JPS6233564A - Method and apparatus for treating contaminated grit - Google Patents
Method and apparatus for treating contaminated gritInfo
- Publication number
- JPS6233564A JPS6233564A JP17475585A JP17475585A JPS6233564A JP S6233564 A JPS6233564 A JP S6233564A JP 17475585 A JP17475585 A JP 17475585A JP 17475585 A JP17475585 A JP 17475585A JP S6233564 A JPS6233564 A JP S6233564A
- Authority
- JP
- Japan
- Prior art keywords
- separator
- water
- water surface
- grit
- sand
- 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.)
- Pending
Links
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ポンプ場や下水処理場における沈砂池などか
らの汚砂の処理方法とその装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method and apparatus for treating sludge from a settling basin in a pumping station or a sewage treatment plant.
近年、生活の向上に伴って、生活汚水中の粗大コミおよ
び有機分の割合が高くなってきている。In recent years, as lifestyles have improved, the proportion of coarse dust and organic components in domestic sewage has increased.
これに伴ってポンプ場または下水処理場の沈砂池におい
ても、比重の重い粗大ゴミならびにし渣を含む有機性の
ゴミ等の廃物類が沈殿し、沈砂池底部はヘドロ化する傾
向にある。Along with this, waste materials such as bulky garbage with a heavy specific gravity and organic garbage containing scum tend to settle in the settling basins of pumping stations or sewage treatment plants, and the bottom of the settling basins tends to turn into sludge.
いずれにしてもこの種のし渣を含む汚砂を、粗大ゴミお
よび有機性のゴミ分と、無機性の砂分とを分離処理する
必要がある。In any case, it is necessary to separate the dirty sand containing this type of sludge into bulky waste and organic waste and inorganic sand.
ちなみに汚水沈砂池−\の流入水中の成分を第7図に示
す。沈降性し渣と浮遊性し渣は便宜的に分類したもので
、両者は一般に同一視されている。Incidentally, the components of the inflow water from the sewage settling pond are shown in Figure 7. Sedimentary sludge and floating sludge are classified for convenience, and the two are generally regarded as the same.
そこで、従来、し渣を含む汚砂の処理に際して、これら
汚砂類をそのまま水切ホラ・ぞ−もしくはサンドベッド
に投入し、水を切るだけで排出する方法のほか、第6図
のように、沈砂池50の汚砂類を水と共にポンプ51に
よシサイクロ152に導水(上水または井水)を供給す
るとともに、曝気ブロア54から送入したエアによりエ
ア攪拌するか、あるいは機械攪拌により洗浄する方法を
一般に採っている。55は沈砂排出機である。Conventionally, when treating sludge containing sludge, there has been a method in which the sludge is simply thrown into a draining hole or sand bed and discharged by simply draining the water, as shown in Figure 6. The sludge in the settling tank 50 is washed with water by supplying water (tap water or well water) to the cyclone 152 by the pump 51, and by agitating with air sent from the aeration blower 54 or by mechanical agitation. method is generally adopted. 55 is a sand discharger.
しかし、前者の水切りのみの方法では、有機性の高い汚
砂の有機分がやがて腐敗し、悪臭やノ・工の発生をもた
らし、2次公害の原因となるとともに、市街地ではトラ
ックによる搬送が困難である。However, with the former method, which involves only draining water, the organic content of the highly organic sludge eventually decomposes, causing foul odors and dirt, causing secondary pollution, and is difficult to transport by truck in urban areas. It is.
この点、後者の方法は、上記問題が少いけれども、サイ
クロン52の出口や配管内において、し渣等により閉塞
するトラブルが頻繁に発生し、これを常時監視する作業
員が必要となシ、閉塞した場合には、配管を分解する必
要があり、維持管理上の大きなネックとなっている。一
方、汚砂洗浄槽では、ヘドロ水が約80%程度入ったし
渣を含む汚砂を洗浄するが、大量の清水を必要とし経済
的でないし、また希釈混合して余剰水中(オーバーフロ
ー水)に浮遊したし渣等から砂分を分離することができ
ず依然、洗浄砂中には40〜50%程度の微細廃物が除
去できずに残留し、完全な処理とは言い難い。しかも、
この方法は、設備全体をみても、処理効率に対する設備
費および運転費があまりにもかかり過ぎる。In this respect, although the latter method has fewer of the above-mentioned problems, troubles such as clogging with scum etc. frequently occur at the outlet of the cyclone 52 and inside the piping, and a worker is required to constantly monitor this. If a blockage occurs, the pipe must be disassembled, which poses a major bottleneck in maintenance and management. On the other hand, in the sludge cleaning tank, the sludge containing about 80% of the sludge water is washed, but it requires a large amount of fresh water and is not economical, and the excess water (overflow water) is diluted and mixed. It is not possible to separate the sand from the residue etc. floating in the washed sand, and about 40 to 50% of fine waste remains in the washed sand without being able to be removed, so it cannot be said that the treatment is complete. Moreover,
This method requires too much equipment cost and operating cost compared to processing efficiency, even when looking at the equipment as a whole.
そこで、本発明の目的は、処理効果が高く、しかる経済
的な処理方法とその装置を提供することにある。SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a highly effective and economical processing method and apparatus.
上記問題点を解決するための本第1発明法は、多数の透
孔を有する分離体を水面部分に実質的に水平方向に配置
し、この分離体へ上方からし渣を含む汚砂を投入し1.
前記分離体を水面下および水面上に交互に位置すべく上
下方向に振動させることを特徴とするものである。The first method of the present invention for solving the above-mentioned problems is to arrange a separator having a large number of through holes in a substantially horizontal direction on the water surface, and to feed dirty sand containing sludge from above into the separator. 1.
The separator is vibrated in the vertical direction so as to be alternately positioned below and above the water surface.
また第2発明法は、多数の透孔を有する分離体を処理槽
内の水面部分に実質的に水平方向に配置し、この分離体
へ上方からし渣を含む汚砂を投入し0.前記分離体を水
面下および水面上に交互に位置すべく上下方向に振動さ
せるとともに、処理槽の底部の沈砂排出手段と前記分離
体との間において実質的に水平方向へ水流を与え微細廃
物を水流に乗せて処理槽外へ排出することを特徴とする
ものである。In addition, in the second invention method, a separator having a large number of through holes is arranged substantially horizontally on the water surface in the treatment tank, and waste sand containing sludge is introduced into the separator from above. The separator is vibrated vertically so as to be positioned alternately below and above the water surface, and a water flow is applied in a substantially horizontal direction between the sediment discharge means at the bottom of the treatment tank and the separator to remove fine waste. It is characterized by being discharged out of the treatment tank along with the water flow.
さらに、本発明装置は、多数の透孔を有し水面部分に実
質的に水平方向に配置されかつし渣を含む汚砂を上方か
ら受ける分離体と、この分離体と水面下および水面上に
交互に位置すべく上下方向に振動させる振動手段と、前
記分離体の有効分離部分の周囲において分離体から下方
に延在し常に水没状態にあるスカート部とを備えたこと
を特徴とするものである。Further, the device of the present invention includes a separator having a large number of through holes and disposed substantially horizontally on the water surface and receiving sludge containing persimmons from above, and a separator that is connected to the separator, below the water surface and above the water surface. It is characterized by comprising vibrating means that vibrate in the vertical direction so as to be alternately positioned, and a skirt portion that extends downward from the separator around the effective separation portion of the separator and is always submerged in water. be.
本発明では、多数の透孔を有する分離体の一部または全
体が水面部分に配される。第2図のようにこの分離体3
を上下に振動させると、その振動に伴って透孔4a部分
において気泡Bi伴う水流Fが生じる。分離板4上のし
渣Nを含む汚砂S(第1図)は、分離板4が水面下に没
する過程で相対的に上昇する水流によってし渣Nを含む
汚砂Sが洗われ、特に気泡Bのエアリフト効果によって
効果的に洗われる。これによって、し渣Nと沈砂Sが分
離される。他方で分離板4が水没状態から水面上へ移行
する過程で、透孔4a部分の汚砂Sは、相対的に下降す
る水流全党け、このとき汚砂Sから分離された微細廃物
Mおよび砂分Slが水流と共に水中へ沈降するようにな
る。し渣Nは、径が大きくまたは粘着性があったシする
ため、分離板4上に残留し、たとえば分離板4端部から
排出される。In the present invention, part or all of the separator having a large number of through holes is placed on the water surface. As shown in Figure 2, this separated body 3
When it is vibrated up and down, a water flow F accompanied by bubbles Bi is generated in the through hole 4a portion due to the vibration. The filthy sand S containing sludge N on the separation plate 4 (FIG. 1) is washed away by a relatively rising water flow while the separation plate 4 is submerged under the water surface. In particular, the air lift effect of bubbles B effectively cleanses the skin. As a result, the residue N and the settled sand S are separated. On the other hand, in the process of the separation plate 4 moving from the submerged state to above the water surface, the filth S in the through-hole 4a part is moved by the entire relatively descending water flow, and at this time, the fine waste M and the filth separated from the filth S are The sand Sl begins to settle into the water along with the water flow. Since the residue N has a large diameter or is sticky, it remains on the separation plate 4 and is discharged from the end of the separation plate 4, for example.
第2発明によれば、分離体3下方において、たとえばノ
ズル13により水平方向の水流が与えられる。その結果
、第1図のように、分離板4の透孔4ai通って沈降す
る微細廃物Mおよび砂分S。According to the second invention, a horizontal water flow is applied below the separator 3 by, for example, the nozzle 13. As a result, as shown in FIG. 1, fine waste M and sand S settle through the through holes 4ai of the separation plate 4.
が水流を受ける。しかるに、砂分S1は比重が大きいの
で、処理槽1の底部にそのまま沈降するのに対して、微
細廃物Mは比重が小さいので、水流全党けると水流に同
伴して水流と共に槽外へ排出される。かくして粗大ゴミ
分のし渣Nと有機分が大部分の微細廃物Mと砂分S1と
が効率的に分離される。receives water flow. However, since the sand S1 has a high specific gravity, it settles as it is at the bottom of the treatment tank 1, whereas the fine waste M has a low specific gravity, so when the entire water flow is blown, it accompanies the water flow and is discharged out of the tank. be done. In this way, the coarse waste residue N, the fine waste M containing most of the organic content, and the sand S1 are efficiently separated.
また、本発明装置では、上記の振動による分離に当って
、スカート部5が形成されている。このスカート部5は
有効分離部分を区画し、分離体3を上下動させるときに
、上下方向の水流およびエアリフトを強める効果がある
。もし、スカート部5がないと、水流およびエアリフト
の効果は小さい。Further, in the device of the present invention, a skirt portion 5 is formed for the separation due to the vibration described above. This skirt portion 5 defines an effective separation area and has the effect of strengthening the vertical water flow and air lift when the separator 3 is moved up and down. If there is no skirt portion 5, the effects of water flow and air lift will be small.
以下本発明を図面に示す具体例によってさらに詳説する
。The present invention will be explained in more detail below with reference to specific examples shown in the drawings.
第1図において、■は処理槽で、その底壁は傾斜されて
おり、底壁に沿ってたとえばスクリューコンベア方式の
沈砂排出機2が設けられている。In FIG. 1, ``■'' is a processing tank, the bottom wall of which is inclined, and a sand settling and discharging machine 2 of, for example, a screw conveyor type is provided along the bottom wall.
処理槽1には、水Wが満たされており、その水面部分に
分離体3が設けられている。この分離体3は、底部に多
数の透孔4aを有し水平配置の分離板4を備えている。The treatment tank 1 is filled with water W, and a separator 3 is provided on the water surface. The separator 3 includes a horizontally arranged separator plate 4 having a large number of through holes 4a at the bottom.
分離板4の左方(第1図において)部分は左上方に傾斜
して水面上より浮き上っている。また、分離板4のほぼ
水平部分を囲んで下方にスカート部5が延在している。The left side (in FIG. 1) of the separation plate 4 is inclined upwardly to the left and floats above the water surface. Further, a skirt portion 5 extends downwardly surrounding a substantially horizontal portion of the separation plate 4.
し渣Nを含む汚砂Sは分離板4上への投入後、分離操作
を受けながら第1図左方へ移動するが滞留時間を長くす
るために、たとえば2枚の邪摩板6.6が汚砂Sの移動
方向に間隔を置いてそれと直交方向に配されている。7
は隔壁で、分離体3の周囲を区画しておシ、移送方向末
端を除くスカート部5はこの隔壁7と一体となっている
。After the dirty sand S containing residue N is placed on the separation plate 4, it moves to the left in FIG. 1 while being subjected to a separation operation. are arranged at intervals in the direction of movement of the dirty sand S and in a direction perpendicular thereto. 7
is a partition wall that partitions the periphery of the separator 3, and the skirt portion 5 except for the end in the transfer direction is integrated with this partition wall 7.
8は投入シュート、9は供給されたし渣Nを含む汚砂S
を巾方向(第1図紙面を貫く方向)に分散させるための
分散樋で、分離板4上の始端部上方に配置されている。8 is a feeding chute, 9 is supplied waste sand S containing residue N
This is a dispersion gutter for dispersing in the width direction (direction penetrating the plane of the paper in FIG. 1), and is disposed above the starting end on the separating plate 4.
かくして汚砂Sは、分離板4上の始端部に投入される。In this way, the dirty sand S is thrown into the starting end on the separation plate 4.
この投入の過程で、汚砂投入コンベア(後述)からのし
渣Nを含む原汚砂に対して洗浄ノズル10から洗浄水が
取水されるようになっている。ここで、し渣を含む原汚
砂は、沈砂池よシボ中ポンプにより多量の汚水と共に投
入してもよい。During this charging process, cleaning water is taken from the cleaning nozzle 10 for the raw dirty sand containing the residue N from the dirty sand input conveyor (described later). Here, the raw sludge containing sludge may be fed into the settling basin together with a large amount of sewage water by means of a mid-grain pump.
分離体3全体は、後述の振動装置により実質的に上下に
振動される。ここで、分離板4の水平部分は、振動に伴
って水面下および水面上に交互に位置すべき位置に予め
配置される。かかる振動に伴う操作によって、前記〔作
用〕の項で述べた原理によって、砂分S1および微細ゴ
ミやヘドロ分の微細廃物Mが分離板4の透孔4aから沈
降され、これと分離されたし渣Nは分離板4に沿って第
1図左方へ邪摩板6,6によりその移動速反が低下され
ながらi、H動する。分離板4の水平部分から傾斜部の
始端部に対向して洗浄ノズル11が設けられ、し渣Nに
対して洗浄水による洗浄が行なわれるようになっている
。洗浄されたし渣Nは、振動に関係なく常時大気中に位
置する水切部4bにおいて、上下振動による水切シ効来
が加えられた状態で水切りが行なわれ、水は槽1内に落
下し、 ゛水切り後のし渣Nは槽1外に近接配置され
た排出コンベア12によって排出される。゛
さて、透孔4aから水中に沈降する砂分S!および微細
廃物Mに対して、分離体3と沈砂排出機2との間にあっ
て、はぼ水平に水流を与えるべく、水平向きの微細廃物
用ノズル13が配置されている。このノズル13からは
、水またはエア、あるいは両者の混合体、さらには水に
代えてオゾン水艷
もしくは次無塩素酸ソーダ含有水などが噴射される。こ
れによって砂分Slは比重的に重いのでそのまま槽1の
底部へ落下するが軽い微細廃物Mはノズル13によって
生成された水流に乗って槽1の端部へ向い、仕切板工4
によって仕切られた流出トラフ15から槽1外へ排出さ
れる。The entire separator 3 is substantially vibrated up and down by a vibration device to be described later. Here, the horizontal portions of the separation plate 4 are arranged in advance at positions that should be alternately located below and above the water surface in response to vibrations. By the operation accompanied by such vibration, the sand S1 and the fine waste M such as fine dust and sludge are settled through the through holes 4a of the separation plate 4 and separated from them. The residue N moves along the separation plate 4 to the left in FIG. A cleaning nozzle 11 is provided from the horizontal portion of the separation plate 4 to face the starting end of the inclined portion, so that the residue N is cleaned with cleaning water. The washed residue N is drained in the draining section 4b, which is always located in the atmosphere regardless of vibration, with a draining effect due to vertical vibration added, and the water falls into the tank 1. ``The drained residue N is discharged by a discharge conveyor 12 disposed close to the outside of the tank 1.゛Now, the sand S that settles into the water from the hole 4a! A horizontally oriented fine waste nozzle 13 is arranged between the separator 3 and the sand settling/discharging machine 2 to apply a water flow almost horizontally to the fine waste M. From this nozzle 13, water or air, or a mixture of the two, or instead of water, ozone water, water containing sodium hypochlorite, or the like is injected. As a result, the sand Sl, which is heavy in specific gravity, falls directly to the bottom of the tank 1, but the light fine waste M rides on the water flow generated by the nozzle 13 and heads toward the end of the tank 1,
It is discharged to the outside of the tank 1 from an outflow trough 15 partitioned by.
槽底へ沈降した砂分S!は沈砂排出機2により掻き上げ
られながら槽外へ排出される。このとき、沈砂分にもな
お微細廃物Mが付着していることもあるので、最終洗浄
ノズルI6によって沈砂排出にしである。なお、第1図
のzlは分離体3上において分離ゾーン、z2はし液洗
浄ゾーン、z3は水切ゾーンである。Sand S that has settled to the bottom of the tank! is scraped up by the sand discharger 2 and discharged to the outside of the tank. At this time, the fine waste M may still be attached to the sediment, so the final cleaning nozzle I6 is used to discharge the sediment. In addition, zl in FIG. 1 is a separation zone on the separator 3, z2 is a removal liquid washing zone, and z3 is a draining zone.
第3図〜第5図は、処理装置の全体側図で、17は汚砂
投入コンベア、工8は加振機、工9はバネ、20は砂排
出口である。3 to 5 are side views of the entire processing apparatus, in which 17 is a dirty sand input conveyor, 8 is a vibrator, 9 is a spring, and 20 is a sand discharge port.
ところで、分離板4の材質としては金属、樹脂、繊維等
のものを用いることができ、その透孔はA?ンチ孔、コ
ニカル孔、網状、スリット状等の適宜のものとすること
ができる。その径は分離効率によって適切に選定される
が2〜101LIIが好ましい。By the way, the material of the separation plate 4 can be metal, resin, fiber, etc., and the through hole is A? It can be formed into an appropriate shape such as a punch hole, a conical hole, a net shape, or a slit shape. The diameter is appropriately selected depending on the separation efficiency, but preferably 2 to 101 LII.
分離板4の振巾tは片側当ジ3〜l0JEI程度が好ま
しい。スカート長は30〜80鵡、特に50〜60fi
が好ましい。また、邪摩板6に代えてS字状の連続する
行路によって滞留時間を取ることも可能である。The swing width t of the separating plate 4 is preferably about 3 to 10 JEI per side. Skirt length is 30-80mm, especially 50-60fi
is preferred. Further, in place of the jamming plate 6, it is also possible to take the residence time by using a continuous S-shaped path.
以上の通り、本発明によれば、粗大弁のし渣と有機分が
主体をなす微細廃物と砂分とに効果的に分離でき、まだ
運転上の閉塞等のトラブルが皆無となジ、さらに装置的
には一つの装置で分離を達成できるなどの利点がもたら
される。As described above, according to the present invention, coarse valve residue, fine waste mainly composed of organic components, and sand can be effectively separated, and there is no problem such as operational blockage. In terms of equipment, there are advantages such as separation can be achieved with one device.
第1図は本発明の概略説明図、第2図は分離原理の説明
図、第3図は本発明装置例の正面図、第′4図は平面図
、第5図は側面図、第6図は従来技術の説明図、第7図
は流入水中の成分の説明図である。
1・・・処理槽、2・・・沈砂排出機、3・・・分離体
、4・・・分離板、4a・・・透孔、5・・・スカート
部、12・・・排出コンベア、13・・・ノズル、15
・・・流出トラフ、S・・・汚砂、N・・・し渣、M・
・・微細廃物、St ・・・砂分、W・・・水。
第1図
第2図
第5図
第6図
第7図
手続補正書
昭和60449月5日
直Fig. 1 is a schematic explanatory diagram of the present invention, Fig. 2 is an explanatory diagram of the separation principle, Fig. 3 is a front view of an example of the device of the present invention, Fig. 4 is a plan view, Fig. 5 is a side view, and Fig. The figure is an explanatory diagram of the prior art, and FIG. 7 is an explanatory diagram of components in inflow water. DESCRIPTION OF SYMBOLS 1... Processing tank, 2... Sand discharger, 3... Separator, 4... Separation plate, 4a... Through hole, 5... Skirt part, 12... Discharge conveyor, 13... Nozzle, 15
... outflow trough, S... sewage, N... sludge, M.
...Fine waste, St...Sand, W...Water. Figure 1 Figure 2 Figure 5 Figure 6 Figure 7 Procedural amendments dated September 5, 1984
Claims (4)
水平方向に配置し、この分離体へ上方からし渣を含む汚
砂を投入し、前記分離体を水面下および水面上に交互に
位置すべく上下方向に振動させることを特徴とする汚砂
の処理方法。(1) A separator having a large number of perforations is arranged substantially horizontally on the water surface, sewage containing sludge is poured into the separator from above, and the separator is placed under and above the water surface. A method for disposing of dirty sand characterized by vibrating it in the vertical direction so as to alternately position it.
に実質的に水平方向に配置し、この分離体へ上方からし
渣を含む汚砂を投入し、前記分離体を水面下および水面
上に交互に位置すべく上下方向に振動させるとともに、
処理槽の底部の沈砂排出手段と前記分離体との間におい
て実質的に水平方向へ水流を与え微細廃物を水流に乗せ
て処理槽外へ排出することを特徴とする汚砂の処理方法
。(2) A separator having a large number of perforations is placed substantially horizontally on the water surface in the treatment tank, waste sand containing sludge is introduced into the separator from above, and the separator is placed under the water surface. and vibrate vertically to alternately position them on the water surface,
A method for treating sludge, comprising: applying a water flow in a substantially horizontal direction between the sediment discharging means at the bottom of the treatment tank and the separator, and discharging fine waste along with the water flow to the outside of the treatment tank.
配置されかつし渣を含む汚砂を上方から受ける分離体と
、この分離体を水面下および水面上に交互に位置すべく
上下方向に振動させる振動手段と、前記分離体の有効分
離部分の周囲において分離体から下方に延在し常に水没
状態にあるスカート部とを備えたことを特徴とする汚砂
の処理装置。(3) A separator that has a large number of holes and is placed substantially horizontally on the water surface and receives the waste sand containing residue from above, and this separator is placed alternately below and above the water surface. What is claimed is: 1. A device for treating dirty sand, comprising: vibrating means for vibrating vertically as much as possible, and a skirt portion extending downward from the separator around the effective separation portion of the separator and always being submerged in water.
分離体の有効分離部分から移行したし渣中の水分を除去
する水切部を有する特許請求の範囲第3項記載の汚砂の
処理装置。(4) Always present in the atmosphere at the horizontal end of the separator,
The waste sand processing apparatus according to claim 3, further comprising a drainage section for removing water in the residue transferred from the effective separation part of the separator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17475585A JPS6233564A (en) | 1985-08-08 | 1985-08-08 | Method and apparatus for treating contaminated grit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17475585A JPS6233564A (en) | 1985-08-08 | 1985-08-08 | Method and apparatus for treating contaminated grit |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6233564A true JPS6233564A (en) | 1987-02-13 |
Family
ID=15984114
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17475585A Pending JPS6233564A (en) | 1985-08-08 | 1985-08-08 | Method and apparatus for treating contaminated grit |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6233564A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5005041A (en) * | 1987-11-05 | 1991-04-02 | Canon Kabushiki Kaisha | Focus detecting apparatus having a plurality of focus detecting areas |
US5084723A (en) * | 1989-07-28 | 1992-01-28 | Olympus Optical Co., Ltd. | Focus detecting device |
JPH06170275A (en) * | 1992-12-09 | 1994-06-21 | Takashi Kawai | Sorting device of powder |
US5440367A (en) * | 1990-11-07 | 1995-08-08 | Canon Kabushiki Kaisha | Focus detecting apparatus provided with a plurality of detection fields |
JP2002136963A (en) * | 2000-11-01 | 2002-05-14 | Konoike Constr Ltd | Decontamination method for contaminated soil and separator used for it |
JP2009136846A (en) * | 2007-12-11 | 2009-06-25 | Kubota Corp | Particle treatment system and particle treatment method |
JP2009183915A (en) * | 2008-02-08 | 2009-08-20 | Kigaku To | Method of cleaning supercritical sand and sand product |
JP2011235275A (en) * | 2010-05-10 | 2011-11-24 | Sanei:Kk | Apparatus for separating sand-residue |
CN103240161A (en) * | 2013-04-24 | 2013-08-14 | 长春奥瑞投资管理有限公司 | Rubbish and water classifying and recycling system |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5836656A (en) * | 1981-08-26 | 1983-03-03 | Hitachi Plant Eng & Constr Co Ltd | Washing device for scum |
-
1985
- 1985-08-08 JP JP17475585A patent/JPS6233564A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5836656A (en) * | 1981-08-26 | 1983-03-03 | Hitachi Plant Eng & Constr Co Ltd | Washing device for scum |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5005041A (en) * | 1987-11-05 | 1991-04-02 | Canon Kabushiki Kaisha | Focus detecting apparatus having a plurality of focus detecting areas |
US5084723A (en) * | 1989-07-28 | 1992-01-28 | Olympus Optical Co., Ltd. | Focus detecting device |
US5440367A (en) * | 1990-11-07 | 1995-08-08 | Canon Kabushiki Kaisha | Focus detecting apparatus provided with a plurality of detection fields |
JPH06170275A (en) * | 1992-12-09 | 1994-06-21 | Takashi Kawai | Sorting device of powder |
JP2002136963A (en) * | 2000-11-01 | 2002-05-14 | Konoike Constr Ltd | Decontamination method for contaminated soil and separator used for it |
JP4646047B2 (en) * | 2000-11-01 | 2011-03-09 | 株式会社鴻池組 | Method for purifying contaminated soil and separation apparatus used therefor |
JP2009136846A (en) * | 2007-12-11 | 2009-06-25 | Kubota Corp | Particle treatment system and particle treatment method |
JP2009183915A (en) * | 2008-02-08 | 2009-08-20 | Kigaku To | Method of cleaning supercritical sand and sand product |
JP2011235275A (en) * | 2010-05-10 | 2011-11-24 | Sanei:Kk | Apparatus for separating sand-residue |
CN103240161A (en) * | 2013-04-24 | 2013-08-14 | 长春奥瑞投资管理有限公司 | Rubbish and water classifying and recycling system |
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