JPH0649200B2 - Treatment method for wet excavated soil - Google Patents
Treatment method for wet excavated soilInfo
- Publication number
- JPH0649200B2 JPH0649200B2 JP63259367A JP25936788A JPH0649200B2 JP H0649200 B2 JPH0649200 B2 JP H0649200B2 JP 63259367 A JP63259367 A JP 63259367A JP 25936788 A JP25936788 A JP 25936788A JP H0649200 B2 JPH0649200 B2 JP H0649200B2
- Authority
- JP
- Japan
- Prior art keywords
- soil
- polymer
- water
- excavated
- added
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21D—SHAFTS; TUNNELS; GALLERIES; LARGE UNDERGROUND CHAMBERS
- E21D9/00—Tunnels or galleries, with or without linings; Methods or apparatus for making thereof; Layout of tunnels or galleries
- E21D9/06—Making by using a driving shield, i.e. advanced by pushing means bearing against the already placed lining
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21D—SHAFTS; TUNNELS; GALLERIES; LARGE UNDERGROUND CHAMBERS
- E21D9/00—Tunnels or galleries, with or without linings; Methods or apparatus for making thereof; Layout of tunnels or galleries
- E21D9/06—Making by using a driving shield, i.e. advanced by pushing means bearing against the already placed lining
- E21D9/0642—Making by using a driving shield, i.e. advanced by pushing means bearing against the already placed lining the shield having means for additional processing at the front end
- E21D9/0678—Adding additives, e.g. chemical compositions, to the slurry or the cuttings
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21D—SHAFTS; TUNNELS; GALLERIES; LARGE UNDERGROUND CHAMBERS
- E21D9/00—Tunnels or galleries, with or without linings; Methods or apparatus for making thereof; Layout of tunnels or galleries
- E21D9/12—Devices for removing or hauling away excavated material or spoil; Working or loading platforms
- E21D9/13—Devices for removing or hauling away excavated material or spoil; Working or loading platforms using hydraulic or pneumatic conveying means
Landscapes
- Engineering & Computer Science (AREA)
- Mining & Mineral Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Excavating Of Shafts Or Tunnels (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、土圧系シールドまたは推進工法のトンネル工
事現場等から発生する含水掘削残土の流動性を消失させ
る土質改良工法に関する。Description: [Industrial application] The present invention relates to a soil improvement method for eliminating the fluidity of water-containing excavated residual soil generated from a tunnel construction site of an earth pressure system shield or a propulsion method.
上記掘削残土は、カッターチャンバー内等から排出され
易い様に流動性を有するとともに止水性を保つ性質があ
る。流動性の管理は、スランプ試験により行われスラン
プ値5cm以上の場合が多い。ダンプカー等による輸送
も非効率である事から従来より各種の流動性消失法が検
討されてきた。The above-mentioned excavated soil has a fluidity so as to be easily discharged from the inside of the cutter chamber and the like, and has a property of maintaining water stopping property. The fluidity is controlled by a slump test and often has a slump value of 5 cm or more. Since transportation by dump trucks etc. is also inefficient, various liquidity disappearance methods have been studied conventionally.
[従来の技術] 含水残土の流動性を除去する為、残土ホッパー内自然放
置や天日乾燥等が行われている。[Prior Art] In order to remove the fluidity of the hydrated residual soil, the residual soil hopper is left to stand naturally or is dried in the sun.
薬剤を添加する例としてはセメント系(特公昭62−4
200,特公昭60−87813)、石灰系(特公昭6
2−318)、高吸水性樹脂(特開昭59−13548
8)等が公知である他、グアーガム等が用いられてい
る。また含水率を下げながら流動性を保持する為気泡を
混入し、消泡により流動性を除去する気泡シールド工法
も提案されている。(特公昭58−47560,特公昭
59−49999) [従来の技術の問題点] 薬剤を用いる処理法においてセメント系ならびに石灰系
の固化剤は、アルカリ性粉塵による作業環境の悪化及び
経時固化によるホッパー閉塞の危険性等がある。As an example of adding a chemical, a cement type (Japanese Patent Publication No. 62-4
200, Japanese Patent Publication 60-87813), lime type (Japanese Patent Publication 6)
2-318), a highly water-absorbent resin (JP-A-59-13548).
8) and the like are known, and guar gum and the like are used. Also, a bubble shield method has been proposed in which bubbles are mixed in order to maintain fluidity while reducing the water content, and fluidity is removed by defoaming. (JP-B-58-47560, JP-B-59-499999) [Problems of the prior art] In the treatment method using a chemical, the cement-based and lime-based solidifying agents deteriorate the working environment due to alkaline dust and block the hopper due to solidification over time. There is a risk of.
高吸水性樹脂の使用は高価である。The use of super absorbent resin is expensive.
グアーガムによる処理土はカビの発生や腐敗等により経
時的に変質を起こす為用途が限定される。また天然物で
あり価格の変動も大きく供給量にも不安がある。The application of guar gum-treated soil is limited because it deteriorates over time due to mold and rot. In addition, it is a natural product, and price fluctuations are large, so there is concern about supply.
[問題点を解決する為の手段] 本発明者は上記の問題を解決すべく鋭意検討した結果、
本発明に到達した。[Means for Solving Problems] As a result of earnest studies to solve the above problems, the present inventor found that
The present invention has been reached.
本発明は前記トンネル工事現場で発生する含水掘削残土
に、アニオン性アクリル系高分子凝集剤分散液とカチオ
ン性有機高分子凝結剤水溶液を含水掘削残土に対し、両
者合わせたポリマー純分として0.01〜0.5重量%
を逐次添加混練する事を特徴とする。In the present invention, the water-containing excavation residual soil generated at the tunnel construction site has an anionic acrylic polymer flocculant dispersion liquid and a cationic organic polymer coagulant aqueous solution as a total polymer content of the water-containing excavation residual soil. 01-0.5% by weight
It is characterized by sequentially adding and kneading.
ここに使用する2液はいずれも粘度1万CP以下であり
濃度10%以上である事が望ましい。It is desirable that the two liquids used here have a viscosity of 10,000 CP or less and a concentration of 10% or more.
粘度が高すぎると混練不均一となり、濃度が低すぎると
残土に多量の水を加える結果、流動防止に悪影響を与え
る。本発明に用いるアニオン性アクリル系高分子凝集剤
としてはアニオン化率3〜100モル%のアクリルアミ
ドとアクリル酸塩の共重合物、アクリルアミドと2−ア
クリルアミドアルキルスルホン酸塩の共重合物等の中か
ら分子量100万以上好ましくは200万以上のアクリ
ル系水溶性高分子が適用され、粒径100μm以下の微
粒子として油または塩水溶液中に分散させた状態で用い
られる。If the viscosity is too high, the kneading becomes uneven, and if the concentration is too low, a large amount of water is added to the residual soil, which adversely affects flow prevention. The anionic acrylic polymer flocculant used in the present invention is selected from among copolymers of acrylamide and acrylate having an anionization rate of 3 to 100 mol%, copolymers of acrylamide and 2-acrylamidoalkyl sulfonate, and the like. An acrylic water-soluble polymer having a molecular weight of 1,000,000 or more, preferably 2,000,000 or more is applied, and is used in the state of being dispersed as fine particles having a particle diameter of 100 μm or less in an oil or an aqueous salt solution.
かかる分散液の製造法は公知であり、油中水型エマルジ
ョンは特公昭34−10644、特公昭52−3941
7及び特公昭55−45783に記載され、塩水溶液中
分散液の製造法は特公昭46−14907及び特開昭6
2−20511に記載されている。一方のカチオン性有
機高分子凝結剤としては分子中にアミノ基又はアンモニ
ウム塩基を含有する分子量100万以下の水溶性高分子
であり、ポリマー純分あたり3meq/g以上のカチオ
ン度を有する。Methods for producing such dispersions are known, and water-in-oil emulsions are disclosed in JP-B-34-10644 and JP-B-52-3941.
7 and JP-B-55-45783, and a method for producing a dispersion in an aqueous salt solution is described in JP-B-46-14907 and JP-A-6-1987.
2-20511. On the other hand, the cationic organic polymer coagulant is a water-soluble polymer having an amino group or ammonium base in the molecule and having a molecular weight of 1,000,000 or less, and has a cation degree of 3 meq / g or more per polymer content.
具体的にはエピハロヒドリン、アルキレンジハライド、
アルキレン多価エポキサイド等を連結剤としてアミンま
たはアンモニアを縮合させた反応物(特公昭38−26
794、特公昭41−17965、特公昭51−224
71、特公昭56−37844等)又はホルムアルデヒ
トを連結剤としてジシアンジアミド、メラミン、グアニ
ジン等の縮合反応物あるいはポリエチレンイミン、ポリ
ジメチルジアリルアンモニウムクロライド、ジアルキル
アミノアルキルアクリレート塩及び又はその四級化物の
(共)重合体等を例示する事ができる。Specifically, epihalohydrin, alkylene dihalide,
A reaction product obtained by condensing an amine or ammonia with an alkylene polyvalent epoxide or the like as a linking agent (Japanese Patent Publication No. 38-26).
794, JP-B-41-17965, JP-B-51-224
71, Japanese Examined Patent Publication No. 56-37844) or formaldehyde, or a condensation reaction product of dicyandiamide, melamine, guanidine or the like, or polyethyleneimine, polydimethyldiallylammonium chloride, dialkylaminoalkyl acrylate salt and / or its quaternary compound (co). Examples thereof include polymers and the like.
これらカチオン性有機高分子凝集剤は濃度10%以上の
水溶液状態で用いられる。These cationic organic polymer flocculants are used in an aqueous solution state having a concentration of 10% or more.
これら2液を含水掘削残土に混練するには、連続ミキサ
ー、強制攪拌ミキサー等の混練機を使用する他、パワー
ショベル、スクリューコンベア等の土木機械を用いる事
も可能である。本発明における2液の含水残土に対する
添加混練は一方が均一に混合した後、他方を添加混練す
る必要があり、同時添加は高分子の不溶化等のトラブル
を招く。In order to knead these two liquids into the water-containing excavated residual soil, it is possible to use a kneading machine such as a continuous mixer or a forced agitation mixer, as well as a civil engineering machine such as a power shovel or a screw conveyor. In the addition and kneading of the two-part hydrous residual soil in the present invention, it is necessary that one is uniformly mixed and then the other is added and kneaded, and simultaneous addition causes troubles such as insolubilization of the polymer.
2液の添加混練順序は任意であるが、アニオン性アクリ
ル系高分子凝集剤分散液を先に添加した場合の方が最終
処理土の性状が好ましい。処理土からの水分分離を防止
する為に高吸水性樹脂を併用することも可能である。The order of addition and kneading of the two liquids is arbitrary, but the properties of the final treated soil are more preferable when the anionic acrylic polymer coagulant dispersion liquid is added first. It is also possible to use a highly water-absorbent resin together in order to prevent the separation of water from the treated soil.
[作用] 本発明の最大の特徴はイオン性を異にする2種のポリマ
ーを併用する事により、粘着性(曳系性)を現出する事
無く含水掘削残土の物性を改善し固化する事を目的とす
る。残土の種類によってアニオン性もしくはカチオン性
ポリマーの何れか一方のみを使用しても或る程度の流動
防止効果を付与する事はできるが粘着性(曳系性)の点
で不満がある。また粉末状あるいは高粘稠ポリマーを含
水残土に均一に混練する事は困難である。[Operation] The greatest feature of the present invention is that by using two kinds of polymers having different ionic properties in combination, the physical properties of the hydrous excavated residual soil are improved and solidified without revealing tackiness (pulling property). With the goal. Depending on the type of the remaining soil, even if only one of the anionic polymer and the cationic polymer is used, a certain degree of anti-fluidity effect can be imparted, but it is unsatisfactory in terms of tackiness (stretchability). Further, it is difficult to uniformly knead the powdery or highly viscous polymer into the hydrous residual soil.
本発明においてアニオン性アクリル系高分子凝集剤は低
粘度の微粒子分散液として添加される為、含水掘削残土
に容易に混合し、土粒子表面に吸着被覆する。カチオン
性有機高分子凝結剤は前記ポリマーのアニオン性基と電
気的に結合し、不溶化析出すると共に強固な接着力を与
える。添加順序が逆になった場合も類似の現象が起こる
と考えられる。In the present invention, the anionic acrylic polymer flocculant is added as a low-viscosity fine particle dispersion liquid, so that it is easily mixed with the water-containing excavated residual soil and adsorbed and coated on the surface of the soil particles. The cationic organic polymer coagulant electrically binds to the anionic groups of the polymer, insolubilizes and precipitates, and provides a strong adhesive force. A similar phenomenon is considered to occur when the order of addition is reversed.
[実施例] 次に本発明を実施例によって説明するが、本発明はその
要旨を越えない限り、以下の実施例に制約されるもので
はない。EXAMPLES Next, the present invention will be described with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist.
合成例−1 攪拌装置、温度計、還流冷却器、窒素導入管を備えた1
の四つ口セパブルフラスコに中油(比重0.83、引
火点138℃)300gを仕込み、ソルビタンモノオレ
ート30gと2.2′−アゾビスイソブチロニトリル
0.3gを室温にて添加溶解した。別にアクリルアミド
133gとアクリル酸アンモニウム167gをイオン交
換水325gに溶解したモノマー溶液を調整後、前述の
セパラブルフラスコ内に注入し攪拌した。Synthesis Example-1 1 equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen inlet tube
300 g of medium oil (specific gravity 0.83, flash point 138 ° C.) was charged into a 4-necked separable flask, and 30 g of sorbitan monooleate and 0.3 g of 2.2′-azobisisobutyronitrile were added and dissolved at room temperature. . Separately, a monomer solution prepared by dissolving 133 g of acrylamide and 167 g of ammonium acrylate in 325 g of ion-exchanged water was prepared, and then poured into the aforementioned separable flask and stirred.
30分間窒素置換を行った後、内温を60℃とし5時間
重合反応を行った。得られたエマルジョンにポリオキシ
エチレンソルビタントリオレート45gを添加混合した
液を試料−1と呼ぶ。試料−1の粘度は25℃にて11
00cpである分子量は600万であった。After performing nitrogen substitution for 30 minutes, the internal temperature was set to 60 ° C. and the polymerization reaction was performed for 5 hours. A liquid obtained by adding and mixing 45 g of polyoxyethylene sorbitan trioleate to the obtained emulsion is referred to as Sample-1. Sample-1 has a viscosity of 11 at 25 ° C.
The molecular weight of 00 cp was 6 million.
合成例−2 合成例−1に使用したと同様のセパラブルフラスコに中
油(比重0.83、引火点138℃)282gを仕込
み、ソルビタンモノオレート10g、ICI社製ハイパ
ーマーB−246 20g及び過酸化ラウロイル0.3
gを室温にて、アルカリ溶解した。別にアクリルアミド
262gとアクリル酸ナトリウム38gをイオン交換水
328gに溶解したモノマー溶液を調整後、前述のセパ
ラブルフラスコ内に注入し攪拌した。30分間窒素置換
を行った後内温を40℃に調整後、アスコルピン酸10
%水溶液0.6mlを添加し重合を開始した。内温を6
5℃に保持し、5時間重合反応を行った後、得られたエ
マルジョンにポリオキシエチレンノニルフェニルエーテ
ル20gとポリオキシエチレンソルビタントリオレート
40gを加えた液を試料−2と呼ぶ。試料−2の粘度は
20℃にて980cpであり、ポリマーの分子量は30
0万であった。Synthesis Example-2 282 g of medium oil (specific gravity 0.83, flash point 138 ° C) was charged in the same separable flask as used in Synthesis Example-1, sorbitan monooleate 10 g, ICI Hypermer B-246 20 g and excess. Lauroyl oxide 0.3
g was dissolved in alkali at room temperature. Separately, 262 g of acrylamide and 38 g of sodium acrylate were dissolved in 328 g of ion-exchanged water to prepare a monomer solution, which was then poured into the aforementioned separable flask and stirred. After purging with nitrogen for 30 minutes, the internal temperature was adjusted to 40 ° C. and then ascorbic acid 10
% Aqueous solution 0.6 ml was added to initiate polymerization. Internal temperature 6
A liquid in which 20 g of polyoxyethylene nonyl phenyl ether and 40 g of polyoxyethylene sorbitan trioleate are added to the obtained emulsion after maintaining at 5 ° C. and performing a polymerization reaction for 5 hours is referred to as Sample-2. Sample-2 has a viscosity of 980 cp at 20 ° C. and a polymer molecular weight of 30.
It was 0,000.
合成例−3 攪拌装置、温度計、還流冷却器及び500mlの滴下漏
斗を備えた1の四つ口セパラブルフラスコにエピクロ
ルヒドリン370gを仕込み、攪拌下内温を10〜45
℃に調節しながら、ジメチルアミン40%水溶液400
gを滴下した。2時間を要して滴下終了後ペンタエチレ
ンヘキサミン40gを添加し内温65〜70℃に保持し
縮合反応を行った。内容物粘度が15,000cpに増
粘した状態で25%硫酸水溶液225gを加え縮合反応
を停止させた。得られたポリカチオン水溶液を試料−3
と呼ぶ。試料−3の粘度は25℃にて5300cpであ
った。Synthesis Example-3 Epichlorohydrin (370 g) was charged into a four-necked separable flask (1) equipped with a stirrer, a thermometer, a reflux condenser and a 500-ml dropping funnel, and the internal temperature under stirring was 10 to 45.
While adjusting to ℃, 40% dimethylamine aqueous solution 400
g was added dropwise. After the dropping was completed over 2 hours, 40 g of pentaethylenehexamine was added and the internal temperature was maintained at 65 to 70 ° C to carry out the condensation reaction. The condensation reaction was stopped by adding 225 g of a 25% aqueous solution of sulfuric acid while the viscosity of the contents was increased to 15,000 cp. The obtained polycationic aqueous solution was used as Sample-3.
Call. The viscosity of Sample-3 was 5300 cp at 25 ° C.
実施例−1 某土木会社の土圧シールド工法によるトンネル工事作業
所の排泥貯槽より採取した含水掘削残土を5mm目のふ
るいにより粗大塊を取り除き試験に供した。Example-1 A lump of coarse lumps was removed from a water-containing excavated residual soil collected from a sludge storage tank of a tunnel construction work site by a soil pressure shield construction method of a civil engineering company, and a test was performed.
その掘削残土の物性値は下記のとおり。The physical properties of the excavated soil are as follows.
上記掘削残土4kgをビニール袋に採取し表−1に記載
した量の試料−1を加え、手で1分間練り混ぜた後、試
料−3を加え、再度練り混ぜて貫入抵抗値を測定した。
結果を表−1に示す。なお添加量は全て含水残土に対す
るポリマー純分あたりの数値である。 4 kg of the above excavated soil was collected in a vinyl bag, sample-1 in the amount shown in Table-1 was added, and after kneading by hand for 1 minute, sample-3 was added and kneaded again to measure the penetration resistance value.
The results are shown in Table-1. The addition amounts are all values per polymer pure content with respect to the residual hydrated soil.
貫入抵抗値が0.3kg/cm2以上であれば一般的に
運搬に際して大きな困難を認められない。 If the penetration resistance value is 0.3 kg / cm 2 or more, generally no great difficulty is recognized in transportation.
この試験における貫入抵抗値の測定方法は次のとおり。The method of measuring the penetration resistance value in this test is as follows.
コンクリートの凝結時間測定用の貫入抵抗測定装置に断
面積7.5cm2の貫入針を取り付け直径15cmの金
属円筒内に満たした処理土に貫入針を10秒間かかって
25mm貫入させて抵抗値を測定する。The penetration resistance measuring device for measuring the setting time of concrete was equipped with a penetration needle with a cross-sectional area of 7.5 cm 2 and the resistance value was measured by allowing the penetration needle to penetrate 25 mm into the treated soil filled in a metal cylinder with a diameter of 15 cm for 10 seconds. To do.
実施例−2 実施例−1と同じ掘削残土に先ず試料−3を添加混練
後、試料−1を加えて混練する以外は実施例−1と同様
の操作を行い、貫入抵抗値を測定した。結果を表−2に
示す。Example-2 A penetration resistance value was measured by performing the same operation as in Example-1, except that Sample-3 was first added and kneaded to the same excavated soil as in Example-1, and then Sample-1 was added and kneaded. The results are shown in Table-2.
実施例−3 実施例−1と同一の掘削残土に先ず試料−2を添加混練
後、試料−3を添加する以外は実施例−1と同様の操作
を行い、貫入抵抗値を測定した。結果を表−3に示す。 Example-3 A penetration resistance value was measured by performing the same operation as in Example-1, except that Sample-2 was first added and kneaded to the same excavated soil as in Example-1, and then Sample-3 was added. The results are shown in Table-3.
比較例−1 実施例−1と同一の掘削残土にアクリルアミド・アクリ
ル酸ナトリウム共重合物(アニオン化率20モル%・分
子量1200万)から成る、粉末状の高分子凝集剤ハイ
モロックSS−120(協立有機製)を添加混練後試料
−3を添加混練した処理土の貫入抵抗値を測定した。結
果を表−4に示す。 Comparative Example-1 A powdery polymer flocculant Hymolok SS-120 (Kyohin Co., Ltd.), which is composed of the same excavated soil as in Example 1 and is composed of an acrylamide-sodium acrylate copolymer (anionization rate: 20 mol%, molecular weight: 12 million) The puncture resistance value of the treated soil in which Sample-3 was added and kneaded after adding and kneading was measured. The results are shown in Table-4.
比較例−2 実施例−1と同一の掘削残土に試料−1を添加混練した
のみの処理土の貫入抵抗値を測定した。結果を表−5に
示す。 Comparative Example-2 The penetration resistance value of the treated soil obtained by only adding and kneading Sample-1 to the same excavated soil as in Example-1 was measured. The results are shown in Table-5.
比較例−3 実施例−1と同一の掘削残土に試料−1を添加混練後、
市販液体PAC(ポリ塩化アルミニウム)を添加混練し
た処理土の貫入抵抗値を測定した。結果を表−6に示
す。 Comparative Example-3 After adding and kneading Sample-1 to the same excavated soil as in Example-1,
The penetration resistance value of the treated soil to which a commercial liquid PAC (polyaluminum chloride) was added and kneaded was measured. The results are shown in Table-6.
比較例−4 実施例−1と同一の掘削残土に試料−3を添加混練した
処理土の貫入抵抗値を測定した。結果を表−7に示す。 Comparative Example-4 The penetration resistance value of the treated soil obtained by adding and kneading Sample-3 to the same excavated soil as in Example-1 was measured. The results are shown in Table-7.
比較例−5 実施例−1と同一の掘削残土にグアーガムを添加混練し
た処理土の貫入抵抗値を測定した。結果を表−8に示
す。 Comparative Example-5 The penetration resistance value of the treated soil obtained by adding and kneading guar gum to the same excavated soil as in Example-1 was measured. The results are shown in Table-8.
Claims (1)
に対し、合算したポリマー純分量が0.01〜0.5重
量%となる様に、下記(A)項に示されるアクリル系高
分子凝集剤分散液と下記(B)項に示されるカチオン性
有機高分子凝集剤水溶液を逐次添加混練する操作によ
り、残土の流動性を消失させる事を特徴とする含水掘削
残土の処理方法。 (A)分子量が100万以上であり、アニオン化率が3
〜100モル%であるアクリル系水溶性高分子を、粒径
100μm以下の微粒子として含有する分散液。 (B)カチオン度が3meq/g以上であり、分子量が
100万以下であるカチオン性有機高分子凝結剤の水溶
液。1. An acrylic polymer as shown in the following item (A) so that the total polymer net content is 0.01 to 0.5% by weight with respect to the hydrous excavated soil having a slump value of 5 cm or more. A method for treating water-containing excavated residual soil, characterized in that the fluidity of the residual soil is eliminated by successively adding and kneading the flocculant dispersion liquid and the aqueous solution of a cationic organic polymer flocculant shown in item (B) below. (A) The molecular weight is 1,000,000 or more and the anionization rate is 3
Dispersion liquid containing up to 100 mol% of an acrylic water-soluble polymer as fine particles having a particle size of 100 μm or less. (B) An aqueous solution of a cationic organic polymer coagulant having a cation degree of 3 meq / g or more and a molecular weight of 1,000,000 or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63259367A JPH0649200B2 (en) | 1988-10-17 | 1988-10-17 | Treatment method for wet excavated soil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63259367A JPH0649200B2 (en) | 1988-10-17 | 1988-10-17 | Treatment method for wet excavated soil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02107400A JPH02107400A (en) | 1990-04-19 |
| JPH0649200B2 true JPH0649200B2 (en) | 1994-06-29 |
Family
ID=17333131
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63259367A Expired - Fee Related JPH0649200B2 (en) | 1988-10-17 | 1988-10-17 | Treatment method for wet excavated soil |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0649200B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3693273B2 (en) * | 1997-05-21 | 2005-09-07 | ハイモ株式会社 | Construction aggregate cleaning waste mud dewatering method |
| JP5969099B1 (en) * | 2015-09-07 | 2016-08-10 | 太平洋セメント株式会社 | Treatment method of mud generated by bubble shield method |
| JP7094517B2 (en) * | 2018-02-21 | 2022-07-04 | ハイモ株式会社 | Dehydration method of organic sludge |
-
1988
- 1988-10-17 JP JP63259367A patent/JPH0649200B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02107400A (en) | 1990-04-19 |
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