JP2011025184A - Dehydrating treatment equipment for spent diatomaceous earth filter medium - Google Patents

Dehydrating treatment equipment for spent diatomaceous earth filter medium Download PDF

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JP2011025184A
JP2011025184A JP2009175088A JP2009175088A JP2011025184A JP 2011025184 A JP2011025184 A JP 2011025184A JP 2009175088 A JP2009175088 A JP 2009175088A JP 2009175088 A JP2009175088 A JP 2009175088A JP 2011025184 A JP2011025184 A JP 2011025184A
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diatomaceous earth
earth filter
filter material
decanter
storage tank
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Yasuhiko Iwasaki
康彦 岩崎
Ryoji Nonaka
良二 野中
Noriyoshi Nishigami
典良 西上
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NIPPON CANPACK KK
OS MACHINERY KK
SANYU KIKI KK
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NIPPON CANPACK KK
OS MACHINERY KK
SANYU KIKI KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide dehydrating treatment equipment which is compact and continuously dehydrates a spent diatomaceous earth filter medium into the desired quantity of water with small labor and allows the dehydrated spent diatomaceous earth filter medium to be disposed of. <P>SOLUTION: The dehydrating equipment comprises a storage tank having stirring device and storing a treating material prepared by adding a prescribed quantity of water to the diatomaceous earth filter medium stripped from a filtration filter arranged in a filtration tank and adjusting them, a constant feed pump having a suction port connected to the storage tank and a decanter type centrifugal separator connected to the discharge port of the constant feed pump. The dehydration is carried out by continuously supplying the treating material stored in the storage tank to the decanter type centrifugal separator at a constant amount by the constant feed pump and continuously separating the treating material into a cake-like solid comprising the diatomaceous earth filter medium and water by the decanter type centrifugal separator. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、各種の濾過手段として用いられる珪藻土フィルターに使用した後の珪藻土濾過材の処理設備に関するものである。   The present invention relates to a treatment facility for a diatomaceous earth filter material after use in a diatomaceous earth filter used as various filtering means.

近時、例えば茶類、ミネラル水、酒類などの飲用物をボトルに充填する際に、飲用物内の濁りによる商品価値の低下を防止し美麗な商品とするため、更には飲み感や味の向上を図る目的で飲用物の最終的処理手段の1つとして例えば特願平11−281256号公報、特開2000−189055号公報など提示されているように、珪藻土濾過材を表面に配置した珪藻土フィルターにより濾過することが行われているように、各種の用途において珪藻土が濾過材として使用されている。   Recently, when filling bottles with drinks such as tea, mineral water, and alcoholic beverages, in order to prevent a drop in product value due to turbidity in the drink, As one of the final treatment means for drinks for the purpose of improvement, for example, as disclosed in Japanese Patent Application No. 11-281256, Japanese Patent Application Laid-Open No. 2000-189055, etc., diatomaceous earth with a diatomaceous earth filter material disposed on the surface Diatomaceous earth is used as a filter material in various applications as it is filtered.

ところで、前記珪藻土濾過材は、自身に形成されている多数の小孔に微細な固形物が蓄積するので、頻繁に使用すると目詰まり等によりフィルター性能が低下することから新たな珪藻土濾過材と交換する必要がある。   By the way, since the diatomaceous earth filter material accumulates fine solids in a large number of small holes formed in itself, the filter performance deteriorates due to clogging when used frequently. There is a need to.

このとき、濾過槽の内部に設置された濾過フィルターの表面に配置された使用済みの珪藻土濾過材を例えば濾過槽に逆洗用エアーを吹き込んで、濾過槽の底部に濾液とともに落下させ、これを脱水して廃棄するのが一般的である。   At this time, used diatomaceous earth filter material placed on the surface of the filtration filter installed inside the filtration tank, for example, blows backwash air into the filtration tank and drops it together with the filtrate at the bottom of the filtration tank. It is common to dehydrate and discard.

特に、珪藻土濾過材の成分である珪藻土は、そのほとんどが単細胞藻類である珪藻の遺骸(珪藻殻)から生成された珪質の堆積物であって、粘土、火山灰、有機物などの混合物であり、茶類、ミネラル水、ワインやビールなどのような各種の飲用物の濾過に用いた場合にはそのまま土壌に投与したとしても地球環境に害を及ぼすことはない。   In particular, diatomaceous earth, which is a component of diatomaceous earth filter media, is a siliceous deposit produced mostly from diatom remains (diatom shell), which is a unicellular algae, and is a mixture of clay, volcanic ash, organic matter, etc. When used for the filtration of various drinks such as tea, mineral water, wine and beer, even if it is administered as it is to the soil, it does not harm the global environment.

しかしながら、珪藻土濾過材の本質は含水非晶質二酸化珪素のコロイド状のものであることから、自身もほぼ4倍程度の重量の水分を吸収保持することになる。特に、前記濾過槽から洗い出した状態の珪藻土濾過材は、濾液と混ざった状態であることから水分量が多くスラリー状であって、脱水しないで、そのままの状態で運搬することならびに土壌に廃棄することはきわめて困難であるばかりか容量が多いとコスト高にもなる。   However, since the essence of the diatomaceous earth filter material is a colloidal form of water-containing amorphous silicon dioxide, the diatomite filter medium itself absorbs and retains about four times the weight of water. In particular, the diatomaceous earth filter material washed out from the filtration tank is in a state of being mixed with the filtrate so that it has a large amount of water and is in a slurry state and is transported as it is without being dehydrated and discarded to the soil. Not only is this very difficult, but the capacity is also expensive.

そこで、従来、前記濾過槽から取り出した使用済みの水分の多いスラリー状の珪藻土濾過材を例えばドラム缶のような縦型の貯留容器に充填して静置し、珪藻土濾過材が沈降した上澄み液を排出して、残ったケーキ状の珪藻土濾過材を掻き出して運搬、廃棄していた。   Therefore, conventionally, the used hydrated slurry diatomaceous earth filter material taken out from the filtration tank is filled in a vertical storage container such as a drum can and allowed to stand, and the supernatant liquid in which the diatomaceous earth filter material settles is used. The remaining cake-like diatomaceous earth filter material was scraped out, transported, and discarded.

そのため、多大な労力と長い時間および広い作業面積を必要としており、特に連続作業が行えない、等の問題があった。   Therefore, a great amount of labor, a long time and a wide work area are required, and there is a problem that continuous work cannot be performed.

また、広範囲な設置場所と多くの人手を要する前記多数のドラム缶に代わって、大型の貯留槽に使い済みの珪藻土濾過材を一括して貯留し、スクリューやプレスなどの加圧手段により機械的に圧搾して脱水時間の迅速化を図る手段がとられているが使用済みの珪藻土濾過材を一度に溜めて加圧脱水する高さの高い大型の貯留槽が必要であったり、メンテナンスも大規模になり、さらに連続して脱水作業ができないので多量の使用済みの珪藻土濾過材を一度に貯めて処理しなければならず作業時には多大な労力を要することにもなる。   Also, instead of the large number of drum cans that require a wide range of installation locations and a lot of manpower, the used diatomite filter media is stored in a large storage tank in a lump and mechanically pressed by means of pressure such as screws and presses. Although measures are taken to expedite dehydration time by pressing, large sized storage tanks that store used diatomaceous earth filter media at once and pressurize and dehydrate are necessary, and maintenance is also extensive. Furthermore, since the dehydration operation cannot be performed continuously, a large amount of used diatomaceous earth filter material must be stored and processed at one time, which requires a lot of labor during the operation.

さらに、前記問題点を解決する手段の1つとして、珪藻土濾過材を配置した濾過槽内の使用済み珪藻土濾過材をその下方に配置した加圧エアーにより加圧して脱水する脱水フィルターを備えた脱水筒に導き脱水する処理手段において、脱水筒に導く前に混合機により使用済み珪藻土と加工液(濾液)を撹拌混合することにより濾過(脱水)の迅速化を図った手段が特開平6−309号公報に提示されているが、この場合にも重量のある大型の濾過槽の下方に混合機や脱水筒を配置する必要があり、現実的でなく、作業効率が悪く、特に、使用済みの珪藻土濾過材を脱水処理する際に濾過槽を使用することができず作業効率が悪いという問題がある。   Furthermore, as one of the means for solving the above problems, a dehydration filter equipped with a dehydration filter that pressurizes and dehydrates a used diatomite filter medium in a filter tank in which a diatomite filter medium is disposed with pressurized air disposed below the filter medium. In the processing means for dehydrating and introducing into a cylinder, means for speeding up the filtration (dehydration) by stirring and mixing the used diatomaceous earth and the processing liquid (filtrate) with a mixer before introducing into the dehydrating cylinder is disclosed in JP-A-6-309. In this case as well, it is necessary to place a mixer and dewatering cylinder below the heavy, large filtration tank, which is impractical and inefficient in work. When dehydrating the diatomaceous earth filter material, there is a problem that the filtration tank cannot be used and work efficiency is poor.

特願平11−281256号公報Japanese Patent Application No. 11-281256 特開2000−189055号公報JP 2000-189055 A 特開平6−309号公報JP-A-6-309

本発明は前記課題を解決するためになされたものであり、コンパクトな設備で使用済みの珪藻土濾過材を少ない労力で連続して所望の水分量に脱水して廃棄することができる脱水処理設備を提供するものである。   The present invention has been made to solve the above-described problems, and provides a dehydration treatment facility that can dehydrate and discard a used diatomaceous earth filter material to a desired amount of water continuously with a small amount of labor. It is to provide.

前記課題を解決するためになされた本発明である使用済み珪藻土濾過材の脱水処理設備は、濾過槽内に配置した濾過フィルターから剥離した珪藻土濾過材に所定量の水分を加えて調整した処理材を貯留する撹拌装置付きの貯留槽と、前記貯留槽に吸込口を連結した定量供給ポンプと、前記定量供給ポンプの吐出口に連結されたデカンタ型遠心分離器とからなり、前記貯留槽に貯留させた処理材を前記定量供給ポンプによりデカンタ型遠心分離器に定量的に連続して供給し、前記デカンタ型遠心分離器にて珪藻土濾過材からなるケーキ状の固形物と水分とに連続的に分離して脱水処理を行うことを特徴とする。   The dewatering equipment for used diatomaceous earth filter material according to the present invention, which has been made to solve the above problems, is a treatment material prepared by adding a predetermined amount of moisture to a diatomaceous earth filter material peeled off from a filtration filter disposed in a filtration tank. And a decanter centrifuge connected to the discharge port of the fixed supply pump. The treated material is quantitatively continuously supplied to the decanter-type centrifuge by the quantitative feed pump, and continuously into cake-like solids and moisture made of diatomaceous earth filter material by the decanter-type centrifuge. It is characterized in that it is separated and dehydrated.

また、本発明において、前記デカンタ型遠心分離器が、下方に形成した空間に収容コンテナを出入自由に配置可能な架台上に載置されているとともに前記架台の載置部に前記デカンタ型遠心分離器における固形物取出口を貫通させて開口部を前記空間に露出させ、前記固形物取出口から取り出される脱水処理済みの珪藻土濾過材からなるケーキ状の固形物が連続して落下するように構成した場合には、脱水処理済みの珪藻土濾過材を連続して収集することができ、特に、前記コンテナを運搬車両に付設される分割式の荷台とした場合にはそのまま積み替えることなしに運搬車両で廃棄場所へ搬送することが可能であり、きわめて効率がよい。   Further, in the present invention, the decanter centrifuge is placed on a pedestal on which a container can be freely placed in and out of a space formed below, and the decanter centrifuge is placed on a placement part of the cradle. A structure in which cake-like solids made of dehydrated diatomaceous earth filter material taken out from the solid matter outlet are continuously dropped by penetrating the solid matter outlet in the vessel to expose the opening in the space. In this case, the dewatered diatomaceous earth filter material can be continuously collected. In particular, when the container is a split type loading platform attached to the transport vehicle, the transport vehicle can be used without being reloaded. Can be transported to a disposal site and is extremely efficient.

さらに、前記貯留槽に貯留させた処理材の水分含有量を110〜120重量%程度とすることにより通常の定量供給ポンプを用いても前記貯留させた処理材を所定の供給量で容易にデカンタ型遠心分離器に連続して供給することが可能であり、また、前記デカンタ型遠心分離器による脱水処理後の固形物の水分含有量が65重量%以下である場合には運搬並びに廃棄に際して含有水分による悪影響がなく、容積や重量も縮小して経済的にも有利である。   Furthermore, by setting the water content of the processing material stored in the storage tank to about 110 to 120% by weight, the stored processing material can be easily decanted with a predetermined supply amount even if a normal metering pump is used. Can be continuously supplied to the mold centrifuge, and when the water content of the solid after dehydration by the decanter centrifuge is 65% by weight or less, it is contained during transportation and disposal. There is no adverse effect due to moisture, and the volume and weight are reduced, which is economically advantageous.

加えて、デカンタ型遠心分離器を形成するスクリューコンベアの表面が硬質のタイル材により覆われている場合には、研磨材に用いられる程の研磨作用を有する珪藻土濾過材とスクリューコンベアとが接触しても摩耗を少なくなり耐久性を増すことができる。   In addition, when the surface of the screw conveyor forming the decanter centrifuge is covered with a hard tile material, the diatomaceous earth filter material having a polishing action enough to be used for the abrasive and the screw conveyor are in contact with each other. However, wear can be reduced and durability can be increased.

本発明によれば、使用済みの珪藻土濾過材をコンパクトな設備で且つ少ない労力で連続して所望の水分量に脱水してきわめて効率よく廃棄することができる。   According to the present invention, a used diatomaceous earth filter medium can be dehydrated continuously to a desired amount of water with a compact facility and with a small amount of labor, and can be disposed of very efficiently.

本発明である使用済み珪藻土濾過材の脱水処理設備の概略を示す説明図。Explanatory drawing which shows the outline of the dehydration processing equipment of the used diatomaceous earth filter material which is this invention. 図1に示した実施の形態に用いられるデカンタ型遠心分離器の断面拡大図である。It is a cross-sectional enlarged view of the decanter-type centrifuge used for embodiment shown in FIG.

図1は例えば茶類飲用のために用いられる濾過槽1内に設置された濾過フィルタ11に配置された珪藻土濾過材12を脱水処理するための設備についての概略を示すものであり、主として、前記濾過槽1の下方に配置されて濾過槽1内に配置した前記濾過フィルター11から剥離した珪藻土濾過材12に所定量の水分を加えて調整して処理材21を形成するための集積槽2、 前記集積槽2内の処理材21を搬送するための供給ポンプ3,前記供給ポンプ3により搬送された前記処理材21を貯留する撹拌装置41付きの貯留槽4と,前記貯留槽4に吸込口51を連結した定量供給ポンプ5と、前記定量供給ポンプ5の吐出口52に連結されたスクリューコンベア61の表面に例えばタングステンカーバイトのような硬質材によるタイルが被覆されたデカンタ型遠心分離器6とからなる。   FIG. 1 shows an outline of equipment for dehydrating a diatomaceous earth filter material 12 disposed in a filter 11 installed in a filter tank 1 used for drinking tea, for example. An accumulation tank 2 for forming a treatment material 21 by adding a predetermined amount of water to the diatomaceous earth filter material 12 disposed below the filter tank 1 and peeled off from the filter filter 11 disposed in the filter tank 1; A supply pump 3 for conveying the processing material 21 in the accumulation tank 2, a storage tank 4 with a stirring device 41 for storing the processing material 21 conveyed by the supply pump 3, and a suction port in the storage tank 4 51, and the surface of the screw conveyor 61 connected to the discharge port 52 of the fixed supply pump 5 is covered with a tile made of a hard material such as tungsten carbide. Decanter type centrifuge 6.

また、前記デカンタ型遠心分離器6が、下方に形成した空間71に収容コンテナ8を出入自由に配置可能とした架台7上に載置されているとともに載置面から前記デカンタ型遠心分離器6における固形物取出口62を貫通させて開口部を下側に形成される空間71に露出させ、また、水分取出口63の下端が地表などに形成した排水溝13に開口している。   The decanter centrifuge 6 is placed on a gantry 7 in which a storage container 8 can be freely placed in and out of a space 71 formed below, and the decanter centrifuge 6 is placed from a placement surface. The solid matter outlet 62 is penetrated to expose the opening in the space 71 formed on the lower side, and the lower end of the moisture outlet 63 opens to the drainage groove 13 formed on the ground surface or the like.

尚、図面中、符号9は例えば浄水H(水道水や地下水など)源に接続された水路であり、91は前記水路に配置された三方向弁、92は電磁弁である。また、
前記デカンタ型遠心分離器6における水分取出口63の下端には取りだされた水分の受けタンク101が配置されているとともに、水分の受けタンク101にはポンプ102および三方向電磁弁103が接続されており、前記三方向電磁弁103の一方の吐出口が地表に構築された排水溝13への水路104か接続され、もう一方の吐出口には前記4へ撹拌装置4への水路105が接続されている。
In the drawings, reference numeral 9 is a water channel connected to, for example, a source of purified water H (tap water, groundwater, etc.), 91 is a three-way valve disposed in the water channel, and 92 is an electromagnetic valve. Also,
At the lower end of the moisture outlet 63 in the decanter type centrifuge 6, a moisture receiving tank 101 is disposed, and a pump 102 and a three-way solenoid valve 103 are connected to the moisture receiving tank 101. One discharge port of the three-way solenoid valve 103 is connected to the water channel 104 to the drainage groove 13 constructed on the ground surface, and the other discharge port is connected to the water channel 105 to the stirring device 4 to the four. Has been.

次に、本実施の形態の使用方法について詳細に説明する。   Next, the usage method of this Embodiment is demonstrated in detail.

始めに、飲用物を濾過している濾過槽1内の珪藻土濾過材12を交換する際に、例えば濾過槽1内に逆洗用エアーを吹き込んで、濾過フィルター11から剥離した珪藻土濾過材12を濾過槽1の底部に配置した集積槽2に濾液とともに落下させ、必要であればこれに水路9から浄水Hを追加して所定の水分含量とした処理物21を供給ポンプ3により貯留槽3に移送する。   First, when replacing the diatomaceous earth filter material 12 in the filtration tank 1 that is filtering the drink, for example, the diatomaceous earth filter material 12 peeled from the filter 11 by blowing back washing air into the filter tank 1 is used. The collected liquid 21 is dropped together with the filtrate into the accumulation tank 2 disposed at the bottom of the filtration tank 1, and if necessary, the treated product 21 having a predetermined water content by adding purified water H from the water channel 9 is supplied to the storage tank 3 by the supply pump 3. Transport.

尚、前記処理物21の水分含量は、供給ポンプ3により搬送可能であればよいが、例えば110〜120重量%であると搬送可能であるとともに全体の容積を少なくすることができるのでその後の貯留槽4の容積を小さくすることができたりデカンタ型遠心分離器6の脱水時間などの減縮や脱水により生じる水分の削減を図ることができる。   The moisture content of the processed product 21 is not limited as long as it can be transported by the supply pump 3. However, for example, when it is 110 to 120% by weight, it can be transported and the entire volume can be reduced. The volume of the tank 4 can be reduced, the dewatering time of the decanter centrifuge 6 can be reduced, and water generated by dehydration can be reduced.

そして、前記貯留槽4に貯留された処理物21は撹拌装置41により常時均質(使用済みの珪藻土濾過材が所定の水分含量のスラリー化している状態)に保たれて貯留され、貯留された処理物は底部に形成した取出口42から定量供給ポンプ5により所定の流量でデカンタ型遠心分離器6へ連続的に供給される。尚、貯留槽4については加熱蒸気や加熱コイルなどの手段により加熱可能とすることにより低温により流動性が低下するのを防ぐことができる。   And the processed material 21 stored in the said storage tank 4 is always kept homogeneous by the stirring apparatus 41 (the used diatomaceous earth filter material is the slurry of the predetermined water content), and is stored and stored. A thing is continuously supplied to the decanter-type centrifuge 6 at a predetermined flow rate by a fixed supply pump 5 from an outlet 42 formed at the bottom. In addition, about the storage tank 4, it can prevent that fluidity falls by low temperature by enabling heating with means, such as a heating steam and a heating coil.

図2は前記デカンタ型遠心分離器6の詳細を示すものであり、ケース71内部に横方向へ延びる外側回転筒72とその内側に僅かな半径方向への隙間を保持させた状態で螺旋状の羽根731を有するスクリューコンベヤ73が主電動機741および差動機742、ギヤボックス743により高速で相対回転自在に設けられている従来周知の構成である。   FIG. 2 shows the details of the decanter type centrifugal separator 6. The outer rotating cylinder 72 extending in the lateral direction inside the case 71 and a slight radial gap inside thereof are held in a spiral shape. This is a conventionally known configuration in which a screw conveyor 73 having blades 731 is provided so as to be relatively rotatable at a high speed by a main motor 741, a differential machine 742, and a gear box 743.

また、前記外側回転筒72は、図示左端に分離した水分211の溢流口721が設けられた大径の平行部722と、これに連続して図示右端に分離した固形物212(珪藻土濾過材)の排出口722が設けられた傾斜部723とからなり、高速回転する外側回転筒72を有し、該外側回転筒72の内部に、僅かな半径方向隙間を保持して螺旋状のコンベヤ羽根731を有するスクリューコンベヤ73が相対回転自在に設けられている。   The outer rotating cylinder 72 includes a large-diameter parallel portion 722 provided with an overflow port 721 for moisture 211 separated at the left end in the figure, and a solid material 212 (diatomaceous earth filter material separated at the right end in the figure continuously from this. ) Having an outer rotating cylinder 72 that rotates at a high speed, and has a slight radial gap inside the outer rotating cylinder 72 to form a spiral conveyor blade. A screw conveyor 73 having 731 is provided to be relatively rotatable.

そして、前記スクリューコンベヤ73の軸75に形成された挿入口751から供給された前記処理材21は前記スクリューコンベヤ73の軸75の途中に形成された吐出口752から前記スクリューコンベヤ73と外側回転筒72との間の空間に搬送されて分離し、水分211が溢流口721から、ケーキ状の固形物(珪藻土濾過材)212が排出口722からそれぞれ所定の容量が連続して排出され、前記ケース71の下端に形成した水分取出口63および固形物取出口62から排出される。   The processing material 21 supplied from the insertion port 751 formed in the shaft 75 of the screw conveyor 73 is transferred from the discharge port 752 formed in the middle of the shaft 75 of the screw conveyor 73 to the screw conveyor 73 and the outer rotating cylinder. 72, the water 211 is discharged from the overflow port 721, the cake-like solid matter (diatomaceous earth filter material) 212 is continuously discharged from the discharge port 722, respectively, It is discharged from a moisture outlet 63 and a solid outlet 62 formed at the lower end of the case 71.

このとき、本実施の形態では、図1に示すように、前記固形物取出口62の下方に形成される開放端は前記架台を貫通して配置されているとともに、架台7の下方に形成した空間71に出入自由に配置可能とした収容コンテナ8に開口しているので前記固形物取出口62から連続して排出されるケーキ状の固形物(珪藻土濾過材)212が集積されるので所定量が堆積したらコンテナ8を引き出して新たに空のコンテナを配置して連続して脱水を行う。   At this time, in the present embodiment, as shown in FIG. 1, the open end formed below the solid material outlet 62 is disposed through the frame and formed below the frame 7. Since the container 8 that can be freely placed in and out of the space 71 is opened, cake-like solid matter (diatomaceous earth filter material) 212 continuously discharged from the solid matter outlet 62 is accumulated, so a predetermined amount. When the water is deposited, the container 8 is pulled out and a new empty container is arranged to continuously perform dehydration.

本実施の形態では特に、前記コンテナ8を運搬車両の分割式の荷台としたことにより(図示せず)、運搬車両をコンテナ8の連結部に連結するだけでそのまま荷台となるので車両の荷台に積み替えることもなくきわめて容易に搬送することができる。   In the present embodiment, in particular, the container 8 is used as a split type loading platform for the transporting vehicle (not shown), so that the transporting vehicle is simply connected to the connecting portion of the container 8 so that it becomes a loading platform as it is. It can be transported very easily without transshipment.

また、本実施の形態では、前記デカンタ型遠心分離器6における水分取出口63の下端には取りだされた水分の受けタンク101が配置されているとともに、水分の受けタンク101にはポンプ102および三方向電磁弁103が接続されており、前記三方向電磁弁103の一方の吐出口が地表に構築された排水溝13への水路104か接続され、もう一方の吐出口には前記貯留槽4への水路105が接続されている。従って、水分の受けタンク101の状況を確認することにより前記デカンタ型遠心分離器6において正常に水分が分離されていることが確認でき、また、分離された水分は必要であれば水路105を介して貯留槽4に使用する水分として利用することができる。   In the present embodiment, a moisture receiving tank 101 is disposed at the lower end of the moisture outlet 63 in the decanter centrifuge 6, and the moisture receiving tank 101 includes a pump 102 and A three-way solenoid valve 103 is connected, and one discharge port of the three-way solenoid valve 103 is connected to the water channel 104 to the drainage groove 13 constructed on the ground surface, and the other discharge port is connected to the storage tank 4. A water channel 105 to is connected. Therefore, by confirming the state of the moisture receiving tank 101, it can be confirmed that the moisture is normally separated in the decanter type centrifuge 6, and the separated moisture is passed through the water channel 105 if necessary. Thus, it can be used as moisture used in the storage tank 4.

本実施の形態では、前記排水を搬送する水路105および浄水を搬送する水路9が前記図1に示す集積槽2、供給ポンプ3,貯留槽4、定量供給ポンプ5およびデカンタ型遠心分離器6に連結されていることから、前記各機器の洗浄も容易にすることができる。   In the present embodiment, the water channel 105 for transporting the waste water and the water channel 9 for transporting the purified water are connected to the accumulation tank 2, the supply pump 3, the storage tank 4, the metering supply pump 5, and the decanter centrifuge 6 shown in FIG. 1. Since they are connected, cleaning of each device can be facilitated.

さらに、スクリューコンベア61の表面にタイルが形成されているので研磨効果を有する珪藻土濾過材を処理したとしても接触摩耗に対処することができる。   Further, since tiles are formed on the surface of the screw conveyor 61, contact wear can be dealt with even if a diatomaceous earth filter material having a polishing effect is processed.

さらにまた、本実施の形態によれば、前記定量供給ポンプ3やデカンタ型遠心分離器6、更には、電磁弁91等を制御装置(図示せず)により電子的に制御することにより全自動化(無人化)を図ることも可能である。   Furthermore, according to the present embodiment, the metering pump 3, the decanter centrifuge 6, and further the electromagnetic valve 91 and the like are electronically controlled by a control device (not shown) to be fully automated ( It is also possible to achieve unmanned operation.

本発明を茶飲用に用いた使用済みの茶入り珪藻土濾過材を水分量(珪藻土:水 = 13:100)に調整した処理材を、樹脂製貯留槽に貯領して定量供給ポンプ(吐出量 300L/h)によりデカンタ型遠心分離器(巴工業株式会社製 TSH005型トモイ−デカンタ)に供給し、3200RPMで4時間脱水処理した。   A treatment material prepared by adjusting the water content of the used tea-containing diatomaceous earth filter medium used for drinking tea to the present invention (diatomite: water = 13: 100) is stored in a resin storage tank, and a fixed amount supply pump (discharge amount) 300 L / h) and supplied to a decanter centrifuge (TSH005 type Tomoy-decanter manufactured by Sakai Kogyo Co., Ltd.) and dehydrated at 3200 RPM for 4 hours.

その結果、デカンタ型遠心分離器から平均含有水65%以下のケーキ状固形物(珪藻土濾過材)を連続してほぼ50kgを分離することができ、本発明がきわめて有効であることが確認された。   As a result, almost 50 kg of cake-like solid (diatomaceous earth filter material) having an average water content of 65% or less can be continuously separated from the decanter type centrifuge, and it was confirmed that the present invention is extremely effective. .

1 濾過槽、2 集積槽、4 貯留槽、5 定量供給ポンプ、6 デカンタ型遠心分離器、7 架台、8 収容コンテナ、11 濾過フィルター、12 珪藻土濾過材、21 処理材、41 撹拌装置、42 取出口、51 吸込口、52 吐出口、62 固形物取出口、71 空間、212 固形物

DESCRIPTION OF SYMBOLS 1 Filtration tank, 2 Accumulation tank, 4 Storage tank, 5 Metering supply pump, 6 Decanter type centrifuge, 7 Mount, 8 Storage container, 11 Filtration filter, 12 Diatomaceous earth filter material, 21 Treatment material, 41 Stirrer, 42 Outlet, 51 Suction port, 52 Discharge port, 62 Solid matter outlet, 71 Space, 212 Solid matter

Claims (6)

濾過槽内に配置した濾過フィルターから剥離した珪藻土濾過材に所定量の水分を加えて調整した処理材を貯留する撹拌装置付きの貯留槽と、前記貯留槽に吸込口を連結した定量供給ポンプと、前記定量供給ポンプの吐出口に連結されたデカンタ型遠心分離器とからなり、前記貯留槽に貯留させた処理材を前記定量供給ポンプによりデカンタ型遠心分離器に定量的に連続して供給し、前記デカンタ型遠心分離器にて珪藻土濾過材からなるケーキ状の固形物と水分とに連続的に分離して脱水処理を行うことを特徴とする使用済み珪藻土濾過材の脱水処理設備。   A storage tank with a stirrer for storing a treatment material prepared by adding a predetermined amount of water to a diatomaceous earth filter material separated from a filtration filter disposed in the filtration tank, and a quantitative supply pump having a suction port connected to the storage tank A decanter centrifuge connected to the discharge port of the metering supply pump, and the processing material stored in the storage tank is quantitatively continuously supplied to the decanter centrifuge by the metering pump. A dewatering equipment for a used diatomaceous earth filter material, wherein the decanter earth filter is continuously separated into a cake-like solid material made of diatomaceous earth filter material and moisture and then dehydrated. 前記デカンタ型遠心分離器が、下方に形成した空間に収容コンテナを出入自由に配置可能な架台上に載置されているとともに前記架台の載置部に前記デカンタ型遠心分離器における固形物取出口を貫通させて開口部を前記空間に露出させ、前記固形物取出口から取り出される脱水処理済みの珪藻土濾過材からなるケーキ状の固形物が連続して落下することを特徴とする請求項1記載の使用済み珪藻土濾過材の脱水処理設備。   The decanter-type centrifuge is placed on a pedestal on which a container can be freely placed in and out of a space formed below, and a solid material outlet in the decanter-type centrifuge is placed on the pedestal placement part. The cake-like solid material made of dehydrated diatomaceous earth filter material taken out from the solid material outlet is continuously dropped, with the opening being exposed to the space by penetrating the material. Of used diatomite filter material. 前記コンテナが運搬車両に付設される分割式の荷台であることを特徴とする請求項2記載の使用済み珪藻土濾過材の脱水処理設備。   The dewatering treatment facility for used diatomaceous earth filter material according to claim 2, wherein the container is a split type loading platform attached to a transport vehicle. 前記処理材の水分含有量が110〜120重量%である請求項1,2または3記載の使用済み珪藻土濾過材の脱水処理設備。   The water content of the said processing material is 110 to 120 weight%, The dehydration processing equipment of the used diatomaceous earth filter material of Claim 1, 2 or 3. 前記デカンタ型遠心分離器による脱水処理後の固形物の水分含有量が65重量%以下である請求項1,2,3または4記載の使用済み珪藻土濾過材の脱水処理設備。   The dewatering equipment for used diatomaceous earth filter material according to claim 1, 2, 3 or 4, wherein the water content of the solid after the dewatering treatment by the decanter centrifuge is 65% by weight or less. 前記デカンタ型遠心分離器を形成するスクリューコンベアの表面が硬質のタイル材により覆われていることを特徴とする請求項1,2,3,4または5記載の使用済み珪藻土濾過材の脱水処理設備。
6. The dewatering equipment for used diatomaceous earth filter material according to claim 1, wherein a surface of a screw conveyor forming the decanter centrifuge is covered with a hard tile material. .
JP2009175088A 2009-07-28 2009-07-28 Dehydrating treatment equipment for spent diatomaceous earth filter medium Pending JP2011025184A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02115735U (en) * 1989-03-06 1990-09-17
JPH10128156A (en) * 1996-11-05 1998-05-19 Nippei Toyama Corp Screw conveyor type centrifugal separator
JP2000288425A (en) * 1999-04-06 2000-10-17 Haruo Kojima Method and device for solid-liquid separation
JP2001062215A (en) * 1999-08-30 2001-03-13 Nifuko Plant Kk Filter device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02115735U (en) * 1989-03-06 1990-09-17
JPH10128156A (en) * 1996-11-05 1998-05-19 Nippei Toyama Corp Screw conveyor type centrifugal separator
JP2000288425A (en) * 1999-04-06 2000-10-17 Haruo Kojima Method and device for solid-liquid separation
JP2001062215A (en) * 1999-08-30 2001-03-13 Nifuko Plant Kk Filter device

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