JP2005095726A - Reacting/crystallizing method and apparatus therefor - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a crystallizing/dephosphorizing method and apparatus therefor, by each of which the amount of agglomerated calcium phosphate to be generated can be reduced without altering the flow rate ratio of circulation water/the water to be treated. <P>SOLUTION: When the water to be treated is introduced into a fluidized bed 14 from a pressure chamber 19 for the water to be treated through a jet nozzle 55 and a distributor 12 and circulation water is also introduced into the fluidized bed 14 through a pressure chamber 20 for the circulation water and the distributor 12, both of the water to be treated and the circulation water are mixed first with each other in a seed crystal of a fluidized state. Though the water to be treated has high phosphorus concentration and the circulation water has high Ca concentration and pH, the phosphorus in the water to be treated is crystallized on the surface of the seed crystal since they are mixed in the presence of the seed crystal. As a result, the amount of the agglomerated calcium phosphate to be generated can be reduced without altering the flow rate ratio of the circulation water/the water to be treated. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

  The present invention relates to a reaction crystallization treatment method and apparatus, and more particularly to a reaction crystallization treatment technique such as crystallization dephosphorization for reducing the amount of aggregates of target components contained in water to be treated.

  For example, as a dephosphorization apparatus for treated water containing phosphorus such as sewage treated water, sludge is not generated as in the case of the coagulation method, and the final product is recovered as a phosphorus resource and can be reused. A possible crystallization dephosphorization method (reaction crystallization treatment method) has attracted attention. As one type, a fluidized bed type crystallization dephosphorization method has been developed. In the fluidized bed type, water to be treated containing phosphorus is passed from a pressure chamber provided in the lower part of the reaction tank through a distributor formed on the upper wall of the pressure chamber toward a fluidized bed provided immediately above the distributor. In the fluidized bed, the seed crystal containing calcium phosphate constituting a part of the fluidized bed is brought into contact with phosphorus in the water to be treated so that phosphorus in the water to be treated is converted into hydroxyapatite. Crystallized and removed from the surface to obtain treated water.

  In this fluidized bed type, it is necessary to always maintain the seed crystal in a fluidized state at a predetermined upward flow rate in the fluidized bed. Therefore, although a pressure chamber is provided in the reaction tank, a sufficient water flow rate through the distributor cannot be obtained only by supplying water to be treated to the pressure chamber. Therefore, in recent years, a method has been developed in which not only the water to be treated but also a part of the treated water is introduced into the pressure chamber as circulating water as in the crystallization dephosphorization method described in Patent Document 1, for example. This method employs a method in which treated water and circulating water are mixed in advance and the mixed water is supplied to the pressure chamber.

JP 2002-301480 A (first page, FIG. 1)

  However, in the method of supplying a mixed liquid of treated water and circulating water to the pressure chamber, the circulating water and treated water are mixed upstream from the fluidized bed. The water to be treated has a high concentration of phosphate ion phosphorus (hereinafter referred to as phosphorus), and the circulating water has a calcium ion concentration and a pH increased in order to perform a crystallization operation. Therefore, if the phosphorus concentration at the time of mixing exceeds the phosphorus solubility determined by the three elements (phosphorus concentration, pH, calcium ion concentration), phosphorus is generated in the mixed solution as fine crystals of calcium phosphate (hereinafter, aggregates). It is easy to be done and is not deposited on the surface of the seed crystal but is discharged out of the system. Therefore, phosphorus is not recovered by the crystallization method.

  In order to avoid the generation of aggregates, conventionally, a method is known in which the flow rate ratio of circulating water / treated water is increased and the phosphorus concentration is reduced to less than the excessive solubility. However, in this method, the circulating water circulation pump becomes large and power consumption may increase. Furthermore, when the required flow state is exceeded, the following inconvenience may occur. That is, (1) Calcium phosphate crystallized on the surface of the seed crystal is worn or peeled off. (2) Inconveniences such as an increase in the flow height of the fluidized bed and an increase in the height of the reaction tank are likely to occur.

  Therefore, as a result of earnest research, the inventor introduced the treated water and the circulating water individually into the fluidized bed without mixing the treated water and the circulating water upstream of the fluidized bed. If the treated water and circulating water are mixed for the first time just before being introduced into the fluidized bed, and the treated water and circulating water are mixed for the first time in the presence of seed crystals in a fluid state, most phosphorus is The present invention was completed by discovering that it was crystallized on the surface of the seed crystal as hydroxyapatite and hardly formed as an aggregate of calcium phosphate.

  The present invention provides a reactive crystallization treatment method and apparatus capable of reducing the amount of aggregates of target components contained in the water to be treated without changing the ratio of the circulating water flow rate / the water to be treated flow rate. That is the purpose.

  According to the first aspect of the present invention, the water to be treated is introduced into the fluidized bed in which the seed crystal exists, and the water to be treated and the seed crystal are brought into contact with each other in the fluidized bed, whereby the surface of the seed crystal is treated. In the reaction crystallization treatment method, a part of the treated water is obtained as circulated water and introduced into the fluidized bed, and the treated water and the circulated water are mixed together. It is a reaction crystallization treatment method in which contact / mixing is performed for the first time just before introduction into the fluidized bed, or individual introduction into the fluidized bed.

  According to the first aspect of the present invention, the treated water and the circulating water are first contacted and mixed immediately before being introduced into the fluidized bed, or individually introduced into the fluidized bed. Is over the solubility of the target component, most of the target component is crystallized on the surface of the seed crystal as a compound. As a result, even if the phosphorus concentration in the water to be treated fluctuates, the amount of calcium phosphate agglomerates generated can be reduced without changing the ratio of the circulating water flow rate / treated water flow rate.

The treated water and the circulating water may be contacted and mixed for the first time immediately before being introduced into the fluidized bed. Moreover, you may introduce into a fluidized bed separately.
The kind of to-be-processed water is not limited. For example, secondary treated water for sewage treatment, return water in sewage sludge treatment process, industrial wastewater, etc. can be employed.
Moreover, the kind of target component is not limited. For example, phosphate phosphorus, fluorine, boron, ammonia, and other heavy metals can be employed.

According to a second aspect of the present invention, a chemical solution is added to the fluidized bed, and the chemical solution is added to the fluidized bed immediately before or after the treated water and circulating water are introduced into the fluidized bed. It is the reaction crystallization processing method of Claim 1 contacted and mixed with water and circulating water.
The chemical solution may be brought into contact with and mixed with the water to be treated and the circulating water just before the water to be treated and the circulating water are introduced into the fluidized bed. Alternatively, it may be in a fluidized bed.
The kind of chemical | medical solution is not limited. For example, an alkaline aqueous solution such as slaked lime (Ca (OH) ₂ ), calcium chloride, sodium hydroxide, magnesium hydroxide can be employed. The amount of the chemical solution added is not limited.

  The invention according to claim 3 is formed above the pressure chamber of the reaction tank through a plurality of outlets formed in the upper wall of the pressure chamber from the pressure chamber formed in the lower part of the reaction tank. Treated water containing phosphorus is introduced into a fluidized bed where crystals are present, and phosphorus in the treated water is brought into contact with the seed crystals in the fluidized bed to crystallize phosphorus in the treated water on the surface of the seed crystals. In the reaction crystallization treatment method, the treated water is introduced into the pressure chamber by introducing into the fluidized bed from the pressure chamber through each outlet as part of the treated water as circulating water. The treated water pressure chamber and the circulating water pressure chamber into which the circulating water is introduced, and the treated water is introduced into the fluidized bed from the treated water pressure chamber through the outlet. The circulating water passes through a different outlet from the outlet for the treated water. From the circulation water pressure chamber is reactive crystallization process method of introducing into the fluidized bed.

  According to this invention, the water to be treated is introduced from the pressure chamber for water to be treated into the fluidized bed through the outlet, and the circulating water is introduced from the pressure chamber for circulating water into the fluidized bed through the other outlet. That is, the water to be treated and the circulating water flow into the fluidized bed through separate flow paths. And circulating water and to-be-processed water are mixed only in the seed crystal of a fluid state. The water to be treated has a high phosphorus concentration, and the circulating water has a high calcium ion concentration and pH. However, since the mixing is performed in the presence of the seed crystals, most of the phosphorus is crystallized on the surface of the seed crystals as hydroxyapatite even if the phosphorus concentration at the time of mixing is higher than the excessive solubility of phosphorus. As a result, even if the phosphorus concentration in the water to be treated fluctuates, the amount of calcium phosphate agglomerates generated can be reduced without changing the ratio of the circulating water flow rate / treated water flow rate.

The kind of to-be-processed water containing phosphorus is not limited. For example, sewage treated water, return water in the sewage sludge treatment process, industrial wastewater, and the like can be mentioned. The arrangement of the pressure chamber for water to be treated and the pressure chamber for circulating water after division is not limited. For example, the pressure chambers may be arranged vertically (in the vertical direction) or left and right (in the horizontal direction). In addition, you may arrange | position both chambers in a center part and an outer peripheral part.
The number of air outlets formed may be one or two or more. As a blower outlet, the distributor which distributes the to-be-processed water of the pressurized chamber for to-be-processed water and the circulating water of the pressurized chamber for circulating water to a some flow, for example is employable.
The outlet is preferably formed separately in the pressure chamber for water to be treated and the pressure chamber for circulating water. However, since the time for the treated water and the circulating water to pass through the outlet is short, the same outlet may be used.

A calcium compound or an alkaline agent can be introduced into the water to be treated in the reaction tank. Moreover, you may throw in both a calcium compound and an alkaline agent. The calcium compound and the alkali agent react with phosphorus in the water to be treated to produce a hardly soluble calcium salt. For example, alkaline aqueous solutions, such as slaked lime, calcium chloride, sodium hydroxide, magnesium hydroxide, are mentioned.
As the seed crystal, for example, a calcium silicate compound, calcium carbonate, phosphate rock, bone charcoal, or calcium phosphate can be employed.
The grain size of the seed crystal is not limited. For example, it is 0.15-0.3 mm.

The crystallization dephosphorization method is a method for growing a hydroxyapatite crystal by a crystallization reaction on the surface of a seed crystal. Hydroxyapatite has several molecular formulas that differ in the number of moles of Ca, OH, and PO ₄ . Typically, it is represented by (Ca ₅ (OH) (PO ₄ ) ₃ ). The crystallization reaction is shown in the following formula.
5Ca ²⁺ + OH ⁻ + 3PO ₄ → Ca ₅ (OH) (PO ₄ ) ₃
In the crystallization reaction, phosphorus in the water to be treated is precipitated as hardly soluble hydroxyapatite. The solubility product of hydroxyapatite is very small (Ks = 10-55.9), and treated water with a low phosphorus concentration can be obtained. The pH of the treated water varies depending on the type and concentration of target treated water and the target phosphorous concentration of treated water, but is generally pH 8 to 10.

  The invention according to claim 4 is a reaction tank in which water to be treated containing phosphorus is stored, a pressure chamber formed in a lower part of the reaction tank, and a plurality of outlets formed in an upper wall; A fluidized bed formed above the pressure chamber in the reaction tank and containing seed crystals, treated water supply means for supplying treated water to the pressure chambers, phosphorus and seed crystals contained in the treated water A part of the treated water obtained by removing phosphorus by crystallizing the surface of the seed water on the surface of the seed crystal, and supplying the pressure chamber as circulating water through each outlet In the reaction crystallization treatment apparatus including water supply means, the pressure chamber is divided into a pressure chamber for water to be treated to which the water to be treated is supplied and a pressure chamber for circulating water to which the circulating water is supplied. The outlet is configured to connect the pressure chamber for water to be treated and the fluidized bed, and the circulating water. A blowout opening communicating with the pressure chamber and the fluidized bed, and the treated water supply means includes a treated water supply flow path for supplying the treated water to the pressure chamber for treated water, and the circulation The water supply means is a reaction crystallization treatment apparatus having a circulating water supply channel for supplying the circulating water to the circulating water pressure chamber.

According to this invention, the water to be treated is introduced from the pressure chamber for water to be treated into the fluidized bed, and the circulating water is introduced from the pressure chamber for circulating water to the fluidized bed. Thereby, circulating water and to-be-processed water are mixed only in the seed crystal of a fluid state. Therefore, even if the phosphorus concentration at the time of mixing is higher than the excessive solubility of phosphorus, most phosphorus is crystallized on the surface of the seed crystal. As a result, even if the phosphorus concentration in the water to be treated fluctuates, the amount of calcium phosphate agglomerates generated can be reduced without changing the ratio of the circulating water flow rate / treated water flow rate.
The to-be-treated water supply means and the circulating water supply means can employ various pumps as drive sources.

According to a fifth aspect of the present invention, the downstream end of the treated water supply flow path is communicated with a treated water pressure chamber from a part of the peripheral wall of the reaction tank, and the circulating water supply flow path 5. The reaction crystallization treatment apparatus according to claim 4, wherein the downstream end is communicated with the circulating water pressure chamber through the reaction vessel.
According to this invention, the downstream end of the treated water supply channel is communicated with the treated water pressure chamber from a part of the peripheral wall of the reaction tank, and the downstream end of the circulating water supply channel is reacted. It communicates with the pressure chamber for circulating water through the tank. Thereby, piping does not exist under the reaction tank, and the construction and maintenance of the reaction tank are facilitated.

  According to the reaction crystallization treatment method according to claim 1 and claim 3 and the reaction crystallization treatment apparatus according to claim 4, the water to be treated and the circulating water are contacted for the first time just before being introduced into the fluidized bed. Because they are mixed or introduced individually into the fluidized bed, the amount of aggregates of the target component generated without changing the ratio of circulating water flow / treated water flow rate even if the phosphorus concentration in the treated water fluctuates Can be reduced.

  In particular, according to the reaction crystallization treatment apparatus according to claim 5, the treated water supply flow path communicates with a pressure chamber for treated water from a part of the peripheral wall of the reaction tank, and the circulating water supply flow path is the reaction tank. Since it communicated with the pressure chamber for circulating water through the inside, there is no piping below the reaction tank, and the construction and maintenance of the reaction tank becomes easy.

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

  In FIG. 1, 10 is a crystallization dephosphorization apparatus (reaction crystallization treatment apparatus) according to Embodiment 1 of the present invention, and this crystallization dephosphorization apparatus 10 is a reaction tank in which water to be treated containing phosphorus is stored. 11, a pressure chamber 13 formed in the lower part of the reaction tank 11, and a number of distributors (outlets) 12... Disposed on the upper wall 51 at a predetermined pitch, and above the pressure chamber 13 in the reaction tank 11. The formed fluidized bed 14 in which seed crystals are present, the water to be treated supplying means 15 for supplying the water to be treated to the pressure chamber 13, and the phosphorus and seed crystals contained in the water to be treated are brought into contact with each other. Circulating water supply means 16 for supplying a part of the treated water obtained by crystallizing and removing phosphorus as hydroxyapatite on the surface of the seed crystal as circulating water, and slaked lime for storing a slaked lime aqueous solution Aqueous solution supply tank 17 and slaked lime solution Slaked lime aqueous solution in the tank 17 and a slaked lime aqueous solution supplying means 18 for supplying to the pressure chamber 13.

The reaction tank 11 is a circular tank in plan view with a lid. The pressure chamber 13 formed in the lower part of the reaction tank 11 includes a lower pressure chamber for water to be treated 19 to which water to be treated is supplied and a pressure chamber for circulating water to the upper side to which circulating water is supplied. It is partitioned by a partition plate 52.
An annular drainage channel 11a through which treated water after dephosphorization is discharged is formed on the outer periphery of the upper edge of the reaction tank 11, and a drainage pipe 11b is communicated with a part of the drainage channel 11a. Further, in the upper part of the reaction tank 11, an annular SS discharge capillary 11c that discharges SS is disposed in a region where treated water is stored through a number of nozzle holes formed at a constant pitch in the circumferential direction. ing. Part of the SS discharge thin tube 11c and the middle portion of the drain tube 11b are communicated with each other through a short communication tube 11d. An open / close valve 11e is provided in the middle of the communication pipe 11d. When the on-off valve 11e is opened and the treated water is allowed to flow through the drain pipe 11b, the inside of the SS discharge narrow pipe 11c becomes negative pressure via the communication pipe 11d. Due to this negative pressure, the SS in the treated water is discharged to the outside through the nozzle hole of the SS discharge thin tube 11c, through the SS discharge thin tube 11c, the communication tube 11d, and the drain tube 11b.

At the center of the reaction tank 11, a long inner cylinder (circulation water supply flow path) 21 whose lower end communicates with the center of the circulating water pressure chamber 20 has its axis aligned with the axis of the reaction tank 11. Standing up. The upper end of the inner cylinder 21 is disposed above the fluidized bed 14 of the reaction tank 11 and in a region where treated water is stored.
The upper end portion of the inner cylinder 21 is integrally formed with an enlarged diameter portion 21a that gradually increases in diameter toward the opening at the upper end. Four large guide blades 21b are erected on the enlarged diameter portion 21a at intervals of 90 degrees in the pipe circumferential direction. Each guide blade 21 b extends to the vicinity of the lid of the reaction tank 11.

  An electric motor 41 for the pump device 40 that draws treated water into the inner cylinder 21 is erected on the central portion of the lid of the reaction tank 11. The output shaft 42 of the electric motor 41 is long, and the front end portion (lower end portion) of the output shaft 42 to which the small rotating blade 22 is fixed is near the base portion of the enlarged diameter portion 21 a along the axis of the reaction tank 11. Is arranged. When the output shaft 42 is rotated by the electric motor 41, the rotary blade 22 is rotated, and a downward water flow is generated in the inner cylinder 21. Thereby, the treated water of the upper part of the reaction tank 11 flows into the circulating water pressure chamber 20 from the enlarged diameter portion 21a through the inner cylinder 21. The inner cylinder 21 is not necessarily arranged on the axis of the reaction tank 11. The inner cylinder 21 and the pump device 40 constitute the circulating water supply means 16.

  The treated water supply means 15 has a treated water storage tank 23. The bottom plate of the treated water storage tank 23 and a part of the peripheral side portion of the treated water pressure chamber 19 are communicated by a treated water supply pipe 24 (treated water supply flow path). A solenoid valve 25 and a treated water supply pump 50 are disposed in the middle of the treated water supply pipe 24 sequentially from the upstream portion. By the operation of the treated water supply pump 50, treated water containing phosphorus in the treated water storage tank 23 is supplied to the pressure chamber 19 for treated water.

Next, the upper wall 51 of the pressure chamber 13 and the distributors 12 will be described in detail with reference to FIGS.
The upper wall 51 has a disk shape, and a fitting hole 51a at the lower end of the inner cylinder 21 is formed at the center. Further, around the fitting hole 51a, six mounting holes 51b ... of the distributor 12 are formed at intervals of 60 degrees. In addition, a total of six narrow communication passages 51c that communicate the outer end surface of the upper wall 51 and the mounting holes 51b are formed radially inside the outer peripheral portion of the upper wall 51 with the fitting hole 51a as the center. ing.

  Around the lower part of the reaction tank 11, an annular connecting pipe 54 that is larger in diameter than the reaction tank 11 and is supplied with the slaked lime aqueous solution supply tank 17 of the slaked lime aqueous solution supply tank 17 through the supply part 54 a is provided through the support member 53. Yes. In the inner peripheral portion of the connecting pipe 54, six nozzle portions 54b, which are inserted into the communication passages 51c, are radially arranged inward at intervals of 60 degrees in the circumferential direction. The length of each nozzle part 54b ... is the same as the length of the corresponding communicating path 51c .... The slaked lime aqueous solution in the slaked lime aqueous solution supply tank 17 is supplied to the connecting pipe 54 via the supply part 54a, and is supplied from the nozzle parts 54b to the corresponding mounting holes 51b. Further, instead of the connecting pipe 54, a rotary valve is arranged at the communicating part of each nozzle part 54b, and the slaked lime aqueous solution is sequentially supplied to the six nozzle parts 54b by opening and closing the rotary valve. Good.

Each distributor 12 has an annular nozzle lower part 12a attached to the lower part of the corresponding attachment hole 51b, an annular nozzle upper part 12b attached to the upper part of the corresponding attachment hole 51b, and a nozzle upper part 12b. .., And nozzle umbrella plates 12 c that allow the fluid that has passed through the nozzle upper portions 12 b to blow out toward the bottom surface of the fluidized bed 14. The upper nozzle portions 12b project slightly upward from the upper surface of the upper wall 51. The nozzle umbrella plate 12c... Holds a predetermined fluid passage gap with the nozzle upper portion 12b... Via four short columns 12d. It is arranged above.
Between the nozzle lower portions 12a and the nozzle upper portions 12b, tips of corresponding nozzle portions 54b are arranged. Therefore, the slaked lime aqueous solution supplied to the connecting pipe 54 is blown out from the corresponding nozzle lower part 12a... And nozzle upper part 12b.

  On the other hand, at the portions of the upper wall 51 facing the mounting holes 51b, there are blowout nozzles 55 in which the opening at the tip is arranged near the center of the lower opening of the corresponding mounting hole 51b. A total of 6 stands. As for each blowing nozzle 55 ..., the lower opening part is connected with the pressure chamber 19 for to-be-processed water. Therefore, the treated water supplied from the treated water storage tank 23 to the treated water pressure chamber 19 passes through the blowing nozzles 55... And the distributor 12, and is blown out to the fluidized bed 14.

The slaked lime aqueous solution supply tank 17 is installed outside the reaction tank 11. Its internal capacity is such that it can store the slaked lime aqueous solution used for the treatment for 7 days. The slaked lime aqueous solution supply tank 17 is provided with a stirring device 27 driven by an electric motor 26. The replenishment of the slaked lime aqueous solution is automatically performed by a replenishment pump (not shown) based on the detection signal of the liquid level sensor provided in the slaked lime aqueous solution supply tank 17.
The slaked lime aqueous solution supply tank 17 communicates with one end of a branch pipe 30 provided with a pump 31 in the middle. The other end of the manifold 30 communicates with the supply unit 54a. The lid of the reaction tank 11 is provided with a pH sensor 100 that detects the pH of the treated water. The pH sensor 100 is connected to the input side of the pH control device 101. The pH of the treated water is detected by the pH sensor 100, and a command for supplying a predetermined amount of the slaked lime aqueous solution to the fluidized bed 14 is issued from the pH controller 101 to the pump 31 based on the obtained detection data. The slaked lime aqueous solution supply means 18 includes a manifold 30 and a pump 31.

Next, the crystallization dephosphorization method of the to-be-processed water containing the phosphorus using the crystallization dephosphorization apparatus 10 of Example 1 is demonstrated.
First, the to-be-treated water supply pump 50 is operated by opening the electromagnetic valve 25, and the to-be-treated water in the to-be-treated water storage tank 23 is supplied to the to-be-treated water pressure chamber 19 through the to-be-treated water supply pipe 24. The circulating water supplies the treated water at the upper part of the reaction tank 11 to the circulating water pressure chamber 20 from the enlarged diameter portion 21a via the inner cylinder 21 by rotating the rotary blade 22 by the electric motor 41. Thereafter, the water to be treated in the pressure chamber 19 for water to be treated is introduced into the fluidized bed 14 through the corresponding nozzles 12 through the blowout nozzles 55. On the other hand, the circulating water in the circulating water pressure chamber 20 is introduced into the fluidized bed 14 through each distributor 12.
Further, the slaked lime aqueous solution to be supplied as needed passes through the manifold 30 and the supply part 54a in order from the slaked lime aqueous solution supply tank 17 by the operation of the pump 31, and then through the connecting pipe 54, each nozzle part 54b. Are introduced into the fluidized bed 14.

  Thus, the water to be treated and the circulating water are contacted and mixed for the first time inside the distributors 12 immediately before being introduced into the fluidized bed 14. The treated water has a high phosphorus concentration. Further, the circulating water has a calcium ion concentration and a pH increased due to the influence of the slaked lime aqueous solution supplied from the slaked lime aqueous solution supply tank 17. However, the mixing of the water to be treated and the circulating water in the fluidized bed 14 is mixing in the presence of seed crystals. Therefore, even if the phosphorus concentration at the time of mixing is higher than the excessive solubility of phosphorus, most phosphorus is crystallized on the surface of the seed crystal as hydroxyapatite. Similarly, the slaked lime aqueous solution supplied as needed is also contacted and mixed with the water to be treated and the circulating water for the first time in each distributor 12... Just before being introduced into the fluidized bed 14.

As a result, phosphorus is hardly generated as an aggregate of calcium phosphate. Therefore, the amount of aggregates that cannot be recovered by the crystallization method can be reduced without changing the circulating water flow rate / treated water flow rate ratio.
Further, in the crystallization dephosphorization apparatus 10, an inner cylinder 21 erected in the reaction tank 11 is adopted as a circulating water supply flow path, and a lower peripheral wall of the reaction tank 11 is used as a water to be treated supply flow path. Since the to-be-processed water supply pipe | tube 24 formed in the part was employ | adopted, piping is removed from the bottom face part of the reaction tank 11 like a conventional apparatus, and construction and maintenance of the reaction tank 11 become easy.

Here, with reference to FIGS. 4 to 6 and the graph of FIG. 7, the results of the crystallization dephosphorization test actually performed on the conventional method and the method of the present invention will be reported. 4 to 6, the same parts as those in the crystallization dephosphorization apparatus 10 in FIG.
In the graph of FIG. 7, in Comparative Example 1, the water to be treated containing phosphorus and the circulating water are mixed in one pressure chamber 13, and the slaked lime aqueous solution is supplied to the lower part of the fluidized bed 14 through the external pipe 40a. An analysis and dephosphorization apparatus 10A (FIG. 4) was employed. In Test Example 1, the pressure chamber 13 is vertically divided into a lower pressure chamber for water to be treated 19 and an upper pressure chamber for circulating water 20, and a circulating water supply pipe 41 a provided on the peripheral wall of the reaction tank 11. A crystallization dephosphorization apparatus 10B (FIG. 5) in which a slaked lime aqueous solution was mixed in the middle through the pipe 40b was adopted. In Test Example 2, the pressure chamber 13 is similarly divided into a lower pressure chamber 19 for water to be treated and an upper pressure chamber 20 for circulating water, and an aqueous solution of slaked lime is supplied to the lower part of the fluidized bed 14 through a pipe 40a from the outside. A crystallization dephosphorization apparatus 10C (FIG. 6) was employed.
As for the experimental conditions, in both Comparative Example 1 and Test Examples 1 and 2, the phosphorus concentration of the treated water (phosphate ion phosphorus concentration) is 4.7 mg / liter, the circulating water flow rate / treated water flow rate ratio is 10, and the fluidized bed 14 Control pH is 9.8, superficial velocity is 10 / hr.

  As is clear from the graph of FIG. 7, even in the same circulating water flow rate / treated water flow rate ratio, Test Examples 1 and 2 generate less aggregates than Comparative Example 1. Therefore, it was found that if the treated water containing phosphorus and the circulating water are mixed in the presence of seed crystals, the generation of aggregates is suppressed.

It is a schematic block diagram of the reaction crystallization processing apparatus which concerns on Example 1 of this invention. It is a principal part expanded sectional view of the reaction crystallization processing apparatus which concerns on Example 1 of this invention. It is a principal part top view of the connection pipe integrated in the reaction crystallization processing apparatus which concerns on Example 1 of this invention. It is a schematic block diagram of the crystallization dephosphorization apparatus which concerns on a conventional means. It is a schematic block diagram of the crystallization dephosphorization apparatus which concerns on the other Example of this invention. It is a schematic block diagram of the crystallization dephosphorization apparatus which concerns on another Example of this invention. It is a graph which shows the phosphorus component in the treated water obtained by this invention method and the conventional method.

Explanation of symbols

10 Crystallization dephosphorization device (reaction crystallization treatment device),
11 reaction tank,
12 Distributor (air outlet),
13 Pressure chamber,
14 fluidized bed,
15 treated water supply means,
16 Circulating water supply means,
18 Slaked lime aqueous solution supply means,
19 Pressure chamber for water to be treated
20 Pressure chamber for circulating water,
21 inner cylinder (circulation water supply flow path),
24 treated water supply pipe (treated water supply flow path).

Claims (5)

By introducing the water to be treated into the fluidized bed in which the seed crystals are present and bringing the water to be treated and the seed crystals into contact with each other in the fluidized bed, the target component in the water to be treated is crystallized as a compound on the surface of the seed crystals. In the reactive crystallization treatment method, a part of the treated water is introduced into the fluidized bed as circulating water.
A reaction crystallization treatment method in which the water to be treated and the circulating water are contacted and mixed for the first time immediately before being introduced into the fluidized bed, or individually introduced into the fluidized bed. A chemical is added to the fluidized bed,
The reaction crystal according to claim 1, wherein the chemical solution is brought into contact with and mixed with the water to be treated and the circulating water immediately before the treated water and the circulating water are introduced into the fluidized bed or in the fluidized bed. Analysis method. From the pressure chamber formed in the lower part of the reaction tank, through a plurality of outlets formed in the upper wall of the pressure chamber, phosphorus is added to the fluidized bed formed above the pressure chamber of the reaction tank and containing seed crystals. The treated water contained is introduced, phosphorus in the treated water is brought into contact with the seed crystal in the fluidized bed, and the treated water is crystallized on the surface of the seed crystal to obtain treated water, In the reaction crystallization treatment method in which a part of the treated water is introduced into the fluidized bed through the outlets from the pressure chamber as circulating water,
The pressure chamber is divided into a pressure chamber for treated water into which the treated water is introduced and a pressure chamber for circulating water into which the circulating water is introduced,
The treated water is introduced into the fluidized bed from the treated water pressure chamber through the blowout port, while the circulating water flows from the circulating water pressure chamber through a different blowout port from the treated water blowout port. A reactive crystallization treatment method introduced into the floor. A reaction tank in which treated water containing phosphorus is stored;
A pressure chamber formed in the lower part of the reaction vessel and having a plurality of outlets formed in the upper wall;
A fluidized bed formed above the pressure chamber in the reaction vessel and containing seed crystals;
A treated water supply means for supplying treated water to the pressure chamber;
A part of the treated water obtained by bringing phosphorus contained in the treated water into contact with a seed crystal and removing phosphorus in the treated water by crystallization on the surface of the seed crystal, In the reaction crystallization treatment apparatus provided with circulating water supply means for supplying the pressure chamber as circulating water through,
The pressure chamber is divided into a pressure chamber for treated water to which the treated water is supplied and a pressure chamber for circulating water to which the circulating water is supplied,
The outlet has an outlet that communicates the pressure chamber for water to be treated and a fluidized bed, and an outlet that communicates the pressure chamber for circulating water and a fluidized bed,
The treated water supply means has a treated water supply flow path for supplying the treated water to a pressure chamber for treated water,
The said circulating water supply means is a reaction crystallization processing apparatus which has the circulating water supply flow path which supplies the said circulating water to the pressure chamber for circulating water. The downstream end of the treated water supply flow path is communicated with a treated water pressure chamber from a part of the peripheral wall of the reaction tank,
The reaction crystallization treatment apparatus according to claim 4, wherein an end portion on the downstream side of the circulating water supply flow path is communicated with the circulating water pressure chamber through the reaction tank.

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