JPH06296979A - Slaked lime aqueous solution manufacturing equipment - Google Patents

Abstract

(57) [Summary] [Objective] An object of the present invention is to provide an apparatus for producing an aqueous slaked lime solution, which promotes the precipitation and dissolution of slaked lime, and can produce an aqueous slaked lime solution with high efficiency. [Structure] In a slaked lime dissolution apparatus having a water supply pipe 6 connected to a lower portion of a cylindrical dissolution tank 1 and a slaked lime aqueous solution extraction pipe 8 connected to an upper portion thereof, and a stirring blade 10 provided at an inner bottom portion of the dissolution tank 1, a water surface of the dissolution tank 1 Partition wall 3 that hangs from the
Accordingly, the inside of the melting tank 1 has a fluidized bed height suppressing device 1
The sub-chamber 5 is provided with a forced contact means 18 for partitioning the slaked lime powder and water supplied on the water surface in the sub-chamber 5 into a main chamber 4 and a sub-chamber 5 for supplying slaked lime. Has been.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing an aqueous slaked lime solution used for improving tap water.

[0002]

2. Description of the Related Art Conventionally, caustic soda injection method, soda ash injection method, slaked lime injection method and the like have been known as measures for preventing red water from tap water, but recently, the slaked lime injection method has been drawing attention. It is said that slaked lime not only raises the pH of water, but also that calcium as a main component is good for health, and that technology has been developed to inject slaked lime not as a powder that easily scatters but as an aqueous solution. Since then, it has been adopted by many water treatment plants.

As an apparatus for continuously producing a slaked lime aqueous solution, for example, an apparatus described in Japanese Patent Publication No. 63-2890 is known. In this known device, a water supply pipe and an insoluble matter discharge port are provided at the bottom of a cylindrical or prismatic dissolution tank, and a horizontally rotating stirring blade is provided immediately above the water supply pipe, and a slaked lime aqueous solution is provided above the tank. It is configured to have an extraction pipe. In this known apparatus, a predetermined amount of slaked lime is supplied from a container bag to the water layer in the dissolution layer by a suction fan or the like, and the production operation of the slaked lime aqueous solution is started after waiting for its natural sedimentation. When the concentration of slaked lime aqueous solution produced decreases,
The operation is stopped once, and slaked lime is newly supplied.

When the operation is stopped, slaked lime is supplied, and the slaked lime powder is restarted after waiting for the natural settling, the slaked lime powder has an apparent specific gravity of about 0.6, and it takes a long time to settle. It has been proposed to prepare two devices and perform a switching operation (Japanese Patent Publication No. 63-35574).

[0005]

As described above, in the above-mentioned known device, not only it takes a long time to supply new slaked lime, but also the rising speed of water in the upper part of the dissolution tank that determines the flow rate of the obtained slaked lime aqueous solution. 0.2 mm at most
/ Sec is the limit. That is, in the above-mentioned known device having no special means other than the agitating blade, if the rising speed of the water is set to the above value or more, the undissolved slaked lime particles are mixed in the slaked lime aqueous solution. Therefore, as for the amount of the aqueous solution produced, the flow rate obtained at the limit value of the ascending speed of 0.2 mm / sec becomes the maximum value.

According to the present invention, by smoothly and accelerating the settling / dissolution of slaked lime, the time required for supplying slaked lime can be shortened, continuous supply can be carried out if necessary, and the flow of undissolved slaked lime particles in the dissolution tank can be improved. An object of the present invention is to provide a slaked lime aqueous solution manufacturing apparatus capable of suppressing the layer height and increasing the rising rate (supply rate) of water.

[0007]

According to the present invention, the above object is to connect a water supply pipe to a lower portion of a cylindrical dissolution tank and a slaked lime aqueous solution extraction pipe to an upper portion thereof, and to provide a stirring blade at a bottom portion inside the dissolution tank. In the slaked lime dissolution apparatus, by the partition wall hanging from the water surface of the dissolution tank to an intermediate position, the inside of the dissolution tank is divided into a main chamber equipped with a fluidized bed height suppressing device and a sub-chamber for supplying slaked lime. This is achieved by providing the sub chamber with a means for forcibly contacting the slaked lime powder and water supplied on the water surface in the chamber.

[0008]

In the device of the present invention, slaked lime is charged / supplied on the water surface in the sub chamber. The sub-chamber is provided with a forced contact means, and the slaked lime is forcibly brought into contact with water to promptly settle into a slurry. Sedimentation is further promoted when the forced contact means is adapted to produce a downward flow.

The slaked lime that has sufficiently contacted with water in the sub chamber settles and deposits as a slurry on the bottom of the dissolution tank. At the bottom of the dissolution tank, the main chamber and the sub chamber communicate with each other, in which the stirring blades are rotating and water is supplied from the water supply pipe. Therefore, the slurry is stirred to form a fluidized bed, and an aqueous slaked lime solution produced by sufficiently dissolving it in water rises in the main chamber with some undissolved slaked lime particles in the fluidized bed.

When the aqueous solution rises, it reaches the fluidized bed height suppressing device, where the undissolved slaked lime particles in the aqueous solution are prevented from further increasing, and only the aqueous solution rises. Thus, only the slaked lime aqueous solution containing almost no undissolved slaked lime is taken out from the slaked lime aqueous solution extraction pipe.

[0011]

Embodiments of the present invention will be described below with reference to the accompanying drawings.

<First Embodiment> FIG. 1 is a schematic block diagram showing a first embodiment of the present invention.

In the figure, reference numeral 1 is a cylindrical melting tank, and the lower part thereof has a taper cross section with a diameter decreasing downward. The melting tank 1 is divided into a main chamber 4 and a sub chamber 5 by a partition wall 3 attached to the lid member 2 so as to hang down to an intermediate position. A water supply pipe 6 for supplying water into the dissolution tank 1 from the outside and a discharge pipe 7 for discharging insoluble matter to the outside at an appropriate time are connected to the bottom of the dissolution tank 1 through valves. ing. A slaked lime aqueous solution extraction pipe 8 is connected to the upper portion of the dissolution tank 1.

The main chamber 4 of the melting tank 1 is provided with a stirring device 11 having a horizontal stirring blade 10 which is rotated by a drive shaft 9 at the bottom of the main chamber 4. Further, a fluidized bed height suppressing device 12 is provided in the main chamber 4 in a range in the height direction of the partition wall 3 that partitions the main chamber 4 and the sub chamber 5.

The fluidized bed height suppressing device 12 preferably comprises two or more inclined plates arranged in parallel at substantially equal intervals as shown in the figure. It is sufficient that the inclined plates are inclined in the same direction, but more preferably, as shown in the drawing, the inclined plates 12A, 12 of the two groups are inclined in opposite directions.
It consists of B. The interval between the parallel inclined plates is 5 to 70 m
m rank is good.

The lid member 2 of the sub chamber 5 is provided with a slaked lime charging hopper 14 via a valve 15, and a spraying device 16 for preventing scattering of the slaked lime charged on the water surface.
Is also provided.

The sub chamber 5 is provided with a bottomless cylindrical body 17 extending downward, and a rotary blade 18 as a forced contact means is provided therein so as to stir water in the vicinity of the water surface. The rotor 18 may simply agitate water, but is preferably adapted to produce a downward flow 19 with agitation.

In the apparatus of this embodiment having such a structure, the slaked lime aqueous solution is manufactured in the following manner.

A predetermined amount of slaked lime is supplied from the hopper 14 to the sub chamber 5
Dropped on the surface of. At this time, the spray 16 prevents the scattered slaked lime particles from escaping to the outside air. Immediately after being dropped, the slaked lime that does not dissolve and floats on the water surface is agitated by the rotary blades 18 and is forcibly brought into contact with water to form a slurry, which promotes sedimentation. The above settling is further promoted if the rotor blades 18 generate the downward flow 19.

The settled slurry is deposited at the bottom of the dissolution tank 1, where it is stirred by the stirring blades 10 to form a fluidized bed, and further, contacted with the water supplied from the water supply pipe 6. , Dissolution progresses and becomes a slaked lime aqueous solution.

The slaked lime aqueous solution rises in the main chamber 4. At this time, the rising slaked lime aqueous solution contains a small amount of undissolved slaked lime particles in the fluidized bed, which also rises.

The slaked lime aqueous solution containing the undissolved slaked lime particles is used between the inclined plates 12A and 12A and between the inclined plates 12B and 12B.
The slaked lime particles having a higher specific gravity with respect to the slaked lime aqueous solution are suppressed by the sloping plate on the upper side of the above channel and are lowered, and only the slaked lime aqueous solution continues to rise.

Thus, in the vicinity of the water surface of the main chamber 4, only the slaked lime aqueous solution containing almost no undissolved slaked lime particles is taken out and taken out from the take-out pipe 8.

<Second Embodiment> Next, a second embodiment will be described with reference to FIG. In the figure, the same parts as those in FIG. 1 in the above-described first embodiment are designated by the same reference numerals and the description thereof will be omitted.

In the apparatus of this embodiment, the fluidized bed height suppressing device 21 provided in the main chamber 4 is composed of a group of inclined plates which are inclined in one direction. As a matter of course, in this embodiment as well, the inclined plates of two groups which are opposite to each other as in the first embodiment may be used. The same applies to the other embodiments described below.

In the present embodiment, the rotary blade 18 is adopted as the forced contact means, but in addition to this, the lower part of the melting tank 1 and the upper part of the sub chamber 5 are connected by a connecting pipe 23 having a pump 22. The slurry in the lower part of the dissolution tank 1 is supplied to the upper part of the sub chamber 5 to further accelerate the dissolution of the slurry, and the slaked lime supplied from the hopper 14 together with the slurry causes the sedimentation of the slaked lime. Speed up.

The slurry is supplied to the upper part of the sub chamber 5 by
Connection pipe 23 having a pump 22A as shown by the chain double-dashed line
By connecting A to the upper part of the main chamber 4, the supply of the slaked lime aqueous solution can be replaced. Also in this case, the settling of slaked lime can be promoted.

In the present embodiment, if a downward swirl flow is generated in the sub chamber 5 as shown in FIG. 3 instead of the rotary blade 18, the settling of slaked lime can be further accelerated, which is effective. is there. For that purpose, for example, the above-mentioned connecting pipe 2
3; 23A is connected to the sub chamber 5 in a tangential direction as viewed from above and slightly downward, so that the above swirl flow is obtained by the slurry from the connecting pipe 23 or the slaked lime aqueous solution from the connecting pipe 23A.

Further, the downward flow in the sub chamber 5 can be generated by providing an attack angle to the rotary blade in the first embodiment, but as shown in FIG. 4, the drive shaft of the rotary blade 18 is extended downward. However, another rotary blade 24 may be provided there, and an attack angle may be provided to the other rotary blade 24. That is, in this case, the upper rotor blade 18 performs only stirring, and the other lower rotor blades 24 serve to generate further stirring and downward flow. In this case, it can be implemented with or without a connecting pipe as shown in FIG.

<Third Embodiment> The present embodiment shown in FIG. 5 is characterized in that the forced contact means causes not only a downward flow but also an upward flow in the sub-chamber 5 to perform vertical circulation. .

Inside the bottomless cylinder 17 in the sub chamber 5 of this embodiment, a draft tube 31 extending downward from an intermediate portion of the bottomless cylinder 17 is provided with a radius relative to the bottomless cylinder 17. They are provided substantially concentrically with a predetermined interval in the direction. The rotary blades 18 and 24 as the forced contact means are arranged in the draft tube 31.

Therefore, in this embodiment, a downward flow is generated in the draft tube 31, and above the draft tube 31, the draft tube 31 and the bottomless cylinder 17 are provided.
The water between the draft tubes 31 is drawn into the draft tube 31, and an upflow occurs outside the draft tube 31. As a result, upper and lower circulating flows are generated in the sub-chamber 5, and the stirring and dissolution of slaked lime are promoted.

In the present embodiment, the forced contact means is replaced with the rotary blades 18 and 24, and as shown in FIG.
Can be used. In that case, the jet flow of the ejector 32 is formed by the slaked lime aqueous solution which is taken from the upper part of the main chamber 4, is pumped by the pump 33, and is supplied to the ejector by the connecting pipe 34. Also in this case, the draft tube 31
Circulating flow occurs both inside and outside.

[0034]

INDUSTRIAL APPLICABILITY As described above, the present invention has a fluidized bed height suppressing device, and when the slaked lime aqueous solution is produced at a high rising rate with high efficiency, slaked lime is forcibly forced in a subchamber with a limited volume. Since it is brought into contact with water, a slurry can be produced very effectively and the production of the slaked lime aqueous solution can be followed. Moreover, since the sub-chamber is partitioned from the main chamber at least in the water surface area, the slaked lime that is introduced into the sub-chamber does not mix in the slaked lime aqueous solution taken from the main chamber. There is no risk of slaked lime depositing, and it becomes possible to continuously produce an aqueous slaked lime solution, thus improving productivity.

[Brief description of drawings]

FIG. 1 is a schematic configuration diagram of a first embodiment device of the present invention.

FIG. 2 is a schematic configuration diagram of a second embodiment device.

FIG. 3 is a schematic configuration diagram showing a modification of the second embodiment device.

FIG. 4 is a schematic configuration diagram showing a further modified example of the second embodiment device.

FIG. 5 is a schematic configuration diagram of a third embodiment device.

FIG. 6 is a schematic configuration diagram showing a modification of the third embodiment device.

[Explanation of symbols]

 DESCRIPTION OF SYMBOLS 1 Dissolution tank 3 Partition wall 4 Main chamber 5 Sub-chamber 6 Water supply pipe 8 Slaked lime aqueous solution extraction pipe 10 Stirring blade 12 Fluidized bed height suppressing device 18 Forced contact means (rotary blade) 22; 22A Pump device 23; 23A Connection pipe 24 Forced contact Means (rotary blade) 31 Draft tube 32 Ejector

 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Akihiro Ito 4-4 Onahama Minatogaoka, Iwaki, Fukushima Prefecture

Claims (8)

[Claims] 1. In a slaked lime dissolution apparatus having a tubular dissolution tank to which a water supply pipe is connected to a lower portion and a slaked lime aqueous solution extraction pipe to an upper portion, respectively, and which has a stirring blade at an inner bottom portion of the dissolution tank, from a water surface of the dissolution tank to an intermediate position. The slaked partition wall divides the inside of the dissolution tank into a main chamber equipped with a fluidized bed height suppressing device and a sub chamber for supplying slaked lime, and the slaked lime powder and water supplied on the water surface in the sub chamber. A device for producing a slaked lime aqueous solution, characterized in that a means for forcibly contacting with is provided in the sub chamber. 2. The apparatus for producing a slaked lime aqueous solution according to claim 1, wherein the forced contact means is a rotary blade provided below the water surface and near the water surface. 3. The apparatus for producing a slaked lime aqueous solution according to claim 2, wherein the rotary blade is adapted to generate a downward flow of water. 4. The slaked lime aqueous solution production according to claim 1, wherein the lower part of the dissolution tank or the upper part of the main chamber and the upper part of the sub chamber are connected via a pump device for supplying water to the sub chamber. apparatus. 5. The apparatus for producing a slaked lime aqueous solution according to claim 1, wherein the forced contact means is a means for generating a swirling flow in the sub chamber. 6. A connecting pipe connecting the lower part of the dissolution tank or the upper part of the main chamber to the upper part of the sub-chamber and opening the sub-chamber with a tangential component in a substantially horizontal plane.
The slaked lime aqueous solution manufacturing apparatus according to claim 5, further comprising a pump device provided in the connection pipe to supply water to the sub chamber. 7. The forced contact means has a downwardly extending draft tube for guiding the downward flow, and the draft tube is kept at a predetermined distance from the side wall of the sub chamber. Alternatively, the slaked lime aqueous solution manufacturing apparatus according to claim 2. 8. The forced contact means includes a draft tube extending downward with a predetermined distance from a side wall of the sub chamber, an ejector arranged in the draft tube, and a connection pipe connecting the upper portion of the main chamber and the ejector. The slaked lime aqueous solution manufacturing apparatus according to claim 1, further comprising: a pump device provided in the connecting pipe for supplying water to the sub chamber.