KR20170010437A - A operating method of system structure of impeller for dispersion-emulsion apparatus based on dual rotator - Google Patents

Abstract

The present invention relates to an installing and operating method of an impeller structure system for a dispersion-emulsion device of a rotator-rotor type, which improves grain size uniformity and, more specifically, to an installing and operating method of an impeller structure system for a dispersion-emulsion device of a rotator-rotor type, comprising: a first drive shaft; a first rotor; a first motor; a first belt; a first mechanical seal; a second drive shaft; a second rotor; a second motor; a second belt; a second mechanical seal; a cylinder; and a material suction pump.

Description

Technical Field [0001] The present invention relates to a rotor-rotor type dispersing and emulsifying apparatus, and more particularly, to an impeller-

The present invention relates to a method of installing and operating an impeller structure system for a rotor-rotor type dispersion and emulsification apparatus, and more particularly, to an impeller structure including a first rotor and a second rotor, Are driven in opposite rotational directions by respective drive motors, and each object to be mixed passes sequentially through the multi-stage impeller parts one-pass at a time, thereby greatly shortening the entire working time for dispersion emulsification processing, The present invention relates to a method of installing and operating an impeller structure system of a rotor-rotor type dispersing and emulsifying apparatus in which uniformity of particle size is improved by finely shearing (cutting) a material (object material)

(Materials) and other materials (substances) selected in the basic material industry in each technical field including food, cosmetics, ink, paint, adhesive, coating agent, fine chemical, medicine, nano- Is used as a base material.

The materials to be mixed as the base material have a significant influence on the quality of the finished product due to the uniformity and fineness of mixing by the dispersing and emulsifying process of each particle, and various dispersing and emulsifying apparatuses suitable for these demands have been developed and used.

Dispersion (homogenization) is a method in which a solid containing a powder is mixed homogeneously in a liquid or a liquid other than the liquid, so that the size of the particle is reduced and uniformly present in a stable state. "And" emulsion "that mixes the" first liquid "and the" second liquid "in which the interface exists.

In other words, dispersion and homogenization means making the particle size small. To make the particle size small, it is necessary to apply the strong energy (driving force) to the material to crush or shear or cut the particle size. Small.

Conventional dispersing and emulsifying apparatus is a high-pressure homogenizer, which converts the kinetic energy of a jet into shear energy by converting the pressure (energy) into a jet to collide or invert the material (material, material) So that dispersion and emulsification are performed. In this method, the pressure and the velocity gradient exist in the reactant (material to be mixed) in the process, so that the air dissolved in the contents generates bubbles, the particles mixed by the bubbles become uneven, And the time required for emulsification is long, resulting in a problem of deteriorating efficiency.

On the other hand, we will look more closely at dispersion versus mixing.

Dispersion is a state in which particles of a substance are made very small and particles and particles are stably and uniformly distributed to each other, and mixing is a simple mutual mixing of a substance (material) and a material (material) unlike dispersion.

When the propeller and impeller are rotated using the mixing equipment such as overhead, the two materials are mixed by the rotation of the impeller blades. This is a simple mixing process in which the particle size is reduced, that is, the homogenization process is omitted.

The unit indicating the degree of particle size reduction in the mixing process is the "shearing force" and the difference between mixing and dispersing is very large as follows.

On the other hand, the viscosity of the object to be dispersed is the most problematic in dispersion performance. Even when the viscosity is higher than about 2,000 mPas, the dispersion efficiency is lowered. When the viscosity is 5000 mPas, dispersion using a general apparatus is not achieved.

Viscous materials increase the rotational speed of the impeller to increase the tip speed of the rotor and provide a fence around the impeller to reduce the numerical value of the clearance or gap The shearing force must be increased.

1 is a functional structural diagram illustrating an ultrasonic dispersion and emulsification method according to an embodiment of the prior art.

As described with reference to the attached drawings, the ultrasound dispersion emulsification emits 20 kHz ultrasound into a solution with a strong intensity, and a lot of microcavity is generated in the solution. When the microcavity is broken, And the particles of the object to be dispersed are broken up very finely (finely) by the shock wave energy. The dispersing and emulsifying method using ultrasonic waves is very effective and has the advantage of enabling nano-sized dispersion and emulsification. However, dispersing and emulsifying the viscous material takes a long time and has limitations on uniformity and homogeneity of mixing.

2 is a functional structural diagram illustrating a rotor-stator type dispersion and emulsification method according to an embodiment of the prior art.

Referring to the accompanying drawings, particles of a target material (material) passing between a rotor and a stator by a strong shearing force, which is composed of a fixed stator and a rotating rotor and is generated by strong rotational energy of the rotor, It is a rotor-stator system in which dispersive emulsification is performed.

The tip speed of the rotor, which rotates at a speed of tens of thousands of rpm by a motor with a strong rotating force, reaches about 20 m / sec, which allows the dispersed object (material) to pass between the rotor- . At this time, the clearance between the rotor and the stator, that is, the gap of the rotor-stator is about 0.1 mm, which forms a very small gap. When the object to be dispersed passes through the gap between the narrow rotor / stator at a strong rotation speed, a shearing effect occurs and the particle size shear or shear instantaneously to a very small extent.

This rotor-stator method was developed decades ago, and for a long time, Germany's IKA had the patent right, and now the patent has expired and its method is already open.

The advantage of this method is that it can disperse high viscosity and has good dispersing and emulsifying effect from the viewpoint of process convenience. Currently, it is the mainstream of dispersing and emulsifying apparatus based on most rotor-stator methods and there are differences in performance. However, .

However, there is still a problem that dispersion of fine particles at the level of nanoparticles having a small particle size to be mixed is difficult to be mixed and takes a long time to process.

Therefore, rotor-rotor method is adopted instead of the rotor-stator method to improve the uniformity of particles by homogenizing the particles by increasing the shear force, and the processing time is improved even in the case of fine particle dispersion oiling at the nanoparticle level Need to develop.

Korean Patent Application No. 10-2001-0053204 (Aug. 31, 2001) "A method of sealing a radial gap between a seal assembly, a turbine rotor and a stator device, and a rotor and a stator ) " Korean Patent Application No. 10-2014-7025991 (Apr. 24, 2013) "VANE-TYPE PUMP HAVING A HOUSING, HAVING A DISPLACABLE STATOR, AND HAVING A ROTOR THAT IS ROTATABLE WITHIN THE STATOR)

SUMMARY OF THE INVENTION The present invention has been made in order to solve the above-mentioned problems, and it is an object of the present invention to solve the problems of the conventional rotor-stator system and to construct the impeller of the rotor-rotor type, thereby constituting the impeller composed of the first rotor and the second rotor in multi- Rotor type dispersing and emulsifying apparatus for improving the grain uniformity by shortening the overall working time of the production and enhancing the particle homogeneity of the product because the material is sequentially passed through the multi-stage impeller all at once, The goal is to provide a method of installation and operation of the rescue system.

However, the object of the present invention is not limited to the above-mentioned objects, and other objects not mentioned can be clearly understood by those skilled in the art from the following description.

In order to achieve the above object, there is provided a method of installing and operating an impeller structural system for a rotor-rotor type dispersing and emulsifying apparatus, including a first drive shaft, a first rotor, a first motor, a first belt, a first mechanical seal, 1. A rotor-rotor type dispersion emulsification apparatus comprising: a first rotor, a second rotor, a second rotor, a second motor, a second belt, a second mechanical seal, a cylinder and a material suction pump, Wherein the first rotor top constituting the first rotor is directed downward and the second rotor top constituting the second rotor is arranged so as to face the first rotor and the second rotor in an upward direction, A first step of inserting the first rotor into the second rotor so that the two rotor blades are adjacent to each other with the gap formed, thereby forming one unit impeller; A second step of vertically stacking one or more unit impellers vertically to form a multi-stage impeller part; The first drive shaft is inserted into the first rotor through hole formed at the center of the impeller portion from the upper side downward and the lower end portion of the first drive shaft is bolted to fix the first rotor to the first drive shaft A third step; Wherein a fixing bracket is formed at an edge portion of the impeller portion to have an outer diameter equal to the outer diameter of the second rotor and formed in a disc shape and having a through hole at the center and a material moving hole through which the material moves, A fourth step of fastening the second rotor by fastening bolts to one or more first fixing parts formed at edge portions of the fixing brackets; And fixing the fixing bracket to the second driving shaft by bolting the second driving shaft to the through hole of the fixing bracket; . ≪ / RTI >

The first fixed shaft, the second fixed shaft, and the impeller are housed in the cylinder, the first fixed shaft is fixed to the upper end of the cylinder in a rotating state, and the first mechanical shaft A sixth step of installing a seal; As shown in FIG.

Wherein the first fixing shaft, the second fixing shaft, and the impeller are housed in a cylindrical interior of the cylinder, and the second fixing shaft is fixed to the lower end of the cylinder in a rotational state to seal the lower end of the cylinder, A seventh step of installing a second mechanical seal; As shown in FIG.

The axial centerline of the first drive shaft and the axial centerline of the second drive shaft are located on a straight line and are positioned on the cylindrical inner center line of the cylinder so that the first rotor and the second rotor are not in contact with each other .

A seventh step of fixing the first motor and the second motor to one side of the cylinder and installing a first belt for transmitting rotational power of the first motor to the first drive shaft; As shown in FIG.

An eighth step of providing a second belt for transmitting rotation power of the second motor to the second drive shaft; As shown in FIG.

Wherein the cylinder is provided with a discharge port through which material is introduced into the cylinder and a discharge port through which material is discharged from the inside of the cylinder, the discharge port being provided at a lower portion of the cylinder, And a material suction pump for supplying the material to the inside of the cylinder may be provided at the front end of the inlet.

The present invention improves the problems of the conventional rotor-stator method and configures and applies the impeller in a rotor-rotor manner. The impeller composed of the first rotor and the second rotor is constructed in a multi-stage structure and the multi- And the dispersion emulsification process is performed by a one-pass treatment process. Therefore, the overall working time is shortened due to the strong shear force, and the particle uniformity of the material to be mixed is improved.

BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a functional block diagram illustrating an ultrasonic dispersion and emulsification method according to an embodiment of the prior art;
FIG. 2 is a functional constitutional view illustrating a rotor-stator type dispersion and emulsification method according to an embodiment of the prior art,
FIG. 3 is an illustration showing a rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention.
4 is a functional structural view illustrating the structure of the first rotor 30a and the second rotor 30b of the rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention,
5 is a perspective view of a rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention,
6 is a side view (FIG. 6A) and a top view (FIG. 6B) of a rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention,
7 is a functional diagram for explaining the overall configuration of a rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 including a control unit and the structure of a multistage impeller 30u for high viscosity dispersion according to an embodiment of the present invention. ,
FIG. 8 is a view for explaining the processing sequence and the processing time by the dispersion-emulsification process of the rotor-rotor type configuration according to the present invention and the configuration according to one embodiment,
FIG. 9 is a flowchart illustrating an installation and operation method of a rotor-rotor type dispersion and emulsification apparatus impeller structure system according to an embodiment of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a detailed description of preferred embodiments of the present invention will be given with reference to the accompanying drawings. In the following description of the present invention, detailed description of known functions and configurations incorporated herein will be omitted when it may make the subject matter of the present invention rather unclear.

In the following description, the rotor and the impeller are used in the same sense and can be used selectively for smooth explanation of the context. Materials and materials are used interchangeably and can be selectively used for contextual explanations.

FIG. 3 is an illustration showing a rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention.

3, the impeller structure system 100 of the rotor-rotor type dispersion and emulsification apparatus includes a first motor 11, a first belt 12, a first drive shaft 13, a first mechanical The first rotor 30a and the second rotor 30b are connected to each other through the seal 14, the second motor 21, the second belt 22, the second drive shaft 23, the second mechanical seal 24, the cylinder 30, 30b, an inlet port 31, a discharge port 32, and a material suction pump 33. [

The rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 can be divided into rotor-rotor type and rotor-stator type as shown in FIG. 2B attached to the description of the prior art, Dispersion, mixing, emulsification and discharge can be processed by a one-pass process.

FIG. 4 is a functional structural view illustrating the structure of the first rotor 30a and the second rotor 30b of the rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention. 5 is a perspective view of a rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention. FIG. 6 is a perspective view of a rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention. (Fig. 6A) and a top view (Fig.

3 to 6, the rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 converts the rotor-stator type rotor-rotor type multi-stage impeller structure according to the prior art, The efficiency of the system is greatly improved.

That is, in the high-viscosity dispersion emulsifying apparatus according to the related art, the material (material) moves in a minute interval between the stopped stator and the rotating rotor, but in the present invention, the second rotor 30b are rotated in the direction opposite to the first rotor 30a to improve the mobility and shear energy of the material (material), thereby improving the dispersion and emulsification efficiency of the highly viscous material having low fluidity.

More specifically, the first drive shaft 13 connected to the first motor 11 through the first belt 12 rotates the first drive shaft 13 along the forward (anticlockwise) rotation of the first motor 11 Rotate in the forward direction (counterclockwise direction).

The first drive shaft 13 is fixedly mounted on the upper end of the central portion of the sealer 30 inside the cylinder 30 which is closed by the first mechanical seal 14 and is formed long from the upper end portion toward the lower end portion, Receives the power of the first motor (11) through the first belt (12) and rotates in the forward direction (counterclockwise direction).

In the following description, the rotation direction of the first motor 11 may be referred to as a first direction.

The first rotor shaft (13) includes a first rotor shaft (13) and a second rotor shaft (13). The first rotor shaft the first rotor 30a having a plurality of teeth 310 arranged at equal intervals on the cascade of the same center is rotated in the forward direction (counterclockwise direction) in association with the first driving shaft 13. Herein, the circumference refers to a line formed by the circumference, and the following description will be made by those skilled in the art that can be easily understood by those skilled in the art.

Here, it is relatively preferable that the circumference of the same center where the first rotor tops 310 are arranged is one or more and three circumferences, and the first rotor 30a provided on the first driving shaft 13 is a one- And is preferably composed of five stages, but it is quite natural that it can be increased or decreased as needed.

The second drive shaft 23 connected to the second motor 21 via the second belt 22 is rotated in the reverse direction (clockwise direction) of the second motor 21 to rotate the second drive shaft 23 in the opposite direction Direction).

In the following description, the rotation direction of the second motor 21 may be referred to as the second direction.

The second drive shaft 23 formed from the lower end portion toward the upper end portion of the cylinder 30 is fixed to the lower portion of the cylinder 30 inside the cylinder 30 which is closed by the second mechanical seal 24 in the reverse direction Clockwise).

A second driving shaft 23 connected to the brackets 23, and a second driving shaft 23 connected to the brackets 23. The first driving shaft 23 is connected to the brackets 23, The second rotor 30b, in which a plurality of rotor teeth 320 are arranged at equal intervals on the cascade of the same center, rotates in the opposite direction (clockwise) in association with the second drive shaft 23.

In this case, it is relatively preferable that the circumference of the same center, in which the second rotor tops 320 are arranged, be one or more and two circumferences, and the second rotor 30b connected to the second driving shaft 13, Is composed of any one value selected from the range of 1 to 10 stages of the same number as that of the rotor 30a, and is preferably composed of 5 stages, but it is quite natural that it can be increased or decreased as needed.

As shown in FIGS. 3 and 4, the embossing projections of the second rotor 30b and the embossing projections of the first rotor 30a are arranged so as to be interlaced with each other without overlapping each other, and the first rotor 30a A minute gap or clearance is formed between the relief projections of the second rotor 30b and the relief projections of the second rotor 30b to shear, disperse, mix, and emulsify the introduced material.

4, the reference numeral 1f denotes a rotating direction of the first rotor 30a, and 2f denotes a substance moving direction. The first rotor 30a and the second rotor 30b form a high viscosity dispersing impeller 30u and the impeller 30u is preferably composed of one or more multistage and five stages. It is quite natural to be able to.

It can be seen that the material (material) moves diagonally along the gaps or intervals between the respective protrusions and the protrusions constituting the first rotor tooth 310 by the rotation of the first rotor 30a have.

The first rotor 30a and the second rotor 30b rotate in opposite directions and the material (material) moving along the gap rotates in the opposite direction by the corresponding protrusions of the first rotor 30a and the second rotor 30b, Dispersed, mixed, and emulsified. This process is repeated by a multi-stage impeller.

Therefore, the number of impellers can be increased or decreased according to the given conditions such as the material (material), the application, the capacity, and the like, and it is generally preferable to configure the impeller in five stages. In the case where the unit number of the impeller is small, Can be introduced into the material inlet pump 33 and then introduced into the inlet 30 by driving the material suction pump 33 and reintroduced into the cylinder 30, The efficiency may be lowered.

7 is a functional diagram for explaining the overall configuration of a rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 including a control unit and the structure of a multistage impeller 30u for high viscosity dispersion according to an embodiment of the present invention. to be.

Hereinafter, with reference to all the accompanying drawings, 1af and 2af in FIG. 7 indicate the moving direction of the charged material (material).

That is, the material (material) charged into the cylinder 30 through the material suction pump 33 and the injection port 31 provided in the lower side surface of the cylinder 30 is supplied to the respective stages of the high viscosity dispersion impeller 30u The rotor 30a and the second rotor 30b are successively passed through the one-pass system sequentially in a multi-stage or five-stage repeated impeller configuration, And the dispersion and emulsification process of discharging through the formed discharge port 32 proceeds.

The load of the first motor 11 and the second motor 21 can be relieved and the first motor 11 and the second motor 21 can be smoothly supplied to the cylinder 30 even in the case of a material having a high viscosity by the material suction pump 33, The motor 11 and the second motor 21 can increase the shear force by the reduced load and increase the dispersion emulsification efficiency.

The rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 is dispersed and emulsified by a high viscosity dispersing impeller 30u including a first rotor 30a and a second rotor 30b, thereby enhancing the efficiency of dispersion emulsification, Parallel type steric dispersion can be performed while passing the object material (material) to be subjected to a vertical multi-stage or five-stage rotor-rotor type impeller 30u, thereby maximizing the efficiency of the dispersion emulsification.

The rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 including the multistage impeller 30u for high viscosity dispersion is a one-pass type flow type, and dramatically enhances the efficiency of the dispersion and emulsification process.

FIG. 8 is a view for explaining the processing sequence and the processing time by the dispersion-emulsification process of the rotor-rotor type configuration according to the present invention and the configuration of the prior art by one embodiment.

Referring to all the drawings, FIG. 8 is a flow type in which the object to be dispersed and emulsified is processed in a one-pass manner from the input to the discharge of raw material, and the process time is shortened to 1/8 level compared to the conventional batch process Which can shorten the production process time and lower the production cost and the defect rate.

In addition, since the reaction time of the dispersion emulsification object is drastically shortened, there is almost no dispersion heat generation compared to the conventional inline mixer, so there is an advantage that the physical properties of the reactant are not changed by the dispersion emulsification process.

Table 1 below illustrates the dispersion and emulsification problems of high viscosity materials and the advantages of the rotor-rotor type dispersion emulsification apparatus impeller structure system 100 according to one embodiment of the present invention.

Problems of high viscosity material dispersion Advantages of the rotor-rotor type dispersing device 100 - High viscosity materials are technically limited to achieve high dispersion in terms of uniformity.
- High cost if you scale up your existing mixer to more than laboratory.
- The larger the treatment capacity, the more the area of agitation, the lower the quality, the longer the treatment time is required (more than 8 hours)
- Low quality and low yield due to backward process - Dispersion and emulsification with high uniformity by rotor-rotor method.
- Large capacity to small capacity can be processed.
- Reduction of work time by flow-type one-pass process from pre-mixing to input and discharge of raw materials.
- The residence time of dispersing reactor is greatly reduced and no deterioration due to heat generation occurs during dispersion emulsification.

The rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 according to an embodiment of the present invention can be applied not only to the material industry but also to a process requiring high efficiency dispersion, emulsification, atomization and mixing, , Adhesives, films, coatings, inks, paints, fine chemicals, electronic materials, and polymer industries.

That is, the rotor-rotor type dispersing and emulsifying apparatus impeller structure system (100) is dispersed and emulsified by a one-pass flow method, and there are difficulties in terms of process time and quality. In the batching process requiring uniform mixing and dispersion with shear energy And the technical ripple effect is expected to be greatly expected.

Hereinafter, examples of application of the rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 and examples of solving the problems will be described by fields.

<Ink Mixing / Manufacturing Process>

Inks are manufactured in a conventional manner, and are complicated processes in which materials are mixed, dissolver, 3-roll mill and bead mill are dispersed, varnish is added, additives are added, and dissolving is performed again.

Rotor-Rotor Dispersion Emulsification Apparatus When the impeller structure system 100 is applied to a process, it is possible to shorten the process time by supplying high shear energy in material mixing and dissolver process.

<Additive Mixing Step of Foaming Adiabatic Agent>

A very small amount of the additive for foaming the insulating material in the step of manufacturing a foam insulating material is added. It is relatively difficult to continuously mix the additive added in a small amount in the production stage.

Application of the rotor-rotor type dispersing and emulsifying apparatus impeller structure system (100) to the process enables a continuous production with a constant quality because a small amount of additive and heat insulating material are respectively injected and dispersed and emulsified in one pass. Even in adiabatic performance, an improved synergistic effect of 30% can be obtained.

<Silicon GUM Blending>

Silicon used for adhesives and films has recently been expanding its demand to be used for special protective films for smart phones. However, in the processing process at the production site where the silicon raw material is dissolved from the GUM state, the storage tank is heated to a temperature of 130 ° C. Since it must be cooled after 48 hours of operation, it takes a lot of production time and cost.

Rotor-Rotor Dispersion Emulsification Apparatus When the impeller structure system 100 is applied to such a process, the process can be completed in about 5 hours by the high shear force of the rotor-rotor, and mass production is possible.

<Technique to disperse graphene thinly and evenly>

Graphene used in touch panels, flexible displays, energy device electrodes and electromagnetic wave shielding films, automotive heat ray glasses, solar cells and semiconductor chips, transparent heaters, smart windows, various sensors and printing electronic inks has different conductivity, flexibility and durability. But it has a disadvantage that it is difficult to utilize it in real life because it is complicated in production process and difficult to mass-produce.

Rotor-Rotor Dispersion Emulsification Apparatus Using the impeller structure system (100), it is possible to mass-produce with the technology utilizing the high shear force of the rotor-rotor.

<Carbon black>

Industrial carbon black is used in a variety of applications such as printing ink, toner, coating, plastic, paper and construction, and is recently used for exterior coating of smart phones. Carbon black is very difficult to disperse as compared with other pigments, and since the components are carbon and the carbon is coagulated due to the characteristics of carbon, it does not fall off well, so that it is difficult to produce uniform quality products.

Rotor-rotor type dispersing and emulsifying apparatus Using the impeller structure system (100), the high shear force of the rotor-rotor is utilized to handle the dispersion emulsification of carbon, so that the product can be mass-produced in a uniform quality.

<Metal Paste Dispersion>

Nanometer metal paste used for chip capacitor, which is a core part of smart phone, is very important to disperse and it causes electrical failure if nano metal paste is not dispersed well.

Chip capacitors are core components that are used extensively in electronic devices and automobiles, as well as in mobile devices such as smart phones and tablet PCs, and serve to control power supply to be supplied in a timely manner as needed for each component.

Rotor-Rotor Dispersion Emulsification Apparatus The use of the impeller structure system (100) makes it possible to disperse and emulsify the nanometer metal paste by the high shear force of the rotor-rotor, thereby reducing electrical failure and mass-producing chip capacitors with uniform quality.

<Dispersion of medical polymer filler and collagen>

The filler which is frequently used in cosmetic molding means that it is filled in English. In the field of cosmetic molding, it refers to a complementary material that hides wrinkles and scars by injecting or inserting into the skin.

Currently, the filler field is divided into a product using a hyaluronic acid component, which is a biomaterial existing on the skin in the human body, and a product using a biocompatible polymer component.

Unlike hyaluronic acid products, which use biocompatible polymers for 6 months to 1 year, they are effective for more than 2 years through a single procedure. And it is known that it has a natural effect like a real organization.

In the domestic beauty sector, the filler market is about 100 billion won, and the global market is known as a large market with more than 2 trillion won, and it is expected to continue to grow due to aging population and increasing interest in beauty.

Collagen, which is a biocompatible polymer, has a problem in that it is difficult to stir and mass-produce because of its high viscosity, and thus the raw material is very expensive.

Rotor-Rotor Dispersion Emulsification Apparatus The impeller structure system (100) makes it possible to mass-produce the filler by utilizing the high shear force of the rotor-rotor and the ONE-PASS type.

&Lt; Secondary Battery Manufacturing >

Rechargeable batteries (lithium batteries) are expected to grow at a CAGR of around 22%, with demand for 125 GWh expected in 2018, driven by a steady increase in IT demand and demand for electric vehicle batteries and energy storage devices (ESS) do.

Lithium battery has a problem that it is not easy to make anode and cathode slurries by dissolving active material and binder in SOLVENT.

Using the rotor-rotor high shear force and one-pass type by using the rotor-rotor type dispersing and emulsifying apparatus impeller structure system (100), the dispersing emulsification time can be shortened very shortly and the coating process Connectivity improves productivity, lowers defects and reduces production costs.

FIG. 9 is a flowchart illustrating an installation and operation method of a rotor-rotor type dispersion and emulsification apparatus impeller structure system according to an embodiment of the present invention.

In the following, all of the drawings will be described in detail. In the following, the first drive shaft 13, the first rotor 30a, the first motor 11, the first belt 12, the first mechanical seal 14, A rotor-rotor type dispersion and emulsification apparatus impeller structure including a drive shaft 23, a second rotor 30b, a second motor 21, a second belt 22, a second mechanical seal 24, In the method of installing and operating the system, at least one of the first rotor and the second rotor is prepared (S1010).

The first rotor top 310 constituting the first rotor faces downward and the second rotor top 320 constituting the second rotor faces upward so that the first rotor faces the second rotor.

At this time, the first rotor is inserted into the second rotor so that the first rotor top and the second rotor top are adjacent to each other, thereby forming one unit impeller.

That is, a configuration in which one first rotor and a second rotor are arranged to face each other will be described below as a unit impeller.

A plurality of unit impellers are vertically stacked in a vertical direction with a value selected from a number ranging from 1 to 10, thereby forming an impeller portion (S1020).

A configuration in which the unit impellers are installed in multiple stages in the vertical direction will be described as an impeller section hereinafter.

A first drive shaft is prepared (S1030).

The first driving shaft is inserted into the first shaft fixing hole 312, which is a through hole formed at the center of the impeller or the first rotor, so that the first rotor is fixed on the outer circumferential surface of the first driving shaft in step S1040.

In this case, the first drive shaft may include a stopper jaw that restricts one or more of the first rotors from moving upward from the designated position, and one or more first rotors at the lower end thereof, A thread is formed to fasten the nut to be fixed to the first drive shaft.

According to another embodiment of the present invention, a first rotor fixing bracket fixed to an outer circumferential surface of the lower end of the first driving shaft and configured to fix one or more first rotors may be provided.

Since the structure for fixing and fixing is generally known easily, a detailed and detailed description will be omitted in the present invention.

A second drive shaft including the second rotor fixing bracket 230 is prepared (S1050).

The edge portion of the second rotor is fixed to the first fixing portion 232 formed at the edge portion of the second rotor fixing bracket 230 having a disk shape. For such a fixed installation, a bolt or a generally known method can be used.

A second drive shaft is fixed to the second fixing part 234 formed on the center of the second rotor fixing bracket, and a bolt or a generally known method can be used for the fixing operation.

The second rotor fixing bracket 230 is hollow as shown in FIGS. 10 to 12, and the first fixing part 232 is protruded outwardly on the outer side of the upper end, and the second rotor fixing bracket 230 is bolted And a second rotor fixing bracket main body 231 which is fixed to the second rotor fixing bracket 231.

A material movement hole (O) for material movement is formed in the second rotor fixing bracket body (231). The material moving hole O has a first material moving hole O2 formed on the upper surface of the second rotor fixing bracket body 231 and a plurality of second material moving holes O2 formed on the side surface of the second rotor fixing bracket body 231 in the circumferential direction And a second material movement hole (O1) that is formed.

That is, as shown in Fig. 3, the material is transferred by the material suction pump 33 and is introduced into the cylinder 30 through the charging port 31. The inserted material is introduced into the second rotor fixing bracket 230 through the second material moving hole O1 of the second rotor fixing bracket 230 installed in the cylinder 30, And is introduced to the second rotor side through the hole O2.

The second driving shaft 23 is fixed to the second fixing part 234 formed on the bottom surface of the second rotor fixing bracket body 231.

That is, when the second drive shaft 23 rotates, the second rotor fixing bracket 230 rotates. Rotation of the second rotor fixing bracket 230 rotates the second rotor.

A cylinder, a first mechanical seal, and a second mechanical seal are prepared (S1070).

The impeller portion in which the first drive shaft and the second drive shaft are fixed is installed inside the cylinder and the first mechanical seal is installed in the closed state at the upper end so that the first drive shaft is fixedly installed in the rotated state. In addition, since the second mechanical seal is installed in a closed state at the lower end of the cylinder, the second drive shaft is fixedly installed in a rotated state (S1080).

Here, it is assumed that the cylinder is provided with a charging port and a discharging port.

A first motor and a second motor each including a first belt and a second belt are prepared (S1090).

The first motor and the second motor are fixed to the periphery of the cylinder and the first motor and the first drive shaft are connected with the first belt so that the driving force of the first motor is transmitted to the first drive shaft. Meanwhile, the second motor and the second driving shaft are connected to each other by the second belt so that the driving force of the second motor is transmitted to the second driving shaft (S1100).

When the installation of the rotor-rotor type dispersion and emulsification apparatus impeller structure system 100 is completed, power is inputted to the first motor and the second motor respectively to check the normal driving state, and after completion of the surrounding cleaning and cleaning, The material is charged, dispersed and emulsified, and discharged to the discharge port.

The first rotor and the second rotor rotate in opposite directions to disperse and emulsify the material, which is the target material, in a state of improved particle size uniformity .

As described above, preferred embodiments of the present invention have been disclosed in the present specification and drawings, and although specific terms have been used, they have been used only in a general sense to easily describe the technical contents of the present invention and to facilitate understanding of the invention , And are not intended to limit the scope of the present invention. It is to be understood by those skilled in the art that other modifications based on the technical idea of the present invention are possible in addition to the embodiments disclosed herein.

11: first motor 12: first belt
13: first drive shaft 14: first mechanical seal
21: second motor 22: second belt
23: second drive shaft 24: second mechanical seal
30: Cylinder 30u: Multistage impeller for dispersion of high viscosity
30a: first rotor 30b: second rotor
31: Inlet port 32: Outlet port
100: Rotor-rotor type dispersion emulsifying apparatus Impeller structure system
230: fixing bracket 232: first fixing portion
234: second fixing part 310: first rotor saw
312: first shaft fixing hole 320: second rotor saw
33: Material suction pump

Claims (2)

A first motor, a second motor, a second motor, a second mechanical seal, a cylinder, a material sucking pump, and a second drive shaft, a first rotor, a first motor, a first belt, a first mechanical seal, a second drive shaft, A method of installing and operating an impeller structure system of a rotor-rotor type dispersing and emulsifying apparatus,
The first rotor top constituting the first rotor is directed downward and the second rotor top constituting the second rotor is arranged so as to face the first rotor and the second rotor in an upward direction, A first step of inserting the first rotor into the second rotor to form one unit impeller so that the rotor top and the second rotor top are adjacent to each other with a gap formed therebetween;
A second step of vertically stacking one or more unit impellers vertically to form a multi-stage impeller part;
The first drive shaft is inserted into the first rotor through hole formed at the center of the impeller portion from the upper side downward and the lower end portion of the first drive shaft is bolted to fix the first rotor to the first drive shaft A third step;
A second rotor fixing bracket having an outer diameter equal to the outer diameter of the second rotor and having a disk shape and having a through hole at the center thereof and a material movement hole through which the material moves, A fourth step of fixing the second rotor by fixing bolts to one or more first fixing parts formed on edge portions of the second rotor fixing brackets; And
A fifth step of securing the fixing bracket to the second driving shaft by bolting the second driving shaft to the through hole of the fixing bracket; , &Lt; / RTI &
The second rotor fixing bracket includes a second rotor fixing bracket body having a hollow shape and the first fixing portion formed on the outer side of the upper end to be bolted to the second rotor,
Wherein the second rotor fixing bracket body is formed with a material movement hole for material movement, the material movement hole includes a first material movement hole formed on the upper surface of the second rotor fixing bracket body, And a second driving shaft is fixed to a second fixing part formed on a bottom surface of the second rotor fixing bracket body,
The material transferred by the material suction pump and introduced into the cylinder through the charging port is introduced into the second rotor fixing bracket through the second material moving hole of the second rotor fixing bracket installed in the cylinder, Rotor type dispersing and emulsifying apparatus impeller structure system which is introduced into a second rotor side through a hole. The method according to claim 1,
Wherein a cylinder is provided with a discharge port through which material is introduced into the cylinder and a discharge port through which material is discharged from the cylinder,
The injection port is provided on the lower side of the cylinder and the discharge port is provided on the upper side of the cylinder,
And a material suction pump for supplying a material to the cylinder is provided at a front end of the inlet. A method of installing and operating an impeller structure system of a rotor-rotor type dispersion and emulsification apparatus.

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