JP4178557B2 - How to treat dredged mud - Google Patents
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- JP4178557B2 JP4178557B2 JP2005285264A JP2005285264A JP4178557B2 JP 4178557 B2 JP4178557 B2 JP 4178557B2 JP 2005285264 A JP2005285264 A JP 2005285264A JP 2005285264 A JP2005285264 A JP 2005285264A JP 4178557 B2 JP4178557 B2 JP 4178557B2
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
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- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Description
本発明は、海や湖沼あるいは河川の底から浚渫された泥土の処理方法に関する。 The present invention relates to a method for treating mud soil dredged from the bottom of a sea, lake, or river.
海や湖沼あるいは河川の水質汚染が進行している場合には、かかる水質汚染の進行を阻止して良好な環境を取り戻すことが生態系維持の観点できわめて重要である。 When water pollution of the sea, lakes, or rivers is progressing, it is extremely important from the viewpoint of maintaining the ecosystem to prevent such water pollution from progressing and restore a good environment.
水質汚染が進行する原因としては、外部からの有機物流入および底泥からの栄養塩の溶出が挙げられ、したがって、湖沼の水質を改善するには、その底泥を浚渫して除去してやるのが効果的である。 The cause of water pollution is the inflow of organic substances from the outside and the elution of nutrients from the bottom mud. Therefore, it is effective to remove and remove the bottom mud to improve the water quality of the lake. Is.
ところが、浚渫された泥土は含水比が高くて膨大な量となり、そのままでは、処分場所を確保することも再利用することも難しい。そのため、かかる浚渫泥土の減容化および強度増大を図ることが必要不可欠となる。 However, dredged mud has a high water content and a huge amount, and as it is, it is difficult to secure a disposal site and reuse it. Therefore, it is essential to reduce the volume and increase the strength of the dredged mud.
従来、浚渫泥土に凝集剤を添加して土粒子をあらかじめ凝集させ、しかる後にフィルタープレス等で脱水を行うことによって減容化を図るとともに、凝集剤とともに固化材を添加することによって処理土の強度向上を図っていた。 Conventionally, coagulant is added to dredged mud to pre-agglomerate the soil particles, and then the volume is reduced by dewatering with a filter press or the like, and the strength of the treated soil is increased by adding a solidifying material together with the coagulant. I was trying to improve.
しかしながら、含水比が高い浚渫泥土を一定の割合まで減容化させるとともにその強度を向上させるには、大量の凝集剤および固化材が必要となり、材料コストが高くつくという問題や、フィルタープレス等の脱水装置を用いた場合、全体の設備費用が高くなるとともに、広い設置スペースを確保せねばならないという問題を生じる。 However, in order to reduce the volume of dredged mud soil with a high water content to a certain ratio and improve its strength, a large amount of aggregating agent and solidifying material are required, resulting in high material costs, filter presses, etc. When a dehydrator is used, the overall equipment cost increases, and a problem arises that a large installation space must be secured.
そこで、本出願人は、新たな浚渫泥土の処理方法を開発し、脱水設備の設備規模の縮小及び凝集剤や固化材の使用量の節約を図ることに成功した。 Therefore, the present applicant has developed a new treatment method for dredged mud soil, and succeeded in reducing the equipment scale of the dewatering equipment and saving the use amount of the coagulant and the solidifying material.
しかしながら、かかる処理方法は、スクリューデカンタのオーバーフロー分を全量脱水処理するものであったため、脱水処理すべき量を減容化するにはどうしても限度があるとともに、オーバーフロー分であるがゆえに濃度が低く、脱水効率も悪いという問題を生じていた。 However, since this treatment method is to dehydrate the entire amount of the screw decanter overflow, there is a limit to reducing the volume to be dehydrated, and the concentration is low because of the overflow, There was a problem that the dehydration efficiency was poor.
本発明は、上述した事情を考慮してなされたもので、脱水設備の規模を大幅に縮小させるとともに脱水効率を向上させることが可能な浚渫泥土の処理方法を提供することを目的とする。 The present invention has been made in consideration of the above-described circumstances, and an object of the present invention is to provide a method for treating dredged mud that can greatly reduce the scale of a dewatering facility and improve the dewatering efficiency.
上記目的を達成するため、本発明に係る装置は請求項1に記載したように、海、河川、湖沼などの底泥を浚渫し、該浚渫された底泥からレキ分等の異物を取り除いた後、振動ふるい及びサイクロンからなる土砂分離装置で脱水分級処理し、該土砂分離装置のサイクロンオーバー分をスクリューデカンタで分級処理し、該スクリューデカンタによる分級処理でオーバーフローした分を濃縮槽に入れ、該濃縮槽内で沈降分離し、沈降分離で沈降した濃縮槽内の濃縮泥を脱水処理するものである。
In order to achieve the above-mentioned object, the apparatus according to the present invention drowns the bottom mud of the sea, rivers, lakes and the like as described in
本発明に係る浚渫泥土の処理方法においては、含水比の高い浚渫泥土をあらかじめ遠心分離によって分級するが、該分級処理でオーバーフローした分を全量脱水処理するのではなく、該オーバーフロー分を沈降分離し、しかる後、該沈降分離で沈降した濃縮泥を所定の方法で脱水処理する。 In the method for treating dredged mud according to the present invention, dredged mud with a high water content is classified by centrifugation in advance, but instead of dewatering the entire amount overflowed in the classified treatment, the overflow is settled and separated. Thereafter, the concentrated mud settled by the sedimentation is dehydrated by a predetermined method.
このようにすると、脱水処理すべき量は、本出願人が先に開発した浚渫泥土の処理方法(特開平 9-155395号公報)に比べて、1/2〜1/10にまで減容化される。また、脱水処理される濃縮泥の比重は、上述したオーバーフロー分よりも大きくなるため、脱水効率も向上する。 In this way, the amount to be dewatered can be reduced to 1/2 to 1/10 compared to the dredged soil treatment method (Japanese Patent Laid-Open No. 9-155395) previously developed by the applicant. Is done. In addition, since the specific gravity of the concentrated mud to be dewatered is larger than the above-described overflow, the dewatering efficiency is improved.
脱水処理方法は、フィルタープレス等の加圧脱水方式を採用してもよいし、スクリューデカンタ等の遠心分離方式を採用してもよい。ちなみに、後者の方法によれば、設備規模をさらにコンパクトにすることが可能となる。 As the dehydration method, a pressure dehydration method such as a filter press may be employed, or a centrifugal separation method such as a screw decanter may be employed. Incidentally, according to the latter method, the facility scale can be further reduced.
以下、本発明に係る浚渫泥土の処理方法の実施の形態について、添付図面を参照して説明する。なお、従来技術と実質的に同一の部品等については同一の符号を付してその説明を省略する。 DESCRIPTION OF EMBODIMENTS Hereinafter, embodiments of a dredged mud disposal method according to the present invention will be described with reference to the accompanying drawings. Note that components that are substantially the same as those of the prior art are assigned the same reference numerals, and descriptions thereof are omitted.
図1は、本実施形態に係る浚渫泥土の処理方法の流れを示したフローチャート、図2及び図3は、同じく設備構成図である。これらの図でわかるように、本実施形態に係る浚渫泥土の処理方法は、まず、海、河川、湖沼などの底泥1を浚渫船2によって浚渫する(図1、ステップ101)。浚渫された底泥1は、スクリーン3でレキ分等の異物を取り除いた後、原水槽4に貯留しておく。
FIG. 1 is a flow chart showing the flow of the dredged clay treatment method according to the present embodiment, and FIGS. 2 and 3 are equipment configuration diagrams. As can be seen from these drawings, in the dredged mud processing method according to the present embodiment, first, the
次に、原水槽4に貯留された泥土を振動ふるい及びサイクロンからなる土砂分離装置5で脱水分級処理する(ステップ102)。
Next, the mud soil stored in the raw water tank 4 is subjected to a dewatering and classifying process by the earth and
次に、土砂分離装置5のサイクロンオーバー分を排水原水槽21にいったん貯留した後、遠心分離機であるスクリューデカンタ6で分級処理する(ステップ103)。分級処理で生じたアンダー分は、ケーキとして排出する。
Next, after the cyclone over portion of the earth and
次に、スクリューデカンタ6による分級処理でオーバーフローした分を濃縮槽7に入れ、該濃縮槽内で沈降分離する(ステップ104)。濃縮槽7の上澄み水については、必要に応じて後述するpH調整槽14でpH調整し、しかる後、元の水域に放流する。 Next, the portion overflowed by the classification process by the screw decanter 6 is put into the concentration tank 7 and settled and separated in the concentration tank (step 104). About the supernatant water of the concentration tank 7, it adjusts pH with the pH adjustment tank 14 mentioned later as needed, and discharges it to the original water area after an appropriate time.
次に、沈降分離で沈降した濃縮槽7内の濃縮泥8をスラリー槽22にいったん貯留し、必要に応じて凝集剤を添加した後、脱水機であるフィルタープレス9で脱水処理する(ステップ105)。脱水処理で生じたアンダー分は、ケーキとして排出する。
Next, the concentrated mud 8 in the concentration tank 7 settled by the settling separation is temporarily stored in the
なお、脱水処理でオーバーフローした分については、ろ水槽10にいったん貯留した後、無機凝集剤タンク11に収容された無機凝集剤および高分子溶解貯蔵タンク12に貯蔵された高分子凝集剤を添加して角形シックナ13で凝集沈降させるとともに、その上澄み分をpH調整槽14で中和して放流し、凝集沈降分を濃縮槽7に戻す(ステップ106)。
In addition, about the part overflowed by the dehydration process, after having once stored in the
ここで、無機凝集剤としては、硫酸バンドやPACと呼ばれるポリ塩化アルミニウム等を使用し、高分子凝集剤としては、水溶性ポリアクリルアミドから製造された市販品から適宜選択することができる。 Here, as an inorganic flocculant, polyaluminum chloride called a sulfate band or PAC is used, and as a polymer flocculant, it can be appropriately selected from commercially available products manufactured from water-soluble polyacrylamide.
以上説明したように、本実施形態に係る浚渫泥土の処理方法によれば、スクリューデカンタ6による分級処理でオーバーフローした分を全量脱水処理するのではなく、該オーバーフロー分を濃縮槽7にて沈降分離し、しかる後、該沈降分離で沈降した濃縮泥8を脱水処理するようにしたので、フィルタープレス9で必要となる脱水処理量を、本出願人が先に開発した浚渫泥土の処理方法(特開平 9-155395号公報)に比べて、1/2〜1/10にまで減容化することが可能となるとともに、脱水処理される対象が濃縮泥8であるため、スクリューデカンタからのオーバーフロー分を直接脱水処理する場合に比べて脱水処理対象物、すなわち濃縮泥8の比重を大きくすることが可能となり、フィルタープレス9での脱水効率が飛躍的に向上する。 As described above, according to the dredged clay treatment method according to the present embodiment, the entire portion that has overflowed in the classification by the screw decanter 6 is not dewatered, but the overflow is settled and separated in the concentration tank 7. After that, since the concentrated mud 8 settled by the settling and separation was dewatered, the amount of dewatering required for the filter press 9 was determined by the dredging mud soil processing method (special Compared to Kaihei 9-155395), the volume can be reduced to 1/2 to 1/10, and the target to be dehydrated is concentrated mud 8, so the overflow from the screw decanter The specific gravity of the object to be dehydrated, that is, the concentrated mud 8, can be increased as compared with the case of directly dewatering the water, and the dewatering efficiency in the filter press 9 is dramatically improved.
そのため、脱水機であるフィルタープレス9の規模を大幅に縮小することができるとともに、それに伴って設備のイニシャルコストの低減及び設置スペースの縮小を図ることが可能となる。 Therefore, the scale of the filter press 9 as a dehydrator can be greatly reduced, and accordingly, the initial cost of equipment and the installation space can be reduced.
次に、本実施形態に係る浚渫泥土の処理方法の作用効果を確認する実験を行ったので、その概要について以下に説明する。 Next, since the experiment which confirms the effect of the treatment method of dredged mud according to this embodiment was performed, the outline thereof will be described below.
実験には、土粒子比重が2.6の浚渫泥土を使用し、上述の手順で浚渫泥土を処理した。結果を表1に示す。 In the experiment, dredged mud soil having a specific gravity of 2.6 was used, and the dredged mud was treated by the above-described procedure. The results are shown in Table 1.
ここで、同表中、ρSIはスクリューデカンタの供給側での比重、ρSOFは同じくオーバーフロー側での比重をそれぞれ示し、C1はスクリューデカンタからのオーバーフロー分に対する濃縮泥の容量比、C2は、スクリューデカンタへの供給分に対する濃縮泥の容量比をそれぞれ示す。また、濃縮泥の比重は、スクリューデカンタの供給側での比重に依存せず、約1.16となった。 In the table, ρ SI indicates the specific gravity on the supply side of the screw decanter, ρ SOF also indicates the specific gravity on the overflow side, C 1 indicates the volume ratio of the concentrated mud to the overflow from the screw decanter, and C 2 Indicates the volume ratio of the concentrated mud to the supply to the screw decanter. The specific gravity of the concentrated mud was about 1.16, not depending on the specific gravity on the screw decanter supply side.
以上の結果から、容量比C2(濃縮泥の容量/スクリューデカンタへの供給分の容量)、すなわち脱水処理前での減容化率は、10.5〜33.3%(1/10〜1/3)となることがわかる。また、脱水処理前での比重1.16は、オーバーフロー側での比重ρSOFよりも上回っていることがわかる。 From the above results, the volume ratio C 2 (concentrated mud volume / volume supplied to the screw decanter), that is, the volume reduction rate before the dehydration treatment was 10.5 to 33.3% (1/10 to 10%). It can be seen that 1/3). Further, it can be seen that the specific gravity 1.16 before the dehydration treatment exceeds the specific gravity ρ SOF on the overflow side.
本実施形態では、スクリューデカンタ6による分級処理でオーバーフローした分をそのまま濃縮槽7に入れて沈降分離させるようにしたが、スクリューデカンタ6のオーバーフロー分に無機凝集剤(PAC)や消石灰を添加して沈降分離の促進を図るようにしてもよい。 In the present embodiment, the portion overflowed in the classification process by the screw decanter 6 is put into the concentration tank 7 as it is for sedimentation separation, but an inorganic flocculant (PAC) or slaked lime is added to the overflow portion of the screw decanter 6. You may make it aim at promotion of sedimentation separation.
1 底泥
6 スクリューデカンタ(遠心分離による分級処理を行う設備)
7 濃縮槽(沈降分離を行う設備)
8 濃縮泥
9 フィルタープレス(脱水処理を行う設備)
1 Bottom mud 6 Screw decanter (equipment for classification by centrifugation)
7 Concentration tank (equipment for sedimentation)
8 Concentrated mud 9 Filter press (Dehydration equipment)
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CN104030536A (en) * | 2014-06-04 | 2014-09-10 | 安徽省交通航务工程有限公司 | Environment-friendly dredged sediment integrated mechanical deep-drying system |
CN104724893A (en) * | 2015-03-06 | 2015-06-24 | 三川德青科技有限公司 | Dredging and classified dewatering treatment method and system for sludge in urban river box culvert |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN104030536A (en) * | 2014-06-04 | 2014-09-10 | 安徽省交通航务工程有限公司 | Environment-friendly dredged sediment integrated mechanical deep-drying system |
CN104724893A (en) * | 2015-03-06 | 2015-06-24 | 三川德青科技有限公司 | Dredging and classified dewatering treatment method and system for sludge in urban river box culvert |
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