JP2013086055A - Adsorption separation apparatus - Google Patents

Adsorption separation apparatus Download PDF

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JP2013086055A
JP2013086055A JP2011230754A JP2011230754A JP2013086055A JP 2013086055 A JP2013086055 A JP 2013086055A JP 2011230754 A JP2011230754 A JP 2011230754A JP 2011230754 A JP2011230754 A JP 2011230754A JP 2013086055 A JP2013086055 A JP 2013086055A
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container
separation apparatus
adsorption
treated water
adsorption separation
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JP5932288B2 (en
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Mitsutoshi Nishioka
光利 西岡
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Satake Chemical Equipment Mfg Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide an adsorption separation apparatus capable of securely carrying out adsorption separation of a material to be adsorbed such as a metal and a heavy metal contained in wastewater.SOLUTION: The adsorption separation apparatus includes: rotor means 6 to generate swirling flow of raw water in a container 2 along the inner circumference surface of the container 2 at the center in the vertical container 2 having a classification leg 3 at the bottom 2b and also connected with a supply line 8 of a carrier at the top; and liquid flow direction change means 7 to stream the raw water upward in the center of the container 2 at the center of the bottom face in the container 2, wherein the discharge line 11 of the carrier P adsorbed with the material to be adsorbed in the raw water is connected to the classification leg 3 and the discharge line 10 of treated water is connected to the upper part of the container 2.

Description

本発明は、排水中に含まれる金属や重金属物質等の被吸着物質を吸着分離するのに好適な吸着分離装置に関する。   The present invention relates to an adsorption / separation apparatus suitable for adsorbing and separating adsorbed substances such as metals and heavy metal substances contained in waste water.

従来の排水中の懸濁物質等を凝集、沈殿、分離する装置として、凝集槽において、流入口より流入する原水と投入口より投入される微生物フロックを攪拌機により撹拌し、原水中の懸濁粒子と微生物フロックが接触し、吸着と架橋作用により凝集フロックが形成され、凝集槽内の凝集フロックを含む水は沈殿槽に送られ、該沈殿槽において、凝集フロックを含む水中の凝集フロックは重力により沈降してホッパー状の底部に集積すると共に、分離した上澄み水は処理水として越流せきから放流するようにした装置が知られている(特許文献1参照。)。   As a conventional device for agglomerating, precipitating, and separating suspended substances in wastewater, in the agglomeration tank, the raw water flowing from the inlet and the microbial floc introduced from the inlet are stirred by a stirrer, and suspended particles in the raw water And microbial flocs come into contact with each other, and agglomeration flocs are formed by adsorption and cross-linking action. An apparatus is known that settles and accumulates at the bottom of the hopper and that the separated supernatant water is discharged from the overflow basin as treated water (see Patent Document 1).

又、排水中の重金属物質や放射性物質を除去するために、これら物質をカセット状の容器に入れられたゼオライト、顔料等の吸着物質で吸着させ、容器ごとに交換する装置が知られている。   In addition, in order to remove heavy metal substances and radioactive substances in the waste water, an apparatus is known in which these substances are adsorbed by an adsorbing substance such as zeolite or pigment contained in a cassette-like container and replaced for each container.

特開2007―307534公報JP 2007-307534 A

この従来の前者の装置によれば、撹拌槽において、撹拌機により微生物フロックを含む原水を単に円周方向に流動させながら撹拌しているので、原水と微生物フロックとの吸着により成長した凝集フロックの形成が得られにくく、その後、沈殿槽において、不十分な成長の凝集フロックは重力による沈殿が充分に行われず、かくて、凝集フロックと上澄み水との分離を確実に達成出来ない問題点があった。   According to this former former apparatus, since the raw water containing the microbial flocs is simply stirred in the stirring tank while flowing in the circumferential direction, the agglomerated flocs grown by adsorption of the raw water and the microbial flocs are stirred. In the precipitation tank, the insufficiently grown flocculated flocs are not sufficiently precipitated by gravity, so that the separation of the flocculated flocs and the supernatant water cannot be achieved reliably. It was.

又、従来の後者の装置によれば、ゼオライト、顔料等の吸着物質は連続的に吸着後に分離できない問題点があった。   Also, according to the latter latter apparatus, there is a problem that adsorbed substances such as zeolite and pigment cannot be separated continuously after adsorption.

本発明はこれらの問題点を解消し、排水中に含まれる金属や重金属物質等の被吸着物質の吸着分離を確実にでき、又、懸濁物質の凝集分離にも応用可能な吸着分離装置を提供することを目的とする。   The present invention eliminates these problems, makes it possible to reliably adsorb and separate adsorbed substances such as metals and heavy metal substances contained in wastewater, and an adsorption separation apparatus that can also be applied to aggregating and separating suspended substances. The purpose is to provide.

本発明はこの目的を達成すべく、底部に分級脚を有すると共に上部に担体の供給管路を接続した縦型の容器内の中心部に、該容器内の原水を該容器の内周面に沿って旋回流を生じさせる回転翼手段を設けると共に、前記容器内の底面の中心部に、前記原水を前記容器の中心部において上方に流動させる液流方向変更手段を設け、前記分級脚に、前記原水中の被吸着物質を吸着した担体の排出管路を接続すると共に、前記容器の上方部に、処理水の排出管路を接続したことを特徴とする。   In order to achieve this object, the present invention achieves this purpose by providing the base water in the center of a vertical container having a classifying leg at the bottom and connecting a carrier supply line at the top, to the inner peripheral surface of the container. A rotary vane means for generating a swirl flow along the center, a liquid flow direction changing means for causing the raw water to flow upward at the center of the container at the center of the bottom of the container, A discharge pipe for the carrier that has adsorbed the adsorbed substance in the raw water is connected, and a discharge pipe for the treated water is connected to the upper part of the container.

本発明によれば、排水中に含まれる金属や重金属物質等の被吸着物質の吸着分離を確実にできる吸着分離装置を提供する効果を有し、又、凝集分離にも応用可能である効果を有する。   According to the present invention, there is an effect of providing an adsorptive separation device that can reliably adsorb and separate substances to be adsorbed such as metals and heavy metal substances contained in wastewater, and an effect that can also be applied to agglomeration separation. Have.

本発明の実施例1の吸着分離装置の縦断面説明図である。It is a longitudinal cross-sectional explanatory drawing of the adsorption separation apparatus of Example 1 of this invention. 図1のI−I線截断面図である。It is the II sectional view taken on the line of FIG. 本発明の実施例2の吸着分離装置の縦断面説明図である。It is a longitudinal cross-sectional explanatory drawing of the adsorption separation apparatus of Example 2 of this invention.

本発明を実施するための形態の実施例を以下に示す。   The example of the form for carrying out the present invention is shown below.

本発明の実施例1を図1及び図2により説明する。   A first embodiment of the present invention will be described with reference to FIGS.

図1は本発明の実施例1の吸着分離装置の縦断面説明図、図2は図1のI−I線截断面図である。   FIG. 1 is a longitudinal sectional explanatory view of an adsorption separation apparatus according to Embodiment 1 of the present invention, and FIG.

1は本実施例の吸着分離装置、2は該吸着分離装置1の容器を示し、該容器2は縦型の有底円筒状でその上端に蓋体2aを結着して構成されている。そして、該容器2の底部2bは下方に向かって湾曲状に形成され、該底部2bの中心部に透孔2cが形成されていると共に該底部2bの下面に分級脚3を固定し、前記透孔2cを介して該分級脚3の内部が前記容器2の内部に連通するようにした。   Reference numeral 1 denotes an adsorption / separation apparatus of the present embodiment, 2 denotes a container of the adsorption / separation apparatus 1, and the container 2 is a vertical bottomed cylindrical shape and is configured by binding a lid 2a to the upper end thereof. The bottom 2b of the container 2 is curved downward, and a through hole 2c is formed at the center of the bottom 2b, and the classification leg 3 is fixed to the lower surface of the bottom 2b. The inside of the classifying leg 3 communicated with the inside of the container 2 through the hole 2c.

4は回転軸を示し、該回転軸4は前記蓋体2aの中心部に固定の軸受部5に回転自在に支持されて前記容器2内の中心部に垂下され、該回転軸4の下端部に回転翼手段である平羽根型の撹拌翼6を固定すると共に、該回転軸4の上端部を回転駆動源(図示せず)に連結し、該回転駆動源の駆動により前記撹拌翼6が回転するようにした。   Reference numeral 4 denotes a rotating shaft. The rotating shaft 4 is rotatably supported by a bearing portion 5 fixed to the center portion of the lid body 2 a and is suspended from the center portion in the container 2, and a lower end portion of the rotating shaft 4. A flat blade type agitating blade 6 as a rotating blade means is fixed to the upper end of the rotating shaft 4 and an upper end portion of the rotating shaft 4 is connected to a rotation driving source (not shown), and the stirring blade 6 is driven by the rotation driving source. I made it rotate.

7は液流方向変更手段を示し、該液流方向変更手段7は前記底部2bの内面に放射状に固定されている複数枚例えば4枚の直線状の帯状板のバッフル7aからなり、これら各バッフル7aは図2に示す如く前記撹拌翼6の回転方向の後方で前記底部2bの中心を通る半径線Rから間隔dの位置に平行に固定されていると共に、各バッフル7aの内方端は前記透孔2cの周縁に一致するようにした。   Reference numeral 7 denotes a liquid flow direction changing means. The liquid flow direction changing means 7 includes a plurality of, for example, four linear strip-like baffles 7a fixed radially to the inner surface of the bottom portion 2b. As shown in FIG. 2, the agitator blades 6a are fixed in parallel to the distance d from the radial line R passing through the center of the bottom portion 2b, and the inner ends of the baffles 7a It was made to correspond to the periphery of the through-hole 2c.

8は前記蓋体2aに接続した担体の供給管路である第1供給管路、9は前記容器2の側壁の中間部に接続した原水の供給管路である第2供給管路、10は該側壁の上方部に接続した処理水の排出管路である第1排出管路、11は前記分級脚3の側壁に接続した担体の排出管路である第2排出管路、12は該分級脚3の下端部に接続した処理水の流入管路を示し、前記第1排出管路10から分岐したリターン管路13は前記流入管路12に連通接続し、該リターン管路13にポンプ14を介在した。   Reference numeral 8 denotes a first supply pipe that is a carrier supply pipe connected to the lid 2a, 9 denotes a second supply pipe that is a raw water supply pipe connected to an intermediate portion of the side wall of the container 2, A first discharge pipe that is a treated water discharge pipe connected to the upper portion of the side wall, 11 is a second discharge pipe that is a carrier discharge pipe connected to the side wall of the classification leg 3, and 12 is the classification. An inflow pipe for treated water connected to the lower end of the leg 3 is shown. A return pipe 13 branched from the first discharge pipe 10 is connected to the inflow pipe 12, and a pump 14 is connected to the return pipe 13. Intervened.

次に本実施例1の吸着分離装置1の作用と効果を説明する。   Next, the operation and effect of the adsorption / separation apparatus 1 of the first embodiment will be described.

金属や重金属物質の被吸着物質を含む排水の原水を前記第2供給管路9より前記容器2内に所定のレベルまで満たしてから、前記回転駆動源を駆動して前記撹拌翼6を回転すると、原水は、前記容器2の内周面に沿って旋回しながら下方に移動する流れFaを生じさせ、該流れFaが前記底部2bの近傍に至ると、各バッフル7aが前記撹拌翼6の回転方向の後方で前記半径方向線Rから間隔dを有しているため、前記バッフル7aに当たった原水は前記容器2の中心部を旋回しながら上昇する流れFbとなり、これらFaとFbの流れにより循環流となる。このような流れによる撹拌混合部15において、ゼオライト、顔料等の多孔質物質や化学的吸着物質の担体Pを前記第1供給管路8より前記容器2内に供給されると、原水中の被吸着物質は担体Pに効率的に吸着されて重い担体Paとなって前記分級脚部3内に流下し、該分級脚部3において分離した重い担体Paは前記第2排出管路11より排出される。   When the raw water of the waste water containing the adsorbed substance of metal or heavy metal substance is filled into the container 2 from the second supply pipe 9 to a predetermined level, the rotation driving source is driven to rotate the stirring blade 6 The raw water generates a flow Fa that moves downward while swirling along the inner peripheral surface of the container 2. When the flow Fa reaches the vicinity of the bottom 2 b, each baffle 7 a rotates the stirring blade 6. Since there is a distance d from the radial line R at the rear of the direction, the raw water hitting the baffle 7a becomes a flow Fb that rises while turning around the center of the container 2, and the flow of Fa and Fb It becomes a circulating flow. In the stirring and mixing unit 15 based on such a flow, when a porous substance such as zeolite or pigment or a carrier P for a chemically adsorbed substance is supplied into the container 2 from the first supply pipe 8, The adsorbed substance is efficiently adsorbed by the carrier P to become a heavy carrier Pa and flows down into the classification leg 3, and the heavy carrier Pa separated in the classification leg 3 is discharged from the second discharge pipe 11. The

他方、原水中から被吸着物質が吸着により除去された処理水は前記第1排出管路10より排出される。そして、該第1排出管路10より排出される処理水の一部は前記ポンプ14によりリターン管路13を経て前記流入管路12より前記分級脚3内に流入し、該分級脚3内における閉塞を防止し流れを良くする。   On the other hand, the treated water from which the substance to be adsorbed is removed from the raw water by adsorption is discharged from the first discharge pipe 10. A part of the treated water discharged from the first discharge pipe 10 flows into the classification leg 3 from the inflow pipe 12 via the return pipe 13 by the pump 14, and in the classification leg 3. Prevent blockage and improve flow.

本発明の実施例2を図3により説明する。   A second embodiment of the present invention will be described with reference to FIG.

図3は本発明の実施例2の吸着分離装置の縦断面説明図である。   FIG. 3 is a longitudinal cross-sectional explanatory view of an adsorption separation apparatus according to Embodiment 2 of the present invention.

本実施例2においては、3個の吸着分離装置、即ち、第1吸着分離装置1Aと第2吸着分離装置1Bと第3吸着分離装置1Cを並置した例を示しており、該第1吸着分離装置1Aの処理水の排出管路10Aの先端部が該第2吸着分離装置1Bの容器2Bの側壁の中間部に接続していると共に、該第2吸着分離装置1Bの処理水の排出管路10Bの先端部が前記第3吸着分離装置1Cの容器2Cの側壁の中間部に接続しており、又、該第3吸着分離装置1Cの容器2Cの側壁の上方部に接続した処理水の排出管路10Cから分岐したリターン管路13Cは、前記第1吸着分離装置1Aの第1分級脚3Aに接続した処理水の流入管路12Aと、前記第2吸着分離装置1Bの第2分級脚3Bに接続した処理水の流入管路12Bと、前記第3吸着分離装置1Cの第3分級脚3Cに接続した処理水の流入管路12Cとに分岐して接続している。   In the second embodiment, an example in which three adsorption separation devices, that is, the first adsorption separation device 1A, the second adsorption separation device 1B, and the third adsorption separation device 1C are juxtaposed is shown. The front end of the treated water discharge line 10A of the apparatus 1A is connected to the middle part of the side wall of the container 2B of the second adsorption / separation apparatus 1B, and the treated water discharge line of the second adsorption / separation apparatus 1B. 10B is connected to the middle part of the side wall of the container 2C of the third adsorption / separation apparatus 1C, and discharged from the treated water connected to the upper part of the side wall of the container 2C of the third adsorption / separation apparatus 1C. A return line 13C branched from the line 10C includes an inflow line 12A for treated water connected to the first classification leg 3A of the first adsorption separation apparatus 1A, and a second classification leg 3B of the second adsorption separation apparatus 1B. Treated water inflow conduit 12B, and the third adsorption separation Connecting branches to the inflow conduit 12C of the treated water which is connected to the third Bunkyuashi 3C of location 1C.

8A、8B、8Cは前記第1吸着分離装置1A、前記第2吸着分離装置1B、前記第3吸着分離装置1Cの容器2A、2B、2Cの蓋体2aにそれぞれ接続した担体Pの供給管路、11A、11B、11Cは前記第1分級脚3A、前記第2分級脚3B、前記第3分級脚3Cにそれぞれ接続した担体Paの第2排出管路を示す。   Reference numerals 8A, 8B, 8C denote carrier P supply lines connected to the lids 2a of the containers 2A, 2B, 2C of the first adsorption separation device 1A, the second adsorption separation device 1B, and the third adsorption separation device 1C, respectively. , 11A, 11B, and 11C denote second discharge conduits of the carrier Pa connected to the first classifying leg 3A, the second classifying leg 3B, and the third classifying leg 3C, respectively.

次に本実施例2の吸着分離装置1A、1B、1Cの作用と効果を説明する。   Next, operations and effects of the adsorption / separation apparatuses 1A, 1B, and 1C according to the second embodiment will be described.

前記第1吸着分離装置1Aにおいて、前記実施例1の如く原水中から担体Pにより金属や重金属物質の被吸着物質が吸着除去された処理水は前記排出管路10Aより排出されると共に、原水中の被吸着物質は担体Pに効率的に吸着されて重い担体Paとなって前記分級脚部3A内に流下し、該分級脚部3Aにおいて分離した重い担体Paは前記排出管路11Aより排出される。更に、前記第2吸着分離装置1Bにおいて、前記排出管路10Aより流入した処理水から担体Pにより更に残る金属や重金属物質の吸着物質が除去され、このように除去された処理水は前記排出管路10Bより排出されると共に処理水の残る金属や重金属物質の被吸着物質は担体Pに効率的に吸着されて重い担体Paが前述の如く前記排出管路11Bより排出され、更に、前記第3吸着分離装置1Cにおいて、更に前述の如く吸着分離が行われて、被吸着物質が残ってない処理水が前記排出管路10Cより排出され、その一部がリターン管路13Cをへて各分級脚3A、3B、3Cに流入する。   In the first adsorption / separation apparatus 1A, treated water obtained by adsorbing and removing a metal or a heavy metal substance to be adsorbed by the carrier P from the raw water as in the first embodiment is discharged from the discharge pipe 10A, and the raw water. The substance to be adsorbed is efficiently adsorbed on the carrier P to become a heavy carrier Pa and flows down into the classification leg 3A, and the heavy carrier Pa separated in the classification leg 3A is discharged from the discharge pipe 11A. The Further, in the second adsorption / separation apparatus 1B, the remaining metal or heavy metal substance adsorbed material is removed by the carrier P from the treated water flowing in from the discharge pipe 10A, and the treated water thus removed is removed from the discharged pipe. The metal or heavy metal substance adsorbed substance discharged from the passage 10B and remaining in the treated water is efficiently adsorbed by the carrier P, and the heavy carrier Pa is discharged from the discharge pipe 11B as described above. In the adsorption / separation apparatus 1C, the adsorption separation is further performed as described above, and the treated water in which the substance to be adsorbed does not remain is discharged from the discharge pipe 10C, and a part of it is returned to the classification leg through the return pipe 13C. Flows into 3A, 3B, 3C.

このように、本実施例2においては、吸着分離が完全におこなわれる。   Thus, in the present Example 2, adsorption separation is completely performed.

前記実施例2においては、3個の吸着分離装置の例を示したが、必要に応じて、2個又は4個以上の吸着分離装置を設置してもよい。   In the second embodiment, an example of three adsorption / separation devices has been described. However, two or four or more adsorption / separation devices may be installed as necessary.

本発明の吸着分離装置は、排水処理・洗浄水処理及び化学品関係、医療品関係、食品関係等における吸着分離に利用される。   The adsorption separation apparatus of the present invention is used for adsorption separation in wastewater treatment / washing water treatment, chemicals, medical products, foods, and the like.

1 吸着分離装置
1A 吸着分離装置
1B 吸着分離装置
1C 吸着分離装置
2 容器
2b 底部
2A 容器
2B 容器
2C 容器
3 分級脚
3A 分級脚
3B 分級脚
3C 分級脚
6 回転翼手段
7 液流方向変更換手段
7a バッフル
8 担体の供給管路
9 原水の供給管路
10 処理水の排出管路
11 担体の排出管路
12 処理水の流入管路
13 リターン管路
DESCRIPTION OF SYMBOLS 1 Adsorption separation apparatus 1A Adsorption separation apparatus 1B Adsorption separation apparatus 1C Adsorption separation apparatus 2 Container 2b Bottom part 2A Container 2B Container 2C Container 3 Classification leg 3A Classification leg 3B Classification leg 3C Classification leg 6 Rotary blade means 7 Liquid flow direction change means 7a Baffle 8 carrier supply line 9 raw water supply line 10 treated water discharge line 11 carrier discharge line 12 treated water inflow line 13 return line

Claims (5)

底部に分級脚を有すると共に上部に担体の供給管路を接続した縦型の容器内の中心部に、該容器内の原水を該容器の内周面に沿って旋回流を生じさせる回転翼手段を設けると共に、前記容器内の底面の中心部に、前記原水を前記容器の中心部において上方に流動させる液流方向変更手段を設け、前記分級脚に、前記原水中の被吸着物質を吸着した担体の排出管路を接続すると共に、前記容器の上方部に、処理水の排出管路を接続した吸着分離装置。   Rotating blade means for generating a swirling flow of the raw water in the container along the inner peripheral surface of the container in the central part of the vertical container having a classification leg at the bottom and connected to the supply pipe of the carrier at the top And a liquid flow direction changing means for causing the raw water to flow upward in the central portion of the container at the central portion of the bottom surface in the container, and adsorbed substances in the raw water are adsorbed on the classification legs. An adsorptive separation apparatus in which a discharge pipe for a carrier is connected and a discharge pipe for treated water is connected to the upper part of the container. 前記分級脚に処理水の流入管路を接続した請求項1に記載の吸着分離装置。   The adsorption separation apparatus according to claim 1, wherein an inflow conduit for treated water is connected to the classification leg. 前記液流方向変更手段は前記底面に放射状に設けたバッフルからなる請求項1又は請求項2に記載の吸着分離装置。   The adsorption separation apparatus according to claim 1 or 2, wherein the liquid flow direction changing means includes baffles provided radially on the bottom surface. 前記バッフルは、前記回転翼手段の回転方向の後方で前記底面の中心の半径線から所定の間隔を存して配設した帯状板からなる請求項3に記載の吸着分離装置。   The adsorption / separation apparatus according to claim 3, wherein the baffle is formed of a belt-like plate disposed at a predetermined distance from a radial line at the center of the bottom surface behind the rotating blade means in the rotational direction. 前記容器を複数並設し、前段の容器の処理水の排出管路を、後段の容器に接続すると共に、最終段の容器の処理水の排出管路から分岐したリターン管路を、その前段の容器の分級脚の前記処理水の流入管路に接続した請求項2乃至請求項4のいずれか1に記載の吸着分離装置。   A plurality of the above-mentioned containers are juxtaposed, and the treated water discharge conduit of the preceding container is connected to the succeeding container, and the return conduit branched from the treated water discharge conduit of the final container is connected to the preceding container. The adsorption separation device according to any one of claims 2 to 4, wherein the adsorption separation device is connected to an inflow pipe of the treated water on a classification leg of a container.
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