CN204170103U - Air cooling dripping pill production line - Google Patents
Air cooling dripping pill production line Download PDFInfo
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- CN204170103U CN204170103U CN201420383996.4U CN201420383996U CN204170103U CN 204170103 U CN204170103 U CN 204170103U CN 201420383996 U CN201420383996 U CN 201420383996U CN 204170103 U CN204170103 U CN 204170103U
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Landscapes
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Abstract
A kind of air cooling dripping pill production line, comprise drop pill system, air cooling blood circulation and control system, drop pill system comprises material tank and coupled water dropper, is provided with vibrating device between material tank and water dropper, and vibrating device drives water dropper up-down vibration, the nibbling shear shear force produced, cut into by the medicinal liquid flowed out in water dropper and drip, form drop pill after falling into the cooling of air cooling blood circulation, water dropper mainly comprises a dish, drip dish and be provided with multiple drip hole, the periphery of drip hole offers spill annular groove; Internal diameter=drip hole the internal diameter+0.4 millimeter of spill annular groove, external diameter >=1.5 millimeter, groove depth is 0.5-5 millimeter.This utility model offers spill annular groove by the periphery of drip hole, and preventing, when thick liquid sprays at a high speed, has remaining medicinal liquid to pile up around spray orifice, finally causes spray orifice block or affect dripping; In conjunction with high frequency cutting dripping, on-line real-time measuremen regulating and controlling drop pill quality, improve productive rate.
Description
Technical field
This utility model relates to a kind of air cooling dripping pill production line, belongs to pill dripping machine manufacturing technology field.
Background technology
Drop pill is a kind of conventional dosage forms in Chinese medicine preparation, with short production cycle with it, onset is rapid, medicine stability is high and the plurality of advantages and obtaining of the storage that is easy to carry generally is approved.
Existing drop pill production method is essentially nature dripping and in conjunction with liquid cools, or the pressurization dropping preparation method to be improved by natural dropping preparation method in conjunction with liquid cools, the defect of existing equipment is: 1, based on the characteristic of liquid cooling medium, adopt the drop pill of this kind of type of cooling dripping, the heavy scope of ball can be subject to certain restrictions, usually, between 20-30mg, micropill or large ball all cannot drippings.2, simultaneously, for ensureing dripping effect, a large amount of substrate need be added in raw material medicinal liquid, causing unit drug loading little, the corresponding increase of dosage.3, in addition, adopt the mode of liquid cools, need the solid-liquor separation carrying out drop pill and liquid coolant, both thorough lock out operation get up more difficult, and therefore, liquid coolant can exist residual unavoidably on drop pill, causes drop pill to pollute.4, when needs adjustment output, traditional dripping equipment is general only to be regulated by change water dropper and pressure, and dripping frequency is lower, add the paraffin heat exchange surface area that needs are larger, cycle efficieny is low, and energy consumption is large, cause equipment volume large, easily there is clean dead angle, cross contamination risk is large.
In addition, existing water dropper, when thick liquid sprays at a high speed, has remaining medicinal liquid and piles up around drip nozzle, finally cause drip nozzle block and affect dripping.In use likely the frequency of occurrences is unstable to be arranged on the vibrating device dripped on dish, causes into ball size heterogeneity, directly affects the end product quality of drop pill.
How existing dripping equipment is improved, comprise the stability in dripping process, effectively increase drop pill forming quality and raising speed of production, improve drug loading, and expand drop pill can dripping size range, reduce energy consumption and coolant simultaneously, preventing drop pill from polluting, is development trend and the research direction of the improvement of current drilling pill device.
Utility model content
Technical problem to be solved in the utility model is for the deficiencies in the prior art, a kind of air cooling dripping pill production line is provided, first vibration dripping, air cooling and fluidized drying coating are combined as a whole, and be applied to dropping pill formulation and drop pill capsule preparations, meet in drop pill preparation high speed dripping, the requirement preparing micropill ability and raising drug loading, significantly improve drop pill drug loading, significantly reduce supplementary product consumption and taking dose; Operation sequence simplifies, and complete organic solvent-free remains; Meet the different process requirement comprising sustained release coating, film coating and sugar coating.Really reach low energy consumption, at a high speed, efficiently, high drug load, possessing widely can dripping scope; Periphery further by drip hole offers spill annular groove, and preventing, when thick liquid sprays at a high speed, has remaining medicinal liquid to pile up around spray orifice, finally causes spray orifice block or affect dripping.
Technical problem to be solved of the present utility model is achieved by the following technical solution:
A kind of air cooling dripping pill production line, comprise drop pill system, air cooling blood circulation and control system, drop pill system comprises material tank and coupled water dropper, is provided with vibrating device between described material tank and water dropper, and vibrating device drives water dropper up-down vibration, the nibbling shear shear force produced, cut into by the medicinal liquid flowed out in water dropper and drip, form drop pill after falling into the cooling of air cooling blood circulation, described water dropper mainly comprises a dish, drip dish and be provided with multiple drip hole, the periphery of drip hole offers spill annular groove.
As required, the internal diameter=drip hole internal diameter+0.4 millimeter of described spill annular groove, external diameter >=1.5 millimeter, groove depth is 0.5-5 millimeter.
For the ease of on-line monitoring and control, described water dropper is provided with on-Line Monitor Device, this device comprises pulse signal trigger mechanism, the tranmitting frequency of described pulse signal trigger mechanism is identical with the frequency of vibration of described vibrating device, control system according to the monitoring result of on-Line Monitor Device, regulating and controlling dripping parameter.
For the ease of observing, described on-Line Monitor Device is arranged on the side below described water dropper; Described pulse signal trigger mechanism is stroboscopic lamp, and described stroboscopic lamp is identical with the frequency of vibration of vibrating device; In order to make observed result more accurately and effectively retain monitoring record, described on-Line Monitor Device also comprises the photographic head that arrange corresponding to stroboscopic lamp, and photographic head and stroboscopic lamp are in same level, and to irradiate route with stroboscopic lamp be 15 ° of-145 ° of angles.
Specifically, described dripping parameter mainly comprises:
The frequency of vibration of described stroboscopic lamp and vibrating device: 50-300HZ, preferred 90-200Hz, optimum 130-140HZ;
Dripping speed: 10-40Kg/hr, preferred 12-30Kg/hr, optimum 15-25Kg/hr;
Dripping acceleration: 1-20G, preferred 3-10G, optimum 3.5-4.5G;
Dripping pressure: 0.5-4.0Bar, preferred 1.0-3.0Bar, optimum 1.8Bar;
Water dropper temperature: 70-200 DEG C, preferred 70-100 DEG C, optimum 75-85 DEG C.
In order to ensure dripping temperature constant, described water dropper outside is provided with incubation cavity, the skin of described incubation cavity is provided with heat-barrier material, internal layer is provided with steam heater or infrared heating device, the below of incubation cavity is provided with opening, the position of opening is corresponding with the exit position of water dropper to be arranged, and the size of opening is corresponding with the width of water dropper to be arranged.
Described air cooling blood circulation comprises: cooling pipe, and is connected with described cooling pipe and the refrigerating plant freezed to cooling pipe, is provided with interlayer outside described cooling pipe, and described interlayer bottom is communicated with cooling pipe inside by connected entrance;
Described refrigerating plant comprises: cold wind refrigerating plant and cold-trap refrigerating plant, wherein:
Described cold wind refrigerating plant comprises: freezer, and the air outlet of described freezer is connected with the cold air inlet of cooling pipe, and cold wind is circulated rising in cooling pipe inner chamber;
Described cold-trap refrigerating plant comprises: the coolant storage tank that coolant is housed, and the refrigeration machine that the coolant in coolant storage tank freezed and heat exchanger, the refrigerant inlet that refrigerant exit and the described interlayer top of described coolant storage tank are arranged is connected, coolant, by refrigerant inlet input interlayer, transfers to interlayer bottom from interlayer top and is transferred to cooling pipe inner chamber; Described coolant circulates with cold wind simultaneously rises in the inner chamber of cooling pipe, and by cooling pipe top discharge or recovery;
In order to reach good cooling effect, described cooling pipe is straight barrel type or spiral type pipe, and its length is 5-10 rice; Be preferably 6 meters.
Frosting is prevented in order to keep clean, described cooling pipe is provided with on-line cleaning equipment, comprise: cleaning unit, control unit, elevation driving unit and lifting unit, described control unit drives lifting unit to drive cleaning unit lifting by elevation driving unit, and described lifting unit is arranged on the cooling pipe top outer of chiller;
Described lifting unit comprises: cleaning unit bracing frame, cleanser conduit, cleanser conduit bracing frame, cleanser conduit storage tray and sealing adapter; Described cleanser conduit bracing frame makes cleanser conduit extend to cooling pipe inside; Described cleaning unit support comprises multiple support wheel, support wheel described in each and cooling pipe medial wall are supported, one end that described cleaning unit extends to cooling pipe inside with described cleanser conduit is connected, and makes cleaning unit prolong the lifting of cooling pipe center by cleaning unit bracing frame; One end of described sealing adapter is connected with the other end of cleanser conduit, for being imported by cleaning solution in described cleanser conduit;
Described lifting unit also comprises: on-Line Monitor Device, described on-Line Monitor Device comprises: image acquisition units and computing unit, described image acquisition units is arranged on described cleaning unit, for gathering the real time imaging in cooling pipe, picture signal is sent to computing unit, described computing unit is converted to numerical value according to this picture signal and compares with threshold value, if this numerical value is greater than threshold value, then sends drive singal to control unit and drives described cleaning unit to clean.
This air cooling dripping pill production line also comprises fluidized drying coated systems, this system mainly comprises fluid bed, the end of described cooling pipe is connected with the entrance of fluid bed by vacuum pipe, and the drop pill element ball vacuum feeding of shaping through air cooling is inputted fluidized drying coating in fluid bed;
Described fluid bed comprises body of heater, material feeding mouth is provided with below body of heater, airflow-distribution board is provided with in the below of described charging aperture, the bottom of described airflow-distribution board is connected with the wind pipe of room temperature low humidity supply air system, low for room temperature humid gas is sent in fluid bed body of heater through wind pipe by described room temperature low humidity supply air system, and carries out fluidized drying process to the material being built in furnace interior;
Described room temperature low humidity supply air system comprises housing and is arranged on the low humidity unit in housing, and housing is provided with intake stack and wind pipe, inputs described body of heater after air enters housing from intake stack after the process of low humidity unit through wind pipe;
Described room temperature low humidity supply air system also comprises the return air duct for air flow recovery, and two ends are connected with housing with described body of heater respectively.
The baking temperature of described fluid bed is-20 DEG C-100 DEG C, and drying time is 1-4 hour; Described fluid bed preferably adopts gradient increased temperature seasoning, and-20-30 DEG C forms fluidisation state, 15-35 DEG C dry 10-120 minute, 35-55 DEG C dry 10-60 minute, 55-100 DEG C of dry 0-60 minute; Most preferably 0-20 DEG C forms fluidisation state, 25 DEG C of dryings 60 minutes, 45 DEG C of dryings 30 minutes, 55 DEG C of dry 0-30 minute.
In sum, vibration dripping, air cooling and fluidized drying coating are combined as a whole by this utility model, and be applied to dropping pill formulation and drop pill capsule preparations, meet in drop pill preparation high speed dripping, the requirement preparing micropill ability and raising drug loading, significantly improve drop pill drug loading, significantly reduce supplementary product consumption and taking dose; Operation sequence simplifies, and complete organic solvent-free remains; Meet the different process requirement comprising sustained release coating, film coating and sugar coating.Really reach low energy consumption, at a high speed, efficiently, high drug load, possessing widely can dripping scope; Periphery further by drip hole offers spill annular groove, and preventing, when thick liquid sprays at a high speed, has remaining medicinal liquid to pile up around spray orifice, finally causes spray orifice block or affect dripping.
Below in conjunction with the drawings and specific embodiments, the technical solution of the utility model is described in detail.
Accompanying drawing explanation
Fig. 1 is this utility model overall structure schematic diagram;
Fig. 2 is that this utility model drips dish sectional view;
Fig. 3 is the A partial structurtes enlarged drawing of Fig. 2;
Fig. 4 is this utility model refrigerating device structure schematic diagram;
Fig. 5 is the overall structure schematic diagram of this utility model on-line cleaning equipment;
Fig. 6 is the control block diagram of this utility model on-line cleaning equipment;
Fig. 7 is the overall structure schematic diagram of this utility model fluid bed.
Detailed description of the invention
Fig. 1 is this utility model overall structure schematic diagram.As shown in Figure 1, this utility model provides a kind of air cooling dripping pill production line, comprise drop pill system, air cooling blood circulation and control system, drop pill system comprises material tank 100 and coupled water dropper 200, vibrating device 300 is provided with between described material tank 100 and water dropper 200, vibrating device drives water dropper up-down vibration, the nibbling shear shear force produced, the medicinal liquid flowed out in water dropper is cut into and drips, drop pill is formed after falling into the cooling of air cooling blood circulation, described water dropper is provided with on-Line Monitor Device, this device comprises pulse signal trigger mechanism, the tranmitting frequency of described pulse signal trigger mechanism is identical with the frequency of vibration of described vibrating device, control system is according to the monitoring result of on-Line Monitor Device, regulating and controlling dripping parameter.Described dripping parameter comprises: the frequency of vibration of described stroboscopic lamp and vibrating device: 50-300HZ, preferred 90-200Hz, optimum 130-140HZ; Dripping speed: 10-40Kg/hr, preferred 12-30Kg/hr, optimum 15-25Kg/hr; Dripping acceleration: 1-20G, preferred 3-10G, optimum 3.5-4.5G; Dripping pressure: 0.5-4.0Bar, preferred 1.0-3.0Bar, optimum 1.8Bar; Water dropper temperature: 70-200 DEG C, preferred 70-100 DEG C, optimum 75-85 DEG C.
As required, described on-Line Monitor Device is arranged on the side below described water dropper; Described pulse signal trigger mechanism is stroboscopic lamp 201, and described stroboscopic lamp is identical with the frequency of vibration of vibrating device.For the ease of observing and record, described on-Line Monitor Device can also comprise the photographic head (not shown) that arrange corresponding to stroboscopic lamp, and photographic head and stroboscopic lamp are in same level, and to irradiate route with stroboscopic lamp be 15 ° of-145 ° of angles.
That is, the vibration dripping that this utility model adopts, mainly by melting medicinal liquid pressurized delivered to water dropper, utilize magnetic force/electronic or pneumatic vibration principle, make water dropper with the upper and lower vibration of setpoint frequency, waveform and amplitude, make oscillatory shear masterpiece for fluid column, make it form drop, under normal circumstances, frequency of vibration is between 50-300Hz.The mode of magnetic force or electric vibrating can be adopted as required, there is frequency of vibration high, the feature that amplitude is little, be applicable to the high speed dripping of low-viscosity material.Generally, the mode of pneumatic vibration, frequency of vibration, amplitude is large.When material viscosity is more than 800cp (centipoise), material then cannot effectively cut by electronic mode.Cause emitter clogging, affect drop pill when preparing, pneumatic vibration mode can be adopted.
In order to eliminate in feed liquid course of conveying, the impact that the pressure pulse springing up generation due to feed liquid produces dripping process, ensures that feeding is steady, is also provided with surge tank 500 between described material tank 100 and water dropper 200.Surge tank 500 is provided with compressed air inlet, is connected with air pump by pressure pipeline, and pressure pipeline is provided with pressure-regulating valve, makes surge tank inner liquid medicine keep supplied with constant voltage.Described surge tank is provided with liquidometer, for controlling charging rate; Surge tank is also provided with heat-insulation layer, adopts water-bath, oil bath and electric tracing thermal insulation; And have temperature sensor monitors feed temperature; The stirring paddle of scalable mixing speed is provided with in surge tank.Tank inner sensor all can be configured to contact or contactless.Tank body material can adopt 304,316L or other heat proof material that can directly contact with product.
Fig. 2 is that this utility model drips dish sectional view; Fig. 3 is the A partial structurtes enlarged drawing of Fig. 2.As Fig. 2 and shown in composition graphs 3, water dropper 200 of the present utility model mainly includes and drips a dish 210, drips a dish 210 and is provided with multiple drip hole 220, and drip hole 220 is dripping circumferentially being equidistantly spaced of dish 210.As shown in Figure 4, drip hole 220 is made up of cylindrical cavity 221, conical cavity 222 and straight tube chamber 223, and drop drips from the end in straight tube chamber 223.At described dish 210 towards on the side of cooling tank 600, the periphery exported in straight tube chamber 223 offers spill annular groove 230.The aperture D0 exported due to straight tube chamber 223 is generally 0.1-5mm, the internal diameter D1=D0+0.4mm of described spill annular groove 230, outer diameter D 2 >=1.5 millimeters, and groove depth h is 0.5-5mm.In addition, the diameter d of cylindrical cavity 221 is 0.5-1mm, and the tapering of conical cavity 222 is 20 °-170 °, and the gross thickness A dripping dish 210 is 6mm, height H=(0.5-6) D0 in straight tube chamber 223.By offering spill annular groove 230 in the periphery of drip hole 220, can prevent when thick liquid sprays at a high speed, the surrounding of drip hole 220 has remaining medicinal liquid to pile up, and finally causes the blocking of drip hole 220 or affects dripping.
Water dropper 200 can select direct exposure, and in order to keep fluid temperature constant, water dropper outside also can be selected to arrange incubation cavity, makes the temperature of water dropper remain on about 70-200 DEG C.The skin of incubation cavity is provided with heat-barrier material, and internal layer is provided with steam heater or infrared heating device, and the medicinal liquid viscosity caused to avoid variations in temperature changes thus affects dripping effect.The below of incubation cavity is provided with opening, and the position of opening is corresponding with the exit position of water dropper to be arranged, and the size of opening is corresponding with the width of water dropper to be arranged.Incubation cavity inside can be designed to certain arc angle, and comparable square cavities dead angle is less, is easier to clean; Incubation cavity lower ending opening, to ensure the normal descend of drop pill.
Simultaneously at the side-lower of water dropper 200, be configured with stroboscopic lamp 201, for the dripping situation of monitoring drop pill.By synchronous stroboscopic principle, operator can only need visual, under Real Time Observation goes out high speed falling state, certainly, in order to observed and recorded is convenient, also can carry out Real-Time Monitoring by photographic head to image.By under a certain frequency of vibration, during dripping speed as: more than 50Hz, to the face shaping of drop pill, realize the real-time monitoring of dripping state and accurately regulate.That is, while dripping process, utilize vibrational waveform as the monitoring index of PAT, the particle size distribution situation of drop pill can be measured, and monitor in real time by the fluidized state of strobe apparatus to drop pill.By regulating vibration parameters, can improve more than drug loading to 50%, adjuvant significantly reduces.By regulating vibration parameters, drop pill diameter can be adjusted between 0.2mm-3mm, and the Miniature Chinese medicine dripping micropill that can meet capsule fill requirement better can be produced.The stroboscopic real-time inspection that this utility model adopts and monitoring technology on-line, make drop pill product yield bring up to more than 95% by traditional 70%.
Shown in composition graphs 1, air cooling blood circulation of the present utility model comprises: cooling pipe 600, and is connected with described cooling pipe 600 and the refrigerating plant freezed to cooling pipe.Described cooling pipe 600 is arranged on immediately below the water dropper 200 of drop pill device, and described cooling pipe 600 can be straight barrel type or spiral type pipe, and as required, the length of described cooling pipe 600 is 5m-10m, and preferred length is 6m.Be provided with interlayer 610 outside described cooling pipe 600, described interlayer 610 bottom is communicated with cooling pipe 600 inside by connected entrance 601.
Fig. 4 is this utility model refrigerating device structure schematic diagram.As shown in Figure 4, described cold wind refrigerating plant comprises: cold wind refrigerating plant 4, described cold wind refrigerating plant comprises freezer 41, the air outlet of described freezer 41 is connected with the cold air inlet of cooling pipe 600, cold wind is circulated rising in cooling pipe 600 inner chamber, and the cold air inlet of described cooling pipe 600 and plane included angle a are then 0 °-90 °.In order to realize quick cooling further, described refrigerating plant also comprises cold-trap refrigerating plant 5, described cold-trap refrigerating plant 5 comprises: the coolant storage tank 51 that coolant is housed, and the refrigeration machine 52 that the coolant in coolant storage tank 51 freezed and heat exchanger 53, the refrigerant exit of described coolant storage tank 51 is connected with the refrigerant inlet that described interlayer 610 top is arranged by pump 54, coolant, by refrigerant inlet input interlayer 610, transfers to interlayer 610 bottom from interlayer 610 top and is transferred to cooling pipe 600 inner chamber; Described coolant circulates with cold wind simultaneously rises in the inner chamber of cooling pipe 600, and discharges or reclaim coolant and cold wind with the gas concentration unit 6 be connected by cooling pipe 600 top.Coolant adopts usually: nitrogen, argon or carbon dioxide etc.
Fig. 5 is the overall structure schematic diagram of this utility model on-line cleaning equipment.As shown in Figure 5, in order to keep clean, described drop pill air cooling production line also comprises: on-line cleaning equipment, and this equipment comprises: cleaning unit 10, clean Monitoring and Controlling unit 11, elevation driving unit 12 and lifting unit 13, described cleaning unit 10 is spray head or the spray head with cleaning cloth.Described clean Monitoring and Controlling unit drives lifting unit to drive cleaning unit 10 to be elevated in cooling pipe 600 by elevation driving unit, and described lifting unit is arranged on the outside at cooling pipe 600 top.Wherein, described lifting unit comprises: cleaning unit bracing frame 131, cleanser conduit 132, cleanser conduit bracing frame 133, cleanser conduit storage tray 134, sealing are taken over and cleaned monitoring device online, as: photographic head.It is inner that described cleanser conduit bracing frame 133 makes cleanser conduit 132 extend to cooling pipe 600.Described cleaning unit support 131 comprises multiple support wheel 1311, described in each, support wheel 1311 and cooling pipe 600 medial wall are supported, one end that described cleaning unit 10 extends to cooling pipe 600 inside with described cleanser conduit 132 is connected, and makes cleaning unit 10 prolong the lifting of cooling pipe 600 center by cleaning unit bracing frame 131.One end of described sealing adapter 135 is connected with the other end of cleanser conduit 132, for being imported by cleaning solution in described cleanser conduit 132.
More specifically, as shown in Figure 5, the elevation driving unit of on-line cleaning equipment comprises: motor 121, driving wheel 122, sprocket wheel 123, belt 124 and regulating wheel 125, described motor 121 is connected with driving wheel 122, described driving wheel 122 is connected with sprocket wheel 123 by belt 124, described sprocket wheel 123 is connected with described cleanser conduit storage tray 134, and described clean Monitoring and Controlling unit 11 is connected with motor 121; Regulating wheel 125 between sprocket wheel 123 and driving wheel 122, and is connected with sprocket wheel 123 and driving wheel 122 by belt 124.Certainly, except the concrete structure described in elevation driving unit of the present utility model, those skilled in the art can also utilize the elevation driving unit of other structure to complete driving lifting work according to actual needs.
Fig. 6 is the control block diagram of this utility model on-line cleaning equipment.As shown in Figure 6, described online clean monitoring device 136 comprises: image acquisition units 1361 and computing unit 1362, described image acquisition units 1361 is arranged on described cleaning unit 10, described image acquisition units 1361 is photographic head, for gathering the real time imaging in cooling pipe 600, picture signal is sent to computing unit 1362, described computing unit 1362 is converted to numerical value according to this picture signal and compares with threshold value, if this numerical value is greater than threshold value, then sends drive singal to clean Monitoring and Controlling unit 11 and drive described cleaning unit 10 to clean.
In sum and composition graphs 5 and Fig. 6, the work process of this utility model on-line cleaning equipment is such: first, the image in image acquisition units 1361 Real-time Collection cooling pipe 600, and by computing unit 1362 that the image collected sends; Secondly, described computing unit 1362 is converted to numerical value according to the image collected in S1, and compare with the threshold value be stored in computing unit 1362, if this numerical value is greater than threshold value, enter in cleaning procedure, otherwise image acquisition units 1361 proceeds to implement to gather image; Again, computing unit 1362 calculates the quantity of cleanout fluid required for cleaning cooling pipe 600 and sends drive singal to clean Monitoring and Controlling unit 11; Then, the signal that described clean Monitoring and Controlling unit 11 sends according to computing unit 1362, stop signal is sent to dripping system, after stopping drop pill work, drive elevation driving unit 12 and valve 142 respectively, make cleaning unit 10 prolong cooling pipe 600 central shaft and run from top to bottom and cleaning showers liquid; When cleaning unit 10 moves to cooling pipe 600 bottom, cleaning terminates, clean Monitoring and Controlling unit 11 controls elevation driving unit 12 and valve 142 respectively, controls cleaning unit 10 stopping and spraying and repeatedly perform cleaning, until clean up after returning to cooling pipe 600 top.
Fig. 7 is the overall structure schematic diagram of this utility model fluid bed.As Fig. 7 and shown in composition graphs 1, this air cooling dripping pill production line also comprises fluidized drying coated systems 700, this system mainly comprises fluid bed 710, described fluid bed 710 comprises body of heater, material feeding mouth 711 is provided with below body of heater, the end of described cooling pipe 600 is connected with the charging aperture 711 of fluid bed 710 by vacuum pipe, and the drop pill element ball of shaping through air cooling is inputted fluidized drying coating in fluid bed from charging aperture 711 vacuum feeding.Be provided with airflow-distribution board 712 in the below of described charging aperture 711, airflow-distribution board 712 is provided with through hole, and room temperature low humidity supply air system 720 is interconnected by pipeline and body of heater, and air intake position is positioned at the below of airflow-distribution board 712, upwards blows.By being arranged on the through hole on airflow-distribution board 712, air-flow both can be made to pass through, and can effectively prevent again the material in body of heater from falling to omitting.
The low humidity unit 722 that room temperature low humidity supply air system 720 comprises housing 721 and is arranged in housing, housing is provided with air inlet 723 and wind pipe 724.After low humidity unit 722 processes, input furnace interior through wind pipe 724 from body of heater air inlet 725 after air enters housing from air inlet 723, and fluidized drying process is carried out to the material being built in furnace interior.In addition, room temperature low humidity supply air system 720 also comprises the return air duct 726 for air flow recovery, and two ends are connected with housing with described body of heater respectively.Described low humidity unit 722 is the combination of multiple blood processor, comprises dust arrester, dehydrating unit, air-supply arrangement, heater, defecator and effective filter successively according to the airflow direction in Fig. 7 shown in arrow.
When fluid bed works, first by charging aperture 711 vacuum feeding above body of heater, the gas crossed through PROCESS FOR TREATMENT such as low humidity unit 722 dry heat filtration compressions is passed into again by body of heater air inlet 725, gas humidity≤5g/kg after processed, expulsion pressure is 1-4bar, temperature is-20-100 DEG C, preferred 20-60 DEG C.Goods fluid is dried to when humidity is 4% and carries out coating, then exported by the finished product after fluidized drying coating by device for discharging discharging, waste gas is discharged from exhaust duct 727.
As required, under normal circumstances, the baking temperature of described fluid bed is-20 DEG C-100 DEG C, and drying time is 1-4 hour.In order to keep drop pill to be in fluidized state, the problem solving drop pill adhesion is enhanced productivity simultaneously, and described fluid bed preferably adopts gradient increased temperature seasoning,-20-30 DEG C forms fluidisation state, 15-35 DEG C dry 10-120 minute, 35-55 DEG C dry 10-60 minute, 55-100 DEG C of dry 0-60 minute; Most preferably 0-20 DEG C forms fluidisation state, 25 DEG C of dryings 60 minutes, 45 DEG C of dryings 30 minutes, 55 DEG C of dry 0-30 minute.Be convenient to control to effectively detect drop pill moisture, the on-line measuring device 800 for monitoring micropill water content and particle size distribution situation is also provided with in described fluid bed, this online moisture content checkout gear can adopt the existing detection part of moisture transducer or probe and so on, owing to being prior art, therefore do not repeat them here.
As dripping cooling and the all-in-one of fluidized drying coating, the fluidized drying increased, solving drop pill prepared by air cooling equipment is depositing in process, the problem that the adhesion that may occur and one-tenth analyze, also ensure that drop pill moisture can reach stationary value, improve the uniformity of equipment medicine carrying and coating.Spray hot melt medicinal liquid and carry out medicine carrying parcel, can further improve drop pill drug loading; Also this equipment can be used to spray and to carry out drop pill coating, to meet different process requirement, as: sustained release coating, film coating, sugar coating etc.
Shown in composition graphs 1 and Fig. 4, specifically, work process of the present utility model is such: utilize surge tank 500 to push medicinal liquid, the medicinal liquid melted is transported in the water dropper 200 with incubation cavity, described water dropper 200 has the outlet with incubation cavity 210 bottom opening equidirectional, guarantees that medicinal liquid can ooze bottom water dropper 200.Utilize pressure, admixing medical solutions is flowed out from the outlet at bottom of water dropper 200.According to the size of required drop pill, regulate pressure or vibration parameters that is pneumatic or electric vibrating water dropper, the medicine making the powder column flowed out from water dropper 200 be cut into required diameter drips.Wherein acceleration of vibration 0-110g (sine), Oscillation Amplitude (0-25.4mm).
Start gas refrigeration, the medicine utilizing low temperature to make to ooze drops in cooled and solidified in cooling pipe 600 and becomes solid granulates, and collects in cooling pipe 600 lower end simultaneously.The upper port of cooling pipe 600 seals with the opening of the incubation cavity lower end of water dropper 200 and is communicated with, and the lower end of cooling pipe 600 is the hatch frame corresponding with drop pill collecting vessel.
The inner chamber circulation that produced cold wind enters into cooling pipe 600 by cold air inlet is risen by freezer 41, coolant is input in interlayer 610 by refrigerant inlet by coolant storage tank 51 simultaneously, now in interlayer 610, the flow direction of coolant is from top to bottom, and the connected entrance 601 be communicated with cooling pipe 600 by this interlayer 610 enters into the inner chamber of cooling pipe 600, mix with the cold wind in cooling pipe 600 inner chamber and circulate and rise, when the mist of coolant and cold wind rises to cooling pipe top, by gas concentration unit 6 respectively by cold wind and refrigerant recovering in freezer 41 or coolant storage tank 51, or by gas concentration unit 6, this mist is disposed in air, concrete discharge process refers to foregoing teachings.
Owing to being directly blown at an angle between cooling-air and cooling pipe 600, cold wind and coolant form laminar flow in cooling pipe 600, make the medicine oozed continuously drip the purging of the gas obtaining a small amount of lower temperature, maintain a certain distance, avoid drop pill to be adhered in this region, affect follow-up molding.
Subsequently, cooling pipe 600 end is connected to fluidized drying coated systems 700 by pipeline, regulate air intake and air draft air quantity, and control temperature scope, dried piller is by negative pressure of vacuum discharging, rejoin fluid bed after sieving, regulate air intake and air draft air quantity, carry out medicine carrying or film coating by technological requirement; After coating, equipment also can connect capsule filling machine and pours into, and capsule check-weighing machine carries out by grain check weighing.Therefore, according to practical application needs, on basis integrally-built shown in Fig. 1, air cooling dripping pill production line provided by the utility model can also configure capsule filling machine and capsule check weighing device.Said apparatus is prior art, does not repeat them here.
Below by way of best exemplifying embodiment, equipment of the present utility model is described in detail further.This example only for illustration of this utility model, and does not limit this utility model.
Embodiment one prepares FUFANG DANSHEN DIWAN
(1) material step: get Salvia miltiorrhiza and Panax notoginseng extract 600g, Borneolum Syntheticum 5g, and polyethylene glycol 6000 (PEG-6000) adjuvant 2000g.First PEG-6000 is added in material tank, be heated to 90 DEG C, in advance melting, add 5000rpm intimate mixing in Salvia miltiorrhiza and Panax notoginseng extract to homogenizer again, time 200min, then 10000rpm homogenizing material, time 100min, temperature 100 DEG C, must be mixed into liquid.
(2) dripping step: the frequency of vibration regulating pneumatic vibration water dropper is 300Hz, moist closet adopts steam jacket insulation, and temperature controls 200 DEG C, dripping speed and step (1) material speeds match, dripping pressure is 3Bar, dripping speed 10kg/hr, dripping acceleration 1G.
(3) condensing steps: supplied gas in material tank by pipeline by air pump, make the aforesaid liquid melted flow into water dropper and ooze in cooling pipe bottom water dropper, cooling pipe is perpendicular to the ground; Start cold air, chilling temperature is made to reach-120 DEG C, the angle of cooling air inlet and horizontal plane is 30 °, and make cold air at cooling pipe internal circulation flow, make to drop in cooled and solidified in cooling pipe from the medicinal liquid oozed and become solid-state drop pill, Fluidized Bed Partial can be connected to from the pipeline of cooling pipe lower end and carry out fluidized drying and medicine carrying coating.
(4) drying steps: then drop pill is carried out fluidized drying and medicine carrying coating, until material after-20 DEG C-30 DEG C good fluidised forms of formation in bed body, 50 DEG C of dryings drying in 2 hours 120 minutes, plain ball moisture Control, 5.0%, obtains middle voxel ball.
(5) coating steps: calculate coating powder consumption according to coating inventory and prescription, the concentration of coating solution is 10%, preparation coating solution, stirs 45 minutes.Setting inlet temperature be 40 DEG C qualified drop pill is dropped into fluid bed after, improve setting inlet temperature to 48 DEG C, after temperature of charge reaches 38 DEG C, start coating.In coating process, temperature of charge controls at 35-45 DEG C, is cooled to 30 DEG C with bottom discharge after coating completes, and sieve ball, particle diameter is 2.0mm drop pill.
Embodiment two prepares Radix Salviae Miltiorrhizae drop pill
(1) material step: get Radix Salviae Miltiorrhizae extract 600g, add water 60g, add polyethylene glycol 6000 adjuvant 1500g, put into material tank and be heated to 90 DEG C, adopt low speed homogenizing (3200rpm) mixed material, after having mixed, improve homogenizing speed and carry out material to 5000rpm, 6 minutes time.Make it melt completely and be mixed into liquid.
(2) dripping step: the frequency of vibration regulating pneumatic vibration water dropper is 50Hz, moist closet adopts Infrared Heating insulation, and temperature controls 70 DEG C, and dripping pressure is 4Bar, dripping speed 40kg/hr, dripping acceleration 3G.
(3) condensing steps: supplied gas in material tank by pipeline by air pump, make to melt uniform aforesaid liquid flow into water dropper and ooze in cooling pipe bottom water dropper, dripping pressure 0.18MPa, cold air is started while aforesaid liquid oozes, chilling temperature is made to reach-10 DEG C, and make cold air at cooling pipe internal circulation flow, the angle of cooling air inlet and horizontal plane is 45 °, make the medicinal liquid oozed from water dropper drop in cooled and solidified in cooling pipe and become solid-state drop pill, and be connected to Fluidized Bed Partial from the pipeline of cooling pipe lower end.
(4) fluidisation: then drop pill is carried out fluidized drying and medicine carrying coating, until material after forming good fluidised form in bed body, be warming up to 25 DEG C of dryings 60 minutes, then be warming up to 45 DEG C of dryings 30 minutes, continue to be warming up to 55 DEG C of dryings 30 minutes, be then cooled to 30 DEG C with bottom discharge.Element ball moisture Control, at 3.0-7.0%, obtains middle voxel ball.
(5) coating steps: calculate coating powder consumption according to coating inventory and prescription, the concentration of coating solution is 18%, preparation coating solution, stirs 45 minutes.Setting inlet temperature be 25 DEG C qualified drop pill is dropped into fluid bed after, improve setting inlet temperature to 48 DEG C, after temperature of charge reaches 38 DEG C, start coating.In coating process, temperature of charge controls at 35-45 DEG C, is cooled to 30 DEG C with bottom discharge after coating completes, and sieve ball, particle diameter is 1.0-2.0mm drop pill.
Embodiment three prepares FUFANG DANSHEN DIWAN
(1) material step: get Salvia miltiorrhiza and Panax notoginseng extract 600g, Borneolum Syntheticum 5g, and polyethylene glycol 6000 adjuvant 2000g.First Polyethylene Glycol is added in material tank, be heated to 80 DEG C, in advance melting, then add Salvia miltiorrhiza and Panax notoginseng extract, put into 2500rpm intimate mixing in homogenizer, time 100min, then 6000rpm homogenizing material, time 20min, temperature 100 DEG C, is mixed into liquid.
(2) dripping step: the frequency of vibration regulating pneumatic vibration water dropper is 90HZ, acceleration 3.5G, dripping speed 12Kg/hr, dripping pressure 1.0Bar.Moist closet adopts steam jacket insulation, and temperature controls 70 DEG C,
(3) condensing steps: supplied gas in material tank by pipeline by air pump, make the aforesaid liquid melted flow into water dropper and ooze in cooling pipe bottom water dropper, cooling pipe is perpendicular to the ground; Start cold air, chilling temperature is made to reach-100 DEG C, the angle of cooling air inlet and horizontal plane is 90 °, and make cold air at cooling pipe internal circulation flow, make to drop in cooled and solidified in cooling pipe from the medicinal liquid oozed and become solid-state drop pill, Fluidized Bed Partial can be connected to from the pipeline of cooling pipe lower end and carry out fluidized drying and medicine carrying coating.Specifically, 20 DEG C form fluidisation states, 25 DEG C of dryings 60 minutes, 45 DEG C of dryings 30 minutes, 55 DEG C of dryings 30 minutes.
Embodiment four prepares FUFANG DANSHEN DIWAN
(1) material step: the mixture of compound Salviae Miltiorrhizae extract and arabic gum and lactose=1:1 is put into 5000rpm intimate mixing in homogenizer, time 200min, then 10000rpm homogenizing material, time 100min, temperature 100 DEG C, obtains intermediate feed liquid;
(2) dripping step: intermediate feed liquid vibrates dripping through water dropper, frequency of vibration is 200Hz, and dripping pressure is 4.0Bar, water dropper temperature 100 DEG C, and dripping speed and step (1) material speeds match are 15kg/hr;
(3) condensing steps: the medicine oozed drop in quick cooled and solidified in refrigerating gas become diameter be 4.0mm drop pill element ball, described refrigerating gas temperature is-300 DEG C.
Fluidized Bed Partial can be connected to from the pipeline of cooling pipe lower end and carry out fluidized drying and medicine carrying coating.Specifically, 0 DEG C forms fluidisation state, 25 DEG C of dryings 60 minutes, 45 DEG C of dryings 30 minutes, 55 DEG C of dryings 30 minutes.
Embodiment five prepares FUFANG DANSHEN DIWAN
Get compound Salviae Miltiorrhizae extract 75g, Borneolum Syntheticum 7.5g, lactose 165g, be prepared into compound Salviae Miltiorrhizae microdroplet ball, preparation method is as follows:
(1) material step: compound Salviae Miltiorrhizae extract and lactose are put into 2500rpm intimate mixing in homogenizer, time 100min, then 6000rpm homogenizing material, time 50min, temperature 80 DEG C, obtains intermediate feed liquid;
(2) dripping step: intermediate feed liquid vibrates dripping through water dropper, frequency of vibration is 130Hz, and dripping pressure is 1.8Bar, water dropper temperature 140 DEG C, and dripping speed and step (1) material speeds match are 25kg/hr;
(3) condensing steps: the medicine oozed drop in quick cooled and solidified in refrigerating gas become diameter be 1mm drop pill element ball, described refrigerating gas temperature is-100 DEG C.
(4) drying steps: adopt fluidization drying apparatus dry ,-20 DEG C of dryings 4 hours, obtain dry drop pill element ball.
(5) coating steps: described drying element ball coating in fluid bed, coating material and plain ball weight ratio are 1:25, and coating solution concentration is 10%, and namely temperature 40 DEG C of coatings obtain coated drop pill.
Embodiment six prepares FUFANG DANSHEN DIWAN
Get compound Salviae Miltiorrhizae extract 75g, Borneolum Syntheticum 7.5g, PEG 8000 165g, be prepared into compound Salviae Miltiorrhizae microdroplet ball, preparation method is as follows:
After compound Salviae Miltiorrhizae extract powder is added water, stir more than 10 minutes in 60 DEG C, obtain pharmaceutical premixed material.
(1) material step:
Compound Salviae Miltiorrhizae extract and PEG 8000 are put into 2500rpm intimate mixing in homogenizer, time 100min, then 6000rpm homogenizing material, time 50min, temperature 80 DEG C, obtains intermediate feed liquid;
(2) dripping step: intermediate feed liquid vibrates dripping through water dropper, frequency of vibration is 140Hz, and dripping pressure is 0.5Bar, water dropper temperature 100 DEG C, and dripping speed and step (1) material speeds match are 30kg/hr;
(3) condensing steps: the medicine oozed drop in quick cooled and solidified in refrigerating gas become diameter be 2mm drop pill element ball, described refrigerating gas temperature is-100 DEG C.
(4) drying steps: adopt fluidization drying apparatus dry, 100 DEG C of dryings 1 hour, obtain dry drop pill element ball.
(5) coating steps: described drying element ball coating in fluid bed, coating material and plain ball weight ratio are 1:25, and coating solution concentration is 10%, and namely temperature 40 DEG C of coatings obtain coated drop pill.
Embodiment seven prepares FUFANG DANSHEN DIWAN
Get compound Salviae Miltiorrhizae extract 90g, Borneolum Syntheticum 2g, cetomacrogol 1000 270g, be prepared into compound Salviae Miltiorrhizae microdroplet ball, preparation method is as follows:
After compound Salviae Miltiorrhizae powdered active ingredient is added water, stir more than 10 minutes in 30 DEG C, obtain pharmaceutical premixed material.
(1) material step: compound Salviae Miltiorrhizae extract and cetomacrogol 1000 are put into 2500rpm intimate mixing in homogenizer, time 100min, then 6000rpm homogenizing material, time 20min, temperature 100 DEG C, obtains intermediate feed liquid;
(2) dripping step: intermediate feed liquid vibrates dripping through water dropper, frequency of vibration 100HZ, acceleration 1G, dripping speed 10Kg/hr, dripping pressure 1.0Bar, water dropper temperature 75 DEG C.
Dripping speed and step (1) material speeds match;
(3) condensing steps: the medicine oozed drop in quick cooled and solidified in refrigerating gas become diameter be 1.5mm drop pill element ball, described refrigerating gas temperature is-80 DEG C.
(4) drying steps: dry adopt gradient increased temperature seasoning ,-20 DEG C form fluidisation states, 15 DEG C of dryings 10 minutes, and 35 DEG C of dryings 10 minutes, obtain dry drop pill element ball.
(5) coating steps: described drying element ball coating in fluid bed, coating material and plain ball weight ratio are 1:25, and coating solution concentration is 10%, and namely temperature 40 DEG C of coatings obtain coated drop pill.
Embodiment eight prepares FUFANG DANSHEN DIWAN
Get compound Salviae Miltiorrhizae extract 100g, Borneolum Syntheticum 5g, the combination 35g of Macrogol 4000 and polyethylene glycol 6000=1:1, be prepared into compound Salviae Miltiorrhizae microdroplet ball, preparation method is as follows:
After compound Salviae Miltiorrhizae extract powder is added water, stir more than 10 minutes in 80 DEG C, obtain pharmaceutical premixed material.
(1) material step: by the combinatorial introduction of compound Salviae Miltiorrhizae extract and Macrogol 4000 and polyethylene glycol 6000=1:1 to 2500rpm intimate mixing in homogenizer, time 100min, then 6000rpm homogenizing material, time 80min, temperature 80 DEG C, obtains intermediate feed liquid;
(2) dripping step: intermediate feed liquid vibrates dripping through water dropper, frequency of vibration 200HZ, acceleration 20G, dripping speed 40Kg/hr, dripping pressure 3.0Bar, water dropper temperature 85 DEG C.
Dripping speed and step (1) material speeds match;
(3) condensing steps: the medicine oozed drop in quick cooled and solidified in refrigerating gas become diameter be 0.5mm drop pill element ball, described refrigerating gas temperature is 120 DEG C.
(4) drying steps: dry adopt gradient increased temperature seasoning, 30 DEG C form fluidisation states, 35 DEG C of dryings 120 minutes, 55 DEG C of dryings 60 minutes, and 100 DEG C of dryings 60 minutes, obtain dry drop pill element ball.
(5) coating steps: described drying element ball coating in fluid bed, coating material and plain ball weight ratio are 1:25, and coating solution concentration is 10%, and namely temperature 40 DEG C of coatings obtain coated drop pill.
In sum, this utility model adopts oscillatory shear dripping, improves drop pill forming speed and drop pill circularity, and reduces drop pill weight differential; Monitor in real time while dripping, by the adjustment of parameters, improve drop pill product yield; Utilize air cooling mode to achieve while drop pill is prepared in high speed dripping micropill and improve drug loading, significantly reduce supplementary product consumption and taking dose; Avoid the organic solvent residual of traditional liquid cooling mode.The drawback that this utility model effectively avoids traditional drilling pill device to exist, really reach low energy consumption, at a high speed, efficiently, high drug load, possessing widely can dripping scope, greatly improves speed of production and dripping effect.
Claims (23)
1. an air cooling dripping pill production line, comprise drop pill system, air cooling blood circulation and control system, drop pill system comprises material tank and coupled water dropper, vibrating device is provided with between described material tank and water dropper, vibrating device drives water dropper up-down vibration, the nibbling shear shear force produced, the medicinal liquid flowed out in water dropper is cut into and drips, drop pill is formed after falling into the cooling of air cooling blood circulation, it is characterized in that, described water dropper mainly comprises a dish, and drip dish and be provided with multiple drip hole, the periphery of drip hole offers spill annular groove.
2. air cooling dripping pill production line as claimed in claim 1, it is characterized in that, the internal diameter=drip hole internal diameter+0.4 millimeter of described spill annular groove, external diameter >=1.5 millimeter, groove depth is 0.5-5 millimeter.
3. air cooling dripping pill production line as claimed in claim 1, it is characterized in that, described water dropper is provided with on-Line Monitor Device, this device comprises pulse signal trigger mechanism, the tranmitting frequency of described pulse signal trigger mechanism is identical with the frequency of vibration of described vibrating device, control system according to the monitoring result of on-Line Monitor Device, regulating and controlling dripping parameter.
4. air cooling dripping pill production line as claimed in claim 3, it is characterized in that, described on-Line Monitor Device is arranged on the side below described water dropper;
Described pulse signal trigger mechanism is stroboscopic lamp, and described stroboscopic lamp is identical with the frequency of vibration of vibrating device;
Described on-Line Monitor Device also comprises the photographic head that arrange corresponding to stroboscopic lamp, and photographic head and stroboscopic lamp are in same level, and to irradiate route with stroboscopic lamp be 15 ° of-145 ° of angles.
5. air cooling dripping pill production line as claimed in claim 4, is characterized in that, the frequency of vibration of described stroboscopic lamp and vibrating device: 50-300HZ;
Water dropper dripping speed: 10-40Kg/hr;
Water dropper dripping acceleration: 1-20G;
Water dropper dripping pressure: 0.5-4.0Bar;
Water dropper temperature: 70-200 DEG C.
6. air cooling dripping pill production line as claimed in claim 5, is characterized in that, the frequency of vibration of described stroboscopic lamp and vibrating device: 90-200Hz.
7. air cooling dripping pill production line as claimed in claim 6, it is characterized in that, the frequency of vibration of described stroboscopic lamp and vibrating device is: 130-140HZ.
8. air cooling dripping pill production line as claimed in claim 5, it is characterized in that, described dripping speed is: 12-30Kg/hr.
9. air cooling dripping pill production line as claimed in claim 8, it is characterized in that, described dripping speed is: 15-25Kg/hr.
10. air cooling dripping pill production line as claimed in claim 5, it is characterized in that, described dripping acceleration is: 3-10G.
11. air cooling dripping pill production lines as claimed in claim 10, it is characterized in that, described dripping acceleration is: 3.5-4.5G.
12. air cooling dripping pill production lines as claimed in claim 5, it is characterized in that, described dripping pressure is: 1.0-3.0Bar.
13. air cooling dripping pill production lines as claimed in claim 12, it is characterized in that, described dripping pressure is: 1.8Bar.
14. air cooling dripping pill production lines as claimed in claim 5, it is characterized in that, described water dropper temperature is: 70-100 DEG C.
15. air cooling dripping pill production lines as claimed in claim 14, it is characterized in that, described water dropper temperature is: 75-85 DEG C.
16. air cooling dripping pill production lines as claimed in claim 1, it is characterized in that, described water dropper outside is provided with incubation cavity, the skin of described incubation cavity is provided with heat-barrier material, internal layer is provided with steam heater or infrared heating device, the below of incubation cavity is provided with opening, and the position of opening is corresponding with the exit position of water dropper to be arranged, and the size of opening is corresponding with the width of water dropper to be arranged.
17. air cooling dripping pill production lines as claimed in claim 1, it is characterized in that, described air cooling blood circulation comprises: cooling pipe, and be connected and the refrigerating plant that cooling pipe is freezed with described cooling pipe, be provided with interlayer outside described cooling pipe, described interlayer bottom is communicated with cooling pipe inside by connected entrance;
Described refrigerating plant comprises: cold wind refrigerating plant and cold-trap refrigerating plant, wherein:
Described cold wind refrigerating plant comprises: freezer, and the air outlet of described freezer is connected with the cold air inlet of cooling pipe, and cold wind is circulated rising in cooling pipe inner chamber;
Described cold-trap refrigerating plant comprises: the coolant storage tank that coolant is housed, and the refrigeration machine that the coolant in coolant storage tank freezed and heat exchanger, the refrigerant inlet that refrigerant exit and the described interlayer top of described coolant storage tank are arranged is connected, coolant, by refrigerant inlet input interlayer, transfers to interlayer bottom from interlayer top and is transferred to cooling pipe inner chamber; Described coolant circulates with cold wind simultaneously rises in the inner chamber of cooling pipe, and by cooling pipe top discharge or recovery;
Described cooling pipe is straight barrel type or spiral type pipe, and length is 5-10 rice.
18. air cooling dripping pill production lines as claimed in claim 17, it is characterized in that, described cooling pipe length is 6 meters.
19. air cooling dripping pill production lines as described in claim 17 or 18, it is characterized in that, described cooling pipe is provided with on-line cleaning equipment, comprise: cleaning unit, control unit, elevation driving unit and lifting unit, described control unit drives lifting unit to drive cleaning unit lifting by elevation driving unit, and described lifting unit is arranged on the cooling pipe top outer of chiller;
Described lifting unit comprises: cleaning unit bracing frame, cleanser conduit, cleanser conduit bracing frame, cleanser conduit storage tray and sealing adapter; Described cleanser conduit bracing frame makes cleanser conduit extend to cooling pipe inside; Described cleaning unit support comprises multiple support wheel, support wheel described in each and cooling pipe medial wall are supported, one end that described cleaning unit extends to cooling pipe inside with described cleanser conduit is connected, and makes cleaning unit prolong the lifting of cooling pipe center by cleaning unit bracing frame; One end of described sealing adapter is connected with the other end of cleanser conduit, for being imported by cleaning solution in described cleanser conduit;
Described lifting unit also comprises: on-Line Monitor Device, described on-Line Monitor Device comprises: image acquisition units and computing unit, described image acquisition units is arranged on described cleaning unit, for gathering the real time imaging in cooling pipe, picture signal is sent to computing unit, described computing unit is converted to numerical value according to this picture signal and compares with threshold value, if this numerical value is greater than threshold value, then sends drive singal to control unit and drives described cleaning unit to clean.
20. air cooling dripping pill production lines as claimed in claim 1, it is characterized in that, this air cooling dripping pill production line also comprises fluidized drying coated systems, this system mainly comprises fluid bed, the end of described cooling pipe is connected with the entrance of fluid bed by vacuum pipe, and the drop pill element ball vacuum feeding of shaping through air cooling is inputted fluidized drying coating in fluid bed;
Described fluid bed comprises body of heater, material feeding mouth is provided with below body of heater, airflow-distribution board is provided with in the below of described charging aperture, the bottom of described airflow-distribution board is connected with the wind pipe of room temperature low humidity supply air system, low for room temperature humid gas is sent in fluid bed body of heater through wind pipe by described room temperature low humidity supply air system, and carries out fluidized drying process to the material being built in furnace interior;
Described room temperature low humidity supply air system comprises housing and is arranged on the low humidity unit in housing, and housing is provided with intake stack and wind pipe, inputs described body of heater after air enters housing from intake stack after the process of low humidity unit through wind pipe;
Described room temperature low humidity supply air system also comprises the return air duct for air flow recovery, and two ends are connected with housing with described body of heater respectively.
21. air cooling dripping pill production lines as claimed in claim 20, is characterized in that, the baking temperature of described fluid bed is-20 DEG C-100 DEG C, and drying time is 1-4 hour.
22. air cooling dripping pill production lines as claimed in claim 21, is characterized in that, described fluid bed-20-30 DEG C forms fluidisation state, 15-35 DEG C dry 10-120 minute, 35-55 DEG C dry 10-60 minute, 55-100 DEG C of dry 0-60 minute.
23. air cooling dripping pill production lines as claimed in claim 22, is characterized in that, described fluid bed 0-20 DEG C forms fluidisation state, 25 DEG C of dryings 60 minutes, 45 DEG C of dryings 30 minutes, 55 DEG C of dry 0-30 minute.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420383996.4U CN204170103U (en) | 2014-07-11 | 2014-07-11 | Air cooling dripping pill production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420383996.4U CN204170103U (en) | 2014-07-11 | 2014-07-11 | Air cooling dripping pill production line |
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| Publication Number | Publication Date |
|---|---|
| CN204170103U true CN204170103U (en) | 2015-02-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420383996.4U Withdrawn - After Issue CN204170103U (en) | 2014-07-11 | 2014-07-11 | Air cooling dripping pill production line |
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| Country | Link |
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| CN (1) | CN204170103U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104274326A (en) * | 2013-07-11 | 2015-01-14 | 天士力制药集团股份有限公司 | Air-cooled dropping pill production line |
| US11013694B2 (en) | 2013-07-11 | 2021-05-25 | Tasly Pharmaceutical Group Co., Ltd. | Formulation of a micro drop pill and the preparation method thereof |
| CN113608512A (en) * | 2021-10-08 | 2021-11-05 | 齐鲁工业大学 | Traditional Chinese medicine water pill manufacturing control method, system, device and terminal |
| USRE49035E1 (en) | 2013-07-11 | 2022-04-19 | Tasly Pharmaceutical Group Co., Ltd. | Traditional Chinese medicine composition, and preparation and application thereof |
| USRE49050E1 (en) | 2013-07-11 | 2022-04-26 | Tasly Pharmaceutical Group Co., Ltd. | Traditional Chinese medicine composition, and preparation and application thereof |
| EP4144357A4 (en) * | 2020-04-29 | 2024-05-29 | Tasly Pharmaceutical Group Co., Ltd. | Traditional chinese medicine composition, and application of preparation of traditional chinese medicine composition in preparing medicine for preventing and/or treating coronavirus disease 2019 |
-
2014
- 2014-07-11 CN CN201420383996.4U patent/CN204170103U/en not_active Withdrawn - After Issue
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104274326A (en) * | 2013-07-11 | 2015-01-14 | 天士力制药集团股份有限公司 | Air-cooled dropping pill production line |
| CN104274326B (en) * | 2013-07-11 | 2018-11-30 | 天士力医药集团股份有限公司 | Be gas-cooled dripping pill production line |
| US11013694B2 (en) | 2013-07-11 | 2021-05-25 | Tasly Pharmaceutical Group Co., Ltd. | Formulation of a micro drop pill and the preparation method thereof |
| USRE49035E1 (en) | 2013-07-11 | 2022-04-19 | Tasly Pharmaceutical Group Co., Ltd. | Traditional Chinese medicine composition, and preparation and application thereof |
| USRE49050E1 (en) | 2013-07-11 | 2022-04-26 | Tasly Pharmaceutical Group Co., Ltd. | Traditional Chinese medicine composition, and preparation and application thereof |
| EP4144357A4 (en) * | 2020-04-29 | 2024-05-29 | Tasly Pharmaceutical Group Co., Ltd. | Traditional chinese medicine composition, and application of preparation of traditional chinese medicine composition in preparing medicine for preventing and/or treating coronavirus disease 2019 |
| CN113608512A (en) * | 2021-10-08 | 2021-11-05 | 齐鲁工业大学 | Traditional Chinese medicine water pill manufacturing control method, system, device and terminal |
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Address after: 300410 Tianjin City Hedong District of Beichen Puji Road No. 2 (city of the modern Chinese Medicine) Patentee after: Tasly Pharmaceutical Group Limited by Share Ltd Address before: 300410 Tianjin City Hedong District of Beichen Puji Road No. 2 city of the modern Chinese Medicine Patentee before: Tasly Pharmaceutical Group Co., Ltd. |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20150225 Effective date of abandoning: 20181130 |
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| AV01 | Patent right actively abandoned |