CN219091900U

CN219091900U - Vertical stirring type concentrated tank

Info

Publication number: CN219091900U
Application number: CN202222642394.3U
Authority: CN
Inventors: 王超; 朱光磊
Original assignee: Individual
Current assignee: Individual
Priority date: 2022-10-09
Filing date: 2022-10-09
Publication date: 2023-05-30
Anticipated expiration: 2032-10-09

Abstract

The utility model relates to a vertical stirring type concentrated mixing tank, and belongs to the technical field of mixing. Including the jar body that has feed inlet and discharge gate, be provided with the cover that adjusts temperature on the outer wall of jar body, its characterized in that: still including being in the puddler in the jar body, the pivoted power unit of drive puddler is installed at the top of the jar body, power unit is including fixing the reduction gear at jar body top, the upper end of puddler extends to jar outside and the power output shaft power connection of reduction gear, the power input shaft and the agitator motor power connection of reduction gear, the well upper portion of the jar body is provided with granule material dispersion devices. The utility model has the following beneficial effects: the granule material also can directly once only get into the jar internal portion through the granule feed inlet, and the granule material is first by preliminary dispersion through granule material dispersion device, and the granule material that disperses can disperse more easily after adding to the solvent again, and product quality is even stable, improves production efficiency.

Description

Vertical stirring type concentrated tank

Technical Field

The utility model relates to a vertical stirring type concentrated mixing tank, and belongs to the technical field of mixing.

Background

The concentrated mixing tank is also called a mixing tank, has the advantages of energy conservation, concentration, strong production capacity, convenient cleaning, simple structure and the like, is mainly used for uniformly stirring medicine materials, other elements and various medicines after being matched, and is indispensable equipment for manufacturing medicines and pharmaceutical factories. In order to ensure the temperature stability of the medicine materials, the temperature adjusting sleeve is arranged on the concentrated preparation tank, and the steam or cooling water is utilized to adjust the temperature of the concentrated preparation tank.

Patent number is CN 201721532376.2's patent discloses a dense jar of joining in marriage for infusion production line, including support, top cap and motor, the upper end welding of support has the jar body, the external portion of jar is equipped with the heat preservation, the bottom of the jar body still is equipped with discharge gate and heating pipe, just one side of the jar body is equipped with the level gauge, the filter screen is installed to the interior bottom of the jar body, the output shaft of motor is connected with the one end of (mixing) shaft, the other end of (mixing) shaft runs through one side of the jar body and is connected with the bearing, just the welding has the stirring leaf on the cross-section of (mixing) shaft, upper end one side of top cap still is equipped with the feed inlet, just the draw-in groove is still installed to one side of top cap, the inside of top cap is equipped with the recess, install the sealing strip in the recess. It can be seen that the following drawbacks exist in use:

the feed inlet divide into liquid feed inlet and granule feed inlet, and traditional jar body does not have granule material dispersion devices, and granule material is direct once only to get into jar internal portion through granule feed inlet, needs to take a long time just to disperse in the solvent, has the stirring inhomogeneous, leads to the medicine to mix the effect poor, influences the medicine quality, problem that mixing efficiency is low.

Disclosure of Invention

According to the defects in the prior art, the technical problems to be solved by the utility model are as follows: in order to solve one of the problems, the vertical stirring type concentrated tank is provided, the granular materials can also directly enter the tank body through the granular feed inlet at one time, the granular materials are initially dispersed through the granular material dispersing device, the dispersed granular materials can be more easily dispersed after being added into the solvent, the product quality is uniform and stable, and the production efficiency is improved.

The utility model relates to a vertical stirring type concentrated tank, which comprises a tank body with a feed inlet and a discharge outlet, wherein a temperature adjusting sleeve is arranged on the outer wall of the tank body, and is characterized in that: still including being in the puddler in the jar body, the pivoted power unit of drive puddler is installed at the top of the jar body, power unit is including fixing the reduction gear at jar body top, the upper end of puddler extends to jar outside and the power output shaft power connection of reduction gear, the power input shaft and the agitator motor power connection of reduction gear, the well upper portion of the jar body is provided with granule material dispersion devices.

Feed inlet divide into liquid feed inlet and granule feed inlet, traditional jar body does not have granule material dispersion devices, granule material is direct once only to get into jar internal portion through granule feed inlet, needs to take a long time just can disperse in the solvent, in this patent, granule material also can be direct once only get into jar internal portion through granule feed inlet, granule material is earlier by preliminary dispersion through granule material dispersion devices, can disperse more easily after the granule material that disperses is added to the solvent again, product quality is even stable, improves production efficiency.

Further, the tank body comprises an upper tank body and a lower tank body positioned below the upper tank body. The split type installation is convenient for arranging the particle material dispersing device on the inner wall of the tank body, and the product is prevented from being polluted by the outside.

Further, the material dispersing device comprises a tank body ring arranged between an upper tank body and a lower tank body, the tank body ring is connected with the upper tank body through an upper side flexible connection corrugated pipe, the tank body ring is connected with the upper tank body through a lower side flexible connection corrugated pipe, a conical disc coaxial with the tank body ring is arranged at the center of the tank body ring, two ends of the conical disc are opened, the upper portion is a large-diameter end, the bottom is a small-diameter end, a plurality of horizontal connecting rods are uniformly distributed on the outer wall of the conical disc, the other ends of the connecting rods are all fixed on the inner wall of the tank body ring, a rod body of the stirring rod penetrates through the conical disc, a stirring rod is provided with a stirring disc matched with the small-diameter end of the conical disc, the stirring disc is arranged below the conical disc, an adjustable gap is formed between the stirring disc and the conical disc, and the upper tank body and the lower tank body are provided with a gap adjusting mechanism for driving the conical disc to be close to or far away from the stirring disc, and the adjustable gap is determined by the height of the conical disc. The external diameter of the large diameter end of the conical disc is slightly smaller than the internal diameter of the tank body ring, the internal diameter of the tank body ring is equal to the internal diameter of the middle part of the tank body, the diameter of the stirring disc is larger than or smaller than or equal to the internal diameter of the small diameter end of the conical disc, the granular materials directly enter the tank body through the granular feed inlet at one time, are collected in the conical disc, the materials at the bottom of the conical disc are piled on the upper surface of the stirring disc, the stirring motor is required to be started at the same time, the stirring motor and the speed reducer control stirring rod to rotate, under the action of centrifugal force, the granular materials are thrown into the lower tank body below the stirring disc by the stirring disc (are dispersed all around) and fall into the solvent which is filled in advance, the granular materials are primarily dispersed, the dispersed granular materials are easier to disperse after being added into the solvent again, the product quality is uniform and stable, and the production efficiency is improved.

Further, the gap adjusting mechanism comprises a plurality of gap adjusting monomers uniformly distributed on the outer side of the tank body ring, each gap adjusting monomer is vertically arranged and located on the same circle with the center line of the tank body ring, the gap adjusting monomers comprise screws, the upper ends of the screws are fixed on the outer wall of the upper tank body, the lower ends of the screws are fixed on the outer wall of the lower tank body, the screws are connected with screw pipes in a threaded mode, the outer ring of the tank body ring is provided with a bearing mounting seat, the screw pipes are arranged on the bearing mounting seat on the outer wall of the tank body ring through thrust bearings, the screw pipes rotate relative to the bearings through rotating the screw pipes under the condition that the relative positions of the upper tank body and the lower tank body are ensured, the bearing applies force to the bearing seat, the tank body ring is lifted, the tank body ring drives the conical disc to lift, the stirring rod is fixed relative to the upper tank body, and accordingly, the gap between the conical disc and the stirring disc is adjusted according to the diameter of the particle materials.

Further, the upper side flexible connection corrugated pipe and the lower side flexible connection corrugated pipe are made of changeable plastic materials and can be replaced periodically.

Further, a plurality of material stirring plates are arranged on the upper surface of the material stirring disc, and the material stirring plates are arranged along the diameter direction of the material stirring disc and are shorter than the radius.

Further, the stirring motor is a variable frequency motor, and the rotating speed of the stirring rod needs to be adjusted according to the requirement.

Further, stirring blades are arranged at the middle part and the bottom of the stirring rod.

Further, a spiral blade for accelerating discharging is arranged on the stirring rod in the conical disc.

Compared with the prior art, the utility model has the following beneficial effects:

the feed inlet is divided into a liquid feed inlet and a particle feed inlet, the traditional tank body is not provided with a particle material dispersing device, the particle material directly enters the tank body through the particle feed inlet once and can be dispersed in a solvent only after a long time.

According to the vertical stirring type concentrated tank, the gap adjusting mechanisms for driving the conical discs to be close to or far from the stirring disc are arranged on the upper tank body and the lower tank body, the size of the adjustable gap is determined by the height of the conical discs, the adjustment is convenient, and meanwhile smooth discharging is ensured.

In order to prevent blockage, the stirring rod in the conical disc is also provided with a spiral blade for accelerating discharging.

The vertical stirring type concentrated preparation tank provided by the utility model has the advantages that the particle material dispersing device is of a built-in type, and the external pollution is avoided during preparation.

Drawings

In order to more clearly illustrate the embodiments of the present utility model or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. Like elements or portions are generally identified by like reference numerals throughout the several figures. In the drawings, elements or portions thereof are not necessarily drawn to scale.

FIG. 1 is a schematic diagram of a first embodiment of the present utility model;

FIG. 2 is a schematic view of the external structure of the gap adjusting mechanism of the present utility model;

FIG. 3 is a schematic view of the internal structure of the kick-out plate of the present utility model;

FIG. 4 is a schematic view showing the internal structure of the present particulate material dispersing apparatus;

FIG. 5 is a schematic diagram of a second embodiment of the present utility model;

in the figure: 1. tank body 2, temperature adjusting sleeve 3, stirring motor 4, reduction gear 5, puddler 6, tank body ring 7, upside flexonics bellows 8, downside flexonics bellows 9, taper dish 10, connecting rod 11, dial charging tray 12, clearance adjustment mechanism 13, dial flitch 14, stirring leaf 15, helical blade.

Detailed Description

The utility model is further described below with reference to the accompanying drawings:

the present utility model is further illustrated by the following examples, which are not intended to be limiting, but any modifications, equivalents, improvements, etc. within the spirit and principles of the present utility model are intended to be included within the scope of the present utility model.

Example 1

As shown in fig. 1, the vertical stirring type thick tank comprises a tank body 1 with a feed inlet and a discharge outlet, wherein the feed inlet is arranged at the top of the tank body, the discharge outlet is arranged at the bottom of the tank body, a temperature adjusting sleeve 2 is arranged on the outer wall of the tank body 1, the vertical stirring type thick tank further comprises a stirring rod 5 arranged in the tank body 1, a power mechanism for driving the stirring rod 5 to rotate is arranged at the top of the tank body 1, the power mechanism comprises a speed reducer 4 fixed at the top of the tank body 1, the upper end of the stirring rod 5 extends to the outer side of the tank body 1 and is in power connection with a power output shaft of the speed reducer 4, a power input shaft of the speed reducer 4 is in power connection with a stirring motor 3, the middle upper part of the tank body 1 is provided with a particle material dispersing device, the feed inlet is divided into a liquid feed inlet and a particle feed inlet, the traditional tank body 1 is not provided with the particle material dispersing device, the particle material is directly disposable to enter the tank body 1 through the particle feed inlet, the inside, the long time is required to be dispersed in a solvent, the particle material is directly disposable to enter the tank body 1, the inside the tank body, the particle material is easy to enter the speed reducer 4, the speed reducer is further, the particle material is dispersed through the particle material dispersing device, the particle material is dispersed into the particle material 1, the particle material uniformly and the particle material after the particle material is dispersed through the primary dispersing device, the particle material and the particle material is stable, the particle material and the particle material is stable, and the particle material quality and the particle material and stable.

Preferably, the tank body 1 comprises an upper tank body and a lower tank body positioned below the upper tank body, and the split installation is convenient for arranging the particle material dispersing device on the inner wall of the tank body 1, so that the product is prevented from being polluted by the outside.

Preferably, as shown in fig. 4, the material dispersing device comprises a tank ring 6 between an upper tank body and a lower tank body, the tank ring 6 is connected with the upper tank body through an upper side flexible connection corrugated pipe 7, the tank ring 6 is connected with the upper tank body through a lower side flexible connection corrugated pipe 8, a conical disc 9 coaxial with the tank ring 6 is arranged at the center of the tank ring 6, two ends of the conical disc 9 are opened, the upper part is a large diameter end, the bottom is a small diameter end, a plurality of horizontal connecting rods 10 are uniformly distributed on the outer wall of the conical disc 9, the other ends of the connecting rods 10 are all fixed on the inner wall of the tank ring 6, the rod body of the stirring rod 5 penetrates through the conical disc 9, a stirring disc 11 matched with the small diameter end of the conical disc 9 is arranged on the stirring rod 5, the stirring disc 11 is arranged below the conical disc 9, an adjustable gap L is arranged between the stirring disc 11 and the conical disc 9, the upper tank body and the lower tank body are provided with a gap adjusting mechanism 12 for driving the conical disc 9 to approach or separate from the stirring disc 11, the size of the adjustable gap is determined by the height of the conical disc 9, the outer diameter of the large diameter end of the conical disc 9 is slightly smaller than the inner diameter of the tank body ring 6, the inner diameter of the tank body ring 6 is always equal to the inner diameter of the middle part of the tank body 1, the diameter of the stirring disc 11 is larger than or smaller than or equal to the inner diameter of the small diameter end of the conical disc 9, particle materials directly enter the tank body 1 through the particle feeding hole at one time and are collected in the conical disc 9, the materials at the bottom of the conical disc 9 are accumulated on the upper surface of the stirring disc 11, at the moment, the stirring motor 3 and the speed reducer 4 are required to be started simultaneously to control the stirring rod 5 to rotate, the particle materials are thrown into the lower tank body below the stirring disc 11 and fall into a solvent which is filled in advance under the action of centrifugal force, the particle materials are initially dispersed, the dispersed granular materials can be more easily dispersed after being added into the solvent, the product quality is uniform and stable, and the production efficiency is improved.

Preferably, as shown in fig. 2, the gap adjusting mechanism 12 includes a plurality of gap adjusting monomers uniformly distributed on the outer side of the tank ring 6, each gap adjusting monomer is vertically arranged and is located on the same circle with the center line of the tank ring 6, the gap adjusting monomer includes a screw 12.1, the upper end of the screw 12.1 is fixed on the outer wall of the upper tank, the lower end of the screw 12.1 is fixed on the outer wall of the lower tank, a screw 12.2 is connected to the screw 12.1 in a threaded manner, the outer ring of the tank ring 6 is provided with a bearing mounting seat, the screw 12.2 is mounted on the bearing mounting seat on the outer wall of the tank ring 6 through a thrust bearing 12.3, the tank ring 6 is lifted by rotating the screw 12.2 under the condition that the relative positions of the upper tank and the lower tank are not moved, the stirring rod 5 is fixed relative to the upper tank, so that the gap between the conical disk 9 and the stirring rod 11 is adjusted, the gap is adjusted according to the diameter of the material, the larger diameter of the material is adjusted, the larger gap is required to be added, and the larger gap is also required to be adjusted smoothly.

Preferably, the upper flexible connection bellows 7 and the lower flexible connection bellows 8 are made of plastic materials which can be replaced periodically.

Preferably, as shown in fig. 3, a plurality of kick-out plates 13 are disposed on the upper surface of the kick-out plate 11, and the kick-out plates 13 are disposed in the diameter direction of the kick-out plate 11 and shorter than the radius.

Preferably, the stirring motor 3 is a variable frequency motor, and the rotation speed of the stirring rod 5 needs to be adjusted as required.

Preferably, stirring blades 14 are arranged at the middle part and the bottom part of the stirring rod 5.

The utility model has three working modes:

mode one: all solvents enter the tank body 1 through a feed inlet at the bottom of the tank body 1, at the moment, the stirring motor 3 is required to be started simultaneously, the granular materials directly enter the tank body 1 through a granular feed inlet at the top of the tank body 1 and are collected in the hollow conical disc 9, the materials at the bottom of the conical disc 9 are stacked on the upper surface of the stirring disc 11, the stirring motor 3 and the speed reducer 4 control the stirring rod 5 to rotate, under the action of centrifugal force, the granular materials are thrown into a lower tank body below the stirring disc 11 and fall into the solvent which is filled in advance, the granular materials are initially dispersed, the dispersed granular materials can be dispersed more easily after being added into the solvent, the product quality is uniform and stable, and the production efficiency is improved.

Mode two: the solvent of some gets into jar body 1 through the feed inlet at jar body 1 top in, need open agitator motor 3 simultaneously this moment, granule material is direct to get into jar body 1 inside through the granule feed inlet at jar body 1 top, collect inside conical dish 9, the material of conical dish 9 bottom is piled up at the upper surface of dialling charging tray 11, agitator motor 3, reduction gear 4 control puddler 5 is rotatory, under the effect of centrifugal force, granule material is thrown into the lower jar body of dialling charging tray 11 below, and fall into in the solvent of pouring into earlier, after the granule material adds, the remaining solvent gets into jar body 1 through the feed inlet at jar body 1 top, granule material is initially dispersed earlier, can disperse more easily after the granule material that disperses is added to the solvent again, product quality is even stable, improve production efficiency.

Mode three: all solvents enter the tank body 1 through a feed inlet at the top of the tank body 1, the stirring motor 3 is required to be started simultaneously, meanwhile, particle materials directly enter the tank body 1 through a particle feed inlet at the top of the tank body 1, the solvents and the particle materials are simultaneously collected in the conical disc 9, the materials at the bottom of the conical disc 9 are stacked on the upper surface of the stirring disc 11, the stirring motor 3 and the speed reducer 4 control the stirring rod 5 to rotate, the particle materials are thrown into a lower tank body below the stirring disc 11 under the action of centrifugal force, the particle materials are initially dispersed, the dispersed particle materials are easier to disperse after being added into the solvents, the product quality is uniform and stable, and the production efficiency is improved.

In practical application, the mode one, the mode two and the mode three have better stirring and preparing effects compared with the traditional thick preparing tank.

In the second embodiment, referring to fig. 5, a first difference from the first embodiment is that, to prevent clogging, the stirring rod 5 in the conical disc 9 further has a spiral blade 15 for accelerating discharging.

In order to prevent blockage, the stirring rod in the conical disc 9 is also provided with a spiral blade for accelerating discharging.

The foregoing has shown and described the basic principles, main features and advantages of the present utility model. It will be understood by those skilled in the art that the present utility model is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present utility model, and various changes and modifications may be made without departing from the spirit and scope of the utility model, which is defined in the appended claims. The scope of the utility model is defined by the appended claims and equivalents thereof.

The present utility model is not described in detail in the present application, and is well known to those skilled in the art.

Claims

1. The utility model provides a jar is joined in marriage to vertical stirring formula is strong, includes the jar body that has feed inlet and discharge gate, be provided with the cover that adjusts the temperature on the outer wall of jar body, its characterized in that still includes the puddler that is in the jar body, the pivoted power unit of drive puddler is installed at the top of jar body, power unit is including fixing the reduction gear at jar body top, the upper end of puddler extends to jar external side and the power take off shaft power connection of reduction gear, the power input shaft and the agitator motor power connection of reduction gear, the well upper portion of jar body is provided with granule material dispersion devices.

2. The vertical stirring tank of claim 1, wherein the tank body comprises an upper tank body and a lower tank body below the upper tank body.

3. The vertical stirring type thick distributing tank according to claim 2, wherein the material dispersing device comprises a tank body ring arranged between an upper tank body and a lower tank body, the tank body ring is connected with the upper tank body through an upper side flexible connection corrugated pipe, the tank body ring is connected with the upper tank body through a lower side flexible connection corrugated pipe, a conical disc coaxial with the tank body ring is arranged at the center of the tank body ring, two ends of the conical disc are opened, the upper part is a large-diameter end, the bottom is a small-diameter end, a plurality of horizontal connecting rods are uniformly distributed on the outer wall of the conical disc, the other ends of the connecting rods are all fixed on the inner wall of the tank body ring, a rod body of a stirring rod penetrates through the conical disc, a stirring disc matched with the small-diameter end of the conical disc is arranged on the stirring rod, the stirring disc is positioned below the conical disc, an adjustable gap is reserved between the stirring disc and the conical disc, and a gap adjusting mechanism for driving the conical disc to be close to or far away from the stirring disc is arranged on the upper tank body and the lower tank body.

4. The vertical stirring type concentrated tank according to claim 3, wherein the gap adjusting mechanism comprises a plurality of gap adjusting monomers uniformly distributed on the outer side of the tank body ring, each gap adjusting monomer is vertically arranged and is positioned on the same circle with the center line of the tank body ring, the gap adjusting monomers comprise a screw, the upper end of the screw is fixed on the outer wall of the upper tank body, the lower end of the screw is fixed on the outer wall of the lower tank body, a screw pipe is connected to the screw rod in a threaded manner, the outer ring of the tank body ring is provided with a bearing mounting seat, and the screw pipe is mounted on the bearing mounting seat on the outer wall of the tank body ring through a thrust bearing.

5. The vertical stirring type thick tank of claim 4, wherein stirring blades are arranged at the middle part and the bottom of the stirring rod.