JPH04110104U - schizkner - Google Patents

schizkner

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Publication number
JPH04110104U
JPH04110104U JP363991U JP363991U JPH04110104U JP H04110104 U JPH04110104 U JP H04110104U JP 363991 U JP363991 U JP 363991U JP 363991 U JP363991 U JP 363991U JP H04110104 U JPH04110104 U JP H04110104U
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Prior art keywords
solid
separation tank
liquid
liquid separation
stock solution
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JP2540886Y2 (en
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俊幸 長沢
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株式会社長沢機械製作所
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Abstract

(57)【要約】 (修正有) 【目的】分離効率が高く、小型で大量の原液の処理が可
能で、無人で運転できかつ液の動揺の少ないシックナの
提供。 【構成】上方縁部がオーバフロー部4、そして下方中心
部がアンダーフロー部Kになっている固液分離槽に、分
散板と、放射状に中心部から外方へ延びた複数枚の垂直
沈降板21とを配置し、垂直沈降板は平面的に見て円弧
状に彎曲するように構成されている。
(57) [Summary] (with amendments) [Purpose] To provide a thickener that has high separation efficiency, is small in size, can process a large amount of stock solution, can be operated unattended, and has little disturbance of the solution. [Structure] A solid-liquid separation tank with an overflow part 4 at the upper edge and an underflow part K at the lower center includes a dispersion plate and a plurality of vertical settling plates extending radially outward from the center. 21, and the vertical settling plate is configured to be curved in an arc shape when viewed from above.

Description

【考案の詳細な説明】[Detailed explanation of the idea]

【0001】0001

【産業上の利用分野】[Industrial application field]

本考案は、固体と液体とを重力により分離するシックナーに関し、更に詳しく は上方縁部からは上澄み液がオーバフローとして、又下方の部分からは濃縮液が アンダーフローとして排出されるようになっている固液分離槽を備えたシックナ ーに関する。 This invention relates to a thickener that separates solids and liquids by gravity. The supernatant liquid overflows from the upper edge, and the concentrated liquid flows from the lower part. A thickener with a solid-liquid separation tank that is discharged as underflow. - related.

【0002】0002

【従来の技術】[Conventional technology]

固体と液体とを分離する装置としては、濾材により分離する装置、重力により 分離する装置、遠心力を利用して分離する装置等色々な装置が知られている。そ の中で重力により分離装置としてはシックナーが知られている。 Devices that separate solids and liquids include devices that separate using filter media, and devices that use gravity to separate solids and liquids. Various devices are known, such as devices for separating and devices for separating using centrifugal force. So Thickeners are known as gravity separation devices.

【0003】 シックナーは、周知のように円筒状の沈降槽と、その底部近く回転駆動可能に 設けられている掻き板とから概略構成されている。したがって、固体或いは固形 物を含んだ処理液を、沈降槽に供給すると、固形物は重力により沈降し、上澄み 液は結果的に上方部分に集まり、両者は分離される。そして上澄み液は、沈降槽 の上縁部からオーバフローとして、また沈降物は掻き板で中心部に集められ、ア ンダフローとして外部に排出される。0003 As is well known, the thickener has a cylindrical sedimentation tank that can be rotated near the bottom. It is generally composed of a scraping board provided. Therefore, solid or solid When the processing liquid containing solids is supplied to the sedimentation tank, the solids settle due to gravity and the supernatant The liquid eventually collects in the upper part and the two are separated. The supernatant liquid is then stored in a sedimentation tank. As overflow from the upper edge, the sediment is collected in the center by the scraping board and It is discharged outside as waste flow.

【0004】 食品加工装置としての固液分離すなわちシックナーも従来から知られている。 例えば製餡加工における分離装置も、沈降槽を有し、この槽内に原液を供給する と餡粒子は重力により沈降する。したがって、製品として餡を得ることができる 。0004 Solid-liquid separation or thickeners as food processing equipment are also known in the art. For example, separation equipment used in bean paste processing also has a sedimentation tank, into which the undiluted solution is supplied. and the bean paste particles settle due to gravity. Therefore, you can get bean paste as a product. .

【0005】[0005]

【考案が解決しようとする課題】[Problem that the idea aims to solve]

前述したようなシックナーは、重力により分離するので、動力を格別に必要と しない利点を有する。したがって、鉱山、土木関係の固液分離装置としては、現 在も多用されている。しかしながら色々な問題点もある。例えば分離効率が悪く 、処理量を増すためには沈降槽を大きくしなければならず、装置が大型化し屋内 には設置できなくなるという問題がある。また製餡用のシックナーにおいては、 溶存タンパクが餡粒子に挟まれて同時に沈降するので、3〜5回繰り返し処理し なければ、所望の製品例えばBrix 0.5%以下の製品を得ることができず 、非効率的で、また多量のさらし用の水を必要とする欠点もある。更には原液は 一般にポンプにより沈降槽に供給されるが、ポンプの脈動、或いは配管系の振動 が沈降槽に伝わり、処理液が揺動し、分離効率を低下させるという欠点もある。 Thickeners like the ones mentioned above separate due to gravity, so they require extra power. It has no advantage. Therefore, as a solid-liquid separator for mining and civil engineering, it is currently It is also frequently used. However, there are various problems. For example, separation efficiency is poor. In order to increase the throughput, the sedimentation tank must be made larger, and the equipment becomes larger and cannot be installed indoors. The problem is that it cannot be installed. In addition, in the thickener for making bean paste, Dissolved proteins are sandwiched between the bean paste particles and precipitate at the same time, so repeat the process 3 to 5 times. Without it, it is not possible to obtain the desired product, for example, a product with a Brix of 0.5% or less. However, it is inefficient and requires a large amount of water for exposure. Furthermore, the undiluted solution Generally, the water is supplied to the sedimentation tank by a pump, but the pulsation of the pump or the vibration of the piping system There is also the disadvantage that the liquid is transmitted to the sedimentation tank, causing the treated liquid to oscillate and reducing the separation efficiency.

【0006】 したがって、本考案は、分離効率が高く、小型で大量の原液或いはスラリーを 処理することができると共に、無人でも運転できるシックナーを提供することを 目的としている。更に具体的には、固液を分離する沈降槽にはポンプ等の振動が 伝わっても、槽内の液に乱れがなく、製餡加工用に適用されると、少量の水で所 望品位の餡を得ることができるシックナーを提供することを目的としている。[0006] Therefore, the present invention has high separation efficiency, is compact and can handle a large amount of stock solution or slurry. Our goal is to provide a thickener that can be used to process wastewater and to operate unattended. The purpose is More specifically, the settling tank that separates solid and liquid is subject to vibrations from pumps, etc. Even if water is transmitted, there is no disturbance to the liquid in the tank, and when applied to bean paste processing, it can be done with a small amount of water. The purpose of the present invention is to provide a thickener that can produce bean paste of desired quality.

【0007】[0007]

【課題を解決するための手段】[Means to solve the problem]

本考案は、上記目的を達成するために、上方縁部から上澄み液がオーバフロー として、又下方から濃縮液がアンダーフローとして排出されるようになっている 固液分離槽と、該分離槽の略中間部に配置され、処理される原液を4方に分散さ せる分散板と、前記固液分離槽の略中心部から外周部に向って放射状に配置され 、供給された原液を固液に分離する複数枚の垂直沈降板とからなり、前記固液分 離槽は略円錐形を呈し、その縮径された下端部に濃縮液排出用のノズルが接続さ れていると共に、前記垂直沈降板は、平面的にみて円弧状に1方向に彎曲するよ うに構成される。 In order to achieve the above purpose, the present invention is designed to prevent supernatant liquid from overflowing from the upper edge. Also, the concentrated liquid is discharged from below as an underflow. A solid-liquid separation tank and a tank located approximately in the middle of the separation tank to disperse the raw solution to be processed in four directions. a dispersion plate disposed radially from approximately the center of the solid-liquid separation tank toward the outer periphery; , consisting of a plurality of vertical sedimentation plates that separate the supplied stock solution into solid and liquid, and the solid-liquid fraction The separation tank has an approximately conical shape, and a nozzle for discharging the concentrated liquid is connected to its reduced diameter lower end. and the vertical settling plate is curved in one direction in an arc shape when viewed from above. It is composed of sea urchins.

【0008】 また本考案は、濃縮液排出用のノズルには、傾斜角が変更自在の排出管が接続 され、その傾斜角を変えることにより固液分離槽の水位が変えられると共に、複 数枚の垂直沈降板は前記固液分離槽から上方に引き上げ可能に構成される。[0008] In addition, in this invention, a discharge pipe whose inclination angle can be changed is connected to the nozzle for discharging the concentrated liquid. By changing the angle of inclination, the water level in the solid-liquid separation tank can be changed, and the Several vertical settling plates are configured to be able to be pulled upward from the solid-liquid separation tank.

【0009】[0009]

【作用】 本考案は、上記のように構成されているので、今処理する原液を連続的に固液 分離槽の略中心部に供給する。そうすると、原液は分散板により四方に分散され る。このとき、原液は垂直沈降板間に略均等に分配され、そして中心部から周縁 部へと流れる。[Effect] Since the present invention is configured as described above, the stock solution to be processed is continuously converted into solid-liquid. Supplied approximately to the center of the separation tank. Then, the stock solution is dispersed in all directions by the dispersion plate. Ru. At this time, the stock solution is distributed almost evenly between the vertical settling plates, and from the center to the periphery. flows to the department.

【0010】 ところで、本考案による垂直沈降板は平面的にみて円弧状に彎曲しているので 、原液が中心部から周縁部に流れるとき、流れ方向が変えられる。その結果比重 の大きい固形物は遠心力により垂直沈降板の表面の方へ集まり、液は相対的に他 面側に集まる。そして両者は分離される。0010 By the way, since the vertical settling plate according to the present invention is curved in an arc shape when viewed from above, , when the stock solution flows from the center to the periphery, the flow direction is changed. As a result, specific gravity Larger solids gather toward the surface of the vertical settling plate due to centrifugal force, and the liquid is relatively Gather on the side. The two are then separated.

【0011】 分離された固形物は重力により沈降し、下方のノズルから外部へ排出される。 一方上澄み液は固液分離槽の上方縁部からオーバフローとして外部へ同様に排出 される。[0011] The separated solids settle due to gravity and are discharged to the outside through a lower nozzle. On the other hand, the supernatant liquid is similarly discharged to the outside as overflow from the upper edge of the solid-liquid separation tank. be done.

【0012】 また、傾斜角が変更自在の排出管が接続され、その傾斜角を変えることにより 固液分離槽の水位が変えられると共に、複数枚の垂直沈降板は前記固液分離槽か ら上方に引き上げ可能に構成すれば、傾斜角が変更自在の排出管を備えているの で、前述の作用に加えて、排出管の角度を変えると、固液分離槽の水位或いはオ ーバフローとアンダーフローとの割合が変わる。また垂直沈降板を引き上げて、 固液分離槽の内部を洗浄することができる。0012 In addition, a discharge pipe whose inclination angle can be changed is connected, and by changing the inclination angle, While the water level of the solid-liquid separation tank is changed, the plurality of vertical settling plates are changed from the solid-liquid separation tank. If it is constructed so that it can be pulled upwards, it will have a discharge pipe whose inclination angle can be changed. In addition to the above-mentioned effects, changing the angle of the discharge pipe will change the water level or operating temperature of the solid-liquid separation tank. The ratio of overflow and underflow changes. Also, pull up the vertical settling plate, The inside of the solid-liquid separation tank can be cleaned.

【0013】[0013]

【実施例】【Example】

以下、本考案の1実施例を添付図面によって説明する。図1において1は固液 分離槽を示している。 Hereinafter, one embodiment of the present invention will be described with reference to the accompanying drawings. In Figure 1, 1 is solid liquid Separation tank is shown.

【0014】 固液分離槽1は、図に示されているように円筒部2と、円錐部3とから構成さ れ、その上方端部の外側には堰4が全周にわたって設けられている。そして堰は 全体的には一方に傾斜し、その下端部にオーバフロー排出管5が接続されている 。このようにして分離槽1の上方縁部はオーバフロー部となっている。[0014] The solid-liquid separation tank 1 is composed of a cylindrical part 2 and a conical part 3, as shown in the figure. A weir 4 is provided around the entire circumference on the outside of its upper end. and the weir The overall structure is inclined to one side, and an overflow discharge pipe 5 is connected to the lower end thereof. . In this way, the upper edge of the separation tank 1 serves as an overflow section.

【0015】 固液分離槽1の底部は、図示されているように、テーパ状に縮径され、その最 下端に濃縮液排出用のノズル6が接続され、このノズルにはレベラー三方コック 7を介して傾斜角が変更自在の排出管8が接続されている。[0015] As shown in the figure, the bottom of the solid-liquid separation tank 1 is tapered in diameter, and its most A nozzle 6 for discharging the concentrated liquid is connected to the lower end, and a leveler three-way cock is attached to this nozzle. A discharge pipe 8 whose inclination angle can be changed is connected via a pipe 7.

【0016】 原液を収容しているホッパ10は、分離槽2の上方位置に配置され、このホッ パからは原液供給管11が、固液分離槽1の略中心部まで延び、そして下方へ垂 下12している。このように供給管が垂直しているので原液が分離槽1に供給さ れても、分離槽内の液が揺動するようなことはない。[0016] A hopper 10 containing the stock solution is placed above the separation tank 2. A stock solution supply pipe 11 extends from the tank to approximately the center of the solid-liquid separation tank 1, and then hangs downward. I'm under 12. Since the supply pipe is vertical in this way, the stock solution is supplied to separation tank 1. The liquid in the separation tank will not fluctuate even if

【0017】 供給管11の垂下部の下端部13は、ベルマウス的に拡径されている。そして その直下に原液分散用の分散板15が、範囲H間を上下方向に調節自在に設けら れている。この分散板15は側面的に見て山形を呈し、この上に原液が供給され ると、原液を四方へ均等に分配する。[0017] The lower end 13 of the hanging portion of the supply pipe 11 is enlarged in diameter in a bell-mouthed manner. and A dispersion plate 15 for dispersing the stock solution is provided directly below the dispersion plate 15, which can be adjusted vertically between ranges H. It is. This dispersion plate 15 has a chevron shape when viewed from the side, and the stock solution is supplied onto this. Then, the stock solution is evenly distributed in all directions.

【0018】 固液分離槽1の上方縁部には、沈降板吊り下げ金具20が載置されるている。 そしてこの金具に複数枚の垂直沈降板21、21・・・が取り付けられている。 したがって、吊り下げ金具20を引き上げると垂直沈降板も分離槽から外部へ引 き上げられることになる。[0018] A settling plate hanging fitting 20 is placed on the upper edge of the solid-liquid separation tank 1 . A plurality of vertical settling plates 21, 21, . . . are attached to this metal fitting. Therefore, when the hanging bracket 20 is pulled up, the vertical settling plate is also pulled out from the separation tank. It will be lifted up.

【0019】 垂直沈降板21、21・・・は、図1、2に示されているように、分離槽1の 中心部分から円周方向に放射状に延び、側面的形状は分離槽1と略同じ形状をし 、分離槽の中間位置Bまで垂直に垂下している。しかしながら、平面的にみると 図2に示されているように、全ての垂直沈降板は同一方向に円弧状に彎曲してい る。なお図1中の符号50は高さ調節自在の脚を示している。[0019] The vertical settling plates 21, 21... are arranged in the separation tank 1 as shown in FIGS. It extends radially from the center in the circumferential direction, and has approximately the same side shape as separation tank 1. , hanging vertically to intermediate position B of the separation tank. However, if you look at it horizontally, As shown in Figure 2, all vertical settling plates are curved in an arc in the same direction. Ru. Note that the reference numeral 50 in FIG. 1 indicates a leg whose height is freely adjustable.

【0020】 次に上記実施例の作用について説明する。ホッパ10から処理すべき原液が連 続的に供給され、定常状態になっていると仮定する。原液は供給管11の垂下部 12から分散板15に向けて重力により供給される。したがって、本実施例によ ると、原液供給用のポンプ等による脈動はない。[0020] Next, the operation of the above embodiment will be explained. The raw solution to be processed is continuously conveyed from the hopper 10. Assume that it is continuously supplied and is in a steady state. The stock solution is in the hanging part of the supply pipe 11 12 toward the distribution plate 15 by gravity. Therefore, according to this example, Then, there is no pulsation caused by the pump for supplying the stock solution.

【0021】 供給された原液は、分散板15により四方へ分散され、そして分離槽1内を周 囲の方へ向って流れる。このとき、垂直沈降板21、21・・・は、彎曲してい るので原液は、沈降板により流れ方向が曲げられ、遠心力が働く。遠心力は比重 の大きい固形物Kにより強く作用するので、固形物は垂直沈降板の凹部側表面に 多く集まり、裏側には相対的に液が集まり両者は分離される。分離された固形物 Hはノズル6から排出管8及び曲管9を通って、例えば濾過袋へと排出される。 上澄み液は分離槽1の上方縁からオーバフローとして排出される。[0021] The supplied stock solution is dispersed in all directions by the dispersion plate 15 and circulated around the separation tank 1. It flows towards the surrounding area. At this time, the vertical settling plates 21, 21... are curved. As a result, the direction of flow of the stock solution is bent by the sedimentation plate, and centrifugal force is applied. Centrifugal force is specific gravity The solids K act more strongly on the large solids K, so the solids are pushed onto the surface of the concave side of the vertical settling plate. A large amount of liquid gathers on the back side, and the two are separated. separated solids H is discharged from the nozzle 6 through a discharge pipe 8 and a bent pipe 9, for example into a filter bag. The supernatant liquid is discharged from the upper edge of the separation tank 1 as an overflow.

【0022】 分離中の分離槽1の水位或いはオーバフローとアンダーフローとの割合は、図 3に示されているように排出管8の傾斜角度θを変えて、変更できる。また沈降 板吊り下げ金具20を吊り上げ、垂直沈降板21、21・・・を分離槽1から取 り出し、分離槽内を洗浄する。本実施例によると原液供給管11、分散板15も 同時に取り外すことができ、洗浄が容易であるので、衛生管理の厳しい食品加工 用のシックナーとして好適である。[0022] The water level of separation tank 1 during separation or the ratio of overflow and underflow is shown in the figure. This can be changed by changing the inclination angle θ of the discharge pipe 8 as shown in FIG. Also sedimentation Lift up the plate hanging bracket 20 and remove the vertical settling plates 21, 21... from the separation tank 1. Take it out and clean the inside of the separation tank. According to this embodiment, the stock solution supply pipe 11 and the dispersion plate 15 are also It can be removed at the same time and is easy to clean, making it ideal for food processing that requires strict hygiene control. It is suitable as a thickener for use.

【0023】[0023]

【考案の効果】[Effect of the idea]

以上のように本考案によると、上方縁部から上澄み液がオーバフローとして、 又下方から濃縮液がアンダーフローとして排出されるようになっている固液分離 槽と、該分離槽の略中間部には処理される原液を4方に分散させる分散板が設け られているので、処理される原液は四方に均等に分散される。このとき分散板は 固液分離槽の略中間部に配置されているので、分離槽内の液に乱れが生じるよう なこともない。また固液分離槽内には、略中心部から外周部に向って放射状に配 置され、供給された原液を固液に分離する複数枚の垂直沈降板が設けられ、該沈 降板は平面的にみて円弧状に彎曲しているので、これらの垂直沈降板で固液は効 率的に分離される。したがって、小さな分離槽で大量の原液を処理することがで きる。また原液は垂直沈降板で流れ方向が曲げられるので、例えば製餡加工用に 適用されると、溶存タンパクを餡粒子から効果的に分離することもできる。更に は垂直沈降板は固液分離槽の内部に設けられているので、これらの沈降板によっ て槽内の液体が揺動する現象も抑えられる。 As described above, according to the present invention, the supernatant liquid overflows from the upper edge. Also, solid-liquid separation in which concentrated liquid is discharged from below as an underflow. A dispersion plate is provided approximately in the middle of the tank and the separation tank to disperse the raw solution to be treated in four directions. The stock solution to be processed is evenly distributed in all directions. At this time, the dispersion plate is Since it is located approximately in the middle of the solid-liquid separation tank, it prevents turbulence from occurring in the liquid in the separation tank. Nothing. In addition, inside the solid-liquid separation tank, there are A plurality of vertical sedimentation plates are installed to separate the supplied stock solution into solid and liquid, and the sedimentation plate is Since the descending plates are curved in an arc shape when viewed from above, the solid-liquid is effectively absorbed by these vertical settling plates. efficiently separated. Therefore, a large amount of raw liquid can be processed in a small separation tank. Wear. In addition, the flow direction of the raw solution is bent by the vertical settling plate, so it can be used for example in bean paste manufacturing. When applied, dissolved proteins can also be effectively separated from the bean paste particles. Furthermore Since the vertical settling plates are installed inside the solid-liquid separation tank, the This also suppresses the phenomenon of the liquid in the tank fluctuating.

【0024】 請求項2記載の本考案によると、濃縮液排出用のノズルには、傾斜角が変更自 在の排出管が接続さているので、上記効果に加えて、排出管の傾斜角を変えるこ とにより固液分離槽の水位が変えられる。また垂直沈降板を引き上げて、分離槽 内を簡単に洗浄することができる。[0024] According to the present invention as set forth in claim 2, the nozzle for discharging the concentrated liquid has an inclination angle that can be changed automatically. Since the existing exhaust pipe is connected, in addition to the above effects, changing the inclination angle of the exhaust pipe is also possible. The water level in the solid-liquid separation tank is changed by Also, pull up the vertical settling plate and remove it from the separation tank. The inside can be easily cleaned.

【0025】 以上のように、種々の効果を有するので室内に設置する必要のある食品加工機 として、例えば、 1. 製餡、デンプン業界の水さらし工程。[0025] As mentioned above, food processing machines that have various effects need to be installed indoors. For example, 1. Water exposure process in the bean paste and starch industries.

【0026】 2. 豆腐業界に於ける上げ生地の上澄水分離、破損豆腐くずの回収。[0026] 2. Separation of supernatant water from raised dough and collection of damaged tofu scraps in the tofu industry.

【0027】 3. 廃水処理に於けるブロック状固液分離。[0027] 3. Block solid-liquid separation in wastewater treatment.

【0028】 4. 上水用沈砂池の連続化。[0028] 4. Continuation of grit basin for water supply.

【0029】 5. 米トギ工程の連続化、豆類洗浄工程に於ける浮遊きょう雑物の除去。等に 適用すると一層の効果を発揮する。[0029] 5. Continuation of the rice togi process and removal of floating impurities in the legume washing process. etc. It is even more effective when applied.

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

【図1】本考案の1実施例を示す側断面図。FIG. 1 is a side sectional view showing one embodiment of the present invention.

【図2】その一部を示す平面図。FIG. 2 is a plan view showing a part of it.

【図3】排出管の実施例を示す側面図。FIG. 3 is a side view showing an embodiment of the discharge pipe.

【符号の説明】[Explanation of symbols]

1・・・固液分離槽 2・・・円筒部 3・・・円錐部 4・・・堰 6・・・ノズル 8・・・排出管 15・・・分散板 20・・・沈降板吊り下げ金具 21・・・垂直沈降板 1...Solid-liquid separation tank 2...Cylindrical part 3... Conical part 4...Weir 6... Nozzle 8...Discharge pipe 15... Dispersion plate 20...Settlement board hanging metal fittings 21...Vertical settling plate

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 上方縁部から上澄み液がオーバフローと
して、又下方から濃縮液がアンダーフローとして排出さ
れるようになっている固液分離槽と、該分離槽の略中間
部に配置され、処理される原液を4方に分散させる分散
板と、前記固液分離槽の略中心部から外周部に向って放
射状に配置され、供給された原液を固液に分離する複数
枚の垂直沈降板とからなり、前記固液分離槽は略円錐形
を呈し、その縮径された下端部に濃縮液排出用のノズル
が接続されていると共に、前記垂直沈降板は、平面的に
みて円弧状に1方向に彎曲していることを特徴とするシ
ックナー。
1. A solid-liquid separation tank from which a supernatant liquid is discharged from an upper edge as an overflow and a concentrated liquid from a lower part as an underflow, and a solid-liquid separation tank disposed approximately in the middle of the separation tank, a dispersion plate that disperses the stock solution in four directions, and a plurality of vertical settling plates that are arranged radially from approximately the center of the solid-liquid separation tank toward the outer periphery and separate the supplied stock solution into solid and liquid. The solid-liquid separation tank has a substantially conical shape, and a nozzle for discharging the concentrated liquid is connected to its reduced diameter lower end, and the vertical settling plate has an arcuate shape when viewed from above. A thickener characterized by being curved in one direction.
【請求項2】 請求項1記載の濃縮液排出用のノズルに
は、傾斜角が変更自在の排出管が接続され、その傾斜角
を変えることにより固液分離槽の水位が変えられると共
に、複数枚の垂直沈降板は前記固液分離槽から上方に引
き上げ可能であることを特徴とするシックナー。
2. A discharge pipe whose inclination angle can be changed is connected to the concentrate discharge nozzle according to claim 1, and by changing the inclination angle, the water level of the solid-liquid separation tank can be changed. A thickener characterized in that the vertical settling plates can be pulled upward from the solid-liquid separation tank.
JP363991U 1991-02-04 1991-02-04 Thickener Expired - Lifetime JP2540886Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP363991U JP2540886Y2 (en) 1991-02-04 1991-02-04 Thickener

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP363991U JP2540886Y2 (en) 1991-02-04 1991-02-04 Thickener

Publications (2)

Publication Number Publication Date
JPH04110104U true JPH04110104U (en) 1992-09-24
JP2540886Y2 JP2540886Y2 (en) 1997-07-09

Family

ID=31898697

Family Applications (1)

Application Number Title Priority Date Filing Date
JP363991U Expired - Lifetime JP2540886Y2 (en) 1991-02-04 1991-02-04 Thickener

Country Status (1)

Country Link
JP (1) JP2540886Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8661869B2 (en) 2005-11-04 2014-03-04 Cyril Bath Company Stretch forming apparatus with supplemental heating and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8661869B2 (en) 2005-11-04 2014-03-04 Cyril Bath Company Stretch forming apparatus with supplemental heating and method

Also Published As

Publication number Publication date
JP2540886Y2 (en) 1997-07-09

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