JP2004033812A - Cleaning method of polluted soil or the like and cleaning equipment - Google Patents
Cleaning method of polluted soil or the like and cleaning equipment Download PDFInfo
- Publication number
- JP2004033812A JP2004033812A JP2002190523A JP2002190523A JP2004033812A JP 2004033812 A JP2004033812 A JP 2004033812A JP 2002190523 A JP2002190523 A JP 2002190523A JP 2002190523 A JP2002190523 A JP 2002190523A JP 2004033812 A JP2004033812 A JP 2004033812A
- Authority
- JP
- Japan
- Prior art keywords
- surfactant
- contaminant
- soil
- liquid phase
- solid
- 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.)
- Granted
Links
- 239000002689 soil Substances 0.000 title claims abstract description 67
- 238000000034 method Methods 0.000 title claims description 37
- 238000004140 cleaning Methods 0.000 title description 7
- 239000004094 surface-active agent Substances 0.000 claims abstract description 62
- 239000007791 liquid phase Substances 0.000 claims abstract description 39
- 238000002156 mixing Methods 0.000 claims abstract description 33
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000002253 acid Substances 0.000 claims abstract description 15
- 238000000926 separation method Methods 0.000 claims abstract description 13
- 239000000203 mixture Substances 0.000 claims abstract description 7
- 239000007790 solid phase Substances 0.000 claims abstract description 7
- 239000007787 solid Substances 0.000 claims abstract description 5
- 239000000356 contaminant Substances 0.000 claims description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 239000000126 substance Substances 0.000 claims description 15
- 238000005406 washing Methods 0.000 claims description 13
- 239000003513 alkali Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000003672 processing method Methods 0.000 claims description 5
- 238000002844 melting Methods 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 238000000197 pyrolysis Methods 0.000 claims description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 2
- 229910052791 calcium Inorganic materials 0.000 claims description 2
- 239000011575 calcium Substances 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 229910010272 inorganic material Inorganic materials 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- 238000011109 contamination Methods 0.000 claims 1
- 239000011147 inorganic material Substances 0.000 claims 1
- 229910052749 magnesium Inorganic materials 0.000 claims 1
- 239000011777 magnesium Substances 0.000 claims 1
- 239000000377 silicon dioxide Substances 0.000 claims 1
- 239000003344 environmental pollutant Substances 0.000 abstract description 10
- 231100000719 pollutant Toxicity 0.000 abstract description 10
- 238000004062 sedimentation Methods 0.000 abstract description 5
- 238000002347 injection Methods 0.000 description 24
- 239000007924 injection Substances 0.000 description 24
- 239000000701 coagulant Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- -1 carboxylate salts Chemical class 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 150000002013 dioxins Chemical class 0.000 description 3
- 238000006386 neutralization reaction Methods 0.000 description 3
- 239000002736 nonionic surfactant Substances 0.000 description 3
- 238000005979 thermal decomposition reaction Methods 0.000 description 3
- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical compound C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000002202 Polyethylene glycol Substances 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000002280 amphoteric surfactant Substances 0.000 description 2
- 125000000129 anionic group Chemical group 0.000 description 2
- 239000003945 anionic surfactant Substances 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- KWIUHFFTVRNATP-UHFFFAOYSA-N glycine betaine Chemical compound C[N+](C)(C)CC([O-])=O KWIUHFFTVRNATP-UHFFFAOYSA-N 0.000 description 2
- 238000011086 high cleaning Methods 0.000 description 2
- 239000004021 humic acid Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000010979 pH adjustment Methods 0.000 description 2
- 229920001223 polyethylene glycol Polymers 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 125000003275 alpha amino acid group Chemical group 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 229960003237 betaine Drugs 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 229940043430 calcium compound Drugs 0.000 description 1
- 150000001674 calcium compounds Chemical class 0.000 description 1
- 239000003093 cationic surfactant Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000006298 dechlorination reaction Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 159000000014 iron salts Chemical class 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 150000003071 polychlorinated biphenyls Chemical class 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 150000008054 sulfonate salts Chemical class 0.000 description 1
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 1
Images
Landscapes
- Processing Of Solid Wastes (AREA)
- Physical Water Treatments (AREA)
- Removal Of Specific Substances (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】
【産業上の利用分野】
本発明は、汚染物質を含有する土壌等を処理する方法および装置に関するものであり、汚染土壌の他に埋立廃棄物や河川・湖沼あるいは海域の底泥、さらには水処理プロセスから発生する汚泥や脱水ケーキの浄化処理にも適用できる。
【0002】
【従来の技術】
汚染土壌等の浄化方法としては、熱分解する方法や微生物によって浄化する方法および薬剤により洗浄する方法等が従来知られている。熱分解する方法は、大量の汚染土壌をダイオキシン類等の汚染物質が分解する温度まで加温するためのエネルギーコストが高く、また微生物によって浄化する方法は浄化処理が終了するまでに年単位の期間を要するという欠点があった。薬剤により洗浄する方法に関しては、例えば特許第3182546号にトリクロロエチレン等で汚染された土壌を界面活性剤で洗浄する方法が示されている。しかし、本方法では洗浄水に含まれる汚染物質の除去に活性炭吸着処理を用いており、界面活性剤および土壌中の様々な有機物質を高濃度に含む洗浄液を活性炭処理するためにその交換頻度が高くなり、高価な活性炭を大量に使用するという問題があった。
【0003】
【発明が解決しようとする課題】
この発明は上記のような問題点を解決するためになされたもので、汚染土壌等に含有される汚染物質を効率よく除去する、汚染土壌等の浄化方法および浄化装置を提供することを目的とする。
【0004】
【課題を解決するための手段】
請求項1の発明は、汚染物質で汚染された土壌等と界面活性剤とを混合・洗浄することによって、該汚染物質を土壌等の固形分から液相に移行させる工程と、この工程の後に、該混合物を固液分離し、固相を浄化物として取り出す工程と、固液分離された液相から界面活性剤と汚染物質の結合体を分離する工程とを備えたことを特徴とする汚染土壌等の浄化方法である。この方法では、液相中の汚染物質および界面活性剤が結合した状態のままで液相から分離するため、清澄な液相が得られる。
【0005】
また、請求項2の発明は、汚染物質で汚染された土壌等と界面活性剤とを混合する前又は混合する際に該土壌等に酸又はアルカリを混合することを特徴とする請求項1に記載の汚染土壌等の浄化方法である。この方法では、土壌等に酸またはアルカリを添加することによって洗浄効果を高めることが出来る。
【0006】
また、請求項3,4,5および6の発明は、酸・アルカリの添加、加温、無機塩の添加または曝気・加圧水注入のいずれかの手段によって液相から界面活性剤と汚染物質の結合体を分離することを特徴とする請求項1および2に記載の処理方法である。又、これらの処理を適宜組み合わせることもできる。
また、請求項7の発明は、界面活性剤と汚染物質の結合体を分離された液相に界面活性剤を添加し、汚染物質で汚染された土壌等の洗浄に再度利用することを特徴とする請求項1乃至6の何れかに記載の処理方法である。この方法では、処理された液相を再利用することによって、補給水量および系外への排水量を大幅に削減することができる。
【0007】
また、請求項8の発明は、液相から分離された界面活性剤と汚染物質の結合体を焼却炉、溶融炉または熱分解炉に投入して汚染物質を加熱分解することを特徴とする請求項1乃至7の何れかに記載の処理方法である。この方法では、液相から分離された汚染物質を加熱分解することによって完全に無害化できる。
【0008】
また、請求項9の発明は、汚染物質で汚染された土壌等と界面活性剤とを混合・洗浄する混合手段、該混合物を固液分離する固液分離手段、固液分離された液相から界面活性剤と汚染物質の結合体を分離する分離手段とを備えることを特徴とする汚染土壌等の浄化装置である。本装置によって本発明の浄化方法を具現化することが出来る。
【0009】
【発明の実施の形態】
以下、本発明に関わる汚染土壌等の浄化方法および浄化装置の実施形態を図に基づいて説明する。
【0010】
(実施形態1)
図1は、本発明に関わる汚染土壌等の浄化方法の一実施形態を示したものである。同図において、1は第一混和槽、2は界面活性剤注入管、3は遠心脱水機、4は酸注入管、5は凝集剤注入管、6は第二混和槽、7は沈殿槽である。
【0011】
汚染物質を含む土壌等は第一混和槽1で界面活性剤注入管2から供給される界面活性剤と混和され、汚染土壌等に含有される汚染物質が液相へ移行する。次いで、遠心脱水機3へ供給され、界面活性剤と汚染物質の結合体を含む液相と、汚染物質が除去された固相とに分離される。固相はそのまま浄化物として取り出される。液相は、第二混和槽6において酸注入管4から供給される酸と凝集剤注入管5から供給される凝集剤と混和され、界面活性剤と汚染物質の結合体は不溶化・凝集された後、沈殿槽7においてスラッジとして沈殿分離される。スラッジは最終的に焼却炉にて焼却処理され、汚染物質は熱分解される。
【0012】
ここで、汚染物質とはダイオキシン類や環境ホルモン類、農薬、PCB等の難分解性有機物質やフッ素・ホウ素・重金属等の無機物質、さらにはこれらの物質と土壌微粒子とが吸着している結合体等であり、特定の物質に限定されるものではない。また、土壌等とは土壌、埋立廃棄物、河川・湖沼あるいは海域の底泥、さらには水処理プロセスから発生する汚泥やその脱水ケーキ等を指す。
【0013】
汚染土壌等の汚染物質含有量ができるだけ高い状態で処理を行った方が界面活性剤と汚染物質の接触効率が高まるため、混合操作を容易にできる範囲において、必要に応じて濃縮処理等を行って汚染土壌等中の有機物含有量を高めた後に界面活性剤と汚染土壌等との混合を実施する方が好ましい。もちろん、土壌等の処理においてそのままの形態では混合操作が困難である場合には、水分を混合操作が容易に行えるまで添加して処理を実施することもできる。
【0014】
本発明で用いる界面活性剤としては、アニオン型、カチオン型、両性型、非イオン型等の様々な界面活性剤を用いることができる。例えば、アニオン型としては、セッケン等のカルボン酸塩、硫酸エステル塩、スルホン酸塩等が、カチオン型として、アミン塩、第4級アンモニウム塩等が、両性型としてはアミノ酸型、ベタイン型等が、非イオン型としてはポリエチレングリコール型等を用いることが出来る。
【0015】
汚染土壌等と界面活性剤との混合・洗浄手段は本実施例に限定されるものではないが、通常攪拌機付の混和槽が用いられる。また、超音波照射手段を併用すると汚染土壌等と界面活性剤との接触効率を高めることができ好適である。このようにすることにより、汚染物質を土壌等の固形分から液相へ移行させることができる。
【0016】
汚染土壌等の固液分離手段としては、遠心脱水機の他に、スクリーン、沈殿槽、フィルタープレス等様々なものを用いることが出来る。
【0017】
液相からの界面活性剤と汚染物質との結合体の分離手段は、適用する界面活性剤の特性に応じて数種類の手段から選択することが出来る。適用する界面活性剤がアミノ酸型両性界面活性剤の場合には、本実施形態のように洗浄操作後に酸を添加してpHを等電点に調整することによって、不溶化することが出来る。また、ポリエチレングリコール型非イオン界面活性剤の場合には加温して曇点より高い温度とすることによって不溶化することが出来る。また、アニオン型界面活性剤の場合にはカルシウム等を主成分とする無機化合物を添加することによって、不溶性の塩を形成させることが出来る。不溶化させた界面活性剤と汚染物質の結合体は、その比重によって浮上または沈降といった手段で分離することができる。また、場合によっては遠心分離を適用することも出来る。
【0018】
なお、単に不溶化させることのみでは分離し難い場合には、凝集剤を添加・混和してフロックを形成させることにより分離を促進させることも可能である。この際に用いられる凝集剤としては、塩化第二鉄やポリ硫酸第二鉄等の鉄塩や、硫酸ばんどやPACのようなアルミニウム塩等が適用可能であり、さらにポリアクリルアミド等の有機高分子化合物を併用することも出来る。
【0019】
一方、起泡性のある界面活性剤を用いる場合には、液相を曝気するか、あるいは液相に気体が過飽和に溶解した加圧水を注入することによって多数の気泡を形成させ、気泡表面に界面活性剤と汚染物質の結合体をスカムとして濃縮して除去することができる。
【0020】
界面活性剤と汚染物質の結合体を分離した液相は、再度浄化処理に用いることが出来る。例えば、界面活性剤を添加して汚染土壌等と接触させることや、洗浄後の土壌に残存する界面活性剤のリンスに用いることが可能である。
【0021】
液相から分離された界面活性剤と汚染物質の結合体は処理前の汚染土壌に比べて濃縮されるため、量が著しく減少する。したがって、オゾン注入による酸化分解や紫外線照射による脱塩素等の様々な手段を用いて低コストに無害化することが可能であるが、加熱方式により短時間でほぼ完全に分解することができる。特に既設の焼却炉、溶融炉または熱分解炉が土壌浄化設備の近傍に存在する場合には、液相から分離された界面活性剤と汚染物質の結合体を該加熱方式設備で処理することにより、設備の建設費を削減できるため好適である。
【0022】
(実施形態2)
図2は、本発明に関わる汚染土壌等の浄化方法の別の実施形態を示したものである。同図において、1は第一混和槽、2は界面活性剤注入管、3は遠心脱水機、4は酸注入管、5は凝集剤注入管、8はpH調整槽、9は中和槽、10はアルカリ注入管、11は処理水循環管、12は第三混和槽、13は浮上分離槽、14は加圧水注入管である。
【0023】
汚染土壌等はpH調整槽8で酸注入管4から供給される酸、処理水循環管11より供給される処理水および補給水と混和され、汚染土壌等に含有されるカルシウム化合物を溶解させる。次に中和槽9においてアルカリ注入管10より供給されるアルカリと混和されてpHを中性に調整される。引き続いて第一混和槽1において界面活性剤注入管2から供給される界面活性剤と混合された後に遠心脱水機3において界面活性剤と汚染物質の結合体を含む液相と、汚染物質が除去された固相とに分離される。液相は、浮上分離槽13において凝集剤注入管5から供給される凝集剤および加圧水注入管14から供給される空気を過飽和に溶解した加圧水と混和され、界面活性剤および汚染物質の結合体は気泡表面に濃縮された後、スカムとして浮上分離され、残余が処理水となる。一方、遠心脱水機で取り出された固相はいったん第三混和槽12において処理水と混合された後に再度遠心脱水機3で固液分離されることにより、残留する界面活性剤と汚染物質の結合体を洗い出した後に浄化物として取り出される。
【0024】
汚染土壌等が石灰成分や鉄、マンガン等の金属成分の含有量が多くこれらが汚染物質と界面活性剤との接触を妨げて高い洗浄効率が得られない場合は、本実施形態のように汚染土壌等と界面活性剤の混合前あるいは混合中に酸を混合して石灰成分や金属成分を溶解させると接触効率が向上して良好な洗浄効果が得られる。一方、汚染土壌等がフミン酸等の有機物の含有量が多く、対象汚染物質と界面活性剤との接触を妨げて高い洗浄効率が得られない場合は、汚染土壌等と界面活性剤の混合前あるいは混合中にアルカリを混合してフミン酸等の有機物を溶解させると接触効率が向上して良好な洗浄効果が得られる。
【0025】
また、本実施形態のように得られた処理水を遠心脱水後の固形分のリンスや界面活性剤の溶解、浄化対象物の水分調整に用いることによって、全体の使用水量を低減でき、浄化コストの低減と排水量の削減の効果が得られる。
【0026】
【実施例】
ダイオキシン類で汚染された土壌を図2に示した処理方法で処理した結果を表1に示した。但し、処理条件は次の通りである。
【0027】
[実施例処理方法]
・界面活性剤の種類:ノニオン界面活性剤(アルコール系)
・界面活性剤との反応時間:30分
・反応温度:常温
・界面活性剤注入率:0.5wt%
【表1】
【0028】
【0029】
【発明の効果】
本発明による処理方法は汚染土壌等と界面活性剤とを撹拌・混合することによって、汚染土壌等に含有される汚染物質を高効率に除去すると共に、洗浄水中の界面活性剤と汚染物質との結合体を効率的に水相から分離するといった効果を奏する。
【図面の簡単な説明】
【図1】本発明に係る汚染土壌等の浄化方法の実施形態を示す図。
【図2】本発明に係る汚染土壌等の浄化方法の別の実施形態を示す図。
【符号の説明】
1…第一混和槽、2…界面活性剤注入管、3…遠心脱水機、4…酸注入管、5…凝集剤注入管、6…第二混和槽、7…沈殿槽、8…pH調整槽、9…中和槽、10…アルカリ注入管、11…処理水循環管、12…第三混和槽、13…浮上分離槽、14…加圧水注入管。[0001]
[Industrial applications]
The present invention relates to a method and an apparatus for treating soil or the like containing pollutants, and in addition to contaminated soil, landfill waste and sediment of rivers, lakes and marshes or sea areas, and sludge generated from a water treatment process. It can also be applied to the purification treatment of dehydrated cake.
[0002]
[Prior art]
As a method for purifying contaminated soil and the like, a method of thermal decomposition, a method of purifying with microorganisms, a method of cleaning with chemicals, and the like are conventionally known. The thermal decomposition method has a high energy cost to heat a large amount of contaminated soil to a temperature at which contaminants such as dioxins can be decomposed, and the method of purifying by microorganisms requires a period of years until the purification treatment is completed. However, there is a disadvantage that the Regarding the method of washing with a chemical, for example, Japanese Patent No. 3182546 discloses a method of washing soil contaminated with trichloroethylene or the like with a surfactant. However, in this method, activated carbon adsorption treatment is used to remove contaminants contained in the wash water, and the replacement frequency is high because the cleaning solution containing surfactants and various organic substances in soil at a high concentration is activated carbon treated. There has been a problem that the cost becomes high and expensive activated carbon is used in large quantities.
[0003]
[Problems to be solved by the invention]
The present invention has been made in order to solve the above problems, and an object thereof is to provide a method and a device for purifying contaminated soil and the like, which efficiently remove contaminants contained in the contaminated soil and the like. I do.
[0004]
[Means for Solving the Problems]
The invention of claim 1 provides a step of mixing and washing a soil or the like contaminated with a contaminant and a surfactant to transfer the contaminant from a solid content of the soil or the like to a liquid phase, and after this step, A contaminated soil, comprising: a step of solid-liquid separating the mixture to remove a solid phase as a purified substance; and a step of separating a complex of a surfactant and a contaminant from the solid-liquid separated liquid phase. And so on. In this method, a contaminant and a surfactant in the liquid phase are separated from the liquid phase while being bound, so that a clear liquid phase is obtained.
[0005]
The invention according to
[0006]
Further, the invention of
The invention according to claim 7 is characterized in that a surfactant is added to the separated liquid phase of the conjugate of the surfactant and the contaminant, and the resultant is reused for cleaning soil and the like contaminated with the contaminant. A processing method according to any one of claims 1 to 6. In this method, by reusing the treated liquid phase, the amount of makeup water and the amount of drainage to the outside of the system can be significantly reduced.
[0007]
The invention according to
[0008]
A ninth aspect of the present invention provides a mixing means for mixing and washing a soil or the like contaminated with a pollutant and a surfactant, a solid-liquid separation means for solid-liquid separation of the mixture, and a solid-liquid separation liquid phase. An apparatus for purifying contaminated soil or the like, comprising: a separation unit that separates a combination of a surfactant and a contaminant. The purification method of the present invention can be realized by the present apparatus.
[0009]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of a method and a device for purifying contaminated soil according to the present invention will be described with reference to the drawings.
[0010]
(Embodiment 1)
FIG. 1 shows an embodiment of a method for purifying contaminated soil and the like according to the present invention. In the figure, 1 is a first mixing tank, 2 is a surfactant injection pipe, 3 is a centrifugal dehydrator, 4 is an acid injection pipe, 5 is a coagulant injection pipe, 6 is a second mixing tank, and 7 is a sedimentation tank. is there.
[0011]
The soil or the like containing the contaminants is mixed with the surfactant supplied from the
[0012]
Here, the pollutants are dioxins, environmental hormones, pesticides, hardly decomposable organic substances such as PCBs, inorganic substances such as fluorine, boron, and heavy metals, and the binding between these substances and soil fine particles. Body, etc., and is not limited to a specific substance. The soil and the like refer to soil, landfill waste, bottom mud of rivers, lakes and marshes, or sea areas, as well as sludge generated from a water treatment process and its dewatered cake.
[0013]
If the treatment is performed with the contaminant content as high as possible in the contaminated soil, etc., the efficiency of contact between the surfactant and the contaminant will be increased. It is more preferable to mix the surfactant with the contaminated soil or the like after increasing the organic matter content in the contaminated soil or the like. Of course, when the mixing operation is difficult in the form of treating soil or the like as it is, it is possible to add water until the mixing operation can be easily performed to perform the processing.
[0014]
As the surfactant used in the present invention, various surfactants such as anionic, cationic, amphoteric, and nonionic surfactants can be used. For example, carboxylate salts such as soaps, sulfate ester salts, sulfonate salts, etc., as the anionic type, amine salts, quaternary ammonium salts, etc., as the cationic type, and amino acid type, betaine type, etc. as the amphoteric type. As the nonionic type, a polyethylene glycol type or the like can be used.
[0015]
The means for mixing and washing the contaminated soil and the like with the surfactant is not limited to this embodiment, but a mixing tank equipped with a stirrer is usually used. Also, it is preferable to use ultrasonic irradiation means in combination, because the efficiency of contact between the contaminated soil and the like and the surfactant can be increased. By doing so, the contaminants can be transferred from the solid content such as soil to the liquid phase.
[0016]
Various means such as a screen, a sedimentation tank, and a filter press can be used as a solid-liquid separation means for contaminated soil and the like, in addition to a centrifugal dehydrator.
[0017]
The means for separating the conjugate of the surfactant and the contaminant from the liquid phase can be selected from several means depending on the characteristics of the surfactant to be applied. When the applied surfactant is an amino acid type amphoteric surfactant, it can be insolubilized by adding an acid after the washing operation and adjusting the pH to the isoelectric point as in the present embodiment. In the case of a polyethylene glycol type nonionic surfactant, it can be insolubilized by heating to a temperature higher than the cloud point. In the case of an anionic surfactant, an insoluble salt can be formed by adding an inorganic compound containing calcium or the like as a main component. The conjugate of the insolubilized surfactant and the contaminant can be separated by means such as floating or sedimentation depending on the specific gravity. In some cases, centrifugation can be applied.
[0018]
In the case where separation is difficult only by simply insolubilizing, separation can be promoted by adding and mixing a flocculant to form flocs. As the coagulant used at this time, iron salts such as ferric chloride and ferric polysulfate, aluminum salts such as sulfate and PAC, and the like, and organic salts such as polyacrylamide can be used. Molecular compounds can be used in combination.
[0019]
On the other hand, when a foaming surfactant is used, a large number of bubbles are formed by aerating the liquid phase or by injecting pressurized water in which a gas is dissolved in supersaturation into the liquid phase, thereby forming an interface on the bubble surface. The conjugate of activator and contaminant can be concentrated and removed as scum.
[0020]
The liquid phase from which the conjugate of the surfactant and the contaminant has been separated can be used again for the purification treatment. For example, it is possible to add a surfactant to make it contact with contaminated soil or the like, or to use it for rinsing the surfactant remaining in the soil after washing.
[0021]
The combined amount of the surfactant and the contaminant separated from the liquid phase is significantly reduced since the condensed soil before the treatment is concentrated. Therefore, it is possible to detoxify at low cost using various means such as oxidative decomposition by ozone injection and dechlorination by ultraviolet irradiation, but it can be almost completely decomposed in a short time by a heating method. In particular, when an existing incinerator, melting furnace or pyrolysis furnace is present near the soil purification facility, the combination of the surfactant and the contaminant separated from the liquid phase is treated by the heating system. This is preferable because the construction cost of the equipment can be reduced.
[0022]
(Embodiment 2)
FIG. 2 shows another embodiment of the method for purifying contaminated soil and the like according to the present invention. In the figure, 1 is a first mixing tank, 2 is a surfactant injection pipe, 3 is a centrifugal dehydrator, 4 is an acid injection pipe, 5 is a coagulant injection pipe, 8 is a pH adjustment tank, 9 is a neutralization tank,
[0023]
The contaminated soil and the like are mixed with the acid supplied from the acid injection pipe 4, the treatment water and the makeup water supplied from the treated
[0024]
If the contaminated soil or the like has a high content of lime components or metal components such as iron and manganese, which prevents the contact between the contaminants and the surfactant and high cleaning efficiency cannot be obtained, the contaminated soil as in this embodiment is used. Mixing an acid before or during mixing the soil and the like with the surfactant to dissolve the lime component and the metal component improves the contact efficiency and obtains a good cleaning effect. On the other hand, if the contaminated soil or the like has a high content of organic substances such as humic acid and prevents the target contaminant from contacting the surfactant and high cleaning efficiency cannot be obtained, the contaminated soil or the like and the surfactant should not be mixed. Alternatively, if an organic substance such as humic acid is dissolved by mixing an alkali during the mixing, the contact efficiency is improved and a good cleaning effect is obtained.
[0025]
Further, by using the treated water obtained as in the present embodiment for rinsing the solid content after centrifugal dehydration, dissolving the surfactant, and adjusting the water content of the object to be purified, the total amount of water used can be reduced, and the purification cost can be reduced. This has the effect of reducing wastewater and reducing wastewater.
[0026]
【Example】
Table 1 shows the results of treating soil contaminated with dioxins by the treatment method shown in FIG. However, the processing conditions are as follows.
[0027]
[Example processing method]
・ Type of surfactant: Nonionic surfactant (alcohol)
・ Reaction time with surfactant: 30 minutes ・ Reaction temperature: normal temperature ・ Surfactant injection rate: 0.5 wt%
[Table 1]
[0028]
[0029]
【The invention's effect】
The treatment method according to the present invention removes the pollutants contained in the contaminated soil and the like with high efficiency by stirring and mixing the contaminated soil and the like with the surfactant, and also removes the surfactant and the contaminants from the washing water. This has the effect of efficiently separating the conjugate from the aqueous phase.
[Brief description of the drawings]
FIG. 1 is a diagram showing an embodiment of a method for purifying contaminated soil and the like according to the present invention.
FIG. 2 is a diagram showing another embodiment of the method for purifying contaminated soil and the like according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... First mixing tank, 2 ... Surfactant injection pipe, 3 ... Centrifugal dehydrator, 4 ... Acid injection pipe, 5 ... Coagulant injection pipe, 6 ... Second mixing tank, 7 ... Precipitation tank, 8 ... pH adjustment Tank, 9: neutralization tank, 10: alkali injection pipe, 11: treated water circulation pipe, 12: third mixing tank, 13: floating separation tank, 14: pressurized water injection pipe.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002190523A JP3918657B2 (en) | 2002-06-28 | 2002-06-28 | Method and apparatus for purifying contaminated soil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002190523A JP3918657B2 (en) | 2002-06-28 | 2002-06-28 | Method and apparatus for purifying contaminated soil |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2004033812A true JP2004033812A (en) | 2004-02-05 |
JP3918657B2 JP3918657B2 (en) | 2007-05-23 |
Family
ID=31700425
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2002190523A Expired - Fee Related JP3918657B2 (en) | 2002-06-28 | 2002-06-28 | Method and apparatus for purifying contaminated soil |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3918657B2 (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006159175A (en) * | 2004-11-09 | 2006-06-22 | Nippon Solid Co Ltd | Mixer and treatment method of polluted water using the mixer |
JP2006212472A (en) * | 2005-02-01 | 2006-08-17 | Jfe Engineering Kk | Wastewater treatment method and apparatus |
JP2006272168A (en) * | 2005-03-29 | 2006-10-12 | Kurita Water Ind Ltd | Chlorine and heavy metal containing waste treatment method |
JPWO2005075363A1 (en) * | 2004-02-10 | 2008-01-10 | 中外写真薬品株式会社 | Borohydrofluoric acid scavenger and wastewater treatment method using the same |
JP2009220015A (en) * | 2008-03-17 | 2009-10-01 | Railway Technical Res Inst | Method for treating washing wastewater containing chlorine-containing organic compound |
WO2009119223A1 (en) * | 2008-03-27 | 2009-10-01 | 株式会社Hi-Van | Method of treating waste and heat-resistant compound obtained using the same |
JP2012011332A (en) * | 2010-07-01 | 2012-01-19 | Taisei Corp | Electrolysis method for polychlorinated biphenyls |
JP2012016637A (en) * | 2010-07-06 | 2012-01-26 | Omega:Kk | Method for washing soil |
JP2012030198A (en) * | 2010-08-03 | 2012-02-16 | Omega:Kk | Reattachment prevention mechanism to soil, such as heavy metal |
JP2013238577A (en) * | 2012-05-11 | 2013-11-28 | Commissariat A L'energie Atomique Et Aux Energies Alternatives | Soil radioactive decontamination process by dispersed air flotation foam and foam thereof |
JP2014062164A (en) * | 2012-09-20 | 2014-04-10 | Fujiken:Kk | Treatment agent |
JP2014062772A (en) * | 2012-09-20 | 2014-04-10 | Fuji Corporation:Kk | Decontamination treatment method |
-
2002
- 2002-06-28 JP JP2002190523A patent/JP3918657B2/en not_active Expired - Fee Related
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2005075363A1 (en) * | 2004-02-10 | 2008-01-10 | 中外写真薬品株式会社 | Borohydrofluoric acid scavenger and wastewater treatment method using the same |
JP4682043B2 (en) * | 2004-02-10 | 2011-05-11 | 中外写真薬品株式会社 | Borohydrofluoric acid scavenger and wastewater treatment method using the same |
JP2006159175A (en) * | 2004-11-09 | 2006-06-22 | Nippon Solid Co Ltd | Mixer and treatment method of polluted water using the mixer |
JP4625894B2 (en) * | 2005-02-01 | 2011-02-02 | Jfeエンジニアリング株式会社 | Wastewater treatment method and treatment apparatus |
JP2006212472A (en) * | 2005-02-01 | 2006-08-17 | Jfe Engineering Kk | Wastewater treatment method and apparatus |
JP2006272168A (en) * | 2005-03-29 | 2006-10-12 | Kurita Water Ind Ltd | Chlorine and heavy metal containing waste treatment method |
JP2009220015A (en) * | 2008-03-17 | 2009-10-01 | Railway Technical Res Inst | Method for treating washing wastewater containing chlorine-containing organic compound |
WO2009119223A1 (en) * | 2008-03-27 | 2009-10-01 | 株式会社Hi-Van | Method of treating waste and heat-resistant compound obtained using the same |
JP2012011332A (en) * | 2010-07-01 | 2012-01-19 | Taisei Corp | Electrolysis method for polychlorinated biphenyls |
JP2012016637A (en) * | 2010-07-06 | 2012-01-26 | Omega:Kk | Method for washing soil |
JP2012030198A (en) * | 2010-08-03 | 2012-02-16 | Omega:Kk | Reattachment prevention mechanism to soil, such as heavy metal |
JP2013238577A (en) * | 2012-05-11 | 2013-11-28 | Commissariat A L'energie Atomique Et Aux Energies Alternatives | Soil radioactive decontamination process by dispersed air flotation foam and foam thereof |
JP2014062164A (en) * | 2012-09-20 | 2014-04-10 | Fujiken:Kk | Treatment agent |
JP2014062772A (en) * | 2012-09-20 | 2014-04-10 | Fuji Corporation:Kk | Decontamination treatment method |
Also Published As
Publication number | Publication date |
---|---|
JP3918657B2 (en) | 2007-05-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20210347649A1 (en) | Industrial waste salt resourceful treatment method and device | |
RU2106312C1 (en) | Method of treating waste waters (versions) | |
JP3697361B2 (en) | Waste water treatment method and waste water treatment equipment | |
US5268128A (en) | Method and apparatus for cleaning contaminated particulate material | |
JP3918657B2 (en) | Method and apparatus for purifying contaminated soil | |
JP2012024737A (en) | Wastewater treatment method and equipment therefor | |
KR100371823B1 (en) | Separation of heavy metals and materials for use in this | |
JP2002210451A (en) | Method for treating harmful material and system therefor | |
JP3236219B2 (en) | Soil purification method and equipment | |
JP3221558B2 (en) | Soil purification method and equipment | |
JP2008043879A (en) | Contaminated soil-cleaning system by washing | |
JPH01310799A (en) | Method and apparatus for mixing treatment of sewage and garbage | |
KR100446165B1 (en) | liquid state wastes treat chemicals | |
JP3347673B2 (en) | Waste treatment method | |
JP3485450B2 (en) | Resource recovery landfill method | |
KR20190137415A (en) | Method for neutralizing dredged soil washed with acid | |
JP3267948B2 (en) | Treatment method for oil-containing waste liquid | |
JP3444783B2 (en) | Removal method of dioxins in sludge | |
JP2003117562A (en) | Active cleaning equipment for water and bottom sediment of water area | |
JP2004188340A (en) | Method for treating liquid containing dioxins | |
KR200248134Y1 (en) | Waste water processing apparatus of food and drink | |
CN105923707A (en) | Desulfurization wastewater vibration membrane treatment method and device | |
KR200321144Y1 (en) | Removal system of dissolved organic matter in water treatment processes by inorganic turbidity addition | |
JPH04322786A (en) | Treatment of dense waste liquid of detergent comprising alkali saponifying agent for printed circuit board | |
JPS61187990A (en) | Treatment of waste water |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20041004 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20060313 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20060620 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20060811 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20060912 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20061027 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20070123 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20070205 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 3918657 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100223 Year of fee payment: 3 |
|
S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100223 Year of fee payment: 3 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110223 Year of fee payment: 4 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110223 Year of fee payment: 4 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120223 Year of fee payment: 5 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120223 Year of fee payment: 5 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130223 Year of fee payment: 6 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140223 Year of fee payment: 7 |
|
LAPS | Cancellation because of no payment of annual fees |