Production equipment and process of granular money-preserving and health-preserving paste

Abstract

The invention discloses production equipment and process for granular youfin-preserving and health-preserving paste, and relates to the technical field of traditional Chinese medicine granule production.The production equipment comprises a production tank, a liquid conveying assembly for conveying liquid medicine into the production tank, a gas inlet assembly for conveying high-temperature gas into the production tank, and an exhaust assembly for exhausting damp and hot gas in the production tank; a droplet generation assembly and a flow guide assembly are arranged in the middle of the inner side of the production tank; a particle treatment assembly is arranged at the lower end of the production tank; the liquid drop generation assembly comprises a rotating seat movably arranged in the middle of the inner side of the production tank, and a plurality of nozzles fixedly arranged on the upper edge of the rotating seat; according to the invention, by utilizing the high-speed rotation of the rotating seat, liquid drops are thrown out in an inclined upward direction after passing through the spray head, so that the heating time of the liquid drops in airflow is greatly prolonged, and the liquid drops can finally form fully-dried particles in the drying process.

Description

Technical Field

[0001] The present invention relates to the technical field of traditional Chinese medicine granule production, and particularly to a production device and process for granular Baojin health care paste. Background Art

[0002] Baojin health care paste is a granular health care product made from traditional Chinese medicinal materials. Its preparation method mainly includes first extracting the effective components from the traditional Chinese medicinal materials to form a medicinal liquid, then refining the medicinal liquid into liquid droplets, and then rapidly evaporating the moisture of the liquid droplets in high-temperature hot air, and finally further drying to form dry granules.

[0003] In the invention patent with the publication number of CN119565180A, a traditional Chinese medicine extract spray dryer is disclosed. When in use, a hot air blower discharges hot air into an exhaust duct, and the hot air sequentially passes through an exhaust rack, an exhaust groove, and an air outlet rack and enters the inside of a fixed tank body. The medicinal liquid enters a discharge tank through a drain pipe, and a spray head is used to spray the medicinal liquid entering the discharge tank in a mist form. Through continuous blowing of the hot air blower, the medicinal liquid entering the fixed tank body is dried into powder, and through the inclined exhaust groove, the air blows more evenly on the spray during the drying process.

[0004] In the above device, the medicinal liquid is atomized, and the atomized medicinal liquid is heated by high-temperature air flow to produce medicinal powder. Although the hot air can blow more evenly on the spray during the drying process and uniformly dry the atomized liquid droplets, since the device sprays downward and the hot air also sprays downward, this causes the high-temperature air flow to accelerate the falling of the liquid droplets, reducing the heating time of the liquid droplets in the air flow, and easily making the produced granules not completely dried; moreover, the hot air sprayed downward easily fuses the liquid droplets sprayed downward together and aggregates them into large-diameter liquid droplets. The formed large liquid droplets are not only not easy to be dried sufficiently, but also easily cause the produced granules to have inconsistent sizes, which will all result in low quality of the produced extract. Therefore, we propose a production device and process for granular Baojin health care paste. Summary of the Invention

[0005] The purpose of the present invention is to provide a production device and process for granular Baojin health care paste, which can effectively solve the problems raised in the background art.

[0006] To solve the above technical problems, the present invention is realized through the following technical solutions:

[0007] The present invention is a production device for granular Baojin health care paste, including a production tank, an infusion assembly for conveying the medicinal liquid into the production tank, an air intake assembly for conveying high-temperature gas into the production tank, and an exhaust assembly for discharging the humid and hot gas inside the production tank. A liquid droplet generating assembly and a diversion assembly are arranged in the middle of the inner side of the production tank, and a granule processing assembly is arranged at the lower end of the production tank;

[0008] The droplet generation assembly includes a rotating seat movably arranged in the middle inside of the production tank, and a plurality of spray heads fixedly arranged on the upper edge of the rotating seat. The rotating seat ejects the liquid medicine introduced by the liquid infusion assembly in the form of droplets in an obliquely upward direction through the spray heads;

[0009] An air inlet pipe is fixedly arranged at the bottom of the production tank. The air outlet end of the air inlet pipe penetrates through the bottom of the production tank and extends into the interior of the production tank. The flow guiding assembly includes a flow guiding seat fixedly arranged above the air outlet end of the air inlet pipe, a flow guiding pipe fixedly arranged above the flow guiding seat, and a fan blade fixedly arranged directly below the spray head. The lower end of the flow guiding seat is an inverted frustum structure, and the fan blade is located inside the flow guiding pipe;

[0010] The particle processing assembly includes a plurality of blanking plates arranged below the interior of the production tank. One end of the blanking plate is fixedly connected to the outer wall of the air inlet pipe. The plurality of blanking plates are distributed in a spiral shape, and there is a gap for gas flow between adjacent two blanking plates.

[0011] Preferably, an inner groove and a plurality of liquid guiding holes are formed inside the rotating seat. The plurality of liquid guiding holes are evenly spaced around the inner groove and are all communicated with the inner groove. The lower end of the inner groove is a frustum structure. The liquid inlet of the liquid guiding hole is located at the lowermost end of the inner groove. The liquid guiding hole is an arc structure. The height of the liquid inlet of the liquid guiding hole is lower than the height of the liquid outlet of the liquid guiding hole. The number of the liquid guiding holes is the same as that of the spray heads and they correspond one by one. The liquid inlet of the spray head is communicated with the liquid outlet of the liquid guiding hole corresponding to the spray head.

[0012] Preferably, a positioning plate is fixedly arranged above the tank cover of the production tank. A positioning pipe is integrally arranged at the bottom of the positioning plate. The bottom of the positioning pipe penetrates through the tank cover of the production tank and extends into the interior of the production tank. A rotating pipe is movably arranged inside the positioning pipe. A positioning seat is fixedly arranged above the positioning plate. The rotating pipe is movably connected to the positioning seat. A transmission assembly for driving the rotating pipe to rotate is fixedly arranged on one side above the production tank. The rotating seat extends into the bottom of the positioning pipe and is fixedly connected to the rotating pipe.

[0013] Preferably, an infusion pipe is arranged inside the rotating pipe. The infusion pipe is movably and sealingly connected to the rotating pipe. A fixed seat is fixedly arranged above the positioning seat. The infusion pipe passes through the interior of the fixed seat and is fixedly connected to the fixed seat. The infusion pipe is communicated with the inner groove. The liquid outlet end of the liquid infusion assembly is fixedly connected to the liquid inlet end of the infusion pipe.

[0014] Preferably, a heat conducting pipe is sleeved above the side surface of the positioning pipe. A plurality of heat conducting discs which are evenly spaced are fixedly arranged on the outer side of the heat conducting pipe. The outer edge of the heat conducting disc is fixedly connected with the inner wall of the production tank. A plurality of exhaust holes are formed in each heat conducting disc. The heat conducting disc is of a frustum-shaped tubular structure. An air outlet pipe communicating with the inside of the production tank is arranged above the side surface of the production tank. The air inlet end of the air outlet pipe is located on one side of the uppermost heat conducting disc. The air inlet end of the exhaust assembly is fixedly connected with the air outlet end of the air outlet pipe.

[0015] Preferably, a plurality of anti-touch rings which are evenly spaced are fixedly arranged at the upper end of the inner wall of the production tank. The cross section of the anti-touch ring is of a triangular structure.

[0016] Preferably, the diversion assembly further includes a connecting pipe fixedly arranged at the air outlet end of the air inlet pipe. The connecting pipe is located directly below the diversion seat. The connecting pipe is of an inverted frustum-shaped structure. A connecting shaft is fixedly installed in the middle of the connecting pipe. An installation frame is fixedly arranged at the upper end of the connecting shaft. The diversion pipe is fixedly arranged above the installation frame.

[0017] Preferably, the particle treatment assembly further includes a spiral sheet arranged below the inside of the production tank. The inner side of the spiral sheet is fixedly connected with the outer wall of the air inlet pipe. The outer side of the spiral sheet is fixedly connected with the inner wall of the production tank. The spiral sheet and a plurality of spiral-shaped blanking plates have the same pitch. The bottom of the spiral sheet contacts with the inner bottom wall of the production tank. The lowermost blanking plate contacts with the inner bottom wall of the production tank. A gap for air flow exists between the spiral sheet and the plurality of spiral-shaped blanking plates. A auxiliary heat pipe is arranged at the bottom of the production tank. The air inlet end of the auxiliary heat pipe is fixedly connected with the air inlet pipe. The air outlet end of the auxiliary heat pipe penetrates through the bottom wall of the production tank and is fixedly connected with the spiral sheet. The air inlet pipe is communicated with the auxiliary heat pipe. The gap between the spiral sheet and the blanking plates is communicated with the auxiliary heat pipe.

[0018] Preferably, a discharge pipe is fixedly arranged at the bottom of the production tank. The feed inlet of the discharge pipe is located at the blanking end of the lowermost blanking plate. A discharge gate is fixedly arranged at the bottom of the discharge pipe. A collection box is fixedly arranged at the bottom of the discharge gate.

[0019] A production process of granular Baojin health care paste includes the following steps:

[0020] S1. Use the air inlet assembly to input high-temperature gas into the air inlet pipe. The high-temperature gas enters the production tank through the air inlet pipe and the auxiliary heat pipe to preheat the inside of the production tank. At the same time, use the exhaust assembly to discharge the gas inside the production tank.

[0021] S2. First, use the infusion component to input the liquid medicine into the inside of the infusion tube, and then use the transmission component to drive the rotating tube and the rotating seat to rotate. The liquid medicine enters the inner groove of the rotating seat, and the rotating seat throws the liquid medicine out in the form of droplets in an obliquely upward direction through the nozzle during the rotation process;

[0022] S3. During the rotation of the nozzle, the nozzle drives the fan blades to rotate synchronously in the diversion tube to form an upward high-temperature airflow. The high-temperature airflow blows the droplets thrown out from the nozzle upward, evaporating the water in the droplets. The upward speed of the droplets gradually decreases until they start to fall. The high-temperature airflow in the intake pipe is discharged through the connecting pipe and then flows obliquely upward through the diversion seat. The obliquely upward flowing airflow holds up the droplets and slows down the falling speed of the droplets;

[0023] S4. During the process from the droplets being ejected from the nozzle to starting to fall, the droplets are dried into particles. The particles continue to move towards the inner wall of the production tank under the action of centrifugal force and the blowing of the airflow. The particles fall on the inclined surface of the anti-touch ring. The particles slide down along the inclined surface of the anti-touch ring and then continue to fall. The falling particles continue to fall onto the inclined surface of the next anti-touch ring under the blowing of the airflow until the particles fall from the inclined surface of the lowermost anti-touch ring onto the lower middle inner wall of the production tank inner wall. Finally, the particles enter the blanking plate and continue to roll downward along the plurality of blanking plates;

[0024] S5. The particles are further dried when contacting the blanking plate. The high-temperature airflow entering the gap between the spiral fins and the blanking plate from the auxiliary heat pipe blows towards the particles through the gap between the blanking plates to dry the particles synchronously;

[0025] S6. The thoroughly dried particles enter the collection box through the discharge pipe and the discharge gate.

[0026] The present invention has the following beneficial effects:

[0027] 1. In the present invention, by using the high-speed rotation of the rotating seat, the droplets are thrown out in an obliquely upward direction after passing through the nozzle, causing the droplets to form a movement trajectory of first rising and then falling in the production tank, increasing the path of the droplets to the inner wall of the production tank, greatly increasing the heating time of the droplets in the airflow, enabling the droplets to finally form fully dried particles during the drying process, and the formed particles will not deform and break after being touched.

[0028] 2. In the present invention, by driving the fan blades to rotate synchronously during the high-speed rotation of the rotating seat, a high-speed upward airflow is formed in the diversion tube. The high-speed airflow pushes the droplets thrown out from the nozzle upward, which further increases the path of the droplets from being thrown out by the nozzle to the inner wall of the production tank, thereby further increasing the heating time of the droplets in the airflow and ensuring more complete drying of the droplets by the device. Moreover, by the structure of the fan blades and the diversion tube, the flow rate of the high-temperature airflow near the droplets is increased, which can quickly take away the water in the droplets and accelerate the drying speed of the droplets.

[0029] 3. In the present invention, by rotating the rotating seat at a high speed to throw out the liquid medicine to form droplets, and using the high-speed air flow generated by the fan blades and the diversion pipe to push the droplets, the droplets discharged from the nozzle can be quickly dispersed, avoiding the contact between the droplets to form large droplets, which may cause inconsistent particle sizes of the produced particles. At the same time, avoiding the contact between the droplets to form large droplets can prevent the incomplete drying of the large droplets by the device, and avoid the problem of high humidity of the produced particles.

[0030] 4. In the present invention, the high-temperature air flow discharged from the air inlet pipe flows obliquely upward after passing through the diversion seat with an inverted frustum-shaped structure, which plays a role in lifting the droplets that are gradually turning into particles, delaying the falling speed of the droplets, and similarly improving the drying time of the droplets in the air flow, and also contributing to the drying of the droplets. And by lifting the particles, the falling speed of the particles can be reduced, the impact force received when the particles collide can be reduced, and the particles can be prevented from being damaged.

[0031] 5. In the present invention, by arranging a plurality of blanking plates below the interior of the production tank, since the blanking plates are always in a high-temperature state when connected to the air inlet pipe, the particles will be continuously dried after contacting the blanking plates, which is convenient for removing the moisture on the surface of the particles, and can make the particles completely dry finally during the process of falling along the plurality of blanking plates. By arranging gaps for gas flow between two adjacent blanking plates, it is convenient for the high-temperature steam generated during the drying process to flow upward through the gaps, facilitating the discharge of the steam, and avoiding the problem that the steam in the plurality of blanking plates is difficult to discharge, resulting in poor drying effect of the structure on the particles. The plurality of blanking plates form a spiral shape, which can not only block the steam above the interior of the production tank, preventing the steam above the interior of the production tank from entering the lower part of the interior of the production tank, but also increase the residence time of the particles in the lower part of the interior of the production tank, making the drying ability of the particles stronger. BRIEF DESCRIPTION OF THE DRAWINGS

[0032] In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following will briefly introduce the drawings required for the description of the embodiments. Obviously, the following drawings are only some embodiments of the present invention. For those of ordinary skill in the art, other drawings can be obtained based on these drawings without creative efforts.

[0033] Figure 1 It is a perspective view of a production device for granular Baojin health care paste according to the present invention;

[0034] Figure 2 It is a perspective cross-sectional view of the production tank of a production device for granular Baojin health care paste according to the present invention;

[0035] Figure 3 It is a perspective cross-sectional view of the droplet generation assembly and the diversion assembly of a production device for granular Baojin health care paste according to the present invention;

[0036] Figure 4 Stereogram of the air inlet pipe and the particle processing component of a granular Baojin health-care paste production device of the present invention;

[0037] Figure 5 Of a granular Baojin health-care paste production device of the present invention Figure 4 Enlarged view of part A in

[0038] Figure 6 Stereogram of the droplet generation component of a granular Baojin health-care paste production device of the present invention;

[0039] Figure 7 Stereo cross-sectional view of the rotating seat of a granular Baojin health-care paste production device of the present invention;

[0040] Figure 8 Stereogram of the heat conduction tube and the heat conduction plate of a granular Baojin health-care paste production device of the present invention;

[0041] Figure 9 Stereogram of the production tank of a granular Baojin health-care paste production device of the present invention;

[0042] Figure 10 Stereogram of the anti-touch ring of a granular Baojin health-care paste production device of the present invention.

[0043] In the drawings, the list of components represented by each reference numeral is as follows:

[0044] 1. Liquid infusion component; 2. Air inlet component; 3. Exhaust component; 4. Production tank; 5. Droplet generation component; 51. Rotating seat; 52. Nozzle; 6. Flow guiding component; 61. Flow guiding seat; 62. Flow guiding tube; 63. Fan blade; 64. Connecting tube; 7. Particle processing component; 71. Feeding plate; 72. Spiral blade; 73. Auxiliary heat conduction tube; 8. Air inlet pipe; 9. Inner groove; 10. Liquid guiding hole; 11. Positioning plate; 12. Positioning tube; 13. Rotating tube; 14. Positioning seat; 15. Transmission component; 16. Liquid infusion tube; 17. Fixed seat; 18. Heat conduction tube; 19. Heat conduction plate; 20. Exhaust hole; 21. Air outlet pipe; 22. Anti-touch ring; 23. Connecting shaft; 24. Mounting frame; 25. Discharge pipe; 26. Discharge gate; 27. Collection box. Detailed implementation manners

[0045] Next, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts belong to the scope of protection of the present invention.

[0046] Embodiment:

[0047] Please refer to Figure 1 - Figure 10 As shown in the figure, a granular Baojin health care paste production device includes a production tank 4, an infusion component 1 for conveying liquid medicine into the production tank 4, an air inlet component 2 for conveying high-temperature gas into the production tank 4, and an exhaust component 3 for discharging the humid and hot gas inside the production tank 4. A liquid droplet generating component 5 and a diversion component 6 are arranged in the middle of the inner side of the production tank 4, and a particle processing component 7 is arranged at the lower end of the production tank 4; the infusion component 1, the air inlet component 2, and the exhaust component 3 are all arranged on the side of the production tank 4.

[0048] The liquid droplet generating component 5 includes a rotating seat 51 movably arranged in the middle of the inner side of the production tank 4, and a plurality of nozzles 52 fixedly arranged on the upper edge of the rotating seat 51. The rotating seat 51 throws the liquid medicine introduced by the infusion component 1 in the form of liquid droplets in an obliquely upward direction through the nozzles 52; the rotating seat 51 rotates at a high speed to throw out the liquid medicine in the nozzles 52 to form liquid droplets, and the liquid droplets enter the high-temperature airflow and are heated. The thrown liquid droplets are affected by the centrifugal force and continuously approach the inner wall of the production tank 4.

[0049] In order to solve the problem that the heating time of the liquid droplets is short during the production of the existing Baojin health care paste, resulting in insufficient drying of the particles formed during the falling process in the production tank 4, and the particles are prone to deformation and breakage after being touched. Based on this device, by using the high-speed rotation of the rotating seat 51, the liquid droplets are thrown out in an obliquely upward direction after passing through the nozzles 52, so that the liquid droplets form a movement trajectory of rising first and then falling in the production tank 4, increasing the path of the liquid droplets to the inner wall of the production tank 4, greatly increasing the heating time of the liquid droplets in the airflow, and enabling the liquid droplets to finally form fully dried particles during the drying process, so that the formed particles will not deform and break after being touched.

[0050] An air inlet pipe 8 is fixedly arranged at the bottom of the production tank 4. The air outlet end of the air inlet pipe 8 penetrates through the bottom of the production tank 4 and extends into the production tank 4. The diversion component 6 includes a diversion seat 61 fixedly arranged above the air outlet end of the air inlet pipe 8, a diversion pipe 62 fixedly arranged above the diversion seat 61, and a fan blade 63 fixedly arranged directly below the nozzle 52. The lower end of the diversion seat 61 is an inverted frustum structure, and the fan blade 63 is located inside the diversion pipe 62.

[0051] In order to further extend the drying time of the droplets in the high-temperature airflow and make the drying capacity of the device for the droplets stronger, based on this device, during the high-speed rotation of the rotating seat 51, the fan blades 63 are driven to rotate synchronously, forming an upward high-speed airflow in the diversion pipe 62. The high-speed airflow is used to push the droplets ejected from the nozzle 52 upward, which further increases the path of the droplets from being ejected from the nozzle 52 to the inner wall of the production tank 4, thereby increasing the heating time of the droplets in the airflow again and ensuring more complete drying of the droplets by the device. Moreover, by the structures of the fan blades 63 and the diversion pipe 62, the flow rate of the high-temperature airflow near the droplets is increased, and the moisture in the droplets can be quickly carried away, accelerating the drying speed of the droplets.

[0052] By making the rotating seat 51 rotate at a high speed to eject the liquid medicine to form droplets and using the high-speed airflow generated by the fan blades 63 and the diversion pipe 62 to push the droplets, the droplets discharged from the nozzle 52 can be quickly dispersed, avoiding the formation of large droplets due to the mutual contact between the droplets, which may lead to inconsistent particle sizes of the produced particles. At the same time, it also avoids the formation of large droplets due to the mutual contact between the droplets, and the incomplete drying of the large droplets by the device, resulting in the problem of high humidity of the produced particles.

[0053] The high-temperature airflow discharged from the air inlet pipe 8 flows obliquely upward after passing through the diversion seat 61 with an inverted frustum-shaped structure, providing a lifting effect for the droplets that are gradually turning into particles, delaying the falling speed of the droplets, and similarly increasing the drying time of the droplets in the airflow, and also contributing to the drying of the droplets. And by lifting the particles, the falling speed of the particles can be reduced, the impact force received when the particles collide can be reduced, and the particles can be prevented from being damaged.

[0054] The particle processing component 7 includes a plurality of blanking plates 71 arranged below the interior of the production tank 4. One end of the blanking plate 71 is fixedly connected to the outer wall of the air inlet pipe 8, and the plurality of blanking plates 71 are spirally distributed, and there are gaps for gas flow between adjacent two blanking plates 71.

[0055] To avoid the influence of high-temperature steam in the production tank 4 on the dried particles and reduce the particle quality, based on this device, by arranging a plurality of blanking plates 71 below the interior of the production tank 4, since the blanking plates 71 are always in a high-temperature state when connected to the air inlet pipe 8, the particles will be continuously dried after contacting the blanking plates 71, facilitating the removal of moisture on the surface of the particles, and enabling the particles to be finally completely dried during the process of falling along the plurality of blanking plates 71. By arranging a gap for gas flow between two adjacent blanking plates 71, it is convenient for the high-temperature steam generated during the drying process to flow upward through the gap, facilitating the discharge of the steam, and avoiding the problem that the steam in the plurality of blanking plates 71 is difficult to discharge, resulting in poor drying effect of the structure on the particles. The plurality of blanking plates 71 forming a spiral shape can not only block the steam above the interior of the production tank 4, preventing the steam above the interior of the production tank 4 from entering the lower part of the interior of the production tank 4, but also increase the residence time of the particles in the lower part of the interior of the production tank 4, making the drying ability of the particles stronger.

[0056] Among them, an inner groove 9 and a plurality of liquid guide holes 10 are formed inside the rotating seat 51. The plurality of liquid guide holes 10 are evenly spaced around the inner groove 9 and are all communicated with the inner groove 9. The lower end of the inner groove 9 is of a frustum-shaped structure. The liquid inlet of the liquid guide hole 10 is located at the lowermost end of the inner groove 9. The liquid guide hole 10 is of an arc-shaped structure. The height of the liquid inlet of the liquid guide hole 10 is lower than the height of the liquid outlet of the liquid guide hole 10. The number of the liquid guide holes 10 and the nozzles 52 is the same and they correspond one by one. The liquid inlet of the nozzle 52 is communicated with the liquid outlet of the liquid guide hole 10 corresponding to the nozzle 52.

[0057] Based on this device, by forming a frustum-shaped inner groove 9 and an arc-shaped liquid guide hole 10 inside the rotating seat 51, the liquid medicine in the inner groove 9 can be subjected to centrifugal force during the high-speed rotation of the rotating seat 51, facilitating the liquid medicine in the inner groove 9 to enter the nozzle 52 through the liquid guide hole 10. After the liquid medicine is completely delivered in the liquid delivery assembly 1, it is convenient to completely discharge the inner groove 9 and the liquid guide hole 10, solving the problem of liquid medicine residue in the inner groove 9 and the liquid guide hole 10.

[0058] Among them, a positioning plate 11 is fixedly arranged above the tank cover of the production tank 4. A positioning tube 12 is integrally arranged at the bottom of the positioning plate 11. The bottom of the positioning tube 12 penetrates through the tank cover of the production tank 4 and extends into the interior of the production tank 4. A rotating tube 13 is movably arranged inside the positioning tube 12. A positioning seat 14 is fixedly arranged above the positioning plate 11. The rotating tube 13 is movably connected to the positioning seat 14. A transmission assembly 15 for driving the rotating tube 13 to rotate is fixedly arranged on one side above the production tank 4. The rotating seat 51 extends into the bottom of the positioning tube 12 and is fixedly connected to the rotating tube 13.

[0059] Based on this device, the positioning plate 11 and the positioning tube 12 are fixedly installed above the lid of the production tank 4. The transmission assembly 15 drives the rotating tube 13 to rotate in the positioning tube 12, thereby driving the rotating seat 51 to rotate. The positioning seat 14 facilitates further positioning of the rotating tube 13, making the rotation of the rotating tube 13 more stable.

[0060] Among them, an infusion tube 16 is arranged inside the rotating tube 13. The infusion tube 16 is movably and hermetically connected to the rotating tube 13. A fixed seat 17 is fixedly arranged above the positioning seat 14. The infusion tube 16 passes through the inside of the fixed seat 17 and is fixedly connected to the fixed seat 17. The infusion tube 16 is communicated with the inner groove 9, and the liquid outlet end of the infusion assembly 1 is fixedly connected to the liquid inlet end of the infusion tube 16.

[0061] Based on this device, by arranging the infusion tube 16 inside the rotating tube 13 and connecting the infusion tube 16 to the infusion assembly 1, it is convenient for the liquid medicine to stably enter the inner groove 9, preventing the liquid medicine from being disturbed during the transportation process, making all the droplet shapes and sizes discharged from the nozzle 52 close, making the shapes and sizes of the granular Baojin health care paste produced consistent, and making the quality of the granular Baojin health care paste produced higher.

[0062] Among them, a heat conduction tube 18 is sleeved above the side surface of the positioning tube 12. A plurality of heat conduction discs 19 evenly spaced are fixedly arranged on the outer side of the heat conduction tube 18. The outer edge of each heat conduction disc 19 is fixedly connected to the inner wall of the production tank 4. A plurality of exhaust holes 20 are opened inside each heat conduction disc 19. The heat conduction disc 19 is a frustum-shaped tubular structure. An air outlet pipe 21 communicated with the inside of the production tank 4 is arranged above the side surface of the production tank 4. The air inlet end of the air outlet pipe 21 is located on one side of the uppermost heat conduction disc 19. The air inlet end of the exhaust assembly 3 is fixedly connected to the air outlet end of the air outlet pipe 21.

[0063] Based on this device, the setting of a plurality of heat conduction discs 19 and the opening of exhaust holes 20 in the heat conduction discs 19 can reduce the cross-section of the air flow channel above the inside of the production tank 4, facilitating the same air flow velocity in each exhaust hole 20 in the heat conduction discs 19, so that the upward air flows in various parts above the inside of the production tank 4 are more similar, making the air flow inside the production tank 4 more regular, and facilitating the movement rules of the liquid droplets and particles inside the production tank 4. Both the heat conduction disc 19 and the heat conduction tube 18 are structures with good heat conduction effects, which are convenient for absorbing the heat in the steam and conducting the heat into the liquid medicine through the positioning tube 12, the rotating tube 13 and the infusion tube 16 in sequence, facilitating the preheating of the liquid medicine in the infusion tube 16, and making it easier for the liquid medicine to be dried after forming droplets.

[0064] Among them, a plurality of evenly spaced anti-touch rings 22 are fixedly arranged at the upper end of the inner wall of the production tank 4. The cross-section of the anti-touch ring 22 is a triangular structure.

[0065] Based on this device, the anti-contact ring 22 is used to prevent the particles from contacting the inner wall of the production tank 4. After the particles fall on the inclined surface of the upper anti-contact ring 22 and are pushed by the airflow, they land on the inclined surface of the lower anti-contact ring 22, so that the particles will not contact the inner wall of the production tank 4, preventing the powder from adhering to the inner wall of the production tank 4 after the particles contact the inner wall of the production tank 4. The height of the inclined surface of the anti-contact ring 22 is small, and the attached powder is less, which is easy to remove under the blowing of the airflow.

[0066] Among them, the diversion assembly 6 further includes a connecting pipe 64 fixedly arranged at the air outlet end of the air inlet pipe 8. The connecting pipe 64 is located directly below the diversion seat 61. The connecting pipe 64 is an inverted frustum-shaped structure. A connecting shaft 23 is fixedly installed in the middle of the interior of the connecting pipe 64. The upper end of the connecting shaft 23 is fixedly provided with a mounting bracket 24, and the diversion pipe 62 is fixedly arranged above the mounting bracket 24.

[0067] Based on this device, the connecting pipe 64 is an inverted frustum-shaped structure, which facilitates the airflow discharged from the connecting pipe 64 to blow obliquely upward, facilitating the formation of an airflow for lifting the particles near the inner wall of the production tank 4.

[0068] Among them, the particle processing assembly 7 further includes a spiral fin 72 arranged below the interior of the production tank 4. The inner side of the spiral fin 72 is fixedly connected to the outer wall of the air inlet pipe 8, and the outer side of the spiral fin 72 is fixedly connected to the inner wall of the production tank 4. The spiral fin 72 and the plurality of spiral-shaped blanking plates 71 have the same pitch. The bottom of the spiral fin 72 contacts the inner bottom wall of the production tank 4, and the lowermost blanking plate 71 contacts the inner bottom wall of the production tank 4. There is a gap for the airflow to flow between the spiral fin 72 and the plurality of spiral-shaped blanking plates 71. A secondary heat pipe 73 is arranged at the bottom of the production tank 4. The air inlet end of the secondary heat pipe 73 is fixedly connected to the air inlet pipe 8, and the air outlet end of the secondary heat pipe 73 penetrates the bottom wall of the production tank 4 and is fixedly connected to the spiral fin 72. The air inlet pipe 8 is communicated with the secondary heat pipe 73, and the gap between the spiral fin 72 and the blanking plate 71 is communicated with the secondary heat pipe 73.

[0069] Based on this device, the high-temperature airflow in the secondary heat pipe 73 enters the gap between the spiral fin 72 and the plurality of spiral-shaped blanking plates 71, facilitating the formation of a strong airflow in the gap between two adjacent blanking plates 71, thereby blowing away the steam on the particles above the blanking plate 71 and the attached powder above the blanking plate 71. At the same time, the spiral fin 72 can block the steam below the blanking plate 71 from contacting the particles above the blanking plate 71, making the drying effect on the particles better.

[0070] Among them, a discharge pipe 25 is fixedly arranged at the bottom of the production tank 4. The feed port of the discharge pipe 25 is located at the discharge end of the lowermost blanking plate 71. A discharge gate 26 is fixedly arranged at the bottom of the discharge pipe 25, and a collection box 27 is fixedly arranged at the bottom of the discharge gate 26.

[0071] During the production process, close the discharge gate 26, and then open the collection box 27 to inspect the quality of the granular Baojin health care paste in the collection box 27.

[0072] A production process for granular Baojin health care paste includes the following steps:

[0073] S1. Input high-temperature gas into the intake pipe 8 using the intake component 2. The high-temperature gas enters the production tank 4 through the intake pipe 8 and the auxiliary heat pipe 73 to preheat the inside of the production tank 4. At the same time, use the exhaust component 3 to discharge the gas inside the production tank 4.

[0074] S2. First, input the liquid medicine into the inside of the infusion pipe 16 using the infusion component 1. Then, use the transmission component 15 to drive the rotation of the rotating pipe 13 and the rotating seat 51. The liquid medicine enters the inner groove 9 of the rotating seat 51, and the rotating seat 51 throws the liquid medicine out in the form of droplets in an obliquely upward direction through the nozzle 52 during the rotation process.

[0075] S3. During the rotation of the nozzle 52, the fan blade 63 is driven to rotate synchronously in the guide pipe 62 to form an upward high-temperature air flow. The high-temperature air flow blows the droplets thrown out from the nozzle 52 upward to evaporate the water in the droplets. The upward speed of the droplets gradually decreases until they start to fall. The high-temperature air flow in the intake pipe 8 is discharged through the connecting pipe 64 and then flows obliquely upward through the guide seat 61. The obliquely upward flowing air flow supports the droplets and slows down the falling speed of the droplets.

[0076] S4. During the process from the droplets being ejected from the nozzle 52 to starting to fall, the droplets are dried into particles. The particles continue to move towards the inner wall of the production tank 4 under the action of centrifugal force and the blowing of the air flow. The particles land on the inclined surface of the anti-contact ring 22, slide down along the inclined surface of the anti-contact ring 22 and then continue to fall. The falling particles continue to fall onto the inclined surface of the next anti-contact ring 22 under the blowing of the air flow until the particles fall from the inclined surface of the lowermost anti-contact ring 22 onto the lower middle inner wall of the inner wall of the production tank 4. Finally, the particles enter the blanking plate 71 and continue to roll downward along the plurality of blanking plates 71.

[0077] S5. The particles come into contact with the blanking plate 71 and are further dried. The high-temperature air flow that enters the gap between the spiral fin 72 and the blanking plate 71 from the auxiliary heat pipe 73 blows through the gap between the blanking plates 71 towards the particles to dry the particles synchronously.

[0078] S6. The thoroughly dried particles enter the collection box 27 through the discharge pipe 25 and the discharge gate 26.

[0079] The preferred embodiments of the present invention disclosed above are only used to help illustrate the present invention. The preferred embodiments do not describe all the details in detail, nor do they limit the invention to only the specific embodiments. Obviously, many modifications and variations can be made according to the content of this specification. These embodiments are selected and specifically described in this specification in order to better explain the principles and practical applications of the present invention, so that those skilled in the art can well understand and utilize the present invention. The present invention is only limited by the claims and their full scope and equivalents.

Claims

1. A granular Baojin health-care paste production device, comprising a production tank (4), an infusion assembly (1) for conveying liquid medicine into the production tank (4), an air inlet assembly (2) for conveying high-temperature gas into the production tank (4), and an exhaust assembly (3) for discharging the humid and hot gas inside the production tank (4), characterized in that: In the middle of the inner side of the production tank (4), a droplet generating assembly (5) and a flow guiding assembly (6) are arranged, and a particle processing assembly (7) is arranged at the lower end of the production tank (4); The droplet generating assembly (5) includes a rotating seat (51) movably arranged in the middle of the inner side of the production tank (4), and a plurality of spray heads (52) fixedly arranged on the upper edge of the rotating seat (51). The rotating seat (51) throws the liquid medicine introduced by the liquid infusion assembly (1) in a droplet shape in an obliquely upward direction through the spray heads (52); An air inlet pipe (8) is fixedly arranged at the bottom of the production tank (4). The air outlet end of the air inlet pipe (8) penetrates through the bottom of the production tank (4) and extends into the interior of the production tank (4). The flow guiding assembly (6) includes a flow guiding seat (61) fixedly arranged above the air outlet end of the air inlet pipe (8), a flow guiding pipe (62) fixedly arranged above the flow guiding seat (61), and a fan blade (63) fixedly arranged directly below the spray head (52). The lower end of the flow guiding seat (61) is an inverted frustum structure, and the fan blade (63) is located inside the flow guiding pipe (62); The particle processing assembly (7) includes a plurality of blanking plates (71) arranged below the interior of the production tank (4). One end of the blanking plate (71) is fixedly connected to the outer wall of the air inlet pipe (8). The plurality of blanking plates (71) are spirally distributed, and there is a gap for gas flow between adjacent blanking plates (71).

2. The granular Baojin health care paste production equipment according to claim 1, characterized in that: An inner groove (9) and a plurality of liquid guiding holes (10) are formed inside the rotating seat (51). The plurality of liquid guiding holes (10) are evenly spaced around the inner groove (9) and are all communicated with the inner groove (9). The lower end of the inner groove (9) is a frustum structure. The liquid inlet of the liquid guiding hole (10) is located at the lowermost end of the inner groove (9). The liquid guiding hole (10) is an arc structure. The height of the liquid inlet of the liquid guiding hole (10) is lower than the height of the liquid outlet of the liquid guiding hole (10). The number of the liquid guiding holes (10) is the same as that of the spray heads (52) and they correspond one by one. The liquid inlet of the spray head (52) is communicated with the liquid outlet of the liquid guiding hole (10) corresponding to the spray head (52).

3. The granular Baojin health-care paste production equipment according to claim 2, characterized in that: A positioning plate (11) is fixedly arranged above the tank cover of the production tank (4). A positioning pipe (12) is integrally arranged at the bottom of the positioning plate (11). The bottom of the positioning pipe (12) penetrates through the tank cover of the production tank (4) and extends into the interior of the production tank (4). A rotating pipe (13) is movably arranged inside the positioning pipe (12). A positioning seat (14) is fixedly arranged above the positioning plate (11). The rotating pipe (13) is movably connected to the positioning seat (14). A transmission assembly (15) for driving the rotating pipe (13) to rotate is fixedly arranged on one side above the production tank (4). The rotating seat (51) extends into the bottom of the positioning pipe (12) and is fixedly connected to the rotating pipe (13).

4. A production device for granular Baojin health-care paste according to claim 3, characterized in that: An infusion tube (16) is arranged inside the rotating tube (13). The infusion tube (16) is movably and sealingly connected to the rotating tube (13). A fixed seat (17) is fixedly arranged above the positioning seat (14). The infusion tube (16) passes through the inside of the fixed seat (17). The infusion tube (16) is fixedly connected to the fixed seat (17). The infusion tube (16) communicates with the inner groove (9). The liquid outlet end of the infusion assembly (1) is fixedly connected to the liquid inlet end of the infusion tube (16).

5. A granular Baojin health care cream production device according to claim 4, characterized in that: A heat-conducting tube (18) is sleeved above the side surface of the positioning tube (12). A plurality of heat-conducting disks (19) evenly spaced are fixedly arranged on the outer side of the heat-conducting tube (18). The outer edge of the heat-conducting disk (19) is fixedly connected to the inner wall of the production tank (4). A plurality of exhaust holes (20) are formed in each of the heat-conducting disks (19). The heat-conducting disk (19) is of a frustum-shaped tubular structure. An air outlet pipe (21) communicating with the inside of the production tank (4) is arranged above the side surface of the production tank (4). The air inlet end of the air outlet pipe (21) is located on one side of the uppermost heat-conducting disk (19). The air inlet end of the exhaust assembly (3) is fixedly connected to the air outlet end of the air outlet pipe (21).

6. A granular Baojin health-care paste production device according to claim 5, characterized in that: A plurality of anti-touch rings (22) evenly spaced are fixedly arranged at the upper end of the inner wall of the production tank (4). The cross section of the anti-touch ring (22) is of a triangular structure.

7. A granular Baojin health care paste production device according to claim 6, characterized in that: The diversion assembly (6) further includes a connecting pipe (64) fixedly arranged at the liquid outlet end of the air inlet pipe (8). The connecting pipe (64) is located directly below the diversion seat (61). The connecting pipe (64) is of an inverted frustum-shaped structure. A connecting shaft (23) is fixedly installed in the middle of the inside of the connecting pipe (64). An installation frame (24) is fixedly arranged at the upper end of the connecting shaft (23). The diversion pipe (62) is fixedly arranged above the installation frame (24).

8. A production device for granular Baojin health care paste according to claim 7, characterized in that: The particle treatment assembly (7) further includes a spiral blade (72) arranged below the inside of the production tank (4). The inner side of the spiral blade (72) is fixedly connected to the outer wall of the air inlet pipe (8). The outer side of the spiral blade (72) is fixedly connected to the inner wall of the production tank (4). The spiral blade (72) has the same pitch as a plurality of spiral distribution blanking plates (71). The bottom of the spiral blade (72) contacts the inner bottom wall of the production tank (4). The lowermost blanking plate (71) contacts the inner bottom wall of the production tank (4). A gap for air flow exists between the spiral blade (72) and the plurality of spiral distribution blanking plates (71). A auxiliary heat pipe (73) is arranged at the bottom of the production tank (4). The air inlet end of the auxiliary heat pipe (73) is fixedly connected to the air inlet pipe (8). The air outlet end of the auxiliary heat pipe (73) penetrates through the bottom wall of the production tank (4) and is fixedly connected to the spiral blade (72). The air inlet pipe (8) communicates with the auxiliary heat pipe (73). The gap between the spiral blade (72) and the blanking plate (71) communicates with the auxiliary heat pipe (73).

9. A production device for granular Baojin health-care paste according to claim 8, characterized in that: A discharge pipe (25) is fixedly arranged at the bottom of the production tank (4). The feed inlet of the discharge pipe (25) is located at the discharge end of the lowermost blanking plate (71). A discharge gate (26) is fixedly arranged at the bottom of the discharge pipe (25), and a collection box (27) is fixedly arranged at the bottom of the discharge gate (26).

10. A production process of granular Baojin health care paste, which is produced by using the equipment described in claim 9, is characterized in that, It includes the following steps: S1. Use the air inlet assembly (2) to input high-temperature gas into the intake pipe (8). The high-temperature gas enters the production tank (4) through the intake pipe (8) and the auxiliary heat pipe (73) to preheat the inside of the production tank (4). At the same time, use the exhaust assembly (3) to discharge the gas inside the production tank (4). S2. First, use the liquid infusion assembly (1) to input the liquid medicine into the liquid infusion pipe (16). Then, use the transmission assembly (15) to drive the rotation of the rotating pipe (13) and the rotating seat (51). The liquid medicine enters the inner groove (9) of the rotating seat (51). During the rotation of the rotating seat (51), the liquid medicine is thrown out in the form of droplets in an obliquely upward direction through the nozzle (52). S3. During the rotation of the nozzle (52), the fan blade (63) is driven to rotate synchronously in the diversion pipe (62) to form an upward high-temperature air flow. The high-temperature air flow blows the droplets thrown out from the nozzle (52) upward to evaporate the water in the droplets. The upward speed of the droplets gradually decreases until they start to fall. The high-temperature air flow in the intake pipe (8) is discharged through the connecting pipe (64) and then flows obliquely upward through the diversion seat (61). The obliquely upward flowing air flow holds up the droplets and slows down the falling speed of the droplets. S4. During the process from being sprayed out of the nozzle (52) to starting to fall, the droplets are dried into particles. The particles continue to move towards the inner wall of the production tank (4) under the action of centrifugal force and the blowing of the air flow. The particles fall on the inclined surface of the anti-touch ring (22). The particles slide down along the inclined surface of the anti-touch ring (22) and then continue to fall. The falling particles continue to fall onto the inclined surface of the next anti-touch ring (22) under the blowing of the air flow until the particles fall from the inclined surface of the lowermost anti-touch ring (22) onto the lower middle inner wall of the inner wall of the production tank (4). Finally, the particles enter the blanking plate (71) and continue to roll down along the multiple blanking plates (71). S5. The particles come into contact with the blanking plate (71) and are further dried. The high-temperature air flow entering the gap between the spiral fin (72) and the blanking plate (71) from the auxiliary heat pipe (73) blows through the gap between the blanking plates (71) to dry the particles synchronously. S6. The completely dried particles enter the collection box (27) through the discharge pipe (25) and the discharge gate (26).

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