CN113769433A - Production line and method for efficiently producing fried burdock formula particles - Google Patents
Production line and method for efficiently producing fried burdock formula particles Download PDFInfo
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Abstract
The invention discloses a production line for efficiently producing stir-fried burdock formula granules, which comprises an extraction device, a double-effect reduced pressure concentrator, a dryer, a stirring device and a granulator which are sequentially connected; the extraction device comprises a main frame, a subframe fixedly arranged at the top of the main frame and an extraction tank fixedly arranged on a top plate of the subframe, wherein lifting oil cylinders are fixedly arranged on the left side wall and the right side wall of the extraction tank respectively, a lifting plate is fixedly arranged between the action ends of piston rods of the two lifting oil cylinders, a barrel is rotatably arranged in the lifting plate, the barrel sequentially penetrates through the lifting plate and the top end of the extraction tank and extends into the extraction tank, and a detachable barrel cover is arranged at the bottom of the barrel; the desiccator includes jar body, rotatory spherical shower nozzle of installing on jar body roof, and the last extension port department of spherical shower nozzle is connected with rotary joint. The invention has the beneficial effects that: prevent sintering, alleviate workman working strength, improve extract preparation efficiency, improve stir-fry burdock formula granule production efficiency, improve the taste of taking.
Description
Technical Field
The invention relates to the technical field of production of stir-fried burdock formula particles, in particular to a production line and a method for efficiently producing stir-fried burdock formula particles.
Background
The fried burdock formula particles have the effects of dispelling wind and heat, ventilating the lung and promoting eruption, and detoxifying and relieving sore throat, are clinically used for treating wind-heat type common cold, cough with excessive phlegm, measles, rubella, sore throat, mumps erysipelas, carbuncle, swelling, sore and the like, and are heat-clearing and exterior-releasing medicines commonly used in traditional Chinese medicine. After entering into the body, the stir-fried arctium fruit formula particles are converted into a demethylated compound of aglycon by intestinal bacteria in the digestive tract, the demethylated compound is recovered into the aglycon under the action of liver catechol-O-methyltransferase, and the aglycon is conveyed to each organ by blood to play a role. The fried burdock formula particle is processed from fried burdock particles, the appearance of the fried burdock particles is flat,
the existing method for producing the fried burdock formula particles comprises the steps of firstly dumping a certain amount of fried burdock particles into an extraction tank, injecting a certain amount of hot water into the extraction tank to decoct the fried burdock particles, and extracting arctigenin in the fried burdock particles into water to form an extracting solution; then pumping the extracting solution into a gauze filter, filtering small particle impurities in the extracting solution through the gauze filter, pumping the filtered extracting solution into a double-effect reduced pressure concentrator, preparing clear paste in the double-effect reduced pressure concentrator by a reduced pressure method, pumping the clear paste into a dryer, spraying the clear paste from a spray head in the dryer, heating the scattered clear paste to form dry paste powder in the dropping process, finally collecting the prepared dry paste powder and adding the dry paste powder into a granulator, and preparing finished product fried burdock formula granules through the granulator, thereby realizing the preparation of the product.
However, although this method can achieve the preparation of the product, the workers often react to the following technical problems in the actual production process: 1. in the extraction process, a large amount of fried arctium particles are accumulated in the extraction tank, the fried arctium particles accumulated on the middle layer and the bottom layer are not fully contacted with hot water at all, so that arctigenin in the fried arctium particles can be completely extracted by waiting for a long time, the time consumed by preparing the extracting solution is prolonged, the preparation efficiency of the extracting solution is reduced, and the production efficiency of products is further reduced. 2. Because stir-fry arctium fruit granule deposit is in the bottom of drawing the jar, after drawing, need the manual work to salvage out the stir-fry arctium fruit granule that draws in the jar to prepare for drawing next time, but artifical fishing speed is slower, can't realize once only salvaging stir-fry arctium fruit granule, has the technical defect that the waste discharge efficiency is low, and then has reduced the production efficiency of product. 3. After in extracting the interior back of liquid delivery economic benefits and social benefits decompression concentrator of jar, the workman need regularly unpack the end cover of gauze filter apart, take out the gauze from the gauze filter again, wash the gauze after taking out again to prevent that the gauze from being stopped up by impurity, but when tearing open the end cover, need twist out a plurality of locking screw on the end cover, could move aside the end cover, and then take out the gauze, this has increased workman's working strength undoubtedly, is unfavorable for the frequent washing to the gauze. 4. In the process of drying the clear paste by the drying machine, the clear paste sprayed out from the spray head is partially sprayed on the inner wall of the drying tank of the drying machine, and if the clear paste attached to the inner wall is not cleaned in time, the clear paste is sintered on the inner wall of the drying tank, so that the yield of dry paste powder is reduced, and the production yield of the fried burdock formula granules is further reduced. 5. In the granulation process, the product prepared by directly utilizing the dry paste powder has over-heavy medicinal taste and very poor mouthfeel.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a production line and a method for efficiently producing fried burdock formula particles, which have the advantages of compact structure, sintering prevention, reduction of the working strength of workers, improvement of the preparation efficiency of an extracting solution, improvement of the production efficiency of fried burdock formula particles and improvement of the taking taste.
The purpose of the invention is realized by the following technical scheme: the production line for efficiently producing the stir-fried burdock formula particles comprises an extraction device, a double-effect reduced pressure concentrator, a drying machine, a stirring device and a granulator which are sequentially connected.
The extraction device comprises a main frame, a subframe fixedly arranged at the top of the main frame, an extraction tank fixedly arranged on a top plate of the subframe, lifting oil cylinders are fixedly arranged on the left side wall and the right side wall of the extraction tank respectively, a lifting plate is fixedly arranged between the action ends of piston rods of the two lifting oil cylinders, a barrel is rotatably arranged in the lifting plate, the barrel sequentially penetrates through the lifting plate, the top end of the extraction tank extends into the extraction tank, a plurality of radial holes positioned in the extraction tank are formed in the cylindrical surface of the barrel, a detachable barrel cover is arranged at the bottom of the barrel, a power unit I for driving the barrel to rotate around the axis of the power unit is arranged on the lifting plate, a locking oil cylinder is fixedly arranged on a top plate of the main frame, an end cover is fixedly arranged on the action end of the piston rod of the locking oil cylinder, gauze is paved in the inner cavity of the end cover, and when the piston rod of the locking oil cylinder completely extends out, the gauze is pressed between the end cover and the bottom surface of the extraction tank, the bottom of the end cover is fixedly provided with a conical tube, and the bottom of the conical tube is connected with a liquid outlet valve.
The dryer comprises a tank body and a spherical spray head rotatably mounted on the top wall of the tank body, wherein a rotary joint is connected to an upper extending port of the spherical spray head, the tank body is fixedly arranged on an auxiliary frame, an upper annular pipe and a lower annular pipe are respectively welded to the inner wall of the tank body and positioned at the upper end part and the lower end part of the tank body, a plurality of upper air outlet holes arranged towards the outer side are formed in the lower surface of the upper annular pipe along the circumferential direction of the upper annular pipe, a plurality of lower air outlet holes arranged towards the inner side are formed in the upper surface of the lower annular pipe along the circumferential direction of the lower annular pipe, a rotating shaft penetrating through the upper annular pipe is welded at the bottom of the spherical spray head, a scraping blade is welded on the rotating shaft, and a driving unit II for driving the spherical spray head to rotate around the axis of the spherical spray head is arranged at the top of the tank body; the dryer also comprises an air blower and an air heater which are connected in sequence, wherein a three-way pipe is connected at an air outlet of the air heater, and two ports of the three-way pipe penetrate through the wall of the tank body and are respectively communicated with the upper annular pipe and the lower annular pipe;
the double-effect pressure-reducing concentrator is arranged below the main frame, a feed inlet of the double-effect pressure-reducing concentrator is connected with a liquid outlet valve through a pipeline, a discharge outlet of the double-effect pressure-reducing concentrator is connected with a material pump I, and a discharge outlet of the material pump I is connected with a top port of a rotary joint through a material pipe.
Draw on the back lateral wall of jar and be located its upper end and be provided with the inlet, inlet department is connected with the stop valve, be provided with the external screw thread on the cylinder of tip under the barrel, be provided with the internal thread on the inner wall of cover, the internal thread and the external screw thread threaded connection of cover.
The portal frame is fixedly arranged on the top plate of the subframe, the temporary storage tank is fixedly arranged on the cross beam of the portal frame, the bottom of the temporary storage tank is connected with a discharge valve, and the bottom port of the discharge valve is connected with the top port of the barrel through a hose.
The driving unit I comprises a speed reducer I fixedly arranged on the lifting plate, a motor I and a driven gear I fixedly arranged at the extending end of the cylinder, an output shaft of the motor I is connected with an input shaft of the speed reducer I, a driving gear I is arranged on an output shaft of the speed reducer I, and the driving gear I is meshed with the driven gear I.
And a plurality of brackets are welded between the scraping piece and the rotating shaft.
The driving unit II comprises a motor II fixedly arranged on the top surface of the tank body, a speed reducer II and a driven gear II arranged on the outer extending end of the spherical spray head, an output shaft of the motor II is connected with an input shaft of the speed reducer II, a driving gear II is arranged on an output shaft of the speed reducer II, and the driving gear II is meshed with the driven gear II.
And a plurality of circles of heating cables are wound outside the tank body.
Agitating unit includes agitator tank, storage tank A and storage tank B, and storage tank A and storage tank B all set firmly on subframe's roof, and the agitator tank sets up in the below of subframe roof, and storage tank A and storage tank B's bottom all is connected with the butterfly valve, and the bottom mouth of butterfly valve is connected with the top mouth of agitator tank, the feed inlet of agitator tank and the bottom mouth of the jar body are connected through the return bend, and the discharge gate department of agitator tank is connected with material pump II, and material pump II's row's material pipe is connected with the entry end of granulator.
The production line further comprises a controller, and the controller is electrically connected with the electromagnetic valve of the lifting oil cylinder, the electromagnetic valve of the locking oil cylinder, the motor I, the motor II, the air blower, the material pump I, the material pump II, the stop valve, the butterfly valve, the liquid outlet valve and the discharge valve.
The method for efficiently producing the stir-fried burdock formula particles by the production line comprises the following steps:
s1, ensuring that the stop valve, the butterfly valve, the liquid outlet valve and the discharge valve are all in a closed state; adding the processed stir-fried burdock particles into a temporary storage tank in advance, and adding lactose and maltodextrin into the storage tank A and the storage tank B respectively;
s2, preparing an extracting solution, wherein the specific operation steps are as follows:
s21, controlling the discharge valve to be opened, enabling the fried burdock particles in the temporary storage tank to sequentially pass through the discharge valve, the hose, the upper port of the barrel and the barrel under the self weight, finally entering the barrel, adding a certain amount of the burdock particles, and closing the discharge valve;
s22, controlling a stop valve at the liquid inlet, pumping hot water into the stop valve, enabling the hot water to flow into an area surrounded by the tank body and the gauze, after a certain amount of hot water is introduced, closing the stop valve at the liquid inlet, enabling the hot water to pass through the radial hole and enter the barrel, immersing the fried burdock particles in the barrel in the hot water, and extracting arctigenin in the fried burdock particles into the hot water to form an extracting solution; in the extraction process, the motor I is controlled to be started, the torque of the motor I is transmitted to the driving gear I after being reduced by the reducer I, the driving gear I rotates, the driving gear I drives the driven gear I to rotate, the driven gear I drives the barrel to rotate around the axis of the barrel, so that the fried burdock particles in the barrel do centrifugal motion in hot water, meanwhile, the piston rod of the lifting oil cylinder is controlled to do reciprocating lifting motion, the piston rod drives the lifting plate to do reciprocating lifting motion, the lifting plate drives the barrel to do reciprocating lifting motion synchronously, and the fried burdock particles in the barrel do up-and-down motion in the hot water; after a period of extraction, preparing an extract containing arctigenin in the tank;
s23, controlling the motor I to be closed, and controlling a piston rod of the lifting oil cylinder to be in a retraction state;
s3, preparing clear paste, controlling a liquid outlet valve to be started, enabling the extracting solution in a tank to pass through gauze under the action of gravity, enabling the extracting solution to finally enter a double-effect pressure-reducing concentrator through a tapered tube, the liquid outlet valve and a pipeline in sequence, starting the double-effect pressure-reducing concentrator after the extracting solution in the extracting tank is completely discharged into the double-effect pressure-reducing concentrator, carrying out pressure-reducing concentration on the extracting solution by the double-effect pressure-reducing concentrator, preparing the clear paste in the double-effect pressure-reducing concentrator after a period of time, and filtering small-particle impurities in the extracting solution by the gauze;
s4, preparation of dry paste powder, which comprises the following specific operation steps:
s41, connecting the joint of the heating cable to a power supply, and heating the heating cable to generate heat after the heating cable is electrified, wherein the heat heats the inside of the tank body;
s42, controlling a motor II to start, transmitting the torque of the motor II to a driving gear II after being reduced by a speed reducer II, driving the driving gear II to drive a driven gear II to rotate, driving a spherical spray head to rotate around the axis of the spherical spray head by the driven gear II, driving a rotating shaft to rotate by the spherical spray head, driving the scraping blade to rotate circumferentially by the rotating shaft through a support, and driving the scraping blade to move on the inner wall of the tank body;
s43, controlling the start of the blower and the air heater, sending outside air into the air heater by the blower, heating hot air by the air heater, enabling the hot air to enter the tee pipe under air pressure, dividing the hot air into two parts, respectively entering the inner cavities of the upper annular pipe and the lower annular pipe, ejecting the hot air in the upper annular pipe from the upper air outlet, ejecting the hot air obliquely downwards onto the inner wall of the tank body, and ejecting the hot air in the lower annular pipe from the lower air outlet, and enabling the hot air to move upwards;
s44, controlling a material pump I to start, pumping out the clear paste in the double-effect decompression concentrator by the material pump I, enabling the pumped clear paste to sequentially pass through the material pump I, a material pipe, a rotary joint, an upper port of a spherical nozzle and the spherical nozzle and finally to be sprayed out from a spray hole of the spherical nozzle, enabling the dispersed clear paste to enter a tank body and then to be heated to become dry paste powder, enabling the dry paste powder to sequentially pass through a central hole of a lower annular pipe and a bent pipe and finally enter a stirring tank to be collected, and finally realizing the preparation of the dry paste powder;
s5, mixing dry paste powder, controlling butterfly valves on a storage tank A and a storage tank B to start, under the gravity, enabling lactose in the storage tank A to enter a stirring tank through the butterfly valves, enabling maltodextrin in the storage tank B to enter the stirring tank through the butterfly valves, closing the butterfly valves after a period of time, then controlling a stirring motor on a stirring device to start, driving a blade to rotate by the stirring motor, and stirring and mixing the lactose, the maltodextrin and the dry paste powder by the blade;
and S6, controlling a material pump II to start, conveying the mixture in the stirring tank into the granulator through a discharge pipe by the material pump II, and conveying the finished stir-fried burdock formula particles out of the granulator.
The invention has the following advantages:
1. the extraction device comprises a main frame, a subframe fixedly arranged at the top of the main frame and an extraction tank fixedly arranged on a top plate of the subframe, wherein lifting oil cylinders are fixedly arranged on the left side wall and the right side wall of the extraction tank respectively, a lifting plate is fixedly arranged between action ends of piston rods of the two lifting oil cylinders, a cylinder is rotatably arranged in the lifting plate, the cylinder sequentially penetrates through the lifting plate and the top end of the extraction tank and extends into the extraction tank, a plurality of radial holes positioned in the extraction tank are formed in the cylindrical surface of the cylinder, a detachable cylinder cover is arranged at the bottom of the cylinder, and a power unit I for driving the cylinder to rotate around the axis of the cylinder is arranged on the lifting plate; the fried arctium fruit granule in the barrel has both been done centrifugal motion, up-and-down motion has been done again, make fried arctium fruit granule scatter apart on a large scale, fried arctium fruit granule and hydrothermal area of contact has been increased, compare traditional formula of piling up and draw, the preparation extraction liquid consumed time has been shortened, the quick hot water that enters into of arctigenin in the fried arctium fruit granule has been promoted, and then very big improvement the preparation efficiency of extract, and then improved the preparation efficiency of fried arctium fruit formula granule.
2. The drying machine comprises a tank body and a spherical spray head rotatably mounted on the top wall of the tank body, wherein a rotary joint is connected to an upper extending port of the spherical spray head, the tank body is fixedly arranged on an auxiliary frame, an upper annular pipe and a lower annular pipe are respectively welded to the upper end part and the lower end part of the inner wall of the tank body, a plurality of upper air outlet holes arranged towards the outer side are formed in the lower surface of the upper annular pipe along the circumferential direction of the upper annular pipe, a plurality of lower air outlet holes arranged towards the inner side are formed in the upper surface of the lower annular pipe along the circumferential direction of the lower annular pipe, a rotating shaft penetrating through the upper annular pipe is welded to the bottom of the spherical spray head, a scraping blade is welded to the rotating shaft, and a driving unit II for driving the spherical spray head to rotate around the axis of the spherical spray head is arranged at the top of the tank body; in the process that the clear paste is sprayed from the spherical nozzle, the rotating scraping blade scrapes the clear paste sprayed on the inner wall of the tank body, and meanwhile, hot air flow sprayed from the upper air outlet hole sprays on the inner wall of the tank body, and then the clear paste attached to the inner wall of the tank body is blown off, so that the clear paste is effectively prevented from being sintered on the inner wall of the tank body, and the yield of products is improved. In addition, the hot air flow jetted from the lower air outlet enables the jetted clear paste to float upwards so as to slow down the falling speed of the clear paste, and then dry paste powder which is drier is prepared.
3. The stirring device comprises a stirring tank, a storage tank A and a storage tank B, wherein the storage tank A and the storage tank B are fixedly arranged on a top plate of a subframe, the stirring tank is arranged below the top plate of the subframe, the bottoms of the storage tank A and the storage tank B are both connected with a butterfly valve, the bottom port of the butterfly valve is connected with the top port of the stirring tank, the feed inlet of the stirring tank is connected with the bottom port of a tank body through a bent pipe, the discharge outlet of the stirring tank is connected with a material pump II, and the discharge pipe of the material pump II is connected with the inlet end of a granulator; controlling butterfly valves on the storage tank A and the storage tank B to start, wherein under the gravity, lactose in the storage tank A enters a stirring tank through the butterfly valves, maltodextrin in the storage tank B enters the stirring tank through the butterfly valves, closing the butterfly valves after a period of time, then controlling a stirring motor on a stirring device to start, driving the blades to rotate by the stirring motor, and stirring and mixing the lactose, the maltodextrin and dry paste powder by the blades; and controlling a material pump II to start, conveying the mixture in the stirring tank into the granulator through a discharge pipe by the material pump II, and conveying the finished stir-fried burdock formula particles out of the granulator. Because the finished stir-fried arctium fruit formula particles also contain lactose and maltodextrin, compared with the traditional single product, the taste of a user is greatly improved.
4. A liquid inlet is formed in the rear side wall of an extraction tank and positioned at the upper end of the extraction tank, a stop valve is connected at the liquid inlet, external threads are formed on the cylindrical surface of the lower end of a cylinder body, internal threads are formed on the inner wall of a cylinder cover, and the internal threads of the cylinder cover are in threaded connection with the external threads; the piston rod of lift cylinder upwards stretches out, and the piston rod drives the lifter plate upward movement, and the lifter plate drives the barrel upward movement, stretches out the back completely as the piston rod, and the workman places the material receiving box under the barrel at this moment that the barrel shifts out from drawing the jar in, spins the cover from the barrel again, and after the back of unscrewing, useless stir-fry arctium fruit granule in the barrel falls into under gravity and connects the material box in and collect to the row material of useless stir-fry arctium fruit granule has been realized. Therefore, the waste stir-fried burdock formula particles do not need to be manually shoveled out of the extraction tank, the working strength of workers is greatly reduced, the waste material is discharged at one time, the time is saved for secondary extraction, the preparation efficiency of the extracting solution is improved, and the production efficiency of products is improved.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a front view of FIG. 1;
FIG. 3 is a schematic view of the structure of the extraction apparatus;
FIG. 4 is a front view of FIG. 3;
FIG. 5 is a schematic view of the connection between the cylinder and the cylinder cover;
FIG. 6 is a schematic view of the structure of the dryer;
FIG. 7 is a front view of FIG. 6;
FIG. 8 is an enlarged view of a portion I of FIG. 6;
FIG. 9 is an enlarged view of a portion of portion II of FIG. 6;
FIG. 10 is a cross-sectional view A-A of FIG. 6;
FIG. 11 is a schematic structural view of a stirring device;
FIG. 12 is a schematic view of the cartridge after it has been extended from the extraction tank;
FIG. 13 is a schematic view of the end cap separated from the extraction tank;
in the figure, 1-an extraction device, 2-a double-effect pressure-reducing concentrator, 3-a dryer, 4-a stirring device, 5-a granulator, 6-a main frame, 7-a subframe, 8-an extraction tank, 9-a lifting oil cylinder, 10-a lifting plate, 11-a cylinder body, 12-a radial hole, 13-a cylinder cover, 14-a locking oil cylinder, 15-an end cover, 16-gauze, 17-a conical pipe, 18-a liquid outlet valve, 19-a cylinder body, 20-a spherical nozzle, 21-an upper annular pipe, 22-a lower annular pipe, 23-an upper air outlet hole, 24-a lower air outlet hole, 25-a rotating shaft, 26-a scraper, 27-an air blower, 28-an air heater, 29-a three-way pipe, 30-a pipeline, 31-a material pump I, 32-material pipe, 33-liquid inlet, 35-external thread, 36-internal thread, 37-portal frame, 38-temporary storage tank, 39-discharge valve, 40-hose, 41-reducer I, 42-motor I, 43-driven gear I, 44-driving gear I, 45-support, 46-motor II, 47-reducer II, 48-driven gear II, 49-driving gear II, 50-heating cable, 51-stirring tank, 52-storage tank A, 53-storage tank B, 54-butterfly valve, 55-elbow, 56-material pump II, 57-discharge pipe, and 58-rotary joint.
Detailed Description
The invention will be further described with reference to the accompanying drawings, without limiting the scope of the invention to the following:
as shown in fig. 1 to 11, the production line for efficiently producing the stir-fried burdock formula granules comprises an extraction device 1, a double-effect reduced pressure concentrator 2, a dryer 3, a stirring device 4 and a granulator 5 which are sequentially connected.
The extraction device 1 comprises a main frame 6, a subframe 7 fixedly arranged at the top of the main frame 6, and an extraction tank 8 fixedly arranged on a top plate of the subframe 7, wherein lifting cylinders 9 are fixedly arranged on the left side wall and the right side wall of the extraction tank 8, a lifting plate 10 is fixedly arranged between action ends of piston rods of the two lifting cylinders 9, a barrel body 11 is rotatably arranged in the lifting plate 10, the barrel body 11 sequentially penetrates through the lifting plate 10, the top end of the extraction tank 8 and extends into the extraction tank 8, a plurality of radial holes 12 positioned in the extraction tank 8 are formed in the cylindrical surface of the barrel body 11, a detachable barrel cover 13 is arranged at the bottom of the barrel body 11, a power unit I for driving the barrel body 11 to rotate around the axis of the power unit is arranged on the lifting plate 10, a locking cylinder 14 is fixedly arranged on the top plate of the main frame 6, an end cover 15 is fixedly arranged on the action end of a piston rod of the locking cylinder 14, gauze 16 is paved in the inner cavity of the end cover 15, and when the piston rod of the locking cylinder 14 completely extends out, the gauze 16 is pressed between the end cover 15 and the bottom surface of the extraction pot 8, a conical tube 17 is fixedly arranged at the bottom of the end cover 15, and a liquid outlet valve 18 is connected at the bottom of the conical tube 17. Draw on jar 8's the back lateral wall and be located its upper end and be provided with inlet 33, inlet 33 department is connected with the stop valve, be provided with external screw thread 35 on the cylinder of tip under barrel 11, be provided with internal thread 36 on the inner wall of cover 13, the internal thread 36 and the external screw thread 35 threaded connection of cover 13. A portal frame 37 is fixedly arranged on a top plate of the subframe 7, a temporary storage tank 38 is fixedly arranged on a cross beam of the portal frame 37, the bottom of the temporary storage tank 38 is connected with a discharge valve 39, and a bottom port of the discharge valve 39 is connected with a top port of the barrel 11 through a hose 40. The driving unit I comprises a speed reducer I41 fixedly arranged on the lifting plate 10, a motor I42 and a driven gear I43 fixedly arranged at the extending end of the cylinder 11, an output shaft of the motor I42 is connected with an input shaft of the speed reducer I41, a driving gear I44 is arranged on an output shaft of the speed reducer I41, and the driving gear I44 is meshed with the driven gear I43.
The drying machine 3 comprises a tank body 19 and a spherical spray head 20 rotatably mounted on the top wall of the tank body 19, the upper extending port of the spherical spray head 20 is connected with a rotary joint 58, the tank body 19 is fixedly arranged on the subframe 7, an upper annular pipe 21 and a lower annular pipe 22 are respectively welded on the inner wall of the tank body 19 and positioned at the upper end and the lower end of the tank body, a plurality of upper air outlet holes 23 arranged towards the outer side are formed in the lower surface of the upper annular pipe 21 along the circumferential direction of the upper annular pipe, a plurality of lower air outlet holes 24 arranged towards the inner side are formed in the upper surface of the lower annular pipe 22 along the circumferential direction of the lower annular pipe, a rotating shaft 25 penetrating through the upper annular pipe 21 is welded at the bottom of the spherical spray head 20, a scraping blade 26 is welded on the rotating shaft 25, and a driving unit II for driving the spherical spray head 20 to rotate around the axis of the tank body 19 is arranged at the top of the tank body 19; the dryer 3 further comprises an air blower 27 and an air heater 28 which are connected in sequence, a three-way pipe 29 is connected to an air outlet of the air heater 28, and two ports of the three-way pipe 29 penetrate through the wall of the tank 19 and are respectively communicated with the upper annular pipe 21 and the lower annular pipe 22. A plurality of brackets 45 are welded between the scraping blade 26 and the rotating shaft 25. The driving unit II comprises a motor II46 fixedly arranged on the top surface of the tank 19, a speed reducer II47 and a driven gear II48 arranged at the outer extending end of the spherical nozzle 20, an output shaft of the motor II46 is connected with an input shaft of the speed reducer II47, an output shaft of the speed reducer II47 is provided with a driving gear II49, and the driving gear II49 is meshed with the driven gear II 48. The tank 19 is externally wound with a plurality of turns of a heating cable 50.
The double-effect pressure-reducing concentrator 2 is arranged below the main frame 6, a feed inlet of the double-effect pressure-reducing concentrator 2 is connected with the liquid outlet valve 18 through a pipeline 30, a discharge outlet of the double-effect pressure-reducing concentrator 2 is connected with a material pump I31, and a discharge outlet of the material pump I31 is connected with a top port of the rotary joint 58 through a material pipe 32.
Agitating unit 4 includes agitator tank 51, storage tank A52 and storage tank B53, and storage tank A52 and storage tank B53 all set firmly on the roof of subframe 7, and agitator tank 51 sets up the below of subframe 7 roof, and storage tank A52 and storage tank B53's bottom all are connected with butterfly valve 54, and the bottom mouth of butterfly valve 54 is connected with agitator tank 51's top port, agitator tank 51's feed inlet and jar 19's bottom mouth are connected through return bend 55, and agitator tank 51's discharge gate department is connected with material pump II56, and material pump II 56's row of material pipe 57 is connected with the entry end of granulator 5.
The production line further comprises a controller, and the controller is electrically connected with the electromagnetic valve of the lifting oil cylinder 9, the electromagnetic valve of the locking oil cylinder 14, the motor I42, the motor II46, the air blower 27, the material pump I31, the material pump II56, the stop valve, the butterfly valve 54, the liquid outlet valve 18 and the discharge valve 39.
The method for efficiently producing the stir-fried burdock formula particles by the production line comprises the following steps:
s1, ensuring that the stop valve, the butterfly valve 54, the liquid outlet valve 18 and the discharge valve 39 are all in a closed state; adding the processed parched fructus Arctii particles into the temporary storage tank 38, and adding lactose and maltodextrin into the storage tank A52 and the storage tank B53 respectively;
s2, preparing an extracting solution, wherein the specific operation steps are as follows:
s21, controlling the discharge valve 39 to be opened, enabling the fried burdock particles in the temporary storage tank 38 to sequentially pass through the discharge valve 39, the hose 40, the upper end opening of the barrel body 11 and the barrel body 11 under the self weight, and finally entering the barrel body 11, and closing the discharge valve 39 after adding a certain amount of the fried burdock particles;
s22, controlling a stop valve at the liquid inlet 33, pumping hot water into the stop valve, enabling the hot water to flow into an area surrounded by the tank body 19 and the gauze 16, and after a certain amount of hot water is introduced, closing the stop valve at the liquid inlet 33, enabling the hot water to pass through the radial hole 12 and enter the barrel body 11, soaking the stir-fried burdock particles in the barrel body 11 in the hot water, and extracting arctigenin in the stir-fried burdock particles into the hot water to form an extracting solution; in the extraction process, the motor I42 is controlled to be started, the torque of the motor I42 is transmitted to the driving gear I44 after being reduced by the reducer I41, the driving gear I44 rotates, the driving gear I44 drives the driven gear I43 to rotate, the driven gear I43 drives the cylinder 11 to rotate around the axis of the cylinder, so that fried burdock particles in the cylinder 11 do centrifugal motion in hot water, meanwhile, a piston rod of the lifting oil cylinder 9 is controlled to do reciprocating lifting motion, the piston rod drives the lifting plate 10 to do reciprocating lifting motion, the lifting plate 10 drives the cylinder 11 to do reciprocating lifting motion synchronously, and the fried burdock particles in the cylinder 11 do up-and-down motion in the hot water; after a period of extraction, the extracting solution containing arctigenin can be prepared in the tank 19; therefore, the fried burdock particles in the cylinder 11 do both centrifugal motion and up-and-down motion, so that the fried burdock particles are dispersed in a large range, the contact area of the fried burdock particles and hot water is increased, compared with the traditional stacking type extraction, the time consumed for preparing the extracting solution is shortened, the arctigenin in the fried burdock particles is promoted to rapidly enter the hot water, the preparation efficiency of the extracting solution is greatly improved, and the preparation efficiency of the fried burdock formula particles is improved;
s23, controlling the motor I42 to be closed, and controlling the piston rod of the lifting oil cylinder 9 to be in a retraction state;
s3, preparing clear paste, controlling the liquid outlet valve 18 to be started, enabling the extracting solution in the tank 19 to pass through the gauze 16 under the action of gravity, enabling the extracting solution to sequentially pass through the conical pipe 17, the liquid outlet valve 18 and the pipeline 30 and finally enter the double-effect reduced-pressure concentrator 2, starting the double-effect reduced-pressure concentrator 2 after all the extracting solution in the extracting tank 8 is discharged into the double-effect reduced-pressure concentrator 2, carrying out reduced-pressure concentration on the extracting solution by the double-effect reduced-pressure concentrator 2, and preparing the clear paste in the double-effect reduced-pressure concentrator 2 after a period of time, wherein the gauze 16 filters out small particle impurities of the extracting solution;
s4, preparation of dry paste powder, which comprises the following specific operation steps:
s41, connecting the joint of the heating cable 50 to a power supply, and heating the heating cable 50 to generate heat after being electrified, wherein the heat heats the inside of the tank 19;
s42, controlling a motor II46 to start, transmitting the torque of a motor II46 to a driving gear II49 after being reduced by a reducer II47, driving the driving gear II49 to drive a driven gear II48 to rotate, driving the spherical spray head 20 to rotate around the axis of the spherical spray head II48, driving the rotating shaft 25 to rotate by the spherical spray head 20, driving the scraping blade 26 to rotate circumferentially by the rotating shaft 25 through a support 45, and moving the scraping blade 26 on the inner wall of the tank 19;
s43, controlling the blower 27 and the air heater 28 to start, wherein the blower 27 sends outside air into the air heater 28, the air heater 28 heats hot air, the hot air enters the three-way pipe 29 under air pressure, the hot air is divided into two parts and respectively enters the inner cavities of the upper annular pipe 21 and the lower annular pipe 22, the hot air in the upper annular pipe 21 is ejected from the upper air outlet hole 23, the hot air is obliquely ejected downwards to the inner wall of the tank body 19, meanwhile, the hot air in the lower annular pipe 22 is ejected from the lower air outlet hole 24, and the hot air moves upwards;
s44, controlling a material pump I31 to start, pumping out the clear paste in the double-effect decompression concentrator 2 by the material pump I31, enabling the pumped clear paste to sequentially pass through the material pump I31, a material pipe 32, a rotary joint 58, an upper port of a spherical nozzle 20 and the spherical nozzle 20 and finally to be sprayed out from a spray hole of the spherical nozzle 20 in a rotating mode, enabling the dispersed clear paste to enter a tank body 19 and then to be heated to become dry paste powder, enabling the dry paste powder to sequentially penetrate through a central hole of a lower annular pipe 22 and a bent pipe 55 and finally enter a stirring tank 51 to be collected, and finally achieving preparation of the dry paste powder; in the process of spraying the clear paste from the spherical nozzle 20, the rotating scraping blade 26 scrapes the clear paste sprayed on the inner wall of the tank body 19, and meanwhile, hot air flow sprayed from the upper air outlet 23 is sprayed on the inner wall of the tank body 19, and then the clear paste attached to the inner wall of the tank body 19 is blown off, so that the clear paste is effectively prevented from being sintered on the inner wall of the tank body 19, and the product yield is improved. In addition, the hot air flow jetted from the lower air outlet 24 enables the jetted clear paste to float upwards so as to slow down the falling speed of the clear paste, and then dry paste powder which is drier is prepared.
S5, mixing dry paste powder, controlling butterfly valves on a storage tank A52 and a storage tank B53 to start, under the gravity, enabling lactose in the storage tank A52 to enter a stirring tank 51 through the butterfly valve 54, enabling maltodextrin in the storage tank B53 to enter the stirring tank 51 through the butterfly valve 54, closing the butterfly valve 54 after a period of time, then controlling a stirring motor on a stirring device 4 to start, driving a stirring blade to rotate, and stirring and mixing the lactose, the maltodextrin and the dry paste powder by the blade;
s6, controlling the material pump II56 to start, and conveying the mixture in the stirring tank 51 into the granulator 5 through the discharge pipe 57 by the material pump II56, and conveying the finished stir-fried burdock formula particles out of the granulator 5. Because the finished stir-fried arctium fruit formula particles also contain lactose and maltodextrin, compared with the traditional single product, the taste of a user is greatly improved.
S7, the row of useless fried burdock granule, the piston rod of control lift cylinder 9 upwards stretches out, the piston rod drives lifter plate 10 upward movement, lifter plate 10 drives barrel 11 upward movement, after the piston rod stretches out completely, barrel 11 shifts out from extracting jar 8 as shown in figure 12, the workman places the material receiving box under barrel 11 this moment, spin down cover 13 from barrel 11 again, after the back of unscrewing, useless fried burdock granule in the barrel 11 falls into under gravity and connects the box collection, thereby realized the row material of useless fried burdock granule. Therefore, the waste stir-fried burdock formula particles are not required to be manually shoveled out of the extraction tank 8, the working strength of workers is greatly reduced, the waste material is discharged at one time, the time is saved for secondary extraction, the preparation efficiency of the extracting solution is improved, and the production efficiency of products is improved.
S8, disassembling and washing the gauze, controlling the piston rod of the locking oil cylinder 14 to retract downwards, driving the end cover 15 to move downwards by the piston rod, separating the end cover 15 from the barrel 11 as shown in fig. 13, and directly taking the gauze 16 away from the end cover 15 by a worker, thereby greatly facilitating the cleaning of the gauze by the worker.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that changes may be made in the embodiments and/or equivalents thereof without departing from the spirit and scope of the invention. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (10)
1. Production line of arctium formula granule is fried in high-efficient production, its characterized in that: the device comprises an extraction device (1), a double-effect reduced pressure concentrator (2), a dryer (3), a stirring device (4) and a granulator (5) which are connected in sequence;
the extraction device (1) comprises a main frame (6), a subframe (7) fixedly arranged at the top of the main frame (6), and an extraction tank (8) fixedly arranged on a top plate of the subframe (7), wherein lifting oil cylinders (9) are fixedly arranged on the left side wall and the right side wall of the extraction tank (8), a lifting plate (10) is fixedly arranged between action ends of piston rods of the two lifting oil cylinders (9), a barrel body (11) is installed in the lifting plate (10) in a rotating manner, the barrel body (11) sequentially penetrates through the lifting plate (10), the top end of the extraction tank (8) extends into the extraction tank (8), a plurality of radial holes (12) positioned in the extraction tank (8) are formed in the cylindrical surface of the barrel body (11), a detachable barrel cover (13) is arranged at the bottom of the barrel body (11), a power unit I used for driving the barrel body (11) to rotate around the axis of the lifting plate (10) is arranged on the lifting plate, a locking oil cylinder (14) is fixedly arranged on the top plate of the main frame (6), an end cover (15) is fixedly arranged on the action end of a piston rod of the locking oil cylinder (14), gauze (16) is laid in the inner cavity of the end cover (15), when the piston rod of the locking oil cylinder (14) is completely extended out, the gauze (16) is pressed between the end cover (15) and the bottom surface of the extraction tank (8), a conical tube (17) is fixedly arranged at the bottom of the end cover (15), and the bottom of the conical tube (17) is connected with a liquid outlet valve (18);
the dryer (3) comprises a tank (19), the spherical spray head (20) is rotatably mounted on the top wall of the tank body (19), a rotary joint (58) is connected to an upper extending port of the spherical spray head (20), the tank body (19) is fixedly arranged on the subframe (7), an upper annular pipe (21) and a lower annular pipe (22) are respectively welded to the upper end and the lower end of the inner wall of the tank body (19), a plurality of upper air outlet holes (23) arranged towards the outer side are formed in the lower surface of the upper annular pipe (21) along the circumferential direction of the upper surface, a plurality of lower air outlet holes (24) arranged towards the inner side are formed in the upper surface of the lower annular pipe (22) along the circumferential direction of the lower surface, a rotating shaft (25) penetrating through the upper annular pipe (21) is welded to the bottom of the spherical spray head (20), a scraping blade (26) is welded to the rotating shaft (25), and a driving unit II for driving the spherical spray head (20) to rotate around the axis of the tank body (19) is arranged at the top of the tank body (19); the dryer (3) further comprises an air blower (27) and an air heater (28) which are connected in sequence, the air outlet of the air heater (28) is connected with a three-way pipe (29), and two ports of the three-way pipe (29) penetrate through the wall of the tank body (19) and are respectively communicated with the upper annular pipe (21) and the lower annular pipe (22);
double-effect vacuum concentrator (2) set up in the below of main frame (6), and its feed inlet is connected through pipeline (30) with play liquid valve (18), and the discharge gate department of double-effect vacuum concentrator (2) is connected with material pump I (31), and the bin outlet of material pump I (31) is connected through material pipe (32) with the top mouth of rotary joint (58).
2. The production line for efficiently producing stir-fried burdock formula particles according to claim 1, is characterized in that: draw on the back lateral wall of jar (8) and be located its upper end and be provided with inlet (33), inlet (33) department is connected with the stop valve, be provided with on the cylinder of tip under barrel (11) external screw thread (35), be provided with on the inner wall of cover (13) internal thread (36), internal thread (36) and external screw thread (35) threaded connection of cover (13).
3. The production line for efficiently producing stir-fried burdock formula particles according to claim 1, is characterized in that: a portal frame (37) is fixedly arranged on a top plate of the subframe (7), a temporary storage tank (38) is fixedly arranged on a cross beam of the portal frame (37), the bottom of the temporary storage tank (38) is connected with a discharge valve (39), and a bottom port of the discharge valve (39) is connected with a top port of the barrel (11) through a hose (40).
4. The production line for efficiently producing stir-fried burdock formula particles according to claim 1, is characterized in that: the driving unit I comprises a speed reducer I (41) fixedly arranged on the lifting plate (10), a motor I (42) and a driven gear I (43) fixedly arranged at the extending end of the cylinder body (11), an output shaft of the motor I (42) is connected with an input shaft of the speed reducer I (41), a driving gear I (44) is arranged on an output shaft of the speed reducer I (41), and the driving gear I (44) is meshed with the driven gear I (43).
5. The production line for efficiently producing stir-fried burdock formula particles according to claim 1, is characterized in that: a plurality of brackets (45) are welded between the scraping blade (26) and the rotating shaft (25).
6. The production line for efficiently producing stir-fried burdock formula particles according to claim 1, is characterized in that: the driving unit II comprises a motor II (46) fixedly arranged on the top surface of the tank body (19), a speed reducer II (47) and a driven gear II (48) arranged on the outer extending end of the spherical spray head (20), an output shaft of the motor II (46) is connected with an input shaft of the speed reducer II (47), a driving gear II (49) is arranged on an output shaft of the speed reducer II (47), and the driving gear II (49) is meshed with the driven gear II (48).
7. The production line for efficiently producing stir-fried burdock formula particles according to claim 1, is characterized in that: the outer part of the tank body (19) is wound with a plurality of circles of heating cables (50).
8. The production line for efficiently producing stir-fried burdock formula particles according to claim 1, is characterized in that: agitating unit (4) are including agitator tank (51), storage tank A (52) and storage tank B (53), and storage tank A (52) and storage tank B (53) all set firmly on the roof of subframe (7), and agitator tank (51) set up in the below of subframe (7) roof, and the bottom of storage tank A (52) and storage tank B (53) all is connected with butterfly valve (54), and the bottom mouth of butterfly valve (54) is connected with the top port of agitator tank (51), the feed inlet of agitator tank (51) is connected through return bend (55) with the bottom mouth of the jar body (19), and the discharge gate department of agitator tank (51) is connected with material pump II (56), and discharge tube (57) of material pump II (56) are connected with the entry end of granulator (5).
9. The production line for efficiently producing stir-fried burdock formula particles according to claim 1, is characterized in that: the production line further comprises a controller, and the controller is electrically connected with an electromagnetic valve of the lifting oil cylinder (9), an electromagnetic valve of the locking oil cylinder (14), a motor I (42), a motor II (46), an air blower (27), a material pump I (31), a material pump II (56), a stop valve, a butterfly valve (54), a liquid outlet valve (18) and a discharge valve (39).
10. The method for efficiently producing the stir-fried burdock formula particle according to any one of claims 1 to 9, which is characterized in that: it comprises the following steps:
s1, ensuring that the stop valve, the butterfly valve (54), the liquid outlet valve (18) and the discharge valve (39) are all in a closed state; adding the processed parched fructus Arctii particles into a temporary storage tank (38), and adding lactose and maltodextrin into a storage tank A (52) and a storage tank B (53), respectively;
s2, preparing an extracting solution, wherein the specific operation steps are as follows:
s21, controlling the discharge valve (39) to be opened, enabling the fried burdock particles in the temporary storage tank (38) to sequentially pass through the discharge valve (39), the hose (40), the upper end opening of the barrel body (11) and the barrel body (11) under the self weight, and finally entering the barrel body (11), adding a certain amount of the burdock particles, and closing the discharge valve (39);
s22, controlling a stop valve at the liquid inlet (33), pumping hot water into the stop valve, enabling the hot water to flow into an area surrounded by a tank body (19) and gauze (16), introducing a certain amount of hot water, closing the stop valve at the liquid inlet (33), enabling the hot water to pass through a radial hole (12) and enter a cylinder body (11), soaking the stir-fried burdock particles in the cylinder body (11) in the hot water, and extracting arctigenin in the stir-fried burdock particles into the hot water to form an extracting solution; in the extraction process, the motor I (42) is controlled to be started, the torque of the motor I (42) is transmitted to the driving gear I (44) after being reduced by the reducer I (41), the driving gear I (44) rotates, the driving gear I (44) drives the driven gear I (43) to rotate, the driven gear I (43) drives the barrel (11) to rotate around the axis of the driven gear I (43), so that the stir-fried burdock particles in the barrel (11) do centrifugal motion in hot water, meanwhile, the piston rod of the lifting oil cylinder (9) is controlled to do reciprocating lifting motion, the piston rod drives the lifting plate (10) to do reciprocating lifting motion, the lifting plate (10) drives the barrel (11) to do reciprocating lifting motion synchronously, and the stir-fried burdock particles in the barrel (11) do up-and-down motion in the hot water; after a period of extraction, the extracting solution containing arctigenin can be prepared in the tank (19);
s23, controlling the motor I (42) to be closed, and controlling a piston rod of the lifting oil cylinder (9) to be in a retraction state;
s3, preparing clear paste, controlling a liquid outlet valve (18) to be started, enabling an extracting solution in a tank body (19) to pass through gauze (16) under the action of gravity, enabling the extracting solution to sequentially pass through a conical pipe (17), the liquid outlet valve (18) and a pipeline (30) and finally enter a double-effect reduced pressure concentrator (2), starting the double-effect reduced pressure concentrator (2) after all extracting solution in an extracting tank (8) is discharged into the double-effect reduced pressure concentrator (2), carrying out reduced pressure concentration on the extracting solution by the double-effect reduced pressure concentrator (2), and preparing the clear paste in the double-effect reduced pressure concentrator (2) after a period of time, wherein small particle impurities in the extracting solution are filtered out by the gauze (16);
s4, preparation of dry paste powder, which comprises the following specific operation steps:
s41, connecting the joint of the heating cable (50) to a power supply, and heating the heating cable (50) after being electrified to emit heat to heat the inside of the tank body (19);
s42, controlling a motor II (46) to start, transmitting the torque of the motor II (46) to a driving gear II (49) after being reduced by a speed reducer II (47), driving the driving gear II (49) to drive a driven gear II (48) to rotate, driving the spherical spray head (20) to rotate around the axis of the spherical spray head II (48), driving a rotating shaft (25) to rotate by the spherical spray head (20), driving a scraping blade (26) to rotate circumferentially by the rotating shaft (25) through a support (45), and moving the scraping blade (26) on the inner wall of a tank body (19);
s43, controlling the starting of the air blower (27) and the air heater (28), sending outside air into the air heater (28) by the air blower (27), heating hot air by the air heater (28), enabling the hot air to enter the three-way pipe (29) under air pressure, dividing the hot air into two parts, respectively entering the inner cavities of the upper annular pipe (21) and the lower annular pipe (22), ejecting the hot air in the upper annular pipe (21) from the upper air outlet hole (23), ejecting the hot air obliquely downwards onto the inner wall of the tank body (19), and ejecting the hot air in the lower annular pipe (22) from the lower air outlet hole (24), and enabling the hot air to move upwards;
s44, controlling a material pump I (31) to start, pumping out the clear paste in the double-effect decompression concentrator (2) by the material pump I (31), enabling the pumped clear paste to sequentially pass through the material pump I (31), a material pipe (32), a rotary joint (58), the upper port of a spherical spray head (20) and the spherical spray head (20) and finally be sprayed out from a spray hole of the spherical spray head (20) in a rotating manner, enabling the dispersed clear paste to enter a tank body (19) and then become dry paste powder due to heating, enabling the dry paste powder to sequentially pass through a central hole of a lower annular pipe (22) and a bent pipe (55) and finally enter a stirring tank (51) to be collected, and finally realizing the preparation of the dry paste powder;
s5, mixing dry paste powder, controlling butterfly valves on a storage tank A (52) and a storage tank B (53) to start, allowing lactose in the storage tank A (52) to enter a stirring tank (51) through the butterfly valve (54) under the gravity, allowing maltodextrin in the storage tank B (53) to enter the stirring tank (51) through the butterfly valve (54), closing the butterfly valve (54) after a period of time, controlling a stirring motor on a stirring device (4) to start, driving the stirring motor to rotate, and stirring and mixing the lactose, the maltodextrin and the dry paste powder by the blades;
s6, controlling the material pump II (56) to start, conveying the mixture in the stirring tank (51) into the granulator (5) through the material discharge pipe (57) by the material pump II (56), and conveying the finished stir-fried burdock formula granules from the granulator (5).
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| CN212215528U (en) * | 2020-05-15 | 2020-12-25 | 潍坊鑫百顺工贸有限公司 | Mixture agitator tank for polyol with high stirring efficiency |
| CN111807544A (en) * | 2020-07-02 | 2020-10-23 | 海南发控智慧环境建设集团有限公司 | River water purifier |
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| CN115624785A (en) * | 2022-09-28 | 2023-01-20 | 河南联源生物科技股份有限公司 | Sealwort processing extraction equipment |
| CN115624785B (en) * | 2022-09-28 | 2023-12-22 | 河南联源生物科技股份有限公司 | Polygonatum sibiricum processing extraction equipment |
| CN117504707A (en) * | 2024-01-05 | 2024-02-06 | 泉州市精翔智能装备科技有限公司 | Powder auxiliary agent dispensing equipment |
| CN117504707B (en) * | 2024-01-05 | 2024-04-02 | 泉州市精翔智能装备科技有限公司 | Powder auxiliary agent dispensing equipment |
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