pipe 4-5-9 and the medicament filling ring 4-5-14 are respectively externally connected to a water adding pump and a drug adding pump; the water adding pump and the drug adding pump are connected to the central controller 9;

The stirring wheel 4-5-4 is composed of several rectangular bent pipes, the number of which is not less than 6; the stirring blade 4-5-8 is located on the inner central axis of the stirring barrel 4-5-12.

The outer edge of the liquid inlet buffer plate 4-5-11, the outer edge of the mixing bucket 4-5-12 top, the outer edge of the muddy water buffer plate 4-5-7, the outer edge of the through-hole plate 4-5-1 1. The outer edge of the sedimentation chamber 4-5-2 is seamlessly welded to the inner wall of the filtrate separation chamber 4-5.

The juicing turntable 4-3 consists of the following components in parts by weight:

Ultrasonic atomized gas-phase pure water 321.6~546.2 parts, methyl dodecyl siloxane 113.6~155.9 parts, 4-methoxy-α-methylphenylacetic acid methyl ester 116.0~225.9 parts, methyl n-hexane 112.2~ 129.1 parts, 115.8-172.9 parts of zymosan, 118.2-179.8 parts of 4,4'-(1-methylethylene) bisphenol and (chloromethyl) ethylene oxide and ethylene oxide polymer , 120.2-175.0 parts of sulfur nanoparticles, 113.5-155.3 parts of polysiloxane and silicone ether, 115.1-155.8 parts of polymers of formaldehyde, 1,3-dimethylbenzene and phenol, m-tert-butylphenylchlorothiomethyl 115.0-138.9 parts of acid ester, 104.7-140.8 parts of 2-[2-(2-methoxyethoxy)ethoxy]ethanol borate, 103.7-146.9 parts of 3-methyl-4-nitrobenzoic acid , 112.4-157.9 parts of N,N'-methyltetraylbis[4-[(4-isocyanatophenyl)methyl]-aniline, 122.1-166.1 parts of Pelargonium chrysanthemum extract, and the mass concentration is 112ppm-379ppm 145.5 to 199.3 parts of tert-butyl α-bromoisobutyrate.

The manufacturing process of the said juicing turntable 4-3 comprises the following steps:

Step 1: In the high-pressure stirred reactor, add ultrasonically atomized gas-phase pure water and methyl dodecyl siloxane, start the mixer in the high-pressure stirred reactor, set the speed at 114rpm-160rpm, and start the high-pressure Heating the oil temperature device in the stirring reactor to raise the temperature to 129.6°C~130.2°C, add 4-methoxy-α-methyl phenylacetate and stir evenly, carry out the reaction for 106.6~117.9 minutes, add methyl n-hexyl Alkanes, the flow rate of 105.8m ³ /min ~ 146.1m ³ /min hydrogen 106.6 ~ 117.9 minutes; then add zymosan in the high-pressure stirred reactor, start the heating oil temperature in the high-pressure stirred reactor again device, raise the temperature to 146.0°C~179.9°C, keep it warm for 106.2~117.1 minutes, add 4,4'-(1-methylethylene)bisphenol and (chloromethyl)oxirane and oxirane the polymer, adjust the pH value of the solution in the high-pressure stirred reactor to 4.8 to 8.9, and keep the temperature for 106.8 to 346.8 minutes;

Step 2: Take another sulfur nanoparticle, and after the sulfur nanoparticle is ultrasonically treated at a power of 6.46KW～11.9KW for 0.112～1.179 hours; add the sulfur nanoparticle into another high-pressure stirred reactor, and add a mass concentration of 116ppm～346ppm polysiloxane and silicone ether disperse sulfur nanoparticles, start the heating oil temperature device in the high-pressure stirred reactor, make the solution temperature between 48°C and 80°C, start the high-pressure stirred reactor Mixer, and stir at a speed of 4×10 ² rpm to 8×10 ² rpm, adjust the pH value between 4.7 and 8.8, keep stirring for 112 to 179 minutes; then stop the reaction and let stand for 6.46×10 to 11.9×10 minutes, Remove impurities; add formaldehyde, 1,3-dimethylbenzene and phenol polymer to the suspension, adjust the pH value between 1.7 and 2.8, and form a precipitate, which is eluted with ultrasonic atomized gas-phase pure water, and passed through a centrifuge in the The solids were obtained at a rotation speed of 4.620×10 ³ rpm to 9.936×10 ³ rpm, dried at a temperature of 2.761×10 ² ℃ to 3.510×10 ² ℃, ground and passed through a 0.620×10 ³ to 1.936×10 ³ mesh sieve, and used for later use;

Step 3: take m-tert-butylbenzene chlorothioformate and sulfur nanoparticles treated in step 2, mix them uniformly and irradiate with solar radiation reflection, the energy of solar radiation reflection irradiation is 103.7MeV～131.9MeV, The dosage is 151.7kGy～191.9kGy, and the irradiation time is 115.7～140.9 minutes, and the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles with changed properties is obtained; the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles The particle mixture is placed in another high-pressure stirred reactor, start the heating oil heater in the high-pressure stirred reactor, set the temperature at 114.4°C to 160.9°C, start the stirrer in the high-pressure stirred reactor, and rotate at a speed of 106rpm to 501rpm , adjust the pH to 4.1-8.1, dehydrate for 115.1-129.1 minutes, and set aside;

Step 4: Add the m-tert-butylbenzene chlorothioformate and sulfur nanoparticle mixture with the changed properties obtained in step 3 to 2-[2-(2-methoxyethane) with a mass concentration of 116ppm～346ppm Oxygen) ethoxy] ethanol borate, and flow into the high-pressure stirred reactor in the first step, the flow rate is 251mL/min～979mL/min; start the high-pressure stirred reactor mixer, set the speed 120rpm~160rpm; stir for 4~8 minutes; then add 3-methyl-4-nitrobenzoic acid, start the heating oil temperature device in the high-pressure stirred reactor, raise the temperature to 150.5°C~187.3°C, and adjust the pH to 4.5 Between ～8.3, the flow rate of hydrogen gas is 105.904m ³ /min～146.962m ³ /min, keep warm and stand for 140.6～170.2 minutes; start the high-pressure stirring reactor mixer again, the speed is 115rpm～160rpm, add N,N '-methyltetraylbis[4-[(4-isocyanatophenyl)methyl]-aniline, and adjust the pH to between 4.5 and 8.3, and keep the temperature for 139.6 to 179.9 minutes;

Step 5: Start the mixer in the high-pressure stirred reactor, set the rotating speed at 112rpm～179rpm, start the heating oil heater in the high-pressure stirred reactor, and set the temperature in the high-pressure stirred reactor to 1.603×10 ² ℃～2.118×10 ² ℃, add geranium chrysanthemum extract, react for 106.0～117.9 minutes; then add tert-butyl α-bromoisobutyrate, start the heating oil heater in the high-pressure stirring reactor, set high pressure The temperature in the stirred reactor is 190.2℃～246.1℃, the pH is adjusted to 4.8～8.8, the pressure is 1.12MPa～1.13MPa, and the reaction time is 0.4～0.9 hours; after that, the pressure is reduced to 0MPa, and the temperature is reduced to 106.0°C～117.9°C discharge the material into the compression molding machine to obtain the juicing turntable 4-3 ;

The particle size of the sulfur nanoparticles is 120 μm˜130 μm.

The following are examples of the manufacturing process of the juicing turntable 4-3 of the present invention. The examples are to further illustrate the content of the present invention, but should not be construed as limiting the present invention. Without departing from the spirit and essence of the present invention, the modifications and substitutions made to the methods, steps or conditions of the present invention all belong to the scope of the present invention.

Unless otherwise specified, the technical means used in the embodiments are conventional means well known to those skilled in the art.

Example 1

Prepare the juicing turntable 4-3 of the present invention according to the following steps, and count in parts by weight:

Step 1: In the high-pressure stirred reactor, add 321.6 parts of ultrasonically atomized gas-phase pure water and 113.6 parts of methyl dodecyl siloxane, start the mixer in the high-pressure stirred reactor, set the speed at 114rpm, Start the heating oil heater in the high-pressure stirring reactor, raise the temperature to 129.6°C, add 116.0 parts of 4-methoxy-α-methylphenylacetic acid methyl ester and stir evenly, carry out the reaction for 106.6 minutes, add methyl n-hexane 112.2 parts, the feed flow rate is 105.8m ³ /min of hydrogen for 106.6 minutes; add 115.8 parts of zymosan in the high-pressure stirred reactor afterwards, start the heating oil temperature device in the high-pressure stirred reactor again, make the temperature rise To 146.0°C, keep warm for 106.2 minutes, add 118.2 parts of polymers of 4,4'-(1-methylethylene)bisphenol, (chloromethyl)ethylene oxide and ethylene oxide, and adjust high-pressure stirring The pH value of the solution in the reactor is 4.8, and it is incubated for 106.8 minutes;

Step 2: Take another 120.2 parts of sulfur nanoparticles, and after the sulfur nanoparticles are ultrasonically treated at a power of 6.46KW for 0.112 hours; the sulfur nanoparticles are added to another high-pressure stirred reactor, and the addition of the polymer with a mass concentration of 116ppm Siloxane and silicone ether 113.5 parts disperse sulfur nanoparticles, start the heating oil temperature device in the high-pressure stirred reactor, make the solution temperature at 48 ° C, start the stirrer in the high-pressure stirred reactor, and use 4 × 10 ² Stir at the speed of rpm, adjust the pH value to 4.7, keep stirring for 112 minutes; then stop the reaction and let it stand for 6.46×10 minutes to remove impurities; add 115.1 parts of polymers of formaldehyde, 1,3-dimethylbenzene and phenol to the suspension , adjust the pH value at 1.7, and form a precipitate, which is eluted with ultrasonically atomized gas-phase pure water. The solid is obtained by a centrifuge at a speed of 4.620×10 ³ rpm, dried at a temperature of 2.761×10 ² ℃, and ground at a temperature of 0.620× 10 ³ -mesh sieve, spare;

Step 3: Take m-tert-butylbenzene chlorothioformate 115.0 and sulfur nanoparticles treated in step 2 in addition, mix them uniformly and use solar radiation reflection irradiation, the energy of solar radiation reflection irradiation is 103.7MeV, and the dose is 151.7kGy, the irradiation time is 115.7 minutes, and the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles with changed properties is obtained; the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles is placed at another high pressure In the high-pressure stirred reactor, start the heating oil heater in the high-pressure stirred reactor, set the temperature at 114.4°C, start the stirrer in the high-pressure stirred reactor, the speed is 106rpm, adjust the pH to 4.1, dehydrate for 115.1 minutes, and set aside;

The 4th step: the m-tert-butylbenzene chlorothioformate and the sulfur nanoparticle mixture that the properties obtained in the 3rd step are changed are added to the 2-[2-(2-methoxyethoxy group whose mass concentration is 116ppm ) Ethoxyl group] in 104.7 parts of ethanol borate, and flow into the high-pressure stirred reactor of the first step, the flow rate is 251mL/min; start the high-pressure stirred reactor stirrer, and the set speed is 120rpm; Stir 4 minutes; then add 103.7 parts of 3-methyl-4-nitrobenzoic acid, start the heating oil temperature device in the high-pressure stirring reactor, raise the temperature to 150.5°C, adjust the pH to 4.5, and feed the hydrogen gas to a flow rate of 105.904m ³ /min, heat preservation and stand still for 140.6 minutes; start the high-pressure stirring reactor mixer again, the speed is 115rpm, add N,N'-methanetetrayl bis[4-[(4-isocyanatophenyl)methyl] - 112.4 parts of aniline, and the pH was adjusted to 4.5, and the heat preservation was left to stand for 139.6 minutes;

Step 5: start the stirrer in the high-pressure stirred reactor, set the rotating speed to be 112rpm, start the heating oil temperature device in the high-pressure stirred reactor, and set the temperature in the high-pressure stirred reactor to be 1.603×10 ² ℃, Add 122.1 parts of geranium chrysanthemum extract, and react for 106.0 minutes; then add 145.5 parts of α-bromoisobutyrate tert-butyl ester with a mass concentration of 112ppm, start the heating oil temperature device in the high-pressure stirring reactor, and set the high-pressure type The temperature in the stirring reactor is 190.2°C, the pH is adjusted to 4.8, the pressure is 1.12MPa, and the reaction time is 0.4 hours; after that, the pressure is reduced to 0MPa, the temperature is lowered to 106.0°C, and the material is discharged into the compression molding machine, and the squeezed juice is obtained Turntable 4-3 ;

The particle size of the sulfur nanoparticles is 120 μm.

Example 2

Prepare the juicing turntable 4-3 of the present invention according to the following steps, and count in parts by weight:

Step 1: In the high-pressure stirred reactor, add 546.2 parts of ultrasonically atomized gas-phase pure water and 155.9 parts of methyl dodecyl siloxane, start the mixer in the high-pressure stirred reactor, set the speed at 160rpm, Start the heating oil heater in the high-pressure stirring reactor, raise the temperature to 130.2°C, add 225.9 parts of 4-methoxy-α-methylphenylacetic acid methyl ester and stir evenly, carry out the reaction for 117.9 minutes, add methyl n-hexane 129.1 parts, the feed flow rate is 146.1m ³ /min of hydrogen for 117.9 minutes; add 172.9 parts of zymosan in the high-pressure stirred reactor afterwards, start the heating oil temperature device in the high-pressure stirred reactor again, make the temperature rise To 179.9°C, keep warm for 117.1 minutes, add 179.8 parts of polymers of 4,4'-(1-methylethylene) bisphenol, (chloromethyl) ethylene oxide and ethylene oxide, and adjust high-pressure stirring The pH value of the solution in the reactor is 8.9, and it is incubated for 346.8 minutes;

Step 2: Take another 175.0 parts of sulfur nanoparticles, and after the sulfur nanoparticles are ultrasonically treated for 1.179 hours at a power of 11.9KW; the sulfur nanoparticles are added to another high-pressure stirred reactor, and the addition of a mass concentration of 346ppm poly Siloxane and silicone ether 155.3 parts disperse sulfur nanoparticles, start the heating oil temperature device in the high-pressure stirred reactor, make the solution temperature between 80 ℃, start the stirrer in the high-pressure stirred reactor, and use 8× Stir at a speed of 10 ² rpm, adjust the pH value to 8.8, keep stirring for 179 minutes; then stop the reaction and let stand for 11.9×10 minutes to remove impurities; add formaldehyde, 1,3-dimethylbenzene and phenol polymer to the suspension 155.8 parts, adjusted the pH value at 2.8, and the precipitate formed was eluted with ultrasonic atomized gas-phase pure water, and the solid was obtained by a centrifuge at a speed of 9.936×10 ³ rpm, dried at a temperature of 3.510×10 ² ℃, and ground 1.936×10 ³ -mesh sieve, spare;

Step 3: Take another 138.9 parts of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles after the treatment in step 2, mix them uniformly and irradiate with solar radiation reflection, the energy of solar radiation reflection radiation is 131.9MeV, dose Be 191.9kGy, irradiation time be 140.9 minutes, obtain the m-tert-butylbenzene chlorothioformate and the sulfur nanoparticle mixture of character change; Put the m-tert-butylbenzene chlorothioformate and sulfur nanoparticle mixture in another In the high-pressure stirred reactor, start the heating oil heater in the high-pressure stirred reactor, set the temperature at 160.9°C, start the stirrer in the high-pressure stirred reactor, the speed is 501rpm, adjust the pH to 8.1, dehydrate for 129.1 minutes, and set aside ;

The 4th step: the m-tert-butylbenzene chlorothioformate and the sulfur nanoparticle mixture that the properties obtained in the 3rd step are changed are added to the 2-[2-(2-methoxyethoxy group whose mass concentration is 346ppm ) Ethoxyl] in 140.8 parts of ethanol borate, and flow into the high-pressure stirred reactor of the first step, the flow rate is 979mL/min; start the high-pressure stirred reactor mixer, and the set speed is 160rpm; stir 8 minutes; then add 146.9 parts of 3-methyl-4-nitrobenzoic acid, start the heating oil temperature device in the high-pressure stirring reactor, raise the temperature to 187.3°C, adjust the pH to 8.3, and feed the hydrogen gas to a flow rate of 146.962m ³ /min, heat preservation and standing for 170.2 minutes; start the high-pressure stirring reactor mixer again, the speed is 160rpm, add N,N'-methanetetrayl bis[4-[(4-isocyanatophenyl)methyl] - 157.9 parts of aniline, and the pH was adjusted to 8.3, and the heat preservation was left to stand for 179.9 minutes;

Step 5: Start the stirrer in the high-pressure stirred reactor, set the rotating speed to 179rpm, start the heating oil temperature device in the high-pressure stirred reactor, and set the temperature in the high-pressure stirred reactor to be 2.118×10 ² ℃, Add 166.1 parts of geranium chrysanthemum extract, and react for 117.9 minutes; then add 199.3 parts of α-bromoisobutyrate tert-butyl ester with a mass concentration of 379ppm, start the heating oil temperature device in the high-pressure stirring reactor, and set the high-pressure type The temperature in the stirred reactor is 246.1°C, the pH is adjusted to 8.8, the pressure is 1.13MPa, and the reaction time is 0.9 hours; after that, the pressure is reduced to 0MPa, the temperature is lowered to 117.9°C, and the material is discharged into the compression molding machine, and the squeezed juice is obtained Turntable 4-3 ;

The particle size of the sulfur nanoparticles is 130 μm.

Example 3

Prepare the juicing turntable 4-3 of the present invention according to the following steps, and count in parts by weight:

Step 1: In the high-pressure stirred reactor, add 321.9 parts of ultrasonically atomized gas-phase pure water and 113.9 parts of methyl dodecyl siloxane, start the mixer in the high-pressure stirred reactor, set the speed at 114rpm, Start the heating oil heater in the high-pressure stirring reactor, raise the temperature to 129.9°C, add 116.9 parts of 4-methoxy-α-methylphenylacetic acid methyl ester and stir evenly, carry out the reaction for 106.9 minutes, add methyl n-hexane 112.9 parts, the feed flow rate is 105.9m ³ /min of hydrogen for 106.9 minutes; then add 115.9 parts of zymosan in the high-pressure stirred reactor, start the heating oil temperature device in the high-pressure stirred reactor again, make the temperature rise To 146.9°C, keep warm for 106.9 minutes, add 118.9 parts of polymers of 4,4'-(1-methylethylene) bisphenol, (chloromethyl) ethylene oxide and ethylene oxide, and adjust the high-pressure stirring The pH value of the solution in the reactor is 4.9, and it is incubated for 106.9 minutes;

Step 2: Take another 120.9 parts of sulfur nanoparticles, and after the sulfur nanoparticles are ultrasonically treated for 0.1129 hours at a power of 6.469KW; the sulfur nanoparticles are added to another high-pressure stirred reactor, and the mass concentration is 116.9ppm Polysiloxane and silicone ether 113.9 parts disperse sulfur nanoparticles, start the heating oil temperature device in the high-pressure stirred reactor, make the solution temperature at 48.9 ° C, start the stirrer in the high-pressure stirred reactor, and use 4.9 × 10 Stir at a speed of ² rpm, adjust the pH value to 4.9, keep stirring for 112.9 minutes; then stop the reaction and let stand for 6.46×10 minutes to remove impurities; add formaldehyde, 1,3-dimethylbenzene and phenol to the polymer 115.9 part, adjust the pH value at 1.9, and form a precipitate, which is eluted with ultrasonically atomized gas-phase pure water. The solid is obtained by a centrifuge at a speed of 4.620×10 ³ rpm, dried at a temperature of 2.761×10 ² ℃, and ground at a temperature of 0.620 ×10 ³ -mesh sieve, spare;

Step 3: Take m-tert-butylbenzene chlorothioformate 115.9 in addition and sulfur nanoparticles after step 2 treatment, mix uniformly and adopt solar radiation reflection irradiation, the energy of solar radiation reflection irradiation is 103.9MeV, and the dose is 151.9kGy, the irradiation time is 115.9 minutes, and the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles with changed properties is obtained; the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles is placed at another high pressure In the high-pressure stirred reactor, start the heating oil heater in the high-pressure stirred reactor, set the temperature at 114.9°C, start the stirrer in the high-pressure stirred reactor, the speed is 106rpm, adjust the pH to 4.9, dehydrate for 115.9 minutes, and set aside;

Step 4: Add the m-tert-butylbenzene chlorothioformate and sulfur nanoparticle mixture with the changed properties obtained in step 3 to 2-[2-(2-methoxyethoxy) with a mass concentration of 116.9ppm base) ethoxyl] ethanol borate 104.9 parts, and flow into the high-pressure stirred reactor of the first step, the flow rate is 251.9mL/min; start the high-pressure stirred reactor mixer, set the speed at 120rpm Stir for 4.9 minutes; Add 103.9 parts of 3-methyl-4-nitrobenzoic acid again, start the heating oil temperature device in the high-pressure stirred reactor, heat up to 150.9 ° C, adjust the pH to 4.9, and feed the hydrogen gas flow rate of 105.9m ³ /min, heat preservation and standing for 140.9 minutes; start the high-pressure stirring reactor mixer again, the speed is 115rpm, add N,N'-methanetetraylbis[4-[(4-isocyanatophenyl)formazol base]-aniline 112.9 parts, and make the pH adjusted to 4.9, keep the heat preservation and stand for 139.9 minutes;

Step 5: start the stirrer in the high-pressure stirred reactor, set the rotating speed to be 112rpm, start the heating oil temperature device in the high-pressure stirred reactor, and set the temperature in the high-pressure stirred reactor to be 1.603×10 ² ℃, Add 122.9 parts of geranium chrysanthemum extract, and react for 106.9 minutes; then add 145.5 parts of α-bromoisobutyrate tert-butyl ester with a mass concentration of 112ppm, start the heating oil temperature device in the high-pressure stirring reactor, and set the high-pressure type The temperature in the stirred reactor is 190.9°C, the pH is adjusted to 4.9, the pressure is 1.12MPa, and the reaction time is 0.41 hours; after that, the pressure is reduced to 0MPa, the temperature is lowered to 106.9°C, and the material is discharged into the compression molding machine, and the squeezed juice is obtained Turntable 4-3;

The particle size of the sulfur nanoparticles is 120 μm.

Comparative example

The comparative example is a commercially available juicing turntable of a certain brand.

Example 4

The juicing turntable 4-3 prepared in Examples 1-3 was compared with the juicing turntable described in the comparative example. The compression duty ratio, extrusion degree, compression output increase rate, and material wear rate of the two are counted, and the results are shown in Table 1.

It can be seen from Table 1 that the juicing turntable 4-3 of the present invention has better indicators such as compression duty ratio, extrusion degree, compression output increase rate, and material wear rate than products produced in the prior art.

In addition, as shown in Fig. 5, it is the statistics of the corrosion resistance of the material of the juicing turntable 4-3 according to the present invention changing with the use time. It can be seen from the figure that the juice-extracting turntable 4-3 used in Examples 1-3 is much better than the existing products in terms of corrosion resistance of the material as a function of time of use.

A working method for a juicing device in fruit and vegetable processing, comprising the following steps:

Step 1: The worker presses the start button on the central controller 9 to start the control valve on the blunt impact crusher 2 and the water inlet pipe 3-4, and feeds the fruits and vegetables to be processed into the blunt impact crushing chamber 3 through the fruit and vegetable feeding port 1 crushing process in the center, and spray clean water into the blunt crushing chamber 3 at the same time, the crushed fruits and vegetables enter the pellet feeding chamber 4-1 under the action of the water body, and under the joint action of the juicing turntable 4-3 and the fixed grinding disc , the crushed fruits and vegetables are ground and squeezed into strips under the action of the compression cover, and discharged from the compression hole on the side of the compression cover into the collection chamber 4-4, and finally passed through the fruit puree The extrusion port 5 enters the collection box, and the mixture of uncompressed minced meat and juice often flows downward through the filter screen into the filtrate separation chamber 4-5;

Step 2: During the crushing process of the fruits and vegetables to be crushed in the bludgeoning crushing chamber 3, the crushing particle size detector 3-3 located in the bludgeoning crushing chamber 3 monitors the crushing particle size of the fruits and vegetables in real time; when the crushing particle size detector 3-3 3. When it is detected that the broken particle size of fruits and vegetables is less than 8 cm, the broken particle size detector 3-3 feeds back the detection signal to the central controller 9, and the central controller 9 reduces the speed of the blunt impact crusher 2 and starts the grinding motor 6 at the same time;

Step 3: The material level gauge 4-2 located in the pellet feeding chamber 4-1 monitors the pellet material level height in real time; when the material level gauge 4-2 detects that the pellet material level height is higher than the system set value During L1, the material level gauge 4-2 sends an electrical signal to the central controller 9, and the central controller 9 reduces the speed of the blunt impact crusher 2 after receiving the electrical signal, and simultaneously increases the grinding motor 6 speed; when the material level gauge 4-2 When it is detected that the material level of the pellets is lower than the system setting value L2, the material level gauge 4-2 sends an electric signal 2 to the central controller 9, and the central controller 9 increases the speed of bludgeoning after receiving the electric signal. Machine 2 speed, reduce grinding motor 6 speed at the same time;

Step 4: The central controller 9 simultaneously starts the transmission motor 4-5-10, the water adding pump and the stirring motor 4-5-5, and the mixture of uncompressed minced meat and juice goes down through the liquid inlet buffer plate 4-5- 11 Enter the mixing tank 4-5-12, and at the same time, the clean water injected by the cleaning ring pipe 4-5-9 enters the mixing tank 4-5-12 together with the mixture, and is driven by the mixing blade 4-5-8 Rotate, and then achieve the purpose of centrifugation, so that the minced meat and juice are quickly separated once, and the separated juice quickly passes through the mud-water buffer plate 4-5-7 and enters the buffer chamber 4-5-6 and then passes through the clear water discharge pipe 4-5-13 Discharge; the separated minced meat is separated through the through-hole plate 4-5-1 and rotated by the stirring wheel 4-5-4 for secondary separation. After stirring, the sediment settles through the bottom mud buffer plate 4-5-3 Enter the sedimentation chamber 4-5-2 for sedimentation;

Step 5: The slag water level gauge 4-7 located in the filtrate separation chamber 4-5 monitors the slag water level situation in the filtrate separation chamber 4-5 in real time; when the slag water level gauge 4-7 detects that the filtrate is separated When the slag water level in chamber 4-5 is higher than the system setting value, the slag water level gauge 4-7 sends a feedback signal to the central controller 9, and the central controller 9 opens the slag discharge pipe after receiving the electrical signal 4-8, the slag water is discharged through the slag discharge pipeline.

Wherein the dosing pump and the medicament filling ring 4-5-14 are used for adding cleaning liquid when the filtrate separation chamber 4-5 is cleaned, so that the filtrate separation chamber 4-5 is cleaned more thoroughly.

Claims (7)

1. A juice extraction device used in fruit and vegetable processing, comprising a crushing mechanism, a grinding mechanism (4) and a stainless steel support (8) arranged at the bottom of the grinding mechanism (4), said crushing mechanism comprising a bludgeoning crushing chamber (3) , a fruit and vegetable feeding port (1) arranged above one side of the blunt crushing chamber (3) and connected to the inner cavity of the blunt crushing chamber (3), an inlet arranged on the upper side of the blunt crushing chamber (3) a water pipe (3-4), a bludgeon crusher (2) fixedly arranged on the top of the bludgeon crushing chamber (3), a crusher shaft (3-1) rotatably arranged at the center of the bludgeon crushing chamber (3), The sieve plate fixedly arranged at the lower opening end of the bludgeoning crushing chamber (3); the upper end of the crusher shaft (3-1) is connected to the output shaft of the bludgeoning crusher (2), and the crusher shaft (3-1) A plurality of crushing hammers (3-2) are uniformly set in the length direction; the feature is that it also includes a central controller (9); The crushing mechanism also includes a crushing particle size detector (3-3) fixedly installed under the inner wall of the bludgeoning crushing chamber (3); The grinding mechanism (4) includes a pellet feeding chamber (4-1) connected through the lower opening end of the blunt crushing chamber (3), and a rotatably arranged below the pellet feeding chamber (4-1). The juicing turntable (4-3), the fixed disc (4-9) fixedly arranged under the juicing turntable (4-3) and matched with it, the fixed disc (4-9) fixedly connected to the lower periphery of the fixed disc (4-9) The collection chamber (4-4), the fruit paste extrusion port (5) arranged on one side of the collection chamber (4-4), the level gauge (4-1) arranged in the pellet feeding chamber (4-1) 2), the filtrate separation chamber (4-5) arranged at the bottom of the collection chamber (4-4) communicated with the collection chamber (4-4), the compression rotating shaft arranged in the filtrate separation chamber (4-5) (4-6), the slag water level gauge (4-7) installed in the filtrate separation chamber (4-5), the slag discharge pipe (4-8) arranged at the bottom of the filtrate separation chamber (4-5), A grinding motor (6) arranged on one side of the bludgeoning crushing chamber (3); The longitudinal direction of the juicing turntable (4-3) is provided with at least one feeding hole connected to its lower surface; -3) It consists of a matching fixed grinding disc, a compression cover surrounding the periphery of the fixed grinding disc, and a support platform carrying the fixed disc (4-9) and the compression cover, and the compression cover and the fixed grinding disc are in clearance fit , the compression cover body is evenly arranged with several compression holes communicating with its inner cavity along its circumference; (4-4) and the filtrate separation chamber (4-5) are provided with a filter screen; the center of the juicing turntable (4-3) is disassembled and connected with a compression rotating shaft (4-6); the compression The upper end of the rotating shaft (4-6) rotatably passes through the support platform and the fixed grinding disc and is installed in the juice-extracting turntable (4-3), and the bottom end of the compressed rotating shaft (4-6) is equipped with a transmission pulley; A main transmission pulley is installed on the output shaft of the grinding motor (6), and the main transmission pulley is connected with the slave transmission pulley by a transmission pulley (7); Both are equipped with grinding teeth that cooperate with each other; The broken particle size detector (3-3), blunt impact crusher (2), material level gauge (4-2), slag water level gauge (4-7), grinding motor (6), slag discharge pipe The solenoid valve on (4-8) and the control valve on the water inlet pipe (3-4) are controlled and connected with central controller (9) by wire respectively; The pellet feeding chamber (4-1) is a cylindrical structure; the stainless steel bracket (8) is made of galvanized material; the grinding motor (6) and the central controller (9) are fixedly installed on the stainless steel bracket (8). 2. A juice extraction device for fruit and vegetable processing according to claim 1, characterized in that, the interior of the filtrate separation chamber (4-5) is sequentially provided with liquid inlets fixedly connected to the top The buffer plate (4-5-11), the mixing bucket (4-5-12) fixedly connected to the upper part, the muddy water buffer plate (4-5-7) fixedly connected to the upper part of the middle part, and the communication tank fixedly connected to the middle part The orifice plate (4-5-1), the stirring wheel (4-5-4) which is rotatably arranged at the lower part and the sedimentation buffer plate (4-5-3) fixedly connected at the lower end; the filtrate separation chamber (4-5-3) -5) The lower opening end is fixedly connected with a funnel-shaped sedimentation chamber (4-5-2), the bottom of the slag discharge pipe (4-8) and the sedimentation chamber (4-5-2) connect through The stirring barrel (4-5-12) is provided with a stirring shaft, the stirring shaft is equipped with a stirring blade (4-5-8), and the stirring shaft is driven by a transmission motor (4-5-10); Stirring wheel (4-5-4) is driven by stirring motor (4-5-5); The space between the mud-water buffer plate (4-5-7) and the through-hole plate (4-5-1) forms a buffer chamber (4-5-6); the liquid-inlet buffer plate (4-5-11 ), the mud-water buffer plate (4-5-7), the through-hole plate (4-5-1) and the sedimentation buffer plate (4-5-3) are all disc structures, and there are several holes on the surface hole; The stirring motor (4-5-5) and the transmission motor (4-5-10) are connected with the central controller (9) by wires. 3. A kind of juicing device used in fruit and vegetable processing according to claim 2, characterized in that, the mixing barrel (4-5-12) is a cone with a large top and a small bottom, and its bottom and top are both It is an open structure, and the inside of the bottom end and the inside of the top end are respectively provided with a medicine filling ring (4-5-14) and a cleaning ring pipe (4-5-9); the medicine filling ring (4-5-14 ), the cleaning ring pipe (4-5-9) is an internal hollow ring structure, and its lower end is evenly provided with a number of spray heads; the upper part of the buffer chamber (4-5-6) is also connected with the inner The clean water discharge pipe (4-5-13) connected to the cavity; The cleaning ring pipe (4-5-9) and the medicament filling ring (4-5-14) are respectively externally connected to a water adding pump and a drug adding pump; the water adding pump and the drug adding pump are connected to the central controller (9); The stirring wheel (4-5-4) is composed of several rectangular elbows, the number of which is not less than 6; the stirring blade (4-5-8) is located on the inner central axis of the stirring barrel (4-5-12) superior. 4. A juice extraction device for fruit and vegetable processing according to claim 3, characterized in that the outer edge of the liquid inlet buffer plate (4-5-11), the mixing barrel (4-5-12) The outer edge of the top, the outer edge of the mud-water buffer plate (4-5-7), the outer edge of the through-hole plate (4-5-1), and the outer edge of the sedimentation chamber (4-5-2) are separated from the filtrate The inner walls of the chamber (4-5) are seamlessly welded. 5. A juice extraction device for fruit and vegetable processing according to claim 4, characterized in that, the juice extraction turntable (4-3) is composed of the following components in parts by weight: Ultrasonic atomized gas-phase pure water 321.6~546.2 parts, methyl dodecyl siloxane 113.6~155.9 parts, 4-methoxy-α-methylphenylacetic acid methyl ester 116.0~225.9 parts, methyl n-hexane 112.2~ 129.1 parts, 115.8-172.9 parts of zymosan, 118.2-179.8 parts of 4,4'-(1-methylethylene) bisphenol and (chloromethyl) ethylene oxide and ethylene oxide polymer , 120.2-175.0 parts of sulfur nanoparticles, 113.5-155.3 parts of polysiloxane and silicone ether, 115.1-155.8 parts of polymers of formaldehyde, 1,3-dimethylbenzene and phenol, m-tert-butylphenylchlorothiomethyl 115.0-138.9 parts of acid ester, 104.7-140.8 parts of 2-[2-(2-methoxyethoxy)ethoxy]ethanol borate, 103.7-146.9 parts of 3-methyl-4-nitrobenzoic acid , 112.4-157.9 parts of N,N'-methyltetraylbis[4-[(4-isocyanatophenyl)methyl]-aniline, 122.1-166.1 parts of Pelargonium chrysanthemum extract, and the mass concentration is 112ppm-379ppm 145.5 to 199.3 parts of tert-butyl α-bromoisobutyrate. 6. A juice extraction device for fruit and vegetable processing according to claim 5, characterized in that the manufacturing process of the juice extraction turntable (4-3) comprises the following steps: Step 1: In the high-pressure stirred reactor, add ultrasonically atomized gas-phase pure water and methyl dodecyl siloxane, start the mixer in the high-pressure stirred reactor, set the speed at 114rpm-160rpm, and start the high-pressure Heating the oil temperature device in the stirring reactor to raise the temperature to 129.6°C~130.2°C, add 4-methoxy-α-methyl phenylacetate and stir evenly, carry out the reaction for 106.6~117.9 minutes, add methyl n-hexyl Alkanes, the flow rate of 105.8m ³ /min ~ 146.1m ³ /min hydrogen 106.6 ~ 117.9 minutes; then add zymosan in the high-pressure stirred reactor, start the heating oil temperature in the high-pressure stirred reactor again device, raise the temperature to 146.0°C~179.9°C, keep it warm for 106.2~117.1 minutes, add 4,4'-(1-methylethylene)bisphenol and (chloromethyl)oxirane and oxirane the polymer, adjust the pH value of the solution in the high-pressure stirred reactor to 4.8 to 8.9, and keep the temperature for 106.8 to 346.8 minutes; Step 2: Take another sulfur nanoparticle, and after the sulfur nanoparticle is ultrasonically treated at a power of 6.46KW～11.9KW for 0.112～1.179 hours; add the sulfur nanoparticle into another high-pressure stirred reactor, and add a mass concentration of 116ppm～346ppm polysiloxane and silicone ether disperse sulfur nanoparticles, start the heating oil temperature device in the high-pressure stirred reactor, make the solution temperature between 48°C and 80°C, start the high-pressure stirred reactor Mixer, and stir at a speed of 4×10 ² rpm to 8×10 ² rpm, adjust the pH value between 4.7 and 8.8, keep stirring for 112 to 179 minutes; then stop the reaction and let stand for 6.46×10 to 11.9×10 minutes, Remove impurities; add formaldehyde, 1,3-dimethylbenzene and phenol polymer to the suspension, adjust the pH value between 1.7 and 2.8, and form a precipitate, which is eluted with ultrasonic atomized gas-phase pure water, and passed through a centrifuge in the The solids were obtained at a rotation speed of 4.620×10 ³ rpm to 9.936×10 ³ rpm, dried at a temperature of 2.761×10 ² ℃ to 3.510×10 ² ℃, ground and passed through a 0.620×10 ³ to 1.936×10 ³ mesh sieve, and used for later use; Step 3: take m-tert-butylbenzene chlorothioformate and sulfur nanoparticles treated in step 2, mix them uniformly and irradiate with solar radiation reflection, the energy of solar radiation reflection irradiation is 103.7MeV～131.9MeV, The dosage is 151.7kGy～191.9kGy, and the irradiation time is 115.7～140.9 minutes, and the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles with changed properties is obtained; the mixture of m-tert-butylbenzene chlorothioformate and sulfur nanoparticles The particle mixture is placed in another high-pressure stirred reactor, start the heating oil heater in the high-pressure stirred reactor, set the temperature at 114.4°C to 160.9°C, start the stirrer in the high-pressure stirred reactor, and rotate at a speed of 106rpm to 501rpm , adjust the pH to 4.1-8.1, dehydrate for 115.1-129.1 minutes, and set aside; Step 4: Add the m-tert-butylbenzene chlorothioformate and sulfur nanoparticle mixture with the changed properties obtained in step 3 to 2-[2-(2-methoxyethane) with a mass concentration of 116ppm～346ppm Oxygen) ethoxy] ethanol borate, and flow into the high-pressure stirred reactor in the first step, the flow rate is 251mL/min～979mL/min; start the high-pressure stirred reactor mixer, set the speed 120rpm~160rpm; stir for 4~8 minutes; then add 3-methyl-4-nitrobenzoic acid, start the heating oil temperature device in the high-pressure stirred reactor, raise the temperature to 150.5°C~187.3°C, and adjust the pH to 4.5 Between ～8.3, the flow rate of hydrogen gas is 105.904m ³ /min～146.962m ³ /min, keep warm and stand for 140.6～170.2 minutes; start the high-pressure stirring reactor mixer again, the speed is 115rpm～160rpm, add N,N '-methyltetraylbis[4-[(4-isocyanatophenyl)methyl]-aniline, and adjust the pH to between 4.5 and 8.3, and keep the temperature for 139.6 to 179.9 minutes; Step 5: Start the mixer in the high-pressure stirred reactor, set the rotating speed at 112rpm～179rpm, start the heating oil heater in the high-pressure stirred reactor, and set the temperature in the high-pressure stirred reactor to 1.603×10 ² ℃～2.118×10 ² ℃, add geranium chrysanthemum extract, react for 106.0～117.9 minutes; then add tert-butyl α-bromoisobutyrate, start the heating oil heater in the high-pressure stirring reactor, set high pressure The temperature in the stirred reactor is 190.2℃～246.1℃, the pH is adjusted to 4.8～8.8, the pressure is 1.12MPa～1.13MPa, and the reaction time is 0.4～0.9 hours; after that, the pressure is reduced to 0MPa, and the temperature is reduced to 106.0°C～117.9°C, the material is discharged into the compression molding machine, and the juicing turntable (4-3) is obtained; The particle size of the sulfur nanoparticles is 120 μm˜130 μm. 7. A working method for a juicing device in fruit and vegetable processing, comprising the following steps: Step 1: The staff presses the start button on the central controller (9), starts the control valve on the blunt impact crusher (2) and the water inlet pipe (3-4), and passes the fruits and vegetables to be processed through the fruit and vegetable feeding port (1 ) into the bludgeoning crushing chamber (3) for crushing treatment, and at the same time spray clean water into the bludgeoning crushing chamber (3), and the crushed fruits and vegetables enter the pellet feeding chamber (4-1) under the action of the water body, Under the combined action of the juicing turntable (4-3) and the fixed grinding disc, the crushed fruits and vegetables are ground and squeezed into strips under the action of the compression cover, and then compressed through the compression holes on the side of the compression cover. It is discharged into the collection chamber (4-4), and finally enters the collection box through the fruit puree extrusion port (5), and the mixture of uncompressed minced meat and juice often flows downward through the filter screen into the filtrate separation chamber (4 -5); Step 2: During the crushing process of the fruits and vegetables to be crushed in the blunt crushing chamber (3), the crushing particle size detector (3-3) located in the blunt crushing chamber (3) monitors the crushing particle size of the fruits and vegetables in real time; When the particle size detector (3-3) detects that the broken particle size of fruits and vegetables is less than 8cm, the broken particle size detector (3-3) feeds back the detection signal to the central controller (9), and the central controller (9) reduces the bluntness. Impact crusher (2) speed, start grinding motor (6) simultaneously; Step 3: The material level gauge (4-2) located in the pellet feeding chamber (4-1) monitors the pellet material level height in real time; when the material level gauge (4-2) detects the pellet material level height When it is higher than the system setting value L1, the material level gauge (4-2) sends an electrical signal to the central controller (9), and the central controller (9) lowers the bludgeon crusher (2) after receiving the electrical signal. Increase the rotating speed of the grinding motor (6) at the same time; when the material level gauge (4-2) detects that the material level of the pellets is lower than the system setting value L2, the material level gauge (4-2) sends a report to the central controller ( 9) Send out electrical signal 2, and the central controller (9) increases the rotational speed of the blunt impact crusher (2) after receiving the electrical signal, and simultaneously reduces the rotational speed of the grinding motor (6); Step 4: The central controller (9) starts the transmission motor (4-5-10), the water adding pump and the stirring motor (4-5-5) at the same time, and the mixture of uncompressed minced meat and juice flows downward through the liquid The buffer plate (4-5-11) enters the mixing tank (4-5-12), and at the same time, the clean water injected by the cleaning ring pipe (4-5-9) enters the mixing tank (4-5-12) together with the mixture , and rotate under the driving of the stirring blade (4-5-8), and then achieve the purpose of centrifugation, so that the minced meat and juice are quickly separated once, and the separated juice quickly passes through the muddy water buffer plate (4-5-7) Enter the buffer chamber (4-5-6) and discharge through the clean water discharge pipe (4-5-13); the separated minced meat passes through the through-hole plate (4-5-1) and goes down through the stirring wheel (4-5- 4) is rotated for secondary separation, and after stirring, the sediment enters the sedimentation chamber (4-5-2) through the sedimentation buffer plate (4-5-3) for sedimentation; Step 5: the slag water level gauge (4-7) in the filtrate separation chamber (4-5) monitors the slag water level situation in the filtrate separation chamber (4-5) in real time; when the slag water level gauge ( 4-7) When it is detected that the slag water level in the filtrate separation chamber (4-5) is higher than the system set value, the slag water level gauge (4-7) sends a feedback signal to the central controller (9), The central controller (9) opens the slag discharge pipe (4-8) after receiving the electric signal, and the slag water is discharged through the slag discharge pipeline.