JP4252516B2 - Method and apparatus for cleaning and dewatering slurry - Google Patents

Method and apparatus for cleaning and dewatering slurry Download PDF

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JP4252516B2
JP4252516B2 JP2004256581A JP2004256581A JP4252516B2 JP 4252516 B2 JP4252516 B2 JP 4252516B2 JP 2004256581 A JP2004256581 A JP 2004256581A JP 2004256581 A JP2004256581 A JP 2004256581A JP 4252516 B2 JP4252516 B2 JP 4252516B2
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slurry
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尚広 立石
昭一 郷田
紀夫 山田
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Ebara Corp
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Description

本発明は、スラリーに含まれる有価物の回収あるいは有害物質、障害物除去のためにスラリーを洗浄し、脱水する方法および装置に関する。   The present invention relates to a method and an apparatus for washing and dewatering a slurry for recovering valuable materials contained in the slurry or removing harmful substances and obstacles.

スラリーに含まれる有価物の回収や有害物質、障害物を除去するために、スラリーを洗浄した後、これを圧搾して余分の水分を除去することは広く行われている。例えば、焼却灰をセメント原料にするために、焼却灰を水に入れて攪拌してスラリーとし、これを複数の洗浄槽と複数の脱水機を使用して洗浄脱水を行い、焼却灰中のクロルイオンを除去する方法が知られている。(特許文献1)
特開2003−211129
In order to recover valuable materials contained in the slurry and remove harmful substances and obstacles, it is widely practiced to wash the slurry and then squeeze it to remove excess moisture. For example, in order to use incineration ash as a raw material for cement, incineration ash is put into water and stirred to form a slurry, which is washed and dehydrated using multiple washing tanks and multiple dehydrators, and chlor in the incineration ash. Methods for removing ions are known. (Patent Document 1)
JP 2003-211129 A

しかしながら、従来のこの種の洗浄脱水方法では複数の洗浄槽と複数の脱水機を使用しなくてはならず装置の設置スペースが大きくなり、複数の工程を通して洗浄を行うために多量の洗浄水を消費していた。また、洗浄と脱水を繰り返すため水量バランスをとるための運転管理が複雑であった。
本発明は、以上のような点に鑑みなされたものであり、スラリーの濾過脱水装置として知られているフィルタープレスを使用し、スラリーを有効に洗浄脱水することを目的とするものである。
However, this type of conventional washing and dehydration method requires the use of a plurality of washing tanks and a plurality of dehydrators, which increases the installation space of the apparatus, and a large amount of washing water is required for washing through a plurality of processes. I was consuming. In addition, since the washing and dehydration are repeated, the operation management for balancing the amount of water is complicated.
The present invention has been made in view of the above points, and an object of the present invention is to effectively wash and dehydrate the slurry using a filter press known as a slurry dewatering apparatus.

すなわち、本発明は、
少なくとも一部が濾布によって画定される濾室と、該濾室にスラリーを供給する手段と、濾室に対して外側から圧力をかけて該濾室を圧縮する加圧手段とを備えるフィルタープレスを用いたスラリーの洗浄脱水方法において、
所定圧力でスラリーを濾室内に供給して濾過する濾過工程と、
濾過工程の後に上記所定圧力よりも高い圧力で洗浄水を濾室内に供給し、該濾室内の濾過残渣を洗浄する洗浄工程と、
洗浄工程の後に加圧手段により濾室を加圧し、該炉室内の洗浄された濾過残渣を圧搾する圧搾工程と
を有することを特徴とするフィルタープレスを用いたスラリーの洗浄脱水方法を提供する。
That is, the present invention
A filter press comprising a filter chamber defined at least in part by a filter cloth, means for supplying slurry to the filter chamber, and pressure means for compressing the filter chamber by applying pressure to the filter chamber from the outside. In the slurry dehydration method using
A filtration step in which the slurry is supplied into the filter chamber at a predetermined pressure and filtered;
A washing step of supplying washing water into the filter chamber at a pressure higher than the predetermined pressure after the filtration step, and washing the filtration residue in the filter chamber;
There is provided a method for washing and dehydrating a slurry using a filter press, comprising: a pressurizing step of pressurizing a filter chamber by a pressurizing means after the cleaning step, and pressing the cleaned filtration residue in the furnace chamber.

具体的には、この洗浄脱水方法では、濾過工程と洗浄工程とを交互に複数回繰り返すようにすることが好ましい。   Specifically, in this washing and dehydrating method, it is preferable to repeat the filtration step and the washing step a plurality of times alternately.

更に、本発明は、
少なくとも一部が濾布によって画定される濾室、濾室に対して外側から圧力をかけて該濾室を圧縮する加圧室を備えるフィルタープレスと、
濾室内に、スラリーを所定圧力で供給して当該スラリーの濾過を行うスラリー加圧供給手段と、
濾室内に、洗浄水を上記所定圧力よりも高い圧力で供給し、濾室内の濾過残渣を洗浄する洗浄水加圧供給手段と、
濾室を圧縮して濾室内の濾過残渣を圧搾するため、加圧室に圧搾水を供給する圧搾水供給手段と、
を有することを特徴とするフィルタープレス装置を提供する。
Furthermore, the present invention provides
A filter press comprising a filter chamber defined at least in part by a filter cloth, a pressurizing chamber for compressing the filter chamber by applying pressure from the outside to the filter chamber;
Slurry pressure supply means for supplying the slurry at a predetermined pressure into the filter chamber and filtering the slurry; and
Wash water pressure supply means for supplying wash water to the filter chamber at a pressure higher than the predetermined pressure, and for washing the filtration residue in the filter chamber;
In order to compress the filter chamber and squeeze the filtration residue in the filter chamber, compressed water supply means for supplying compressed water to the pressure chamber;
The filter press apparatus characterized by having is provided.

具体的には、この洗浄脱水装置は、スラリー加圧供給手段と洗浄水加圧供給手段とを交互に複数回作動させ、その後、圧搾水供給手段を作動させる制御手段を備えるようにすることが好ましい。   Specifically, the cleaning and dehydrating apparatus may include a control unit that alternately operates the slurry pressure supply unit and the cleaning water pressure supply unit a plurality of times, and then operates the compressed water supply unit. preferable.

具体的には、スラリー加圧供給手段が、スラリー貯留槽と、該スラリー貯留槽から濾室にスラリーを供給するスラリー供給ラインと、該スラリー供給ライン内に設けられた第1開閉弁及び第1ポンプとを有し、
洗浄水加圧供給手段が、貯水槽と、該貯水槽から濾室にスラリー洗浄のための水を供給する洗浄水供給ラインと、該洗浄水供給ライン内に設けられた第2開閉弁及び第2ポンプとを有し、
圧搾水供給手段が、貯水槽と、濾室を加圧圧縮するための水を上記加圧室に供給する圧搾水供給ラインと、該圧搾水供給ライン内に設けられた第3開閉弁及び第3ポンプとを有することができる。
Specifically, the slurry pressure supply means includes a slurry storage tank, a slurry supply line for supplying slurry from the slurry storage tank to the filter chamber, a first on-off valve provided in the slurry supply line, and a first A pump,
The cleaning water pressure supply means includes a water storage tank, a cleaning water supply line for supplying water for slurry cleaning from the water storage tank to the filter chamber, a second on-off valve provided in the cleaning water supply line, and a second 2 pumps,
The compressed water supply means includes a water storage tank, a compressed water supply line that supplies water for compressing and compressing the filter chamber to the pressurized chamber, a third on-off valve provided in the compressed water supply line, and a second 3 pumps.

更に、スラリー供給ライン内の第1開閉弁が第1ポンプよりも上流側に設けられており、
洗浄水供給ライン内の第2開閉弁が第2ポンプよりも上流側に設けられており、
スラリー供給ラインの第1ポンプよりも下流側と、洗浄水供給ラインの第2ポンプよりも下流側とが一体に接続されて濾室に連通されるものとすることができる。
Furthermore, the 1st on-off valve in a slurry supply line is provided in the upstream rather than the 1st pump,
A second on-off valve in the washing water supply line is provided upstream of the second pump;
The downstream side of the first pump of the slurry supply line and the downstream side of the second pump of the cleaning water supply line may be integrally connected to communicate with the filter chamber.

本発明では、スラリーの濾過、洗浄及び圧搾脱水を行うのに1つのフィルタープレスを用いて行うので、複数の洗浄槽と複数の脱水機を使用する従来の洗浄脱水装置に比べて設置スペースを大幅に削減することができる。   In the present invention, the filtration, washing and squeezing and dewatering of the slurry are performed using a single filter press, so that the installation space is greatly increased compared to the conventional washing and dehydrating apparatus using a plurality of washing tanks and a plurality of dehydrators. Can be reduced.

また、フィルタープレス内で複数の行程を連続的に行えるために、従来の洗浄脱水装置で必要とされていた洗浄水槽での脱水ケーキの再溶解、際溶解されたスラリーの再洗浄などの煩雑な作業を省くことができ、それら再溶解、再洗浄などに必要な水量を削減することができる。   In addition, since a plurality of processes can be continuously performed in the filter press, complicated processes such as re-dissolution of the dehydrated cake in the washing water tank and re-washing of the slurry that has been dissolved in the conventional washing dehydration apparatus are required. Work can be omitted, and the amount of water required for re-dissolution and re-washing can be reduced.

更に、洗浄のための水は、スラリーを濾室に供給するときよりも高圧で供給するようにすることにより、濾過によって固化した濾過残滓を迅速に粉砕し洗浄することができ、短時間での洗浄作業を可能とする。   Furthermore, by supplying the water for washing at a higher pressure than when the slurry is fed into the filter chamber, the filtration residue solidified by filtration can be quickly crushed and washed. Enables cleaning work.

以下、本発明に係るスラリーの洗浄脱水方法及び該方法に用いられるフィルタープレス装置の実施形態につき、添付図面に基づき説明する。   Hereinafter, embodiments of a method for washing and dehydrating a slurry according to the present invention and a filter press device used in the method will be described with reference to the accompanying drawings.

図1は、本発明に係るフィルタープレス装置10の概要を示す。すなわち、該フィルタープレス装置10は、フィルタープレス12と、該フィルタプレス12に対してスラリーを供給するためのスラリー供給手段14と、フィルタプレス内に供給されたスラリーを洗浄したり、圧搾したりするための加圧水を供給するための加圧水供給手段16とを備える。   FIG. 1 shows an outline of a filter press apparatus 10 according to the present invention. That is, the filter press apparatus 10 cleans or squeezes the filter press 12, the slurry supply means 14 for supplying slurry to the filter press 12, and the slurry supplied into the filter press. And pressurized water supply means 16 for supplying pressurized water for the purpose.

フィルタープレス12は、一般的なものと同様に、スラリーを受け入れて圧搾するための複数の濾過脱水ユニットを備えており、各ユニットは、図2に示すように、濾枠18と、該濾枠内に設けられ、濾室20を形成する濾布22と、該濾布22と濾枠18の内面との間に設けられ、濾枠18の内面との間に加圧室24を形成するダイアフラム26とを備える。ダイアフラム26の濾布22と接する面には凹凸26−1が形成され、濾室20から濾布22を通して外部に出る液体が、該ダイアフラム26と濾布22との間を流下できるようにしている。   The filter press 12 includes a plurality of filter dewatering units for receiving and squeezing the slurry, as in a general case, and each unit includes a filter frame 18 and a filter frame as shown in FIG. A filter cloth 22 that is provided in the filter chamber 20 and that is provided between the filter cloth 22 and the inner surface of the filter frame 18, and that forms a pressurizing chamber 24 between the filter frame 18 and the inner surface of the filter frame 18. 26. Concavities and convexities 26-1 are formed on the surface of the diaphragm 26 in contact with the filter cloth 22, so that liquid exiting from the filter chamber 20 through the filter cloth 22 can flow between the diaphragm 26 and the filter cloth 22. .

スラリー供給手段14は、スラリーSを収納するスラリー槽30と、該スラリー槽30から濾室20にスラリーSを供給するスラリー供給ライン32とを有する。該スラリー供給ライン32には、上流側から開閉弁34及びポンプ36が設けられている。   The slurry supply unit 14 includes a slurry tank 30 that stores the slurry S, and a slurry supply line 32 that supplies the slurry S from the slurry tank 30 to the filter chamber 20. The slurry supply line 32 is provided with an on-off valve 34 and a pump 36 from the upstream side.

加圧水供給手段16は、貯水槽40と、濾室20を加圧圧縮するための加圧水Wを上記加圧室24に供給する圧搾水供給ライン42とを有する圧搾水供給手段44を備える。該圧搾水供給ライン42には、上流側から開閉弁46及びポンプ48が設けられている。
本発明に係るフィルタープレス装置10では、加圧水供給手段16に更に、濾室20内の濾過残渣を洗浄するための加圧水を濾室に供給するため、圧搾水供給ライン42から分枝した洗浄水供給ライン52を有する洗浄水供給手段54が設けられている。該洗浄水供給ライン52には、ポンプ56及び開閉弁58が設けられている。
The pressurized water supply means 16 includes a compressed water supply means 44 having a water storage tank 40 and a compressed water supply line 42 for supplying pressurized water W for compressing and compressing the filter chamber 20 to the pressure chamber 24. The compressed water supply line 42 is provided with an on-off valve 46 and a pump 48 from the upstream side.
In the filter press device 10 according to the present invention, the supply of washing water branched from the compressed water supply line 42 to supply the pressurized water supply means 16 with pressurized water for washing the filtration residue in the filter chamber 20 to the filter chamber. Washing water supply means 54 having a line 52 is provided. The cleaning water supply line 52 is provided with a pump 56 and an opening / closing valve 58.

図示の例では、スラリー供給ライン32は、洗浄水供給ライン52に、開閉弁58よりも下流側で接続されている。   In the illustrated example, the slurry supply line 32 is connected to the cleaning water supply line 52 on the downstream side of the on-off valve 58.

このフィルタープレス装置を用いてスラリーSの洗浄脱水を行う場合は、先ず、開閉弁34を開くとともに他の開閉弁46,58は閉じ、ポンプ36によってスラリーSを所定圧力で濾室20内に供給する。濾室20内に供給されるスラリーは、ポンプによる加圧により濾布22によって濾過され、濾室20内に残されるスラリーは固形分の濃度が高い状態とされる。   When washing and dehydrating the slurry S using this filter press apparatus, first, the on-off valve 34 is opened and the other on-off valves 46 and 58 are closed, and the slurry S is supplied into the filter chamber 20 by a pump 36 at a predetermined pressure. To do. The slurry supplied into the filter chamber 20 is filtered by the filter cloth 22 by pressurization with a pump, and the slurry remaining in the filter chamber 20 is in a state in which the solid content is high.

次に、開閉弁34を閉じて開閉弁58を開き、ポンプ56によって加圧水Wを、ポンプ36によるスラリー供給圧力よりも高い圧力で濾室20に供給する。濾室20内に残されたスラリー残渣は、この高い圧力の加圧水により急激に攪拌されるとともに、スラリー残渣内に残されていた有害物質等は、水と共に濾布の外側に流出し、当該スラリー残渣の洗浄が行われる。   Next, the on-off valve 34 is closed and the on-off valve 58 is opened, and the pressurized water W is supplied to the filter chamber 20 by the pump 56 at a pressure higher than the slurry supply pressure by the pump 36. The slurry residue left in the filter chamber 20 is rapidly stirred by the high-pressure pressurized water, and harmful substances left in the slurry residue flow out to the outside of the filter cloth together with water. The residue is washed.

更に、次の段階として、開閉弁58を閉じて開閉弁46を開き、ポンプ46により加圧水を高圧にて加圧室24内に供給する。加圧室内に供給された加圧水はダイアフラム26を濾室側に膨らませ、これにより濾室20内のスラリー残渣は圧搾されてケーキが形成される。該ケーキは、濾枠18を開くことによって外部へ排出される。   Further, as the next step, the on-off valve 58 is closed and the on-off valve 46 is opened, and pressurized water is supplied into the pressurizing chamber 24 by the pump 46 at a high pressure. The pressurized water supplied into the pressurizing chamber causes the diaphragm 26 to swell toward the filter chamber, whereby the slurry residue in the filter chamber 20 is squeezed to form a cake. The cake is discharged to the outside by opening the filter frame 18.

上記濾室20へのスラリー供給と、該濾室内のスラリー残渣の洗浄とは順次数回繰り返して行うことが、これは濾過洗浄効果を上げる上で好ましい。   The supply of the slurry to the filter chamber 20 and the cleaning of the slurry residue in the filter chamber are preferably repeated several times in order to increase the filter cleaning effect.

図中60は、上記スラリー供給濾過、スラリー残渣洗浄、スラリー残渣圧搾を行うため、開閉弁34、46,58、ポンプ36、48,56を所定の順序に従ってシーケンス制御するための制御器である。   In the figure, reference numeral 60 denotes a controller for sequence-controlling the on-off valves 34, 46, 58 and the pumps 36, 48, 56 in a predetermined order in order to perform the slurry supply filtration, slurry residue washing, and slurry residue pressing.

以下、本発明に係るフィルタプレス装置を用いて、大豆粕に含まれるクロルイオンを除去する作業を行った実施例につき説明する。 Hereinafter, the Example which performed the operation | work which removes the chloro ion contained in soybean meal using the filter press apparatus which concerns on this invention is described.

初めに塩酸処理した大豆粕スラリーをスラリー貯留槽30に貯留した。このときの大豆粕スラリーのクロルイオン濃度は18.2gCl/kg-DSで、スラリー濃度は約5%であった。   The soybean meal slurry first treated with hydrochloric acid was stored in the slurry storage tank 30. At this time, the chlorine ion concentration of the soybean meal slurry was 18.2 gCl / kg-DS, and the slurry concentration was about 5%.

まず、開閉弁46、58を閉とし、開閉弁34を開としてポンプ36により、スラリー貯留槽30から大豆粕スラリー150リットルをフィルタープレス12の濾室20内に圧力0.6MPaで供給し、濾過した後に、開閉弁34を閉じて開閉弁58を開き、濾室容積25リットルの3.6倍である89リットルの洗浄水を、洗浄水供給ライン52のポンプ56により圧力0.8MPaで圧入して濾室内の濾過残渣を洗浄した。次に、開閉弁58を閉じ、開閉弁46を開いてポンプ48により圧力1.6MPaで加圧水を加圧室24内に供給し、濾室を圧縮し、該濾室内で洗浄された濾過残滓を圧搾し、大豆粕の脱水ケーキを得た。   First, the on-off valves 46 and 58 are closed, the on-off valve 34 is opened, and 150 liters of soybean meal slurry is supplied from the slurry storage tank 30 into the filter chamber 20 of the filter press 12 at a pressure of 0.6 MPa. After that, the on-off valve 34 is closed and the on-off valve 58 is opened, and 89 liters of washing water, which is 3.6 times the filtration chamber volume of 25 liters, is injected by the pump 56 of the washing water supply line 52 at a pressure of 0.8 MPa. The filter residue in the filter chamber was washed. Next, the on-off valve 58 is closed, the on-off valve 46 is opened, and pressurized water is supplied into the pressurizing chamber 24 at a pressure of 1.6 MPa by the pump 48, the filter chamber is compressed, and the filtration residue washed in the filter chamber is removed. It was pressed to obtain a dehydrated cake of soybean meal.

測定の結果、この脱水ケーキは、含水率58.5%、クロルイオン濃度2.3gCl/kg-DSであり、クロルイオン濃度の目標値である2.3gCl/kg-DS以下の数値となることが分かった。   As a result of the measurement, this dehydrated cake has a water content of 58.5%, a chloroion concentration of 2.3 gCl / kg-DS, and a numerical value less than the target value of chloroion concentration of 2.3 gCl / kg-DS. I understood.

このように、本発明では、一つのフィルタープレスにより洗浄と脱水ができるため、従来装置において必要とされていた洗浄水槽での脱水ケーキの再溶解、再度の洗浄作業等の煩雑な操作を必要としない上、大幅な水量を節減することができた。また、洗浄においてはクロルイオンだけでなく、脱水阻害物質も除去されることもあり、脱水後のケーキの含水率は上記のように低いものとすることができた。   Thus, in the present invention, since it can be washed and dehydrated with a single filter press, complicated operations such as re-dissolution of the dehydrated cake in the washing water tank and re-washing work required in the conventional apparatus are required. In addition, a significant amount of water was saved. In addition, not only chloro ions but also dehydration-inhibiting substances may be removed during washing, and the moisture content of the cake after dehydration can be reduced as described above.

また、濾室に対する洗浄のための水供給圧力をスラリー供給圧力より高くすることにより、洗浄時間を短くすることができた。洗浄水圧力をスラリー供給圧力と同程度の0.6MPaとした場合に、洗浄に要する時間は約7分を要したのに比べて、本実施例では洗浄水供給圧力を0.8MPaとした結果、洗浄に要した時間は約3分と1/2以下の時間とすることができた。   Moreover, the washing time could be shortened by making the water supply pressure for washing the filter chamber higher than the slurry supply pressure. When the cleaning water pressure is set to 0.6 MPa, which is about the same as the slurry supply pressure, the time required for cleaning is about 7 minutes, compared with the result of setting the cleaning water supply pressure to 0.8 MPa in this example. The time required for washing could be about 3 minutes and less than 1/2.

第2の実施例では、大豆粕スラリーを50リットルずつ3回に分けてフィルタープレスに圧入濾過し、そのつど洗浄も行った。洗浄水量は初回25リットル、2回目30リットル、3回目34リットルとした。洗浄後、圧搾脱水した脱水ケーキの含水率は56.2%となり、クロルイオン濃度は2.0gCl/kg-DSとなった。   In the second example, the soybean meal slurry was divided into 50 liters in three portions, press-fitted into a filter press, and washed each time. The amount of washing water was 25 liters for the first time, 30 liters for the second time, and 34 liters for the third time. After washing, the water content of the dehydrated cake that had been pressed and dehydrated was 56.2%, and the chloroion concentration was 2.0 g Cl / kg-DS.

すなわち、スラリーを分割圧入して洗浄を行った方がケーキ含水率は低下し、クロルイオン濃度も低下して洗浄効果が高かった。   That is, when the slurry was dividedly injected and washed, the moisture content of the cake was lowered and the chloro ion concentration was also lowered, resulting in a higher washing effect.

また、濾過に要する時間も一括洗浄では15分要したが、分割洗浄では12分と短縮され、フィルタープレスの濾過速度が向上した。この場合、洗浄水は同量づつにしてもよいし、順次水量を減量してもよいが、上記実施例のように漸増する方が好ましい。また、1回の洗浄水量は少なくとも濾室容積以上の量にするのが好ましい。   Also, the time required for filtration was 15 minutes for batch cleaning, but was shortened to 12 minutes for divided cleaning, and the filtration speed of the filter press was improved. In this case, the amount of washing water may be the same amount, or the amount of water may be decreased sequentially, but it is preferable to gradually increase as in the above embodiment. Further, it is preferable that the amount of washing water at one time is at least the volume of the filter chamber.

以上の実施例では、スラリー残渣を洗浄するのに水を用いたが、水の代りに温水を用いてもよく、また、スラリーを加温して供給してもよい。また、熱源装置を設け、スラリーや水を供給する際に加温しながら供給してもよく、さらに、脱水促進のため真空装置で濾液排出ラインを真空下にしてもよい。   In the above embodiment, water is used to wash the slurry residue, but hot water may be used instead of water, and the slurry may be heated and supplied. In addition, a heat source device may be provided and heated while supplying slurry or water, and the filtrate discharge line may be placed under vacuum with a vacuum device to promote dehydration.

本発明に係るフィルタープレス装置の概要を示す図である。It is a figure which shows the outline | summary of the filter press apparatus which concerns on this invention. 図1のフィルタープレス装置で用いられるフィルタープレスの濾過圧搾ユニットの一例を示す図である。It is a figure which shows an example of the filtration pressing unit of the filter press used with the filter press apparatus of FIG.

符号の説明Explanation of symbols

10 フィルタープレス装置
12 フィルタープレス
14 スラリー供給手段
16 加圧水供給手段
18 濾枠
20 濾室
22 濾布
24 加圧室
26 ダイアフラム
26−1 凹凸
30 スラリー槽
32 スラリー供給ライン
34 開閉弁
36 ポンプ
40 貯水槽
42 圧搾水供給ライン
44 圧搾水供給手段
46 開閉弁
48 ポンプ
52 洗浄水供給ライン
54 洗浄水供給手段
56 ポンプ
58 開閉弁
60 制御器

DESCRIPTION OF SYMBOLS 10 Filter press apparatus 12 Filter press 14 Slurry supply means 16 Pressurized water supply means 18 Filter frame 20 Filter chamber 22 Filter cloth 24 Pressurization chamber 26 Diaphragm 26-1 Concavity and convexity 30 Slurry tank 32 Slurry supply line 34 On-off valve 36 Pump 40 Water storage tank 42 Pressed water supply line 44 Pressed water supply means 46 On-off valve 48 Pump 52 Wash water supply line 54 Wash water supply means 56 Pump 58 Open / close valve 60 Controller

Claims (6)

少なくとも一部が濾布によって画定される濾室と、該濾室にスラリーを供給する手段と、濾室に対して外側から圧力をかけて該濾室を圧縮する加圧手段とを備えるフィルタープレスを用いたスラリーの洗浄脱水方法において、
所定圧力でスラリーを濾室内に供給して濾過する濾過工程と、
濾過工程の後に上記所定圧力よりも高い圧力で洗浄水を濾室内に供給し、該濾室内の濾過残渣を粉砕して洗浄する洗浄工程と、
洗浄工程の後に加圧手段により濾室を加圧し、該炉室内の洗浄された濾過残渣を圧搾する圧搾工程と
を有することを特徴とするフィルタープレスを用いたスラリーの洗浄脱水方法。
A filter press comprising a filter chamber defined at least in part by a filter cloth, means for supplying slurry to the filter chamber, and pressure means for compressing the filter chamber by applying pressure to the filter chamber from the outside. In the slurry dehydration method using
A filtration step in which the slurry is supplied into the filter chamber at a predetermined pressure and filtered;
A washing step of supplying washing water into the filter chamber at a pressure higher than the predetermined pressure after the filtration step, and crushing and washing the filtration residue in the filter chamber;
A method for cleaning and dehydrating a slurry using a filter press, comprising: a pressurizing step of pressurizing a filter chamber by a pressurizing means after the cleaning step, and pressing the cleaned filtration residue in the furnace chamber.
該濾過工程と該洗浄工程とを交互に複数回繰り返す工程後に加圧手段により濾室を加圧し、該濾室内の洗浄された濾過残渣を圧搾するようにした請求項1に記載のスラリーの洗浄脱水方法。   The washing of the slurry according to claim 1, wherein the filtration chamber is pressurized by a pressurizing means after the filtration step and the washing step are alternately repeated a plurality of times, and the washed filtration residue in the filtration chamber is squeezed. Dehydration method. 少なくとも一部が濾布によって画定される濾室、濾室に対して外側から圧力をかけて該濾室を圧縮する加圧室を備えるフィルタープレスと、
濾室内に、スラリーを所定圧力で供給して当該スラリーの濾過を行うスラリー加圧供給手段と、
濾室内に、洗浄水を上記所定圧力よりも高い圧力で供給し、濾室内の濾過残渣を粉砕して洗浄する洗浄水加圧供給手段と、
濾室を圧縮して濾室内の濾過残渣を圧搾するため、加圧室に圧搾水を供給する圧搾水供給手段と、
スラリー加圧供給、洗浄水加圧供給、洗浄水加圧供給及び圧搾水供給の作動を制御する制御手段と
を有することを特徴とするフィルタープレス装置。
A filter press comprising a filter chamber defined at least in part by a filter cloth, a pressurizing chamber for compressing the filter chamber by applying pressure from the outside to the filter chamber;
Slurry pressure supply means for supplying the slurry at a predetermined pressure into the filter chamber and filtering the slurry; and
Wash water pressure supply means for supplying wash water to the filter chamber at a pressure higher than the predetermined pressure, and pulverizing and washing the filtration residue in the filter chamber;
In order to compress the filter chamber and squeeze the filtration residue in the filter chamber, compressed water supply means for supplying compressed water to the pressure chamber;
Control means for controlling the operation of slurry pressure supply, wash water pressure supply, wash water pressure supply and compressed water supply ;
The filter press apparatus characterized by having.
スラリー加圧供給手段と洗浄水加圧供給手段とを交互に複数回作動させ、その後、圧搾水供給手段を作動させるようにした請求項3に記載の制御手段と、
を有することを特徴とするフィルタープレス装置。
The control means according to claim 3, wherein the slurry pressure supply means and the washing water pressure supply means are alternately operated a plurality of times, and then the compressed water supply means is operated.
The filter press apparatus characterized by having.
スラリー加圧供給手段が、スラリー貯留槽と、該スラリー貯留槽から濾室にスラリーを供給するスラリー供給ラインと、該スラリー供給ライン内に設けられた第1開閉弁及び第1ポンプとを有し、
洗浄水加圧供給手段が、貯水槽と、該貯水槽から濾室にスラリー洗浄のための水を供給する洗浄水供給ラインと、該洗浄水供給ライン内に設けられた第2開閉弁及び第2ポンプとを有し、
圧搾水供給手段が、貯水槽と、濾室を加圧圧縮するための水を上記加圧室に供給する圧搾水供給ラインと、該圧搾水供給ライン内に設けられた第3開閉弁及び第3ポンプとを有することを特徴とする請求項3若しくは4に記載のフィルタープレス装置。
The slurry pressure supply means has a slurry storage tank, a slurry supply line for supplying slurry from the slurry storage tank to the filter chamber, and a first on-off valve and a first pump provided in the slurry supply line. ,
The cleaning water pressure supply means includes a water storage tank, a cleaning water supply line for supplying water for slurry cleaning from the water storage tank to the filter chamber, a second on-off valve provided in the cleaning water supply line, and a second 2 pumps,
The compressed water supply means includes a water storage tank, a compressed water supply line that supplies water for compressing and compressing the filter chamber to the pressurized chamber, a third on-off valve provided in the compressed water supply line, and a second 5. The filter press device according to claim 3, comprising three pumps.
スラリー供給ライン内の第1開閉弁が第1ポンプよりも上流側に設けられており、
洗浄水供給ライン内の第2開閉弁が第2ポンプよりも上流側に設けられており、
スラリー供給ラインの第1ポンプよりも下流側と、洗浄水供給ラインの第2ポンプよりも下流側とが一体に接続されて濾室に連通されている
ことを特徴とする請求項5に記載のフィルタープレス装置。
A first on-off valve in the slurry supply line is provided upstream of the first pump;
A second on-off valve in the washing water supply line is provided upstream of the second pump;
The downstream side of the first pump of the slurry supply line and the downstream side of the second pump of the washing water supply line are integrally connected and communicated with the filter chamber. Filter press device.
JP2004256581A 2004-09-03 2004-09-03 Method and apparatus for cleaning and dewatering slurry Expired - Fee Related JP4252516B2 (en)

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