JPH042374A - Treatment of organic chlorine compound solvent - Google Patents
Treatment of organic chlorine compound solventInfo
- Publication number
- JPH042374A JPH042374A JP10392390A JP10392390A JPH042374A JP H042374 A JPH042374 A JP H042374A JP 10392390 A JP10392390 A JP 10392390A JP 10392390 A JP10392390 A JP 10392390A JP H042374 A JPH042374 A JP H042374A
- Authority
- JP
- Japan
- Prior art keywords
- organic chlorine
- converter
- compound solvent
- chlorine compound
- hot metal
- 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.)
- Pending
Links
- 239000002904 solvent Substances 0.000 title claims abstract description 35
- 150000004045 organic chlorine compounds Chemical class 0.000 title abstract 5
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000007664 blowing Methods 0.000 claims abstract description 12
- 239000002184 metal Substances 0.000 claims abstract description 11
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 4
- 239000010959 steel Substances 0.000 claims abstract description 4
- 229910001882 dioxygen Inorganic materials 0.000 claims abstract description 3
- 239000000460 chlorine Substances 0.000 claims description 31
- 229910052801 chlorine Inorganic materials 0.000 claims description 31
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 30
- 238000000034 method Methods 0.000 claims description 10
- 231100000614 poison Toxicity 0.000 abstract description 12
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 abstract description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 4
- 239000007789 gas Substances 0.000 abstract description 4
- 239000001301 oxygen Substances 0.000 abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 239000000428 dust Substances 0.000 abstract description 3
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 abstract description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 238000000354 decomposition reaction Methods 0.000 abstract description 2
- 230000007096 poisonous effect Effects 0.000 abstract 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract 1
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 abstract 1
- 239000003440 toxic substance Substances 0.000 description 11
- 238000002485 combustion reaction Methods 0.000 description 8
- 150000002013 dioxins Chemical class 0.000 description 7
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 239000003673 groundwater Substances 0.000 description 3
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 2
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- RFFLAFLAYFXFSW-UHFFFAOYSA-N 1,2-dichlorobenzene Chemical compound ClC1=CC=CC=C1Cl RFFLAFLAYFXFSW-UHFFFAOYSA-N 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 2
- RWNKSTSCBHKHTB-UHFFFAOYSA-N Hexachloro-1,3-butadiene Chemical compound ClC(Cl)=C(Cl)C(Cl)=C(Cl)Cl RWNKSTSCBHKHTB-UHFFFAOYSA-N 0.000 description 2
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000009841 combustion method Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 229950011008 tetrachloroethylene Drugs 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- AVGQTJUPLKNPQP-UHFFFAOYSA-N 1,1,1-trichloropropane Chemical compound CCC(Cl)(Cl)Cl AVGQTJUPLKNPQP-UHFFFAOYSA-N 0.000 description 1
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- SEQRDAAUNCRFIT-UHFFFAOYSA-N 1,1-dichlorobutane Chemical compound CCCC(Cl)Cl SEQRDAAUNCRFIT-UHFFFAOYSA-N 0.000 description 1
- PGEVTVXEERFABN-UHFFFAOYSA-N 1,1-dichloropentane Chemical compound CCCCC(Cl)Cl PGEVTVXEERFABN-UHFFFAOYSA-N 0.000 description 1
- RELMFMZEBKVZJC-UHFFFAOYSA-N 1,2,3-trichlorobenzene Chemical compound ClC1=CC=CC(Cl)=C1Cl RELMFMZEBKVZJC-UHFFFAOYSA-N 0.000 description 1
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- KNKRKFALVUDBJE-UHFFFAOYSA-N 1,2-dichloropropane Chemical compound CC(Cl)CCl KNKRKFALVUDBJE-UHFFFAOYSA-N 0.000 description 1
- QMSVNDSDEZTYAS-UHFFFAOYSA-N 1-bromo-1-chloroethane Chemical compound CC(Cl)Br QMSVNDSDEZTYAS-UHFFFAOYSA-N 0.000 description 1
- VFWCMGCRMGJXDK-UHFFFAOYSA-N 1-chlorobutane Chemical compound CCCCCl VFWCMGCRMGJXDK-UHFFFAOYSA-N 0.000 description 1
- SQCZQTSHSZLZIQ-UHFFFAOYSA-N 1-chloropentane Chemical compound CCCCCCl SQCZQTSHSZLZIQ-UHFFFAOYSA-N 0.000 description 1
- WLVCBAMXYMWGLJ-UHFFFAOYSA-N 3-(chloromethyl)heptane Chemical compound CCCCC(CC)CCl WLVCBAMXYMWGLJ-UHFFFAOYSA-N 0.000 description 1
- QKUNKVYPGIOQNP-UHFFFAOYSA-N 4,8,11,14,17,21-hexachlorotetracosane Chemical compound CCCC(Cl)CCCC(Cl)CCC(Cl)CCC(Cl)CCC(Cl)CCCC(Cl)CCC QKUNKVYPGIOQNP-UHFFFAOYSA-N 0.000 description 1
- OSDWBNJEKMUWAV-UHFFFAOYSA-N Allyl chloride Chemical compound ClCC=C OSDWBNJEKMUWAV-UHFFFAOYSA-N 0.000 description 1
- CAHQGWAXKLQREW-UHFFFAOYSA-N Benzal chloride Chemical compound ClC(Cl)C1=CC=CC=C1 CAHQGWAXKLQREW-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- KCXMKQUNVWSEMD-UHFFFAOYSA-N benzyl chloride Chemical compound ClCC1=CC=CC=C1 KCXMKQUNVWSEMD-UHFFFAOYSA-N 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229950005499 carbon tetrachloride Drugs 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- NEHMKBQYUWJMIP-NJFSPNSNSA-N chloro(114C)methane Chemical compound [14CH3]Cl NEHMKBQYUWJMIP-NJFSPNSNSA-N 0.000 description 1
- HRYZWHHZPQKTII-UHFFFAOYSA-N chloroethane Chemical compound CCCl HRYZWHHZPQKTII-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229960003750 ethyl chloride Drugs 0.000 description 1
- VHHHONWQHHHLTI-UHFFFAOYSA-N hexachloroethane Chemical compound ClC(Cl)(Cl)C(Cl)(Cl)Cl VHHHONWQHHHLTI-UHFFFAOYSA-N 0.000 description 1
- VFDYKPARTDCDCU-UHFFFAOYSA-N hexachloropropene Chemical group ClC(Cl)=C(Cl)C(Cl)(Cl)Cl VFDYKPARTDCDCU-UHFFFAOYSA-N 0.000 description 1
- ULYZAYCEDJDHCC-UHFFFAOYSA-N isopropyl chloride Chemical compound CC(C)Cl ULYZAYCEDJDHCC-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229940073584 methylene chloride Drugs 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- BNIXVQGCZULYKV-UHFFFAOYSA-N pentachloroethane Chemical compound ClC(Cl)C(Cl)(Cl)Cl BNIXVQGCZULYKV-UHFFFAOYSA-N 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 210000000689 upper leg Anatomy 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Fire-Extinguishing Compositions (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、IC(集積回路)の洗浄等に使用されてい
るトリクロロエチレン等の有機塩素系溶剤を安全に廃棄
処理する方法に係り、製鋼用転炉でこの有機塩素系溶剤
を1000℃以上の高温で燃焼させることによって、有
毒物質の発生を皆無にする有機塩素系溶剤の処理方法に
関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a method for safely disposing of organic chlorine solvents such as trichlorethylene used for cleaning ICs (integrated circuits), etc. The present invention relates to a method for treating an organic chlorine solvent in which no toxic substances are generated by burning the organic chlorine solvent at a high temperature of 1000° C. or higher.
従来の技術
トリクロロエチレン等の有機塩素系溶剤は、ハイテク産
業分野におけるICの洗浄用に大量に使用されている。BACKGROUND OF THE INVENTION Organochlorine solvents such as trichlorethylene are used in large quantities for cleaning ICs in high-tech industries.
これは、トリクロロエチレンは集積回路に付着した油分
を除去するのにガソリンの数倍という抜群の能力を持っ
ているためである。This is because trichlorethylene has an outstanding ability several times that of gasoline to remove oil adhering to integrated circuits.
しかし、一方でトリクロロエチレンは、発がん性があり
、かつ燃やせば塩素やダイオキシン、ホスゲン等の猛毒
物質が発生する。また、ドラム管等に詰めて長年放置し
たり、地下に埋めて投棄すれば、底が腐り中身が流れ出
して地面に吸込まれる。このため、我国においては、有
毒物質として地下水への排出が規制されるようになった
(平成1年10月より)。However, on the other hand, trichlorethylene is carcinogenic, and when burned, it releases highly toxic substances such as chlorine, dioxins, and phosgene. Also, if it is left in a drum pipe or the like for many years or buried underground and dumped, the bottom will rot and the contents will flow out and be sucked into the ground. For this reason, in Japan, its discharge into groundwater as a toxic substance has been regulated (from October 1999).
ところで、トリクロロエチレン等の有機塩素系溶剤は1
000℃以上の高温で燃やすと、前記ダイオキシンやホ
スゲン等の有毒物質は発生しないことが知られている。By the way, organic chlorine solvents such as trichlorethylene
It is known that toxic substances such as dioxins and phosgene are not generated when burned at a high temperature of 000° C. or higher.
しかし、トリクロロエチレン等の有機塩素系溶剤を処理
できる業者は、全国でもわずか約30社しがなく、不法
投棄等の事例もあり大きな社会問題となっている。しか
も、これら処理業者においても適正な処理がなされてい
るかははなはだ疑問な点も多い。However, there are only about 30 companies in the country that can process organic chlorine solvents such as trichlorethylene, and there are cases of illegal dumping, which has become a major social problem. Moreover, there are many questions as to whether these processing companies are disposing of waste properly.
環境庁の調査によれば、 4.6%の井戸から水質基準
以下のトリクロロエチレンが検出され、同じ有機塩素系
溶剤のテトラクロロエチレンは6.3%、1・ 1・
1トリクロロエタンは0.4%検出される等、汚染は全
国に広がっており、拡大の勢いは衰えを見せていないこ
とがわかった。According to a survey by the Environment Agency, trichlorethylene, which is below water quality standards, was detected in 4.6% of wells, and tetrachlorethylene, which is the same organic chlorine solvent, was detected in 6.3% of wells.
The contamination is spreading across the country, with 0.4% of 1-trichloroethane detected, showing no signs of slowing down.
発明が解決しようとする課題
トリクロロエチレン等の有機塩素系溶剤は、前記した通
り、地下に埋めて投棄すれば、地下水の汚染が問題とな
る。一方、1000℃を超える高温で燃やさないと、ダ
イオキシンやホスゲン等の有毒物質が発生する。Problems to be Solved by the Invention As mentioned above, if organic chlorine solvents such as trichlorethylene are buried and dumped underground, contamination of groundwater becomes a problem. On the other hand, if it is not burned at a high temperature exceeding 1,000 degrees Celsius, toxic substances such as dioxins and phosgene will be generated.
このため、有機塩素系溶剤の処理は、1000℃以上の
高温燃焼法か、化学的方法に頼らざるを得なす、コスト
高を余儀なくされているため、処理需要をまかなえでい
ないのが実情である。For this reason, the treatment of organic chlorine solvents has to rely on high-temperature combustion methods of over 1000°C or chemical methods, which are expensive and cannot meet the demand for treatment. .
二の発明は、このような実情に鑑みて、トリクロルエタ
ン/ン等の有機塩素系溶剤を1000℃を超える高温で
かつ定コストにて燃焼処理し、有毒物質の排出を防止す
る方法を提案しようとするものである。In view of these circumstances, the second invention proposes a method of burning organic chlorine solvents such as trichloroethane at a high temperature exceeding 1000°C at a fixed cost to prevent the emission of toxic substances. That is.
課題を解決するための手段
トリクロロエチレン等の有機塩素系溶剤を高温燃焼法で
廃却処理する場合、ダイオキシン、ホスゲン等の猛毒物
質を発生させないためには、1000℃を越える高温で
燃焼させる必要がある。しかし、通常の燃焼炉で安定し
て1000℃を超える高温を得るのは極めて困難である
。Means to solve the problem When disposing of organic chlorine solvents such as trichlorethylene using high-temperature combustion methods, it is necessary to burn them at high temperatures exceeding 1000°C in order to avoid generating highly toxic substances such as dioxins and phosgene. . However, it is extremely difficult to stably obtain a high temperature exceeding 1000° C. using a normal combustion furnace.
そこで、この発明者は、製鋼用転炉に着目し、転炉によ
り1000℃を超える高温でトリクロロエチレン等の有
機塩素系溶剤を燃焼処理できることを見い出したのであ
る。Therefore, the inventor focused on a converter for steel manufacturing and discovered that an organic chlorine solvent such as trichlorethylene can be burned at a high temperature exceeding 1000° C. using a converter.
転炉においては周知の通り、1300℃前後の溶銑を装
入し、純酸素で溶銑中の炭素を燃焼するため、常に13
00℃以上の燃焼温度が確保されている。したがって、
転炉内でトリクロロエチレン等の有機塩素系溶剤を燃焼
させると、猛毒物質の発生を防止できる。As is well known, in a converter, hot metal at around 1300°C is charged and the carbon in the hot metal is burned with pure oxygen, so the temperature is always 130°C.
A combustion temperature of 00°C or higher is ensured. therefore,
Burning organic chlorine solvents such as trichlorethylene in a converter can prevent the generation of highly toxic substances.
かかる知見より、この発明は溶銑または溶鋼が貯えられ
た転炉内に底吹き羽口等を介して有機塩素系溶剤を導入
し、酸素ガスを吹込んで1000℃を越える温度で燃焼
させることを要旨とするもものである。Based on this knowledge, the gist of this invention is to introduce an organic chlorine solvent into a converter where hot metal or steel is stored through a bottom blowing tuyere, blow in oxygen gas, and burn it at a temperature exceeding 1000°C. It is a thigh.
作 用
トリクロロエチレン等の有機塩素系溶剤の燃焼処理温度
を1000℃を越える温度に限定したのは、1000℃
以下の温度ではダイオキシン、ホスゲン等の有毒物質が
発生するためである。Effect The combustion treatment temperature of organic chlorine solvents such as trichlorethylene was limited to a temperature exceeding 1000°C.
This is because toxic substances such as dioxins and phosgene are generated at temperatures below.
転炉への有機塩素系溶剤の導入方法としては、炉底ある
いは炉側壁に設置されている既設の羽口やノズル等を使
用することができる。As a method for introducing the organic chlorine solvent into the converter, existing tuyeres or nozzles installed on the bottom of the furnace or the side wall of the furnace can be used.
転炉内における有機塩素系溶剤の反応は、次のように進
行する。The reaction of the organic chlorine solvent in the converter proceeds as follows.
■ 浴内の高温雰囲気下における分解反応CI H+n
C1n=1−C+m−H+n−C1■ 酸素ジェット
の表面および火点近傍における燃焼反応
C+1/20よ=CO
H2+1/202= Ht。■ Decomposition reaction CI H+n under high temperature atmosphere in bath
C1n=1-C+m-H+n-C1■ Combustion reaction on the surface of the oxygen jet and near the fire point C+1/20 = CO H2+1/202= Ht.
C+ 02= CO2
したがって、ダイオキシン、ホスゲン等の物質を発生さ
せることなく分解ないしは燃焼させることができるので
ある。C+ 02 = CO2 Therefore, it can be decomposed or burned without generating substances such as dioxins and phosgene.
ここで、有機塩素系溶剤としては、トリクロロエチレン
の他、次に記載するものが知られている。Here, as the organic chlorine solvent, in addition to trichlorethylene, the following are known.
塩化メチル、塩化メチレン、四塩化炭素、塩化エチル、
塩化エチレン、塩化エチリデン、トリクロルエタン、テ
トラクロルエタン、パークロルエチレン、ペンタクロル
エタン、ヘキサクロルエタン、ブロモクロルエタン、塩
化アリル、塩化イソプロピル、塩化プロピレン、トリク
ロルプロパン、塩化ブチル、ジクロルブタン、ヘキサク
ロルプロピレン、ヘキサクロルブタジェン、塩化アミル
、ジクロルペンタン、塩化2−エチルヘキシル、クロル
コサン、クロルベンゼン、O−ジクロルベンゼン、トリ
クロルベンゼン、クロルトルエン、ジクロルトルエン、
またはこれらの混合物。Methyl chloride, methylene chloride, carbon tetrachloride, ethyl chloride,
Ethylene chloride, ethylidene chloride, trichloroethane, tetrachloroethane, perchlorethylene, pentachloroethane, hexachloroethane, bromochloroethane, allyl chloride, isopropyl chloride, propylene chloride, trichloropropane, butyl chloride, dichlorobutane, hexachloropropylene, Hexachlorobutadiene, amyl chloride, dichloropentane, 2-ethylhexyl chloride, chlorcosane, chlorobenzene, O-dichlorobenzene, trichlorobenzene, chlorotoluene, dichlorotoluene,
or a mixture of these.
実 施 例
第1図はこの発明の一実施例を示す概略図で、(1)は
転炉、(2)は底吹き羽口、(3)は上吹ランス、(4
)は溶銑、(5)はスラグ、(6)はトリクロロエチレ
ン等の有機塩素系溶剤をそれぞれ示す。Embodiment FIG. 1 is a schematic diagram showing an embodiment of the present invention, in which (1) is a converter, (2) is a bottom blowing tuyere, (3) is a top blowing lance, and (4) is a bottom blowing tuyere.
) indicates hot metal, (5) indicates slag, and (6) indicates an organic chlorine solvent such as trichlorethylene.
すなわち、炉内に適当量の溶銑(4)が貯えられた転炉
(1)に、トリクロロエチレン等の有機塩素系溶剤(6
)を例えばNt ガスと共に底吹き羽口(2)より吹込
みながら、上吹ランス(3)より酸素を吹込んで炉内を
1000℃を超える温度に保持して有機塩素系溶剤を燃
焼させる。That is, a converter (1) in which an appropriate amount of hot metal (4) is stored is charged with an organic chlorine solvent (6) such as trichlorethylene.
) is blown in from the bottom blowing tuyere (2) together with, for example, Nt 2 gas, while oxygen is blown in from the top blowing lance (3) to maintain the inside of the furnace at a temperature exceeding 1000° C. to burn the organic chlorine solvent.
実施例1
処理溶銑量10トン規模の第1図に示す構造の小型試験
炉により、第1表に示す吹錬条件にてトリクロロエチレ
ン(CHCI CC1,)を燃焼処理した結果を第2表
に示す。Example 1 Table 2 shows the results of combustion treatment of trichlorethylene (CHCI CC1,) under the blowing conditions shown in Table 1 in a small test furnace having the structure shown in FIG. 1 and having a processing capacity of 10 tons of hot metal.
なお比較のため、従来の燃焼炉でトリクロロエチレンを
燃焼させた場合の燃焼条件および結果を併せて示す。For comparison, the combustion conditions and results when trichlorethylene was burned in a conventional combustion furnace are also shown.
第2表の結果より明らかなごとく、従来法では燃料(重
油)が大量に必要であり、かつ排ガス中のHCIが高い
のに加え、燃焼温度が低いため猛毒物質であるダイオキ
シン、ホスゲンが発生するのに対し、本発明では熱源に
溶銑を用いているので、燃料(重油)が不要であり経済
的であるとともに、ダイオキシン、ホスゲンを皆無にす
ることができた。また、排ガス中のHCI%Cl tは
高々250ppmと従来法の半分以下であり、しかもこ
れらはその大半を既設の湿式集塵装置により除去できる
ので、何等問題にはならない。As is clear from the results in Table 2, the conventional method requires a large amount of fuel (heavy oil), and in addition to high HCI in the exhaust gas, the low combustion temperature generates highly toxic substances such as dioxin and phosgene. On the other hand, in the present invention, since hot metal is used as a heat source, fuel (heavy oil) is unnecessary and economical, and dioxin and phosgene can be completely eliminated. Furthermore, HCI%Cl t in the exhaust gas is at most 250 ppm, which is less than half of the conventional method, and most of it can be removed by the existing wet type dust collector, so there is no problem.
以下余白
第
表
第
表
発明の詳細
な説明したごとく、この発明方法によれば、トリクロロ
エチレン等の有機塩素系溶剤を、ダイオキシン、ホスゲ
ン等の有毒物質を発生させることなく低コストで燃焼処
理することができ、しかも塩素ガス等も既設の集塵装置
によりほぼ完全に除去できるので、有機塩素系溶剤の処
理方法として極めて有効であり、有機塩素系溶剤による
地下水汚染など環境汚染の防止に大なる効果を奏するも
のである。As described in detail in Table 1 below, according to the method of this invention, organic chlorine solvents such as trichlorethylene can be combusted at low cost without generating toxic substances such as dioxins and phosgene. Furthermore, chlorine gas can be almost completely removed using existing dust collectors, making it extremely effective as a treatment method for organic chlorine solvents, and it is highly effective in preventing environmental pollution such as groundwater contamination caused by organic chlorine solvents. It is something to play.
【図面の簡単な説明】
第1図はこの発明の一実施例を示す概略図である。
1・・・転炉 2・・底吹羽口3・・
・上吹ランス 4・・溶銑6・・・有機塩素
系溶剤BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram showing an embodiment of the present invention. 1... Converter 2... Bottom blowing tuyere 3...
・Top blowing lance 4...Hot metal 6...Organic chlorine solvent
Claims (1)
上の温度で燃焼させる方法において、溶銑または溶鋼が
貯えられた転炉内に底吹き羽口等を介して有機塩素系溶
剤を導入し、酸素ガスを炉内に吹込んで1000℃を超
える温度で該有機塩素系溶剤を燃焼させることを特徴と
する有機塩素系溶剤の処理方法。In a method of burning an organic chlorine solvent such as trichlorethylene at a temperature of 1000°C or higher, the organic chlorine solvent is introduced into a converter in which hot metal or molten steel is stored through a bottom blowing tuyere, etc., and oxygen gas is injected into the furnace. A method for treating an organic chlorine solvent, which comprises blowing the organic chlorine solvent into a tank and burning the organic chlorine solvent at a temperature exceeding 1000°C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10392390A JPH042374A (en) | 1990-04-19 | 1990-04-19 | Treatment of organic chlorine compound solvent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10392390A JPH042374A (en) | 1990-04-19 | 1990-04-19 | Treatment of organic chlorine compound solvent |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH042374A true JPH042374A (en) | 1992-01-07 |
Family
ID=14366949
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10392390A Pending JPH042374A (en) | 1990-04-19 | 1990-04-19 | Treatment of organic chlorine compound solvent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH042374A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7407126B2 (en) | 2003-07-31 | 2008-08-05 | Fujifilm Corporation | Recording tape cartridge |
CN103596704A (en) * | 2011-04-29 | 2014-02-19 | 同济大学 | Treatment method of persistent organic pollutant in particulates |
-
1990
- 1990-04-19 JP JP10392390A patent/JPH042374A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7407126B2 (en) | 2003-07-31 | 2008-08-05 | Fujifilm Corporation | Recording tape cartridge |
CN103596704A (en) * | 2011-04-29 | 2014-02-19 | 同济大学 | Treatment method of persistent organic pollutant in particulates |
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