JP2021146326A5 - - Google Patents
Download PDFInfo
- Publication number
- JP2021146326A5 JP2021146326A5 JP2020052108A JP2020052108A JP2021146326A5 JP 2021146326 A5 JP2021146326 A5 JP 2021146326A5 JP 2020052108 A JP2020052108 A JP 2020052108A JP 2020052108 A JP2020052108 A JP 2020052108A JP 2021146326 A5 JP2021146326 A5 JP 2021146326A5
- Authority
- JP
- Japan
- Prior art keywords
- adsorbent
- contaminated soil
- contaminated
- mud
- separating
- 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 claims description 18
- 239000003463 adsorbent Substances 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 11
- 238000004140 cleaning Methods 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 9
- YFSUTJLHUFNCNZ-UHFFFAOYSA-N perfluorooctane-1-sulfonic acid Chemical compound OS(=O)(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F YFSUTJLHUFNCNZ-UHFFFAOYSA-N 0.000 claims description 8
- SNGREZUHAYWORS-UHFFFAOYSA-N perfluorooctanoic acid Chemical compound OC(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F SNGREZUHAYWORS-UHFFFAOYSA-N 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 8
- 150000001875 compounds Chemical class 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000010419 fine particle Substances 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 6
- 239000003344 environmental pollutant Substances 0.000 claims description 5
- 231100000719 pollutant Toxicity 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 claims description 2
- 229910000040 hydrogen fluoride Inorganic materials 0.000 claims description 2
- 238000000197 pyrolysis Methods 0.000 claims description 2
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 2
- 239000002912 waste gas Substances 0.000 claims description 2
- 239000000356 contaminant Substances 0.000 claims 2
- 239000002699 waste material Substances 0.000 claims 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims 1
- 229910052731 fluorine Inorganic materials 0.000 claims 1
- 239000011737 fluorine Substances 0.000 claims 1
- 150000002894 organic compounds Chemical class 0.000 claims 1
- 239000008187 granular material Substances 0.000 description 4
- 239000000428 dust Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
Description
さらに、本発明の一側面に係る汚染土壌の湿式清浄方法では、前記吸着剤の熱処理は、熱分解炉による前記汚染物質の熱分解であり、前記吸着剤は、粒状活性炭であってよい。 Furthermore, in the wet cleaning method for contaminated soil according to one aspect of the present invention, the heat treatment of the adsorbent may be thermal decomposition of the pollutant in a pyrolysis furnace, and the adsorbent may be granular activated carbon.
なお、本実施形態に係る汚染土壌の湿式清浄システム1では、吸着剤分離装置5により分離した吸着剤のみを熱処理装置6にて熱処理するものとしたが、これに替え、脱水装置8により得られる清浄細粒から分離される、PFOS及びPFOA類縁化合物を含む水を熱処理装置6により熱処理するようにしてもよい。ただし、この場合には水分を十分に加熱する必要があるため、エネルギーコストの点で不利が予想される。 In the contaminated soil wet cleaning system 1 according to the present embodiment, only the adsorbent separated by the adsorbent separation device 5 is heat-treated by the heat treatment device 6. The water containing PFOS and PFOA analogous compounds separated from the clean granules may be heat-treated by the heat treatment device 6 . However, in this case, since it is necessary to sufficiently heat the water, it is expected to be disadvantageous in terms of energy cost.
そこで、ステップS23において、ウォータージェット処理を行い、水流を利用して上述の小径の粒子を砂及び細粒に破砕し、また砂の表面に付着した細粒を剥離する。このウォータージェット処理は、単に高圧水を吹き付ける処理であってもよいし、コリジョンジェット(登録商標)処理と称される、砂、細粒及び水の混合物であるスラリー自体に高圧をかけ高速の噴流として噴出させ、適宜のターゲットに衝突させ、あるいは、噴流同士を互いに衝突させる方法によりなされてもよい。この処理の結果、スラリーは、細粒及びPFOS及びPFOA類縁化合物が剥離された清浄な砂と、PFOS及びPFOA類縁化合物を吸着した解砕された細粒と、PFOS及びPFOA類縁化合物が溶解した水との混合物となっている。 Therefore, in step S23, a water jet process is performed to crush the above-mentioned small-diameter particles into sand and fine particles using water flow, and to separate the fine particles adhering to the surface of the sand. This water jet treatment may be simply a treatment of spraying high-pressure water, or a high-speed jet flow by applying high pressure to the slurry itself, which is a mixture of sand, fine particles, and water, which is called collision jet (registered trademark) treatment. and collide with an appropriate target, or by colliding the jets with each other. As a result of this treatment, the slurry consisted of clean sand from which fine granules and PFOS and PFOA-related compounds were removed, crushed fine granules adsorbing PFOS and PFOA-related compounds, and water in which PFOS and PFOA-related compounds were dissolved. It is a mixture of
排ガス中には高濃度のフッ化水素ガスが含まれる可能性があり、これをそのまま大気中に放出することはできないため、ステップS6では、かかる排ガスの清浄化、すなわち、廃ガス中からの有害物質の除去を排ガス清浄化装置7により行う。 Since the exhaust gas may contain hydrogen fluoride gas of high concentration and cannot be discharged into the atmosphere as it is, in step S6, such exhaust gas is purified, that is, harmful substances are removed from the waste gas. Substance removal is performed by the exhaust gas cleaning device 7 .
また、排ガス中に含まれる他の汚染物質を除去するため、排ガス清浄化装置7には、除塵装置や、脱硫装置等の装置が含まれてもよい。また、各汚染物質の除去装置において処理を行う際の排ガスの温度が適正なものとなるよう、排ガス清浄化装置7は熱交換器を備えていてもよい。かかる排ガス清浄化装置7により清浄化された清浄排気は大気中に放出され、水性液中に溶解し、あるいは固定化されたフッ化化合物や塵埃、硫化物などは、それぞれ適宜の処理乃至再利用がなされる。 In order to remove other pollutants contained in the exhaust gas, the exhaust gas purification device 7 may include devices such as a dust remover and a desulfurization device. Further, the exhaust gas purifying device 7 may be provided with a heat exchanger so that the temperature of the exhaust gas when being treated in each pollutant removal device becomes appropriate. The clean exhaust gas cleaned by the exhaust gas cleaner 7 is released into the atmosphere, and the fluoride compounds, dust, sulfides, etc. dissolved or fixed in the aqueous liquid are appropriately treated or reused. is done.
そして、ステップS4において吸着剤が分離された後の残渣である汚染泥は、ステップS7において脱水され、清浄細粒と、少量のPFOS及びPFOA類縁化合物を溶解した水とに分離される。脱水された水は、ステップS2における清浄砂礫の分離の際に添加する水として循環利用される。 The polluted sludge, which is the residue after the adsorbent is separated in step S4 , is dehydrated in step S7 and separated into clean granules and water in which a small amount of PFOS and PFOA-related compounds are dissolved. The dehydrated water is recycled as water added during separation of clean gravel in step S2.
Claims (8)
前記汚染土壌を清浄砂礫と汚染泥に分離する工程と、
前記汚染泥に、所定粒径より大きい吸着剤を混合する工程と、
前記汚染泥中の細粒と前記吸着剤を分離する工程と、
前記吸着剤を熱処理する工程と、
を含む汚染土壌の湿式清浄方法。 A wet cleaning method for soil contaminated with contaminants containing at least one of PFOS and PFOA-related compounds,
separating the contaminated soil into clean gravel and contaminated mud;
A step of mixing an adsorbent larger than a predetermined particle size with the contaminated mud;
A step of separating fine particles in the polluted mud and the adsorbent;
heat-treating the adsorbent;
A method for wet cleanup of contaminated soil containing
前記汚染土壌から清浄礫を分離する工程と、
礫分離後の前記汚染土壌中の砂から、ウォータージェットにより、前記汚染物質及び細粒を剥離する工程と、
礫分離後の前記汚染土壌から清浄砂を分離する工程と、
を含む請求項1~4のいずれか1項に記載の汚染土壌の湿式清浄方法。 The step of separating the contaminated soil into clean gravel and contaminated mud,
a step of separating clean gravel from the contaminated soil;
A step of stripping the pollutants and fine grains from the sand in the contaminated soil after gravel separation by a water jet;
a step of separating clean sand from the contaminated soil after gravel separation;
The wet cleaning method for contaminated soil according to any one of claims 1 to 4, comprising
前記汚染土壌を清浄砂礫と汚染泥に分離する清浄砂礫分離装置と、
前記汚染泥に、所定粒径より大きい吸着剤を混合する混合装置と、
前記汚染泥中の細粒と前記吸着剤を分離する吸着剤分離装置と、
前記吸着剤を熱処理する熱処理装置と、
を含む汚染土壌の湿式清浄システム。 a device for supplying contaminated soil with contaminants containing at least one of PFOS and PFOA analogues;
a clean gravel separator for separating the contaminated soil into clean gravel and contaminated mud;
A mixing device for mixing an adsorbent larger than a predetermined particle size with the contaminated mud;
an adsorbent separation device for separating fine particles in the polluted mud and the adsorbent;
a heat treatment device for heat-treating the adsorbent;
Wet cleanup systems for contaminated soil, including
請求項7に記載の汚染土壌の湿式清浄システム。 The supply device, the clean gravel separation device, the mixing device, the adsorbent separation device and the heat treatment device are portable,
The wet cleaning system for contaminated soil according to claim 7.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2020052108A JP7481140B2 (en) | 2020-03-24 | 2020-03-24 | Method and system for wet cleaning of contaminated soil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2020052108A JP7481140B2 (en) | 2020-03-24 | 2020-03-24 | Method and system for wet cleaning of contaminated soil |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2021146326A JP2021146326A (en) | 2021-09-27 |
JP2021146326A5 true JP2021146326A5 (en) | 2023-02-24 |
JP7481140B2 JP7481140B2 (en) | 2024-05-10 |
Family
ID=77850251
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2020052108A Active JP7481140B2 (en) | 2020-03-24 | 2020-03-24 | Method and system for wet cleaning of contaminated soil |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP7481140B2 (en) |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005103436A (en) | 2003-09-30 | 2005-04-21 | Meidensha Corp | Method and system for purifying water-containing soil |
JP5490035B2 (en) | 2010-02-10 | 2014-05-14 | 株式会社アステック東京 | How to clean contaminated soil |
JP6034721B2 (en) | 2013-02-27 | 2016-11-30 | 株式会社クレハ環境 | Incineration method for drums |
JP6396075B2 (en) | 2014-05-23 | 2018-09-26 | 前田建設工業株式会社 | Method and apparatus for wet classification cleaning of contaminated soil |
WO2017131972A1 (en) | 2016-01-25 | 2017-08-03 | Oxytec Llc | Soil and water remediation method and apparatus for treatment of recalcitrant halogenated substances |
AU2017371390A1 (en) | 2016-12-05 | 2019-07-18 | Virotec Pty Ltd | Treatments for persistent organic pollutants |
JP7105080B2 (en) | 2018-03-29 | 2022-07-22 | 前田建設工業株式会社 | Waste muddy water volume reduction treatment device and volume reduction treatment method |
-
2020
- 2020-03-24 JP JP2020052108A patent/JP7481140B2/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR100639261B1 (en) | Hybrid-type apparatus for treating exhaust gas having a condenser | |
US20090193968A1 (en) | Method and apparatus for removing contaminants from industrial processing plants | |
JP2007237101A (en) | Air cleaning apparatus and coating equipment | |
JP6242761B2 (en) | Waste water treatment apparatus and treatment method | |
KR100755910B1 (en) | The process for recovering petroleum-contaminated soil and its apparatus | |
RU2595690C2 (en) | System and method of cleaning activated coal and coal combustion residues | |
JP3226914B2 (en) | Flue gas cleaning method | |
JP2000229217A (en) | Method and device for removing harmful material in waste gas or the like from incineration furnace or the like | |
KR20000017239A (en) | Method for cleaning of flue gas | |
JP2021146326A5 (en) | ||
KR101885757B1 (en) | Apparatus for recycleing activated carbon | |
KR101570840B1 (en) | Apparatus for collecting coating material dusts and VOCS | |
JP3236219B2 (en) | Soil purification method and equipment | |
JP2007000853A (en) | Method for cleaning and treating pcb-contaminated soil | |
WO1997045191A1 (en) | Apparatus and method for wet type simultaneous decontaminating and dust-removing gas treatment | |
JP3811705B2 (en) | Exhaust gas treatment method and equipment | |
JP7481140B2 (en) | Method and system for wet cleaning of contaminated soil | |
JP6052041B2 (en) | Waste water treatment method and waste water treatment equipment | |
JP2002001042A (en) | Wet dust collecting method for exhaust gas | |
JP2020148373A (en) | PFCs-CONTAINING EXHAUST GAS TREATMENT DEVICE AND METHOD | |
CN211514071U (en) | Environment-friendly and energy-saving cremation machine tail gas treatment system | |
WO2021049246A1 (en) | Exhaust gas treatment method and treatment equipment | |
WO2012092307A1 (en) | Method and apparatus to clean ash from ash ponds or a landfill | |
JP2003088729A (en) | Method for removing dioxins by activated carbon adsorption and removal apparatus therefor | |
JPH07213837A (en) | Treatment device for waste combustion gas and treatment of waste combustion gas |