CN113207970A - Processing technology of compound protein beverage - Google Patents
Processing technology of compound protein beverage Download PDFInfo
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- CN113207970A CN113207970A CN202110507658.1A CN202110507658A CN113207970A CN 113207970 A CN113207970 A CN 113207970A CN 202110507658 A CN202110507658 A CN 202110507658A CN 113207970 A CN113207970 A CN 113207970A
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C11/00—Milk substitutes, e.g. coffee whitener compositions
- A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
- A23C11/06—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing non-milk proteins
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C3/00—Preservation of milk or milk preparations
- A23C3/02—Preservation of milk or milk preparations by heating
- A23C3/03—Preservation of milk or milk preparations by heating the materials being loose unpacked
- A23C3/033—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C3/00—Preservation of milk or milk preparations
- A23C3/04—Preservation of milk or milk preparations by freezing or cooling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/09—Mixing systems, i.e. flow charts or diagrams for components having more than two different of undetermined agglomeration states, e.g. supercritical states
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/70—Pre-treatment of the materials to be mixed
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/70—Pre-treatment of the materials to be mixed
- B01F23/708—Filtering materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/70—Pre-treatment of the materials to be mixed
- B01F23/713—Sieving materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/83—Mixing plants specially adapted for mixing in combination with disintegrating operations
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/181—Preventing generation of dust or dirt; Sieves; Filters
- B01F35/187—Preventing generation of dust or dirt; Sieves; Filters using filters in mixers, e.g. during venting
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/06—Mixing of food ingredients
- B01F2101/14—Mixing of ingredients for non-alcoholic beverages; Dissolving sugar in water
Abstract
The application relates to the technical field of processing of compound protein drinks, and discloses a processing technology of a compound protein drink, which mainly comprises the following steps: step S1: pretreatment of raw materials: preprocessing raw materials for making the compound protein beverage and mixing the preprocessed raw materials with water; step S2: preparing materials: adding the pretreated various raw materials into a blending tank for mixing to form a mixture; step S3: preheating: heating the mixture; step S4: homogenizing: conveying the preheated mixture into a homogenizer for processing; step S5: and (3) sterilization: performing ultrahigh-temperature instantaneous sterilization on the mixture by using an ultrahigh-temperature instantaneous sterilizer; step S6: filling: and cooling the sterilized mixture to room temperature and filling. The application has the effect of improving the processing efficiency of the compound protein beverage.
Description
Technical Field
The application relates to the field of compound protein drinks, in particular to a compound protein drink processing technology.
Background
The compound protein beverage is prepared by processing or fermenting milk or dairy products and different vegetable proteins serving as main raw materials.
At present, Chinese patent application with publication number CN104814492A discloses an oil sunflower and red date composite protein beverage and a preparation method thereof, the oil sunflower and red date composite protein beverage comprises red date juice, oil sunflower sauce, citric acid, white granulated sugar, glyceryl monostearate, sodium stearoyl lactate and a composite stabilizer; a preparation method of an oil sunflower and red date compound protein beverage comprises the following steps: diluting oil sunflower sauce with 11 times of water to obtain oil sunflower milk, and preparing 0.25% citric acid solution; respectively adding oil sunflower milk, red date juice, a composite stabilizer, glyceryl monostearate, sodium stearoyl lactylate and white granulated sugar into a mixing barrel, adding purified water, mixing and stirring uniformly, and adding a citric acid solution while stirring; homogenizing twice after fine grinding by a colloid mill, and then filling, sterilizing and cooling.
In view of the above-mentioned related technologies, the inventor thinks that after homogenizing and filling, the beverage is sterilized and cooled, and before filling, the beverage after homogenizing needs to be cooled, and after sterilizing, the beverage after filling needs to be cooled again, and there is a defect that the production and processing efficiency of the composite protein beverage is affected.
Disclosure of Invention
In order to improve the production and processing efficiency of the compound protein beverage, the application provides a compound protein beverage processing technology.
The application provides a processing technology of a compound protein beverage, which adopts the following technical scheme:
a processing technology of a compound protein beverage mainly comprises the following steps: step S1: pretreatment of raw materials: preprocessing raw materials for making the compound protein beverage and mixing the preprocessed raw materials with water; step S2: preparing materials: adding the pretreated various raw materials into a blending tank for mixing to form a mixture; step S3: preheating: heating the mixture; step S4: homogenizing: conveying the preheated mixture into a homogenizer for processing; step S5: and (3) sterilization: performing ultrahigh-temperature instantaneous sterilization on the mixture by using an ultrahigh-temperature instantaneous sterilizer; step S6: filling: and cooling the sterilized mixture to room temperature and filling.
By adopting the technical scheme, the sterilization is directly carried out after the mixture is homogenized, the mixture is cooled after the sterilization, the mixture is cooled to the room temperature, the filling is carried out after the mixture is cooled, the processing is completed after the filling, and the production and processing efficiency of the compound protein beverage is improved.
Optionally, the blending tank in step S2 includes cylinder body, rabbling mechanism and filter screen, the rabbling mechanism includes motor and puddler, motor fixed connection is in the one end that ground was kept away from to the cylinder body, the puddler is located inside the cylinder body, the puddler is perpendicular with cylinder body bottom, the main shaft and the coaxial fixed connection of puddler of motor, the filter screen sets up inside the cylinder body, filter screen and the coaxial fixed connection of (mixing) shaft, the filter screen is inside with the cylinder body to be cut apart into upper chamber and lower chamber, the feed inlet has been seted up at the cylinder body top, feed inlet and upper chamber intercommunication, the discharge gate has been seted up to the cylinder body bottom, discharge gate and lower chamber intercommunication.
Through adopting above-mentioned technical scheme, set up the filter screen in that the cylinder body is inside, the filter screen divide into cavity and lower cavity with the cylinder body, utilizes the filter screen to filter the material that gets into in the cylinder body through the feed inlet, makes great solid matter stay in the cavity of going up, reduces the solid matter in the raw and other materials and to the influence of allotment jar mixing effect, improves the production machining efficiency of beverage.
Optionally, one side that ground was kept away from to the filter screen is provided with broken mechanism, broken mechanism includes planetary gear assembly, first broken subassembly and the broken subassembly of second, planetary gear assembly and stirring shaft connection, planetary gear assembly is located the filter screen and keeps away from one side of cylinder body bottom, first broken subassembly is connected in one side that planetary gear assembly is close to the filter screen, the broken subassembly of second is connected in one side that the filter screen is close to planetary gear assembly.
Through adopting above-mentioned technical scheme, set up broken mechanism in the filter screen one side of keeping away from ground, utilize broken mechanism to carry out the breakage to the solid matter that stays in the epicoele indoor, reduce the possibility that the filter screen is blockked up by the solid matter.
Optionally, the planetary gear assembly includes planet carrier, first gear, a plurality of second gear and ring gear, the planet carrier cover is established in the puddler outside, planet carrier and cylinder body fixed connection, first gear and the coaxial fixed connection of puddler, the coaxial cover of ring gear is established in the first gear outside, and is three the second gear sets up along first gear circumference equidistant, second gear meshing is connected between first gear and ring gear, the second gear rotates with the planet carrier to be connected, ring gear and first broken subassembly fixed connection.
Through adopting above-mentioned technical scheme, first gear and the coaxial fixed connection of puddler, second gear engagement is connected between ring gear and first gear, and first gear rotates with the puddler synchronization under the drive of puddler, and the ring gear rotates with first gear antiport under the transmission of second gear.
Optionally, the first crushing assembly comprises a plurality of upper connecting rods, and the second crushing assembly comprises a plurality of lower connecting rods; many go up the rotation axis of the equal perpendicular to puddler of connecting rod, many go up the connecting rod and set up, many along puddler circumference interval go up the connecting rod all with ring gear fixed connection, many go up the one end that the connecting rod is close to the puddler and rotate with the puddler and be connected, many the connecting rod sets up along the equidistant of puddler circumference down, many the connecting rod all is connected with the filter screen down, one side that the filter screen was kept away from down to the connecting rod is provided with many first crushing poles along its length direction interval, first crushing pole and the perpendicular fixed connection of lower connecting rod, adjacent two be provided with the second crushing pole between the first crushing pole, the second crushing pole is connected with the perpendicular fixed connection of last connecting rod.
Through adopting above-mentioned technical scheme, first crushing pole rotates along the direction opposite with the puddler rotation direction under the drive of ring gear, and the second crushing pole rotates along the direction opposite with the puddler rotation direction under the drive of filter screen, and the crushing pole of second is located between the adjacent two first crushing poles, carries out the breakage through the cooperation of first crushing pole and second crushing pole to the solid.
Optionally, the ultra-high temperature instantaneous sterilizer in step S5 includes a preheating mechanism, an ultra-high temperature sterilization mechanism and a distribution mechanism for communicating with the homogenizer, the distribution mechanism includes a communicating pipe, a distribution valve, a liquid outlet pipe for communicating with the feed end of the homogenizer, a liquid inlet pipe for communicating with the discharge end of the homogenizer, and two switch valves, one end of the communicating pipe communicates with the preheating mechanism, the other end of the communicating pipe communicates with the ultra-high temperature sterilization mechanism, the distribution valve is disposed on the communicating pipe, the distribution valve communicates with the communicating pipe, the liquid outlet pipe is disposed between the distribution valve and the preheating mechanism, the liquid inlet pipe communicates with the communicating pipe, the liquid inlet pipe is disposed between the distribution valve and the ultra-high temperature sterilization mechanism, one of the switch valves communicates with the liquid inlet pipe, and the other switch valve communicates with the liquid outlet pipe.
By adopting the technical scheme, the flow dividing mechanism is arranged between the preheating mechanism and the ultra-high temperature sterilization mechanism, the preheating mechanism and the ultra-high temperature sterilization mechanism are communicated by utilizing the communicating pipe, the flow dividing valve is arranged on the communicating pipe, the communicating pipe is communicated with the feeding end of the homogenizer through the liquid outlet pipe, and the communicating pipe is communicated with the discharging end of the homogenizer through the liquid inlet pipe; before homogenizing the beverage, conveying the mixture processed by the blending tank into a preheating mechanism for preheating; the flow dividing valve is closed, the two switch valves are opened, the preheated mixture is conveyed to enter the homogenizer for homogenization, and after the homogenization is completed, the mixture enters the ultra-high temperature sterilization mechanism through the discharge pipe for sterilization, so that the production and processing efficiency of the beverage is improved.
Optionally, the preheating mechanism includes a preheating box and a first feeding pipe, the first feeding pipe is located in the preheating box, the first feeding pipe is fixedly connected to the preheating box, one end of the first feeding pipe is communicated with the communicating pipe, the other end of the first feeding pipe is communicated with the outside of the preheating box, a first liquid inlet and a first liquid outlet are formed in the preheating box, and the first feeding pipe is a serpentine coil.
By adopting the technical scheme, the mixture is conveyed by the first feeding pipe, the heating water enters the preheating box through the first liquid inlet, and the mixture in the first feeding pipe is heated by the heating water, so that the effect of preheating the mixture is achieved; through setting up first conveying pipe into serpentine coil, increase the path length that the mixture removed in the preheating cabinet to improve the heating effect of preheating the mechanism to the mixture.
Optionally, the ultra-high temperature sterilization mechanism is communicated with a cooling mechanism, the cooling mechanism comprises a cooling box and a second feeding pipe, the second feeding pipe is located in the cooling box, the second feeding pipe is fixedly connected with the cooling box, one end of the second feeding pipe is communicated with the ultra-high temperature sterilization mechanism, the other end of the second feeding pipe is communicated with the outside of the cooling box, and a second inlet and a second liquid outlet are formed in the cooling box.
By adopting the technical scheme, the ultrahigh temperature sterilization mechanism is communicated with the cooling mechanism, the mixture subjected to ultrahigh temperature sterilization enters the cooling box through the second feeding pipe, the cooling water enters the cooling box through the second liquid inlet, and the mixture in the second feeding pipe is cooled by the cooling water; the second liquid outlet is communicated with the first liquid inlet, the temperature of the cooling water rises after the mixture is cooled by the cooling water, and the cooling water with the increased temperature is conveyed into the preheating box to preheat the mixture, so that the consumption of external energy is reduced, and the device is energy-saving and environment-friendly.
Optionally, a heating pipe is arranged in the preheating box, and the heating pipe is sleeved outside the first feeding pipe.
Through adopting above-mentioned technical scheme, set up the heating pipe in the preheating cabinet, utilize the heating pipe to heat the water in the preheating cabinet, reduce the possibility that the temperature height of water in the preheating cabinet is not enough.
In summary, the present application includes at least one of the following beneficial technical effects:
1. the filter screen is arranged in the cylinder body, the cylinder body is divided into the upper chamber and the lower chamber by the filter screen, and materials entering the cylinder body through the feeding hole are filtered by the filter screen, so that larger solid matters are retained in the upper chamber, the influence of the solid matters in raw materials on the mixing effect of the preparation tank is reduced, and the production and processing efficiency of the beverage is improved;
2. the preheating mechanism is communicated with the ultra-high temperature sterilization mechanism through a communicating pipe, a diverter valve is arranged on the communicating pipe, the communicating pipe is communicated with a feeding end of a homogenizer through a liquid outlet pipe, the communicating pipe is communicated with a discharging end of the homogenizer through a liquid inlet pipe, the diverter valve is closed before the beverage is homogenized, two switch valves are opened, the mixture processed by a blending tank is conveyed into the preheating mechanism to be preheated, the preheated mixture is conveyed into the homogenizer to be homogenized, and the mixture enters the ultra-high temperature sterilization mechanism through a discharging pipe to be sterilized after the homogenization is completed, so that the production and processing efficiency of the beverage is improved;
3. through communicating second liquid outlet and first inlet, cooling water cools off the back to the mixture, and cooling water temperature risees, carries the cooling water that the temperature risees and gets into the preheating cabinet and preheat the mixture, reduces the consumption of external energy, and is energy-concerving and environment-protective.
Drawings
FIG. 1 is a process flow diagram of an embodiment of the present application;
FIG. 2 is a schematic diagram of the overall configuration of a portion of a dispensing canister according to an embodiment of the present application;
FIG. 3 is a schematic structural view of a crushing mechanism portion according to an embodiment of the present application;
FIG. 4 is a schematic structural view of portions of a planetary gear assembly, a first crushing assembly portion and a second crushing assembly portion embodying the present application;
FIG. 5 is a schematic structural diagram of the whole of an ultrahigh-temperature instantaneous sterilization mechanism in the embodiment of the application;
fig. 6 is a schematic structural view of a cooling mechanism portion according to an embodiment of the present application.
Reference numerals: 100. a blending tank; 110. a cylinder body; 111. a feed inlet; 112. a discharge port; 200. a stirring mechanism; 210. a motor; 220. a stirring rod; 300. a filter screen; 400. a crushing mechanism; 410. a planetary gear assembly; 411. a planet carrier; 412. a first gear; 413. a second gear; 414. a ring gear; 420. a first crushing assembly; 421. an upper connecting rod; 422. a second crushing bar; 430. a second crushing assembly; 431. a lower connecting rod; 432. a first crushing bar; 500. a liquid level tube; 600. an ultra-high temperature instantaneous sterilizer; 610. a preheating mechanism; 611. a preheating box; 612. a first liquid inlet; 613. a first liquid outlet; 614. a first feed pipe; 615. heating a tube; 620. an ultra-high temperature sterilization mechanism; 630. a flow dividing mechanism; 631. a communicating pipe; 632. a flow divider valve; 633. a liquid outlet pipe; 634. a liquid inlet pipe; 700. an on-off valve; 800. a cooling mechanism; 810. a cooling tank; 811. a second liquid inlet; 812. a second liquid outlet; 820. a second feed tube; 900. a temporary storage pool; 910. and (4) a water pump.
Detailed Description
The present application is described in further detail below with reference to figures 1-6.
The embodiment of the application discloses a processing technology of a compound protein beverage. Referring to fig. 1, a processing technology of a compound protein beverage mainly comprises the following steps: step S1: pretreatment of raw materials: after being dry-mixed, the stabilizer and the white granulated sugar are put into pure water at the temperature of 80-85 ℃, and are sheared for 15-20 minutes by an emulsification tank, so that the dry-mixed stabilizer and the white granulated sugar are fully dissolved to obtain sugar water, wherein the weight ratio of the stabilizer to the white granulated sugar to the pure water in the sugar water is 0.1:10: 40; putting the milk powder into purified water at 50-60 ℃ for dissolving, and hydrating for 30 minutes to obtain milk liquid, wherein the weight ratio of the milk powder to the purified water in the milk liquid is 1: 9; putting peanut butter and walnut butter into purified water at the temperature of 80 ℃ and stirring for 5-10 minutes to obtain compound protein butter, wherein the weight ratio of the peanut butter, the walnut butter and the purified water in the compound protein butter is 1:1: 23; step S2: adding the sugar water, the milk liquid and the compound protein sauce into a blending tank 100 to mix to form a mixture, wherein the weight ratio of the sugar water to the milk liquid to the compound protein sauce in the mixture is 1:1: 2; step S3: preheating: preheating the mixture to enable the temperature of the mixture to reach 70 ℃; step S4: homogenizing: performing primary homogenization on the mixture under the pressure of 25map, and breaking large particles into small particles; the mixture is subjected to secondary homogenization under the pressure of 28mpa, so that the small particles are prevented from being aggregated again, and the taste of the compound protein beverage is improved; step S4: and (3) sterilization: heating the mixture to 138 ℃ by using an ultrahigh-temperature instantaneous sterilizer 600, and sterilizing for 10 to 15 seconds; step S6: and cooling the sterilized mixture to room temperature and filling.
Referring to fig. 2 and 3, the blending tank 100 includes a cylinder body 110, a feeding port 111 is provided at the top of the cylinder body 110, a discharging port 112 is provided at the bottom of the cylinder body 110, a plurality of raw materials to be mixed are conveyed into the cylinder body 110 through the feeding port 111, and a mixed material after blending leaves the cylinder body 110 through the discharging port 112. The cylinder 110 is connected to a stirring mechanism 200, and the stirring mechanism 200 stirs and mixes a plurality of types of raw materials in the cylinder 110. The stirring mechanism 200 is connected with a filter screen 300, the inside of the cylinder body 110 is divided into an upper chamber communicated with the feeding hole 111 and a lower chamber communicated with the discharging hole 112 by the filter screen 300, and the filter screen 300 reserves large solid matters in the upper chamber, so that the influence of the solid matters in the raw materials on the mixing effect of the preparation tank 100 is reduced. A crushing mechanism 400 is arranged above the filter screen 300, the crushing mechanism 400 is connected with the cylinder body 110, and the crushing mechanism 400 is used for crushing large solid matters in the upper chamber.
Referring to fig. 2 and 3, the cylinder body 110 is a cylindrical structure, and the axis of the cylinder body 110 is vertically disposed. The stirring mechanism 200 comprises a motor 210, the motor 210 is fixedly connected to the top of the cylinder body 110, a stirring rod 220 is coaxially and fixedly connected to a main shaft of the motor 210, the stirring rod 220 is located inside the cylinder body 110, and the main shaft of the motor 210 penetrates through the top of the cylinder body 110 and is coaxially and fixedly connected with the stirring rod 220.
Referring to fig. 2 and 3, the filter screen 300 is coaxially and fixedly connected with the stirring rod 220, and the side wall of the filter screen 300 far away from the stirring rod 220 is connected with the inner wall of the cylinder body 110 in a sliding manner; in the process that the motor 210 drives the stirring rod 220 to rotate, the filter screen 300 and the stirring rod 220 synchronously rotate, so that the possibility that the filter screen 300 is blocked by larger solid matters is reduced.
Referring to fig. 3 and 4, the crushing mechanism 400 includes a planetary gear assembly 410, the planetary gear assembly 410 includes a planet carrier 411 fixedly connected to the cylinder 110, the cross section of the planet carrier 411 is circular, and the planet carrier 411 and the coaxial sleeve are disposed outside the stirring rod 220. The stirring rod 220 is coaxially and fixedly connected with a first gear 412, the first gear 412 is circumferentially and equidistantly meshed with three second gears 413, the three second gears 413 are rotatably connected with the planet carrier 411, and the rotating axis of the first gear 412 is parallel to that of the second gear 413; the outer sides of the three second gears 413 are sleeved with gear rings 414, the gear rings 414 are coaxially arranged with the first gears 412, and the gear rings 414 are meshed with the second gears 413.
The crushing mechanism 400 further includes a first crushing assembly 420 and a second crushing assembly 430; first broken subassembly 420 is located ring gear 414 below, and first broken subassembly 420 includes six upper connecting rods 421, and six upper connecting rods 421 set up along puddler 220 circumference equidistant, and upper connecting rod 421 one end rotates with puddler 220 to be connected, upper connecting rod 421 and ring gear 414 fixed connection. The lower end of the upper connecting rod 421 is vertically and fixedly connected with a plurality of second crushing rods 422, and the plurality of second crushing rods 422 are arranged at equal intervals along the length direction of the upper connecting rod 421.
The second crushing assembly 430 comprises six lower connecting rods 431, the six lower connecting rods 431 are arranged at equal intervals along the circumferential direction of the stirring rod 220, and the lower connecting rods 431 are fixedly connected with the filter screen 300. A first crushing rod 432 is arranged in the middle between two adjacent second crushing rods 422, the first crushing rods 432 are vertically and fixedly connected with the lower connecting rod 431, and the plurality of first crushing rods 432 connected to the same lower connecting rod 431 are arranged at equal intervals along the length direction of the lower connecting rod 431.
The stirring rod 220 rotates to drive the first gear 412 to rotate, the second gear 413 is meshed and connected between the gear ring 414 and the first gear 412, and the gear ring 414 rotates in the opposite direction of the stirring rod 220 under the transmission of the second gear 413; the filter screen 300 is driven by the stirring rod 220 to rotate in the same direction as the stirring rod 220. The first crushing rods 432 are driven by the gear ring 414 to rotate in the direction opposite to the rotating direction of the stirring rod 220, the second crushing rods 422 are driven by the filter screen 300 to rotate in the direction opposite to the rotating direction of the stirring rod 220, the second crushing rods 422 are positioned between two adjacent first crushing rods 432, and solid matters are crushed by matching the first crushing rods 432 with the second crushing rods 422.
Referring to fig. 3, a liquid level pipe 600 vertically disposed is fixedly connected to the side wall of the cylinder body 110, the upper end of the liquid level pipe 600 is fixedly connected to a position close to the top of the side wall of the cylinder body 110, the lower end of the liquid level pipe 600 is fixedly connected to a position close to the bottom of the side wall of the cylinder body 110, and the upper end and the lower end of the liquid level pipe 600 are both communicated with the inside of the cylinder body 110. Through fixed connection liquid level pipe 600 on the lateral wall of cylinder body 110, the operating personnel of being convenient for observes the volume of the interior material of cylinder body 110, improves the convenience that allotment jar 100 used.
Referring to fig. 5 and 6, the ultra-high temperature instantaneous sterilizer 600 includes a preheating mechanism 610 for preheating the mixture, the preheating mechanism 610 is communicated with an ultra-high temperature sterilization mechanism 620 through a shunt mechanism 630, and both the preheating mechanism 610 and the ultra-high temperature sterilization mechanism 620 are communicated with the homogenizer through the shunt mechanism 630. The ultra-high temperature sterilization mechanism 620 is communicated with the cooling mechanism 800, and the mixture leaving the ultra-high temperature sterilization mechanism 620 is cooled by the cooling mechanism 800. The cooling mechanism 800 is communicated with the preheating mechanism 610, and cooling water after the cooling mechanism 800 works flows into the preheating mechanism 610 to preheat the mixture.
Referring to fig. 5 and 6, the preheating mechanism 610 includes a preheating chamber 611, and the preheating chamber 611 has a hollow rectangular parallelepiped box structure; a first liquid outlet 613 is formed in the position, close to the bottom, of the side wall of the preheating box 611, a first liquid inlet 612 is formed in the position, close to the top, of the side wall of the preheating box 611, and the first liquid inlet 612 and the first liquid outlet 613 are both communicated with a switch valve 700; a first feeding pipe 614 is fixedly connected in the preheating box 611, one end of the first feeding pipe 614 is communicated with the outside of the preheating box 611, and the other end of the first feeding pipe 614 is communicated with the diversion mechanism 630; the mixture enters the preheating tank 611 through the first feeding pipe 614, heating water is input into the preheating tank 611 through the first liquid inlet 612, and the mixture in the first feeding pipe 614 is heated by the heating water, so that the effect of preheating the mixture is achieved.
The first feeding pipe 614 is a serpentine coil, and the path length of the mixture moving in the preheating box 611 is increased by setting the first feeding pipe 614 as the serpentine coil, so that the heating effect of the preheating mechanism 610 on the mixture is improved. The heating pipe 615 is sleeved outside the first feeding pipe 614, and the heating pipe 615 is fixedly connected with the preheating box 611. By providing the heating pipe 615 in the preheating tank 611, the possibility of insufficient water temperature in the preheating tank 611 is reduced.
Referring to fig. 5 and 6, the ultra-high temperature sterilization mechanism 620 is fixedly connected above the preheating chamber 611; the flow distribution mechanism 630 comprises a communication pipe 631, one end of the communication pipe 631 is communicated with the first feeding pipe 614, and the other end of the communication pipe 631 is communicated with the ultra-high temperature sterilization mechanism 620; the communicating pipe 631 is provided with a flow dividing valve 632, and the flow dividing valve 632 is communicated with the communicating pipe 631; communicating pipe 631 is communicated with a liquid outlet pipe 633, liquid outlet pipe 633 is located between diverter valve 632 and first feeding pipe 614, communicating pipe 631 is communicated with a liquid inlet pipe 634, liquid inlet pipe 634 is located between diverter valve 632 and ultra-high temperature sterilization mechanism 620, and liquid outlet pipe 633 and liquid inlet pipe 634 are both communicated with switch valve 700.
The preheating mechanism 610 is communicated with the ultra-high temperature sterilization mechanism 620 through a communicating pipe 631, a flow dividing valve 632 is arranged on the communicating pipe 631, the communicating pipe 631 is communicated with the feeding end of the homogenizer through a liquid outlet pipe 633, and the communicating pipe 631 is communicated with the discharging end of the homogenizer through a liquid inlet pipe 634; when need carry into the homogenizer to the mixture that preheats in carrying out the homogeneity, close diverter valve 632, open two ooff valves 700, make the mixture that preheats carry and carry out the homogeneity in getting into the homogenizer, get into after the homogeneity is accomplished and get into super pasteurization mechanism 620 through the discharging pipe and disinfect, diverter mechanism 630 uses conveniently.
Referring to fig. 5 and 6, the cooling mechanism 800 includes a cooling box 810, the cooling box 810 is a hollow rectangular parallelepiped box structure, and the cooling box 810 is fixedly connected above the ultra-high temperature sterilization mechanism 620; a second liquid outlet 812 is formed in the position, close to the bottom, of the side wall of the cooling box 810, a second liquid inlet 811 is formed in the position, close to the top, of the side wall of the cooling box 810, and the second liquid inlet 811 and the second liquid outlet 812 are both communicated with a switch valve 700; a second feeding pipe 820 is fixedly connected in the cooling box 810, one end of the first feeding pipe 614 is communicated with the ultra-high temperature sterilization mechanism 620, and the other end of the second feeding pipe 820 is communicated with the outside of the cooling box 810; the mixture that passes through ultra-high temperature sterilization gets into the cooling box 810 through second conveying pipe 820 in, cooling water gets into the cooling box 810 through second inlet 811, utilizes the cooling water to cool down the mixture in the second conveying pipe 820.
The second liquid outlet 812 is communicated with the first liquid inlet 612, and after the mixture is cooled by cooling water through the second liquid outlet 812 and the first liquid inlet 612, the temperature of the cooling water is increased, and the cooling water with the increased temperature is conveyed into the preheating tank 611 to preheat the mixture, so that the consumption of external energy is reduced, and the device is energy-saving and environment-friendly.
Referring to fig. 6, the first liquid outlet 613 is communicated with the temporary storage tank 900, the heating water flowing out of the preheating tank 611 flows into the temporary storage tank 900 to be cooled, the water pump 910 is fixedly connected to the temporary storage tank 900, an inlet of the water pump 910 is communicated with the temporary storage tank 900, an outlet of the water pump 910 is communicated with the second liquid inlet 811, and the cooled water pump 910 is reused in the cooling tank 810 by the water pump 910, so that water recycling is realized.
The implementation principle of the processing technology of the compound protein beverage in the embodiment of the application is as follows: in the processing process of the composite protein beverage, the mixture is directly sterilized after being homogenized, the mixture is cooled after being sterilized, the mixture is cooled to the room temperature, filling is carried out after the mixture is cooled, the processing is finished after the filling, and the production and processing efficiency of the composite protein beverage is improved.
The above embodiments are preferred embodiments of the present application, and the protection scope of the present application is not limited by the above embodiments, so: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.
Claims (9)
1. A processing technology of a compound protein beverage is characterized in that: the method mainly comprises the following steps: step S1: pretreatment of raw materials: preprocessing raw materials for making the compound protein beverage and mixing the preprocessed raw materials with water; step S2: preparing materials: adding the pretreated raw materials into a blending tank (100) for mixing to form a mixture; step S3: preheating: heating the mixture; step S4: homogenizing: conveying the preheated mixture into a homogenizer for processing; step S5: and (3) sterilization: performing ultrahigh-temperature instantaneous sterilization on the mixture by using an ultrahigh-temperature instantaneous sterilizer (600); step S6: filling: and cooling the sterilized mixture to room temperature and filling.
2. The process for processing a composite protein beverage according to claim 1, wherein the process comprises the following steps: the blending tank (100) in the step S2 comprises a cylinder body (110), a stirring mechanism (200) and a filter screen (300), wherein the stirring mechanism (200) comprises a motor (210) and a stirring rod (220), the motor (210) is fixedly connected to one end, far away from the ground, of the cylinder body (110), the stirring rod (220) is located inside the cylinder body (110), the stirring rod (220) is perpendicular to the bottom of the cylinder body (110), a main shaft of the motor (210) is coaxially and fixedly connected with the stirring rod (220), the filter screen (300) is arranged inside the cylinder body (110), the filter screen (300) is coaxially and fixedly connected with a stirring shaft, the filter screen (300) divides the inside of the cylinder body (110) into an upper cavity and a lower cavity, a feed inlet (111) is formed in the top of the cylinder body (110), the feed inlet (111) is communicated with the upper cavity, a discharge outlet (112) is formed in the bottom of the cylinder body (110), the discharge hole (112) is communicated with the lower chamber.
3. The process for preparing a compound protein beverage as claimed in claim 2, wherein: one side that ground was kept away from in filter screen (300) is provided with broken mechanism (400), broken mechanism (400) include planetary gear assembly (410), first broken subassembly (420) and second broken subassembly (430), planetary gear assembly (410) and stirring shaft connection, planetary gear assembly (410) are located filter screen (300) and keep away from one side of cylinder body (110) bottom, one side that planetary gear assembly (410) are close to filter screen (300) is connected in first broken subassembly (420), one side that planetary gear assembly (410) are close to in second broken subassembly (430) are connected in filter screen (300) is close to planetary gear assembly (410).
4. The process for preparing a compound protein beverage as claimed in claim 3, wherein: planetary gear subassembly (410) includes planet carrier (411), first gear (412), a plurality of second gear (413) and ring gear (414), the puddler (220) outside is established in planet carrier (411), planet carrier (411) and cylinder body (110) fixed connection, first gear (412) and the coaxial fixed connection of puddler (220), ring gear (414) coaxial cover is established in the first gear (412) outside, and is three second gear (413) are along the equidistant setting of first gear (412) circumference, second gear (413) meshing connection is between first gear (412) and ring gear (414), second gear (413) rotate with planet carrier (411) and are connected, ring gear (414) and first broken subassembly (420) fixed connection.
5. The process for preparing a compound protein beverage as claimed in claim 4, wherein: the first crushing assembly (420) comprises a plurality of upper connecting rods (421), the second crushing assembly (430) comprises a plurality of lower connecting rods (431); many go up connecting rod (421) all perpendicular to the axis of rotation of puddler (220), many go up connecting rod (421) and set up along puddler (220) circumference interval, many go up connecting rod (421) all with ring gear (414) fixed connection, many go up the one end that connecting rod (421) are close to puddler (220) and be connected with puddler (220) rotation, many lower connecting rod (431) set up along puddler (220) circumference interval such as, many lower connecting rod (431) all are connected with filter screen (300), a plurality of first crushing rods (432) are arranged at intervals along the length direction of one side of the lower connecting rod (431) far away from the filter screen (300), the first crushing rods (432) are vertically and fixedly connected with the lower connecting rod (431), a second crushing rod (422) is arranged between every two adjacent first crushing rods (432), the second crushing rod (422) is vertically and fixedly connected with the upper connecting rod (421).
6. The process for processing a composite protein beverage according to claim 1, wherein the process comprises the following steps: the ultra-high temperature instantaneous sterilizer (600) in step S5 comprises a preheating mechanism (610), an ultra-high temperature sterilization mechanism (620) and a distribution mechanism (630) for communicating with the homogenizer, wherein the distribution mechanism (630) comprises a communicating pipe (631), a distribution valve (632), a liquid outlet pipe (633) for communicating with a feeding end of the homogenizer, a liquid inlet pipe (634) for communicating with a discharging end of the homogenizer and two switch valves (700), one end of the communicating pipe (631) is communicated with the preheating mechanism (610), the other end of the communicating pipe (631) is communicated with the ultra-high temperature sterilization mechanism (620), the distribution valve (632) is arranged on the communicating pipe (631), the distribution valve (632) is communicated with the communicating pipe (631), the liquid outlet pipe (633) is communicated with the communicating pipe (631), the liquid outlet pipe (631) is located between the distribution valve (632) and the preheating mechanism (610), the liquid inlet pipe (634) is communicated with the communicating pipe (631), the liquid inlet pipe (634) is positioned between the flow dividing valve (632) and the ultra-high temperature sterilization mechanism (620), one of the switch valves (700) is communicated with the liquid inlet pipe (634), and the other switch valve (700) is communicated with the liquid outlet pipe (633).
7. The process of claim 6 for preparing a complex protein beverage, wherein: the preheating mechanism (610) comprises a preheating box (611) and a first feeding pipe (614), the first feeding pipe (614) is located in the preheating box (611), the first feeding pipe (614) is fixedly connected with the preheating box (611), one end of the first feeding pipe (614) is communicated with a communicating pipe (631), the other end of the first feeding pipe (614) is communicated with the outside of the preheating box (611), a first liquid inlet (612) and a first liquid outlet (613) are formed in the preheating box (611), and the first feeding pipe (614) is a serpentine coil.
8. The process of claim 7 for preparing a complex protein beverage, wherein: the ultra-high temperature sterilization mechanism (620) is communicated with a cooling mechanism (800), the cooling mechanism (800) comprises a cooling box (810) and a second feeding pipe (820), the second feeding pipe (820) is located in the cooling box (810), the second feeding pipe (820) is fixedly connected with the cooling box (810), one end of the second feeding pipe (820) is communicated with the ultra-high temperature sterilization mechanism (620), the other end of the second feeding pipe (820) is communicated with the outside of the cooling box (810), and a second liquid inlet (811) and a second liquid outlet (812) are formed in the cooling box (810).
9. The process of claim 8 for preparing a complex protein beverage, wherein: a heating pipe (615) is arranged in the preheating box (611), and the heating pipe (615) is sleeved on the outer side of the first feeding pipe (614).
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Cited By (1)
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| CN115669727A (en) * | 2022-11-17 | 2023-02-03 | 昆山亿政咖啡有限公司 | Homogeneous sterilization equipment for milk beverage preparation and sterilization method thereof |
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| CN113207970B (en) | 2023-03-17 |
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