JP5753702B2 - Formation method of initial mother floc in high speed coagulation sedimentation basin - Google Patents

Description

  The present invention is a high-speed coagulation sedimentation basin implemented in the water treatment field for producing tap water, industrial water and the like, and the water treatment field for treating sewage. The present invention relates to a method of forming an initial mother floc that is performed when starting or restarting a pond.

In water treatment of river water, groundwater, rainwater, etc., treatment for removing turbidity components, algae and the like, which are insoluble components, is performed by solid-liquid separation techniques such as coagulation sedimentation treatment and sand filtration treatment.
Among these, the coagulation-precipitation treatment is performed by adding an inorganic coagulant or pH adjuster to the raw water to precipitate the pollutant in the raw water, or adsorbing the pollutant on the flocs generated from the inorganic coagulant. Is a treatment method in which flocs containing water are settled and removed from raw water.

  In the conventional coagulation-precipitation treatment, a mixing tank, a floc-forming tank and a precipitation tank are installed in succession, and after mixing raw water (treated water) and the inorganic flocculant in the mixing tank, this is transferred to the flock-forming tank and the precipitation tank. The so-called cross-flow type sedimentation basin was adopted, in which flocks were formed while purifying the raw water. However, this method has a problem that a flocs sedimentation rate is slow and a large area is required to treat certain raw water.

Therefore, a “high-speed coagulating sedimentation basin” was proposed in which the ascending flow rate of the sedimentation section can be increased to reduce the facility area of the sedimentation section.
FIG. 2 is a schematic diagram showing a configuration example of an implementation of the high-speed coagulation sedimentation basin. After the inorganic flocculant 58 is added to the raw water 51, it is sent to a stirring unit having a primary stirring chamber 52 and a secondary stirring chamber 53, where slurry is generated. And while this slurry forms a slurry interface in the precipitation part 54, the lower part of the precipitation part 54 is connected with the primary stirring chamber 52, and the slurry (; containing floc) in the precipitation part 54 is The slurry is returned to the primary stirring chamber 52 and a new slurry is generated in the primary stirring chamber 52 in the presence of the existing slurry. On the other hand, the settling water 55 in the settling portion 54 overflows from the upper overflow port and flows out as settling water.

  The high-speed coagulation sedimentation basin makes use of the fact that the floc formation speed is proportional to the square of the number of floc particles and the cube of the floc particle size, so that a portion having a high floc concentration is provided to allow raw water to pass therethrough. In this way, the initial fine flocs are aggregated while supplementing the already grown flocs (referred to as “mother flocs” in the present invention) to increase the efficiency of aggregation precipitation (Non-patent Document 1). Therefore, according to the high-speed coagulating sedimentation basin, flocs can be formed quickly, and the generated flocs are coarse and have a large sedimentation rate, so that the sedimentation basin area can be reduced. Further, since it is not necessary to use a polymer flocculant, it is widely used in the water treatment field where safety and security are required, such as waterworks.

  Regarding such a high-speed coagulation sedimentation site, Patent Document 1 discloses that the zeta potential when added to the water to be treated is -40 mV or less as an insoluble coagulant auxiliary agent to be added to the water to be treated together with the inorganic flocculant. An agglomeration aid having a specific gravity of 2.0 or more and 4.0 or less, an abundance ratio of particles having a particle size distribution of 100 μm or more is 5 mass% or less, and an abundance ratio of particles of 10 μm or less is 30 mass% or less is disclosed. ing.

“Water Supply Facility Design Guidelines 2000”, pp. 199-201

JP 2006-7086 A

In this type of high-speed coagulation sedimentation basin, it is necessary to perform inspections and repairs about once a year. In each case, the sedimentation basin is emptied for inspection and repairs, and then the sedimentation becomes empty. New raw water is drawn into the pond, and based on the turbid content derived from the raw water, a mother flock (referred to as “initial mother flock” in the present invention) that becomes a seed for flock formation is formed and retained in the sedimentation pond. There is a need.
Conventionally, it took a long time to form the initial mother floc and allow it to stay in the sedimentation basin sufficiently. I had a problem. Moreover, in recent years, river repairs such as dam installations have progressed, and the turbidity of river water as a water intake source tends to become lower, and therefore the period required to form the initial mother floc tends to be further prolonged.

  Therefore, an object of the present invention is to propose a method capable of forming the initial mother floc in a shorter time when starting up the high-speed coagulation sedimentation basin, that is, when starting or restarting the operation of the high-speed coagulation sedimentation basin. There is to do.

The present invention, in the water tank has an initial raw water, and an inorganic coagulant, at a mass ratio of more than 100μm is less than 5%, a and particle size distribution mass ratio of less 10μm is 30% or less, and a specific gravity Agglomeration aid comprising fine sand having a zeta potential of −30 mV to −60 mV when added to the raw water at a concentration of 100 mg / L to 4000 mg / L in the water tank , was added and the initial mother floc was formed from the initial raw water, then, the initial base floc performed when starting up the suspended solids ponds and forming a floc from the raw water in the presence of the initial base floc The formation method of this is proposed.

  The `` water tank '' of the high-speed coagulation sedimentation basin means the entire tank in which the initial raw water stays in the high-speed coagulation sedimentation basin. It means to include.

  According to the method for forming the initial mother floc proposed by the present invention, the initial mother floc is formed when the high-speed coagulation sedimentation basin is started up, that is, when the operation of the high-speed coagulation sedimentation basin is started or restarted. Can be done in a short time.

It is the schematic diagram which showed the structure of the experimental apparatus used in the Example and the comparative example, ie, the experimental apparatus which simulated the high-speed coagulation sedimentation basin of real equipment. It is the schematic diagram which showed the structural example of the high-speed coagulation sedimentation basin.

  Next, an example of an embodiment of the present invention will be described. However, the present invention is not limited to the embodiment described here.

<Initial mother floc formation method>
The initial mother floc formation method in the present embodiment is a method of forming an initial mother floc from the initial raw water by causing an inorganic flocculant and a coagulant auxiliary to exist together with the initial raw water in the water tank when the high-speed coagulation sedimentation basin is started up ( (Referred to as “this initial mother floc forming method”).
After forming the initial mother floc in this way, the raw water, that is, the water to be treated is drawn into the water tank, the floc is formed from the raw water (treated water) in the presence of the initial mother floc, and the purified treated water is A series of normal operations can be started or resumed.

As a specific method for forming an initial mother floc, for example, an inorganic flocculant and a coagulant auxiliary agent are introduced after the initial raw water is introduced into an empty water tank and the necessary amount is stored, or while the initial raw water is stored in the water tank. Can be added to the initial raw water and stirred to form an initial mother floc from the initial raw water without causing the treated water to flow out (referred to as “batch type forming method”).
In addition, an inorganic flocculant and a coagulant auxiliary agent are introduced into an empty water tank together with the initial raw water, and stirred in the water tank to form an initial mother floc from the initial raw water, while the treated water is discharged from the water tank at that time ( (Referred to as “flow type forming method”).
However, it is not limited to these methods, and methods other than these methods can also be adopted.

(Initial raw water)
In the present invention, “initial raw water” means raw water (treated water) used to form an initial mother floc. In the batch type forming method, the raw water is stored in the water tank for the initial mother floc formation, and in the flow type forming method, it is all the raw water introduced into the water tank for the initial mother flock formation.

  The initial raw water includes, for example, river water, groundwater and rainwater, as well as water that requires purification, such as treated water for sewage, human waste, and industrial wastewater.

The initial raw water turbidity is preferably 10 degrees or less. If the turbidity of the initial raw water is higher than 10 degrees, there is a possibility that the initial mother floc can be formed in a sufficiently short time depending on the floc forming conditions during normal operation without adopting this initial mother floc forming method. Because.
Thus, from the viewpoint of further enjoying the effects of the present invention, the turbidity of the initial raw water is more preferably 5 degrees or less, and even more preferably 3 degrees or less.

It is preferable to adjust the pH of the initial raw water to a range of 6.0 to 8.0.
If the raw water (treated water) is strongly acidic, for example, when using a flocculant containing a metal salt such as aluminum or iron, aluminum exists in the form of simple ions (Al ³⁺ ), It becomes difficult to form a floc. Moreover, when raw | natural water is acidic, there are many ratios which aluminum melt ^| dissolves as ^{Al3 +} , and solid content comes to precipitate when to-be-processed water is made into a neutral region by subsequent processing. On the other hand, when the raw water (treated water) is alkaline, the proportion of aluminum dissolved as a negative charge (AlO ²⁻ ) increases, and solids are deposited when the treated water is neutralized in the subsequent treatment. On the other hand, when the pH of the raw water (treated water) is near neutral, the proportion of Al ³⁺ and hydroxide ions combined increases, resulting in electrically neutral and insoluble aluminum hydroxide. This insoluble aluminum hydroxide takes in the turbidity component and the coagulation aid to form a floc.
From such a viewpoint, it is preferable to adjust the pH of the initial raw water to a range of 6.0 to 8.0, particularly 7.0 or more and 7.5 or less.

Therefore, it is preferable to add an inorganic flocculant and an agglomeration aid after adjusting the pH by adding a pH adjuster to the initial raw water as necessary.
At this time, when a metal salt such as aluminum or iron is used as a flocculant, the metal salt is weakly acidic, so that the pH is lowered when added to water. If the pH drops more than necessary at this time, flocs may not be formed as described above. In this case, the pH of the initial raw water is adjusted using alkali (caustic soda, lime, sodium bicarbonate, etc.). It is desirable to do.

(Aggregating aid)
The fine sand as an agglomerating aid has a particle size distribution in which the mass ratio of 100 μm or more is 5% or less and the mass ratio of 10 μm or less is 30% or less, and the specific gravity is 2.0 to 4.0. It is important to be.
When such fine sand is used as an agglomeration aid, floc formation and growth can be effectively promoted in agglomeration and precipitation treatment of various turbidity components such as clay, color colloid, and organic colloid.

It is important that the fine sand has a particle size distribution in which the mass ratio of 100 μm or more is 5% or less and the mass ratio of 10 μm or less is 30% or less.
Particles having a particle size of 100 μm or more are larger than particles usually called fine particles and have a high sedimentation speed. Therefore, in order to prevent sedimentation and uniformly disperse in raw water, the stirring speed must be increased. In addition, the fact that the particle size of the coagulation aid is large means that the particle surface area becomes small even if the addition amount on the mass basis is the same, and the contact probability between the coagulation aid and the inorganic coagulant can be reduced. Therefore, it can be said that it is more preferable that there are not so many particles having a size of 100 μm or more as the aggregation assistant. Furthermore, particles having a size of 10 μm or less mean that the number of particles is increased even if the addition amount on the mass basis is the same, and this can increase the proportion of the coagulation aid that is not taken into the floc. Therefore, it can be said that it is preferable that there are not more particles of 10 μm or less than necessary as an aggregation aid. That is, in order to prevent the coagulation aid that has not been taken into the flocs from being settled by itself and mixed into the treated water, the particle size is not too fine and a settling rate of a certain level (that is, a certain level or more). Specific gravity).

It is further important that the fine sand has a specific gravity of 2.0 to 4.0. If the specific gravity is too large, it is necessary to increase the stirring speed in order to uniformly disperse it in the water to be treated. If the specific gravity is too small, the action of increasing the sedimentation speed of the floc becomes insufficient and it is taken into the floc. Otherwise, it is difficult for the flocculation aid itself to settle, and the flocculation aid may be mixed into the water to be treated.
From this viewpoint, the specific gravity of fine sand is more preferably 2.4 or more or 2.7 or less.
Regarding the coagulation aid, the description in paragraphs [0022]-[0034] of JP-A-2006-7086 is also cited.
The fine sand may be added in the form of powder or solution as long as it is not blocked by the injection line.

It is important that the fine sand is insoluble in water and has a zeta potential of −30 mV to −60 mV when added to the water to be treated.
The zeta potential is the potential at the shear plane between the moving and non-moving layers at the same time when the particles in the liquid move, that is, the potential at the sliding surface of the particles. Value.
Such fine sand having a zeta potential is preferable in that it is efficiently taken into flocs produced from the inorganic flocculant and hardly remains in the treated water. While the flocculant (PAC, aluminum sulfate, etc.) produces aluminum hydroxide in water, it takes in the flocculant together with the turbidity component to form a floc. The flocculent aid has a zeta potential of -30 mV to -60 mV. It becomes easy to be taken in by the floc.
From this viewpoint, the zeta potential of the fine sand is particularly preferably −50 mV or less.

It is preferable to adjust the amount of such fine sand so that the concentration of fine sand in the water tank (concentration with respect to the initial raw water) is 100 to 4000 mg / L. That is, if it is a batch type formation method, it is preferable that the addition amount of the fine sand with respect to initial raw water is 100-4000 mg / L, and if it is a flow type formation method, the added fine sand will flow out of a water tank. Therefore, it is preferable to control so that the concentration of the fine sand with respect to the initial raw water is within the range of 100 to 4000 mg / L.
If there is little fine sand, coagulation failure will occur and the initial mother floc will not be generated sufficiently, the turbid matter that was not trapped by aggregation will float, overflow with the treated water at startup, and the treated water turbidity will increase, It takes a long time. On the other hand, when there is too much fine sand, extra fine sand may remain in the treated water, leading to a decrease in the quality of the treated water.
Therefore, from this point of view, the amount of fine sand added is such that the concentration of fine sand relative to the initial raw water in the aquarium is 200 mg / L or more or 2000 mg / L or less, of which 350 mg / L or more or 1200 mg / L or less. It is more preferable to adjust the addition amount so that it becomes 900 mg / L or less.

Regarding the addition rate of fine sand, in the batch-type forming method, the rate of increase in the average concentration of fine sand in the water tank after the start of introduction of fine sand into the water tank is in the range of 1 to 90 mg / L / min. It is preferable to control so that it becomes. It has been confirmed that if the rate of increase in the average concentration of fine sand is too low, the efficiency is poor, whereas if it is too high, agglomeration failure occurs and the formation efficiency of the initial mother flocs decreases. From this point of view, in the batch-type forming method, it is more preferable to control so that the rate of increase in the average concentration of fine sand in the water tank after starting the introduction of fine sand into the water tank is 60 mg / L / min or less. Even more preferred.
On the other hand, in the flow-type forming method, for the same reason as described above, the rate of increase in the average concentration of fine sand in the water tank after starting the introduction of fine sand into the water tank is 120 mg / L / min or less. It is preferable to control, in particular, it is more preferable to control to be 1 mg / L / min or more or 90 mg / L / min or less, and particularly, 60 mg / L / min or less.

(Flocculant)
As the inorganic flocculant to be added at the time of forming the initial mother floc, a general flocculant used in an ordinary flocculent precipitation water treatment method can be used. Examples thereof include polyaluminum chloride (PAC), sulfated clay, solid aluminum sulfate, liquid aluminum sulfate, and ferric sulfate. One or more of these can be used in combination.

The flocculant is preferably added in an amount of 10 to 150 parts by mass with respect to 100 parts by mass of fine sand.
During normal operation, it is preferable to adjust both amounts so that the ratio of the coagulant aid to the coagulant is within a certain range, but when the initial mother block is formed, the amount of coagulant added to the fine sand is within the range. It is preferable to adjust so that it becomes. At this time, if the amount of the flocculant with respect to the fine sand is too small, fine sand that is not taken into the agglomeration will be generated. Conversely, if the amount is too large, the floc swells and flocs with poor sedimentation are formed. As a result, there is a possibility that the water quality is lowered after the operation is started.
Therefore, from such a viewpoint, it is more preferable to add the flocculant at a ratio of 25 parts by mass or more and 100 parts by mass or less with respect to 100 parts by mass of fine sand, and among them, a ratio of 40 parts by mass or more or 60 parts by mass or less. It is even more preferred to add a flocculant at

(Initial mother flock formation method)
The order of adding the coagulant aid and fine sand may be any, or may be added simultaneously.
The injection point of the flocculant and the fine sand is preferably the same, but from the viewpoint of preventing the flocculant and fine sand from remaining in the treated water, it is preferable to add the fine sand having sedimentation property first.

  The initial raw water, the flocculant and the fine sand are preferably introduced into the water tank or after the initial raw water in the water tank is stirred.

(Configuration of high-speed coagulation sedimentation pond)
The configuration of the high-speed coagulation sedimentation basin is not particularly limited. For example, the classification of the principle and mechanism of the high-speed coagulation sedimentation basin, and the classification described in the reference (design guideline), the “slurry circulation type”, “sludge blanket type”, “composite type” all forms the initial mother floc formation. The method can be applied.
Moreover, it is applicable also to the deformation | transformation and combination which are generally used for water treatment, such as the structure which combined sedimentation apparatuses, such as an inclined plate, with the high-speed coagulation sedimentation basin.

<Explanation of terms>
In the present invention, when expressed as “X to Y” (X and Y are arbitrary numbers), “X is preferably greater than X” and “preferably Y”, with the meaning of “X to Y” unless otherwise specified. It means “smaller”.
Further, in the present invention, when expressed as “X or more” (X is an arbitrary number), it means “preferably larger than X” unless otherwise specified, and “Y or less” (Y is an arbitrary number). ) Includes the meaning of “preferably smaller than Y” unless otherwise specified.

  EXAMPLES Hereinafter, although an Example and a comparative example demonstrate this invention further in detail, this invention is not restrict | limited by the following Example.

(Experimental device)
FIG. 1 is a schematic diagram showing the configuration of an experimental apparatus used in Examples and Comparative Examples (hereinafter referred to as “the present experimental apparatus”), that is, an experimental apparatus simulating a high-speed coagulation sedimentation basin of actual equipment.
On the downstream side of the raw water storage tank, a stirring unit including a primary stirring chamber 2 (5.0 L) and a secondary stirring chamber 3 (1.5 L) and a precipitation unit 4 are sequentially arranged. The sedimentation part 4 has a diameter of 120 mm and a height of 1500 mm, an ascending flow rate (standard) of 50 mm / min, and the amount of water (ascending flow rate) is variable depending on the raw water pump injection amount. A line for returning the slurry to the primary stirring chamber 2 of the stirring unit via the circulation pump P3 is provided on the downstream side of the precipitation unit 4. Moreover, the overflow part is provided in the sedimentation part 4, and when processing to-be-processed water at the time of a normal driving | operation, ie, completion | finish of initial stage mother floc formation, the overflowed treated water is set to the sedimentation treated water 5 from an overflow port. It comes to leak.

In the initial mother floc forming process of the examples and comparative examples, the flocculant and fine sand were added only to the raw water in the primary stirring chamber.
In addition, during the initial mother floc forming process of the example and the comparative example, the circulation pump P3 is always operated so as not to overflow from the overflow port of the sedimentation section, and the pump P4 used for draining mud is not operated. I made it.

(Example 1-8 and Comparative Example 1-3)
Using this experimental apparatus, kaolin as a turbidity source was added to city water (Fujisawa city tap water) and mixed and stirred in the raw water storage tank to prepare initial raw water (turbidity 1 degree, pH 7, water temperature 15 ° C. (room temperature)).
Next, the prepared initial raw water is introduced into the primary stirring chamber 2, and after the initial raw water of the amount that the stirring blades are completely immersed is accumulated in the stirring portion, the flocculant and fine particles are added at the amount and addition rate shown in Table 1. Sand was added and stirring was started.
After adding the flocculant and fine sand, after the time shown in Table 1 (initial mother floc formation time), it was confirmed that a slurry interface was formed in the sedimentation portion 4, so at this time the initial mother floc was formed. Completed.

In addition, as "flocculating agent", PAC (existing chemical substance official gazette announcement number: 1-12 and 1-17, CAS No.1327-41-9, JIS standard polyaluminum chloride JISK1475, general formula [Al ₂ (OH ) nC _l6-n ] m (0 <n <6, m ≦ 10, basicity = n / 6 × 100%), specific gravity 1.25 / 20 ° C., viscosity 11 cps / 20 ° C., pH 2.5 / 20 ° C.) Was used.
As “fine sand”, components: SiO ₂ 94% or more, Al ₂ O ₃ 5% or less, Fe ₂ O ₃ 0.5% or less, particle size distribution (laser diffraction particle size distribution measuring device SALD-2100 (Shimadzu Corporation): 100 μm Fine sand having a mass ratio of 3% and a mass ratio of 10 μm or less of 20%, a specific gravity of 2.7, and a zeta potential of −50 mV was used.
In the agglomeration operation, as a matter of course, when the aggregating agent is injected, the alkali is consumed, and when the alkali is insufficient, the agglutination reaction is inhibited. Therefore, in Examples and Comparative Examples, caustic soda is injected in a timely manner and the pH in the water tank is controlled to be 7.0 ± 0.5, but is not particularly described here.
In Comparative Example 3, kaolin was added instead of fine sand.

In Table 1, “concentration of fine sand and flocculant” refers to the ratio of fine sand or flocculant added to the initial raw water amount, that is, added to the initial raw water amount (L) present in the agitation part and the precipitation part. The ratio (mg / L) of the amount (mg) of fine sand or flocculant is shown.
“Concentration increase rate of fine sand and flocculant” indicates the increase rate (mg / L / min) after the start of the average concentration of fine sand or flocculant present in the stirring part and the precipitation part.
The “initial mother floc formation time” indicates a time during which it was possible to visually confirm that a slurry interface was formed in the settled portion 4 after adding the flocculant and fine sand.
“Slurry interface (mm)” was measured using a direct-view water level gauge with reference to the lower end of the draft tube.

The “SV value (%)” in Table 1 was measured as follows.
1) First, slurry (mother floc) was collected above the second stirring chamber, put into a measuring cylinder, and the volume (volume 1) was measured.
2) The mixture was allowed to stand for 5 minutes, and the slurry was deposited while being concentrated.
3) The volume (volume 2) of the deposited slurry was measured.
4) Then, SV value (%) was calculated by the formula: SV value (%) = volume 2 ÷ volume 1 × 100.

  “Processed water turbidity” in Table 1 is intended to measure the treated water turbidity after starting normal operation, after the formation of the initial mother floc as described above, at a design throughput of 0.5 L / min. The turbidity of the treated water obtained by allowing the precipitated treated water 5 to flow out from the overflow port of the precipitation part 4 was measured. At that time, the turbidity was measured with a highly sensitive turbidimeter (“TR-55” manufactured by Kasahara Chemical Co., Ltd.).

  The conditions shown in Example 1-8, that is, when starting up the high-speed coagulation sedimentation basin, by setting the concentration of fine sand in the water tank to a range of 100 mg / L to 4000 mg / L, the initial raw water to the initial mother floc It has been found that the time until the formation of can be made shorter than those in Comparative Examples 1 and 3, and the process can be shifted to a normal process in which the treated water turbidity is always lower than the raw water turbidity. Therefore, according to such a method for forming the initial mother floc, the initial mother floc can be formed in a shorter time than before when the operation of the high-speed coagulation sedimentation basin is started or restarted.

DESCRIPTION OF SYMBOLS 1 Raw water 2 Primary stirring chamber 3 Secondary stirring chamber 4 Precipitation part 5 Precipitation water 7 Waste mud 9 Agitation blade 11 Coagulant and fine sand P1, P2, P3, P4, P5 Pump 51 Raw water 52 Primary stirring chamber 53 Secondary stirring Chamber 54 Precipitation part 55 Precipitation water 57 Waste mud 58 Inorganic flocculant 59 Stirring blade 60 Outer draft tube

Claims (7)

Water tank has an initial raw water, and an inorganic coagulant, at a mass ratio of more than 100μm is less than 5%, a particle size distribution mass ratio of less 10μm is 30% or less, and a specific gravity of 2.0 4.0, and a concentration in the water tank of 100 mg / L to 4000 mg / L, and a zeta potential when added to the raw water is -30 mV to -60 mV, and an agglomeration aid is added, and A method for forming an initial mother floc, which is performed when a high-speed coagulation sedimentation basin is started, characterized in that an initial mother floc is formed from initial raw water, and then a floc is formed from raw water in the presence of the initial mother floc. The method for forming an initial mother floc performed when the high-speed coagulation sedimentation basin is started up according to claim 1, wherein fine sand of 100 mg / L to 4000 mg / L is added to the initial raw water. The method for forming an initial mother floc performed when the high-speed coagulation sedimentation basin is started according to claim 1 , wherein the coagulant is added in an amount of 10 to 150 parts by mass with respect to 100 parts by mass of the fine sand. After reservoir the initial raw water in the water tank, or from the middle for storing the initial raw water in the water tank, the inorganic coagulant and the flocculation aid stirring in addition to the initial raw water, thereby flow out the initial raw water without forming method of the initial base floc performed when starting up the high speed aggregation sedimentation basin according to any one of claims 1 to 3, characterized in that to form the initial base floc from the initial raw water. While the addition of the inorganic coagulant and the flocculating aid with the initial raw water in the water tank, while effluent treated water from the water tank, and characterized in that by stirring in a water bath to form an initial base floc from the initial raw water A method for forming an initial mother floc that is performed when the high-speed coagulation sedimentation basin according to claim 1 is started up . 5. The high-speed coagulation precipitation according to claim 4, wherein the rate of increase in the average concentration of the coagulation aid in the water tank after the start of the addition of the coagulation aid into the water tank is 1 to 90 mg / L / min. A method of forming an initial mother flock when starting a pond . 6. The high-speed coagulation sedimentation basin according to claim 5, wherein the rate of increase in the average concentration of the coagulation aid in the water tank is 120 mg / L / min or less after the start of the addition of the coagulation aid into the water tank. A method of forming an initial mother flock when starting up .

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