KR20200125042A - Apparatus for manufacturing high activated hydrated lime using a vibrated chamber - Google Patents

Abstract

An apparatus for preparing highly activated hydrated lime using the vibration of a chamber comprises a mixing chamber, a filter chamber, a digestion reaction unit, and a storage unit. The mixing chamber uniformly receives quicklime and uniformly carries out sintering. The filter chamber is connected to an upper portion of the mixing chamber. The digestion reaction unit injects a digestion reaction liquid into the mixing chamber through the filter chamber. The storage unit stores hydrated lime generated from the mixing chamber. In this case, the mixing chamber includes an upper chamber vibrating in a horizontal direction to mix the digestion reaction liquid and the quicklime, and a lower chamber providing saturated steam and dry air from the lower side of the upper chamber to the upper chamber.

Description

Highly active slaked lime manufacturing equipment using chamber vibration{APPARATUS FOR MANUFACTURING HIGH ACTIVATED HYDRATED LIME USING A VIBRATED CHAMBER}

The present invention relates to an apparatus for producing highly active slaked lime, and more particularly, by mixing a reactant such as quicklime using vibration of a chamber, and using chamber vibration capable of producing a product such as highly active slaked lime through a digestion reaction. It relates to an apparatus for producing activated slaked lime.

In general, dust and harmful substances generated in industrial sites or incinerators cause fatal diseases when absorbed into the human body through air as well as environmental pollution, so a dust collecting device is used to remove pollutants and dust contained in gases and air. do.

In addition, the dust collector is largely divided into a dry dust collector and a wet dust collector.The dry separator uses a filter to remove dust and harmful substances contained in the air, and while the structure is simple, the efficiency of removing dust and pollutants is improved. There is a low problem. On the other hand, the wet dust collector is used mainly in recent years because of the high efficiency of removing dust and contaminants compared to the dry dust collector to collide with harmful gas and dust by spraying water.

Slaked lime is used in such a dry dust collector, and in the case of slaked lime, the dust and contaminants can be more effectively removed only when the specific surface area and pore volume are large.

On the other hand, a method for preparing highly reactive or highly active slaked lime has been developed in various ways, and Korean Patent Laid-Open No. 10-2001-0073716 describes a method of inhibiting the growth of slaked lime by adding alcohol in the wet digestion process of quicklime. It is starting.

In addition, Korean Patent Registration No. 10-1434253 discloses a method for producing highly reactive slaked lime having a high specific surface area, characterized by applying a process of irradiating the slaked lime with microwaves in order to have a high specific surface area.

However, even through the method for producing slaked lime that has been developed so far, the surface area and pore volume are large, so it is difficult to manufacture slaked lime that can more effectively remove dust and contaminants.

Republic of Korea Patent Publication No. 10-2001-0073716 Korean Patent Registration No. 10-1434253

Accordingly, the technical problem of the present invention is conceived in this respect, and an object of the present invention is to mix a reactant such as quicklime by using the vibration of the chamber, thereby producing a product such as highly active slaked lime through a digestion reaction. It is to provide a highly active slaked lime production apparatus using.

A highly active slaked lime production apparatus according to an embodiment for realizing the object of the present invention includes a mixing chamber, a filter chamber, a digestion reaction unit, and a storage unit. The mixing chamber is uniformly sintered by receiving quicklime uniformly. The filter chamber is connected to an upper portion of the mixing chamber. The extinguishing reaction unit injects the extinguishing reaction liquid into the mixing chamber through the filter chamber. The storage unit stores slaked lime produced in the mixing chamber. In this case, the mixing chamber includes an upper chamber vibrating in a horizontal direction to mix the digestion reaction liquid and the quicklime, and a lower chamber providing saturated steam and dry air to the upper chamber from a lower portion of the upper chamber. do.

In one embodiment, it may further include a driving unit connected to the upper chamber to vibrate the upper chamber in a horizontal direction.

In one embodiment, the driving unit may include a driving unit connected to the upper chamber to vibrate the upper chamber in a horizontal direction, and a bearing unit connected to the lower chamber to slide the lower chamber in a horizontal direction. .

In one embodiment, the bearing unit may include a guide extending parallel to a bottom surface of the lower chamber, and at least one conveying unit fixed to a bottom surface of the lower chamber and moving in a horizontal direction along the guide.

In one embodiment, the upper chamber is disposed in a first space of the upper chamber, a plurality of first diaphragms disposed with a first inclination, and a second inclination different from the first inclination It may include a diaphragm portion including a plurality of second diaphragms.

In one embodiment, each of the first and second diaphragms may decrease in size from the inlet of the quicklime toward the outlet of the slaked lime.

In one embodiment, the lower chamber may include a first supply pipe through which saturated steam is introduced from the outside, and a second supply pipe through which dry air is introduced from the outside.

In one embodiment, the lower chamber is located above the first distribution plate and the first distribution plate for uniformly dispersing the dry air introduced from the second supply pipe in the upper direction, and flows from the first supply pipe. It may include a second dispersion plate for uniformly dispersing the saturated steam in the upper direction.

In one embodiment, the first dispersion plate is a porous plate disposed in a horizontal direction, and the second dispersion plate has a'V'-shaped cross section, and a plurality of the first dispersion plates may be disposed spaced apart from each other.

In one embodiment, the extinguishing reaction unit includes a storage unit in which the extinguishing reaction solution is stored, a connection line extending from the storage unit to a lower space of the filter chamber to move the extinguishing reaction solution, and the filter chamber. It is provided in the connection line located in the lower space, it may include a spray nozzle for injecting the extinguishing reaction liquid into the interior of the upper chamber.

In one embodiment, the extinguishing reaction unit may further include a stirring part for mixing the extinguishing reaction liquid in which the extinguishing reaction retardant and the additive are mixed, and a heating part for heating the extinguishing reaction liquid.

In one embodiment, the filter chamber includes a filter unit provided in an upper space to collect scattered products generated from the formation of the slaked lime, and an air injection unit for injecting air to the filter unit above the filter unit. I can.

In one embodiment, a fan part connected to the upper part of the filter chamber may further include a fan part for sucking the scattered product collected in the filter part.

According to the embodiments of the present invention, since the mixing chamber in which the quicklime is mixed with the digestion reaction liquid is vibrated in the horizontal direction, the mixing of the quicklime can be promoted more uniformly and effectively, thereby improving the production efficiency of slaked lime. .

In addition, in consideration of the increase in the specific surface area and pore volume of slaked lime produced as the reaction between the quicklime and the digestion reaction solution proceeds in the upper chamber, the area decreases in the direction of the outlet and a plurality of installed in an inclined direction. By providing the diaphragms, the digestion reaction of quicklime can be further accelerated, and the uniformity of the overall mixing can be further improved.

In addition, the first and second dispersion plates are formed in the lower chamber, so that the dry air and saturated steam provided to the upper chamber can be more evenly distributed. In particular, the first dispersion plate is a porous dispersion plate to provide dry air. The second dispersion plate may be uniformly distributed, and a plurality of the second dispersion plates are arranged in a'V' shape, so that the material in a state in which saturated steam and dry air are mixed can be uniformly distributed upward.

On the other hand, the extinguishing reaction liquid is uniformly sprayed from the top of the upper chamber through the injection nozzle, so that the quicklime on the upper chamber is sprayed with a uniform extinguishing reaction liquid, so that the interface between the surface of the quicklime and the pores is more By uniformly activated, the specific surface area and pore volume of slaked lime to be produced can be increased.

In addition, through the filter unit provided in the filter chamber, a scattered product, which is a material scattered during the digestion reaction, may be recovered, thereby further improving the production efficiency of slaked lime.

1 is a schematic diagram showing a highly active slaked lime manufacturing apparatus according to an embodiment of the present invention.
FIG. 2 is a schematic diagram showing a flow state of quicklime in a mixing chamber of the highly active slaked lime production apparatus of FIG. 1.
3 is a schematic diagram showing a driving unit of the highly active slaked lime manufacturing apparatus of FIG. 1.
4 is a schematic diagram showing a mixing chamber of the highly active slaked lime manufacturing apparatus of FIG. 1.
5 is a schematic diagram showing an upper chamber of the highly active slaked lime manufacturing apparatus of FIG. 1.

The present invention will be described in detail in the text, since various modifications can be made and various forms can be obtained. However, this is not intended to limit the present invention to a specific form of disclosure, it is to be understood as including all changes, equivalents, or substitutes included in the spirit and scope of the present invention. In describing each drawing, similar reference numerals have been used for similar elements. Terms such as first and second may be used to describe various components, but the components should not be limited by the terms.

These terms are used only for the purpose of distinguishing one component from another component. The terms used in the present application are only used to describe specific embodiments, and are not intended to limit the present invention. Singular expressions include plural expressions unless the context clearly indicates otherwise.

In the present application, terms such as "comprise" or "consist of" are intended to designate the presence of features, numbers, steps, actions, elements, parts, or a combination thereof described in the specification, but one or more other features. It is to be understood that the presence or addition of elements or numbers, steps, actions, components, parts, or combinations thereof, does not preclude in advance the possibility of being added.

Unless otherwise defined, all terms used herein, including technical or scientific terms, have the same meaning as commonly understood by one of ordinary skill in the art to which the present invention belongs. Terms as defined in a commonly used dictionary should be interpreted as having a meaning consistent with the meaning in the context of the related technology, and should not be interpreted as an ideal or excessively formal meaning unless explicitly defined in this application. Does not.

Hereinafter, preferred embodiments of the present invention will be described in more detail with reference to the accompanying drawings.

1 is a schematic diagram showing a highly active slaked lime manufacturing apparatus according to an embodiment of the present invention. FIG. 2 is a schematic diagram showing a flow state of quicklime in a mixing chamber of the highly active slaked lime production apparatus of FIG. 1. 3 is a schematic diagram showing a driving unit of the highly active slaked lime manufacturing apparatus of FIG. 1. 4 is a schematic diagram showing a mixing chamber of the highly active slaked lime manufacturing apparatus of FIG. 1. 5 is a schematic diagram showing an upper chamber of the highly active slaked lime manufacturing apparatus of FIG. 1.

1 to 5, the highly active slaked lime manufacturing apparatus 10 according to the present embodiment includes a providing unit 100, a quantitative supply unit 200, a mixing chamber 300, a driving unit 400, and a storage unit. 500, a filter chamber 600, a fan part 700, and a fire extinguishing reaction unit 800.

The provision unit 100 stores quicklime (CaO) therein, and the quantitative supply device 200 is connected to the lower portion thereof to provide the quicklime to the quantitative supply device 200.

The quantitative supply device 200 has one end connected to the lower end of the providing unit 100 to receive the quicklime, and the other end connected to the mixing chamber 300, which will be described later, to transfer the quicklime to the mixing chamber ( 300).

In this case, the quantitative supply device 200 provides a constant amount of quicklime provided to the mixing chamber 300, and for this purpose, although not shown in detail, a separate quantitative supply feeder is provided therein. As a result, it is possible to implement quantitative provision.

The mixing chamber 300 includes an upper chamber 310 and a lower chamber 320, and is a chamber for generating slaked lime by performing a digestion reaction on the quicklime.

Specifically, the upper chamber 310 forms a first space 316 therein and extends in one direction, and an inlet 311 is formed at one end to uniformly distribute the quicklime from the quantitative supply device 200. Are provided.

In addition, the upper chamber 310 has an outlet portion 321 formed at the other end in the extending direction, that is, the second surface 313 of the upper chamber 310, and is generated by reacting in the first space 316 The slaked lime (Ca(OH) ₂ ) is provided to the storage unit 500.

In the first space 316 of the upper chamber 310, the quicklime provided from the quantitative supply device 200 is a digestion reaction liquid provided through the digestion reaction unit 800, and the lower chamber ( As the saturated steam and dry cane provided from the bottom through 320 are mixed with each other, the digestion reaction is carried out and accelerated, thereby generating slaked lime as a reactant.

In the first space 316 of the upper chamber 310, a partition 317 is disposed, and the partition 317 includes a plurality of first partitions 318 and a plurality of second partitions 319 ).

As shown, the first diaphragms 318 are disposed while having a first slope that is an acute angle with respect to the traveling direction according to the reaction of the quicklime.

In contrast, as shown, the second diaphragms 319 are in a direction of progression according to the reaction of the quicklime (that is, a direction from the inlet 311 to the outlet 321, or the first surface ( 312) in the direction toward the second surface 313), which is an obtuse second inclination.

In this case, the first slope and the second slope may intersect each other, and may be vertical, for example.

That is, each of the first partition plates 318 and each of the second partition plates 319 may be disposed in a direction that intersects each other or, for example, vertically.

In addition, the size of each of the first diaphragms 318 decreases along the traveling direction, and similarly, the second diaphragms 319 are formed to decrease in size along the traveling direction. .

That is, the quicklime provided to the upper chamber 310 is controlled to flow through the first and second diaphragms 318 and 319 having a relatively large size, and the quicklime located close to the outlet 321, that is, reaction The quicklime produced by this process is controlled to flow through the first and second partitions 318 and 319 having a relatively small size.

This is because the size of the quicklime decreases as the reaction proceeds in the upper chamber 310, the specific surface area and the pore volume increase, so that the flow is guided through the diaphragms of a relatively small size, thereby uniformity of the overall flow. It is to maintain the reaction effect more effectively.

Meanwhile, as shown in FIG. 2, as the first and second diaphragms 318 and 319 are arranged inside the upper chamber 310, the mixture of the quicklime and the digestion reaction solution is shown by an arrow. It can flow along the specified direction, and through this, the uniformity of the digestion reaction can be further improved, and the production efficiency of highly active slaked lime can be further improved.

The lower chamber 320 is connected to the bottom surface 314 of the upper chamber 310, and the boundary surface 315, which is an overlapping portion of the lower chamber 320 and the upper chamber 310, comprises a predetermined dispersion plate ( (Not shown) are interposed and connected to each other.

In this case, the boundary surface 315 prevents reactants such as quicklime and digestion reaction liquid located inside the upper chamber 310 from descending into the lower chamber 320 and from the lower chamber 320. The dispersion plate may be interposed so that saturated steam or dry air can be effectively provided to the upper chamber 310.

The lower chamber 320 forms a second space 324 therein, and may be formed as a whole with a smaller capacity than the upper chamber 310.

The lower chamber 320 may be formed integrally with the upper chamber 310, and may be separately manufactured and combined. However, the upper chamber 310 and the lower chamber 320 are one structure and vibrate simultaneously in the horizontal direction.

As shown in FIG. 4, the lower chamber 320 is connected to a first supply pipe 322 through a side portion and a second supply pipe 323 through a lower portion.

Through the first supply pipe 322, saturated steam is provided and introduced from the outside, and through the second supply pipe 323, dry air is supplied and introduced from the outside.

In this case, in the second space 324 of the lower chamber 320, a first dispersion plate 326 is formed on the lower side, and a second dispersion plate 327 is formed on the upper side of the first dispersion plate 326. Is formed.

The first dispersion plate 326 may be a porous plate extending in a horizontal direction, and accordingly, the first dispersion plate 326 is formed by dividing the second space 324 of the lower chamber 320.

Accordingly, the dry air provided from the outside through the second supply pipe 323 passes through the first dispersion plate 326 and rises, and the first dispersion plate 326 is a porous plate, so the second Dry air provided locally through the supply pipe 323 is uniformly raised upward through the first dispersion plate 326.

A plurality of second dispersion plates 327 may be formed at uniform intervals from each other, and each may be formed in an inverted'V' shape.

The second dispersion plate 327 is positioned above the first supply pipe 322, and the saturated steam flowing through the first supply pipe 322 is directed upward by the second dispersion plate 327. The flow to the flow is obstructed, and accordingly, it can be provided uniformly in the upward direction.

That is, as the second dispersion plate 327 is disposed, the dry air passed through the first dispersion plate 326 and uniformly provided upward is mixed with the saturated steam, and the second dispersion plate Through (327), the flow in the upper direction is uniformly obstructed, so that a uniform flow is performed in the upper direction.

Meanwhile, as described above, the mixed material of dry air and saturated steam uniformly flowing upwards passes through the interface 315 and is provided to the first space 316 of the upper chamber 310, and the interface If 315 is also formed as a dispersion plate, it may be provided more uniformly to the first space 316.

As described above, since dry air and saturated steam are uniformly provided to the upper chamber 310, the digestion reaction of the quicklime and the digestion reaction liquid located in the upper chamber 310 can be further promoted, and thus, high activity It is possible to manufacture slaked lime, and the specific surface area and pore volume of the slaked lime to be prepared are increased.

The driving unit 400 vibrates the mixing chamber 300 in a horizontal direction, that is, in a direction from the first surface 312 to the second surface 313, and the driving unit 410 and the bearing unit 420 Includes.

More specifically, as shown in FIG. 3, the driving unit 410 includes a motor 411 rotating in one direction and a driving shaft 412 eccentrically connected to a rotation shaft of the motor 411.

In this case, the first end 413 of the drive shaft 412 is eccentrically fixed to the rotation shaft of the motor 411, and thus, even if the motor 411 rotates in only one direction, the drive shaft 412 ) Can be driven reciprocally.

Meanwhile, in FIG. 3, in order to describe the driving mechanism of the driving unit 400, it is shown that the driving unit 410 and the bearing unit 420 are directly connected. As shown in FIGS. 1 and 2, the The mixing chamber 300 is connected between the driving part 410 and the bearing part 420.

That is, the second end of the driving part 410 is connected to the first surface 312 of the upper chamber 310, and the bearing part 420 is connected to the bottom surface of the lower chamber 320.

Thus, when the driving shaft 412 reciprocates in the horizontal direction according to the driving of the driving part 410, the upper chamber 310 and the lower chamber 320 connected to the driving shaft 412 are horizontally As a result, reciprocating motion, that is, vibration is performed.

Meanwhile, the bearing part 420 includes a guide 421 and a pair of first and second conveying parts 422 and 423, and the first and second conveying parts 422 and 423 are the lower chamber It is fixed to the bottom surface 325 of (320).

In addition, the first and second conveying parts 422 and 423 slide along the guide 421.

Thus, the lower chamber 320 performs a sliding movement along the guide 421, and as a result, the upper chamber 310 and the lower chamber 320 are driven by the driving unit 410 as a whole. It reciprocates along 421, and this realizes vibration of the upper chamber 310 and the lower chamber 320.

As described above, as the upper chamber 310 vibrates, the quicklime 1, the digestion reaction liquid, the saturated steam and the dry air located on the first space 316 are more effectively mixed, and thus slaked lime Can improve the production efficiency.

In this case, the first and second conveying parts 422 and 423 have been illustrated that they are respectively fixed to both ends of the bottom surface 325 for stable fixing, but the number or fixing positions of the conveying parts may vary. can be changed.

The storage unit 500 is connected to the outlet unit 321 and receives and stores the slaked lime 2 generated in the upper chamber 310.

In this case, a discharge valve 510 is provided at the lower end of the storage unit 500 so that the slaked lime 2 stored in the storage unit 500 may be selectively discharged.

As the saturated steam and dry air are provided in the upper chamber 310, the quicklime reacted with the digestion reaction liquid is manufactured as slaked lime and is floated. The suspended slaked lime, the outlet 321 It is provided to the storage unit 500 through.

On the other hand, in the upper chamber 310, substances that do not float but sink to the bottom are gradually floated upwards according to the execution of an additional digestion reaction, and accordingly, are stored sequentially through the outlet 321 It is to be provided as a part 500.

The filter chamber 600 is connected to an upper portion of the mixing chamber 300 and forms a lower space 601 and an upper space 602.

The filter chamber 600, including a connection unit 650, connects the lower end of the filter chamber 600 and the upper surface 315 of the upper chamber 310 to each other, and the connection unit 650 is open Thus, the upper chamber 310 is opened toward the filter chamber 600.

In this case, the upper surface 315 of the upper chamber 310 may be formed to be inclined obliquely as shown, and accordingly, the connection unit 350 is also formed to be inclined, so that the filter chamber 600 and the The upper surface 315 of the upper chamber 310 may be connected.

A filter unit 610 is provided on the upper space 602 of the filter chamber 600, and an air supply unit 620 and an air injection unit 621 are positioned above the filter unit 610.

The filter unit 610 filters and collects the scattered product scattered upwards by the heat of digestion reaction as a reaction occurs in the upper chamber 310, and the scattered product collected in the filter unit 610, The air provided from the air providing unit 620 and injected through the air injection unit 621 may be provided to the upper chamber 310 located at the lower side.

Accordingly, in the upper chamber 310, the extinguishing reaction is induced again, so that the scattered product may be manufactured as slaked lime.

On the other hand, the fan part 700 is connected to the upper side of the upper space 602 of the filter chamber 600, that is, the upper side of the filter part 610, and sucks the scattered product collected in the filter part 610 Can be removed to the outside.

That is, the scattered product collected in the filter unit 610 may be provided in a downward direction by the air injection unit 621 to induce a extinguishing reaction again to generate slaked lime, and is not removed in the downward direction. The scattered product remaining in the filter unit 610 may be sucked by the fan unit 700 and removed to the outside.

The digestion reaction unit 800 includes a storage unit 810, a stirring unit 820, a heating unit 830, a supply pump 840, a flow meter 850, a connection pipe 860, and an injection nozzle 870. do.

The storage unit 810 stores a fire extinguishing reaction solution in which a fire retardant and an additive are mixed, and the stirring unit 820 uniformly mixes the retarder and the additive, and the heating unit 830 Heat is applied to the digestion reaction liquid to increase the effect.

The digestion reaction liquid stored in the storage unit 810 is supplied through the connection pipe 860 by the supply pump 840, and the flow rate of the digestion reaction liquid supplied through the connection pipe 860 is the It is measured through the flow meter 850.

Thus, the flow rate of the digestion reaction liquid provided through the connection pipe 860 can be kept constant.

Meanwhile, the connection pipe 860 extends from the storage unit 810 to the lower space 601 of the filter chamber 600, and on the connection pipe 860 positioned in the lower space 601 The injection nozzle 870 is formed.

That is, the injection nozzle 870 is positioned above the upper chamber 310 and uniformly sprays the extinguishing reaction liquid toward the upper chamber 310.

In this way, as the spray nozzle 870 uniformly sprays the digestion reaction liquid into the upper chamber 310, the quicklime 1 located on the upper chamber 310 can be uniformly digested.

On the other hand, since the digestion reaction solution contains a digestion reaction retardant, the digestion reaction in the upper chamber 310 can be appropriately delayed, and at the same time, the surface and the interface between the pores of the slaked lime 2 By activation, the slaked lime (2) is prepared with high activity, and the specific surface area and pore volume can be increased.

According to the embodiments of the present invention as described above, since the mixing chamber in which the quicklime is mixed with the digestion reaction liquid is vibrated in the horizontal direction, mixing of the quicklime can be promoted more uniformly and effectively, thereby improving the production efficiency of slaked lime. I can make it.

In addition, in consideration of the increase in the specific surface area and pore volume of slaked lime produced as the reaction between the quicklime and the digestion reaction solution proceeds in the upper chamber, the area decreases in the direction of the outlet and a plurality of installed in an inclined direction. By providing the diaphragms, the digestion reaction of quicklime can be further accelerated, and the uniformity of the overall mixing can be further improved.

In addition, the first and second dispersion plates are formed in the lower chamber, so that the dry air and saturated steam provided to the upper chamber can be more evenly distributed. In particular, the first dispersion plate is a porous dispersion plate to provide dry air. The second dispersion plate may be uniformly distributed, and a plurality of the second dispersion plates are arranged in a'V' shape, so that the material in a state in which saturated steam and dry air are mixed can be uniformly distributed upward.

On the other hand, the extinguishing reaction liquid is uniformly sprayed from the top of the upper chamber through the injection nozzle, so that the quicklime on the upper chamber is sprayed with a uniform extinguishing reaction liquid, so that the interface between the surface of the quicklime and the pores is more By uniform activation, the specific surface area and pore volume of slaked lime to be produced can be increased.

In addition, through the filter unit provided in the filter chamber, it is possible to recover the scattered product, which is a material scattered during the digestion reaction, so that the production efficiency of slaked lime may be further improved.

Although the above has been described with reference to preferred embodiments of the present invention, those skilled in the art will be able to variously modify and change the present invention without departing from the spirit and scope of the present invention described in the following claims. You will understand that you can.

10: slaked lime manufacturing apparatus 100: providing unit
200: quantitative supply device 300: mixing chamber
310: upper chamber 317: diaphragm
320: lower chamber 326, 327: dispersion plate
400: drive unit 410: drive unit
420: bearing part 500: storage part
600: filter chamber 610: filter unit
700: fan part 800: fire extinguishing reaction unit
860: connection line

Claims (13)

A mixing chamber that receives quicklime evenly and fires it uniformly;
A filter chamber connected to an upper portion of the mixing chamber;
A fire extinguishing reaction unit for injecting a fire extinguishing reaction liquid into the mixing chamber through the filter chamber; And
It includes a storage unit for storing the slaked lime generated in the mixing chamber,
The mixing chamber,
An upper chamber vibrating in a horizontal direction to mix the digestion reaction liquid and the quicklime; And
And a lower chamber for supplying saturated steam and dry air to the upper chamber from a lower portion of the upper chamber. The method of claim 1,
A highly active slaked lime manufacturing apparatus further comprising a driving unit connected to the upper chamber and vibrating the upper chamber in a horizontal direction. The method of claim 2, wherein the driving unit,
A driving unit connected to the upper chamber to vibrate the upper chamber in a horizontal direction; And
And a bearing part connected to the lower chamber to slide the lower chamber in a horizontal direction. The method of claim 3, wherein the bearing part,
A guide extending parallel to the bottom surface of the lower chamber; And
A highly active slaked lime manufacturing apparatus comprising at least one conveying part fixed to the bottom of the lower chamber and moved in a horizontal direction along the guide. The method of claim 1, wherein the upper chamber,
A diaphragm disposed in a first space of the upper chamber and including a plurality of first diaphragms disposed with a first inclination, and a plurality of second diaphragms disposed with a second inclination different from the first inclination Highly active slaked lime production apparatus comprising a part. The method of claim 5,
The first and second diaphragms, the size of each of the slaked lime production apparatus, characterized in that the size decreases from the inlet of the quicklime toward the outlet of the slaked lime. The method of claim 1, wherein the lower chamber,
A first supply pipe through which saturated steam is introduced from the outside; And
Highly active slaked lime manufacturing apparatus comprising a second supply pipe through which dry air is introduced from the outside. The method of claim 7, wherein the lower chamber,
A first dispersion plate uniformly dispersing the dry air introduced from the second supply pipe in an upward direction; And
And a second dispersion plate positioned above the first dispersion plate and uniformly dispersing the saturated steam flowing in the upper direction from the first supply pipe. The method of claim 8,
The first dispersion plate is a porous plate disposed in a horizontal direction,
The second dispersion plate has a'V'-shaped cross-section and a plurality of highly active slaked lime manufacturing apparatus, characterized in that the spaced apart from each other. The method of claim 1, wherein the digestion reaction unit,
A storage unit for storing the digestion reaction liquid;
A connection line extending from the storage unit to a lower space of the filter chamber to move the digestion reaction liquid; And
And a spray nozzle provided in the connection line located in the lower space of the filter chamber to inject the digestion reaction liquid into the upper chamber. The method of claim 10, wherein the digestion reaction unit,
A stirring unit for mixing the digestion reaction solution in which the digestion reaction retardant and the additive are mixed; And
Highly active slaked lime production apparatus, characterized in that it further comprises a heating unit for heating the digestion reaction liquid. The method of claim 1, wherein the filter chamber,
A filter unit provided in the upper space to collect fugitive products generated in the formation of the slaked lime; And
Highly active slaked lime production apparatus, characterized in that it comprises an air injection unit for injecting air to the filter unit above the filter unit. The method of claim 12,
A highly active slaked lime production apparatus further comprising a fan connected to an upper portion of the filter chamber to suck the scattered product collected in the filter unit.

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