JP2003128445A - Method of converting organic polluted soil into cement raw material - Google Patents
Method of converting organic polluted soil into cement raw materialInfo
- Publication number
- JP2003128445A JP2003128445A JP2001323978A JP2001323978A JP2003128445A JP 2003128445 A JP2003128445 A JP 2003128445A JP 2001323978 A JP2001323978 A JP 2001323978A JP 2001323978 A JP2001323978 A JP 2001323978A JP 2003128445 A JP2003128445 A JP 2003128445A
- Authority
- JP
- Japan
- Prior art keywords
- cement
- container
- soil
- raw material
- kiln
- 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
- 239000004568 cement Substances 0.000 title claims abstract description 68
- 238000000034 method Methods 0.000 title claims abstract description 57
- 239000002689 soil Substances 0.000 title claims abstract description 57
- 239000002994 raw material Substances 0.000 title claims abstract description 28
- 238000003860 storage Methods 0.000 claims abstract description 18
- 239000002957 persistent organic pollutant Substances 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims abstract description 3
- -1 cyanide compound Chemical class 0.000 claims description 16
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical group O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 claims description 14
- 150000003071 polychlorinated biphenyls Chemical group 0.000 claims description 8
- 239000011521 glass Substances 0.000 claims description 7
- 229920003023 plastic Polymers 0.000 claims description 6
- 239000004033 plastic Substances 0.000 claims description 6
- 238000011109 contamination Methods 0.000 claims description 5
- 239000004793 Polystyrene Substances 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims description 4
- 229920002223 polystyrene Polymers 0.000 claims description 4
- 239000004800 polyvinyl chloride Substances 0.000 claims description 4
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 2
- 229920005989 resin Polymers 0.000 claims description 2
- 239000000446 fuel Substances 0.000 abstract description 6
- 238000003912 environmental pollution Methods 0.000 abstract description 5
- 238000012856 packing Methods 0.000 abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 239000004698 Polyethylene Substances 0.000 description 8
- 229920000573 polyethylene Polymers 0.000 description 8
- 239000007789 gas Substances 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- 239000004927 clay Substances 0.000 description 5
- 239000000428 dust Substances 0.000 description 5
- 238000010304 firing Methods 0.000 description 5
- 230000001681 protective effect Effects 0.000 description 5
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- 239000004743 Polypropylene Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 150000002013 dioxins Chemical class 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229920001155 polypropylene Polymers 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 2
- LFYJSSARVMHQJB-QIXNEVBVSA-N bakuchiol Chemical compound CC(C)=CCC[C@@](C)(C=C)\C=C\C1=CC=C(O)C=C1 LFYJSSARVMHQJB-QIXNEVBVSA-N 0.000 description 2
- 238000009841 combustion method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000000241 respiratory effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000009284 supercritical water oxidation Methods 0.000 description 2
- 229910052718 tin Inorganic materials 0.000 description 2
- 239000011135 tin Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000011398 Portland cement Substances 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000009412 basement excavation Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000003421 catalytic decomposition reaction Methods 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000003908 quality control method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005067 remediation Methods 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000005028 tinplate Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/24—Cements from oil shales, residues or waste other than slag
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/43—Heat treatment, e.g. precalcining, burning, melting; Cooling
- C04B7/44—Burning; Melting
- C04B7/4407—Treatment or selection of the fuel therefor, e.g. use of hazardous waste as secondary fuel ; Use of particular energy sources, e.g. waste hot gases from other processes
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
(57)【要約】
【課題】 有機系汚染土壌をセメントキルンで処理する
際に、汚染土壌の飛散による二次的な環境汚染を効果的
に防止すると共に、キルンの燃料の節約を図る。
【解決手段】 有機系汚染物質に汚染された土壌を収納
容器に梱包し、容器ごとセメントキルンに投入してセメ
ント原料と共に燃焼させることにより、有機系汚染土壌
をセメント原料として用いることを特徴とする有機系汚
染土壌のセメント原料化方法。(57) [Summary] [PROBLEMS] To effectively prevent secondary environmental pollution due to scattering of contaminated soil and to save fuel for the kiln when treating organic contaminated soil with a cement kiln. SOLUTION: The organic polluted soil is used as a cement raw material by packing soil contaminated with organic pollutants in a storage container, throwing the whole container into a cement kiln and burning it together with a cement raw material. Method of converting organic polluted soil into cement material.
Description
【0001】本発明は、有機系汚染土壌をセメント原料
として再利用する処理方法とそのセメントに関する。具
体的には、ダイオキシン、PCB、またはシアン化物な
どを含む有機系汚染土壌について、これをセメントの粘
土原料として活用する場合、更なる環境汚染を引き起こ
さずに処理することができる処理方法に関する。The present invention relates to a treatment method for recycling organic contaminated soil as a cement raw material and the cement. More specifically, the present invention relates to a treatment method for treating organically contaminated soil containing dioxin, PCB, cyanide or the like, when it is used as a clay raw material for cement, without causing further environmental pollution.
【0002】[0002]
【従来の技術】近年、ごみ焼却施設の周辺等において、
ダイオキシンやPCBなどによる汚染が問題になってい
る。これらの汚染土壌を無害化する方法としては、熱脱
着分離方法、溶融固化法(ジオメルト法)、アルカリ触媒
分解法、超臨界水酸化方法、メカノケミカル法、真空加
熱分離法、バイオレメディエーション法、間接加熱キル
ン法、ロータリーキルン焼却方法などがある.2. Description of the Related Art Recently, in the vicinity of garbage incineration facilities,
Contamination due to dioxin and PCB has become a problem. Methods for detoxifying these contaminated soils include thermal desorption separation method, melt solidification method (geomelt method), alkali catalytic decomposition method, supercritical water oxidation method, mechanochemical method, vacuum heating separation method, bioremediation method, indirect method. There are heating kiln method and rotary kiln incineration method.
【0003】一方、シアン化合物を含有した汚染土壌の
処理方法としては、アルカリ塩素法、オゾン酸化法、電
解酸化法、紺青法(難溶性錯化合物沈殿法)、酸分解燃焼
法、煮詰法(煮詰高温燃焼法)、湿式加熱分解法、吸着
法、生物的処理法などが知られている。On the other hand, as a method for treating a contaminated soil containing a cyanide compound, an alkali chlorine method, an ozone oxidation method, an electrolytic oxidation method, a dark blue method (a sparingly soluble complex compound precipitation method), an acid decomposition combustion method, and a boiling method (cooking) High temperature combustion method), wet thermal decomposition method, adsorption method, biological treatment method and the like are known.
【0004】[0004]
【発明が解決しようとする課題】しかし、上述の処理方
法のうちプラント系処理方法はその建設に数億円以上の
費用がかかる上、処理した土壌の搬出先を確保すること
も課題になる。超臨界水酸化法やメカノケミカル法はそ
の規模が現状では室内レベルでありプラントレベルの実
績はない。、一方、ダイオキシン類による汚染土壌をバ
イオレメディエーシヨンによって処理する方法について
は期待が大きい。特にこの方法は土壌掘削、焼却用燃
料、あるいは薬剤等をほとんど必要としないので処理コ
ストが低く、経済性に優れると云う利点がある。また、
植物を使用するので安全性が高いと考えられる。しか
し、バイオレミディエーション法は分解反応速度が小さ
く、浄化修復期間が長いので、浄化目標が厳しい場合に
はこれを達成するのが難しい。そのため、この処理方法
については分解速度が革新的に早い技術が開発され、処
理時間が大幅に短縮されない限り、長い処理期間中の人
体暴露リスクのため、修復法としての適用に限界があ
る。However, among the above-mentioned treatment methods, the plant treatment method requires a construction cost of several hundred million yen or more, and it is also a problem to secure a destination for the treated soil. The scale of the supercritical water oxidation method and mechanochemical method is at the indoor level at present, and there is no record at the plant level. On the other hand, there are great expectations for a method of treating soil contaminated with dioxins with bioremediation. In particular, this method has advantages that the treatment cost is low and the economy is excellent because it hardly requires soil excavation, incineration fuel, chemicals or the like. Also,
It is considered to be highly safe because it uses plants. However, since the bioremediation method has a low decomposition reaction rate and a long purification / repair period, it is difficult to achieve this when the purification target is strict. Therefore, unless a technology with an innovatively high decomposition rate is developed for this treatment method and the treatment time is significantly shortened, there is a limit to its application as a remediation method due to the risk of human exposure during a long treatment period.
【0005】本発明は、従来の処理方法におけるこのよ
うな問題を克服したものであり、有機系汚染物質を含む
土壌をセメントの粘土原料として利用する方法であっ
て、その際に更なる環境汚染を生じない処理方法を提供
するものである。The present invention overcomes such problems in the conventional treatment method, and is a method of utilizing soil containing organic pollutants as a clay raw material for cement, in which case further environmental pollution. The present invention provides a processing method that does not cause
【0006】[0006]
【課題を解決するための手段】すなわち、本発明によれ
ば以下の構成からなる有機系汚染土壌のセメント原料化
方法とそのセメントが提供される。
(1)有機系汚染物質に汚染された土壌を収納容器に梱
包し、容器ごとセメントキルンに投入してセメント原料
と共に燃焼させることにより、有機系汚染土壌をセメン
ト原料として用いることを特徴とする有機系汚染土壌の
セメント原料化方法。
(2)有機系汚染物質に汚染された土壌を、汚染現場で
収納容器に梱包し、セメント工場で容器ごとセメントキ
ルンに投入する上記(1)の方法。
(3)有機系汚染物質がダイオキシン、ポリ塩化ビフェ
ニル(PCB)、シアン化合物である上記(1)または(2)の
方法。
(4)収納容器がプラスチック製容器、金属製容器、木
製容器、またはガラス製容器である上記(1)、(2)または
(3)の方法。
(5)収納容器の材質がポリスチレン、ABS樹脂、ポ
リビニルクロライドであって、キルンの燃焼温度が14
00℃以上である上記(1)、(2)または(3)の方法。
(6)収納容器がペール缶、ドラム缶またはガラス瓶で
ある上記(1)〜(5)の何れかに記載する方法。
(7)上記(1)〜(6)の何れかの方法によって製造したセ
メント。That is, according to the present invention, there is provided a method for converting an organic polluted soil into a cement raw material and the cement thereof, which has the following constitution. (1) Organic soil characterized by being used as a cement raw material by packing soil contaminated with organic pollutants in a storage container, putting the whole container into a cement kiln, and burning it together with the cement raw material. Method for making cement soil as a raw material for cement. (2) The method of (1) above, in which soil contaminated with organic pollutants is packed in a storage container at the pollution site and the container is put into a cement kiln at a cement plant. (3) The method according to (1) or (2) above, wherein the organic pollutant is dioxin, polychlorinated biphenyl (PCB), or a cyanide compound. (4) The storage container is a plastic container, a metal container, a wooden container, or a glass container (1), (2), or
Method (3). (5) The material of the storage container is polystyrene, ABS resin, polyvinyl chloride, and the combustion temperature of the kiln is 14
The method according to (1), (2) or (3) above, wherein the temperature is 00 ° C or higher. (6) The method according to any one of (1) to (5) above, wherein the storage container is a pail, a drum or a glass bottle. (7) A cement produced by the method according to any one of (1) to (6) above.
【0007】本発明のセメント原料化方法によれば、有
機系汚染物質に汚染された土壌(有機系汚染土壌と略称
する)を収納容器に梱包し、具体的には、例えばペール
缶などに密閉し、この容器ごとセメントキルンに投入す
るので、梱包、搬送およびキルンへの投入の各処理工程
において汚染物質が周囲に飛散することがなく、周囲の
環境汚染を防止することができる。また、梱包した容器
ごとキルンに投入して燃焼させるので、ポリエチレン製
やポリプロピレン製などのプラスチック製容器を用いる
と、その燃焼時にかなりの熱を発生するので、これをセ
メント焼成の熱源の一部に利用することができるので、
セメント製造工程において、焼成燃料をいくらか節約で
きる利点がある。According to the method for producing a cement raw material of the present invention, soil polluted with organic pollutants (abbreviated as organic polluted soil) is packed in a storage container, specifically, for example, sealed in a pail can or the like. Since this container is put into the cement kiln, pollutants do not scatter to the surroundings in each processing step of packing, transporting, and putting into the kiln, and environmental pollution of the surroundings can be prevented. In addition, since the packed container is put into a kiln and burned, if a plastic container such as polyethylene or polypropylene is used, considerable heat is generated at the time of burning, so use this as a part of the heat source for cement firing. Can be used,
There is the advantage of saving some calcined fuel in the cement manufacturing process.
【0008】[0008]
【発明の実施の形態】以下、本発明を実施形態に基づい
て具体的に説明する。本発明の方法は、有機系汚染物質
に汚染された土壌を収納容器に梱包し、容器ごとセメン
トキルンに投入してセメント原料と共に燃焼させること
により、有機系汚染土壌を主にセメントの粘土原料の一
部に利用するセメント原料化方法である。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described below based on embodiments. The method of the present invention packs soil polluted with organic pollutants in a storage container, and puts the container into a cement kiln and burns it together with the cement raw material, so that the organic polluted soil is mainly used as a clay raw material for cement. This is a cement raw material method that is partially used.
【0009】有機系汚染土壌とは、例えば、ダイオキシ
ン、PCB、シアン化合物によって汚染された土壌であ
り、これら有機系汚染物質を含む土壌である。収納容器
は、好ましくはセメント原料と共に焼成したときに、焼
成されるセメント中の微量成分がJIS規格を満足する
ような組成であることを要する。すなわち、収納容器に
含まれる塩素や全アルカリ量が、焼成されるセメントの
組成としてそれぞれ0.02%以下および0.75%以下
となることが必要である。このような容器を用いること
により、容器ごと汚染土壌を燃焼させたときに、ダイオ
キシン類やPCBの発生源である塩素量を極力低減する
ことができる。収納容器は、具体的には、例えば、ポリ
エチレン、ポリプロピレンなどのプラスチック製容器、
スチールなどの金属製容器、ガラス瓶などのガラス製容
器、樽などの木製容器である。なお、ポリスチレン、A
BS樹脂、ポリビニルクロライドは十分に高い温度、例
えば1400℃以上で燃焼すればダイオキシンを発生さ
せる可能性が少ないので収納容器として用いることがで
きる。因みに、通常のセメントキルンの焼成温度は14
00℃〜1500℃程度であるので、通常のセメント製
造キルンであれば材質がポリスチレン、ABS樹脂、ポ
リビニルクロライドなどの容器も用いることができる。
なお、トタンやブリキなどのスチール製容器はセメント
原料の鉄分の量が過剰にならないように投入量を調整す
る。The organic polluted soil is, for example, a soil polluted with dioxin, PCB, and a cyanide compound, and is a soil containing these organic pollutants. The storage container preferably has such a composition that, when fired together with the cement raw material, the trace components in the fired cement satisfy the JIS standard. That is, it is necessary that the amounts of chlorine and total alkali contained in the storage container are 0.02% or less and 0.75% or less, respectively, as the composition of the cement to be fired. By using such a container, when the contaminated soil is burned together with the container, the amount of chlorine, which is a generation source of dioxins and PCB, can be reduced as much as possible. The storage container is, for example, a plastic container such as polyethylene or polypropylene,
Metal containers such as steel, glass containers such as glass bottles, and wooden containers such as barrels. In addition, polystyrene, A
Since BS resin and polyvinyl chloride are less likely to generate dioxin when burned at a sufficiently high temperature, for example, 1400 ° C. or higher, they can be used as a container. By the way, the firing temperature of a normal cement kiln is 14
Since the temperature is about 00 ° C to 1500 ° C, a container made of polystyrene, ABS resin, polyvinyl chloride or the like can be used as long as it is a normal cement manufacturing kiln.
For steel containers such as galvanized iron and tin, the amount of iron is adjusted so that the iron content of the cement raw material does not become excessive.
【0010】この収納容器はペール缶やドラム缶、樽な
どのような密閉容器が好ましい。汚染現場で密閉容器に
有機系汚染土壌を入れ、蓋をして梱包した状態とする。
汚染現場における容器への詰め込みは、手作業で行って
も良く、機械作業でも良い。例えば、現場で汚染土壌を
容器に入れる際にバイブレータつきシュート(振動手段
を備えた傾斜板)などを用いて缶内に詰め込む。なお、
容器に梱包した状態とは汚染土壌が外部に容易に飛散し
ない状態を云う。例えば、ペール缶などに蓋をして密閉
した状態、厚いポリ袋などに詰めて口を閉じた状態など
を云う。有機汚染土壌を現場で容器に梱包することによ
り、汚染土壌の飛散による二次汚染を防止すると共に作
業性が向上する。The storage container is preferably a closed container such as a pail, a drum or a barrel. Put the organic contaminated soil in a closed container at the contamination site, cover it with a lid, and pack it.
The filling of the container at the contamination site may be performed manually or mechanically. For example, when the contaminated soil is put into the container at the site, it is packed in the can using a chute with a vibrator (an inclined plate equipped with a vibrating means). In addition,
The state of being packed in a container means a state in which contaminated soil is not easily scattered to the outside. For example, it means a state in which a pail can or the like is covered and sealed, or a thick plastic bag or the like is filled and the mouth is closed. By packing the organically contaminated soil in a container on site, secondary pollution due to scattering of the contaminated soil is prevented and workability is improved.
【0011】有機系汚染土壌を収納容器に梱包した状態
で、容器ごとセメントキルンに投入してセメント原料と
共に燃焼させる。キルンの温度は通常のセメント焼成温
度であれば良い。キルン内の高温によって土壌に含まれ
る有機汚染物質が分解され、また土壌は粘土化してセメ
ント原料の粘土原料の一部になる。さらに容器ごと燃焼
することによって、ポリエチレン製やポリプロピレン製
などのプラスチック製容器などは高温を発生するので、
その燃焼熱がセメント焼成の熱源の一部に利用される。The organic contaminated soil is packed in a container, and the container is put into a cement kiln and burned together with the cement raw material. The temperature of the kiln may be a normal cement firing temperature. Due to the high temperature in the kiln, organic pollutants contained in the soil are decomposed, and the soil becomes clay and becomes a part of the clay raw material of the cement raw material. Furthermore, by burning the entire container, plastic containers such as polyethylene and polypropylene will generate high temperatures.
The combustion heat is used as part of the heat source for cement firing.
【0012】有機汚染土壌のキルンへの投入量は、(イ)
ポルトランドセメント、または混合セメントのJIS規
格に定めらた化学成分の規格値、および、(ロ)この化学
組成値から算出した水硬率、ケイ酸率、活動係数、石灰
飽和度などの品質管理値に基づいて管理すれば良い。The amount of organic polluted soil input to the kiln is (a)
Standard values of chemical components defined in JIS standard of Portland cement or mixed cement, and (b) Quality control values such as hydraulic modulus, silicic acid rate, activity coefficient, lime saturation calculated from this chemical composition value. It should be managed based on.
【0013】セメント製造方法は、最近ではSP方式と
NSP方式にほぼ限定されており、これらプロセスはサ
スペンションプレヒーターと廃熱発電設備を有してお
り、有機系汚染物質が分解して発生する塩素ガスや酸性
ガスは、大量のアルカリ性のセメント原料により吸着さ
れる。さらに、セメントキルンの排ガスは廃熱ボイラー
によって短時間に急冷却されるためダイオキシンやPC
Bは再合成しない。従って、本処理方法によれば、ダイ
オキシン類が系外に放出される虞がない。なお、念のた
め、作業中は防塵マスク等の呼吸器用保護、土壌の付着
し難い保護服や保護手袋を着用するのが好ましい。Recently, the cement manufacturing method is almost limited to the SP system and the NSP system, and these processes have a suspension preheater and waste heat power generation equipment, and chlorine generated by decomposition of organic pollutants is generated. Gas and acid gas are adsorbed by a large amount of alkaline cement raw materials. Furthermore, the exhaust gas from the cement kiln is rapidly cooled in a short time by the waste heat boiler, so it is possible to use dioxins and PC.
B is not resynthesized. Therefore, according to this treatment method, there is no risk that dioxins will be released from the system. In addition, as a precaution, during work, it is preferable to wear respiratory protective equipment such as a dust mask, and wear protective clothing and gloves to prevent soil from adhering.
【0014】以下、本発明を実施例によって具体的に示
す。処理した土壌のダイオキシン含有量は1000〜6
800pg-TEQ/gであり、国の環境基準(1000pg-TEQ/g)を
大きく上回るダイオキシン類を含む土壌であり、処理量
は約150m3(約250t)である。The present invention will be specifically described below with reference to examples. Dioxin content of treated soil is 1000-6
It is a soil containing dioxin that is 800 pg-TEQ / g, which greatly exceeds the national environmental standard (1000 pg-TEQ / g), and the treated amount is about 150 m 3 (about 250 t).
【0015】〔実施例〕粉塵の飛散防止対策(散水等)を
講じたダイオキシン汚染土壌を汚染現場でミニバックホ
ウを用いて掘削し、ポリエチレン製のペール缶(10L容
量、16kg)にバイブレータ付シュートを用いて詰め込ん
だ。この詰め込み作業によって生じた粉塵量は大気1m3
当たり0.03〜0.06mgであり、ダイオキシン濃度が
高かった土壌を基準にして換算しても、大気中のダイオ
キシン濃度は0.204〜0.408pg-TEQ/Nm3であり、
国の環境基準(0.6pg-TEQ/Nm3)を満足するものであっ
た。汚染土壌を詰めたペール缶をさらにコンテナに収納
し、梱包してセメント工場にトラック輸送し、キルンに
既設のシュートを利用してキルン内に投入した。なお、
この既設シュートに合わせて300mm角程度のペール缶
を使用したが、キルンに投入できれば良いのでペール缶
の大きさは制限されない。トラック輸送中とその搬出後
に土壌のロスは認められなかった。従ってペール缶中の
土壌の全量がセメントキルン内に投入されたことにな
る。輸送の際にはウィング車を使用するなどして荷こぼ
れ等を防止した。輸送後、セメント工場内の一時保管場
所に設置した。これらの作業中、作業員は防塵マスク等
の呼吸器用保護、土壌の付着し難い保護服および保護手
袋を着用した。これらの保護具等は作業後毎に廃棄して
新規なものを着用し、使用後はキルンで焼却処分した。
キルン内に投入した汚染土壌をセメント原料と共に約1
450℃で約250時間焼成し、セメント約36000
tを製造した。因みに、汚染現場で土壌を容器に入れ
ず、トラックにバラ積みしてセメント工場に輸送し、ベ
ルトコンベアーを用いて汚染土壌をキルンの投入口に移
送し、スコップでキルンに投入した場合、発生した粉塵
量から換算したダイオキシン濃度は3.0pg-TEQ/Nm3で
あり、国の環境基準を上回った。[Example] Dioxin-contaminated soil for which dust scattering prevention measures (sprinkling, etc.) were taken, was excavated at the contamination site using a mini backhoe, and a polyethylene pails (10 L capacity, 16 kg) was equipped with a chute with a vibrator. Used and stuffed. The amount of dust generated by this packing work is 1 m 3 in the air.
The amount is 0.03 to 0.06 mg per day, and the dioxin concentration in the air is 0.204 to 0.408 pg-TEQ / Nm 3 even when converted based on the soil in which the dioxin concentration was high.
It satisfied the national environmental standard (0.6 pg-TEQ / Nm 3 ). Pail cans filled with contaminated soil were further stored in a container, packed, transported by truck to a cement factory, and put into the kiln using an existing chute. In addition,
A pail can of about 300 mm square was used according to the existing chute, but the size of the pail can is not limited as long as it can be put into the kiln. No soil loss was observed during and after truck transport. Therefore, the total amount of soil in the pail can was put into the cement kiln. During transportation, wing cars were used to prevent spills. After transportation, it was installed at a temporary storage location in the cement plant. During these operations, workers wore respiratory protective equipment such as dust masks, protective clothing and soil-resistant gloves that were resistant to soil. These protective gears were discarded after each work, new ones were worn, and after use, they were incinerated in a kiln.
Contaminated soil put into the kiln together with cement raw materials for about 1
Approximately 250 hours at 450 ℃, about 36,000 cement
manufactured. By the way, it occurred when the soil was not put in a container at the polluted site, it was loaded on a truck in bulk and transported to a cement factory, the contaminated soil was transferred to the kiln input port using a belt conveyor, and the scoop was put into the kiln. The dioxin concentration converted from the amount of dust was 3.0 pg-TEQ / Nm 3 , which exceeded the national environmental standard.
【0016】本実施例では約16000個のポリエチレ
ン製ペール缶を使用した。このペール缶の空重量は0.
5kg/個であり、投入したポリエチレン缶の総重量は8
000kgである。ポリエチレンの燃焼熱は軟質、硬質と
もに約11000kcal/kgであるので、セメント約36
000tを製造するに当たり、約11000kcal/kg×
8000kg=88×106kcalの熱量に見合う燃料を節
約できたことになる。なお、ポリプロピレン製ペール缶
を用いても同様に88×106kcalの熱量に見合う燃料
を節約することができる。In this embodiment, about 16,000 polyethylene pail cans were used. The empty weight of this pail can is 0.
It is 5 kg / piece, and the total weight of the added polyethylene cans is 8
It is 000 kg. The combustion heat of polyethylene is about 11,000 kcal / kg for both soft and hard, so cement is about 36
Approximately 11,000 kcal / kg x for producing 000t
This means that the fuel equivalent to the heat quantity of 8000 kg = 88 × 10 6 kcal can be saved. Even if a polypropylene pail can is used, fuel equivalent to the heat quantity of 88 × 10 6 kcal can be saved.
【0017】なお、スチール製のペール缶は上記と同様
のサイズの場合、空重量はポリエチレン製缶の約8倍で
あり、従って、セメント原料の鉄を8000kg×8=6
4000kg低減することができる。但し、トタン、ブリ
キ、ステンレスは鉄の他に亜鉛、すず、クロムを含有
し、これらがセメントに混入するには好ましくないの
で、これらの缶は避けたほうが良い。また、ガラス瓶を
用いた場合には、セメント原料のなかでシリカ源が最も
高価であるため好適なシリカ原料になる。ただし、過剰
に加えた場合にはセメント中の全アルカリ量のJIS規
格0.75%を上回る懸念があるので、これを越えない
ように注意を要する。When the steel pail can has the same size as the above, the empty weight is about eight times as large as that of the polyethylene pail. Therefore, the cement raw material iron is 8000 kg × 8 = 6.
It can be reduced by 4000 kg. However, galvanized iron, tin plate, and stainless steel contain zinc, tin, and chromium in addition to iron, which are not preferable for mixing with cement, so these cans should be avoided. Further, when a glass bottle is used, the silica source is the most expensive of the cement raw materials, and is therefore a suitable silica raw material. However, if added in excess, there is a concern that the total amount of alkali in the cement will exceed the JIS standard 0.75%, so care must be taken not to exceed this.
【0018】ダイオキシン汚染土壌を10t/日(10時間
稼働)の割合で処理し、1ヶ月(実働22日)間で220tを
焼成処理した。焼成処理中にセメントキルン排ガスから
排出されるガス中と、セメント工場の製品であるクリン
カー中のダイオキシン濃度を測定した。この結果、処理
前と処理中の排ガス中のダイオキシン濃度には大きな差
が見られなかった。また、得られたセメントの強度、凝
結特性、および水和熱特性などのセメントの一般的な諸
物性を評価したところ、これらは本発明に係るセメント
は汚染土壌を加えずに製造した従来のセメントと同様で
あることを確認した。Dioxin-contaminated soil was treated at a rate of 10 t / day (10 hours operation), and 220 t was fired for 1 month (22 working days). The dioxin concentration in the gas discharged from the cement kiln exhaust gas during the firing process and in the clinker, which is a product of the cement factory, was measured. As a result, no significant difference was found in the dioxin concentration in the exhaust gas before and during the treatment. In addition, when the general properties of the cement such as strength, setting property, and heat of hydration property of the obtained cement were evaluated, it was found that the cement according to the present invention is a conventional cement produced without adding contaminated soil. It was confirmed to be similar to.
【0019】[0019]
【発明の効果】本発明の処理方法は、従来、現実的な処
理方法が確立されていなかったダイオキシンなどによる
汚染土を無害化してセメント原料として利用できるよう
にし、しかも汚染土壌を容器に梱包して取り扱うことに
より、処理作業中の汚染土壌の飛散による二次的な環境
汚染を効果的に防止し、さらには容器ごとキルンに投入
して燃焼させることによりキルンの燃料を節約すること
ができる。EFFECTS OF THE INVENTION The treatment method of the present invention detoxifies soil contaminated by dioxin, etc. for which a practical treatment method has not been established, and makes it usable as a cement raw material. The secondary environmental pollution due to the scattering of contaminated soil during the treatment work can be effectively prevented, and the fuel in the kiln can be saved by putting the whole container into the kiln and burning it.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 木立 明利 千葉県佐倉市大作二丁目4番2号 太平洋 セメント株式会社中央研究所内 (72)発明者 山口 修 千葉県佐倉市大作二丁目4番2号 太平洋 セメント株式会社中央研究所内 (72)発明者 後藤 俊朗 高知県高知市孕東町25 太平洋セメント株 式会社土佐工場内 (72)発明者 原口 輝美 東京都千代田区西神田三丁目8番1号 太 平洋セメント株式会社内 (72)発明者 長井 純 東京都千代田区西神田三丁目8番1号 太 平洋セメント株式会社内 (72)発明者 横田 昭博 高知県土佐市蓮池841−3 Fターム(参考) 4D004 AA41 AB05 AB06 AB07 AC07 BA02 BB09 CA28 CA30 CB02 CC13 CC17 4G012 KA02 KA08 ─────────────────────────────────────────────────── ─── Continued front page (72) Inventor Akitoshi Kitachi 2-4 Daisaku, Sakura City, Chiba Prefecture Pacific Ocean Central Research Institute of Cement Co., Ltd. (72) Inventor Osamu Yamaguchi 2-4 Daisaku, Sakura City, Chiba Prefecture Pacific Ocean Central Research Institute of Cement Co., Ltd. (72) Inventor Toshiro Goto 25 Taito-cho, Kochi City, Kochi Prefecture Taiheiyo Cement Co., Ltd. Ceremony company Tosa factory (72) Inventor Terumi Haraguchi 3-8-1, Nishikanda, Chiyoda-ku, Tokyo Heiyo Cement Co., Ltd. (72) Inventor Jun Nagai 3-8-1, Nishikanda, Chiyoda-ku, Tokyo Heiyo Cement Co., Ltd. (72) Inventor Akihiro Yokota 841-3 Hasuike, Tosa City, Kochi Prefecture F-term (reference) 4D004 AA41 AB05 AB06 AB07 AC07 BA02 BB09 CA28 CA30 CB02 CC13 CC17 4G012 KA02 KA08
Claims (7)
容器に梱包し、容器ごとセメントキルンに投入してセメ
ント原料と共に燃焼させることにより、有機系汚染土壌
をセメント原料として用いることを特徴とする有機系汚
染土壌のセメント原料化方法。1. The soil contaminated with organic pollutants is packed in a storage container, and the whole container is put into a cement kiln and burned together with the cement raw material to use the organic polluted soil as a cement raw material. Method for converting organic contaminated soil into a cement raw material.
染現場で収納容器に梱包し、セメント工場で容器ごとセ
メントキルンに投入する請求項1の方法。2. The method according to claim 1, wherein soil contaminated with organic pollutants is packed in a storage container at the site of contamination, and the whole container is put into a cement kiln at a cement factory.
化ビフェニル(PCB)、シアン化合物である請求項1ま
たは2の方法。3. The method according to claim 1, wherein the organic pollutant is dioxin, polychlorinated biphenyl (PCB), or a cyanide compound.
容器、木製容器、またはガラス製容器である請求項1、
2または3の方法。4. The container according to claim 1, wherein the storage container is a plastic container, a metal container, a wooden container, or a glass container.
Method 2 or 3.
樹脂、ポリビニルクロライドであって、キルンの燃焼温
度が1400℃以上である請求項1、2または3の方
法。5. The material of the storage container is polystyrene or ABS
The method according to claim 1, 2 or 3, which is a resin or polyvinyl chloride and has a kiln combustion temperature of 1400 ° C or higher.
ラス瓶である請求項1〜5の何れかに記載する方法。6. The method according to claim 1, wherein the storage container is a pail can, a drum can or a glass bottle.
造したセメント。7. A cement produced by the method according to claim 1.
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JP2001323978A JP4341001B2 (en) | 2001-10-22 | 2001-10-22 | Method for converting organic contaminated soil into cement |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006110504A (en) * | 2004-10-18 | 2006-04-27 | Taiheiyo Cement Corp | Treatment method of shellfishes |
JP2008253912A (en) * | 2007-04-04 | 2008-10-23 | Taiheiyo Cement Corp | How to handle hazardous substances |
JP2014161841A (en) * | 2013-02-27 | 2014-09-08 | Kureha Ecology Management Co Ltd | Incineration treatment method of drum can |
CN110606677A (en) * | 2019-10-22 | 2019-12-24 | 天津金隅振兴环保科技有限公司 | Ecological sintering material and preparation method and application thereof |
JP2021053591A (en) * | 2019-09-30 | 2021-04-08 | 住友大阪セメント株式会社 | Contaminated soil treatment method |
-
2001
- 2001-10-22 JP JP2001323978A patent/JP4341001B2/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006110504A (en) * | 2004-10-18 | 2006-04-27 | Taiheiyo Cement Corp | Treatment method of shellfishes |
JP2008253912A (en) * | 2007-04-04 | 2008-10-23 | Taiheiyo Cement Corp | How to handle hazardous substances |
JP2014161841A (en) * | 2013-02-27 | 2014-09-08 | Kureha Ecology Management Co Ltd | Incineration treatment method of drum can |
JP2021053591A (en) * | 2019-09-30 | 2021-04-08 | 住友大阪セメント株式会社 | Contaminated soil treatment method |
JP7215387B2 (en) | 2019-09-30 | 2023-01-31 | 住友大阪セメント株式会社 | Contaminated soil treatment method |
CN110606677A (en) * | 2019-10-22 | 2019-12-24 | 天津金隅振兴环保科技有限公司 | Ecological sintering material and preparation method and application thereof |
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