TW414721B - Treating agent for packet solidification of wastes and the purification method of waste treatment - Google Patents

Treating agent for packet solidification of wastes and the purification method of waste treatment Download PDF

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Publication number
TW414721B
TW414721B TW088100218A TW88100218A TW414721B TW 414721 B TW414721 B TW 414721B TW 088100218 A TW088100218 A TW 088100218A TW 88100218 A TW88100218 A TW 88100218A TW 414721 B TW414721 B TW 414721B
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Taiwan
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waste
film
black smoke
patent application
inorganic compound
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TW088100218A
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Chinese (zh)
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Katsuhiro Kokuta
Naoto Kokuta
Hideaki Uchida
Kenji Kokuta
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Kokuta Hiroshi
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/14Disinfection, sterilisation or deodorisation of air using sprayed or atomised substances including air-liquid contact processes
    • A61L9/145Disinfection, sterilisation or deodorisation of air using sprayed or atomised substances including air-liquid contact processes air-liquid contact processes, e.g. scrubbing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/005Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by heat treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/64Heavy metals or compounds thereof, e.g. mercury
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/75Multi-step processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact

Abstract

A method for packet solidification of wastes including harmful gases of black smoke or foul heavy metals or flying ashes, or bottom ashes at the bottom of an incinerator, etc., comprises to make the combustion gas of the wastes contact to an aqueous film-making inorganic compound of silane and silanolic salt, thereby generating a film-making expansion foam and a combustion residue capable of containing the black smoke or smell, harmful gas and heavy metal, and meanwhile sealing these harmful materials inside. The present invention also relates to a treating agent for packet solidification which is used in this method. The treating agent is an aqueous film-making inorganic compound formed of silane and silanolic salt.

Description

> 414721 ;五、發明說明π) ! 【發明說明】: i : 本發明係關於廢棄物之包固處理劑及使用此劑之廢棄 j i物之淨化處理方法,尤關於一種對含黑煙或惡臭與重金 | i屬、飛灰之有害氣體及堆積在焚化裝置底部之底灰等之廢 :棄物施以淨化處理之處理劑及其淨化處理方法u I 生活環境中之廢棄物,在燃燒之際1當會產生黑煙或 :惡臭,而拋棄之焚化灰渣、或排出之飛灰所含有害重金屬 之溶出公害,在歐洲已被嚴定排放標準之戴奥辛排放方 :面,現皆已有嚴格之規定。 現今處理廢棄物之焚化方法,在政策指導之下,已有 i .' 丨由批次式運轉之中小型焚化爐轉換至連續式運轉之大型焚 | :化爐焚化法之趨勢。然而,由於上述之排放規定,至使營 丨 丨運中小型爐之地方自治團體或中間廢棄物處理業者,被迫 ί 1 ; 必須投入高額之設備改善費用,或放棄廢棄物處理事業。 本發明之目的即為解決此現實問題,而提供一種新穎的淨 化處理物質及其淨化處理方法= 廢棄物若含重金屬或CL成份,則於有機物燃燒時,該>414721; V. Description of the invention π)! [Explanation of the invention]: i: This invention relates to a packaging treatment agent for waste and a method for purifying waste materials using the agent, especially a method for treating black smoke or Foul odor and heavy gold | I, hazardous gases of fly ash, bottom ash deposited on the bottom of incineration equipment, etc .: The waste is treated with purification treatment and its purification method u I Waste in the living environment is burning On the occasion, 1 will produce black smoke or: foul odor, and the dissolution of hazardous heavy metals contained in discarded incineration ash or discharged fly ash will have a strict emission standard in Europe. There are strict rules. Today's waste incineration methods, under the guidance of policies, have been transformed from batch-type small and medium-sized incinerators to continuous-type large-scale incinerators. However, due to the above-mentioned emission regulations, local autonomous organizations or intermediate waste disposal operators that transport small and medium-sized furnaces have been forced to do so; they must invest high equipment improvement costs or abandon the waste treatment business. The purpose of the present invention is to solve this practical problem, and provide a novel purification treatment substance and its purification treatment method. If the waste contains heavy metals or CL components, the

I 等成份將成為有害氣體之戴奥辛之前驅物。再者,在排氣 :流往排氣處理之最終工程之非耐高熱性之袋濾器途中,即 :使施以冷卻處理或洗滌處理,依然有戴奥辛之產生,其間 ;雖可以無機物或礦物予以吸著處理,但又須再處理其殘渣 i物或吸著劑,是以在完全處理上,必須使用複雜之處理技 丨術及南額之設備。 | 焚化殘渣之底灰殘存有公害之重金屬,以往係使用螯Ingredients such as I will be the precursors of dioxin for harmful gases. In addition, in the exhaust: the non-high heat resistant bag filter flowing to the final process of the exhaust treatment, that is, the cooling or washing treatment, the dioxin is still produced, in the meantime, although it can be inorganic or mineral Adsorption treatment, but its residues or sorbents must be treated again, in order to complete the treatment, complex processing techniques and equipment must be used. Contaminated heavy metals remain in the bottom ash of incineration residues.

第4頁 414721 i .................................................' .................................—.................... i I五、發明說明(2) 丨 I合劑予以處理,或運至特定管理之掩埋場予以投棄處理,| 但就長期安定性而言,其安全性仍有間題,尤其在飛灰方 - 面,重金屬及戴奥辛等係濃縮殘存其内,以螯合劑處理仍 具困難。 ' i 再者,在小型焚化爐方面,其焚化產生之黑煙或惡臭Page 4 414721 i ............... .... '.................................--.......... ......... i I. Description of the invention (2) 丨 I mixture is disposed of, or it is transported to a landfill with specific management for disposal, | but in terms of long-term stability, its safety is still However, especially in fly ash, heavy metals and dioxin are concentrated and remain in it, and it is still difficult to treat with chelating agents. 'i Furthermore, in the case of small incinerators, the black smoke or foul odor produced by the incineration

1 I 將會影響周邊居民,而設有可解決此問題之設備的焚化爐 之價格又極昂貴,因此急待找出一簡單價廉之解決方法。 如欲達到環保署之對戴奥辛、其他氣體或重金屬等之i -規定值要求,則舊有焚化裝置之改造費用將極高昂,焚化 營運亦將被迫停止,而完全處理法之各種溶融爐又須巨額 |之造價,亦將增加居民之環保負擔費用。 按焚化爐之排氣為200 °C〜800 °C之高溫,在此高溫之 下,尚未見有能將黑煙及惡臭予以過濾之有機物式過濾 器,遂須施以冷卻處理或洗滌處理,或其他之各種構造之 處理,或以陶瓷觸媒或吸著体予以處理並冷卻,再送往袋 式集塵器進行過濾者,但因此等裝置價格極高,遂期待有 | 一種不需後處理之可耐高溫之無機過濾器或吸著材被開 發,本發明即為解決此問題而開發者。 , 以往對於含有已知重金屬之底灰或飛灰之處理法,已 有以有機物之如氨基甲酸之螯合劑予以混合之處理法,該 法雖已廣泛被使用,但螯合法安定與否,在化學上尚難以 評斷,是以對重金屬施以在化學上安定之離子結合之方法 I甚有必要。 歐洲在甚早之前便已對戴奥辛採取防制對策,及至近 -1 I will affect the surrounding residents, and the cost of incinerators with equipment to solve this problem is extremely expensive, so it is urgent to find a simple and cheap solution. If you want to meet the EPA ’s i-rated requirements for dioxin, other gases, or heavy metals, the cost of retrofitting the old incineration plant will be extremely high, and the incineration operation will be forced to stop. The huge cost will also increase the environmental protection burden of residents. According to the exhaust gas of the incinerator is a high temperature of 200 ° C ~ 800 ° C, under this high temperature, no organic matter filter that can filter black smoke and foul odor has been seen, so it must be cooled or washed. Or other various structure treatments, or ceramic catalysts or sorbents for treatment and cooling, and then sent to the bag dust collector for filtering, but because the device is extremely expensive, I look forward to | The treated inorganic filter or absorbing material capable of withstanding high temperature is developed, and the present invention is developed by the present invention to solve this problem. In the past, for the treatment method of bottom ash or fly ash containing known heavy metals, there has been a treatment method of mixing organic substances such as carbamic acid chelating agents. Although this method has been widely used, the chelation is stable or not. It is difficult to judge chemically, and the method I of applying chemically stable ion bonding to heavy metals is necessary. Europe has taken countermeasures against dioxin long before, and as recently as-

第5頁 Λ ^ /ί Γ? 1 ..上......................................................................................................................... _·.··..— 五、發明說明(3) 年來仍以排氣冷卻法為其主流,但依最近之研究觀之,其 為戴奥辛前驅物之HCL於低溫時即會產生戴奥辛,為了解 決此問題,以在4 5 0 °C以上高溫下可使用之活性碳或生石 |灰做為吸著劑之吸著法乃被採用,但是此吸著劑之後處理 又成為新問題,而即使如此仍必需使用袋濾器,且須將殘 丨存於袋濾器之含重金屬之飛灰施以洗滌之處理=即,排氣 i處理當然除了須有對含戴奥辛前驅物及氯化鐵或重金屬之 I飛灰處理,也須有將對戴奥辛前驅物有分解作用之觸媒或 i公害物予以吸著之袋濾器,而欲再使用此袋濾器時,又須 要加以後續之處理。 本發明旨在解決上述之問題而開發者。當使用本發明 丨時,即使使用批次式運轉之中小型爐,被認為最難清除之 i戴奥辛規定值,亦可容易達成,且裝置成本或舊爐改造之 ! 丨費用及居民之環保負擔等皆可減輕,另外尚可廣範應用於 其他產業上。 ! 本發明人前曾揭示有「水性造膜性無機化合物之製造Page 5 Λ ^ / ί Γ? 1 .. .............................. ........................................ .................................. _ ·. ·· ..— V. Description of Invention (3) Years The exhaust cooling method is still the mainstream, but according to recent research, the HCL, which is a precursor of dioxin, will produce dioxin at low temperatures. In order to solve this problem, it can be used at high temperatures above 450 ° C. Activated carbon or raw stone | ash is used as the sorbent adsorption method, but this sorbent after treatment has become a new problem, and even then a bag filter must be used, and the residue must be stored in the bag filter The heavy metal-containing fly ash is subjected to a washing treatment = that is, the exhaust gas i treatment must, of course, not only have to deal with dioxin precursors and ferric chloride or heavy metal I fly ash, but also have to decompose the dioxin precursors. The bag filter to which the catalyst or i public pollutants are adsorbed, and when this bag filter is to be used again, it must be treated subsequently. The present invention was developed by a developer aiming at solving the above-mentioned problems. When the present invention is used, even if the batch-type operation of small and medium-sized furnaces is used, the specified value of iDioxine, which is considered to be the most difficult to remove, can be easily achieved, and the cost of the equipment or the transformation of the old furnace! 丨 Costs and environmental protection burden of residents Can be alleviated, but also can be widely used in other industries. ! The inventor has previously disclosed "Production of water-based film-forming inorganic compounds

II

丨法」(g本專利特許第2028203號及特公平7-14801號),| 1 「防災、防火 '耐火複合材」(日本專利特許第2015694 I i 號)等,以下皆總稱為前發明矽烷醇鹽液。按該前發明矽 | 烷醇鹽液係使用甲基矽與硼砂或氟化鈉、亞礦酸或其鹽類 丨及驗金屬(Na, K, LI),由固體及漢厚驗溶液反應而製 I造,其不同於水玻璃,係由矽氧烷及矽烷醇鹽所構成。 I 第一圖至第四圖乃示本發明使用之水性造膜性無機化 |合物LC之耐熱無機物,以分別於20t、50°C、550°C及950丨 Law "(G Patent Patent No. 2028203 and Special Fair No. 7-14801), | 1" Disaster prevention and fire-resistant 'fire-resistant composite materials' (Japanese Patent License No. 2015694 I i), etc., are collectively referred to below as the pre-invented silanes Alkoxide solution. According to the previous invention, the silicon | alkoxide solution uses methyl silicon and borax or sodium fluoride, sub-mineral acid or its salts and test metals (Na, K, LI). It is made of silicon, which is different from water glass and is composed of siloxane and alkoxide. I The first to fourth figures show the heat-resistant inorganic compounds of the aqueous film-forming inorganic compound LC used in the present invention at 20t, 50 ° C, 550 ° C, and 950, respectively.

第6頁 414721 I五 '發明說明(4) ——" ............................................ °C時之FTIR分析,顯示水分子尖峰會由於加熱而變低並造 膜之示意圖。又於第一圖至第四圖中,以橫軸表示波數 (Wave Numbers)及縱轴表示吸光度(Abs〇rvance)。此 由東麗研究中心之分析報告’係以第一圖至第四圖之FTIR j分析,表示於780cni-l時矽氧烷之存在及於9⑽,i〇〇〇24〇〇 〜3800cm 1時矽烷醇之存在。本發明矽烷醇鹽液縱使處於 排氣2 0 0 °C ~ 10 0(TC時之任何高溫範圍内,均為具有耐熱性 且不會分解之財熱材。 前 )。上 石者。 XRD ( X 物之特 在 長,而 療,顯 能說明 由。事 之液体 器加熱 止,以 形成漿 微鏡觀 中,上 發明矽 述東麗 其結晶 ray D i 殊裝置 第五圖 C u為乾_ 示其在 其保有 實上, 塗於鐵 ,均會 後隨著 化及塗 察該現 段圖乃 烷醇鹽 研究中 化速度 f f rac t ° )之 中,縱 村。前 低溫時 之水份 即使將 板上, 顯示膨 加熱溫 臈化, 象。第 示水性 液^…、有膨脹發泡性(inturaescence 心之分析報告,係以6 5 (TC時生成泡 之,供速可從如第五圖所示之5 0 G°C \〇n X先解析裝置,係僅為分析s丨化 與水破璃之尖峰差異比較而判斷者α 轴係X光的吸收光譜cmVg,橫軸為波 發明石夕烷醇鹽液之結晶尖峰非常明 即成為固相前驅物而造膜之情形,且 如蒸發時可呈現膨脹發泡現象之原 含前發明矽烷醇液之固形成份為5 〇% 而自鐵板下部加熱,或自上方藉燃燒 脹發泡現象。此現象持續至6 5 (TC為 度之上升,膨脹發泡現象終至消失而 使用日本HI TEC (株)公司之高溫顯 六圖即為該現象之示意圖。在第六圖 造臈性無機化合物(LC )藉排氣而行 414721 [ I五、發明說明(5)Page 6 414721 I five 'invention description (4)-" ........................ ............ FTIR analysis at ° C shows that the water molecule spikes will become low due to heating and form a film. In the first to fourth figures, the horizontal axis represents the wave number (Wave Numbers) and the vertical axis represents the absorbance (Absorvance). This analysis report from Toray Research Center is based on the FTIR j analysis of the first to fourth graphs, indicating the presence of siloxane at 780cni-1, and at 9 °, i002400 ~ 3800cm 1 The presence of silanols. The silanolate solution of the present invention is a heat-resistant material that does not decompose even if it is at an exhaust temperature of 200 ° C to 100 ° C (at any high temperature range at TC. Front). On the stone. XRD (X matter is long, and the treatment, obviously can explain the reason. The liquid device is heated to form a slurry micro-mirror view, the crystal silicon ray ray D i special device invented on the fifth figure C u For the sake of dryness, it shows that in its possession, it is coated with iron, and it will be followed by the chemical transformation and the investigation of the current section of the research on the rate of chemical transformation (ff rac t °) in the study of alkanolate in this section. Before the low-temperature moisture even if the board, the display shows a large temperature, the temperature is reduced, and the phenomenon. The aqueous solution shown in the figure ^ ..., has an expansion foaming (inturaescence heart analysis report, the bubble is generated at 6 5 (TC, the supply rate can be from 50 G ° C \ 〇n X as shown in the fifth figure) The first analysis device is only for the purpose of analyzing the difference between the peaks of the water and the glass. The absorption spectrum cmVg of the α-axis X-ray is judged, and the horizontal axis is the crystal peak of the cetyl alcohol salt solution of the invention. In the case of solid phase precursors and film formation, and if the expansion and foaming phenomenon can occur during evaporation, the solid content of the original silanol solution containing the former invention is 50%, and it is heated from the lower part of the iron plate, or expanded and foamed from the top by combustion Phenomenon. This phenomenon continues until 65 (TC is an increase in degrees, and the expansion and foaming phenomenon eventually disappears. Using the high temperature display of Japan HI TEC Co., Ltd. is a schematic diagram of this phenomenon. Inorganic compounds (LC) run by exhaust gas 414721 [I. Description of the invention (5)

I 泡洙化及塗膜化並形成為膠質過濾膜,遂呈只放出水蒸 汽、二氧化碳等之經淨化處理氣體之狀態之示意圖。中段 圖乃示殘渣物之溫度下降而發泡消減呈鎮靜之狀態之示意 圖。下段圖則示回到常溫而將排氣殘渣物包在塗膜内呈塗 膜化狀態之示意圖。如此,水性造膜性無機化合物(LC ) 膠質乃具有形成耐熱過濾膜之作用°廢棄物之焚化排氣係 含有高溫之氣體及含重金屬之飛灰,為使前發明矽烷醇鹽 液可包圍上述排氣,則須使該排煙管道為可充滿膨脹發泡 之程度,由於前發明矽烷醇鹽液係藉高溫排氣而形成為造 膜膨脹發泡物,遂具有可達成本目的之過濾作用之功效° 矽烷醇於加熱時,Η及0H即脫水而形成為矽氧烷。此 時,如有重金屬,被認為將與S i - 0 - R結合。依據將前發明 矽烷醇鹽液與重金屬含有物之混合物之焚化物分析結果, 顯示未見有重金屬之溶出。若為只是如塗料之塗怖隱蔽 時,予以粉碎後,即會有重金屬之溶出,但在將試料予以 粉碎而行試驗之方法之結果t,以8 0 0 °C高溫予以固化之 後,再行粉碎之粉碎物並未見有重金屬之溶出,因此被認 為應係成離子結合,此即表示其係具有捕捉重金屬之作 用。 前發明矽烷醇鹽液係0. 1〜1微米大小之膠質1如第一 圖至第四圖之FTIR分析所示,即使加熱至900 °C時,羥基 並未消失。第七圖僥將前發明矽烷醇鹽液於加熱氣體溫度 450 °C及噴嘴溫度180 °C時,經喷霧乾燥器喷乾而形成粉狀 化之顯微鏡相片,顯示呈5 0 ~ 8 0微米大小之發泡氣球化之 4"f 4721 ▲ j五 '發明說明(β) .........................................._-... ...............................................................................- i $怒。又如第六圖之示意圖所巾’在過量之水存在之條件 i右以尚溫排氣而行加熱時,造臈膨脹發泡化之膠質係 j表面之凝膠狀物溶覆著,凝膠保有之水份蒸發後,便藉 由該膠臈過濾作用將廢棄物固形成份包覆於内部,而將殘 渣物包容堆積。由於排氣中有害之戴奥辛反應在45〇t以 |上時不會產生,因此若能先補捉其前驅物及鹽酸成份’則 於冷卻至戴奥辛容易產生之40 0 t以下時,亦能抑制戴奥 辛之產生。 I 前發明矽烷醇鹽液係鹼金屬鹽,當將此鹽液以έ! 口溫 度2 0 0 °C之喷霧乾燥器除袪過剩水分而形成粉体化之後, 再以40%重量比混入PVC t以滾筒攪拌,接著以多爾曼 | (Dolman)元素分析計施以7 5 0 t;之燃燒’並予以分析τ分 |析結果乃示,揮發性鹽酸減至微少量,不揮發性H C L則增 加至6 0 0 0倍’煙塵藉由過濾補集分析法測知約減少至 | 2 5?4 ’因此’揮發性鹽酸及煙塵顯著減少,惡臭亦減少。 |第八圖係將第七圖所示固形化粒狀物與p vc混合而行焚燒 !後之氣體,經日本Zew分析中心所做之氣體分析結果報 表。依此分析結果能知前發明矽烷醇鹽液係具有減少黑煙 |及減少惡臭之筆因氣體之效果。尤其,鹽酸之L i鹽(氣化 |鋰)即使捕捉氣氣亦不易於低溫分解,是以,前發明矽烷 :醇Li鹽液乃可有效防制PVC之戴奥辛之產生。 J 廢棄物中之重金屬之Pb(鉛)成份為含有量最多者,茲 以此為標本試料,即以含Pb為500ρρπι至2000ppm之底灰, 及含?1)為15000口口111之飛灰,依含?13量,混入10%至140%之I Foaming and coating film formation and formation into a colloidal filtration membrane, then it is a schematic diagram showing the state of purified treatment gas such as water vapor, carbon dioxide and the like. The middle diagram is a schematic diagram showing the temperature of the residue falling and the foaming reduction being sedated. The lower diagram shows the state where the exhaust gas residue is wrapped in the coating film and returned to normal temperature. In this way, the aqueous film-forming inorganic compound (LC) colloid has the function of forming a heat-resistant filter film. The waste incineration exhaust system contains high-temperature gas and heavy metal-containing fly ash. For exhaust, the exhaust pipe must be filled with expansion and foaming. Because the silane alkoxide solution was formed into a film-forming expansion foam by high temperature exhaust gas, it has a filtering effect that can reach cost. Efficacy ° When silanol is heated, tritium and 0H are dehydrated to form siloxanes. At this time, if there is a heavy metal, it is considered to be combined with S i-0-R. According to the results of incineration analysis of the mixture of the silane alkoxide solution and the heavy metal content of the previous invention, no elution of heavy metals was shown. If it is only concealed like coating, after pulverization, the heavy metal will dissolve, but after the sample is pulverized and tested, the result t is cured at a high temperature of 800 ° C, and then it is carried out. The pulverized material does not see the dissolution of heavy metals, so it is considered to be ionic bonding, which means that it has the function of capturing heavy metals. The silane alkoxide solution of the previous invention is 0.1 to 1 micron in size of colloid 1. As shown in the FTIR analysis of the first to fourth graphs, even when heated to 900 ° C, the hydroxyl group has not disappeared. The seventh picture: When the silane alkoxide solution of the previous invention is heated at 450 ° C and the nozzle temperature is 180 ° C, it is spray-dried by a spray dryer to form a powdered micrograph, which shows that it is 50 to 80 microns. The size of the bubble balloon 4 " f 4721 ▲ j five 'invention description (β) .................... ........._-... ....................... .............................- i $ anger . As shown in the schematic diagram of the sixth figure, when the condition of excess water is present and the exhaust gas is heated at a high temperature, the gel on the surface of the colloidal system j that expands and foams is dissolved, and the gel After the moisture contained in the gum evaporates, the solid components of the waste are coated inside by the filtering effect of the gum, and the residue is contained and accumulated. Since the harmful dioxin reaction in the exhaust gas does not occur when it is more than 45t, if its precursors and hydrochloric acid components can be captured first, it can also be suppressed when it is cooled to less than 40t which is easily produced by dioxin. The birth of Dioxin. I previously invented the silane alkoxide solution as an alkali metal salt. When this salt solution was sprayed with a spray dryer at a mouth temperature of 200 ° C to remove excess water to form a powder, it was mixed in at 40% by weight. The PVC t was stirred by a roller, followed by the application of 7 50 0 t in a Dolman elemental analysis; the combustion was analyzed and the τ score was analyzed. The analysis results show that the volatile hydrochloric acid is reduced to a small amount and is not volatile. HCL increased to 6 0 0 times. 'Smoke and dust were reduced to approximately | 2 5? 4' by filtering supplementary analysis. Therefore, 'volatile hydrochloric acid and soot were significantly reduced, and malodor was also reduced. The eighth figure is a mixture of solidified granules shown in the seventh figure and pvc for incineration. The gas analysis results reported by the Japanese Zew Analysis Center are reported. Based on the results of this analysis, it can be known that the silanolate liquid system of the previous invention has the effect of reducing black smoke | In particular, the Li salt of hydrochloric acid (gasification | lithium) is not easy to decompose at low temperature even if it captures gas. Therefore, the silane: alcohol Li salt solution of the previous invention can effectively prevent the production of dioxin from PVC. J The Pb (lead) component of the heavy metal in the waste is the one with the highest content, so this is the sample sample, that is, the bottom ash containing Pb from 500ρρπ to 2000ppm, and the content of? 1) Is the fly ash of 15000 mouth 111, depends on? 13 volumes, mixed with 10% to 140%

第9頁 414721 ;五、發明說明¢7) 前發明矽烷醇鹽液中,而加熱至9 0 0 °C以上,則於任何情 況下P b溶出試驗之結果中,皆可獲得安定型分析值之每公 升0. 0 1 ppm之結果,認為應係生成上述說明之矽氧烷結合 ,之故。 做為木材防腐劑使用之CCA係含有鉻及紕素,將此5% | 溶液混入1 0 %前發明矽烷醇鹽液中再予加熱至9 0 0 3C而使其 固化,則形成為綠色固化物,縱使在此固化物溶出試驗 中,其Cr、Cu' As之含量為O.Olppm以下,認為此等重金 I屬亦已產生離子結合。 若將前發明矽烷醇鹽液直接喷霧於200 °C以上之高溫 排氣時,則因瞬間凝膠造膜而膨脹發泡化,遂可將黑煙或 惡臭氣體含包於内,同時其膠質膜具有過濾作用,故將矽 i烷醇鹽液向排氣喷霧是為有效之淨化處理方法。噴霧手段 丨因要求瞬間之擴散效果,若使用產生高壓之喷射器來喷霧 時,將產生足以吸引之負壓,而形成可將排氣含包於上述 矽烷醇鹽液之造膜膨脹發泡物内之作用,遂產生亦含飛灰 之殘渣物,在其壓送之際乃藉比重差而行堆積,其間只有丨 ! i 丨蒸汽可蒸發。是以,上述矽烷醇鹽液不論是對以送風機吹Page 9 414721; V. Description of the invention ¢ 7) In the silane alkoxide solution previously invented and heated to more than 900 ° C, the stability analysis value can be obtained in the results of the Pb dissolution test under any circumstances. The result of 0.01 ppm per liter is considered to be due to the generation of the siloxane combination described above. The CCA used as a wood preservative contains chromium and halogens. This 5% | solution is mixed into 10% of the silane alkoxide solution previously invented and then heated to 9 0 3C to cure it, forming a green solidification Although the content of Cr and Cu 'As in this solidified product dissolution test is below 0.01 ppm, it is considered that these heavy metals I have also produced ion bonding. If the previously invented silanolate solution is directly sprayed at a high temperature above 200 ° C, it will expand and foam due to instant gel film formation, so that black smoke or malodorous gas can be contained in it, and its The colloidal membrane has a filtering effect, so spraying the alkanolate liquid on the exhaust gas is an effective purification treatment method. Spraying method 丨 Due to the need for an instantaneous diffusion effect, if a high-pressure ejector is used for spraying, a negative pressure sufficient to attract will be generated, and a film can be formed to expand and foam the exhaust gas containing the silane alkoxide solution. The action within the object then produces a residue that also contains fly ash. When it is pressed, it is accumulated by the difference in specific gravity, during which only steam can evaporate. Therefore, whether the above silanolate solution is blown by a blower

I 丨送之排氣施以加壓喷霧、或滴灑矽烷醇鹽液,皆會產生相 j I同之作用,故而矽烷醇鹽液之加壓、喷霧、或滴灑係必要 手段。前發明矽烷醇鹽液與上述排氣接觸之方法,不論是 對吸引及送風之排氣施以喷霧狀矽烷醇鹽液、或滴灑矽烷 醇鹽液,或是相反地將高溫排氣吹入前發明矽烷醇鹽液内 而行接觸,皆會產生造膜膨脹發泡而達成相同之作用效The exhaust gas sent by I 丨 is subjected to pressurized spraying or dripping of the alkanolate solution, which will have the same effect. Therefore, pressurization, spraying, or dripping of the alkoxide is a necessary means. The method of contacting the silanolate liquid with the above-mentioned exhaust gas in the previous invention, whether it is spraying silanolate liquid on the exhaust gas that attracts and sends air, dripping silanolate liquid, or blowing high-temperature exhaust gas on the contrary When contacted in the silane alkoxide solution before the invention, the film formation will expand and foam, which will achieve the same effect.

第10頁 414721 ........... !五、發明說明(8) 丨果。又,殘潰係藉比重差而產生堆積,若混入高嶺土或碳 酸鈣等之礦物粉亦有效。 含有機物、重金屬、土壤或水份等之廢棄物可容易與Page 10 414721 ...........! V. Description of the invention (8) 丨 Fruit. In addition, the crumb is piled up due to the difference in specific gravity, and it is also effective if it is mixed with mineral powder such as kaolin or calcium carbonate. Wastes containing organic objects, heavy metals, soil or water can be easily contacted

I ί前發明矽烷醇鹽液混合,如上所述,當有機物燃燒時,其 ! | 丨混合之前發明矽烷醇鹽液即行造膜膨脹發泡,而將燃燒氣I i體包含於其内,且將碳化、氣化之煙塵或CL氣體予以捕 丨 :捉,並發揮僅使水蒸汽通過之過濾作用。同時亦可將前發 明矽烷醇鹽液混入底灰,亦有淨化之作用。若將前發明矽 烷醇鹽液向上述排氣直接喷霧時,則可同時對底灰及排氣 發揮本發明之淨化處理作用之效果。 如上所述,含有前發明矽烷醇鹽液之排氣殘渣之堆積 ! i 丨物或底灰若焚燒至8 0 0 °C以上,例如以旋轉爐焚燒時,即 使其含有重金屬,也會形成陶瓷化,而可降至不會溶出重 金屬之安定型有價物之指定比率内。 以下就本發明解決上述問題之手段說明之。 | ; j 1.本發明之特徵係將由矽氧烷及矽烷醇鹽形成之水性造膜 | 性無機化合物,接觸含有黑煙或惡臭及重金屬、飛灰之 ! 廢棄物所焚燒之排氣,而產生造膜膨脹發泡物,並形成 可將黑煙或惡臭、有害氣體及重金屬包含於内部之燃燒 I殘渣物,藉此以將上述黑煙或惡臭及有害氣體及重金屬 等有害物或公害物予以封止於内之淨化處理物質。 | 2.本發明之特徵係將由矽氧烷及矽烷醇鹽形成之水性造膜 | 性無機化合物*混入推積在焚化廢棄物之焚化裝置底部 ! 之底灰内而形成混合物,藉此以獲得表面被上述水性造I I previously invented the silane alkoxide solution to mix, as mentioned above, when the organic matter burns, it! | 丨 Invented the silane alkoxide solution to form a film to expand and foam before mixing, and the combustion gas I i body is included in it, and Capture carbonized and vaporized soot or CL gas: and capture the filtering effect of passing only water vapor. At the same time, the silanolate solution of the previous invention can be mixed into the bottom ash, which also has the function of purification. If the silanolate solution of the previous invention is directly sprayed onto the exhaust gas, the effect of the purification treatment of the present invention can be exerted on the bottom ash and exhaust gas simultaneously. As mentioned above, the accumulation of exhaust residues containing the silanolate solution of the previous invention! I 丨 If the incineration or bottom ash is incinerated to more than 800 ° C, for example, when it is incinerated in a rotary furnace, it will form ceramics even if it contains heavy metals It can be reduced to the specified ratio of stable metals that do not dissolve heavy metals. The means for solving the above problems by the present invention will be described below. ; J 1. The feature of the present invention is that the water-based film formed from siloxane and silanolate is an inorganic compound that comes into contact with black smoke or foul odor, heavy metals, and fly ash! Exhaust gas incinerated by waste, and Produce film-forming expansion foams, and form combustion residues that can contain black smoke or foul odors, harmful gases, and heavy metals inside, thereby using the above black smoke or foul odors, harmful gases, heavy metals, and other harmful substances or public pollutants A purification treatment substance sealed in it. 2. The feature of the present invention is to form an aqueous film made of siloxane and silanolate | inorganic compound | mixed into the bottom ash of the incineration device of incineration waste to form a mixture, thereby obtaining a mixture The surface is made of the above water

苐11頁 414721 五、發明說明(9) 膜性無機化合物之包膜所包覆之燃燒殘渣物,而將有害 物或公害物予以封止於内之淨化處理物質。 3. 本發明係將申請專利範圍第1項或第2項或該兩項所述之 表面被上述水性造膜性無機化合物之膜所包覆之燃燒殘 渣物,或其兩者之混合物,施以800°C以上高溫之燃燒 丨 固化為特徵者。 | 4. 本發明係將由矽氧烷及矽烷醇鹽形成之水性造膜性無機 I 化合物,接觸焚燒廢棄物所生排氣或飛灰,而產生造膜| 膨脹發泡物,並形成將黑煙或惡臭、有害氣體及重金屬I 包含於内部之燃燒殘渣物,同時將上述黑煙或惡臭、有 害氣體及重金屬等有害物或公害物包封於其内之廢棄物 予以焚燒,如此能同時將此廢棄物焚燒所生之黑煙或惡i 臭與有害氣體及重金屬含有物等之有害物或公害物施以 封止淨化處理之廢棄物之淨化處理方法。 5. 本發明依申請專利範圍第4項所述之上述接觸係將由矽 氧烷及矽烷醇鹽形成之水性造膜性無機化合物,對廢棄 物之焚燒氣體施以喷霧而行接觸者。 6. 本發明依申請專利範圍第5項所述之水性造膜性無機化 合物與廢棄物之焚燒氣體接觸之際,係藉由於煙道或吸 引側道安裝之加壓喷霧裝置將水性造膜性無機化合物對丨苐 Page 11 414721 V. Description of the invention (9) A purification treatment substance in which the combustion residues covered by the coating of the membrane-type inorganic compound are sealed, and the harmful substances or public pollutants are sealed therein. 3. The present invention is to apply the combustion residues covered by the above-mentioned aqueous film-forming inorganic compound film on the surface described in item 1 or item 2 of the patent application scope, or a mixture of the two. Characterized by combustion and solidification at high temperature above 800 ° C. 4. The present invention is to form an aqueous film-forming inorganic I compound formed of siloxane and silane alkoxide into contact with the exhaust gas or fly ash generated by incineration of waste to produce a film | expanded foam and form a black Smoke or foul odor, harmful gas and heavy metal I contained in the internal combustion residues. At the same time, the above-mentioned black smoke or foul odor, harmful gas, heavy metal and other harmful substances or public pollutants enclosed in it will be burned. The purification treatment method of the black smoke or malodor generated by the incineration of this waste, the harmful odors such as harmful gases and heavy metal contents, or the public pollutants is applied to the purification treatment. 5. According to the present invention, the above-mentioned contact according to item 4 of the scope of the application patent is a person who sprays the incineration gas of the waste with an aqueous film-forming inorganic compound formed of a siloxane and a alkoxide. 6. When the water-based film-forming inorganic compound described in item 5 of the patent application comes into contact with the incineration gas of the waste, the water-based film is formed by a pressure spray device installed in the flue or suction side channel. Inorganic Compounds 丨

I 焚燒氣體施以喷霧,並藉由喷霧之際所生之負壓將黑煙 或惡臭與有害氣體及重金屬予以吸引者。 7. 本發明依申請專利範圍第4項所述之水性造膜性無機化 合物與廢棄物之焚燒氣體之接觸,係將2 0 0 °C以上之上I The incineration gas is sprayed, and the black smoke or malodor, harmful gases and heavy metals are attracted by the negative pressure generated during the spraying. 7. According to the present invention, the contact between the water-based film-forming inorganic compound and the incineration gas of the waste according to item 4 of the scope of the patent application is to be above 200 ° C.

第12頁 五'發明說明(10) | 述廢棄物之焚燒氣體吹入上述水性造膜性無機化合物液 内,而形成可將黑煙或惡臭及有害氣體或重金屬包含於 内部之燃燒殘渣物者。 8.本發明係將由矽氧烷及矽烷醇鹽形成之水性造膜性無機 化合物,接觸該焚燒廢棄物之焚化裝置底部之底灰,而 i : 產生造膜膨脹發泡物,並將有害物或公害物予以封止之 i 廢棄物之淨化處理方法。 | 9.本發明係將依申請專利範圍第4項第8項所述之廢棄物淨 : 化處理方法所產生之同時將有害物或公害物予以封止之 處理物,或焚燒此廢棄物所生之之底灰或飛灰與上述水 性造膜性無機化合物混合之後,再加熱至8 0 0 °C以上而 形成陶瓷化,遂而防止有害物或公害物之溶出者α 在上述三種淨化處理物及五種廢棄物之處理方法中,由前 發明矽氧烷及矽烷醇鹽液形成之水性造膜性無機化合物最 丨好為使用:將金屬鋁或金屬矽,及加水之硼砂、硼酸、氟 i化鈉或氟酸及鋅酸化合物,及苛性鹼、苛性鈉或苛性鍟之 i鹼金屬進行反應之際,在水中或上述含礦酸化合物之溶液 丨中,產生與上述金屬固體及鹼金屬之高濃度溶液反應,該 丨反應熱係控制於50°C以上至100°C以内,同時生成物之比 重為1 . 1以上之水性造膜性無機化合物為佳。再者,於上 | 述生成之水性造膜性無機化合物内加入金屬之化合物,而 使金屬成份呈過剩狀態亦為可行。尚且,亦可於水性造膜 性無機化合物内加入加有或未加有礦酸之醇類予以混合而 生成具有比重為1. 3以上之沉澱物。或於水性造膜性無機Page 12 5'Invention description (10) | The incineration gas of the waste is blown into the above-mentioned aqueous film-forming inorganic compound liquid to form a combustion residue that can contain black smoke or foul odors and harmful gases or heavy metals inside . 8. The present invention is an aqueous film-forming inorganic compound formed of siloxane and a silanolate, which contacts the bottom ash at the bottom of the incineration device of the incineration waste, and i: generates a film-forming expanded foam, and causes harmful substances Or the purification method of the waste which is sealed by the pollution. 9. The present invention is to treat the waste as described in item 4 and item 8 of the scope of the patent application: chemical treatment, which is a treatment product that simultaneously seals harmful substances or public pollutants, or burns the waste. The raw bottom ash or fly ash is mixed with the above-mentioned aqueous film-forming inorganic compound, and then heated to more than 800 ° C to form a ceramic, so as to prevent the elution of harmful substances or public pollutants. Α In the above three purification treatments Among the five methods of processing waste and five types of waste, the aqueous film-forming inorganic compounds formed from the previously invented siloxane and silanolate salts are best used: metal aluminum or silicon metal, and borax, boric acid, When reacting sodium fluoride or fluoric acid and zinc acid compounds with caustic alkali, caustic soda or caustic alkali metal i, in water or in the solution containing the above-mentioned mineral acid compounds, the metal solid and alkali For high-concentration solution reaction of metals, the heat of reaction is controlled at 50 ° C or higher and 100 ° C or lower, and the water-forming film-forming inorganic compound having a specific gravity of 1.1 or more is preferred. Furthermore, it is also feasible to add a metal compound to the above-mentioned aqueous film-forming inorganic compound, so that the metal component is in an excess state. Moreover, an alcohol with or without mineral acid may be added to the aqueous film-forming inorganic compound and mixed to form a precipitate having a specific gravity of 1.3 or more. Water-based film-forming inorganic

第13頁 414721 五、發明說明(11) 化合物内加入天然或 物,而增黏者仍屬可 入金屬氫氧化物,而 總括而言,做為 合物係由矽氧烷及矽 該矽氧烷具有一 該矽烷醇鹽為一 [Si (HnOH卜J ]M, 氧烷與矽烷醇鹽之混 百分比,該混合物復 P Η值 1 1〜1 3 比重 1 . 0 1〜2 . 粘度 在比重1. 顏色 有色透明 由各種試驗結果 成為戴奥辛前驅物之 皆可藉由本發明之淨 捉。再者,本發明係 發泡之現象,其凝膠 蒸發,而包含於其内 燒固至9 0 0 °C以上時, 價物質。尚且,不論 或是相反地將排氣吹 產生同樣之造膜膨脹 合成之礦物粉、礦物纖維或礦物層狀 行。另於水性造膜性無機化合物内加 形成硬水性组成物者皆屬可行。 淨化處理劑之上述水性造膜性無機化 烷醇鹽所組成,其中 般式[H3SiOSiH3], 種矽烷醇金屬鹽,具有一般式 式中η為1〜3,M為Na,I(或Li;而砂 合物之混合比為1 0〜9 0 : 9 0〜丨0重量 具有下列特性: 5常溫下為300以下 證實,廢棄焚燒排氣之黑煙、惡臭及 鹽酸或其溫床之飛灰、或重金屬等, 化處理而無需藉助袋式集塵器予以捕 有異於一般之液體,顯現有造膜膨脹 狀固化塗膜化之結果,乃使水份得以 部之殘渣物則呈凝膠狀堆積,經加熱 則形成重金屬不會溶出之安定型有 上述矽烷醇鹽液是吹入高溫排氣内, 入矽烷醇鹽液内而行接觸反應,皆會 發泡及過濾作用之效果。Page 13 414721 V. Description of the invention (11) Natural compounds or substances are added to the compounds, but the thickeners can still be metal hydroxides. In a word, the compounds are composed of siloxane and siloxane. Alkane has a silane alkoxide of [Si (HnOH, BJ) M, the percentage of oxane and silane alkoxide, the mixture has a P value of 1 1 ~ 1 3, specific gravity 1. 0 1 ~ 2. Viscosity in specific gravity 1. The color is colored and transparent. The dioxin precursors can be captured by the present invention from various test results. Furthermore, the present invention is a phenomenon of foaming, the gel of which is evaporated, and it is contained and fired to 90 °. Above ° C, it is a valence substance. Moreover, the exhaust gas is blown to produce the same mineral powder, mineral fiber or mineral layered line formed by the same film formation expansion. In addition, hard water is added to the aqueous film forming inorganic compound All of the above-mentioned water-soluble film-forming inorganic alkanolates of the purifying treatment agent are composed of the general formula [H3SiOSiH3], a kind of silanol metal salt, wherein η is 1 to 3, M Na, I (or Li; and the mixing ratio of the sand compound is 10 to 9 0: 9 0 ~ 丨 0 weight has the following characteristics: 5 It is 300 or less at room temperature. It is confirmed that waste smoke, foul odor and hydrochloric acid, or fly ash, or heavy metals, etc. of waste incineration waste are chemically processed without the need of a bag type collector. The dust collector catches liquids different from ordinary liquids. It shows the result of the existing film-forming swelling solidified coating film, so that the residues of the water can be accumulated in a gel-like form. After heating, it will form a stable state where heavy metals will not dissolve. The above-mentioned silane alkoxide solution is blown into the high-temperature exhaust gas, and the contact reaction occurs in the silane alkoxide solution, which will have the effects of foaming and filtering.

第14頁 > 414721 丨五、發明說明(12) 按焚燒排氣中戴奥辛為最有害之氣體,為戴奥辛前驅 物之氣在4 5 0 °C以上高溫時不會合成為定論,若能在此階 I段將氯除去,就能阻止戴奥辛之產生,但迄今尚無能夠在 |此高溫之下使用之袋濾器。前發明矽烷醇鹽液係如第一圖 !至第四圖所示具有耐熱性,且如第六圖所示,其膠質會行 膨脹發泡而呈氣球化,遂形成如第六圖之示意圖所示之具 |有過濾器之作用,又如上所述,因係鹼金屬鹽而可捕捉 HCL,而使之成為不揮發性成份,同時可抑制煙塵之產 生。第九圖及第十圖係對一般垃圾(MS W)及碎斷機塵埃 (SD)使用燃燒試驗所做之工業分析及成份分析之結果報 表。吹入排氣内之前發明矽烷醇鹽液係使用大量過剩水稀 丨釋之稀釋溶液,上述碎烧醇鹽液之比熱於高溫之下甚少變 化,其與大量過剩水共存之下,更能產生吸熱冷卻之作 用,而能冷卻排氣,又因中小型爐係批次式運轉之爐,容 易造成產生戴奥辛之低溫2 0 0 °C〜4 0 0 °C之環境溫度之危 險,但若將上述本發明之矽烷醇鹽液吹入時,不論其為批 丨次式運轉之焚化爐,或是連績式運轉之高溫焚化爐,皆可 I不致產生公害問題。 | 按上述本發明之矽烷醇鹽液吹入20(TC〜800 °c之高溫 丨排氣時,即可一邊使水份蒸發,一邊產生膨脹發泡現象, 而將有機物燃燒所生之黑煙或惡臭包含於内部,遂具有形 成為耐熱無機過遽器作用之效果而使之無公害化。 以下依照本發明之實施例就上述問題之解決及本發明 之作用功效說明之。Page 14 > 414721 丨 V. Description of the invention (12) Dioxin is the most harmful gas in the incineration exhaust gas, and the gas that is the precursor of dioxin will not be synthesized at a temperature of more than 450 ° C. If it can be concluded here, The removal of chlorine in stage I can prevent the production of dioxin, but so far there is no bag filter that can be used at this high temperature. The silane alkoxide solution of the previous invention has heat resistance as shown in the first picture! To the fourth picture, and as shown in the sixth picture, its gum will expand and foam and become balloon, so it is formed as shown in the sixth picture As shown, it has the function of a filter, and as mentioned above, because it is an alkali metal salt, it can capture HCL, make it a non-volatile component, and can suppress the generation of smoke and dust. The ninth and tenth graphs are the results of industrial analysis and composition analysis of general waste (MS W) and crusher dust (SD) using combustion tests. Before blowing into the exhaust gas, it was invented that the silane alkoxide solution was a diluted solution diluted with a large amount of excess water. The specific heat of the above-mentioned crushed alkoxide solution changed little at high temperatures. It coexisted with a large amount of excess water and was more capable of It has the effect of endothermic cooling, which can cool the exhaust gas, and because the small and medium-sized furnaces are batch-operated furnaces, it is easy to cause the danger of generating low-temperature ambient temperature of 2 0 ° C ~ 4 0 ° C. When the silanolate liquid of the present invention is blown in, whether it is a batch-type incinerator or a continuous-type high-temperature incinerator, it can cause no pollution problems. | When the silanolate solution of the present invention is blown into a high temperature of 20 (TC ~ 800 ° C) 丨 when exhausting, it can evaporate water and produce expansion and foaming, and the black smoke generated by burning organic matter Or foul odor is contained in the interior, so that it has the effect of forming a heat-resistant inorganic filter to make it pollution-free. The following is a description of the solution of the above problem and the effect of the present invention according to the embodiment of the present invention.

414721 [......................................................................... ..............................................................———................................... 五、發明說明(13) 【第一實施例】 ,可慢慢 ^過程則 9 5 0 3C 時 昆度之上 ,LC雖含 :艮定於此 按前發明矽烷醇鹽液LC受到加熱也不會分解 加熱至1 0 0 Ot:以進行徐徐脫水而形成為矽氧烷,: ;如第一圖〜第四圖之分別於20DC 、50°C 、550°C及 之FTIR圖(東麗研究中心之分析結果)所示。隨著i 升,其水分子尖峰會變低而行造膜。 i【第二實施例】 上述實施例使用之LC之分析值係如表一所示 i 有使用原料成分,唯分析後之成分構成比例並不F 丨表所示者。 【表一】 底層玻料 前發明矽烷醇鹽液 組成物 比率(重量 55 SI0, 60. ?,Ί 20 Na'C 21. 92 15 β2〇3 1 6 . 44 5 CaF, 1 . 37 AGNE技術中心之分析結果 由於此成份組成比率係類似於琺瑯之下釉藥分析值, ,...............................................414721..............>................................................................................................................................————————...................._ .......................................... !五、發明說明(14) 遂可同樣加熱硬化而形成陶瓷塗膜化= |【第三實施例】 I 前發明矽烷醇鹽液之固形成份50%之比重為1.5及PH值 |為12.2之LC-150,所保有之水分依溫度之不同之減水量係 |如表二所示,再者,其於2 0〜1 2 0 0 °C間之比熱、擴散係數 |及斷熱係數係如表三所示(AGNE技術中心之分析值)。 i 其脫水係持績至高溫為止,比熱及斷熱係數亦自常溫 至1 0 0 0 °C之間並無明顯之變化,此乃因LC- 1 5 0之溫度即使 ;於高溫環境之下亦不易上升,而可做為排氣溫度之吸熱 劑。若有過剩水時,係以相乘效果而具有吸熱急冷之作· 用。 I【表二】 加熱減水量分析結果 加熱溫度°c_減水量/保有水 | 22〜200 94.07 200〜500 4. 643 500-1000 1.282414721 [................................................ ............................................... .....................................--——............ ............ V. Description of the invention (13) [First embodiment], can be slowly ^ process is 9 5 0 3C Above Kundu, although the LC contains: According to the previous invention, the silane alkoxide liquid LC will not be decomposed and heated to 100 Ot when heated: it is dehydrated to form siloxane, which is: The FTIR charts (analysis results of Toray Research Center) at 20DC, 50 ° C, 550 ° C and FTIR are shown in Figures ~ 4th. As i rises, its water molecule spikes become lower and the membrane is formed. i [Second embodiment] The analysis value of the LC used in the above embodiment is shown in Table 1. i The raw material components are used, but the component composition ratio after analysis is not shown in the table. [Table 1] The composition ratio of the silanolate solution before the bottom frit (weight 55 SI0, 60.?, Ί 20 Na'C 21. 92 15 β2 03 1 6. 44 5 CaF, 1. 37 AGNE Technology Center The analysis result is because the composition ratio of this component is similar to the analysis value of glaze under enamel, .................... ....... 414721 ............. > ...... ........................................ ........................................ ............————————...................................... ....................... V. Description of the Invention (14) Then it can be similarly heated and hardened to form a ceramic coating. Membraneization = | [Third Embodiment] I The proportion of 50% of the solid content of the silanolate solution of the previous invention is 1.5 and the PH value is LC-150 of 12.2. The amount of water retained depends on the temperature. As shown in Table 2, moreover, its specific heat, diffusion coefficient, and thermal cutoff coefficient between 20 and 120 ° C are shown in Table 3 (Analyzed value of AGNE Technology Center). I Its dehydration system Until the high temperature, the specific heat and thermal insulation coefficient are also from room temperature There is no obvious change between 1 0 0 ° C, this is because the temperature of LC- 1 50 is not easy to rise even in high temperature environment, and can be used as heat sink for exhaust temperature. If there is excess water In the case of multiplication effect, it has the function of endothermic quenching. I [Table 2] Analysis result of heating water reduction heating temperature ° c_ water reduction / retained water | 22 ~ 200 94.07 200 ~ 500 4. 643 500-1000 1.282

I j I【表三】 : 斷熱諸特性分析結果 ; 溫度 比熱 熱擴散係數 數熱傳導度I j I [Table 3]: Analysis results of adiabatic characteristics; temperature specific heat thermal diffusion coefficient number thermal conductivity

°C C a 1 / g. °C . C in V s Cal/cm/s. °C 20 0.200 0.00696 0.00203 414721 五、發明說明(15) 300 0. 363 0.00340 0.00175 400 0.310 0.00356 0.00161 600 0.312 0.00352 0.00160 800 0.326 0.00392 0.00167 1 000 0.358 0.00239 0.00126 [ 第 四實 施 例 ] 前發 明 矽 烷醇鹽 液LC - 1 5 0係藉大 河 原化工機公司之裝 置 以LPG瓦斯溫度450 °C 及出口溫度 1 8 0 °C之條件下進行 喷 ±μ 乾 °因 LC係 膠質且 具有 膨脹發泡性 遂可形成為50〜80 微 米 之氣 球 〇 此氣球 化之 顯微鏡照相 係 如第七圖所示。此 係 將 20〜50之重量份及規定量之安定劑及其他等加入PVC内 加 以 混拌 而 形 成片材 〇 其 於ΖΕΟΝ分析 中 心以7 5 0 °C燃燒之 分 析 結果 則 如 第八圖 所示 。該分析係 藉 多_曼元素分析 儀 離子 色 讀 分析及 過濾 器捕集法而 實 施者,其結果顯示 即 使 將PVC以7 5 0 °C 燃 燒時 ,其揮發性 鹽 酸將會大量減少, 而 不 揮發 性 鹽 酸量則 增至 6000倍,煙 塵 乃減少至2 5 %。 即 縱使 燃 燒 PVC或其他含CL物質時 亦可充分捕捉其可 形 成 為戴 奥 辛 之揮發 性CL ,遂具有能 抑 制戴奥辛形成之作 用 〇 同時 亦 可 阻礙煙 塵或 惡臭之產生 〇 [ 第 五實 施 例 ] 上述 LC -1 5 0特性 經以 Si-MAS-NMR(密西根州立大學開 發 之 獨特 分 析 裝置)分析之結果(由岩 乎 大學委託密西根州° CC a 1 / g. ° C. C in V s Cal / cm / s. ° C 20 0.200 0.00696 0.00203 414721 V. Description of the invention (15) 300 0. 363 0.00340 0.00175 400 0.310 0.00356 0.00161 600 0.312 0.00352 0.00160 800 0.326 0.00392 0.00167 1 000 0.358 0.00239 0.00126 [Fourth Embodiment] The silanol alkoxide LC-1 50, which was previously invented, is based on the equipment of Ogawara Chemical Machinery Co., Ltd. under the conditions of LPG gas temperature 450 ° C and outlet temperature 180 ° C. Spraying ± μ dry ° Because of the LC-based colloid and expansion and foaming, it can be formed into a balloon of 50 ~ 80 microns. The photomicrograph of this balloon is shown in Figure 7. This is a 20 to 50 parts by weight and a predetermined amount of stabilizer and other added to PVC and mixed to form a sheet. The analysis results of the combustion at 750 ° C at the ZENE analysis center are as shown in Figure 8. Show. This analysis was carried out by a multi-man elemental analyzer ion ion reading analysis and filter capture method. The results show that even when PVC is burned at 750 ° C, its volatile hydrochloric acid will be greatly reduced without The amount of volatile hydrochloric acid increased to 6000 times, and soot was reduced to 25%. Even when burning PVC or other CL-containing substances, it can fully capture the volatile CL that can be formed into dioxin, which has the effect of inhibiting the formation of dioxin. At the same time, it can also prevent the generation of smoke or foul odor. [Fifth embodiment] The above LC -1 50 characteristics analyzed by Si-MAS-NMR (a unique analysis device developed by Michigan State University)

第18頁 ........................................................................414721..................................................................................................................................................................................——一 …— 五、發明說明(16) 立大學所做之試驗結果)係如第五圖所示=分析結果表示 ;LC係由二聚物' 三聚物所構成。第五圖乃示上述本發明之 |矽烷醇鹽液於平均排氣溫度500度之下具有顯著之結晶尖 聲,水玻璃因係無結晶合金而未顯示結晶尖_峰1'此乃顯示 上述矽烷醇鹽液於排氣溫度400〜800 °C之間具有造膜性之 :作用。即,呈膠質之上述LC於剩餘水份消失後,膠質便能 |聚集而形成具有耐熱及吸熱性之造膜功能。 【第六實施例】 本例係將上述LC-150塗於不鏽鋼板上,再自常溫加熱 至900 t:為止,其間一邊加熱升溫一邊以日本Hi-Tec(株) 公司之高溫觀察顯微鏡予以攝影觀察。其在1 (] 0 t至3 0 0 t 之間係形成泡沫化,隨後擦拭鏡片乾淨後再觀察,結果, 膨脹發泡之現象持續至約6 5 0 °C ,而固化為蛋白石(泡石)Page 18 ............... ......... 414721 .............. ........................................ ........................................ ........................................ ....—— 一… — 5. Description of the invention (16) The results of experiments conducted by the State University) are shown in the fifth figure = the analysis results are shown; LC is composed of a dimer and a trimer. The fifth figure shows the above-mentioned silanolate solution of the present invention has a pronounced crystal squeak under an average exhaust temperature of 500 degrees, and water glass does not show a crystalline tip because it is a non-crystalline alloy. _Peak 1 'This shows the above The silane alkoxide solution has film-forming property between the exhaust temperature of 400 ~ 800 ° C: role. That is, after the above-mentioned LC that is in a colloidal state disappears, the colloidal substance can aggregate to form a film-forming function having heat resistance and heat absorption. [Sixth embodiment] This example is coated with the above-mentioned LC-150 on a stainless steel plate, and then heated from normal temperature to 900 t: while heating and raising the temperature while taking pictures with a high-temperature observation microscope of Japan Hi-Tec Co., Ltd. Observed. It forms a foam between 1 (] 0 t to 3 0 0 t, and then observes after wiping the lens clean. As a result, the phenomenon of expansion and foaming continues to about 6 50 ° C, and it solidifies into opal (foamite )

I I狀,至800 °C以上時則可塑化而呈麥芽糖狀之漿狀化狀 態。而呈現如第六圖所示概念之過程變化。即可理解只要 |將上述LC對燃燒排氣拼煙道施以噴霧時,瞬間即會形成膨 丨脹發泡之現象。排煙道應具有足可讓LC呈泡沫化充滿管道 之程度之直徑者即可有效作用。又將高溫之排氣導入矽烷 醇鹽液内亦可產生同樣之堆積作用效果。 【第七實施例】 第六圖係本發明之作用之示意圖,在第六圖中,上述 本發明矽烷醇鹽液係藉排氣而形成泡沫化,其膠質乃行造I I shape, above 800 ° C, it can be plasticized into a maltose-like syrupy state. And presents the process change of the concept as shown in the sixth figure. It can be understood that as long as the above LC is sprayed on the combustion exhaust fight flue, the phenomenon of expansion and foaming will be formed instantly. The flue gas duct should have a diameter sufficient to allow the LC to foam and fill the pipe. Introducing high-temperature exhaust gas into the silane alkoxide solution can also produce the same accumulation effect. [Seventh embodiment] The sixth diagram is a schematic diagram of the effect of the present invention. In the sixth diagram, the silane alkoxide solution of the present invention is foamed by exhaust gas, and its gum is made.

第19頁 414721 五、發明說明(17) 膜 而形成 為 過 濾膜,而 只 放 出 淨 化 之水蒸 汽1二 氧化瑞 等 ,泡沫 最 後 會沉靜下 來 而 形 成 凝 膠膜。 上述實 驗結果全 部 可獲得 完 全 與示意圖 相 同 之 狀 態 0 [ 第八實 施 例 ] 對於 含 有 每公升2 2 2 0 mg / 之 PbO之飛灰之分析值及 對 此 飛灰1 0 0重量份 混合, 以20〜 1 00重 :量份之L C後之情形 列 載 如表四 所 示 。將此物 燒 固 至 9 0 0 °C :之後 ,經由神奈川 縣 產 業總合 研 究 所所做之 溶 出 試 驗 結 果,則 如表五 所示c '其 任 一者之 溶 出 試驗結果 皆 達 到 安 定 型有價 物之規 定值 0 ‘ 0 1 p p m以下, 而 顯示有淨化重金屬 之作用。 焚化灰之分析 值係如下表所示, 而Pb溶出量為每公 升 222 mg ° [ 表四】 灰 之分相 •值 % SIO, 9 ‘ 7 4. 73 ΖπΟ 0.62 A 1 z03 5 ,75 Na 2. 54 PbO 0. 18 C aO 42 .15 Cl 1 3. 31 CuO 0.05 MgO 2 .02 S0H 4. 34 F e2〇3 1. 09 [ 表五】 灰 100 100 100 灰 由NKK提 供 混合L C d ]形成 份 18 36 5 4 分 析係依; 坪奈川 縣 414721 五、發明說明(18) 產業總合研究所之 試驗結果 溶出量 0.01 0.01 0.01 以下以下 【第九實施例】 以下為神戶製鋼所提供之都市垃圾焚化飛灰及下水 道污泥焚化灰之重金屬分析值。此係將上述LC - 1 4 0 (固形 成份4 0 ?f)以丨0〜2 0重量百分比混合入上述灰内之後,再以 9 5 0 °C予以燒固之後,由神戶製鋼所所作溶出試驗結果以 表六表示 型規定值 重金 之,其 以下。 屬 中 Pb 、 As 、 重金屬 都市垃 Ce之重金屬之溶出量 分析值 圾 下水道污泥 皆在安定 Pb mg /K 503 200 As m g / K 1.2 40 Ce mg/K 0.4 <0.1 【表六】 下水道污 泥焚J匕 混合L C重量份P b m g As mg Ce mg 飛灰 10份 0.007 0.007 <0.001 15份 0.002 0.005 <0.001 20份 0.005 0. 005 <0.001 都市垃圾 焚化 10份 0.01 < <Page 19 414721 V. Description of the invention (17) The membrane is formed as a filtration membrane, and only the purified water vapor 1 is released. The foam will finally settle down to form a gel film. All the above experimental results can be obtained in the same state as the schematic diagram. [Eighth embodiment] Analytical value of fly ash containing 2 220 mg / L of PbO per liter and mixing 100 parts by weight of the fly ash to 20 ~ 100 weight: The situation after the amount of LC is shown in Table 4. This material was fired to 900 ° C: After that, according to the dissolution test results made by the Kanagawa Prefectural Institute of Industrial Synthesis, the results of the dissolution test of any one of them are shown in Table 5 c. The specified value of the substance is below 0 '0 1 ppm, which shows the effect of purifying heavy metals. The analysis value of incineration ash is shown in the following table, and the dissolution amount of Pb is 222 mg per liter ° [Table 4] Phase fraction of ash • Value% SIO, 9 '7 4. 73 Znπ 0.62 A 1 z03 5, 75 Na 2 54 PbO 0. 18 C aO 42 .15 Cl 1 3. 31 CuO 0.05 MgO 2 .02 S0H 4. 34 F e2〇3 1. 09 [Table 5] Ash 100 100 100 Ash is provided by NKK mixed LC d] 18 18 5 5 4 Analysis analysis; Panagawa 414721 V. Description of the invention (18) Test results of the Industrial Research Institute Dissolution amount 0.01 0.01 0.01 or less [ninth embodiment] The following is the municipal waste provided by Kobe Steel Analysis value of heavy metals in incineration fly ash and sewage sludge incineration ash. This system mixes the above LC-1 4 0 (solid content 40 f) into the above ash at a weight percentage of 0 ~ 20, and then solidifies it at 95 ° C, and then dissolves by Kobe Steel. The test results are shown in Table 6 as the specified value, which is below. Analytical value of heavy metal dissolution of Pb, As and heavy metals in urban waste Ce. The sewage sludge is stable at Pb mg / K 503 200 As mg / K 1.2 40 Ce mg / K 0.4 < 0.1 [Table 6] Sewer sewage Mud-burning J dagger mixed LC weight parts P bmg As mg Ce mg fly ash 10 parts 0.007 0.007 < 0.001 15 parts 0.002 0.005 < 0.001 20 parts 0.005 0. 005 < 0.001 urban waste incineration 10 parts 0.01 < <

第21頁 ..................................................4147^1.............................................................................................................................................................. 五、發明說明(19) 丨飛灰 1 5份 0.0 0 9 < < 2 0 份 0.0 04 < < 土 壤環境基準值 O.Olmg 0 . 0 1 in g 0 . 0 1 mg 【第十實施例】 第十一圖係本發明之飛灰處理實驗裝置,此裝置構成 |於一普通焚化爐(a)之煙道加設一旁道(b),又設有一將本 ; |發明之LC-140以20容量份/ lm3(50倍)加以混合之水溶液 |櫃(c ),而上述LC稀釋係液藉高壓幫浦(d )加壓並經喷霧器 i (e)喷入該旁道(b)内,LC液即與藉高壓幫浦之負壓所吸引i I ; 丨之棑氣及飛灰一邊形成泡泳化,一邊包容,而被導入沉ί殿 槽(f),並在此形成污泥沈積於槽底,而自排出口( g)則僅 排出經處理過之無黑煙及無惡臭之水蒸汽、二氧化碳等氣 |體,另自沉澱槽(f)底部取出之污泥則投入一旋轉窯爐(h) | : i 丨内,而經由900t燒固後之排出物(i)便形成安定型有價 1 物。Page 21 ......................................... ... 4147 ^ 1 .................. ........................................ ........................................ ................... 5. Description of the invention (19) 丨 Fly ash 1 5 parts 0.0 0 9 < < 2 0 parts 0.0 04 < < Reference value of soil environment O.Olmg 0. 0 1 in g 0. 0 1 mg [Tenth embodiment] The eleventh figure is an experimental device for fly ash treatment according to the present invention. This device constitutes an additional side channel in the flue of an ordinary incinerator (a). (B), there is also an aqueous solution of | LC-140 of the invention mixed with 20 capacity parts / lm3 (50 times) | cabinet (c), and the above-mentioned LC dilution system liquid is added by high pressure pump (d) Pressure and spray into the side channel (b) through the sprayer i (e), the LC liquid is attracted by the negative pressure of the high pressure pump i i; It is contained, and is introduced into the sink hall (f), where sludge is deposited on the bottom of the tank, and the self-exhaust port (g) only emits treated black smoke and foul-free water vapor, carbon dioxide, etc. gas |, The sludge taken out from the bottom of the sedimentation tank (f) is put into a rotary kiln (h) |: i 丨, and the effluent (i) after 900t firing is formed into a stable valuable product.

II

I 【第十一實施例】 第九圖乃示一般垃圾〔MSW)及碎斷機塵埃廢料〔SD)之 i 工業分析及元素分析結果。上述SD含有達2, 2%之稍高量CL | 成份9第十圖係記載其焚化灰之重金屬或微量稀有金屬之; 分析結果。第九圖中,戴奥辛前驅物之Fe20 3佔417 2%(重 量百分比)'〇1^占25.70〇111钇/1<£、211貝|]為38,00〇1]1羟/反尽° 牙1J 用上述實施例之焚化爐實驗裝置以焚燒前述之RDF,在尚I [Eleventh Embodiment] The ninth figure shows the results of industrial analysis and element analysis of general waste [MSW] and crusher dust waste [SD]. The above SD contains a slightly higher amount of CL of 2.2% | Component 9 The tenth chart is the heavy metal or trace rare metal of its incineration ash; the analysis result. In the ninth figure, the dioxin precursor Fe20 3 accounts for 4172% (weight percentage) '〇1 ^ accounts for 25.70〇111 yttrium / 1 < £, 211 shell |] is 38,00〇1] 1 hydroxyl / reverse exhaust ° Ya 1J used the incinerator experimental device of the above embodiment to incinerate the aforementioned RDF.

414721 , :五、發明說明C20) 未對其投入LC液前,煙囪(j )有產生黑煙及惡臭’但是將 該LC液以2 0 0 kg/era2壓力一開始吹入時,煙i ( j )則僅排 出白色蒸汽,黑煙及惡臭全部消失°此工程經日本(株)鋼 管計測公司依J Ϊ S有害氣體分析法進行分析而得。按戴奥 辛最易發生之排氣溫度為260 aC〜350 aC ,但其生成要因之 HCL係由250〜1100 ppm激減至2.4〜2. 9ppm,而於蒸汽排 |出口之戴奥辛雖為200 ngTEQ,但平均值則1. QngTEQ/Nm3 本實施例並未使用袋式過濾器,亦未使用石灰做為吸 著劑,顯見為矽烷醇鹽液係具有耐熱過濾器之作用,遂可 過濾淨化鹽酸及戴奥辛。而對污泥在經旋轉窯爐(h )燒固 後之溶出試驗中,其有害重金屬為0. 0 1 ppm以下°縱使將 毛巾覆蓋於上述蒸汽排出口( g)時,也未見有碳煙附著於 |毛巾上,且不會聞到有臭氣。沉澱槽(ί)之溫度係藉由上 i述LC液之吸熱作用,而不會處於生成戴奧辛之1〇〇°C以下 之5 0〜7 (TC内之環境溫度内。 【第十二實施例】 第九及第十圖中之SD係含有多量重金屬:Pb為 1,313 ppm 'Cd為 29 ppm 、Zn為 38, 000 ppm、Cr為 831 ppm、As為29 ppm。而將此以SD:LC=10: 10 (固形成份 比)混合之,再將其置於電爐内以9 5 (TC燃燒兩小時固化之 後,進行J I S之溶出試驗。試驗結果可達到上述土壤環境 414721 五、發明說明(21) 【第十三實施例】 將第九圖中之SD予以粉碎,再將上述本發明之矽烷醇 鹽液LC-150以10%重量加入而予混合做為燃燒之廢棄物, 上述喷射式喷霧液係為混合有5%之LC (固形成份2, 5%)之稀 釋液,再將該LC稀釋液加壓至Kg / Cm2而進行如同第十一 實施例之燃燒,則由於廢棄物及排氣兩者皆混合有LC,結 果遂能達到上述土壤環境基準值之1公升含Pb CL 0 1 mg、 Cd 0.01 mg' Cr 0.05 rag、As 0.01 mg以下之目標值,而 以嗅覺及視覺均未覺察到有臭氣及黑煙產生。 [第十四實施例】 落融爐所產生之飛灰中原含有Pb: 17, 000 ppm(新曰 南公司提供),在該飛灰中添加以含上述固形成份6 0 %之 LC-1 50至24 0%而予以混合,再將其置於電爐内以9 0 0 °C燃 燒一小時固化之後,經由依照日本環境廳告示第十三號之 溶出試驗結果降至(K 0 1 ρ ρ πι以下。 【第十五實施例】414721,: V. Description of the invention C20) Before the LC liquid was put into it, the chimney (j) produced black smoke and foul odor, but when the LC liquid was first blown in at a pressure of 200 kg / era2, the smoke i ( j) Only white steam is emitted, and all black smoke and malodor disappear. ° This project was obtained by Japan Steel Pipe Measurement Co., Ltd.'s analysis based on JΪS harmful gas analysis method. According to dioxin, the most likely exhaust temperature is 260 aC ~ 350 aC, but the reason for its generation is that the HCL is sharply reduced from 250 ~ 1100 ppm to 2.4 ~ 2.9 ppm, while the dioxin at the steam exhaust | export is 200 ngTEQ, but The average value is 1. QngTEQ / Nm3 In this embodiment, no bag filter is used, and lime is not used as the sorbent. It is obvious that the silane alkoxide solution has the function of a heat-resistant filter, so it can filter and purify hydrochloric acid and dioxin. . In the dissolution test after the sludge was solidified by the rotary kiln (h), the harmful heavy metals were below 0.1 ppm. Even when the towel was covered with the steam outlet (g), no carbon was found. Smoke attaches to the towel and does not smell odorous. The temperature of the sedimentation tank (ί) is based on the endothermic effect of the LC liquid described above, and will not be within the range of 50 to 7 (TC ambient temperature below 100 ° C). [Twelfth implementation Example] The SD series in the ninth and tenth drawings contain a large amount of heavy metals: 1,313 ppm of Pb, 29 ppm of Cd, 38,000 ppm of Zn, 831 ppm of Cr, and 29 ppm of As. Let this be SD: LC = 10: 10 (solid content ratio) mixed, and then put it in an electric furnace to burn after curing for 2 hours at TC (2 hours after TC solidification, and then perform the JIS dissolution test. The test results can reach the above-mentioned soil environment 414721 V. Description of the invention (21 ) [Thirteenth embodiment] The SD in the ninth figure is pulverized, and then the above-mentioned silane alkoxide liquid LC-150 of the present invention is added at 10% by weight and mixed as a burning waste. The mist liquid is a 5% LC (solid content 2, 5%) diluted liquid, and then the LC diluted liquid is pressurized to Kg / Cm2 for combustion as in the eleventh embodiment. Both of the exhaust gas are mixed with LC, and the result can reach 1 liter of the above-mentioned soil environmental reference value, including Pb CL 0 1 mg, Cd 0.01 The target values of mg 'Cr 0.05 rag and As 0.01 mg, but no odor and black smoke were detected by smell and vision. [Fourteenth Example] The original fly ash produced by the melting furnace contains Pb: 17, 000 ppm (supplied by Shinyue Minami Co., Ltd.), and the fly ash is mixed with LC-1 50 to 24% containing 60% of the solid content mentioned above, and then mixed in an electric furnace at 900 After curing for one hour at ° C, it was reduced to (K 0 1 ρ ρ π π or less) by the dissolution test result according to the thirteenth notice of the Japan Environment Agency. [Fifteenth embodiment]

第十一圖係使用於本發明之焚化裝置之示意圖,係構 i成於一般焚化爐(a)之煙囪(j)連結有一煙囪旁道(b),LC i 稀釋液(c)係藉高壓幫浦(d)加壓及喷嘴(e)而喷入煙囪旁 道(b)内,再行導入沉澱槽(f ),隨後排出之水蒸汽將為無 害、無臭及無色者,而沉積之堆積物係藉由旋轉窯爐(h) 丨予以焚化,焚化後之排出物(i )則形成為安定型有價物。 ίThe eleventh figure is a schematic diagram of the incineration device used in the present invention. The structure i is formed in a chimney (j) of a general incinerator (a) and connected with a chimney bypass (b). The LC i diluent (c) is a high pressure The pump (d) is pressurized and the nozzle (e) is sprayed into the side of the chimney (b), and then introduced into the sedimentation tank (f), and the water vapor discharged thereafter will be harmless, odorless and colorless, and the deposits will accumulate. The material is incinerated by the rotary kiln (h) 丨, and the incineration effluent (i) is formed into stable value. ί

第24頁 414721 I五、發明說明(22) i 以第十一圖之裝置將混合有會產生黑煙及惡臭之電纜 i橡膠、PVC片材及苯乙烯發泡碎屑之廢棄物予以焚燒。如 i此直接焚燒時,於周邊產生無法忍受之黑煙及惡臭,因此 |停止焚燒。但改以上述LC之2% (固形成份1%)調整上述裝 置之水溶液櫃(c)之溶液後,再以此L C溶液每1公升(固形 成份20g)對lm3燃燒氣體量之比率,籍由噴霧器以壓力 1 00Kg / era2喷入排氣内而開始進行焚燒時,周邊就感覺不 到有黑煙及惡臭。在沉澱槽(f)内則沉積著内含有碳垢之 黑色污泥堆積物。又藉由另行設置之LC水溶液櫃,而將上 述4 0 0 °C排氣經由排氣管導引吹入該水溶液櫃(c )時,瞬間 形成發泡膨漲化,惡臭即行消失,排出之蒸汽並無黑煙產 生。縱使燃燒聚酯塗料時,也同樣可消除黑煙及惡臭,而 僅有淨化之蒸汽排出。此外,水溶液櫃内之溶液亦無須倒 棄,而可重覆使用3 | 按本發明係使用本發明人所研發之水性造膜性無機化 I合物之溶液而成功者。本發明使用之矽烷醇鹽液即使於當 溫之下亦可行造膜之故,對排氣溫度2 0 0〜8 0 ere之高低均 不影響其產生發泡膨漲造膜之現象,此現象充滿於排氣煙 道内,藉此將含有害氣體或重金屬之排氣包容於泡膜内, 遂具有冷卻排氣以降溫及做為耐熱膠質過濾器之作用,同 丨時具有將包含其内之污染性包含物予以淨化,而只排出無 ί害之蒸汽之作用。 上述本發明使用之矽烷醇鹽液係鹼金屬鹽類,有捕捉 HCL之作用,又於高溫時形成矽氧烷,而具有結合重金屬 414721 五、發明說明(23) 與氧之作用,且燒固之後則具有阻止捕捉到之重金屬溶出 之效果。因此,本發明係可捕捉其為戴奥辛之前驅物之氣 化金屬或鹽酸,遂具有對戴奥辛之產生有防範於未然之作 用及效果。 上述矽烷醇鹽液係依CL或重金屬量,而選擇混合之溶 液量為1〜3 0 0 %,但從反應當量考量之,則上述矽烷醇鹽 液有必要含有重金屬分子量之1〜5倍量之固形成份。再 者,因排氣送風係藉送風裝置而可增加風量,實際送風量 之配合比例則宜將反應氣體保持為中性以上之程度,並考 量溶液之稀釋限度及吹入量限度而定°唯各種要素之配合 均可以實驗而予以確認。 按本發明係可同時處理因燃燒而產生之碳垢或有機、 i 無機之惡臭及含重金屬之飛灰,尤其對於必須嚴袼規制之 戴奥辛生成之防止方面,可藉由排氣處理,便能同時一併 進行對惡臭、黑煙及重金屬等污染物之處理3Page 24 414721 I. Description of the invention (22) i Use the device in the eleventh figure to incinerate wastes that are mixed with black smoke and malodorous cables i rubber, PVC sheet and styrene foaming debris. If i directly burns it, it will produce intolerable black smoke and foul odors around it, so | stop burning. However, after adjusting the solution of the aqueous solution cabinet (c) of the above device by 2% of the above LC (1% of solid content), the ratio of 1 liter (20g of solid content) of the LC solution to the amount of lm3 combustion gas is calculated by When the nebulizer is injected into the exhaust gas at a pressure of 100Kg / era2 and the incineration is started, no black smoke or foul odor is felt around it. In the sedimentation tank (f), black sludge deposits containing carbon scale are deposited. When the above-mentioned 400 ° C exhaust gas is guided into the aqueous solution cabinet (c) through the exhaust pipe through the LC aqueous solution cabinet provided separately, the foaming and expansion will immediately occur, and the malodor will disappear and be discharged. No black smoke was generated from the steam. Even when polyester coatings are burned, soot and odor can be eliminated, and only purified steam is emitted. In addition, the solution in the aqueous solution cabinet does not need to be discarded, and can be used repeatedly 3 | According to the present invention, it is successful to use the solution of the aqueous film-forming inorganic compound I developed by the inventor. The silanolate solution used in the present invention can be formed even under the current temperature. The exhaust gas temperature of 200 ~ 80 0 ere does not affect the phenomenon of foaming, swelling and film formation. This phenomenon It is filled in the exhaust flue, so that the exhaust containing harmful gases or heavy metals is contained in the bubble film, so it has the role of cooling the exhaust to reduce the temperature and acting as a heat-resistant gel filter. The polluting inclusions are purified and only the harmless steam is emitted. The silanolate liquid alkali metal salts used in the present invention have the function of capturing HCL, and form siloxanes at high temperatures, and have the function of combining heavy metals 414721 V. Description of the invention (23) and the action of oxygen, and solidification After that, it has the effect of preventing the elution of the captured heavy metals. Therefore, the present invention can capture the vaporized metal or hydrochloric acid which is the precursor of dioxin, and has the function and effect of preventing the occurrence of dioxin. The above silanolate solution is based on the amount of CL or heavy metal, and the amount of the mixed solution is 1 to 300%. However, considering the reaction equivalent, the silanolate solution must contain 1 to 5 times the molecular weight of the heavy metal. Solid component. In addition, because the exhaust air supply system can increase the air volume through the air supply device, the actual air supply volume should be proportional to the reaction gas above neutral, and the dilution limit of the solution and the limit of the blow-in volume should be considered. The cooperation of various elements can be confirmed through experiments. According to the present invention, the carbon scale or organic, inorganic inorganic odor and heavy metal-containing fly ash generated by combustion can be simultaneously processed. Especially for the prevention of dioxin generation that must be strictly regulated, it can be treated by exhaust gas. Simultaneous treatment of pollutants such as stench, black smoke and heavy metals 3

第26頁Page 26

Claims (1)

六、申請專利範圍 1 . 一種廢棄物之包固處理劑,其係用於將黑煙 '惡臭或燃 燒殘渣予以包固其内之處理劑,其特徵為該處理劑係由 矽氧烷及矽烷醇鹽為有效成份所形成之水性造膜性無機 化合物,其令 該矽氧烷具有一般式[H3Si OS i H3], 該矽烷醇鹽為一種矽烷醇金屬鹽,具有一般式 [Si (HnOH4_„) ]M -式中 η為 1〜3,M為 Na,K或 Li; 而矽氧烧與矽烧醇鹽之混合物之混合比為1 0〜9 Ο : 9 Ο 〜1 0重量百分比,該混合物復具有下列特性: ΡΗ值 11〜13 比重 1 . Ο 1〜2, 0 粘度 在比重1. 5常溫下為3 0 0以下 顏色 有色透明 2. 如申請專利範圍第1項之廢棄物之包固處理劑,該處理 ! 劑係由矽氧烷及矽烷醇鹽形成之水性造膜性無機化合 I 物,而藉由與含有黑煙、惡臭與重金屬、飛灰之有害廢 I 棄物之燃燒氣體接觸及/或與焚燒該廢棄物之裝置底部 所生底灰混合以形成混合物,而生成造膜膨脹發泡物, 藉此以得表面由生成之泡臈包覆之燃燒殘渣物,同時將 所含黑煙、惡臭及重金屬等有害物或公害物包封於膜 内0 3. 如申請專利範圍第1項或第2項之廢棄物之包固處理劑, 其中該表面已被水性造膜性無機化合物之該包固處理劑 之膜所邑覆之燃燒殘渣物,或兩者之混合物,係經施以6. Scope of patent application 1. A waste treatment agent for treating waste, which is used for enclosing black smoke, malodor or combustion residue, and is characterized in that the treatment agent is composed of siloxane and silane An alkoxide is an aqueous film-forming inorganic compound formed by an effective ingredient. The alkoxide has a general formula [H3Si OS i H3]. The alkoxide is a metal alkoxide having the general formula [Si (HnOH4_ „ )] M-where η is 1 ~ 3, M is Na, K or Li; and the mixing ratio of the mixture of silicon oxide and silicon alkoxide is 1 0 ~ 9 〇: 9 〇 ~ 10 weight percent, The mixture has the following characteristics: PH value 11 ~ 13 Specific gravity 1. 〇 1 ~ 2, 0 Viscosity at normal temperature 1.5 Normal temperature is below 3 0 0 Color is colored and transparent 2. Such as the package of waste in the scope of patent application No. 1 Solid treatment agent, this treatment! Agent is an aqueous film-forming inorganic compound I formed by siloxane and silanolate, and by burning with hazardous waste containing black smoke, stench and heavy metals, fly ash I waste Gas contact and / or mixing with bottom ash produced at the bottom of the device that burns the waste to form To form a film-forming expanded foam, so as to obtain combustion residues whose surface is covered by the generated foam, and at the same time enclose the harmful substances or public pollutants such as black smoke, malodor and heavy metals in the film 0 3. If the encapsulation treatment agent for the waste of item 1 or item 2 of the scope of the patent application, wherein the surface has been covered with the combustion residue of the film of the encapsulation treatment agent of the aqueous film-forming inorganic compound, Or a mixture of both, 第29頁Page 29 六、申請專利範圍 1 . 一種廢棄物之包固處理劑,其係用於將黑煙 '惡臭或燃 燒殘渣予以包固其内之處理劑,其特徵為該處理劑係由 矽氧烷及矽烷醇鹽為有效成份所形成之水性造膜性無機 化合物,其令 該矽氧烷具有一般式[H3Si OS i H3], 該矽烷醇鹽為一種矽烷醇金屬鹽,具有一般式 [Si (HnOH4_„) ]M -式中 η為 1〜3,M為 Na,K或 Li; 而矽氧烧與矽烧醇鹽之混合物之混合比為1 0〜9 Ο : 9 Ο 〜1 0重量百分比,該混合物復具有下列特性: ΡΗ值 11〜13 比重 1 . Ο 1〜2, 0 粘度 在比重1. 5常溫下為3 0 0以下 顏色 有色透明 2. 如申請專利範圍第1項之廢棄物之包固處理劑,該處理 ! 劑係由矽氧烷及矽烷醇鹽形成之水性造膜性無機化合 I 物,而藉由與含有黑煙、惡臭與重金屬、飛灰之有害廢 I 棄物之燃燒氣體接觸及/或與焚燒該廢棄物之裝置底部 所生底灰混合以形成混合物,而生成造膜膨脹發泡物, 藉此以得表面由生成之泡臈包覆之燃燒殘渣物,同時將 所含黑煙、惡臭及重金屬等有害物或公害物包封於膜 内0 3. 如申請專利範圍第1項或第2項之廢棄物之包固處理劑, 其中該表面已被水性造膜性無機化合物之該包固處理劑 之膜所邑覆之燃燒殘渣物,或兩者之混合物,係經施以6. Scope of patent application 1. A waste treatment agent for treating waste, which is used for enclosing black smoke, malodor or combustion residue, and is characterized in that the treatment agent is composed of siloxane and silane An alkoxide is an aqueous film-forming inorganic compound formed by an effective ingredient. The alkoxide has a general formula [H3Si OS i H3]. The alkoxide is a metal alkoxide having the general formula [Si (HnOH4_ „ )] M-where η is 1 ~ 3, M is Na, K or Li; and the mixing ratio of the mixture of silicon oxide and silicon alkoxide is 1 0 ~ 9 〇: 9 〇 ~ 10 weight percent, The mixture has the following characteristics: PH value 11 ~ 13 Specific gravity 1. 〇 1 ~ 2, 0 Viscosity at normal temperature 1.5 Normal temperature is below 3 0 0 Color is colored and transparent 2. Such as the package of waste in the scope of patent application No. 1 Solid treatment agent, this treatment! Agent is an aqueous film-forming inorganic compound I formed by siloxane and silanolate, and by burning with hazardous waste containing black smoke, stench and heavy metals, fly ash I waste Gas contact and / or mixing with bottom ash produced at the bottom of the device that burns the waste to form To form a film-forming expanded foam, so as to obtain combustion residues whose surface is covered by the generated foam, and at the same time enclose the harmful substances or public pollutants such as black smoke, malodor and heavy metals in the film 0 3. If the encapsulation treatment agent for the waste of item 1 or item 2 of the scope of the patent application, wherein the surface has been covered with the combustion residue of the film of the encapsulation treatment agent of the aqueous film-forming inorganic compound, Or a mixture of both, 第29頁 414721 六、申請專利範園 8 0 0 °C以上高溫之焚燒而陶瓷化。 4. 一種廢棄物之淨化處理方法,係將如申請專利範圍第1 項之處理劑與該廢棄物之燃燒氣體或飛灰接觸,而生成 造膜膨脹發泡物,並形成將黑煙、惡臭或有害氣體及重 金屬包含於其内部之燃燒殘渣物,同時亦將上述黑煙、 臭惡或有害氣體及重金屬等有害物或公害物包封於其内| 部之廢棄物予以焚燒,而將此廢棄物焚燒所生之黑煙或 惡臭與有害氣體及重金屬含有物等之有害物或公害物同 時施以包固淨化處理之廢棄物之淨化處理方法° 5. 如申請專利範圍第4項之廢棄物之淨化處理方法,其中 上述接觸係將做為處理劑之由矽氧烷及矽烷醇鹽形成之 水性造膜性無機化合物,對廢棄物之焚燒氣體施以喷霧 而行接觸者。 6. 如申請專利範圍第5項之廢棄物之淨化處理方法,其中 ! 上述水性造膜性無機化合物與廢棄物之焚燒氣體接觸之 際,係藉由於煙道或吸引側管道安裝之加壓喷霧裝置將 水性造膜性無機化合物對焚燒氣體施以喷霧,並藉由喷 霧之際所生之負壓將黑煙或惡臭與有害氣體及重金屬予 以吸引者。 i 7.如中請專利範圍第4項之廢棄物之淨化處理方法,其中 上述水性造膜性無機化合物與廢棄物之焚燒氣體之接 觸,係將20Gt以上之上述廢棄物之焚燒氣體吹入上述 水性造膜性無機化合物内,而形成可將黑煙或惡臭及有 害氣體或重金屬包封於其内之燃燒殘渣物者。Page 29 414721 VI. Patent Application Fan Yuan Burning and ceramizing at temperatures above 800 ° C. 4. A method for purifying and treating waste, which involves contacting a treatment agent such as item 1 of the scope of the patent application with the combustion gas or fly ash of the waste, thereby generating a film-forming expanded foam, and forming black smoke and foul odor. Or combustion residues contained in or harmful gases and heavy metals, and also enclose the above-mentioned black smoke, odorous or harmful gases and heavy metals or harmful substances such as heavy metals | Purification and treatment methods for wastes from the burning of black smoke or foul odors, and harmful or harmful substances such as harmful gases and heavy metal contents at the same time. 5. Disposal if the scope of patent application is 4 A method for purifying materials, in which the above-mentioned contact is a water-forming film-forming inorganic compound formed of siloxane and alkoxide as a treating agent, and the contact is made by spraying waste incineration gas. 6. The method for purifying and treating wastes in the scope of patent application item 5, where! When the above-mentioned aqueous film-forming inorganic compounds come into contact with the incineration gas of the waste, the pressure spray The mist device sprays the incineration gas with the aqueous film-forming inorganic compound, and attracts black smoke or foul odor, harmful gases and heavy metals by the negative pressure generated during the spraying. i 7. The method for purifying and treating wastes as described in item 4 of the patent, wherein the contact between the above-mentioned aqueous film-forming inorganic compound and the incineration gas of the waste is to blow the incineration gas of the above waste into the above 20Gt Water-based film-forming inorganic compounds that form combustion residues that can enclose black smoke or foul odors and harmful gases or heavy metals. 第30頁 414721 、 六、申請專利範圍 8. —種廢棄物之淨化處理方法,係將如申請專利範圍第1 項之處理劑與焚燒該廢棄物之焚化裝置底部所堆積之底 灰接觸,而產生造膜膨脹發泡物,並將該有害物或公害 物予以包固封止之廢棄物之淨化處理方法。 9. 如申請專利範圍第4項或第8項之廢棄物之淨化處理方 法,其中上述同時將有害物或公害物予以封止之處理 物,或焚燒廢棄物所生之底灰或飛灰係經與上述水性造 膜性無機化合物混合之後,再加熱至8 0 0 °C以上而形成 陶瓷化,以防止有害物或公害物之溶出者。Page 414721, VI. Patent Application Range 8. — A method of purifying and treating waste, which involves contacting the treatment agent in item 1 of the patent application scope with the bottom ash deposited on the bottom of the incineration device that burns the waste, and A method of purifying and treating waste that generates a film-forming swelling foam, and encapsulates the harmful or public pollutant in a sealed form. 9. If the method of purifying and treating wastes in the scope of patent application No. 4 or No. 8, in which the above-mentioned treatments that simultaneously seal off harmful or public pollutants, or the bottom ash or fly ash generated by incineration of waste After mixing with the above-mentioned aqueous film-forming inorganic compound, it is then heated to more than 800 ° C to form a ceramic, so as to prevent the elution of harmful substances or public pollutants.
TW088100218A 1998-01-10 1999-01-08 Treating agent for packet solidification of wastes and the purification method of waste treatment TW414721B (en)

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