TW200944717A - Method of treating waste and heat-resistant compound obtained using the same - Google Patents

Method of treating waste and heat-resistant compound obtained using the same Download PDF

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Publication number
TW200944717A
TW200944717A TW098109858A TW98109858A TW200944717A TW 200944717 A TW200944717 A TW 200944717A TW 098109858 A TW098109858 A TW 098109858A TW 98109858 A TW98109858 A TW 98109858A TW 200944717 A TW200944717 A TW 200944717A
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Taiwan
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waste
heat
compound
dispersion
parts
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TW098109858A
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Chinese (zh)
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Osamu Sugiyama
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Hi Van Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/40Valorisation of by-products of wastewater, sewage or sludge processing

Abstract

Provided is a method of waste treatment by which a waste is efficiently treated without fail with satisfactory working efficiency and in which the waste is less apt to fly off or volatize. In particular, the waste treatment method renders substances containing a harmful chlorine compound harmless. Also provided is a technique for recycling and effectively utilizing a product obtained using the waste treatment method. The waste treatment method is characterized by depositing a waste dispersion comprising a waste, polyaluminum chloride, an alkaline substance, a sugar, and water on a granular substance and then subjecting this granular substance to a heat treatment. In particular, the method is a waste treatment method in which the waste is a chlorine compound. Further provided is a heat-resistant compound obtained using the waste treatment method.

Description

200944717 六、發明說明: 【發明所屬之技術領域】 本發明係關於廢棄物處理方法,詳言之,係關於將含有多 氣化紹之廢棄物为政液載持於粒狀物後再進行熱處理之廢 棄物處理方法’以及使用該方法所得之对熱性化合物。 【先前技術】 近年來,於廢棄物處理設施中焚燒廢棄物時,係被指摘會 β 生成戴奥辛類等毒性極強之物質。此現象之原因在於,廢棄 物中所含之多氣聯苯(PCB)等有機含氯化合物因為不完全 焚燒處理而不分解地以戴奥辛類之形式被再合成,並排放至 大氣中。又,含有PCB等有機含氯化合物之廢棄物,不僅於 焚燒時會產生戴奧辛類等而污染大氣,其本身亦有累積於土 壤中’會被吸收至農作物中’或者因雨水等而流出等的引起 環境污染之疑慮。 ® 多亂聯苯(PCB)因其優異的物性,係被廣泛使用作為熱 媒體、絕緣油等。因1968年Kanemi油症事件之發生,其對 生物體之毒性成為社會問題,於1972年全面被禁止製造· 使用。然而,目前仍有47000噸的PCB廢棄物以未處理之狀 態被保管著,若不儘速解決,將為後代種下禍根。 關於PCB處理,由於其耐熱性•耐水性,加上長期殘留 性、生物濃縮性、揮發移動性,在熱分解方面已知有以 l〇〇〇°C以上之高溫進行電漿分解之方法(參照專利文獻 098109858 3 200944717 卜使用觸媒等予以脫氣化之方法(參照專利文獻2)等。 」而上述方去均不是成本效益與安全性優異的方法需要 魔大的能量與時間。 另方面’作為試圖將廢棄物處理後之生成物的再資源化 的技術’例如可舉出專利文獻3。專利文獻3係藉由將含有 驗金屬離子等之無害化處理劑施用於含有重金屬、PCB等之 有0廢棄物,將有害廢棄物予以水泥固化,將所得之水泥固 化物再利用作為混凝土二次製品等之耐久性資材。然而,專 利文獻3係僅將PCB封入水泥固化物中並抑制其溶出至外 邛’對於以熱處理所進行之pCB分解處理並無揭示,以pCB 之完全無害化之觀點而言係為不完全。 (專利文獻1)日本專利特開2005-262196號公報 (專利文獻2)日本專利特開2005_263776號公報 (專利文獻3)日本專利特開2001-145859號公報 【發明内容】 (發明所欲解決之問題) 本發明係有鑑於上述技術背景而完成者,其目的在於提供 一種作業性良好,廢棄物不易飛散或揮散,且可效率良好地 確實處理廢棄物之方法。尤其係提供將上述般之含有有害含 氣化合物之物質予以無害化的廢棄物處理方法。並且將使用 該廢棄物處理方法所得之生成物予以再資源化並有效利用。 (解決問題之手段) 098109858 4 200944717 本發明人係為了解決上诚 疋問題而重複進行深入檢討,結果 發現’藉由將含有廢棄物、之 多氯化鋁、鹼性物質、醣類及水 之廢棄物分餘_於特定的粒狀物上,可防止有害之化合 ^專漏出至輯中,且藉由對载持有婦定廢棄物分散液之 、 止s乳化合物之不完全燃燒等所造 成之戴奥辛類等的發生,&amp; 遂70成本發明。此外,亦發現,使 用該廢棄物處理方法所 Ο ❹ ^獲件之生成物可再資源化為耐熱 性、導電性、耐藥品性等 … 赏吳的化合物,並可予以有效利用, 遂完成本發明。 亦即,本發明提供-種廢棄物處理方法,其特徵為將至少 有廢棄物夕氯她、驗性物質、醣類及水之廢棄物分散 液載持於粒狀物後,以如代以上進行域理。 又’本發明提供㈣轉棄物處理方法所得之_性化合 又本I明提供使用該廢棄物處理方法之财熱性化合物 的製造方法。 (發明效果) 根據本發明彳以良好作業性在廢棄物不易飛散或揮散之 片.兄下放率仏地確實處理廢棄物。又,藉由將廢棄物分散 液=持於粒狀物並進行熱處理’可將—等有害含氯化合物 等70全無害化’能夠提供環境性能亦優異之廢棄物處理方 根據本發@ ’藉由將載持著廢棄物分散液之粒狀物 予以熱處理,可提供能夠防止含氯化合物之不完全燃燒所造 098109858 5 200944717 成之戴奥辛類的產生,且環境性能優異之廢棄物處理方法。 此外,使用本發明之廢棄物處理方法所獲得之生成物係可提 供耐熱性、導電性、耐藥品性等優異之耐熱性化合物。 【實施方式】 以下針對本發明進行說明,但本發明並不限定於以下之實 施具體形態’可任意變化予以實施。 〈廢棄物分散液之組成〉 本發明係關於一種廢棄物處理方法,其特徵為將至少含有 廢棄物、多氣化鋁、鹼性物質、醣類及水之廢棄物分散液載 持於粒狀物後,以60(Tc以上進行熱處理。 廢棄物」係指必須丟棄的廢物,係為固形狀者(以下稱 為固體廢棄物」)或液狀者(以下稱為「液體廢棄物」)。 其中,作為本發明中所使用之「廢棄物」,κ要為可燃燒處 里者即可,無特別限定,可使用所有種類之廢棄物。其中, ^為該廢棄物H步發揮本發明之上述效果的觀點而 5,較佳為含有含氣化合物者,特佳為「因為其毒性而必須 特別管理廢棄物處理之含氯化合物」。 一,為「含氯化合物」,可舉出PCB(多氯聯苯)、四氯化碳、 氯甲垸、1,2-二氯乙@、i,i—二氯乙稀、順式―仏二氯 1烯反式-1,2-二氣乙烯、12_二氣丙烧、u—二氣丙稀、 —氣乙烧、1,1,2-二氯乙烷、三氣乙烯、四氯乙烷、 氯乙婦、DDT (二氣二笨基三氣乙燒)、pcp (多氣盼)、氯 098109858 200944717 人子〜氣笨、戴奥辛等。其中,pcB (多氣聯苯)係特別 適口「本發明 亦即,本發明較佳係使用於⑽之處理。 /氣化鋁」係以[AlXOfQnCih% ( igng5)表示之物 '質係礼以〇H所交聯之鋁的多核錯合體作為主成分的物質 之水办液。製造方法並無特別限制,較佳係將氫氧化鋁溶解 酸中’於加壓下或視需要而增加溶解助劑,並對其添加 邊基作為聚合促進劑,使其反應而成者。溶解助劑或聚合 促進劑係只要^損及本發明之效果,職特別限定。上述式 中m以10以下為佳。另外,以下,有時將上述水溶液簡 寫為「PAC」。本發明中,作為「多氣化鋁」或「pAC」,較佳 可使用一般市售之水之淨化用或廢水處理用者。所使用之 pAC中的鋁含有量並無特別限定,以Ah〇3換算計,較佳為 3〜30質量%,更佳為5〜20質量%,特佳為8~15質量%,尤隹 為10〜11質量%。又,jIS K 1475所規定者亦為特佳。 ® 作為「鹼性物質」’可舉出鹼金屬之氫氧化物(氩氧化鈉、 氩氧化鉀等)、鹼土類金屬之氫氧化物(氫氧化鎂、氫氧化 鈣、氫氧化鋇等)、其他金屬之氫氧化物(氫氧化鋁等)、錯 鹽之游離鹼(free base)的氫氧化物、氨、胺類(曱基胺、 乙基胺、乙醇胺等)、鹼金屬或鹼土類金屬之碳酸鹽(碳酸 鈉等)、鹼金屬或鹼土類金屬之碳酸氫鹽(碳酸氫鈉等)等。 藉由使用鹼性物質,可促進乳化與分散,且因為發熱,溶解、 分散作業等變得容易進行,亦可帶來成本之降低。使用氫氧 098109858 7 200944717 化鈉係可有效地乳化紐廢棄物,從生成「液_ 化=」之觀點、成本上有利之觀點而言,係為特J 作為_」,係可舉出葡萄糖、果糖等之單 : 等之雙醣類;殿粉類等之多聽類;㈣等。由於酶類二 =元:,故會成為熱處理中或熱處理後所生成之碳;: 的原枓’或促進燃燒。從容易操作、對水之 性高=價等觀點而言’以㈣類、纖維素等多 之竹生鱗輕。賴«衍线之縣並輯㈣t = 上述觀點而言’特佳為上白糖、三溫糖等砂糖;來自竿頭、 玉米等植物之殿粉或澱㈣之糊;米粉、糯米粉、小麥粉、 玉米粉、太白粉等榖類之粉末等。 「水」可含於上述PAC +,亦可另外添加。亦即,可在調 製廢棄物分散液時另外添加水,亦可不添加而僅為含於Μ 中之水。經由熱處理,水會有部分蒸發,但亦可能因反應、 父聯、配位等而被帶入多氣化紹中。 上述廢棄物分散液中,亦可進-步含有醇類。藉由含有醇 類,可暫時_ PCB等高減祕廢聽、醇可溶性廢棄物 等之低黏度醇稀釋物,可容易地载持於粒狀物上。又,其對 於促進廢棄物分散液之分散或乳化係為有效的。此外,=有 促進鹼性物質所造成之熱分解的效果。 乙 醇類係可舉出甲醇、乙醇、丙醇、丁醇等之丨元醇類; 丙二醇、三丙二醇 醇、二乙二醇、三乙二醇、丙二醇、二 098109858 8 200944717 等之2元醇類;甘油、季戊四醇、三羥p基丙貌等之多元醇 類等。其中,由環境保護及安全性之觀點而言,使用乙醇較 佳。 上述廢棄物分散液中,可進一步含有界面活性劑。經由含 有界面活性劑,係具有可使液體廢棄物之乳化分散液的調製 變得容易、可使個體廢棄物容易分散、可使廢棄物分散液容 易載持於粒狀物、促進乳化或熱分解等之效果。 _ 「界面活性劑」並無特別限定,可使用從陽離子性界面活 性劑、陰離子性界面活性劑、非離子性界面活性劑之中所選 擇之至少1種或2種以上之界面活性劑。其中,本發明中, 從降低環境負荷之觀點而言,使用陰離子系界面活性劑較 佳。作為陰離子系界面活性劑,可舉出長鏈脂肪酸之鹽等作 為較佳者。作為長鏈脂肪酸,特佳為來自植物者。 廢棄物、多氯化銘、驗性物質、醣類、水、醇類、界面活 生劑之調配比並無特別限定’較佳係廢棄物W質量份、多 氣化链(PAC)(紹含有量係換算為以A·換算計為1〇質量 %者之質量)5~10質量份、驗性物質(有結晶水之情況為除 °曰曰水之質量)4〜10質量份、糖類15〜20質量份、水(除 _的水之負量)◦〜質量份、醇類0~2質量份、界 面活性劑〇〜5質量份。 〈廢棄物分散液之形態〉 廢棄物分散液」只要為欲I棄的液體及/或個體的單- 098109858 200944717 物質或混合物分散於分㈣中所成者即可,其分散狀態並無 特別限定,當廢棄物為液體時,較佳係該液體廢棄物乳化分 散於含有水之分散射而成的液^亦即,本發明之「廢棄 物分散液」較佳為紐廢棄物之乳化分散液或固體廢棄物之 固體分散液。 「礼化分散液」係指在某種液體中將不溶解於其之其他液 體以細粒狀態分散,生成乳騎(emulsiQn,乳化液)之狀 態的液體。「㈣廢棄物之乳化分散液」係指例如於水中分 散廢油等液體廢棄物的狀態之液體。又,「 指於液體中分刪之㈣叫,並== (suspension)之狀態的液體。「固體廢棄物之固體分散液」 係指例如污泥等©體廢棄物分散於水等之巾的狀態之液體。 在此,作為「液體廢棄物」,例如可舉出含有上述pcB、 三氣乙烯等含氯化合物或含有其之廢油、絕緣油、廢酸、廢 驗等。又’作為「固體廢棄物」,例如可舉出廢木材、廢紙、 樅木殼、污泥、廢塑膠類、各種蛋白f殘渣(食料殘渣)等。 該等係視需要被進行前處理,錢其容易成為廢棄物分散 液。 &lt;粒狀物〉 本發明之廢棄滅理方法之魏在於,將上述廢棄物分散 液載持於綠物後’騎減理。#由_妹狀物,可使 作業性變佳’廢棄物不易缝或揮散,可效率佳地確實處理 098109858 10 200944717 廢棄物。又,亦有所得生成物可再利用作為有價物之情況。 在此,「粒狀物」只要係可載持上述廢棄物分散液之物質 即可,並無特別限定’特佳係使用從以下之中所選擇之物質: (1)碳質物; ⑴將含有多氯化減有機物之水系分散料以緞燒而成 之含鋁化合物; (3) 對無機粒子含浸含衫氣化滅有機物之水溶液並鍛 ❹燒而成之含鋁化合物被覆無機化合物; (4) 來自植物之粒狀物; 因可更有縣地㈣廢棄物分散液,並可提賴分解性。另 外,因同樣的理由,粒狀物以多孔性為佳。 (1)碳質物200944717 VI. Description of the invention: [Technical field to which the invention pertains] The present invention relates to a waste disposal method, and more particularly to a heat treatment in which a waste gas containing a plurality of gases is supported by a government liquid in a granular form. Waste treatment method 'and the thermal compound obtained by using the method. [Prior Art] In recent years, when waste is incinerated in a waste treatment facility, it is accused of β to form a highly toxic substance such as dioxin. The reason for this phenomenon is that organic chlorine-containing compounds such as polystyrene (PCB) contained in wastes are re-synthesized in the form of dioxins and are discharged into the atmosphere because they are not completely incinerated. In addition, wastes containing organic chlorine-containing compounds such as PCBs not only cause dioxins and the like to be polluted when incinerated, but also accumulate in the soil, which will be absorbed into crops, or flow out due to rain or the like. Concerns about environmental pollution. ® Multi-disinfected biphenyl (PCB) is widely used as a heat medium, insulating oil, etc. due to its excellent physical properties. Due to the occurrence of the Kanemi oil disease in 1968, its toxicity to living organisms became a social problem. In 1972, it was completely banned from manufacturing and use. However, there are still 47,000 tons of PCB waste that are kept in an untreated state. If not resolved as soon as possible, it will plant the bane for future generations. Regarding PCB processing, due to its heat resistance and water resistance, long-term residual property, bioconcentration property, and volatilization mobility, a method of plasma decomposition at a high temperature of 10 ° C or higher is known in thermal decomposition ( Reference Patent Document 098109858 3 200944717 A method of degassing using a catalyst or the like (refer to Patent Document 2), etc. The above-described method is not cost-effective and safety, and requires a large amount of energy and time. For example, Patent Document 3 discloses a technique for re-recycling a product that has been subjected to waste treatment. Patent Document 3 applies a harmless treatment agent containing a metal ion or the like to a heavy metal, a PCB, or the like. There is 0 waste, the hazardous waste is solidified by the cement, and the obtained cement cured product is reused as a durable material such as a concrete secondary product. However, Patent Document 3 only seals the PCB into the cement cured product and suppresses it. The elution to the outer enthalpy' is not disclosed for the pCB decomposition treatment by heat treatment, and is incomplete from the viewpoint of the complete detoxification of pCB. Japanese Patent Laid-Open Publication No. 2005-262196 (Patent Document 2) Japanese Laid-Open Patent Publication No. Hei. No. Hei. No. 2001-145859 (Patent Document 3). The present invention has been made in view of the above-described technical background, and an object of the present invention is to provide a method which is excellent in workability, in which waste is not easily scattered or volatilized, and which can efficiently treat waste efficiently. The substance of the gas compound is subjected to a harmless waste disposal method, and the product obtained by using the waste treatment method is re-resourced and effectively utilized. (Means for solving the problem) 098109858 4 200944717 The inventor of the present invention is to solve the problem. Repeatedly conducted an in-depth review of the problem and found that 'by removing waste containing polychlorinated aluminum, alkaline substances, sugars and water _ on specific granules, it can prevent harmful The chemical compound is leaked out into the series, and is caused by the incomplete combustion of the s milk compound by holding the dispersion of the woman's waste. In the case of the occurrence of dioxin, etc., it has also been found that the product of the waste treatment method can be recycled into heat resistance, electrical conductivity, chemical resistance, etc. The invention can be used effectively and can be used effectively. That is, the present invention provides a waste disposal method characterized in that at least a waste of chlorine, an organic substance, a sugar, and water can be used. After the waste dispersion is carried on the granules, it is subjected to the domain treatment as above. Further, the present invention provides (iv) the detachment treatment method, and the present invention provides the enthusiasm of using the waste treatment method. (Effect of the Invention) According to the present invention, the waste is not easily scattered or volatilized in the workability with good workability. In addition, by disposing the waste dispersion liquid in a granular material and performing heat treatment, it is possible to provide all of the harmful chlorine-containing compounds and the like 70, which can provide environmentally-friendly and excellent waste treatment according to the present invention. By heat-treating the granules carrying the waste dispersion, it is possible to provide a waste treatment method which is capable of preventing the incomplete combustion of the chlorine-containing compound and which is produced by 098109858 5 200944717 and having excellent environmental performance. Further, the product obtained by the waste treatment method of the present invention can provide a heat-resistant compound excellent in heat resistance, electrical conductivity, chemical resistance, and the like. [Embodiment] The present invention will be described below, but the present invention is not limited to the specific embodiments described below, and can be arbitrarily changed. <Composition of Waste Dispersion> The present invention relates to a waste treatment method characterized in that a waste dispersion containing at least waste, multi-aluminized aluminum, an alkaline substance, a saccharide, and water is carried in a granular form. After the material, heat treatment is performed at 60 (Tc or more. Waste) refers to waste that must be discarded, and is a solid shape (hereinafter referred to as solid waste) or a liquid (hereinafter referred to as "liquid waste"). In addition, as the "waste" used in the present invention, κ is not particularly limited, and all kinds of wastes can be used. Among them, ^ is the waste H step to exhibit the present invention. From the viewpoint of the above-mentioned effects, it is preferable to contain a gas-containing compound, and it is particularly preferable to "specify the chlorine-containing compound to be disposed of by the waste because of its toxicity." First, the "chlorine-containing compound" includes a PCB ( Polychlorinated biphenyls), carbon tetrachloride, chloroformamidine, 1,2-dichloroethane@, i,i-dichloroethylene, cis-indole dichloro-1-ene trans-1,2-digas Ethylene, 12_di-propylene, u-dipropylene, gas-fired, 1,1,2-dichloro Alkane, triethylene glycol, tetrachloroethane, chloroethene, DDT (two gas, two stupid, three gas, ethylene), pcp (multiple gas), chlorine, 098,109,858, 200944717, son, gas, stupid, dioxin, etc. Among them, pcB (Multi-gas biphenyl) is particularly suitable for the present invention. In other words, the present invention is preferably used in the treatment of (10). /Gasified aluminum is a product represented by [AlXOfQnCih% ( igng5). a method for producing a cross-linked aluminum multi-core complex as a main component. The production method is not particularly limited, and it is preferred to dissolve the aluminum hydroxide in an acid to increase the dissolution aid under pressure or as needed. The addition of a side group as a polymerization accelerator is carried out, and the dissolution aid or the polymerization accelerator is particularly limited as long as it has the effect of the present invention. In the above formula, m is preferably 10 or less. In the present invention, the above-mentioned aqueous solution may be abbreviated as "PAC". In the present invention, as the "polyaluminized aluminum" or "pAC", it is preferable to use a commercially available water for purification or wastewater treatment. The aluminum content in the pAC is not particularly limited, and is preferably in terms of Ah 〇 3 3 to 30% by mass, more preferably 5 to 20% by mass, particularly preferably 8 to 15% by mass, especially 10 to 11% by mass. Also, it is particularly preferable as defined by jIS K 1475. The "physical substance" may be an alkali metal hydroxide (such as sodium argon oxide or potassium argon oxide) or an alkali earth metal hydroxide (magnesium hydroxide, calcium hydroxide or barium hydroxide) or hydrogen of another metal. An oxide (such as aluminum hydroxide), a free base hydroxide of a wrong salt, ammonia, an amine (mercaptoamine, ethylamine, ethanolamine, etc.), an alkali metal or an alkaline earth metal carbonate ( A sodium carbonate or the like, a hydrogencarbonate such as an alkali metal or an alkaline earth metal (such as sodium hydrogencarbonate), etc. By using an alkaline substance, emulsification and dispersion can be promoted, and since heat generation, dissolution and dispersion work can be easily performed. It can also bring down the cost. Use of oxyhydrogen 098109858 7 200944717 Sodium hydride can effectively emulsifie new waste. From the viewpoint of producing "liquid _ _ =" and cost-effective, it is a special J as _", which is exemplified by glucose. Fructose and other singles: such as disaccharides; more than the class of temple powder; (four) and so on. Since the enzyme is two = element: it will become the carbon produced during or after the heat treatment; or the original 枓' or promote combustion. From the viewpoints of easy handling, high water quality, and price, it is lighter in bamboos such as (four) and cellulose. Lai «Dianxian County Compilation (4) t = From the above point of view, 'excellently is sugar on white sugar, three warm sugar, etc.; from the powder of the taro, corn and other plants or the paste of the lake (four); rice noodles, glutinous rice flour, wheat flour, Powder of glutinous rice such as corn flour and white powder. "Water" may be included in the above PAC + and may be additionally added. That is, water may be additionally added during the preparation of the waste dispersion, or may be added only to the water contained in the crucible. After heat treatment, the water will partially evaporate, but it may also be brought into the gasification process due to reaction, parental association, coordination, and the like. The waste dispersion may further contain an alcohol in a stepwise manner. By containing an alcohol, it is possible to temporarily carry a low-viscosity alcohol dilution such as high-definition, waste-absorbing, alcohol-soluble waste, etc., which can be easily carried on the granular material. Further, it is effective for promoting dispersion or emulsification of the waste dispersion. In addition, there is an effect of promoting thermal decomposition caused by alkaline substances. Examples of the alcohols include methanols such as methanol, ethanol, propanol, and butanol; propylene glycol, tripropylene glycol alcohol, diethylene glycol, triethylene glycol, propylene glycol, and di-ols such as 098109858 8 200944717; Polyols such as glycerin, pentaerythritol, trishydroxy-p-propyl and the like. Among them, the use of ethanol is preferable from the viewpoint of environmental protection and safety. The waste dispersion may further contain a surfactant. By containing a surfactant, the preparation of the emulsified dispersion of liquid waste can be easily made, the individual waste can be easily dispersed, and the waste dispersion can be easily carried on the granules, promoting emulsification or thermal decomposition. Etc. The "surfactant" is not particularly limited, and at least one or two or more surfactants selected from the group consisting of a cationic surfactant, an anionic surfactant, and a nonionic surfactant can be used. Among them, in the present invention, an anionic surfactant is preferably used from the viewpoint of reducing environmental load. As the anionic surfactant, a salt of a long-chain fatty acid or the like is preferable. As a long-chain fatty acid, it is particularly preferred to be from a plant. The blending ratio of waste, polychlorinated, test substances, sugars, water, alcohols, and interface bioactive agents is not particularly limited. 'Better waste W mass parts, multi-gasification chain (PAC) The content is 5 to 10 parts by mass in terms of A· conversion, and the amount of the test substance (in the case of crystal water, the mass of the water is removed) 4 to 10 parts by mass, sugar 15 to 20 parts by mass, water (negative amount of water other than _) ◦ to parts by mass, 0 to 2 parts by mass of the alcohol, and 5 to 5 parts by mass of the surfactant. <Form of Waste Dispersion> The waste dispersion is not limited as long as it is a liquid or/or individual of the liquid to be discarded and/or the individual is dissolved in the sub-(4). When the waste is a liquid, it is preferred that the liquid waste is emulsified and dispersed in a liquid containing water, that is, the "waste dispersion" of the present invention is preferably an emulsion dispersion of New Waste. Or a solid dispersion of solid waste. The "liqueced dispersion" refers to a liquid in which a liquid which is not dissolved in a liquid is dispersed in a fine particle state to form a milk riding (emulsiQn, emulsion) state. "(4) Emulsified dispersion of waste" means a liquid in a state in which liquid waste such as waste oil is dispersed in water, for example. In addition, "the liquid in the state of the liquid and the liquid in the state of the liquid, such as sludge, etc." State of the liquid. Here, examples of the "liquid waste" include a chlorine-containing compound such as pcB or triethylene, or a waste oil, insulating oil, waste acid, waste, or the like. Further, examples of the "solid waste" include waste wood, waste paper, eucalyptus shell, sludge, waste plastics, and various protein f residues (food residue). These systems are pre-treated as needed, and they are easy to become waste dispersions. &lt;Grained material&gt; The waste sterilizing method of the present invention is based on the fact that the above-mentioned waste dispersion liquid is carried on the green matter and is then subjected to riding reduction. #由_妹妹, can make workability better. 'Waste is not easy to sew or sway, can be processed efficiently 098109858 10 200944717 waste. Further, there are cases where the resultant product can be reused as a valuable product. Here, the "granular substance" is not particularly limited as long as it can carry the above-mentioned waste dispersion liquid, and it is not particularly limited to use a substance selected from the following: (1) carbonaceous matter; (1) (A) an aqueous solution containing an aluminum compound impregnated with an aqueous solution containing an organic solvent and immersed in an inorganic solution; ) granules from plants; because of the county (4) waste dispersion, and can be decomposed. Further, for the same reason, the granular material is preferably porous. (1) Carbonaceous matter

「碳質物」係指實質上以單體碳作為主成 係可载持上述廢棄物分錄者,職㈣限定,^木炭要 竹厌專係Μ表面積纽為多孔性之觀點而言,可有效地吸 附廢棄物’且可提升分解熱,因此特職合使用。 ⑴將含有錢化減有機物之水系錢⑽燒而成之含 減人Γ有多氣⑽及有機物之水系分散液锻燒而成之含 Γ有ΪΓ町簡稱「含紹化合物」)」係指將含有多氯化紹 H物之水溶_ 26{rc〜綱力喊所生成之含銘化合 物3銘化合物中亦有含有碳質物之情況。 098109858 11 200944717 在此,作為使用於含紹化合物之「 本發明中所使用之「多氯化銘」相同:氣化叙」,可使用與 或「㈣」,可較佳使用一般市 者。作為「多氯化錯」 者(例如川U475所規定者等)。之錢用或廢水處理用 有量並無特別限制’以Ai2〇3換料所=用之PAC中的叙含 更佳為5〜20質量%,特佳為81 :為3,質量%, 進一步追加水而使用。 °。另外,亦可適當地 作為「有機物」,只要 下為液體之有機物或kv&gt;厌’、’則無特別限定’常溫 有機物或水溶性有機物 沸點高且處理容易、對水之溶解性古=使用。其中,由 利用锻燒而獲得比重小 ㈤*全性局、低價、可 為葡萄糖、果糖、_、化合物等觀點而言,較佳 '、’又粉4醣類或醣類之衍生物等。 夕氣化鋁(PAC)與有機物 好之含銘化合物的方式n配比率,只要以可生成良 飞調配,則無特別限定,當鋁含有量以 二,計為1G f#%之W的情況,相對於該PAC 100 、伤有機物較佳為1〇〜彻質量份更佳為質量 寺佳為30〜100質量份。當紹含有量不為10質量%之PAC :、上述厢己比率以紹換算計進行比例增減之範 圍為較 佳範圍。 作為锻燒之方法,可舉出在加熱爐中靜置並煅燒之方法、 直接接觸於火焰之方法、供給至連續锻燒爐之方法、以滑行 ,下方式進行之方法等。其中,以熱效率之觀點*言’利用 098109858 ◎ ❹ 12 200944717 杯式燃燒器等而直接接觸於火焰之方、土 、乃击係為較佳。直接接觸 於火焰之方法中’燃燒氣體並無特別限制,較佳為氨、尹燒、 乙烷、丙烷、丁烷、一氧化碳、都市氣體等。 锻燒通常於鮮C〜讓。C之範财進行。職溫度較佳 為40〇。02〇0代之範圍,更佳為_。(&gt;18〇〇。〇:之範圍,特 佳為700°C〜1500°C之範圍,最佳為8〇(rc〜1〇〇〇t:之範圍。 又,煅燒環境並無特別限定,可為真空中;氮、氬等惰性氣 ❹體中;空氣、氧等活性氣體中等之任一者。 煅燒之時間並無特別限定,在靜置於加熱爐中煅燒之方法 中,較佳為10〜60分鐘,更佳為分鐘,特佳為2〇 25 分鐘。又,在直接接觸於火焰之方法中,較佳為2分鐘〜3〇 分鐘,更佳為3分鐘〜20分鐘,特佳為5〜10分鐘。另外, 瓜燒可在氧存在下等之氧化環境中進行,亦可在非氧化環境 中進行,特佳為在氧存在下等之氧化環境中進行。 ❹ 煅燒所得之碳鋁複合化合物係視需要而予以解碎或粉 碎,製成粒狀物。 (3)對無機粒子含浸含有多氯化鋁及有機物之水溶液並煅 燒而成之含鋁化合物被覆無機化合物 . 「對無機粒子含浸含有多氣化鋁及有機物之水溶液並煅 燒而、成之含鋁化合物被覆無機化合物(以下簡稱為「含鋁化 合物被覆無機化合物」)」係將上述「含有多氣化鋁及有機物 之水溶液」含浸於含有無機粒子之物質中,將其以 098109858 13 200944717 260°C〜2800°C煅燒而成之含鋁化合物被覆無機化合物。 「含鋁化合物被覆無機化合物」之構造係可為無機粒子經 過煅燒,在化學上及/或形狀上經變化之無機粒子的周圍, 被覆上述(2)「含鋁化合物」而成之構造;亦可於該無機粒 子中滲透「多氣化鋁及含有機物之水溶液」,於該狀態下同 時進行缎燒而藉以生成單獨的無機粒子。又,亦可為具有兩 者之組合者,亦即作為芯之無機粒子發生改質,且具有被覆 構造者。 在此,「無機粒子」之種類、形狀均無特別限定。種類係 可舉出碳酸鈣、硫酸鋇、滑石、無機著色顏料、石綿、合成 硬賴石、玻璃纖維(亦包含玻璃絨)#。作為上述無機粒 子,較佳係含於廢棄物巾’ U石纟帛、合成硬销石:玻璃 纖維等之有害廢棄物為佳。又,屬於廢棄物之「含填充材之 樹脂」中普遍含有之上述泛用填充材亦特佳。 作為含鋁化合物被覆無機化合物中所使用之「多氯^ 銘」,只要使用與本發明中作為必須成分所❹d j 紹:)或上述⑴「含銘化合物」製造 相同者即可。"Carbonaceous matter" means that the above-mentioned wastes can be carried mainly by the monomeric carbon as the main system, and the job is limited to four (4), and the charcoal is generally porous. The ground adsorption waste 'can increase the heat of decomposition, so it is used in special occupations. (1) The water containing the money and the organic matter (10), which is made of a water-based dispersion containing a reduced amount of sputum and suffocating (10) and organic matter, is abbreviated to include Γ Γ ΪΓ 简称 简称 简称 简称 简称 简称 简称 简称 简称The water-soluble solution containing the polychlorinated H compound _ 26 {rc ~ Gang Li shouted by the containing compound 3 Ming compound also contains carbonaceous material. 098109858 11 200944717 Here, as the "multi-chlorination" used in the present invention, the "gasification" used in the present invention can be used in conjunction with or "(4)", and the general market can be preferably used. As a "polychlorinated error" (for example, as specified by Chuan U475). There is no particular limitation on the amount of money used or waste water treatment. 'Replacement with Ai2〇3 = more preferably 5 to 20% by mass in the PAC, especially 81: 3, mass%, further Use water instead. °. Further, it may be suitably used as an "organic substance", and it is not particularly limited as long as it is a liquid organic substance or kv&gt;, and the organic substance or the water-soluble organic substance has a high boiling point and is easy to handle, and has a solubility in water. Among them, by using calcination to obtain a small specific gravity (five) * full nature, low price, can be glucose, fructose, _, compounds, etc., preferably ', ' and powder 4 sugar or sugar derivatives, etc. . In the case where the ratio of the aluminum compound (PAC) to the organic compound is better than that of the compound containing the compound, the ratio is not particularly limited as long as it can be used to form a good fly. When the aluminum content is two, it is 1 G f#% of W. It is preferable that the PAC 100 and the organic matter to be damaged are preferably 1 〇 to the mass part, and the mass is preferably 30 to 100 parts by mass. When the content of PAC is not 10% by mass, the ratio of the above-mentioned ratio is proportional to the range of increase or decrease. Examples of the calcination method include a method of standing and calcining in a heating furnace, a method of directly contacting a flame, a method of supplying to a continuous calcining furnace, a method of performing sliding, and the like. Among them, from the viewpoint of thermal efficiency, it is preferable to use the 098109858 ◎ ❹ 12 200944717 cup type burner or the like to directly contact the flame side, the earth, and the blasting system. The method of directly contacting the flame is not particularly limited, and is preferably ammonia, yin, ethane, propane, butane, carbon monoxide, or municipal gas. Calcination is usually done in fresh C~. C's fanship is carried out. The job temperature is preferably 40 〇. 02〇0 generation range, better _. (&gt;18〇〇.〇: The range, particularly preferably in the range of 700 ° C to 1500 ° C, preferably 8 〇 (rc ~ 1 〇〇〇 t: range. Also, the calcination environment is not particularly limited It may be in a vacuum; an inert gas such as nitrogen or argon; or any one of an active gas such as air or oxygen. The calcination time is not particularly limited, and it is preferably a method of calcination in a heating furnace. It is preferably 10 to 60 minutes, more preferably 2 minutes and 25 minutes. Further, in the method of directly contacting the flame, it is preferably 2 minutes to 3 minutes, more preferably 3 minutes to 20 minutes. Preferably, the melon burning can be carried out in an oxidizing atmosphere such as in the presence of oxygen, or in a non-oxidizing environment, and particularly preferably in an oxidizing atmosphere such as in the presence of oxygen. The carbon-aluminum composite compound is pulverized or pulverized as needed to form a granule. (3) The inorganic compound is impregnated with an aqueous solution containing aluminum chloride and an organic substance and calcined to form an inorganic compound coated with an inorganic compound. The inorganic particles are impregnated with an aqueous solution containing a plurality of vaporized aluminum and an organic substance and calcined The aluminum-containing compound-coated inorganic compound (hereinafter referred to as "aluminum-containing compound-coated inorganic compound") is obtained by impregnating the above-mentioned "aqueous solution containing a plurality of vaporized aluminum and an organic substance" into a substance containing inorganic particles, and 098109858 200944717 An aluminum compound-coated inorganic compound calcined at 260 ° C to 2800 ° C. The structure of "aluminum-containing compound-coated inorganic compound" may be an inorganic particle whose inorganic particles are calcined and chemically and/or shape-changed. The structure is covered with the above (2) "aluminum-containing compound"; it is also possible to infiltrate the "polyaluminized aluminum and the organic-containing aqueous solution" into the inorganic particles, and simultaneously perform satin burning in this state to generate a separate In addition, the inorganic particles may be modified as the inorganic particles of the core, and may have a coating structure. The type and shape of the "inorganic particles" are not particularly limited. Examples thereof include calcium carbonate, barium sulfate, talc, inorganic coloring pigments, asbestos, synthetic hard lye, and glass fiber (also including glass wool). It is preferable that the inorganic particles are contained in a waste waste such as U-stone, synthetic hard stone: glass fiber, etc. Also, it is a "resin-containing resin" of waste. The above-mentioned general-purpose filler is also particularly preferable. As the "organic compound" used as the inorganic compound-coated inorganic compound, as long as it is used as an essential component in the present invention, the above-mentioned (1) or "Ming compound" can be manufactured the same.

+ m 「 以)含鋁化合物I 所使用之「有機物」相同者即可。锻燒 與上述⑴「含紹化合物」之情沉相同之二與條件亦, 瓜燒所付之含銘化合物被覆無機化人物’、、 , 098109858 109858 ' 200944717 粉碎而做成粒狀物。 (4)來自植物之粒狀物 作為「來自植物之粒狀物」,只要為可載持上述廢棄物分 散液者,則無特別限定,例如可舉出木屑、美人蕉(canna) 碎屑等之木質粒子·,廢紙、瓦榜紙、碎紙等之紙類;豆渣殘 造;玉米、麥、稻等之·;稻殼、祕殼等之穀類殼等。 該等來自植物之粒狀物’利用熱處理或至少於熱處理之初 ❹ 期中’係成為碳質物或「鋁與碳之複合物」。 〈廢棄物處理方法〉 本發明之廢聽處财㈣至少包含⑴錢物分散液 之調製、⑺對粒狀物之載持以及(3)熱處理。 (1)廢棄物分散液之調製 廢棄物分散液之調製方法並無特別限定。具體而言,例如 首先可至少適量調配氫氧化鈉等驗性物質之水溶液、PC 廢棄物以及多氣化鋁(PAC)並予以 等驗性物質亦發揮使_有機廢。二’氫氧化納 使之發熱㈣低價使分散等處理變得容^力用。又,可 亦可適當添加W等賴及/或細1階段中, 使用在溶解KB等有機廢棄物而調製 醇類亦可適當 乳化與分散有所幫助。 ★。界面活性劑係對 醣類亦可與廢棄物等同時添加於 中,但較佳係作為下—㈣,之後 /㈣之水溶液 _ 4加於上述溶液中。 200944717 2可在將廢棄物分驗_於_物上後’將最初載持廢 絲分散躲粒狀⑽之該廢棄物分散液中所未含有之= ^未全1含有之成分’在其後載持於粒狀物上。此情況, 本發明之「廢棄物分散液」係载持於粒狀物並且完成調製。 之後’作為可載持於粒狀物者,可舉出PCB等廢棄物、PAC、 醣類之水溶液等。尤其在_鹼性物f後藉由在之後 PAC載持於粒狀物’發生反應發熱分解,可促進乳化或熱分 © 解’且有因被覆效果而防止含氯化合物揮發等之效果。、刀 (2)對粒狀物之載持 將廢棄物分散液麟於粒狀物之方法並無特別限定,例々 可對上述所_之廢棄物分散液加人適量粒狀物,利用私 攪拌等而進行。該粒狀物係具有選擇吸附廢棄物中之^ 等的作用。當進行混合_,減會慢慢增加,生成載持有 廢棄物分散液之㈣物Ux下稱為「絲齡餘載持粒狀 物」)。 相對於粒狀物100質量份,較佳係麟卜2〇質量份之廢 :物分散液,更佳係載持2〜10質量份,特佳係栽持3 5質 量伤。相對於粒狀物,若廢棄物分散液過少,則可能有廢棄 物處理之效率降低的情況,若過多,則可能無法防止飛=與 揮散,或者有即便經過熱處理,仍無法完全無害化之情況。 (3)熱處理 月 作為熱處理之方法,可舉出靜置於加熱爐中之方法、直接 098109858 16 200944717 接觸火焰之方法、供給至連續加熱爐之方法、以滑行落下方 式進行之方法等。其中,由於在加熱爐中進行熱處理之方法 係可使含氯化合物完全燃燒,因而可抑制有毒燃燒氣體之發 生,可釋出無害的氣體,故以提升安全性等之觀點而言為 . 佳。加熱爐中之熱處理係例如將廢棄物分散液載持粒狀物塞 入棒子等中,將其放入5方位由陶瓷斷熱所包圍之加熱爐中 等而進行。由熱效率之觀點而言,直接接觸於火焰之方法亦 ❹較佳。直接接觸於火焰之方法中,燃燒氣體並無特別限定, 較佳為氫、曱烧、乙烧、丙烧、丁焼、一氧化碳、都市氣體 等。 於加熱爐中進行熱處理之情況,較佳係於爐内之環境溫度 (以下有時簡記為「爐内溫度」)為6〇〇〜28〇〇ΐ之溫度條件 下進行。又,「加熱爐之設定溫度」或「放入廢棄物分散液 前之爐内溫度」,較佳為60(TC〜180(TC之範圍,更佳為 ® 700°c〜150〇°C之範圍,特佳為80{TC〜100(TC之範圍。相較 於必須預先將加熱爐之溫度設定為100(rc以上的電漿分解 法,本發明之方法可將加熱爐之溫度設定為較低溫。 於加熱爐中進行熱處理之情況,經由熱處理,可將燃燒中 之物質的溫度(以下有時簡記為「燃燒溫度」)定為9〇〇»c 以上。進一步可定為95(TC以上,亦可定為1〇〇〇。(:以上。因 此’為了使從含氯化合物等廢棄物所產生之屬於有害有機物 的分解氣體燃燒,燃燒溫度較佳為900〇c以上,更佳為95(rc 098109858 17 200944717 以上,特佳為1000Ϊ以上。 ^熱處理環境並無特別限定,可為真空巾;氮、氬等惰 氣體中,4氣、氧等活性氣體中等之任一者。本發明中, 從操作之各易度的觀點而言,較佳係於空氣中進行加熱。 直接接觸於火焰之方法的熱處理溫度以及在加熱爐中進 行…處理之情況㈣燒溫度’储由將熱電偶輻射溫度計感 、朱針(外稍尺寸為例如Φ8χ500πιιη)插入待測物之中而+ m "Yes" is the same as the "organic matter" used in the aluminum compound I. Calcination The same conditions and conditions as in the above (1) "containing the compound" are also the conditions. The infused compound of the melon-burning compound is coated with the inorganic character ',, 098109858 109858 ' 200944717 and pulverized to form a granular material. (4) The granules of the plant are not particularly limited as long as they are capable of carrying the above-mentioned waste dispersion, and examples thereof include wood chips and canna crumbs. Wood particles, waste paper, tiled paper, shredded paper, etc.; bean residue; corn, wheat, rice, etc.; rice husks, shells and other cereal shells. These plant-derived granules are "carbonized or "a composite of aluminum and carbon" by heat treatment or at least in the initial stage of heat treatment. <Waste disposal method> The waste disposal service (4) of the present invention includes at least (1) preparation of a money dispersion, (7) loading of a granular material, and (3) heat treatment. (1) Preparation of waste dispersion The preparation method of the waste dispersion is not particularly limited. Specifically, for example, at least an appropriate amount of an aqueous solution of an organic substance such as sodium hydroxide, a PC waste, and a polyaluminized aluminum (PAC) can be prepared at least in an appropriate amount, and the same substance can be used as an organic waste. The second 'sodium hydroxide makes it heat up. (4) The low price makes the treatment such as dispersion become more powerful. Further, it is also possible to appropriately add emulsification and dispersion in order to dissolve the alcohol by dissolving organic waste such as KB in the first step. ★. The surfactant may be added to the sugar at the same time as the waste, but it is preferably added as the lower-(four), and then the aqueous solution _4 is added to the above solution. 200944717 2 After the waste is inspected _ after the _ thing, the waste material which is initially contained in the waste dispersion (10) is not contained in the waste dispersion which is not contained in the waste dispersion. Loaded on the granules. In this case, the "waste dispersion" of the present invention is carried on the granules and the preparation is completed. Then, as a sample which can be carried on a granular material, waste such as a PCB, an aqueous solution of PAC or a saccharide, or the like can be given. In particular, after the basic substance f, the PAC is carried by the particulate matter in the subsequent reaction, and the emulsification or heat separation is promoted, and the effect of preventing the volatilization of the chlorine-containing compound by the coating effect is promoted. The method of the knives (2) for carrying the granules is not particularly limited as long as the waste dispersion liquid is granulated. For example, the above-mentioned waste dispersion may be added with an appropriate amount of granules, and the granules may be used. It is carried out by stirring or the like. The granules have an effect of selectively selecting the adsorbed waste. When mixing _, the decrease will gradually increase, and the (4) Ux under the load holding waste dispersion will be referred to as "silk-loaded granules". With respect to 100 parts by mass of the granules, it is preferred to use 2 parts by mass of the waste material, more preferably 2 to 10 parts by mass of the granules, and more preferably 3 to 5 parts by weight. If the amount of the waste dispersion is too small, the efficiency of the waste treatment may be lowered. If the amount is too large, the fly may not be prevented from being scattered or volatilized, or the heat treatment may not be completely harmless. . (3) Heat treatment month As a method of heat treatment, a method of standing in a heating furnace, a method of directly contacting 098109858 16 200944717, a method of supplying to a continuous heating furnace, a method of sliding down, and the like are exemplified. Among them, since the heat treatment in the heating furnace can completely burn the chlorine-containing compound, the generation of the toxic combustion gas can be suppressed, and the harmless gas can be released, so that it is preferable from the viewpoint of improving safety and the like. In the heat treatment in the heating furnace, for example, the waste dispersion-carrying granular material is placed in a rod or the like, and placed in a heating furnace surrounded by ceramic heat insulation in five directions. From the viewpoint of thermal efficiency, a method of directly contacting the flame is also preferred. In the method of directly contacting the flame, the combustion gas is not particularly limited, and is preferably hydrogen, helium, ethylene, propylene, butadiene, carbon monoxide, and city gas. The heat treatment in the heating furnace is preferably carried out at a temperature of 6 Torr to 28 Torr depending on the ambient temperature in the furnace (hereinafter sometimes referred to as "in-furnace temperature"). Further, "the set temperature of the heating furnace" or "the temperature in the furnace before the waste dispersion liquid is placed" is preferably 60 (TC to 180 (the range of TC, more preferably 700 ° C to 150 ° ° C) The range is particularly preferably 80{TC~100 (the range of TC. The method of the present invention can set the temperature of the heating furnace to be compared with the plasma decomposition method in which the temperature of the heating furnace must be previously set to 100 (rc or more). When the heat treatment is performed in a heating furnace, the temperature of the substance in combustion (hereinafter sometimes abbreviated as "combustion temperature") can be set to 9 〇〇»c or more by heat treatment. Further, it can be set to 95 (TC or higher). It can also be set to 1 〇〇〇. (: Above. Therefore, in order to burn a decomposition gas belonging to harmful organic substances generated from wastes such as chlorine-containing compounds, the combustion temperature is preferably 900 〇c or more, more preferably 95. (rc 098109858 17 200944717 or more, particularly preferably 1000 Å or more. ^The heat treatment environment is not particularly limited, and may be any one of a vacuum napkin, an inert gas such as nitrogen or argon, or an active gas such as 4 gas or oxygen. From the point of view of the ease of operation, the system is preferred. Heating in the air. The heat treatment temperature of the method of direct contact with the flame and the treatment in the heating furnace. (4) The burning temperature is stored by the thermocouple radiation thermometer, and the needle (the outer size is, for example, Φ8χ500πιιη) is inserted into the test. Among things

測疋,本|明之上述熱處理溫度係定義為以此種方法測定 者0 理之二:時間並無特別限定在靜置於加熱爐中進行熱》 為7 、較佳為3分鐘以上,更佳為分鐘,特4 為7〜40分鐘,最佳為7 .^ ^ 刀隹里。又,相較於靜置於加熱丈 中而進行熱處理之方法, I ^ 雖由於生成氣體有一部分會釋出戈 大軋中,以方法而言稍有缺 μ比 令缺,點值使用直接接觸火焰之方The above-mentioned heat treatment temperature is defined as the second measurement by the method: the time is not particularly limited, and the heat is set in the heating furnace to be 7, preferably 3 minutes or more, more preferably For the minute, the special 4 is 7 to 40 minutes, and the best is 7. ^ ^ Knife. Moreover, compared with the method of heat treatment which is placed in the heating chamber, I ^, although a part of the generated gas will be released into the Goda rolling, the method is slightly lacking in μ ratio, and the point value is directly contacted. Flame side

的情況,較佳為1分鐘〜3〇 ^ ^ U刀鐘,更佳為2分鐘〜20分鐘 特佳為5〜10分鐘。 〈耐熱性化合物〉 使用本發月之廢棄物處理方法,則會生成财熱性化/The case is preferably 1 minute ~ 3 〇 ^ ^ U knife clock, more preferably 2 minutes ~ 20 minutes Tejia is 5 to 10 minutes. <Heat-resistant compound> When using the waste disposal method of this month, it will generate heat/heating/

物。該耐熱性化合物係可作A 馬有價物而使用於各種用途。; 發明同時係關於使用本發明 廢棄物處理方法所獲得之《i 熱性化合物。本發明之耐埶 *、、、生化合物以下述評估方法予以1 估時之外觀係實質上不產生 雙化,質量變化為0.3質量%〗 098109858 200944717 下。另外,耐熱性化合物之質量變化亦包含於因吸附水分之 汽化而產生者。 [耐熱性之評估] 將使用本發明之廢棄物處理方法所獲得之耐熱性化合物 的粉末20g、或20g之成型為大致立方體的該耐熱性化合 物,置入實質上遮蔽空氣之烙室爐中,以130ITC加熱24小 時,觀察外觀、質量之變化。 ❹ 本發明之耐熱性化合物不僅耐熱性,導電性及/或耐藥品 性亦優異。關於導電性,以下述評估方法評估時,比電阻可 在1(Γ6Ω · cm以下。因此’較佳係ι〇_6ω · cm以下者。 〈導電性之評估〉 將使用本發明之廢棄物處理方法所獲得之耐熱性化合物 以研体粉碎製成粉末’將其塞入φ 7则1、長200mm之丙稀酸 系樹脂製管之中’從2cm之高度拍打5次。其後,從塞入管 ® 中之試料的上方與下方施加直流電壓,測定20°C下之電流 值。從電流值算出塞成該形狀之粉末於該形狀下之比電阻。 〈财藥品性之評估〉 關於耐藥品性,當以下述評估方法評估時,不管對於何種 藥品’以目視均無法觀察到化學反應。因此,關於耐藥品性, 當以下述評估方法評估時,較佳係對任何藥品均不發生化學 反應。 取使用本發明之廢棄物處理方法所獲得之㈣性化合物 098109858 19 200944717 l〇g置於燒瓶中’分別添加丨晚之1N(標準濃度)稀硫酸、 5質量錢氧化納、丙_,靜置於赃下,觀察化學反應之 有無。 本發明之廢棄物處理方法中,使用含有量18%之PCB做為 廢棄物時’所得之耐熱性化合物中的PCB含有量以氣相色層 分析法進行定量(中外Techn〇s公司分析)時,可為定量下 限值0. 0016mg/kg以下。因此,本發明之耐熱性化合物較佳 係以耽相色層分析進行評估時為〇 . Q 〇 1 6mg/kg以下者。 根據本發明之廢棄物處理方法則不會產生有害之燃燒氣 體的作用•原理尚不明朗,但可考慮如下。但本發明並不限 定於以下之作用效果的範圍。亦即,將含有廢棄物、多氯化 鋁、鹼性物質、醣類及水之廢棄物分散液載持於粒狀物後, 進行熱處理,則僅有從含氣化合物等廢棄物所產生之有害有 機物分解氣體進行表面燃燒,而其燃燒溫度亦到達例如 980°C以上,所產生之有害有機物分解氣體係完全燃燒,僅 釋出無害之燃燒氣體。此情況,燃燒溫度與爐内之環境溫度 (爐内溫度)之差係例如平均有200〜230°C,進行劇烈燃 燒’熱效率亦極南’可以卽省此源之方式進行無害化。 (實施例) 以下,舉出實施例及比較例’更具體地說明本發明’但只 要不超出本發明之要旨’則本發明並不限定於該等實施例。 以下’只要無特別限定,「份」係表示「質量份」,只要無特 098109858 20 200944717 別限'定’「%」係表示「質量%」 (實施例1) 〈廢棄物分散液之調製與對粒狀物之载持〉 將氳氧⑽4份溶解於水6份巾,對其添加含⑽ 物(以m含有PCB之絕緣油)4份、乙醇i份進行2 混合。其次’將小麥粉q於叙^ ς 1 見 』H 9f禮水51份現合,對其添加 (王子製紙公司製之「PAC」(銘量以Al2〇3換算為!。〜u 7份及爾、糖水驗6份,㈣加Μ於多孔性碳之竹户 12份’作為粒狀物,進行㈣混合。藉此,獲得將廢棄= 分散液載躲纽性碳之聽高黏㈣。以下將其 持體」。 ^ 〈熱處理〉 將上述所得之載持體於棒子内塞入堆積高度1〇〜15丽,插 人保持為爐内設定溫度(亦即置入前爐内溫度)綱。c之加 熱爐中。將棒子插人加熱爐㈣始丨分鐘後點火'點火後, 分解氣體在表面燃燒4分鐘。開始點火6分鐘後,表面氣體 之燃燒停止,得讀理廢棄物H爐岐度於置入時為 ⑼代小分鐘後為犯代小分鐘後為湖^分鐘後為 -9抓,4分鐘後為916。(:,5分鐘後為9肌。 燃:燒停止經過30秒後,從加熱爐取出熱處理後之物質(以 下稱為「耐熱性化合物」),使其恢復至常溫。之後,以研钵 予以粉碎,製成粉末。 098109858 21 200944717 〈評估〉 對所得之耐熱性化合物之粉末,以前述方法評估耐熱性 導電性及耐藥品性。又,PCB之含有量係以氣相色層=析' 行定量。 % [而才熱性評估] 外觀與質量之變化均未被觀察到。 [導電性之評估] 比電阻均為1(T6q · cm以下。 [耐藥品性之評估] 學反 不管對於何種藥品均無外觀之變化,亦不會進行化 應。 [PCB濃度測定] 未檢出(0. 0016mg/kg以下)殘留PCB量。 (實施例2) &lt;廢棄物分散液之調製與對粒狀物之载持〉 除了取代多孔性碳(竹炭)12份而添加下述含鋁化八物 A12份作為粒狀物之外,與實施例1同樣地獲得栽持體。 [含鋁化合物A] 將蔗糖25份加入水25份中,以50〇C加熱溶解,於其中 加入PAC (王子製紙公司製之「pAc」(鋁量以Aha換算為 1 (Ml%)) 50份,攪拌並均勻混合。以下,將如此獲得之水 溶液簡記為「XSP」。將xspi〇〇g以厚度2匪之方式裝入棒子 098109858 22 200944717 中,於2〇°C下靜置5小時後,對試料表面由燃燒器直接接 觸1300°C之火焰,進行熱處理。熱處理係於空氣中進行。 將K熱電偶溫度計外鞘放入試料之表面層附近所測定之溫 度為750〜880°C。從燃燒器接觸火焰開始後20分鐘後,獲 得完全均勻之黑色且為粒子狀之含鋁化合物。 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理。廢 〇 棄物經處理,獲得耐熱性化合物。 〈評估〉 對於所得之耐熱性化合物,以上述方法評估耐熱性、導電 性及耐藥品性。又,PCB之含有量係以氣相色層分析進行定 量0 [耐熱性評估] 外觀與質量之變化均未被觀察到。 ❿[導電性之評估] 比電阻均為10—6 Ω · cm以下。 [耐藥品性之評估] 不管對於何種藥品均無外觀之變化,亦不會進行化學反 應。 [PCB濃度測定] 未檢出(0· 〇〇16mg/kg以下)殘留PCB量。 (實施例3) 098109858 23 200944717 〈調配〉 除了取代添加多孔性碳12份而添加下述之含銘化合物被 覆,,、、機化。物A12份以外’與實施例丨同樣地獲得載持體。 〈含鋁化合物被覆無機化合物A&gt; 於不鐵鋼容器中襄入上述XSP1〇〇份,將厚度3醒之石綿 織物100份浸潰於其中。於2(rc下浸潰1〇小時後,拉起並 以重力使附著之多餘液體落下後,將浸透有XSp之石綿織物 水平置於不燃性片材上。由燃燒器對石綿織物之表面直接接 觸火焰進行煅燒。煅燒係於空氣中進行《將溫度計置入石綿 織物之下5mm的部分’測定接觸火焰正下方之溫度。以 1200°C加熱10分鐘,不進行熱溶融,獲得含鋁化合物被覆 無機化合物。 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理。廢 棄物經處理,獲得耐熱性化合物。 〈評估〉 對於所得之耐熱性化合物,以上述方法評估耐熱性、導電 性及耐藥品性。又,PCB之含有量係以氣相色層分析進行定 量。 [耐熱性評估] 外觀與質量之變化均未被觀察到。 [導電性之評估] 098109858 24 200944717 比電阻均為1(Γ6Ω · cm以下。 [财藥品性之評估] 不管對於何種藥品均無外觀之變化,亦不會進行化學反 應。 [PCB濃度測定] 未檢出(0.0016mg/kg以下)殘留PCB量。 (實施例4) 〇 &lt;廢棄物分散液之調製與對粒狀物之栽持〉 除了取代多孔性碳(竹炭)12份而添加稻殼與木屑之5〇% 混合物(來自植物之粒狀物)15份作為粒狀物之外,與實 施例1同樣地獲得載持體。 〈熱處理〉 將所得之戴持體以與實施例1同樣的條件進行熱處理。廢 棄物經處理,獲得耐熱性化合物。 ® 〈評估〉 對於所得之耐熱性化合物,以上述方法評估耐熱性、導電 性及耐藥品性。又,PCB之含有量係以氣相色層分析進行定 量。 [耐熱性評估] 外觀與質量之變化均未被觀察到。 [導電性之評估] 比電阻均為10—6Ω · cm以下。 098109858 25 200944717 [耐藥品性之評估] 不管對於何種藥品均無外觀之變化,亦不會進行化學反 應。 [PCB濃度測定] 未檢出(3mg/kg以下)殘留PCB量。 (實施例5) 〈廢棄物分散液之調製與對粒狀物之載持〉 除了取代氫氧化納4份而添加氩氧化斜5份之外,與實施 例1同樣地獲得載持體。 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理。廢 棄物經處理,獲得耐熱性化合物。 〈評估〉 對於所得之耐熱性化合物,以上述方法評估耐熱性、導電 性及财藥品性。又,PCB等之含氯化合物的含有量係以氣相 色層分析進行定量。 [而寸熱性評估] 外觀與質量之變化均未被觀察到。 [導電性之評估] 比電阻均為1(Γ6Ω · cm以下。 [耐藥品性之評估] 不管對於何種藥品均無外觀之變化,亦不會進行化學反 098109858 26 200944717 應。 [PCB濃度測定] 未檢出(0.0016rog/kg以下)殘留PCB量。 (實施例6) 〈廢棄物分散液之調製與對粒狀物之載持〉 於實施例1中,除了取代小麥粉9份而使用15%濃度水溶 太白粉60份(太白粉9份)’取代50%蔗糖水溶液6份而使 ❹ 用葡萄糖5份之外,與實施例1同樣地獲得栽持體。(另外, 由於醣類係於熱處理途中成為碳質物’因此與粒狀物同樣地 具有可有效果地吸附廢棄物並將其分解之機能。) 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理。廢 棄物經處理,獲得耐熱性化合物。 〈評估〉 ® 對於所得之耐熱性化合物,以上述方法評估耐熱性、導電 性及耐藥品性。又,PCB之含有量係以氣相色層分析進行定 量。 [对熱性評估] 外觀與質量之變化均未被觀察到。 [導電性之評估] 比電阻均為1 (Γ6Ω . cm以下。 [而f樂品性之評估] 098109858 27 200944717 不管對於何種藥品均無外觀之變化,亦不會進行化學反 應。 [PCB濃度測定] 未檢出(0. 0015mg/kg以下)殘留PCB量。 (實施例7) 〈廢棄物分散液之調製與對粒狀物之載持〉 於實施例1中,除了未添加乙醇以外,與實施例1同樣地 獲得載持體。雖熱分解性有稍微劣化,但仍順利獲得載持體。 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理。廢 棄物經處理,獲得财熱性化合物。 〈評估〉 對於所得之耐熱性化合物,以上述方法評估耐熱性、導電 性及耐藥品性。又,PCB之含有量係以氣相色層分析進行定 量。 [耐熱性評估] 外觀與質量之變化均未被觀察到。 [導電性之評估] 比電阻均為1(Γ6Ω · cm以下。 [耐藥品性之評估] 不管對於何種藥品均無外觀之變化,亦不會進行化學反 應。 098109858 28 200944717 [PCB濃度測定] 未檢出(0.0017mg/kg以下)殘留PCB量。 (實施例8) 〈廢棄物分散液之調製與對粒狀物之載持&gt; 於實施例1中,除了與氫氧化鈉水溶液、含PCB廢棄物及 乙醇I進步加入以月桂酸納作為主成分之粉末皂類5Things. The heat resistant compound can be used as a valuable product for various purposes. The invention also relates to "i thermal compounds" obtained by using the waste treatment method of the present invention. The appearance of the sputum resistance of the present invention, which is evaluated by the following evaluation method, is substantially not doubled, and the mass change is 0.3% by mass. 098109858 200944717. Further, the change in the mass of the heat resistant compound is also included in the vaporization due to adsorption of moisture. [Evaluation of heat resistance] 20 g of the powder of the heat-resistant compound obtained by the waste treatment method of the present invention or 20 g of the heat-resistant compound which is formed into a substantially cubic shape is placed in a furnace which substantially shields the air. Heated at 130 ITC for 24 hours to observe changes in appearance and quality.耐热 The heat resistant compound of the present invention is excellent not only in heat resistance but also in electrical conductivity and/or chemical resistance. When the conductivity is evaluated by the following evaluation method, the specific resistance can be 1 (Γ6 Ω·cm or less. Therefore, it is 'better than 〇6 Ω · cm or less. <Evaluation of Conductivity> The waste treatment using the present invention will be used. The heat-resistant compound obtained by the method is pulverized into a powder by a grind and inserted into a tube of acrylic resin having a diameter of φ 7 and a length of 200 mm, 5 times from a height of 2 cm. A DC voltage is applied to the top and bottom of the sample in the inlet tube, and the current value at 20 ° C is measured. The specific resistance of the powder plugged into the shape in the shape is calculated from the current value. Sexuality, when evaluated by the following evaluation method, no chemical reaction can be observed visually regardless of the drug. Therefore, regarding chemical resistance, it is preferred that no chemical is applied to any drug when evaluated by the following evaluation method. The (four) compound obtained by using the waste treatment method of the present invention is 098109858 19 200944717 l〇g is placed in a flask to add 1N (standard concentration) dilute sulfuric acid, 5 mass% of sodium oxide in the evening. , C, _, resting under the armpit, observing the presence or absence of a chemical reaction. In the waste treatment method of the present invention, when a PCB containing 18% of the content is used as waste, the PCB content in the obtained heat-resistant compound is gas. When the colorimetric layer analysis method is used for the quantification (analysis by the Chinese and foreign Techn〇s company), the quantitative lower limit value is 0. 0016 mg/kg or less. Therefore, the heat resistant compound of the present invention is preferably evaluated by the 耽 phase chromatography analysis. It is Q. Q 〇1 6 mg/kg or less. The waste treatment method according to the present invention does not cause harmful combustion gas action. The principle is not clear, but it can be considered as follows. However, the present invention is not limited to the following The range of effects, that is, the waste dispersion containing waste, polyaluminum chloride, alkaline substances, sugars, and water is carried on the granules, and heat treatment is performed only from gas-containing compounds. The harmful organic matter decomposition gas generated by the waste is surface-burned, and the combustion temperature thereof reaches, for example, 980 ° C or higher, and the harmful organic matter decomposition gas system generated is completely burned, and only the harmless combustion gas is released. In the case, the difference between the combustion temperature and the ambient temperature in the furnace (temperature in the furnace) is, for example, 200 to 230 ° C on average, and the violent combustion 'thermal efficiency is also extremely south' can be decontaminated in a manner that saves the source. In the following, the present invention will be described more specifically by way of Examples and Comparative Examples. However, the present invention is not limited to the embodiments as long as it does not deviate from the gist of the present invention. Indicates "mass parts" as long as there is no special 098109858 20 200944717. It is limited to 'fixed' and '%' means "% by mass" (Example 1) <Preparation of waste dispersion and loading of granular materials> (10) Four parts were dissolved in 6 parts of water, and 4 parts of (10) (insulating oil containing PCB) and 2 parts of ethanol were added and mixed. Next, 'when the wheat flour q is in the ^ ς 1 see 』 H 9f Lishui 51 copies, add it ("PAC" made by Oji Paper Co., Ltd. (The amount is converted to Al2〇3! 6 parts of sugar and syrup, and (4) 12 parts of bamboo house added to porous carbon as 'granules', and (4) mixing. Thereby, it is obtained that the waste will be discarded and the dispersion will be highly viscous (four). Hold the body. ^ <Heat treatment> The carrier obtained above is inserted into the rod at a height of 1 〇 to 15 liters, and the inserted person is kept at the set temperature in the furnace (that is, the temperature in the furnace before being placed). In the heating furnace of c. Insert the rod into the heating furnace (4) and start the ignition after ignition. After ignition, the decomposition gas is burned on the surface for 4 minutes. After the ignition is started for 6 minutes, the combustion of the surface gas is stopped, and the waste H furnace is read. When it is placed, it is (9) generation after a small minute, it is a small minute after the death. It is -9 for the lake after ^ minutes, and 916 for 4 minutes. (:, 9 minutes after 5 minutes. Burning: 30 seconds after burning stops After that, the heat-treated material (hereinafter referred to as "heat-resistant compound") is taken out from the heating furnace and returned to normal temperature. It is pulverized to obtain a powder. 098109858 21 200944717 <Evaluation> For the powder of the obtained heat-resistant compound, heat resistance and chemical resistance are evaluated by the above methods. Further, the content of the PCB is determined by gas phase chromatography. Quantitative. % [Thermal evaluation] The change in appearance and quality has not been observed. [Evaluation of conductivity] The specific resistance is 1 (T6q · cm or less. [Evaluation of drug resistance] There is no change in the appearance of the drug, and it will not be converted. [PCB concentration measurement] The amount of residual PCB (0. 0016mg/kg or less) is not detected. (Example 2) &lt;Preparation and pairing of waste dispersion The carrier of the granules was obtained in the same manner as in Example 1 except that 12 parts of the porous carbon (bamboo charcoal) was replaced by the following 12 parts of the aluminized arsenic A12. A] 25 parts of sucrose was added to 25 parts of water, and dissolved by heating at 50 ° C, and 50 parts of PAC ("AcAc" (amount of aluminum in 1% (Ml%)) manufactured by Oji Paper Co., Ltd. was added thereto, and stirred. Mix evenly. Hereinafter, the aqueous solution thus obtained is simply referred to as "XSP". Xspi〇〇g was placed in a rod of 098109858 22 200944717 in a thickness of 2 ,, and after standing at 2 ° C for 5 hours, the surface of the sample was directly contacted with a flame of 1300 ° C by a burner for heat treatment. The temperature of the outer surface of the K thermocouple thermometer placed near the surface layer of the sample was 750 to 880 ° C. After 20 minutes from the start of the flame contact with the burner, a completely uniform black color was obtained. Aluminum-containing compound. <Heat treatment> The obtained carrier was heat-treated under the same conditions as in Example 1. The waste material is treated to obtain a heat resistant compound. <Evaluation> With respect to the obtained heat resistant compound, heat resistance, electrical conductivity, and chemical resistance were evaluated by the above methods. Further, the content of the PCB was determined by gas chromatography chromatography. [Heat resistance evaluation] Changes in appearance and quality were not observed. ❿ [Evaluation of Conductivity] The specific resistance is 10-6 Ω · cm or less. [Evaluation of drug resistance] No chemical change is made regardless of the type of drug. [PCB concentration measurement] The amount of residual PCB was not detected (0·〇〇16 mg/kg or less). (Example 3) 098109858 23 200944717 <Preparation> In addition to the addition of 12 parts of porous carbon, the following compound containing the following compound was added, and it was machined. The carrier was obtained in the same manner as in Example 以外 except for the A12 portion. <Aluminum-containing compound-coated inorganic compound A> The XSP1 portion was placed in a non-ferrous steel container, and 100 parts of a stone wool fabric having a thickness of 3 was immersed therein. After immersing for 1 hour at 2 rc, pull up and drop the excess liquid by gravity, and place the asbestos fabric impregnated with XSp horizontally on the non-combustible sheet. The surface of the asbestos fabric is directly from the burner. The flame was calcined by contact with a flame. The calcination was carried out in air to "put the thermometer into a portion of 5 mm below the asbestos fabric" to measure the temperature directly under the contact flame. The mixture was heated at 1200 ° C for 10 minutes without thermal fusion to obtain an aluminum-containing compound coating. <The heat treatment> The obtained carrier was heat-treated under the same conditions as in Example 1. The waste was treated to obtain a heat-resistant compound. <Evaluation> The heat resistance of the obtained heat-resistant compound was evaluated by the above method. Conductivity and chemical resistance. Moreover, the content of PCB was quantified by gas chromatography. [Heat resistance evaluation] Changes in appearance and quality were not observed. [Evaluation of Conductivity] 098109858 24 200944717 Specific resistance Both are 1 (Γ6 Ω · cm or less. [Evaluation of the drug's properties] No chemical change is observed for any drug, and no chemical reaction will occur. Concentration measurement] The amount of residual PCB was not detected (0.0016 mg/kg or less). (Example 4) 〇 &lt;Preparation of waste dispersion and cultivation of granular matter> In addition to replacing 12 parts of porous carbon (bamboo charcoal) The carrier was obtained in the same manner as in Example 1 except that 15 parts of a mixture of rice hulls and wood chips (granular matter derived from plants) was added as a granular material. <Heat treatment> The obtained wearing body was The heat treatment was carried out under the same conditions as in Example 1. The waste was treated to obtain a heat-resistant compound. <Evaluation> For the heat-resistant compound obtained, heat resistance, electrical conductivity, and chemical resistance were evaluated by the above methods. It was quantified by gas chromatography. [Heat resistance evaluation] Changes in appearance and quality were not observed. [Evaluation of Conductivity] The specific resistance was 10-6 Ω · cm or less. 098109858 25 200944717 [Chemical resistance] Evaluation] No chemical reaction is observed regardless of the type of drug. [PCB concentration measurement] The amount of residual PCB (3 mg/kg or less) is not detected. (Example 5) <Waste dispersion Modulation and granularity The carrier was obtained in the same manner as in Example 1 except that the argon oxidation was added in 5 parts instead of 4 parts of sodium hydroxide. <Heat treatment> The obtained carrier was subjected to the same conditions as in Example 1. The heat treatment is carried out, and the waste is treated to obtain a heat-resistant compound. <Evaluation> The heat-resistant compound obtained is evaluated for heat resistance, conductivity, and chemical properties by the above method. Further, the content of the chlorine-containing compound such as PCB is Gas chromatographic analysis was performed for quantitative analysis. [Insulation evaluation] The change in appearance and quality was not observed. [Evaluation of Conductivity] The specific resistance was 1 (Γ6 Ω·cm or less). [Evaluation of drug resistance] No chemical change is made regardless of the type of drug, and no chemical reaction is required. 098109858 26 200944717 should be applied. [PCB concentration measurement] The amount of residual PCB (not less than 0.0016 rog/kg) was not detected. (Example 6) <Preparation of waste dispersion and support for granules> In Example 1, except for replacing 9 parts of wheat flour, 60 parts of 15% water-soluble white powder (9 parts of white powder) was used. A plant was obtained in the same manner as in Example 1 except that 6 parts of a 50% sucrose aqueous solution was replaced with 5 parts of glucose. (In addition, since the saccharide is a carbonaceous material in the middle of heat treatment, it has a function of adsorbing waste and decomposing it in a manner similar to the granular material.) <Heat treatment> The obtained carrier is in the same manner as the example. 1 Heat treatment was carried out under the same conditions. The waste is treated to obtain a heat resistant compound. <Evaluation> ® For the obtained heat-resistant compound, heat resistance, electrical conductivity, and chemical resistance were evaluated by the above methods. Also, the content of the PCB is quantified by gas chromatography. [Evaluation of heat] No changes in appearance and quality were observed. [Evaluation of Conductivity] The specific resistance is 1 (Γ6Ω·cm or less. [And the evaluation of the quality] 098109858 27 200944717 No chemical reaction is observed for any drug, no chemical reaction. Measurement] The amount of residual PCB (0. 0015 mg/kg or less) was not detected. (Example 7) <Preparation of waste dispersion and loading on granules> In Example 1, except that ethanol was not added, The carrier was obtained in the same manner as in Example 1. Although the thermal decomposition property was slightly deteriorated, the carrier was smoothly obtained. <Heat treatment> The obtained carrier was heat-treated under the same conditions as in Example 1. Treatment to obtain a heat-generating compound. <Evaluation> For the obtained heat-resistant compound, heat resistance, electrical conductivity, and chemical resistance were evaluated by the above methods. Further, the content of the PCB was quantified by gas chromatography. Evaluation] Changes in appearance and quality have not been observed. [Evaluation of Conductivity] The specific resistance is 1 (Γ6 Ω · cm or less. [Evaluation of Chemical Resistance] No change in appearance for any drug, nor Will progress 098109858 28 200944717 [Measurement of PCB concentration] The amount of residual PCB (0.0017 mg/kg or less) was not detected. (Example 8) <Preparation of waste dispersion and carrying of granules> In the examples In addition to the addition of sodium hydroxide solution, PCB-containing waste and ethanol I, powder soaps containing sodium laurate as a main component are added.

份以外’與實施例1同樣地獲得載持體。經由添加作為界面 活性劑讀末4類,乳化•熱分㈣急速進行 與空氣之接觸,於作業中變得容易抑制PCB之汽化,安2 提局。相較於實施例1,含PCB廢棄物之乳化更進一牛進: 分散性變佳,可街4 扎儿文進一步進行, &lt;熱處理 &gt; 更4良好地簡於粒狀物。 棄栽與實施例1同樣的條件進行熱處理喷 X停耐熱性化合物。 〈評估〉 對於所得之耐熱 性及耐藥品性。 人The carrier was obtained in the same manner as in Example 1 except for the portion. By adding 4 as the surfactant, the emulsification and the heat (4) are rapidly contacted with the air, which makes it easy to suppress the vaporization of the PCB during the operation, and the safety is improved. Compared with the first embodiment, the emulsification containing the PCB waste is further advanced: the dispersibility is better, and the street can be further carried out, &lt;heat treatment &gt; 4 is better in the form of granules. The heat treatment was carried out under the same conditions as in Example 1 to spray the heat-stopping compound. <Evaluation> For the heat resistance and chemical resistance obtained. people

量。 [耐熱性評估J 化均未被觀察到。 Q · cm以下。 外觀與質量之變 [導電性之評估] 比電阻均為10、6 098109858 29 200944717 * [耐藥品性之評估] 不管對於何種藥品均無外觀之變化,亦不會進行化學反 應。 [PCB濃度測定] 未檢出(0· 0015mg/kg以下)殘留PCB量。 (實施例9) 〈廢棄物分散液之調製與對粒狀物之載持〉 於實施例1中,除了取代含PCB廢棄物4份而添加三氯乙 烯4份以外,與實施例1同樣地獲得載持體。 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理。廢 棄物經處理,獲得对熱性化合物。 〈評估〉 對於所得之耐熱性化合物,以上述方法評估耐熱性、導電 性及耐藥品性。又,三氯乙烯之含有量係以氣相色層分析進 行定量。 [耐熱性評估] 外觀與質量之變化均未被觀察到。 [導電性之評估] 比電阻均為10_6Ω · cm以下。 [耐藥品性之評估] 不管對於何種藥品均無外觀之變化,亦不會進行化學反 098109858 30 200944717 ’ 應。 [三氯乙烯濃度測定] 未檢出(0. 001mg/kg以下)殘留三氯乙烯量。 (實施例10) 龜 〈廢棄物分散液之調製與對粒狀物之載持〉 i. 於實施例1中,除了取代含PCB廢棄物4份而添加氯化苯 10份、選礦排土懸濁沉澱粒子20份、木屑10份以外,與 ❹ 實施例1同樣地獲得載持體。 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理。廢 棄物經處理,獲得财熱性化合物。 〈評估〉 對於所得之耐熱性化合物,以上述方法評估耐熱性、導電 性及财藥品性。 ❿[耐熱性評估] 外觀與質量之變化均未被觀察到。 [導電性之評估] 比電阻均為10—6Ω · cm以下。 [耐藥品性之評估] 不管對於何種藥品均無外觀之變化,亦不會進行化學反 應。 (比較例1) 098109858 31 200944717 〈廢棄物分散液之調製與對粒狀物之載持〉 於實施例1中,除了未添加多氣化鋁以外,欲與實施例j 同樣獲得載持體,但乳化與熱分解均未進行,液體與固體之 融合容易變得不佳,確認有殘留分離液。該殘留分離液明顯 為 PCB。 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理,結the amount. [Heat resistance evaluation was not observed. Q · cm or less. Appearance and quality change [Evaluation of conductivity] Specific resistance is 10,6 098,109,858 29 200944717 * [Evaluation of chemical resistance] No chemical change is observed for any drug. [PCB concentration measurement] The amount of residual PCB (0. 0015 mg/kg or less) was not detected. (Example 9) <Preparation of waste dispersion and carrying of granules> In the same manner as in Example 1, except that 4 parts of trichloroethylene were added instead of 4 parts of PCB-containing waste. Obtain the carrier. <Heat Treatment> The obtained carrier was heat-treated under the same conditions as in Example 1. The waste is treated to obtain a thermophilic compound. <Evaluation> With respect to the obtained heat resistant compound, heat resistance, electrical conductivity, and chemical resistance were evaluated by the above methods. Further, the content of trichloroethylene was quantified by gas chromatography. [Heat resistance evaluation] Changes in appearance and quality were not observed. [Evaluation of Conductivity] The specific resistance is 10_6 Ω · cm or less. [Evaluation of drug resistance] No chemical change is made regardless of the type of drug, and no chemical reaction is required. 098109858 30 200944717 ' [Measurement of Trichloroethylene Concentration] The amount of residual trichloroethylene was not detected (0. 001 mg/kg or less). (Example 10) Turtle <Preparation of waste dispersion and loading on granules> i. In Example 1, except for replacing 4 parts of PCB waste, 10 parts of chlorinated benzene was added, and the ore dressing was suspended. The carrier was obtained in the same manner as in Example 1 except that 20 parts of turbid precipitated particles and 10 parts of wood chips were used. <Heat Treatment> The obtained carrier was heat-treated under the same conditions as in Example 1. The waste is treated to obtain a fatty compound. <Evaluation> With respect to the obtained heat resistant compound, heat resistance, electrical conductivity, and chemical property were evaluated by the above methods. ❿ [Heat resistance evaluation] Changes in appearance and quality were not observed. [Evaluation of Conductivity] The specific resistance is 10-6 Ω · cm or less. [Evaluation of drug resistance] No chemical change is made regardless of the type of drug. (Comparative Example 1) 098109858 31 200944717 <Preparation of Waste Dispersion and Loading of Granular Materials> In Example 1, a carrier was obtained in the same manner as in Example j except that no polyaluminized aluminum was added. However, neither the emulsification nor the thermal decomposition proceeded, and the fusion of the liquid and the solid was liable to be inferior, and the residual separation liquid was confirmed. The residual separation liquid is clearly a PCB. <Heat Treatment> The obtained carrier was heat-treated under the same conditions as in Example 1 to form a knot.

果發生黑煙並爆炸性地燃燒。因廢棄物分散液之燃燒,無法If black smoke occurs and it burns explosively. Unable to burn due to waste dispersion

確認爐内溫度之上升,推定爐内設定溫度為75(rc〜78〇t:M 内。此溫度區域中,廢棄物中之含氯化合物並未完全分解, 有產生戴奥辛類之虞。最後,廢棄物消失並被燃燒,僅獲得 灰分。 〈評估〉 [耐熱性評估][導電性之評估][耐藥 測定] 品性之評估][PCB濃度After confirming the increase in the temperature inside the furnace, it is estimated that the set temperature in the furnace is 75 (rc~78〇t: M. In this temperature range, the chlorine-containing compound in the waste is not completely decomposed, and there is a dioxin-like state. Finally, The waste disappears and is burned, and only ash is obtained. <Evaluation> [Heat resistance evaluation] [Evaluation of conductivity] [Resistance determination] Evaluation of character] [PCB concentration

由於熱處理後已灰化,故無法獲得耐熱性化合物。耐熱 性、導電性、耐藥品性、PCB濃度均無法評估。 (比較例2) 〈廢棄物分散液之調製與對粒狀物之载持〉 _^施例1中除了未添加氫氧化納以外,欲與實施例1 ::獲得載持體,但含PCB廢棄物對於「pAc、乙醇及水」 ,、以分散。發生液相分離,因此未順利進行對粒狀物之載 098109858 32 200944717 持。又,由於未發熱,故作業緩慢。又,亦有溶劑於大氣中 之揮發揮散、乳化與熱分解性不良之問題。 〈熱處理〉 將所得之載持體以與實施例1同樣的條件進行熱處理。 PCB未乳化而發生液相分離,故廢棄物燃燒而產生有害燃燒 氣體。 (比較例3) ❿〈廢棄物分散液之調製與對粒狀物之載持〉 於實施例1中,除了未添加小麥粉與蔗糖(亦即,未加入 醣類)以外,欲與實施例1同樣獲得載持體,但雖會吸收殘 留分離液(幾乎全部為PCB)卻不充分,熱分解性不佳,故 未增黏,完全無法期待因被覆效果所帶來的PCB揮發之防 止。 上述實施例及比較例之配方係示於下表1。 ❹ 098109858 33 200944717 〔1&lt;〕 粒狀物 (1)碳質物:竹炭12份 (2)含鋁化合物:12份 (3)含鋁化合物被覆無機化合物:12份 (4)來自植物之粒狀物:稻殼+木屑15份 (1)碳質物:竹炭12份 (1)碳質物:竹炭12份 (1)碳質物:竹炭12份 (1)碳質物:竹炭12份 ’ (1)碳質物:竹炭12份 (1)碳質物:竹炭12份 (1)碳質物:竹炭12份 (1)碳質物:竹炭12份 (1)碳質物:竹炭12份 界面活性劑 41 碟 月桂酸鈉皂5份 磯 醇類 乙醇1份 乙醇1份 乙醇1份 乙醇1份 乙醇1份 乙醇1份 乙醇1份 乙醇1份 乙醇1份 乙醇1份 乙醇1份 乙醇1份 醣類 傘CO ΟΪ挺 龕紱 七窭 傘CO ΟΪ赵 燊紱 七窭 小麥粉9份 蔗糖水溶液6份 小麥粉9份 蔗糖水溶液6份 小麥粉9份 蔗糖水溶液6份 cr&gt; in 条窭 « 或¥ 小麥粉9份 蔗糖水溶液6份i 小麥粉9份 嚴糖水溶液6份: 小麥粉9份 蔗糖水溶液6份 傘CO CT&gt;挺 条妫 4« 七窭 傘CO 05赵 龕钕 七窭 驗性物質 氫氧化納4份 氫氧化納4份 氫氧化鈉4份 氫氧化納4份 氫氧化鉀5份 氫氧化鈉4份 氫氧化納4份 氫氧化納4份 氫氧化鈉4份 氫氧化納4份 -1 氫氧化納4份 氫氧化鈉4份 〇 £ 7份 7份 7份 7份 7份 7份 7份1 7份 7份 7份 7份 7份 廢棄物 ^ PCB 4 份 PCB 4 份 PCB 4 份 PCB 4 份 PCB 4 份 i PCB 4 份 1 PCB 4 份 1 PCB 4 份 ! 三氯乙稀4份 氣化苯10份 選礦排土懸濁沉澱粒子20份I 木屑10份 PCB 4 份 PCB 4 份 PCB 4 份 ^0 實施例1 實施例2 實施例3 實施例4 實施例5 實施例6 實施例7 實施例8 實施例9 實施例10 -1 比較例1 比較例2 比較例3 ο ο 8-601860 200944717 實施例中均可良好地處理 等有 、㈣物°此時’並未發生戴奥辛 ㈣。又’如上述評估結果所明顯得知,本發明之實 包例句未檢測出殘留pcB, 埶性、導 Χ廢棄物,喊_,可獲得耐 丄導電性、耐樂品性均優異之「耐熱性化合物」。 方面,比較例1中,無法獲得耐熱性化合物僅 二飛2中則由於乳化與熱分解不佳而有殘_ ❹ ❷ ΡΓ… 較例3中同樣因為熱分解性不佳,有殘留 PCB揮發飛散之虞。 ㈣屬殘留 (產業上之可利用性) 物=:=方法係—氣廢棄 至環境tn賴廢棄物㈣ 仃夕之廢棄物處理方法,並且可古 政活用所得之結果物,且了有 又,使用本發明之廢棄物處理:、=物處理之. 由於耐熱性、難燃性、=方::敝耐熱 :=屏蔽物、導電_、不燃碳、繼= ==機金屬代替物、活性碳、有害物質吸附材、 ㈣、橡膠1強Γ抗紫外線劑、顏料、C/C組合超耐熱過 處:_補強材、石綿耐熱提升劑、土壤改良材等。 本案係以2008年3月27曰所申性夕n 士由 2008-084977 ^ ^ ^ 明之日本專利申請案特願 -084277為基礎,該_之内容全咖至此,寫入 於本案發明之說明書巾作為揭㈣容。 ‘· 098109858 35Since it was ashed after the heat treatment, a heat resistant compound could not be obtained. Heat resistance, electrical conductivity, chemical resistance, and PCB concentration were not evaluated. (Comparative Example 2) <Preparation of Waste Dispersion and Loading of Granular Material> In Example 1, except that sodium hydroxide was not added, the carrier was obtained in the same manner as in Example 1: The waste is dispersed in "pAc, ethanol and water". Liquid phase separation occurred, so the loading of the granules was not carried out smoothly. 098109858 32 200944717. Moreover, since there is no heat, the work is slow. Further, there is also a problem that the solvent is dispersed in the atmosphere, and the dispersion, emulsification, and thermal decomposition are poor. <Heat Treatment> The obtained carrier was heat-treated under the same conditions as in Example 1. The PCB is not emulsified and liquid phase separation occurs, so the waste burns to produce harmful combustion gases. (Comparative Example 3) 调制 <Preparation of waste dispersion and support for granules> In Example 1, except that wheat flour and sucrose were not added (that is, no saccharide was added), (1) Although the carrier is obtained in the same manner, the residual separation liquid (almost all of which is PCB) is insufficient, and the thermal decomposition property is not good, so that the viscosity is not increased, and the prevention of PCB volatilization due to the coating effect cannot be expected at all. The formulations of the above examples and comparative examples are shown in Table 1 below. 098 098109858 33 200944717 [1&lt;] granules (1) carbonaceous material: 12 parts of bamboo charcoal (2) aluminum-containing compound: 12 parts (3) aluminum-containing compound coated inorganic compound: 12 parts (4) granules derived from plants : Rice husk + wood chips 15 parts (1) Carbonaceous material: 12 parts of bamboo charcoal (1) Carbonaceous material: 12 parts of bamboo charcoal (1) Carbonaceous material: 12 parts of bamboo charcoal (1) Carbonaceous material: 12 parts of bamboo charcoal ' (1) Carbonaceous material: 12 parts of bamboo charcoal (1) Carbonaceous material: 12 parts of bamboo charcoal (1) Carbonaceous material: 12 parts of bamboo charcoal (1) Carbonaceous material: 12 parts of bamboo charcoal (1) Carbonaceous material: 12 parts of bamboo charcoal surfactant 41 dish of sodium laurate soap 5 parts Alcohol alcohol 1 part ethanol 1 part ethanol 1 part ethanol 1 part ethanol 1 part ethanol 1 part ethanol 1 part ethanol 1 part ethanol 1 part ethanol 1 part ethanol 1 part ethanol 1 part sugar umbrella CO ΟΪ pretty 龛绂 seven umbrella CO ΟΪ 燊绂 燊绂 燊绂 窭 窭 窭 窭 窭 9 9 9 9 9 9 9 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 蔗糖 in in in in in in in in in in in in in in in in in in in in in 6 parts of strict sugar aqueous solution: wheat flour 9 parts sucrose aqueous solution 6 parts umbrella CO CT> 挺条妫4« 七窭伞CO 05赵龛钕七窭Detective substance sodium hydroxide 4 parts sodium hydroxide 4 parts sodium hydroxide 4 parts sodium hydroxide 4 parts potassium hydroxide 5 parts sodium hydroxide 4 parts sodium hydroxide 4 parts sodium hydroxide 4 parts sodium hydroxide 4 parts hydroxide 4 parts - 1 sodium hydroxide 4 parts sodium hydroxide 4 parts 7 7 parts 7 parts 7 parts 7 parts 7 parts 7 parts 7 parts 1 7 parts 7 parts 7 parts 7 parts 7 parts waste ^ PCB 4 parts PCB 4 PCB 4 parts PCB 4 parts PCB 4 parts i PCB 4 parts 1 PCB 4 parts 1 PCB 4 parts! Trichloroethylene 4 parts gasified benzene 10 parts dressing soil suspended sediment particles 20 parts I wood chips 10 parts PCB 4 parts PCB 4 parts PCB 4 parts ^1 Example 1 Example 2 Example 3 Example 4 Example 5 Example 6 Example 7 Example 8 Example 9 Example 10 -1 Comparative Example 1 Comparative Example 2 Comparative Example 3 ο 8-601860 200944717 In the examples, it is possible to treat well, etc. (4) At this time, 'Dioxin (4) does not occur. Further, as apparent from the above evaluation results, the actual example of the present invention does not detect residual pcB, sputum, lead waste, shouting _, and can obtain excellent heat resistance and resistance to sputum. Compound." On the other hand, in Comparative Example 1, the heat-resistant compound could not be obtained only in the case of the second fly 2, and the residue was poor due to poor emulsification and thermal decomposition. _ ❹ ❷ ... The same as in the case of Example 3, the residual PCB was scattered due to poor thermal decomposition property. After that. (4) Residues (industrial availability) Substance =:=Methods--------------------------------------------------------------------------------------------------------------------------------------- Use of the waste treatment of the present invention: = treatment of materials. Due to heat resistance, flame retardancy, = square:: heat resistance: = shield, conductive _, non-combustible carbon, followed = = = machine metal substitute, activated carbon , harmful substances adsorption materials, (four), rubber 1 strong anti-UV agent, pigment, C / C combination of super heat-resistant places: _ reinforcing materials, asbestos heat-resistant enhancers, soil improvement materials. This case is based on the Japanese Patent Application No. 084277 of the 2008-084977 ^ ^ ^ Ming, which was written on March 27, 2008. The contents of this _ are all here, and are written in the specification of the invention. As a cover (four) capacity. ‘· 098109858 35

Claims (1)

200944717 七、申請專利範圍: 1. 一 種廢棄物處理方法,其特徵為將至少含有廢棄物、多 氣德、驗性物f、醣織权廢棄物分讀_於粒狀物 後,進行熱處理 2. 如申,專利範圍第i項之廢棄物處理方法,其中,上述 廢棄物分散液錢體廢棄物之乳化分散液。、 3. 如申請專利第丨項之廢棄物處理方法,其中,上述 廢棄物分散液係固體廢棄物之個體分散液。 、4.如申請專利範圍第1至3項中任一項之廢棄物處理方 法,其中,上述廢棄物為含氯化合物。 5.如申請專利範圍第4項之廢棄物處理方法,其中,上述 含氯化合物為多氯聯苯(PCB)。 6·如申請專利範圍第!至5項中任—項之廢棄物處理方 法’其中,上述粒狀物為碳質物。 7.如申請專利範圍第1至5項巾任—項之廢棄物處理方 法,其中,上述粒狀物係將含有多氣化鋁及有機物之水系分 散液予以锻燒而成之含銘化合物。 8·如申請專利範圍第!至5項中任一項之廢棄物處理方 法,其中,上述粒狀物為對無機粒子含浸含有多氯化鋁及有 機物之水溶液並予以锻燒而成之含鋁化合物被覆無機化合 物。 9.如申請專利範圍第1至5項中任一項之廢棄物處理方 098109858 36 200944717 法’其中’上述粒狀物為來自植物之粒狀物。 10.如申請專利範圍第項中任一項之廢棄物處理方 法,其中,上述醣類為殿粉類。 lh如申請專利範圍第⑴G項中任-項之廢棄物處理方 , 法,其中,上述廢棄物分散液係進一步含有醇類。 、12.如申請專·圍第⑴丨項中任—項之廢棄物處理方 法’其中’上述廢棄物分散液係進—步含有界面活性劑。 ❿13.如巾料·圍第1至12射任—項之廢棄物處理方 法,其中,上述熱處理係於爐内環境溫度6〇〇〜28〇〇。匸之加 熱爐中進行。 14. 如申請專利範圍第丨至12項中任—項之廢棄物處理方 法,其中,藉由上述熱處理,使燃燒溫度成為9〇(rc以上。 15. 種耐熱性化合物,其係使用申請專利範圍第1至14 項中任一項之廢棄物處理方法而獲得。 ® 16.種耐熱性化合物之製造方法,係用以製造申請專利 範圍第15項之耐熱性化合物,其係使用申請專利範圍第i 至14項中任一項之廢棄物處理方法。 098109858 37 200944717 四、指定代表圖: (一) 本案指定代表圖為:無 (二) 本代表圖之元件符號簡單說明: 無 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: 無 098109858 2200944717 VII. Scope of application for patents: 1. A waste disposal method characterized in that at least waste, multi-virtuality, test substance f, and sugar weaving waste are read-by-granular, and heat treatment is performed 2 The invention relates to a waste disposal method according to item ith of the patent scope, wherein the waste dispersion liquid is an emulsified dispersion of the body waste. 3. The waste disposal method according to the application of the patent item, wherein the waste dispersion is an individual dispersion of solid waste. 4. The waste disposal method according to any one of claims 1 to 3, wherein the waste is a chlorine-containing compound. 5. The waste disposal method according to item 4 of the patent application, wherein the chlorine-containing compound is polychlorinated biphenyl (PCB). 6. If you apply for a patent scope! The waste treatment method of any one of the five items, wherein the granular material is a carbonaceous material. 7. The waste disposal method according to any one of claims 1 to 5, wherein the granular material is a compound containing a water-based dispersion containing a plurality of vaporized aluminum and an organic substance. 8. If you apply for a patent scope! The waste treatment method according to any one of the items 5, wherein the granular material is an inorganic compound-coated inorganic compound obtained by impregnating inorganic particles with an aqueous solution containing polyaluminum chloride and an organic substance and calcining the aluminum compound. 9. The waste disposal party according to any one of claims 1 to 5, wherein the above-mentioned granules are granules derived from plants. 10. The waste disposal method according to any one of the preceding claims, wherein the saccharide is a temple powder. Lh The waste disposal method according to any one of the items (1)G of the patent application, wherein the waste dispersion further contains an alcohol. 12. The waste disposal method of the application of the above-mentioned item (1), wherein the above-mentioned waste dispersion further contains a surfactant. ❿ 13. For the waste material treatment method of the towel material, the first to the 12th, the heat treatment is performed in the furnace at an ambient temperature of 6 〇〇 28 〇〇. It is carried out in a heating furnace. 14. The waste disposal method according to any one of the above-mentioned claims, wherein the combustion temperature is 9 〇 or more by the above heat treatment. 15. The heat-resistant compound is used for patent application. It is obtained by the waste treatment method according to any one of the items 1 to 14. The method for producing a heat-resistant compound is a method for producing a heat-resistant compound of claim 15 which is a patent application scope. Waste disposal method according to any one of items i to 14. 098109858 37 200944717 IV. Designation of representative drawings: (1) The representative representative of the case is: No (2) Simple description of the symbol of the representative figure: No. 5, the case If there is a chemical formula, please reveal the chemical formula that best shows the characteristics of the invention: No. 098109858 2
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