JP2002282668A - Slurry storage method and storage apparatus - Google Patents

Slurry storage method and storage apparatus

Info

Publication number
JP2002282668A
JP2002282668A JP2001090750A JP2001090750A JP2002282668A JP 2002282668 A JP2002282668 A JP 2002282668A JP 2001090750 A JP2001090750 A JP 2001090750A JP 2001090750 A JP2001090750 A JP 2001090750A JP 2002282668 A JP2002282668 A JP 2002282668A
Authority
JP
Japan
Prior art keywords
slurry
fly ash
tank
rotating
slurry tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001090750A
Other languages
Japanese (ja)
Other versions
JP4181754B2 (en
Inventor
Shinichiro Saito
紳一郎 齋藤
Tomomichi Nakamura
朋道 中村
Eiji Fukamachi
英司 深町
Soichiro Okamura
聰一郎 岡村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Taiheiyo Cement Corp
Original Assignee
Taiheiyo Cement Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Taiheiyo Cement Corp filed Critical Taiheiyo Cement Corp
Priority to JP2001090750A priority Critical patent/JP4181754B2/en
Publication of JP2002282668A publication Critical patent/JP2002282668A/en
Application granted granted Critical
Publication of JP4181754B2 publication Critical patent/JP4181754B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To store fly ashes in form of a slurry for a long duration. SOLUTION: A slurry is supplied to a cylindrical slurry tank 2 made to have a circular bottom part, a rotation truck 3 extended from the rotary shaft installed in the center of the circle of the slurry tank 2 in the outer circumferential direction of the circle is rotated at a period of not shorter than 15 minutes and not longer than 3 hours, and stirring blades 4a attached to a single or a plurality of stirring apparatuses 4 installed on the rotation truck 3 in rotatable manner just like a planet are rotated at a circumferencial speed of 0.01 m/s to 1 m/s. Since the rotation truck 3 and the stirring blades 4a of the stirring apparatuses 4 are rotated at a low speed, the operation motive force can be suppressed to low and since no facility for blowing compressed air or the like is needed, the installation cost can be suppressed to low.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、スラリーの貯蔵方
法及び貯蔵装置に関し、特に、都市ごみ焼却場で発生し
た飛灰を水洗脱塩処理した後の飛灰スラリー等を、一定
期間ポンプにて圧送可能な性状のまま貯蔵することので
きるスラリーの貯蔵方法及び貯蔵装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for storing a slurry, and more particularly, to a method for pumping a fly ash slurry or the like obtained after washing and desalinating fly ash generated in an incineration plant for municipal solid waste. The present invention relates to a method and a storage device for storing a slurry that can be stored as it can be pumped.

【0002】[0002]

【従来の技術】従来、都市ゴミ焼却飛灰等の焼却飛灰を
セメント原料として再利用するにあたって、焼却飛灰中
の塩素化合物によって生ずるセメント焼成工程における
トラブルを回避する必要があるため、焼却飛灰を水洗し
て塩素化合物を除去することが行われている。
2. Description of the Related Art Conventionally, when incinerating fly ash such as municipal waste incineration fly ash is reused as a raw material for cement, it is necessary to avoid troubles in the cement burning process caused by chlorine compounds in the incineration fly ash. The ash is washed with water to remove chlorine compounds.

【0003】塩素化合物を水洗除去した後の約0.5%
の残留塩素をもつ焼却飛灰をセメント製造工程において
原料として利用するにあたって、セメントキルンの休転
中に受け入れた飛灰を休転後に処理する必要があるが、
原料中に許容される塩素量および飛灰スラリー圧送設備
能力等の制約から、全原料に対する飛灰の使用量の割合
が一定量に制限されるため、水洗脱塩後の飛灰スラリー
を2〜4ヶ月程度ポンプで圧送可能な性状のまま貯蔵
し、定常処理品に少量ずつ加えながら原料へ添加処理す
る必要がある。しかし、飛灰をスラリーとして長期保存
する試みは従来行われたことはなかった。
Approximately 0.5% after chlorine compounds are removed by washing with water
When using incinerated fly ash with residual chlorine as a raw material in the cement manufacturing process, it is necessary to treat fly ash received during the suspension of cement kiln after suspension,
Since the ratio of the amount of fly ash used to all the raw materials is limited to a certain amount due to restrictions on the amount of chlorine allowed in the raw materials and the capacity of the fly ash slurry pumping facility, the fly ash slurry after washing and desalination is reduced to 2%. It is necessary to store it in a state that can be pumped by a pump for about 4 months, and to add it to the raw material while adding it little by little to the constantly processed product. However, no attempt has been made for long-term storage of fly ash as a slurry.

【0004】一方、特開平6−299171号公報に
は、スラリー中の固形分の沈降を防止するため、タンク
底面を傾斜させるとともに、傾斜面の低い方側からスラ
リーを吸い込み、ポンプでスラリー上部に吐出すること
によってスラリーを攪拌する方法及び装置が開示されて
いる。
On the other hand, Japanese Patent Application Laid-Open No. 6-299171 discloses that in order to prevent sedimentation of solids in the slurry, the bottom of the tank is inclined, the slurry is sucked from the lower side of the slope, and the slurry is pumped to the upper part of the slurry. A method and apparatus for stirring a slurry by discharging is disclosed.

【0005】また、特開平7−216369号公報に
は、液面に浮かぶフロートに取り付けられた吸込口から
スラリーの上澄み液を吸い込み、ポンプで加圧してタン
クの循環流を形成させてスラリーを均質に保つ技術が開
示されている。
Japanese Patent Application Laid-Open No. Hei 7-216369 discloses that the supernatant liquid of a slurry is sucked from a suction port attached to a float floating on the liquid surface, and is pressurized by a pump to form a circulating flow in a tank to homogenize the slurry. A technique for keeping the information is disclosed.

【0006】[0006]

【発明が解決しようとする課題】しかし、上記特開平6
−299171号公報及び特開平7−216369号公
報に記載されたスラリー攪拌方法及び装置は、微細な粉
末にした石炭を水中に分散懸濁させてスラリー状とした
CWMをハンドリングするためのものであって、都市ご
み焼却場で発水した飛灰を水洗脱塩処理した後の飛灰ス
ラリー等をセメント製造のために利用するには適当でな
い。
However, Japanese Patent Application Laid-Open No.
The slurry stirring method and apparatus described in JP-A-299171 and JP-A-7-216369 are for handling a CWM which is made into a slurry by dispersing and suspending fine powdered coal in water. However, it is not suitable to use the fly ash slurry or the like after the fly ash generated in the municipal solid waste incineration plant is washed with water and desalinated for the production of cement.

【0007】そこで、本発明は、飛灰をスラリーとして
長期間保存することのできるスラリーの貯蔵方法及び貯
蔵装置を提供することを目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a slurry storage method and a storage device capable of storing fly ash as a slurry for a long period of time.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するた
め、本発明者は、研究を重ね種々の試験を行った結果、
円筒形のスラリータンクにおいて、回転台車の周期と撹
拌翼の周期を一定の範囲内にすることによって、所要動
力を抑制しながら、ポンプ圧送性を長期間確保すること
ができることを見出し、本発明を完成するに至った。
Means for Solving the Problems In order to achieve the above object, the present inventor has conducted various studies and conducted various tests.
In a cylindrical slurry tank, it has been found that by setting the cycle of the rotary cart and the cycle of the stirring blade within a certain range, it is possible to secure the pumping property for a long period of time while suppressing the required power. It was completed.

【0009】すなわち、本発明にかかるスラリーの貯蔵
方法は、円形部を底部とした円筒形のスラリータンク内
にスラリーを供給し、前記スラリータンクの円形の中心
に設置した回転軸から円の外周方向に延設された回転台
車を、15分以上3時間以下の周期で回転させ、前記回
転台車に遊星状に回転可能に取り付けられた単数または
複数の攪拌機に装着された攪拌翼を、0.01m/秒以
上1m/秒以下の周速で回転させることを特徴とする。
That is, in the method of storing slurry according to the present invention, the slurry is supplied into a cylindrical slurry tank having a circular portion at the bottom, and the slurry is supplied from a rotating shaft installed at the center of the circular shape of the slurry tank to the outer circumferential direction of the circle. Is rotated at a period of 15 minutes or more and 3 hours or less, and a stirring blade attached to one or a plurality of stirrers rotatably mounted in a planetary shape on the rotating carriage is 0.01 m in length. It is characterized by being rotated at a peripheral speed of not less than 1 m / s and not more than 1 m / s.

【0010】そして、本発明によれば、スラリーを長期
間圧送可能な性状に保ち、回転台車及び攪拌機の撹拌翼
を低速度で回転させて撹拌するため、運転動力を低く抑
えながらスラリーを貯蔵することができる。
According to the present invention, since the slurry is maintained in a state capable of being pumped for a long period of time and the rotating carriage and the stirring blades of the stirrer are rotated at low speed and stirred, the slurry is stored while the operating power is kept low. be able to.

【0011】上記方法によって、都市ごみ焼却場から発
生する飛灰のスラリーを貯蔵すると、焼却場ストーカー
炉等から発生する飛灰を水洗脱塩してセメント原料とし
て利用する際に、灰粒子と水分の分離を防ぎ、水洗脱塩
処理後の飛灰スラリーをポンプ圧送可能な性状のまま長
期間貯蔵することができる。
According to the above method, when the slurry of fly ash generated from the municipal waste incineration plant is stored, the fly ash generated from the stoker furnace etc. of the incineration plant is washed with water and desalted to be used as a cement raw material. The separation of water can be prevented, and the fly ash slurry after the water washing and desalting treatment can be stored for a long period of time while maintaining pumpable properties.

【0012】また、本発明にかかる飛灰スラリーの貯蔵
装置は、円形部を底部とした円筒形のスラリータンク
と、該スラリータンクの円形の中心に設置した回転軸を
軸として回転し、該軸から円の外周方向に延設された回
転台車と、該回転台車に遊星状に回転可能に取り付けら
れ、回転軸を中心に回転する攪拌翼を備えた単数または
複数の攪拌機とを備えるが、従来の湿式セメント製造工
程で使用されていたスラリーベースンのように圧縮空気
吹き込み設備も必要としないため、設備費を低く押さえ
ることもできる。
Further, the fly ash slurry storage device according to the present invention comprises a cylindrical slurry tank having a circular portion at the bottom and a rotary shaft installed at the center of the circular shape of the slurry tank. And a rotating carriage extending in the outer circumferential direction of a circle, and one or more agitators having stirring blades that are rotatably mounted in a planetary manner on the rotating carriage and rotate about a rotation axis. Unlike the slurry basin used in the wet cement production process of the above, no equipment for blowing compressed air is required, so that the equipment cost can be kept low.

【0013】[0013]

【発明の実施の形態】次に、本発明の実施の形態の具体
例を図面を参照しながら説明する。図1は、本発明にか
かるスラリーの貯蔵装置の一実施例を示し、この貯蔵装
置1は、大別して、円筒状のスラリータンク2と、スラ
リータンク2内で一定速度で回転する回転台車3と、回
転台車3に遊星状に回転可能に取り付けられるととも
に、回転可能な攪拌翼4aを備えた単数または複数の攪
拌機4とで構成される。
Next, a specific example of an embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows an embodiment of a slurry storage device according to the present invention. The storage device 1 is roughly divided into a cylindrical slurry tank 2 and a rotating truck 3 rotating at a constant speed in the slurry tank 2. And one or a plurality of stirrers 4 that are rotatably mounted in a planetary manner on the rotating carriage 3 and have rotatable stirring blades 4a.

【0014】スラリータンク2は、底部2aを円形部と
して全体が円筒形に形成される。スラリータンク2の側
壁2bの上部にはスラリーの供給口9が設けられ、底部
2aには排出口10が設けられる。
The whole slurry tank 2 is formed in a cylindrical shape with the bottom 2a being a circular portion. A slurry supply port 9 is provided at the top of the side wall 2b of the slurry tank 2, and a discharge port 10 is provided at the bottom 2a.

【0015】回転台車3は、スラリータンク2の円形の
中心に設置した回転軸5を軸として回転し、回転軸5か
ら円の外周方向に延設されている。
The rotary cart 3 rotates around a rotary shaft 5 installed at the center of the circular shape of the slurry tank 2 and extends from the rotary shaft 5 in the outer circumferential direction of the circle.

【0016】攪拌機4は、回転台車3に複数取り付けら
れ、回転軸4bを中心に回転する攪拌翼4aを備える。
撹拌翼4aは、例えば、図2に示すように、4本の平鋼
4cを上下方向に平行に延設し、これらの平鋼4cを3
本の水平部材4dで固定したものである。そして、図1
に示すように、攪拌機4全体が回転台車3の回転ととも
に遊星状に回転するとともに、撹拌翼4aが回転軸4b
の回りを自転する。尚、本実施例では、2つの攪拌機4
を設けたが、大型のスラリータンク2を使用する場合に
は、攪拌機の機械的強度を考慮し、3〜4つの攪拌機を
設けることもある。
The agitator 4 has a plurality of agitating blades 4a attached to the rotating carriage 3 and rotating about a rotating shaft 4b.
As shown in FIG. 2, for example, the stirring blade 4a extends four flat steels 4c in parallel in the vertical direction, and
It is fixed by four horizontal members 4d. And FIG.
As shown in FIG. 2, the whole of the stirrer 4 rotates in a planetary manner with the rotation of the rotary carriage 3, and the stirring blade 4a is rotated by a rotating shaft 4b.
Spin around. In this embodiment, two stirrers 4 are used.
However, when a large slurry tank 2 is used, three to four stirrers may be provided in consideration of the mechanical strength of the stirrer.

【0017】スラリータンク2の上方には、直射日光等
による水分の蒸発を押さえるため等の目的で屋根6が設
置される。スラリータンク2には、タンク内のスラリー
の水分を調整するための給水配管8が配設され、スラリ
ーの水分が蒸発した場合でも、水分を補給してスラリー
の粘度(攪拌動力)を適当な範囲に収めることができ
る。
A roof 6 is provided above the slurry tank 2 for the purpose of suppressing evaporation of water due to direct sunlight or the like. The slurry tank 2 is provided with a water supply pipe 8 for adjusting the water content of the slurry in the tank. Even when the water content of the slurry evaporates, the water is replenished to adjust the viscosity of the slurry (agitating power) within an appropriate range. Can be stored.

【0018】次に、上記構成を有するスラリーの貯蔵装
置の試験例として、都市ごみ焼却場から発生する飛灰の
スラリーを用い、この飛灰スラリーをポンプ圧送可能な
状態に保つ場合について説明する。
Next, as a test example of the slurry storage device having the above configuration, a case where a fly ash slurry generated from a municipal solid waste incineration plant is used and the fly ash slurry is maintained in a pumpable state will be described.

【0019】この飛灰には、都市ごみ焼却場のストーカ
ー炉から発生したものを使用し、飛灰を水洗脱塩して水
分50%程度のものをスラリーの供給口9から受け入れ
てスラリータンク(1.0m×2.6mΦ)2に貯蔵し
た。そして、スラリーの貯蔵装置1の回転台車3の周期
及び撹拌翼4aの周速を種々変化させ、飛灰スラリーの
水分(スラリータンク2内の平均水分)を45〜46%
に維持しながら1週間経過後、底部2aの排出口10か
らピストンポンプで圧送可能か否か試験した。
As the fly ash, a fly ash generated from a stoker furnace at an incinerator for municipal waste is used. The fly ash is washed and desalted, and a fly ash having a water content of about 50% is received from a slurry supply port 9 and fed to a slurry tank. (1.0m × 2.6mΦ) 2. Then, the cycle of the rotating cart 3 of the slurry storage device 1 and the peripheral speed of the stirring blades 4a are variously changed, and the water content of the fly ash slurry (average water content in the slurry tank 2) is 45 to 46%.
After a lapse of one week while maintaining the pressure, it was tested whether or not it could be pumped by the piston pump from the outlet 10 of the bottom 2a.

【0020】まず、最初に、撹拌翼4aの周速を0.1
m/秒に固定し、回転台車3の周期を、5分、15分、
30分、1時間、2時間、3時間、5時間と変化させて
ポンプで圧送可能か否か試験したところ、表1のような
結果となった。尚、表中の評価の欄に記載の記号は、
「○」がポンプによって圧送可能な場合、「×」が圧送
不可の場合を示す。この結果より、最長で3時間に1回
撹拌することにより飛灰スラリーの沈降・分離を防止で
きることが判る。回転台車3の周期が5時間の場合に
は、飛灰粒子と水分が分離して沈降し、沈降した飛灰粒
子によって輸送配管が閉塞して圧送できなくなる。
First, the peripheral speed of the stirring blade 4a is set to 0.1
m / sec, and the cycle of the rotating car 3 is 5 minutes, 15 minutes,
The results were as shown in Table 1 when it was tested whether the pumping was possible by changing the pressure to 30 minutes, 1 hour, 2 hours, 3 hours, and 5 hours. In addition, the symbol described in the column of evaluation in the table,
“O” indicates that the pumping is possible, and “X” indicates that the pumping is impossible. From this result, it can be understood that sedimentation / separation of the fly ash slurry can be prevented by stirring once every three hours at the maximum. If the cycle of the rotary cart 3 is 5 hours, fly ash particles and water separate and settle, and the settled fly ash particles block the transportation pipe and cannot be pumped.

【0021】[0021]

【表1】 [Table 1]

【0022】また、表1に示すように、回転台車3の周
期が3時間以下の場合には、飛灰スラリーの沈降・分離
を防止でき、ポンプによって圧送可能であるが、周期が
15分を下回ると、回転台車3の動力が急上昇するた
め、周期を15分以上とすることが好適である。
Further, as shown in Table 1, when the cycle of the rotary truck 3 is 3 hours or less, the settling and separation of the fly ash slurry can be prevented, and the pump can be pumped by a pump. If it falls below, the power of the rotating car 3 rises sharply. Therefore, it is preferable to set the cycle to 15 minutes or more.

【0023】次に、回転台車3の周期を1時間に固定
し、撹拌翼4aの周速を0.005m/秒、0.01m
/秒、0.1m/秒、1m/秒、3m/秒、5m/秒と
変化させてポンプで圧送可能か否か試験したところ、表
2のような結果となった。尚、表中の評価の欄に記載の
記号は、表1と同様の内容を意味する。
Next, the cycle of the rotating carriage 3 is fixed to one hour, and the peripheral speed of the stirring blade 4a is set to 0.005 m / sec and 0.01 m.
/ M, 0.1 m / s, 1 m / s, 3 m / s, and 5 m / s were tested to see if they could be pumped by the pump. The symbols described in the column of evaluation in the table mean the same contents as in Table 1.

【0024】[0024]

【表2】 [Table 2]

【0025】表2に示すように、撹拌翼4aの周速が
0.01m/秒以上の場合には、飛灰スラリーの沈降・
分離を防止でき、ポンプによって圧送可能であるが、周
速が1m/秒を越えると、撹拌機4の動力が急上昇する
ため、周速を0.01m/秒以上1m/秒以下とするこ
とが好適である。
As shown in Table 2, when the peripheral speed of the stirring blade 4a is 0.01 m / sec or more, the sedimentation of fly ash slurry
Separation can be prevented, and pumping can be performed by a pump. However, if the peripheral speed exceeds 1 m / sec, the power of the stirrer 4 rises sharply. Therefore, the peripheral speed is set to 0.01 m / sec or more and 1 m / sec or less. It is suitable.

【0026】更に、回転台車周期を1時間に、攪拌翼周
速を0.1m/秒に固定し、攪拌期間が1週間、1ヶ
月、2ヶ月、4ヶ月のそれぞれの時点で、台車動力およ
び攪拌動力を測定し、スラリーのポンプ圧送の可否を調
べた。その結果を表3に示す。攪拌期間が4ヶ月以内な
らば、台車動力、攪拌動力には大きな変化はなく、問題
なくスラリーをポンプ圧送可能であることがわかった。
Further, the cycle of the rotating bogie is fixed at one hour, the peripheral speed of the stirring blade is fixed at 0.1 m / sec, and the bogie power and the bogie power are set at one week, one month, two months, and four months, respectively. The stirring power was measured to determine whether the slurry could be pumped. Table 3 shows the results. If the stirring period was within 4 months, there was no significant change in the truck power and the stirring power, and it was found that the slurry could be pumped without any problem.

【0027】[0027]

【表3】 [Table 3]

【0028】尚、スラリーの性状及び貯蔵期間によって
は、回転台車3または撹拌翼4a、あるいはこれらの両
方を間欠的に運転することも可能であり、運転動力を更
に低く押さえることができる。
It should be noted that, depending on the properties of the slurry and the storage period, it is possible to intermittently operate the rotary cart 3 or the stirring blades 4a, or both, so that the driving power can be further reduced.

【0029】[0029]

【発明の効果】以上説明したように、本発明によれば、
運転動力及び設備費用を低く押さえながら、飛灰スラリ
ー等を長期間圧送可能な性状で貯蔵することができる。
As described above, according to the present invention,
Fly ash slurry and the like can be stored for long-term pumpability while keeping operating power and equipment costs low.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明にかかるスラリーの貯蔵装置の一実施例
を示す全体構成図である。
FIG. 1 is an overall configuration diagram showing an embodiment of a slurry storage device according to the present invention.

【図2】図1のスラリーの貯蔵装置の攪拌翼を示す図で
あって、(a)は正面図、(b)は側面図、(c)は上
面図である。
FIGS. 2A and 2B are views showing a stirring blade of the slurry storage device of FIG. 1, wherein FIG. 2A is a front view, FIG. 2B is a side view, and FIG.

【符号の説明】 1 スラリーの貯蔵装置 2 スラリータンク 2a 底部 2b 側壁 3 回転台車 4 攪拌機 4a 攪拌翼 4b 回転軸 4c 平鋼 4d 水平部材 5 回転軸 6 屋根 8 給水配管 9 供給口 10 排出口[Description of Signs] 1 Slurry storage device 2 Slurry tank 2a Bottom 2b Side wall 3 Rotating cart 4 Stirrer 4a Stirrer blade 4b Rotating shaft 4c Flat steel 4d Horizontal member 5 Rotating shaft 6 Roof 8 Water supply pipe 9 Supply port 10 Discharge port

───────────────────────────────────────────────────── フロントページの続き (72)発明者 深町 英司 埼玉県熊谷市大字三ヶ尻5378 太平洋セメ ント株式会社設備技術部技術開発センター 内 (72)発明者 岡村 聰一郎 埼玉県熊谷市大字三ヶ尻5378 太平洋セメ ント株式会社設備技術部技術開発センター 内 Fターム(参考) 3E070 AA02 AB04 FA08 RA01 VA05 WA05 4D059 AA30 BJ01 BK12 BK30 4G035 AB46 4G078 AA23 AB20 BA05 BA07 DA01 DB04  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Eiji Fukamachi 5378 Mikajiri, Kumagaya-shi, Saitama Pref. 3E070 AA02 AB04 FA08 RA01 VA05 WA05 4D059 AA30 BJ01 BK12 BK30 4G035 AB46 4G078 AA23 AB20 BA05 BA07 DA01 DB04

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 円形部を底部とした円筒形のスラリータ
ンク内にスラリーを供給し、 前記スラリータンクの円形の中心に設置した回転軸から
円の外周方向に延設された回転台車を、15分以上3時
間以下の周期で回転させ、 前記回転台車に遊星状に回転可能に取り付けられた単数
または複数の攪拌機に装着された攪拌翼を、0.01m
/秒以上1m/秒以下の周速で回転させることを特徴と
するスラリーの貯蔵方法。
1. A slurry is supplied into a cylindrical slurry tank having a circular portion as a bottom portion, and a rotary bogie extending from a rotary shaft installed at the center of the circular shape of the slurry tank in the outer peripheral direction of the circle is provided. Rotate at a cycle of not less than minutes and not more than 3 hours, and stirrers attached to one or more stirrers rotatably mounted in a planetary manner on the rotating carriage are 0.01 m
A method for storing a slurry, characterized in that the slurry is rotated at a peripheral speed of not less than 1 m / sec and not more than 1 m / sec.
【請求項2】 貯蔵されるスラリーが、都市ごみ焼却場
から発生する飛灰のスラリーであることを特徴とする請
求項1に記載のスラリーの貯蔵方法。
2. The method for storing slurry according to claim 1, wherein the slurry to be stored is a slurry of fly ash generated from a municipal waste incineration plant.
【請求項3】 円形部を底部とした円筒形のスラリータ
ンクと、 該スラリータンクの円形の中心に設置した回転軸を軸と
して回転し、該軸から円の外周方向に延設された回転台
車と、 該回転台車に遊星状に回転可能に取り付けられ、回転軸
を中心に回転する攪拌翼を備えた単数または複数の攪拌
機とを有する飛灰スラリーの貯蔵装置。
3. A cylindrical slurry tank having a circular portion as a bottom portion, and a rotary bogie rotating around an axis of rotation provided at the center of the circular shape of the slurry tank and extending from the axis in the outer circumferential direction of the circle. A fly ash slurry storage device comprising: one or more stirrers attached to the rotating carriage so as to be rotatable in a planetary manner and provided with stirring blades rotating about a rotation axis.
JP2001090750A 2001-03-27 2001-03-27 Slurry storage method and storage device Expired - Fee Related JP4181754B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001090750A JP4181754B2 (en) 2001-03-27 2001-03-27 Slurry storage method and storage device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001090750A JP4181754B2 (en) 2001-03-27 2001-03-27 Slurry storage method and storage device

Publications (2)

Publication Number Publication Date
JP2002282668A true JP2002282668A (en) 2002-10-02
JP4181754B2 JP4181754B2 (en) 2008-11-19

Family

ID=18945495

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001090750A Expired - Fee Related JP4181754B2 (en) 2001-03-27 2001-03-27 Slurry storage method and storage device

Country Status (1)

Country Link
JP (1) JP4181754B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102641706A (en) * 2012-04-28 2012-08-22 苏州市金翔钛设备有限公司 Vertical heating tank
EP4043112A1 (en) * 2021-02-12 2022-08-17 AIK Technik AG Extraction vessel for extracting recyclable compounds from ash

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102641706A (en) * 2012-04-28 2012-08-22 苏州市金翔钛设备有限公司 Vertical heating tank
EP4043112A1 (en) * 2021-02-12 2022-08-17 AIK Technik AG Extraction vessel for extracting recyclable compounds from ash

Also Published As

Publication number Publication date
JP4181754B2 (en) 2008-11-19

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