JP2011255257A - Centrifuge - Google Patents

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JP2011255257A
JP2011255257A JP2010129485A JP2010129485A JP2011255257A JP 2011255257 A JP2011255257 A JP 2011255257A JP 2010129485 A JP2010129485 A JP 2010129485A JP 2010129485 A JP2010129485 A JP 2010129485A JP 2011255257 A JP2011255257 A JP 2011255257A
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rotating body
lid
center
flow path
centrifuge
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Tetsuyuki Nakazato
哲之 中里
Kiyoji Kawanobe
喜代二 川延
Yoshiaki Takeuchi
善昭 竹内
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AMEROIDO NIPPON SERVICE SHA KK
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AMEROIDO NIPPON SERVICE SHA KK
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Abstract

PROBLEM TO BE SOLVED: To provide a centrifuge capable of separating a substantial amount, reducing time required for separation treatment, and saving space for installation.SOLUTION: The centrifuge 1 includes: a cylindrical rotating body 1021 comprising an adjustment cover body 1021a, an upper cover plate 1021b, a lower cover plate 1021c, a porous bottom plate 1021e having holes at or around the center, and a side plate 1021d, all of them having a common center; an inlet tube for a mixed solution 201 which introduce a mixed solution D from the top of the rotating body 1021; a disc-shaped shake-off plate 1023 which radially scatters (diffuses) the mixed solution D introduced through the inlet tube for the mixed solution 201; a flow tract for a light solution 303r which derives the light solution separated from the mixed solution D; a flow tract for a heavy solution 403r which derives the heavy solution separated from the mixed solution; a relative adjustment mechanism to adjust according to the difference in levels between light and heavy solutions; 6 porous straightening plates 1024 to improve separation efficiency of the mixed solution and the like.

Description

本願発明は、比重の異なる2種以上の混合液を、比重の軽い軽液と比重の重い重液とに分離する遠心分離機に関するものである。   The present invention relates to a centrifugal separator that separates two or more kinds of mixed liquids having different specific gravities into a light liquid having a low specific gravity and a heavy liquid having a high specific gravity.

従来、混合液の分離には様々な方式が利用されている。自然重力を利用する沈降又は沈殿方式もよく利用される分離方式であり、比重の異なる2種以上の混合液を、比重の軽い軽液と比重の重い重液とに分離する場合にも利用される。   Conventionally, various methods are used to separate a mixed solution. Sedimentation or precipitation using natural gravity is also a separation method that is often used to separate two or more mixed liquids with different specific gravity into light liquid with low specific gravity and heavy liquid with high specific gravity. The

なお、混合液の分離に沈降又は沈殿方式を利用した装置、設備又はシステムは数多く存在する。例えば、特開2001−190904である。   There are many devices, equipment, or systems that use a sedimentation or precipitation method to separate the mixed solution. For example, it is Unexamined-Japanese-Patent No. 2001-190904.

しかし、自然重力による沈降又は沈殿装置、設備又はシステムでは分離処理に時間がかかってしまい不便である。また、相当程度の分離処理量をまかなうためには広大な設置スペースを要する場合が多い。   However, the sedimentation or sedimentation apparatus, equipment or system by natural gravity is inconvenient because it takes time for the separation process. Further, in order to cover a considerable amount of separation processing, a large installation space is often required.

特開平2001−190904号公報JP-A-2001-190904

上述の様に、自然重力による沈降又は沈殿装置、設備又はシステムでは分離処理に時間がかかってしまう及び相当程度の分離処理量をまかなうためには広大な設置スペースを要するといった不都合がある。   As described above, the sedimentation or sedimentation apparatus, equipment, or system using natural gravity has a disadvantage that it takes time for the separation process and a large installation space is required to cover a considerable amount of separation process.

そこで、比重の異なる2種以上の混合液の分離処理装置であって、この不都合を解決する混合液の分離処理装置を提供することを課題とする。   Accordingly, it is an object of the present invention to provide a separation processing apparatus for two or more kinds of mixed liquids having different specific gravities, which can solve this problem.

本願発明は、上述の課題を解決するために、比重の異なる2種以上の混合液を回転体内に導入し、比重の軽い軽液と比重の重い重液とに分離する遠心分離機において、中心が共通する円形状の第一蓋体又は当該第一蓋体よりも上部に位置する第二蓋体と、中心部分又は中心付近に孔を有する有孔底面と、側面とで構成する円筒形状の回転体と、前記第一蓋体の下面に接合し、前記回転体の垂直軸心位置から半径方向に向けて設置する複数の仕切り羽根と、前記第一蓋体よりも下部に位置し、前記第一蓋体と平行、かつ、中心が共通する振切り板と、前記振切り板の上部近傍位置から前記第一蓋体又は第二蓋体及び筐体を貫通し、中心が前記回転体の垂直軸心位置である混合液導入管と、前記回転体の有孔底面と当該有孔底面よりもさらに下部に位置する底面基材との隙間に存在する軽液流路と、前記軽液流路と連通する軽液収容室と、前記第一蓋体又は第二蓋体のうち少なくとも上部に装備する蓋体に孔を設け、当該孔を流路の一部として構成する重液流路と、重液流路と連通する重液収容室と、前記第一蓋体又は第二蓋体のうち少なくとも上部に装備する蓋体の中心部分又は中心付近に設けた孔の前記回転体の垂直軸心に対する径方向の最外径と、前記回転体の有孔底面の中心部分又は中心付近に設けた孔の前記回転体の垂直軸心に対する径方向の最外径と、を相対的に調整する相対調整機構と、を有する遠心分離機を提供する。   In order to solve the above-mentioned problems, the present invention introduces a mixture of two or more different specific gravities into a rotating body and separates them into a light liquid with a low specific gravity and a heavy liquid with a high specific gravity. A cylindrical first lid having a common circular-shaped first lid or a second lid located above the first lid, a perforated bottom surface having a hole at or near the center, and a side surface. A rotating body, a plurality of partition blades that are bonded to the lower surface of the first lid body and are installed in a radial direction from a vertical axis position of the rotating body, and are positioned below the first lid body, A swing plate that is parallel to the first lid and has a common center, and passes through the first lid or the second lid and the housing from a position near the upper portion of the swing plate, and the center of the rotary body A mixed liquid introduction pipe which is a vertical axis position, a perforated bottom surface of the rotating body, and a lower part than the perforated bottom surface A light liquid flow path that exists in a gap with the bottom base material positioned; a light liquid storage chamber that communicates with the light liquid flow path; and a lid body that is provided at least in the first lid body or the second lid body. A heavy liquid flow path configured as a part of the flow path, a heavy liquid storage chamber communicating with the heavy liquid flow path, and at least an upper portion of the first lid body or the second lid body. The outermost diameter in the radial direction with respect to the vertical axis of the rotating body of the hole provided at or near the center of the lid to be equipped, and the hole provided at or near the center of the perforated bottom surface of the rotating body A centrifuge having a relative adjustment mechanism that relatively adjusts an outermost diameter in a radial direction with respect to a vertical axis of a rotating body is provided.

また、本願発明は、上述の課題を解決するために、比重の異なる2種以上の混合液を回転体内に導入し、比重の軽い軽液と比重の重い重液とに分離する遠心分離機において、中心が共通する円形状の第一蓋体又は当該第一蓋体よりも上部に位置する第二蓋体と、中心部分又は中心付近に孔を有する有孔底面と、側面とで構成する円筒形状の回転体と、前記第一蓋体の下面に接合し、前記回転体の垂直軸心位置から半径方向に向けて設置する複数の仕切り羽根と、前記第一蓋体よりも下部に位置し、前記第一蓋体と平行、かつ、中心が共通する振切り板と、前記振切り板の上部近傍位置から前記第一蓋体又は第二蓋体及び筐体を貫通し、中心が前記回転体の垂直軸心位置である混合液導入管と、前記回転体の有孔底面と当該有孔底面よりもさらに下部に位置する底面基材との隙間に存在する軽液流路と、前記軽液流路と連通する軽液収容室と、前記第一蓋体又は第二蓋体のうち少なくとも上部に装備する蓋体に孔を設け、当該孔を流路の一部として構成する重液流路と、重液流路と連通する重液収容室と、前記第一蓋体又は第二蓋体のうち少なくとも上部に装備する蓋体の中心部分又は中心付近に設けた孔の前記回転体の垂直軸心に対する径方向の最外径と、前記回転体の有孔底面の中心部分又は中心付近に設けた孔の前記回転体の垂直軸心に対する径方向の最外径と、を相対的に調整する相対調整機構と、を有し、さらに、前記振切り板よりも下部に位置し中心が前記回転体の垂直軸心位置であり、有孔で、かつ、円形状の整流板を複数有する遠心分離機を提供する。   Further, in order to solve the above-described problems, the present invention is a centrifugal separator that introduces two or more kinds of mixed liquids having different specific gravities into a rotating body and separates them into a light liquid having a low specific gravity and a heavy liquid having a high specific gravity. , A cylindrical first lid having a common center or a second lid positioned above the first lid, a perforated bottom surface having a hole at or near the center, and a side surface A rotary body having a shape, a plurality of partition blades that are joined to the lower surface of the first lid body and are installed in a radial direction from a vertical axis position of the rotary body, and are positioned below the first lid body. A swing plate that is parallel to the first lid and has a common center, and passes through the first lid or the second lid and the housing from a position near the top of the swing plate, and the center is the rotation A mixed liquid introduction pipe which is a vertical axis position of the body, a perforated bottom surface of the rotating body, and a perforated bottom surface of the rotating body. A light liquid flow path that exists in a gap with a bottom base material located at a lower part, a light liquid storage chamber that communicates with the light liquid flow path, and at least an upper part of the first lid or the second lid. Provided with a hole in the lid, a heavy liquid flow path configured as a part of the flow path, a heavy liquid storage chamber communicating with the heavy liquid flow path, and at least one of the first lid and the second lid The outermost diameter in the radial direction with respect to the vertical axis of the rotating body of the hole provided in the central part or near the center of the lid equipped on the upper part, and the hole provided in the central part or near the center of the perforated bottom surface of the rotating body A relative adjustment mechanism that relatively adjusts the outermost diameter in the radial direction with respect to the vertical axis of the rotating body of the rotating body, and is further positioned below the swing plate and the center of the rotating body Provided is a centrifuge having a plurality of circular rectifying plates at a vertical axis position and having a hole.

また、本願発明は、上述の課題を解決するために、比重の異なる2種以上の混合液を回転体内に導入し、比重の軽い軽液と比重の重い重液とに分離する遠心分離機において、中心が共通する円形状の第一蓋体又は当該第一蓋体よりも上部に位置する第二蓋体と、中心部分又は中心付近に孔を有する有孔底面と、側面とで構成する円筒形状の回転体と、前記第一蓋体の下面に接合し、前記回転体の垂直軸心位置から半径方向に向けて設置する複数の仕切り羽根と、前記第一蓋体よりも下部に位置し、前記第一蓋体と平行、かつ、中心が共通する振切り板と、前記振切り板の上部近傍位置から前記第一蓋体又は第二蓋体及び筐体を貫通し、中心が前記回転体の垂直軸心位置である混合液導入管と、前記回転体の有孔底面と当該有孔底面よりもさらに下部に位置する底面基材との隙間に存在する軽液流路と、前記軽液流路と連通する軽液収容室と、前記第一蓋体又は第二蓋体のうち少なくとも上部に装備する蓋体に孔を設け、当該孔を流路の一部として構成する重液流路と、重液流路と連通する重液収容室と、前記第一蓋体又は第二蓋体のうち少なくとも上部に装備する蓋体の中心部分又は中心付近に設けた孔の前記回転体の垂直軸心に対する径方向の最外径と、前記回転体の有孔底面の中心部分又は中心付近に設けた孔の前記回転体の垂直軸心に対する径方向の最外径と、を相対的に調整する相対調整機構と、を有し、さらに、前記回転体の底面の全面及び側面の全面又は一部面を覆う、底面と側面とで構成する円筒形状の第二回転体を有し、当該第二回転体の底面又は側面に軽液流路を構成し連通する孔を設けた遠心分離機を提供する。   Further, in order to solve the above-described problems, the present invention is a centrifugal separator that introduces two or more kinds of mixed liquids having different specific gravities into a rotating body and separates them into a light liquid having a low specific gravity and a heavy liquid having a high specific gravity. , A cylindrical first lid having a common center or a second lid positioned above the first lid, a perforated bottom surface having a hole at or near the center, and a side surface A rotary body having a shape, a plurality of partition blades that are joined to the lower surface of the first lid body and are installed in a radial direction from a vertical axis position of the rotary body, and are positioned below the first lid body. A swing plate that is parallel to the first lid and has a common center, and passes through the first lid or the second lid and the housing from a position near the top of the swing plate, and the center is the rotation A mixed liquid introduction pipe which is a vertical axis position of the body, a perforated bottom surface of the rotating body, and a perforated bottom surface of the rotating body. A light liquid flow path that exists in a gap with a bottom base material located at a lower part, a light liquid storage chamber that communicates with the light liquid flow path, and at least an upper part of the first lid or the second lid. Provided with a hole in the lid, a heavy liquid flow path configured as a part of the flow path, a heavy liquid storage chamber communicating with the heavy liquid flow path, and at least one of the first lid and the second lid The outermost diameter in the radial direction with respect to the vertical axis of the rotating body of the hole provided in the central part or near the center of the lid equipped on the upper part, and the hole provided in the central part or near the center of the perforated bottom surface of the rotating body A relative adjustment mechanism that relatively adjusts the outermost diameter in the radial direction with respect to the vertical axis of the rotating body, and further, the entire bottom surface and the entire or partial surface of the side surface of the rotating body. A cylindrical second rotating body composed of a bottom surface and a side surface is covered, and a light liquid passage is provided on the bottom surface or side surface of the second rotating body. Providing a centrifuge having a structure with communicating pores.

本願発明の遠心分離機は、比重の異なる2種以上の混合液の分離処理装置であって、相当程度の分離処理量をまかない、分離処理時間を短縮でき、さらに設置場所を省スペースにすることを可能とする。   The centrifuge of the present invention is a separation processing apparatus for two or more kinds of mixed liquids having different specific gravities, which does not cover a considerable amount of separation processing, shortens the separation processing time, and further saves installation space. Is possible.

また、本願発明の遠心分離機は、重液を回転体の上方から、軽液を回転体の下方から排出していることにより、回転体の下方に存在するベアリング寿命を延ばすこともできる。ミスト状の重液(水溶性液)が回転体の下方に存在するベアリングに進入し難くなるからである。   Moreover, the centrifuge of this invention can also extend the lifetime of the bearing which exists under a rotary body by discharging | emitting heavy liquid from the upper direction of a rotary body, and discharging | emitting light liquid from the lower part of a rotary body. This is because it is difficult for mist-like heavy liquid (water-soluble liquid) to enter the bearing existing below the rotating body.

また、分離効率が低くなる悪条件下でも、相当程度の分離処理量と分離処理時間とを保つことを可能とする。   Further, it is possible to maintain a considerable amount of separation processing and separation processing time even under adverse conditions in which the separation efficiency is low.

なお、分離効率が低くなる悪条件下とは、混合液の処理流量が大量になった場合(遠心力を受けている時間が短くなるから)や、混合液中に含まれる軽液と重液との比重差が少ない場合(遠心力における差が少ないから)や、混合液中に含まれる油の動粘度が高い場合(粘性が悪影響をあたえるから)等の条件下をいう。   In addition, the bad condition that the separation efficiency is low means that the processing flow rate of the mixed liquid becomes large (because the time during which the centrifugal force is applied is shortened), or the light liquid and heavy liquid contained in the mixed liquid. And the specific gravity difference is small (because the difference in centrifugal force is small), and the kinematic viscosity of the oil contained in the mixed liquid is high (because the viscosity has an adverse effect).

また、混合液に微粒又は微粉の固形成分が含まれる条件下において、回転体の内周面に付着堆積する固形成分の除去、清掃作業を向上させることを可能とする。   Further, it is possible to improve the removal and cleaning work of the solid component that adheres and accumulates on the inner peripheral surface of the rotating body under the condition that the mixed liquid contains a solid component of fine particles or fine powder.

図1は、遠心分離機の切断断面図である。FIG. 1 is a cross-sectional view of a centrifuge. 図2は、混合液分離部の回転体ユニットの説明図である。FIG. 2 is an explanatory diagram of a rotating body unit of the mixed liquid separation unit. 図3は、軽液流路及び重液流路の説明図である。FIG. 3 is an explanatory diagram of the light liquid flow path and the heavy liquid flow path. 図4は、整流板を有する構成の遠心分離機の切断断面図である。FIG. 4 is a cross-sectional view of a centrifuge having a configuration including a current plate. 図5は、整流板の平面図である。FIG. 5 is a plan view of the current plate. 図6は、第二回転体を有する構成の遠心分離機の切断断面図である。FIG. 6 is a cross-sectional view of a centrifuge having a second rotating body. 図7は、第二回転体を有する構成の遠心分離機における混合液分離部の説明図である。FIG. 7 is an explanatory diagram of a mixed liquid separation unit in a centrifugal separator having a second rotating body.

回転体内に油水混合液を導入し、遠心分離方式で油成分と水成分とに分離する遠心分離機として使用する。   An oil / water mixture is introduced into a rotating body and used as a centrifuge for separating oil and water components by a centrifugal separation method.

まずは、実施例1の遠心分離機の構成について、図1から図3に従い説明する。   First, the structure of the centrifuge of Example 1 is demonstrated according to FIGS. 1-3.

実施例1の遠心分離機(1)は、油水混合液を比重の軽い油成分と、比重の重い水成分とに遠心力により分離する混合液分離部(10)と、油水混合液を導入する混合液導入部(20)と、分離された油成分を導出する軽液導出部(30)と、分離された水成分を導出する重液導出部(40)とからなる。   The centrifugal separator (1) of Example 1 introduces a mixed liquid separation unit (10) that separates an oil / water mixture into an oil component having a low specific gravity and a water component having a high specific gravity by centrifugal force, and an oil / water mixture. The liquid mixture introducing unit (20), a light liquid deriving unit (30) for deriving the separated oil component, and a heavy liquid deriving unit (40) for deriving the separated water component.

混合液分離部(10)は、筐体(101)と、回転体ユニット(102)と、回転体ユニット駆動部(103)とからなる。   The mixed liquid separation unit (10) includes a casing (101), a rotating body unit (102), and a rotating body unit driving section (103).

回転体ユニット(102)は、中心が共通する円形状の下部蓋板(1021c)と、前記下部蓋板(1021c)よりも上部に位置する上部蓋板(1021b)と、前記上部蓋板(1021b)よりさらに上部に位置し、相対調整機構の役割を担う有孔調整蓋板(1021a)と、中心部分に孔を有する有孔底面(1021e)と、側面(1021d)とで構成する円筒形状の回転体(1021)と、前記下部蓋板(1021c)の下面に接合し、前記回転体(1021)の垂直軸心位置から半径方向に向けて設置する4枚の仕切り羽根(1022)と、前記下部蓋板(1021c)よりも下部に位置し前記下部蓋板(1021c)と平行、かつ、中心が共通する円形状の振切り板(1023)とからなる。   The rotating body unit (102) includes a circular lower lid plate (1021c) having a common center, an upper lid plate (1021b) positioned above the lower lid plate (1021c), and the upper lid plate (1021b). ) Is a cylindrical shape composed of a perforated adjustment cover plate (1021a), which has a role of a relative adjustment mechanism, a perforated bottom surface (1021e) having a hole in the central portion, and a side surface (1021d). A rotating body (1021), four partition blades (1022) that are joined to the lower surface of the lower lid plate (1021c) and are installed in a radial direction from a vertical axis position of the rotating body (1021); It consists of a circular swing plate (1023) located below the lower lid plate (1021c), parallel to the lower lid plate (1021c) and having a common center.

なお、相対調整機構の役割を、前記有孔調整蓋板(1021a)で担っているが、相対的な調整であるので、前記有孔調整蓋板(1021a)を装備することなく、前記上部蓋板(1021b)又は前記下部蓋板(1021c)のうち上部に装備する有孔蓋板の中心部分又は中心付近に設けた孔で担うことも可能であるし、また、前記回転体(1021)の有孔底面(1021e)の中心部分又は中心付近に設けた孔で担うことも可能である。   Although the perforated adjustment cover plate (1021a) plays a role of the relative adjustment mechanism, since it is a relative adjustment, the upper cover is not equipped with the perforated adjustment cover plate (1021a). It can be carried by a hole provided at or near the center of the perforated cover plate mounted on the upper part of the plate (1021b) or the lower cover plate (1021c), and the rotating body (1021) It can also be carried by a hole provided at or near the center of the perforated bottom surface (1021e).

なお、前記有孔調整蓋板(1021a)の孔形状及び大きさは、内径がφ158の円形状であるが、混合液の種類などに応じて適宜設計変更し得る。混合液の種類により軽液と重液との比重差が異なるためである。   The hole shape and size of the perforated adjustment cover plate (1021a) is a circular shape having an inner diameter of φ158, but can be appropriately changed in design according to the type of the mixed solution. This is because the specific gravity difference between the light liquid and the heavy liquid varies depending on the type of the mixed liquid.

なお、実際には内径がφ120〜φ170の有孔調整蓋板を複数枚用意しておき、混合液の種類に応じてより適切な有孔調整蓋板に交換して使用する。   In practice, a plurality of perforated adjustment cover plates having an inner diameter of φ120 to φ170 are prepared, and are replaced with a more suitable perforation adjustment cover plate according to the type of the mixed solution.

なお、前記下部蓋板(1021c)から前記回転体の底面(1021e)に向かう方向に、前記回転体の側面(1021d)に沿った隔壁(図示せず)を設けることもできる。   A partition wall (not shown) along the side surface (1021d) of the rotating body may be provided in a direction from the lower lid plate (1021c) toward the bottom surface (1021e) of the rotating body.

なお、前記下部蓋板(1021c)と、前記上部蓋板(1021b)及び前記有孔調整蓋板(1021a)とは、平行で、かつ、中心が共通する。   The lower cover plate (1021c), the upper cover plate (1021b), and the perforated adjustment cover plate (1021a) are parallel and have a common center.

なお、前記仕切り羽根(1022)相互間の角度は、90度であるが、前記仕切り羽根(1022)の枚数に応じて均一であればよい(例えば、2枚の場合は180度、3枚の場合は120度、8枚の場合は45度)。   The angle between the partition blades (1022) is 90 degrees, but may be uniform according to the number of the partition blades (1022) (for example, 180 degrees, 3 sheets in the case of two sheets). 120 degrees in the case, 45 degrees in the case of 8 sheets).

なお、前記仕切り羽根(1022)の枚数は、4枚に限られず、混合液の処理流量や混合液の動粘度や混合液の種類などにより適宜設計変更し得る。   The number of the partition blades (1022) is not limited to four, and the design can be appropriately changed depending on the processing flow rate of the mixed liquid, the kinematic viscosity of the mixed liquid, the type of the mixed liquid, and the like.

なお、前記振切り板(1023)の形状は、円形状であるが、混合液を振切り板(1023)に沿って相当程度飛散(拡散)させることができれば良く、適宜設計変更し得る   The shape of the shaking plate (1023) is circular, but it is sufficient that the mixed liquid can be scattered (diffused) along the shaking plate (1023), and the design can be changed as appropriate.

回転体ユニット駆動部(103)は、前記回転体ユニット(102)を回転させる動力源である駆動モータ(1031)と、前記駆動モータ(1031)の駆動軸の一端に挿入された駆動軸プーリ(1032)と、前記回転体ユニット(102)が結合された回転軸(1035)と、前記回転軸(1035)の一端に挿入された回転軸プーリ(1034)と、前記回転軸プーリ(1034)と前記駆動軸プーリ(1032)とを結合し前記駆動モータ(1031)の動力を伝達する伝達ベルト(1033)とからなる。   The rotator unit drive unit (103) includes a drive motor (1031) that is a power source for rotating the rotator unit (102), and a drive shaft pulley inserted into one end of the drive shaft of the drive motor (1031). 1032), a rotating shaft (1035) to which the rotating body unit (102) is coupled, a rotating shaft pulley (1034) inserted into one end of the rotating shaft (1035), and the rotating shaft pulley (1034). It comprises a transmission belt (1033) that is coupled to the drive shaft pulley (1032) and transmits the power of the drive motor (1031).

混合液導入部(20)は、前記振切り板(1023)の上部近傍位置から前記下部蓋板(1021c)、前記上部蓋板(1021b)、前記有孔調整蓋板(1021a)及び筐体(101)を貫通し、中心が前記回転体(1021)の垂直軸心位置である混合液導入管(201)からなる。   The mixed liquid introducing section (20) is arranged so that the lower cover plate (1021c), the upper cover plate (1021b), the perforated adjustment cover plate (1021a) and the casing (from the vicinity of the upper portion of the shaking plate (1023) 101), and a liquid mixture introduction pipe (201) whose center is the vertical axis position of the rotating body (1021).

軽液導出部(30)は、中心部分に孔を有する前記回転体の有孔底面(1021e)と、前記回転体の有孔底面(1021e)よりもさらに下部に位置する最下部底面(301)との隙間に存在する軽液流路(303r)と、前記軽液通路(303r)と連通する軽液収容室(304r)と、前記軽液収容室(304r)と連通する軽液排出管(305)とからなる。   The light liquid lead-out portion (30) has a perforated bottom surface (1021e) of the rotating body having a hole in a central portion, and a lowermost bottom surface (301) positioned further below the perforated bottom surface (1021e) of the rotating body. A light liquid flow path (303r) existing in the gap, a light liquid storage chamber (304r) communicating with the light liquid passage (303r), and a light liquid discharge pipe communicating with the light liquid storage chamber (304r) ( 305).

なお、前記回転体の有孔底面(1021e)の孔径及び孔形状は、内径がφ120の円形状であるが、軽液流路(303r)としての機能を果たせればよく、混合液の処理流量や混合液の動粘度や混合液の種類などにより適宜設計変更し得る。   In addition, although the hole diameter and hole shape of the perforated bottom surface (1021e) of the rotating body are circular with an inner diameter of φ120, it is sufficient that the function as a light liquid flow path (303r) can be achieved. In addition, the design can be changed as appropriate depending on the kinematic viscosity of the mixed solution, the kind of the mixed solution, and the like.

重液導出部(40)は、前記回転体(1021)の内周面を経由し、前記上部蓋板(1021b)の下面と前記下部蓋板(1021c)の上面との隙間を経由し、前記上部蓋板(1021b)の垂直軸心位置近傍から半径方向に設けた長孔を経由し、前記有孔調整蓋板(1021a)の下面と前記下部蓋板(1021c)の上面との隙間を経由し、前記有孔調整蓋板(1021a)の上面に到達する重液流路(403r)と、前記重液流路(403r)と連通する重液収容室(404r)と、前記重液収容室(404r)と連通する重液排出管(405)とからなる。   The heavy liquid outlet (40) passes through the inner peripheral surface of the rotating body (1021), passes through the gap between the lower surface of the upper lid plate (1021b) and the upper surface of the lower lid plate (1021c), and Via the long hole provided in the radial direction from the vicinity of the vertical axis position of the upper lid plate (1021b), via the gap between the lower surface of the perforated adjustment lid plate (1021a) and the upper surface of the lower lid plate (1021c) A heavy liquid flow path (403r) reaching the upper surface of the perforated adjustment lid plate (1021a), a heavy liquid storage chamber (404r) communicating with the heavy liquid flow path (403r), and the heavy liquid storage chamber (404r) and a heavy liquid discharge pipe (405).

なお、前記有孔調整蓋板(1021a)は、前記上部蓋板(1021b)の側面側の端部で接合され、前記上部蓋板(1021b)の垂直軸心位置近傍から半径方向に設けた長孔の一部を覆う位置で固定されている。   The perforated adjustment cover plate (1021a) is joined at the end of the upper cover plate (1021b) on the side surface, and is provided in a radial direction from the vicinity of the vertical axis position of the upper cover plate (1021b). It is fixed at a position covering a part of the hole.

次に、実施例1の遠心分離機(1)の動作ついて、比重0.75の油成分と水成分との混合液A(油成分6:水成分1の割合)を1分間に5リットルから60リットルの量を導入した場合を例に取り、図1から図3に従い説明する。   Next, regarding the operation of the centrifugal separator (1) of Example 1, a mixed liquid A (oil component 6: water component 1 ratio) of an oil component and a water component having a specific gravity of 0.75 is started from 5 liters per minute. The case where a volume of 60 liters is introduced will be described as an example with reference to FIGS.

駆動モータ(1031)の起動により、駆動モータ(1031)の駆動軸の一端に挿入された駆動軸プーリ(1032)が回転する。   When the drive motor (1031) is activated, the drive shaft pulley (1032) inserted into one end of the drive shaft of the drive motor (1031) rotates.

前記駆動軸プーリ(1032)が回転することにより、伝達ベルト(1033)を介して回転軸プーリ(1034)が回転する。   As the drive shaft pulley (1032) rotates, the rotation shaft pulley (1034) rotates via the transmission belt (1033).

前記回転軸プーリ(1034)が回転することにより、回転軸(1035)が回転する。   As the rotating shaft pulley (1034) rotates, the rotating shaft (1035) rotates.

前記回転軸(1035)が回転することにより、前記回転軸(1035)に連結された回転体(1021)が回転する。   As the rotating shaft (1035) rotates, the rotating body (1021) connected to the rotating shaft (1035) rotates.

なお、回転体(1021)の回転速度は、混合液の処理流量や混合液の動粘度や混合液の種類などにより適宜設計変更し得るものではあるが、2000rpm〜3000rpm程度を想定している。   The rotational speed of the rotating body (1021) can be appropriately changed depending on the processing flow rate of the mixed liquid, the kinematic viscosity of the mixed liquid, the type of the mixed liquid, and the like, but is assumed to be about 2000 rpm to 3000 rpm.

前記回転中の回転体(1021)内に混合液導入管(201)から混合液Aを導入すると混合液Aは、前記仕切り板(1023)の中心付近に放出され前記仕切り板(1023)に沿って放射状に飛散(拡散)する。   When the mixed liquid A is introduced from the mixed liquid introducing pipe (201) into the rotating body (1021) that is rotating, the mixed liquid A is discharged near the center of the partition plate (1023) and along the partition plate (1023). Scattered radially.

前記飛散(拡散)した混合液Aは、4枚の仕切り羽根(1022)により仕切られた空間に流れ落ちる。   The scattered (diffused) mixed liquid A flows down into a space partitioned by four partition blades (1022).

前記空間に流れ落ちた混合液Aは、遠心力により、以下のように分離される。   The mixed liquid A that has flowed down into the space is separated as follows by centrifugal force.

比重の重い水成分Cは前記回転体(1021)の内周面側に分離沈降する。   The water component C having a high specific gravity separates and settles on the inner peripheral surface side of the rotating body (1021).

比重の軽い油成分Bは分離沈降した水成分Cの上面側、すなわち前記回転体(1021)の軸心側に分離浮上する。   The oil component B having a light specific gravity separates and floats on the upper surface side of the separated and settled water component C, that is, on the axial center side of the rotating body (1021).

前記回転体(1021)の軸心側に分離浮上した油成分Bが、前記回転体の有孔底面(1021e)の孔位置(つまりφ120の位置)を超えると前記回転体(1021)内から溢れ出し、前記回転体の底面(1021e)と最下部底面(301)との隙間の軽液流路(303r)に導出される。   When the oil component B separated and floated on the axial center side of the rotating body (1021) exceeds the hole position (that is, the position of φ120) of the perforated bottom surface (1021e) of the rotating body, the oil overflows from the rotating body (1021). To the light liquid passage (303r) in the gap between the bottom surface (1021e) of the rotating body and the bottom bottom surface (301).

前記軽液流路(303r)に導出された油成分Bは、前記軽液流路(303r)と連通した軽液収容室(304r)へと導出される。   The oil component B led out to the light liquid channel (303r) is led out to the light liquid storage chamber (304r) communicating with the light liquid channel (303r).

前記軽液収容室(304r)へと導出された油成分Bは、前記軽液収容室(304r)と連通した軽液排出管(305)を介して遠心分離機(1)外に排出される。   The oil component B led out to the light liquid storage chamber (304r) is discharged out of the centrifuge (1) through the light liquid discharge pipe (305) communicating with the light liquid storage chamber (304r). .

一方、前記回転体(1021)の内周面側に分離沈降した水成分Cが、前記上部蓋板(1021b)の下面と前記下部蓋板(1021c)との隙間に到達すると、水成分Cの流れる方向は前記重液流路(403r)に沿って軸心側に変わる。   On the other hand, when the water component C separated and settled on the inner peripheral surface side of the rotating body (1021) reaches the gap between the lower surface of the upper lid plate (1021b) and the lower lid plate (1021c), The flowing direction changes to the axial side along the heavy liquid flow path (403r).

前記軸心側に流れた水成分Cが、前記上部蓋板(1021b)の長孔部分の位置を超えると前記有孔調整蓋板(1021a)の下面と前記下部蓋板(1021c)の上面との隙間に導出される。   When the water component C flowing to the axial center side exceeds the position of the long hole portion of the upper lid plate (1021b), the lower surface of the perforated adjustment lid plate (1021a) and the upper surface of the lower lid plate (1021c) It is derived in the gap.

前記有孔調整蓋板(1021a)の下面と前記下部蓋板(1021c)の上面との隙間に導出された水成分Cが、さらに前記有孔調整蓋板(1021a)の端部位置(つまりφ158の位置)を超えると前記有孔調整蓋板(1021a)の上面に沿って前記回転体(1021)から溢れ出し、重液流路(303r)と連通した重液収容室(404r)へと導出される。   The water component C introduced into the gap between the lower surface of the perforated adjustment lid plate (1021a) and the upper surface of the lower lid plate (1021c) is further positioned at the end of the perforated adjustment lid plate (1021a) (that is, φ158). ) Overflows from the rotating body (1021) along the upper surface of the perforated adjustment cover plate (1021a) and leads to the heavy liquid storage chamber (404r) communicating with the heavy liquid flow path (303r). Is done.

前記重液収容室(404r)へ導出された水成分Cは、前記重液収容室と連通した後重液排出管(405)を介して遠心分離機(1)外に排出される。   The water component C led to the heavy liquid storage chamber (404r) is discharged to the outside of the centrifuge (1) through the heavy liquid discharge pipe (405) after communicating with the heavy liquid storage chamber.

実施例2の遠心分離機(1)は、有孔で、かつ、円形状の整流板(1024)を複数の有する遠心分離機(1)である。   The centrifuge (1) of Example 2 is a centrifuge (1) having a plurality of perforated and circular rectifying plates (1024).

まずは、実施例2の遠心分離機(1)の構成について、図4及び図5に従い変更点のみを説明する。   First, only the changes in the configuration of the centrifuge (1) of Example 2 will be described with reference to FIGS.

回転体ユニット(102)は、中心が共通する円形状の下部蓋板(1021c)と、前記下部蓋板(1021c)よりも上部に位置する上部蓋板(1021b)と、前記上部蓋板(1021b)よりさらに上部に位置し、相対調整機構の役割を担う有孔調整蓋板(1021a)と、中心部分に孔を有する有孔底面(1021e)と、側面(1021d)とで構成する円筒形状の回転体(1021)と、前記下部蓋板(1021c)の下面に接合し、前記回転体(1021)の垂直軸心位置から半径方向に向けて設置する4枚の仕切り羽根(1022)と、前記下部蓋板(1021c)よりも下部に位置し前記下部蓋板(1021c)と平行、かつ、中心が共通する円形状の振切り板(1023)と、前記振切り板(1023)よりも下部に位置し中心が前記回転体(1012)の垂直軸心位置であり、有孔で、かつ、円形状の6枚の整流板(1024)とからなる。   The rotating body unit (102) includes a circular lower lid plate (1021c) having a common center, an upper lid plate (1021b) positioned above the lower lid plate (1021c), and the upper lid plate (1021b). ) Is a cylindrical shape composed of a perforated adjustment cover plate (1021a), which has a role of a relative adjustment mechanism, a perforated bottom surface (1021e) having a hole in the central portion, and a side surface (1021d). A rotating body (1021), four partition blades (1022) that are joined to the lower surface of the lower lid plate (1021c) and are installed in a radial direction from a vertical axis position of the rotating body (1021); A circular swing plate (1023) located below the lower cover plate (1021c), parallel to the lower cover plate (1021c) and having a common center, and below the swing plate (1023) Place And the center is perpendicular axis position of the rotating body (1012), in perforated and consists a circular six rectifying plates (1024).

なお、前記整流板(1024)の孔形状及び孔個数は、同一形状の角丸三角孔(図5)を4孔設けているが、混合液の処理流量や混合液の動粘度や混合液の種類などにより適宜設計変更し得る。   In addition, although the hole shape and the number of holes of the rectifying plate (1024) are provided with four rounded triangular holes having the same shape (FIG. 5), the processing flow rate of the mixed liquid, the kinematic viscosity of the mixed liquid, and the mixed liquid The design can be changed as appropriate depending on the type.

なお、前記整流板(1024)の枚数は、6枚装備しているが、混合液の処理流量や混合液の動粘度や混合液の種類などにより適宜設計変更し得る。   The number of the current plates (1024) is six, but the design can be appropriately changed depending on the processing flow rate of the mixed solution, the kinematic viscosity of the mixed solution, the type of the mixed solution, and the like.

なお、前記整流板(1024)相互間の間隔は、同じ隙間になっていればよく、混合液の処理流量や混合液の動粘度や混合液の種類などにより適宜設計変更し得る。   In addition, the space | interval between the said baffle plates (1024) should just become the same clearance gap, and can change a design suitably according to the process flow rate of liquid mixture, the kinematic viscosity of liquid mixture, the kind of liquid mixture, etc.

なお、前記整流板(1024)の傾きは、前記振切り板(1023)と平行であるが、混合液の処理流量や混合液の動粘度や混合液の種類などにより適宜設計変更し得る。   The inclination of the rectifying plate (1024) is parallel to the shaking plate (1023), but the design can be appropriately changed depending on the processing flow rate of the mixed liquid, the kinematic viscosity of the mixed liquid, the type of the mixed liquid, and the like.

次に、実施例2の遠心分離機(1)の動作について、混合液中に含まれる軽液と重液との比重差が少ない場合を例に取り、図4に従い説明する。   Next, the operation of the centrifuge (1) according to the second embodiment will be described with reference to FIG. 4, taking as an example a case where the specific gravity difference between the light liquid and the heavy liquid contained in the mixed liquid is small.

駆動モータ(1031)を起動し回転中の前記回転体(1021)内に、混合液導入管(201)から混合液Dを導入する。   The drive motor (1031) is started and the mixed solution D is introduced into the rotating body (1021) that is rotating from the mixed solution introduction pipe (201).

前記回転中の回転体(1021)内に前記混合液導入管(201)から前記混合液Dを導入すると前記混合液Dは、前記仕切り板(1023)の中心付近に放出され前記仕切り板(1023)に沿って放射状に飛散(拡散)する。   When the mixed solution D is introduced into the rotating rotating body (1021) from the mixed solution introducing pipe (201), the mixed solution D is discharged near the center of the partition plate (1023) and the partition plate (1023). ) To radiate (diffuse) radially.

前記飛散(拡散)した混合液Dは、4枚の仕切り羽根(1022)により仕切られた空間に流れ落ちる。   The scattered (diffused) mixed liquid D flows down into a space partitioned by four partition blades (1022).

前記空間に流れ落ちた混合液D中に含まれる軽液成分Eは、前記整流板(1024)の上面に沿って前記回転体(1021)の軸心側に分離浮上する。   The light liquid component E contained in the mixed liquid D flowing down into the space separates and floats along the upper surface of the rectifying plate (1024) toward the axis of the rotating body (1021).

前記回転体(1021)の軸心側に分離浮上した軽液成分Eが、前記整流板(1024)の孔位置を超え、さらに前記回転体の有孔底面(1021e)の孔位置(つまりφ120の位置)を超えると前記回転体(1021)から溢れ出し、軽液流路(303r)に導出される。   The light liquid component E separated and floated on the axial center side of the rotating body (1021) exceeds the hole position of the rectifying plate (1024), and further the hole position of the perforated bottom surface (1021e) of the rotating body (that is, φ120 If it exceeds the position, it overflows from the rotating body (1021) and is led out to the light liquid flow path (303r).

なお、前記整流板(1024)を装備することにより、前記整流板(1024)相互間の各層に平均して遠心力が作用し、また、前記整流板(1024)の面に液体が沿うことで油水の抵抗差から分離性を促進する。   In addition, by providing the current plate (1024), an average centrifugal force acts on each layer between the current plates (1024), and liquid flows along the surface of the current plate (1024). Promotes separability from the difference in resistance between oil and water.

前記軽液流路(303r)に達した軽液及び前記回転体(1021)の内周面側に分離沈降した重液のその後の動作については、実施例1の遠心分離機と同様であるので省略する。   The subsequent operation of the light liquid reaching the light liquid flow path (303r) and the heavy liquid separated and settled on the inner peripheral surface side of the rotating body (1021) is the same as that of the centrifuge of the first embodiment. Omitted.

実施例3の遠心分離機(1)は、円筒形状の外回転体(1025)を有する遠心分離機(1)である。   The centrifuge (1) of Example 3 is a centrifuge (1) having a cylindrical outer rotating body (1025).

まずは、実施例3の遠心分離機(1)の構成について、図5及び図6に従い変更点のみを説明する。   First, only the changes in the configuration of the centrifuge (1) of Example 3 will be described with reference to FIGS.

回転体ユニット(102)は、中心が共通する円形状の下部蓋板(1021c)と、前記下部蓋板(1021c)よりも上部に位置する上部蓋板(1021b)と、前記上部蓋板(1021b)よりさらに上部に位置し、相対調整機構の役割を担う有孔調整蓋板(1021a)と、中心部分に孔を有する有孔底面(1021e)と、側面(1021d)とで構成する円筒形状の回転体(1021)と、前記下部蓋板(1021c)の下面に接合し、前記回転体(1021)の垂直軸心位置から半径方向に向けて設置する4枚の仕切り羽根(1022)と、前記下部蓋板(1021c)よりも下部に位置し前記下部蓋板(1021c)と平行、かつ、中心が共通する円形状の振切り板(1023)と、前記回転体の有孔底面(1021e)の全面及び側面(1021d)の全面又は一部面を覆う、底面(1025e)と側面(1025d)とで構成する有孔で、かつ、円筒形状の外回転体(1025)と、前記回転体(1021)と前記外回転体(1025)とを結合する結合ネジ(1026)とからなる。   The rotating body unit (102) includes a circular lower lid plate (1021c) having a common center, an upper lid plate (1021b) positioned above the lower lid plate (1021c), and the upper lid plate (1021b). ) Is a cylindrical shape composed of a perforated adjustment cover plate (1021a), which has a role of a relative adjustment mechanism, a perforated bottom surface (1021e) having a hole in the central portion, and a side surface (1021d). A rotating body (1021), four partition blades (1022) that are joined to the lower surface of the lower lid plate (1021c) and are installed in a radial direction from a vertical axis position of the rotating body (1021); A circular swing plate (1023) located below the lower lid plate (1021c), parallel to the lower lid plate (1021c) and having a common center, and a perforated bottom surface (1021e) of the rotating body all A cylindrical outer rotating body (1025) having a bottom surface (1025e) and a side surface (1025d) covering the entire surface or part of the side surface (1021d), and the rotating body (1021). And a connecting screw (1026) for connecting the outer rotating body (1025).

前記外回転体(1025)に設けている前記軽液流路(303r)を構成し連通する孔は、前記外回転体の底面(1025e)の側縁部近傍位置に設けているが、軽液収容室(304r)に連通していればよく、前記外回転体の側面(1025d)の底縁部近傍位置などに設けてもよい。   The holes constituting and communicating with the light liquid flow path (303r) provided in the outer rotating body (1025) are provided in the vicinity of the side edge portion of the bottom surface (1025e) of the outer rotating body. It only needs to communicate with the storage chamber (304r), and may be provided near the bottom edge of the side surface (1025d) of the outer rotating body.

実施例3の遠心分離機(1)の清掃時の動作について、図7に従い説明する。   The operation at the time of cleaning of the centrifuge (1) of Example 3 will be described with reference to FIG.

混合液に微粒又は微粉の固形成分が含まれる場合、混合液に混在した固形成分は、遠心力により、前記回転体(1021)の内周面側に付着堆積する。   When the mixed solution contains a solid component of fine particles or fine powder, the solid component mixed in the mixed solution adheres and accumulates on the inner peripheral surface side of the rotating body (1021) by centrifugal force.

前記回転体(1021)の内周面側に付着堆積した固形成分を除去、清掃するため、前記駆動モータ(1031)を停止し、前記結合ネジ(1026)を緩めて取り外し、前記回転体(1021)を前記外回転体(1025)から取り外す。   In order to remove and clean the solid components adhered and accumulated on the inner peripheral surface side of the rotating body (1021), the drive motor (1031) is stopped, the coupling screw (1026) is loosened and removed, and the rotating body (1021) is removed. ) Is removed from the outer rotating body (1025).

取り外した前記回転体(1021)の内周面を清掃又は洗浄する。   The inner peripheral surface of the removed rotating body (1021) is cleaned or washed.

なお、清掃又は洗浄後は、前記回転体(1021)を前記外回転体(1025)に取り付け、前記結合ネジ(1026)を締めて前記回転体(1021)を前記外回転体(1025)に固定する。   After cleaning or washing, the rotating body (1021) is attached to the outer rotating body (1025), and the coupling screw (1026) is tightened to fix the rotating body (1021) to the outer rotating body (1025). To do.

次に、遠心分離中の軽液成分の軽液流路(303r)内での動作について、図6に従い説明する。   Next, the operation of the light liquid component during centrifugation in the light liquid channel (303r) will be described with reference to FIG.

前記4枚の仕切り羽根(1022)により仕切られた空間に流れ落ちた混合液中に含まれる軽液成分は、前記回転体(1021)の軸心側に分離浮上する。   The light liquid component contained in the mixed liquid that has flowed down into the space partitioned by the four partition blades (1022) separates and floats on the axial center side of the rotating body (1021).

前記回転体(1021)の軸心側に分離浮上した軽液成分が、前記回転体の有孔底面(1021e)の孔位置(つまりφ120の位置)を超えると前記回転体(1021)から溢れ出し、前記回転体の有孔底面(1021e)と前記外回転体の底面(1025e)との隙間の軽液流路(303r)に導出される。   When the light liquid component separated and floated on the axial center side of the rotating body (1021) exceeds the hole position (that is, the position of φ120) of the perforated bottom surface (1021e) of the rotating body, it overflows from the rotating body (1021). , And is led to a light liquid flow path (303r) in a gap between the perforated bottom surface (1021e) of the rotating body and the bottom surface (1025e) of the outer rotating body.

前記軽液流路(303r)に導出された軽液成分は、前記軽液流路(303r)と連通した軽液収容室(304r)へと導出される。   The light liquid component led to the light liquid flow path (303r) is led to the light liquid storage chamber (304r) communicating with the light liquid flow path (303r).

前記軽液収容室(304r)へと導出された軽液成分は、前記軽液収容室(304r)と連通した軽液排出管(305)を介して遠心分離機(1)外に排出される。   The light liquid component led out to the light liquid storage chamber (304r) is discharged out of the centrifuge (1) through the light liquid discharge pipe (305) communicating with the light liquid storage chamber (304r). .

前記軽液収容室(304r)へ導出された軽液及び前記回転体(1021)の内周面側に分離沈降した重液のその後の動作については、実施例1の遠心分離機と同様であるので省略する。   The subsequent operation of the light liquid led out to the light liquid storage chamber (304r) and the heavy liquid separated and settled on the inner peripheral surface side of the rotating body (1021) is the same as that of the centrifuge of the first embodiment. I will omit it.

本願発明の遠心分離機は、比重の異なる2種以上の混合液の分離処理装置であって、相当程度の分離処理量をまかない、分離処理時間を短縮でき、さらに設置場所を省スペースにすることを可能とするため、処理効率及び運用効率を飛躍的に向上させる装置であるので、産業上の利用性を有する。   The centrifuge of the present invention is a separation processing apparatus for two or more kinds of mixed liquids having different specific gravities, which does not cover a considerable amount of separation processing, shortens the separation processing time, and further saves installation space. Therefore, it is an apparatus that dramatically improves processing efficiency and operational efficiency, and thus has industrial applicability.

1 遠心分離機
10 混合液分離部
101 筐体
102 回転体ユニット
1021 円筒形状の回転体
1021a 調整蓋体(円形状の調整蓋板)
1021b 第二蓋体(円形状の上部蓋板)
1021c 第一蓋体(円形状の下部蓋板)
1021d 側面
1021e 有孔底面
1022 仕切り羽根
1023 振切り板(円形状の振切り板)
1024 有孔円形整流板
1025 第二回転体(円筒形状の外回転体)
1025d 側面
1025e 有孔底面
1026 結合ネジ
103 回転体ユニット駆動部
1031 駆動モータ
1032 駆動軸プーリ
1033 伝達ベルト
1034 回転軸
1035 回転軸プーリ
20 混合液導入部
201 混合液導入管
30 軽液導出部
301 底面基材(最下部底面)
303r 軽液流路
304r 軽液収容室
305 軽液排出管
40 重液導出部
403r 重液流路
404r 重液収容室
405 重液排出管
A 比重0.75油と水との混合液
B 混合液Aから遠心分離した油成分
C 混合液Aから遠心分離した水成分
D 比重差の少ない2種以上の混合液
E 混合液Dから分離した軽液成分
DESCRIPTION OF SYMBOLS 1 Centrifugal separator 10 Mixed liquid separation part 101 Case 102 Rotating body unit 1021 Cylindrical rotating body 1021a Adjustment lid body (circular adjustment lid plate)
1021b Second lid (circular upper lid plate)
1021c first lid (circular lower lid)
1021d side surface 1021e perforated bottom surface 1022 partition blade 1023 swing plate (circular swing plate)
1024 Perforated circular current plate 1025 Second rotating body (cylindrical outer rotating body)
1025d Side surface 1025e Perforated bottom surface 1026 Coupling screw 103 Rotating body unit driving portion 1031 Driving motor 1032 Driving shaft pulley 1033 Transmission belt 1034 Rotating shaft 1035 Rotating shaft pulley 20 Mixed liquid introducing portion 201 Mixed liquid introducing tube 30 Light liquid leading portion 301 Bottom surface base Material (bottom bottom)
303r Light liquid flow path 304r Light liquid storage chamber 305 Light liquid discharge pipe 40 Heavy liquid outlet 403r Heavy liquid flow path 404r Heavy liquid storage chamber 405 Heavy liquid discharge pipe A A Mixed liquid of 0.75 specific gravity oil and water B Mixed liquid Oil component centrifuged from A C Water component centrifuged from mixture A D Two or more mixtures with small specific gravity difference E Light liquid component separated from mixture D

Claims (3)

比重の異なる2種以上の混合液を回転体内に導入し、比重の軽い軽液と比重の重い重液とに分離する遠心分離機において、
中心が共通する円形状の第一蓋体又は当該第一蓋体よりも上部に位置する第二蓋体と、中心部分又は中心付近に孔を有する有孔底面と、側面とで構成する円筒形状の回転体と、
前記第一蓋体の下面に接合し、前記回転体の垂直軸心位置から半径方向に向けて設置する複数の仕切り羽根と、
前記第一蓋体よりも下部に位置し、前記第一蓋体と平行、かつ、中心が共通する振切り板と、
前記振切り板の上部近傍位置から前記第一蓋体又は第二蓋体及び筐体を貫通し、中心が前記回転体の垂直軸心位置である混合液導入管と、
前記回転体の有孔底面と当該有孔底面よりもさらに下部に位置する底面基材との隙間に存在する軽液流路と、
前記軽液流路と連通する軽液収容室と、
前記第一蓋体又は第二蓋体のうち少なくとも上部に装備する蓋体に孔を設け、当該孔を流路の一部として構成する重液流路と、
重液流路と連通する重液収容室と、
前記第一蓋体又は第二蓋体のうち少なくとも上部に装備する蓋体の中心部分又は中心付近に設けた孔の前記回転体の垂直軸心に対する径方向の最外径と、前記回転体の有孔底面の中心部分又は中心付近に設けた孔の前記回転体の垂直軸心に対する径方向の最外径と、を相対的に調整する相対調整機構と、
を有する遠心分離機。
In a centrifuge that introduces a mixture of two or more of different specific gravity into a rotating body and separates it into a light liquid with a low specific gravity and a heavy liquid with a high specific gravity.
Cylindrical shape composed of a circular first lid having a common center or a second lid positioned above the first lid, a perforated bottom surface having a hole at or near the center, and a side surface A rotating body of
A plurality of partition blades that are joined to the lower surface of the first lid and are installed in the radial direction from the vertical axis position of the rotating body;
A swing plate located below the first lid, parallel to the first lid, and having a common center;
A liquid mixture introduction pipe penetrating through the first lid or the second lid and the housing from a position near the upper part of the shaking plate, the center being the vertical axis position of the rotating body;
A light liquid flow path present in the gap between the perforated bottom surface of the rotating body and the bottom base material located further below the perforated bottom surface;
A light liquid storage chamber communicating with the light liquid flow path;
A heavy liquid flow path configured to provide a hole in a cover body provided on at least an upper part of the first cover body or the second cover body, and configure the hole as a part of the flow path;
A heavy liquid storage chamber communicating with the heavy liquid flow path;
The outermost diameter in the radial direction with respect to the vertical axis of the rotating body of the hole provided in or near the center of the lid body provided on at least the upper part of the first lid body or the second lid body, A relative adjustment mechanism that relatively adjusts the outermost diameter in the radial direction with respect to the vertical axis of the rotating body of the hole provided at or near the center of the perforated bottom surface;
Centrifuge.
前記振切り板よりも下部に位置し中心が前記回転体の垂直軸心位置であり、有孔で、かつ、円形状の整流板を複数有する請求項1の遠心分離機。   The centrifuge according to claim 1, wherein the centrifuge has a plurality of perforated and circular rectifying plates located at a lower part than the swing plate and having a center at a vertical axis position of the rotating body. 前記回転体の底面の全面及び側面の全面又は一部面を覆う、底面と側面とで構成する円筒形状の第二回転体を有し、当該第二回転体の底面又は側面に軽液流路を構成し連通する孔を設けた請求項1及び請求項2の遠心分離機。   A cylindrical second rotating body composed of a bottom surface and a side surface covering the entire bottom surface and all or part of the side surface of the rotating body, and a light liquid flow path on the bottom surface or side surface of the second rotating body; The centrifuge of Claim 1 and Claim 2 which provided the hole which comprises and communicates.
JP2010129485A 2010-06-05 2010-06-05 Centrifuge Pending JP2011255257A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015198461A1 (en) * 2014-06-27 2015-12-30 サイチ工業株式会社 Centrifuge for separating particles having differences in specific gravity
EP3605232A4 (en) * 2017-03-31 2020-04-29 FUJIFILM Corporation Treatment method and treatment device

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JPH07501744A (en) * 1991-12-12 1995-02-23 フレイモ ディベロップメンツ ユーケー リミテッド centrifuge
JPH1147638A (en) * 1997-07-31 1999-02-23 Toyobo Co Ltd Inside disk, centrifugal separator using the same and separation
JP2004298855A (en) * 2003-03-28 2004-10-28 Cnk:Kk Centrifugal separator provided with liquid separation function

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Publication number Priority date Publication date Assignee Title
JPS53103274A (en) * 1977-02-18 1978-09-08 Flottweg Werk Bruckmayer Hermetically sealed screw conveyor type centrifugal separator for liquiddsolid mixture
JPH07501744A (en) * 1991-12-12 1995-02-23 フレイモ ディベロップメンツ ユーケー リミテッド centrifuge
JPH1147638A (en) * 1997-07-31 1999-02-23 Toyobo Co Ltd Inside disk, centrifugal separator using the same and separation
JP2004298855A (en) * 2003-03-28 2004-10-28 Cnk:Kk Centrifugal separator provided with liquid separation function

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015198461A1 (en) * 2014-06-27 2015-12-30 サイチ工業株式会社 Centrifuge for separating particles having differences in specific gravity
EP3605232A4 (en) * 2017-03-31 2020-04-29 FUJIFILM Corporation Treatment method and treatment device
US10691022B2 (en) 2017-03-31 2020-06-23 Fujifilm Corporation Processing method and processing apparatus

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