TW512077B - Detoxification treatment process of incineration ash by diffusing and decomposing incineration ash atoms and equipment for the same process - Google Patents
Detoxification treatment process of incineration ash by diffusing and decomposing incineration ash atoms and equipment for the same process Download PDFInfo
- Publication number
- TW512077B TW512077B TW090131325A TW90131325A TW512077B TW 512077 B TW512077 B TW 512077B TW 090131325 A TW090131325 A TW 090131325A TW 90131325 A TW90131325 A TW 90131325A TW 512077 B TW512077 B TW 512077B
- Authority
- TW
- Taiwan
- Prior art keywords
- treatment
- ash
- ashes
- burning
- dehydration
- Prior art date
Links
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Classifications
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D3/00—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
- A62D3/30—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents
- A62D3/37—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents by reduction, e.g. hydrogenation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/006—General arrangement of incineration plant, e.g. flow sheets
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/08—Toxic combustion residues, e.g. toxic substances contained in fly ash from waste incineration
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/40—Inorganic substances
- A62D2101/43—Inorganic substances containing heavy metals, in the bonded or free state
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2203/00—Aspects of processes for making harmful chemical substances harmless, or less harmful, by effecting chemical change in the substances
- A62D2203/10—Apparatus specially adapted for treating harmful chemical agents; Details thereof
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/10—Drying by heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/20—Dewatering by mechanical means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/80—Shredding
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/10—Combustion in two or more stages
- F23G2202/101—Combustion in two or more stages with controlled oxidant supply
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/30—Solid combustion residues, e.g. bottom or flyash
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Business, Economics & Management (AREA)
- Emergency Management (AREA)
- Chemical & Material Sciences (AREA)
- Toxicology (AREA)
- General Health & Medical Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Food Science & Technology (AREA)
- Processing Of Solid Wastes (AREA)
- Disintegrating Or Milling (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
五、發明說明(1) 本發明 (飛灰、主 灰燼擴散分 全·穩定形 習知以 的大量生產 問題因而社 處理佔主流 但是, 問題,和垃 染問題。 係關於從環 灰)與產生 解而無害化 式有效地利 來,垃圾係 、大量消費 會問題化。 ,現在則70 伴隨垃圾的 圾燃燒灰燼 境污染 之排氣 的處理 用為再 以掩埋 的擴展 因此, %以燃 燃燒處 中含有 的觀點,將一般燃燒灰燼 無害化處理,並藉由將燃燒 方法,以及其裝置而以安 生資源。 或燃燒處理,但近十年過多 而增加之垃圾,隨著處理的 垃圾的處理,以自治體燃燒 燒處理。 理的增加,發生戴奥辛生成 之重金屬問題等多種環境污 從習知的燃燒設施的爐排出的燃燒灰燼’一般係以掩 埋處理,但燃燒灰燼中多含有未燃成份。該未燃成份,含 有多數未燃碳素成份和碳化氫等生成有害物質的前驅體。 又,以燃燒設施的集塵機收集之飛灰中’含有多量有機氯 化合物、重金屬類、戴奥辛類。 該等有害物質的前驅體,有機氯化合物以及戴奥辛, 疋垃圾不完全燃燒結果產生的。因此,若能使垃圾完全燃 燒,則不會產生有害物質。但是,習知的燃燒設施多半沒 有使垃圾完全燃燒的能力,目前係將含有大量戴奥辛之燃_ 燒灰燼掩埋處理。 又,,為近年的掩埋處理場的不足,以就近不法丟置 處理、保官燃燒灰燼之地方自治體增加,垃圾造成之環境 污染問題更進一步加深。V. Description of the invention (1) The present invention (the mass production problem known as fly ash, main ash diffusion, and stable form) is therefore the mainstream, but the problem, and the problem of waste pollution. Related to the ash from the environment) The solution is effective and beneficial, and the garbage system and large consumption will be problematic. Now, 70% of the waste gas that accompanies the garbage burning ash environment pollution is used to expand the landfill. Therefore, from the point of view of the content in the combustion area, the general combustion ash is harmlessly treated, and the combustion method is used. , And its installations and resources. It may be burned, but the waste that has increased over the past ten years has been treated by the municipality as a waste. Increasing management, various environmental pollutions such as the problem of heavy metals generated by dioxin, and the like, the combustion ashes discharged from the furnaces of conventional combustion facilities are generally treated by burying, but most of the combustion ashes contain unburned components. This unburned component contains most unburned carbon components and precursors that generate harmful substances such as hydrocarbons. The fly ash collected by the dust collector of the combustion facility contains a large amount of organic chlorine compounds, heavy metals, and dioxins. The precursors of these harmful substances, organochlorine compounds, and dioxin, plutonium are generated as a result of incomplete combustion of rubbish. Therefore, if the garbage can be completely burned, no harmful substances will be generated. However, most of the conventional combustion facilities do not have the ability to completely burn the garbage. At present, the system will contain a large amount of dioxin's combustion _ burned ashes to be buried. In addition, due to the shortage of landfill disposal sites in recent years, the number of local governments that have illegally disposed nearby and burnt ashes by warders has increased, and the problem of environmental pollution caused by garbage has further deepened.
2036-4563-PF(N);ph〇ebe.ptd2036-4563-PF (N); ph〇ebe.ptd
、氣體化溶融方式等的 。但是,即使以最優良 素物質,即,鹵素供給 化,而成為燃燒灰燼中 ’該氯素化化合物成為 溫溶融方式,燃燒後會 此,燃燒灰燼成為與土 害物質的鉛和水銀、錦 燒灰燼以原樣掩埋處理 ,希望能開發在掩埋之 灰燼為資源的方法。 全燃燒、燃 減量化垃 的方法。 。藉此,是 氣中,以高 的處理方 要莫大的資 將使稅金浪 以高溫溶融 條件使垃圾 源存在時, 含有的有害 前驅體而產 產生約20 % 壤成分相近 、六價鉻、 係為土壤污 前無害化處 512077 五、發明說明(2) 因此,厚生省獎勵以高溫溶融爐將垃 燒殘渣物的再資源化。 圾70 導入該高溫溶融爐的第一目的為,— 圾。但是’該方法只不過是考慮丟棄於::由 物質為固體、液體、氣體之三態的任:種 :::不是固體者’則將其改變為氡體放出於大 融之垃圾的減量化並不是絕對對環境優良 金二此到設備費用、處理費用亦需 因此對母日丟出之垃圾進行這樣的處理, 使用南溫溶融方式 方式’可完全燃燒垃圾 燃燒’燃燒時仍含有氯 垃圾同時被氧化與_素 之氯素化化合物。於是 生戴奥辛類等有害物質 又,即使利用該高 的燃燒灰燼與飛灰。在 之組成,含有指定為有 坤、石西等6種。 所以,由於將該燃 染和地下水污染的緣故 理,或可二次利用燃燒 2036-4563-PF(N);phoebe.p td 第5頁 、發明說明(3) 本發明之目的為提供將產生之排氣無害化處理並從都 一般燃燒灰燼到將來的重金屬類和戴奥辛類皆不 污染環境之燃燒灰燼的處理方法以及其裝置。 、本發明人等經過重複詳細檢討的結果,發現以如下構 成解決上述課題。即藉由將燃燒灰燼之原子擴散以分解並 且無害化之處理方法,其包括: 使燃燒灰燼的含水率降低的脫水乾燥步驟; 將藉由前述脫水乾燥步驟產生之排氣在遷移金屬觸媒 的存在下加熱處理的排煙處理步驟; 將前述脫水乾燥處理步驟乾燥處理之燃燒灰燼粉碎處 理之粉碎處理步驟;以及 將前述粉碎處理步驟粉碎處理之燃燒灰燼,在與外氣 絕緣之低氧狀態的空間,以一定溫度及一定時間維持處理 之步驟組成之燃燒灰燼的無害化、再資源化的 其中在前述與外氣絕緣之低氧狀態的空間,以一定溫 度以及一定時間維持處理的步驟,係利用原子的擴散現象 將燃燒灰燼中的有害物質無害化,並穩定& (中請專利範 如此構成,利用被粉碎處理之燃燒灰燼中含有的原子 的擴散現象’能將燃燒灰燼中含有之戴奥辛類等的有害物 質(特別疋含有氣素等的鹵類物質)㈣鹵化而分解的同 時,穩定燃燒灰燼中含有的重金屬類而替換組成為無害的 化合物。 又,刖述脫水乾燥步驟,係在爐内溫度5〇〇〜7〇〇它加 五、發明說明(4) ^行(申請專利範圍第2項)。這樣的構成,可除去燃 、又燼中3有的水分,而容易在後續的粉碎步驟進行粉碎 處理。 又’在前述粉碎處理步驟之前,設置破碎· 圍第3項)。這樣的構成,混入燃燒灰爐中 碎處理又由於玻璃類被微粉化,係為微粉 =,在前述粉碎處理步驟,係給予慣性 5=:請專利範圍第4項卜這樣的構成,以給予償二 理步驟的is灰燼有效率地調整為適合後續還原反應處 = 而做出促進在後續之還原處 、’、/、他的雜質原子的游離狀態。 又,在前述與外氣絕緣之低氧狀態的空間,以__ 度以及維持-定時間處理的步 ::::疋- 濃度^下進行還原Λ處二f/二;㈣氧 化反應中有害物質的產生。 步驟之爐内的乳 又,具備將燃燒灰燼含有之.八 乾燥處理裝置; 刀進仃脫水乾燥的脫水 選擇被脫水乾燥之燃燒灰燼 之玻璃類破碎之破碎選擇裝置; 有之玻璃類,將選擇 破碎選擇後之燃燒灰爐的料金 麗的微粉化,與使燃燒灰燼中含 第7頁 2036-4563-PF(Ν);phoebe.p t d 512077 五、發明說明(5) ---- 有之原子的結晶格子内齡知原子之破碎處理之粉碎處理裝 置: 利用粉碎處理後的燃燒灰燼含有之原子的擴散反應, 將有害物質無害化之還原反應處理襞置; 利用還原反應處理後的燃燒灰燼所含之原子的擴散反 應,將燃燒灰燼含有之金屬類變換成穩定的化合物之穩定 化處理裝置;以及, Gasification and melting methods. However, even if the best elemental substance, namely halogen, is supplied, it becomes a burning ash. The chlorinated compound becomes a warm-melt method. After burning, the burning ash becomes lead and mercury with soil harmful substances. The ash is buried as it is, and it is hoped that the method of burying ashes as a resource can be developed. The method of total combustion and reduction of quantitative waste. . In this way, it is necessary to make a large amount of capital in the treatment of the gas. When the tax wave makes the waste source exist under high temperature melting conditions, the harmful precursors contained will produce about 20% of the soil. Similar hexavalent chromium, For the harmlessness of soil before contamination 512077 V. Description of the invention (2) Therefore, the Ministry of Health and Welfare rewards the use of high-temperature melting furnaces to recycle waste residues. The first purpose of introducing the refuse 70 into the high temperature melting furnace is to refuse. But 'this method is only considering discarding in: any of the three states of matter: solid, liquid, and gas: species ::: not solid' then change it to the reduction of the carcass into the garbage of the melting It is not absolutely necessary to treat the environment and the equipment cost, and the disposal cost. Therefore, the waste thrown on the mother's day must be treated in this way. Using the South temperature melting method to 'completely burn the garbage', the chlorine-containing garbage is still burned at the same time. A chlorinated compound that is oxidized with carbon. Therefore, harmful substances such as dioxins are used, and even if the high combustion ash and fly ash are used. In its composition, there are 6 kinds designated as Kun, Shixi and so on. Therefore, due to the reason of the combustion and groundwater pollution, secondary combustion can be used 2036-4563-PF (N); phoebe.p td page 5, description of the invention (3) The purpose of the present invention is to provide The exhaust gas is harmlessly treated, and from the general burning of ash to the future heavy metal and dioxin-type non-polluting environment burning ash processing method and device thereof. As a result of repeated detailed reviews, the present inventors have found that the above-mentioned problems are solved as follows. That is, the treatment method by decomposing and harmless by diffusing the atoms of the combustion ash includes: a dehydration and drying step to reduce the moisture content of the combustion ash; and the exhaust gas generated by the foregoing dehydration and drying step is transferred to the metal catalyst. A smoke exhaust treatment step in the presence of heat treatment; a pulverization treatment step for pulverizing the burning ashes of the aforementioned dehydration and drying treatment step; The space is maintained at a certain temperature and for a certain period of time. The steps of maintaining the harmlessness and re-recycling of burning ashes composed of the steps in the aforementioned low-oxygen state insulated from the outside air are maintained at a certain temperature and for a certain time. Utilizing the diffusion phenomenon of atoms to detoxify the harmful substances in the burning ashes, and stabilizing the & Harmful substances (especially halogenated substances containing gas) Rhenium is halogenated and decomposed, and it stably burns heavy metals contained in ashes and replaces the composition with harmless compounds. In addition, the dehydration and drying step described above is carried out at a temperature of 500 to 700 in the furnace. 4) ^ line (No. 2 in the scope of patent application). Such a structure can remove the moisture in the combustion and embers, and it is easy to perform the pulverization process in the subsequent pulverization step. Broken · Wai Item 3). Such a structure, which is mixed into a combustion ash furnace and crushed because the glass is micronized, is a fine powder =, and in the aforementioned crushing processing step, is given an inertia 5 =: Please refer to the fourth scope of the patent scope for compensation The ashes of the second step are efficiently adjusted to be suitable for the subsequent reduction reaction = to promote the free state of the impurity atoms at the subsequent reduction points. Also, in the aforementioned low-oxygen space insulated from outside air, the steps of processing at __ degrees and maintaining for a fixed time: ::: 疋-concentration ^ is performed at Λ 2 f / 二; 有害 oxidation is harmful in the reaction The production of matter. The milk in the furnace of the step is equipped with eight drying treatment devices; the knife selection 仃 dehydration drying dewatering selection is broken by the dehydration drying burning ash glass crushing selection device; some glass types will be selected After crushing the selected material of the burning ash furnace, Jin Li's micronization, and the burning ash contains page 7 2036-4563-PF (N); phoebe.ptd 512077 V. Description of the invention (5) ---- Some atoms Crushing processing device for crushing treatment of aging atoms in the crystal lattice: Use the diffusion reaction of the atoms contained in the combustion ash after the pulverization treatment to set up a reduction reaction treatment that harmless the harmful substances; use the combustion ash after the reduction reaction treatment A stabilizing treatment device for the diffusion reaction of contained atoms to convert the metals contained in the burning ash into stable compounds; and
將脫水乾燥裝置、還原反應處理裝置、以及穩定化處 理裝置產生之排煙的無害化處理之排煙處理裝置的處理裝 置(申請專利範圍第6項)。 藉由這樣的構成,可將燃燒灰燼中含有之戴奥辛類盔 害化處理,同時將燃燒灰燼中含有之重金屬類改變化成& 疋化之化合物。 接著’使用圖面說明本發明之一實施例。再者,第1 圖係為本發明之藉由將燃燒灰燼之原子擴散以分解並且無 害化之處理方法的流程圖。 本發明之燃燒灰燼的處理方法,係使用主灰(bottom ash)舨灰(fiy ash)、該等的混合灰(燃燒殘渣)、其 他產業廢棄物等、燃燒之後產生之全部的燃燒灰燼(下稱 為原灰)為原料(原灰回收)。該原灰一般含有近4〇%的 水/刀,為了在後續步驟容易進行,使用熱風於使爐内溫度 為500〜700 °C,更佳為60(TC進行乾燥處理。 忒乾燥步驟由於是在空氣的存在下進行,能使原灰中 含有的未燃燒物完全燃燒。A processing device for a dewatering and drying device, a reduction reaction processing device, and a detoxification treatment device for detoxifying the smoke generated by a stabilization processing device (item 6 of the scope of patent application). With such a structure, the dioxin helmets contained in the burning ashes can be damaged, and the heavy metals contained in the burning ashes can be changed into & tritified compounds. Next, one embodiment of the present invention will be described using drawings. In addition, Fig. 1 is a flowchart of a processing method of the present invention for decomposing and detoxifying by diffusing the atoms of combustion ashes. The combustion ash treatment method of the present invention uses a main ash (fiy ash), such mixed ash (combustion residue), other industrial waste, etc., and all the combustion ash generated after combustion (down It is called raw ash) as raw material (raw ash recycling). The raw ash generally contains nearly 40% water / knife. In order to facilitate the subsequent steps, use hot air to dry the furnace at a temperature of 500 ~ 700 ° C, more preferably 60 ° C. 忒 The drying step is In the presence of air, the unburned material contained in the raw ash can be completely burned.
五、發明說明(6) 氣化了防止原灰中含有之有害物質在熱風乾焊時 軋化而被放出於大翁+^ ^ Bf 使用觸媒等處理排氣中含^ ^ ^ ^步驟產生之排氣,經由 被放屮於士,士,、 S有之有害物質的排煙處理步驟, 被放出於大氣中(排煙處理步驟)。 7驟 在此,該排煙處理’亦可 驟、#定♦卢_車_ + ^後边之還原反應處理步 化處理步驟產生之排煙進行處理。 而取出Ϊ本使Ϊ燥處理之原灰含有之金屬類磁著於磁石等 而取出除去,並以振動篩早 艰石# 再者,選擇之祐斑猫Γ 4擇玻璃類以及粗大雜質。 筛子之原灰混♦(粉碎細微粉碎後,與通過V. Description of the invention (6) Gasification prevents the harmful substances contained in the raw ash from being rolled out during hot air dry welding and released from the big man + ^ ^ Bf The use of catalysts to process the exhaust gas containing ^ ^ ^ ^ steps generated The exhaust gas is discharged into the atmosphere through the smoke exhaust treatment step of harmful substances placed on the taxi, taxi, and S (the smoke exhaust treatment step). 7 Steps Here, the smoke exhaust treatment ’can also be treated as # 定 ♦ 卢 _ 车 _ + ^ the reduction reaction processing step in the subsequent step. And take out the sample, make the raw ash of the dried ash, magnetize the magnets and so on, remove it, and use a vibrating sieve as early as hard stone # Furthermore, choose the safari cat Γ 4 choose glass and coarse impurities. The original ash of the sieve is mixed
將在前述粉碎選摞舟a β 鈐边撒从咕本 释少驟除去金屬類、雜質之原灰,LV 粉碎機粉碎處理,並使用斿 丫、久,以 原灰之中特定粒徑以上者再回到粉碎機中二' 火的粒徑成為既定的粒徑卩 使原 T仅〔粉碎處理步驟)〇 該原灰中含有之各種合屬_ 尤颔笙兮够人Η 種金屬類’例如鐵、錯、鋼、鎘、 水銀4,該等金屬類在後螗 ‘、 一般來規今Μ鎚M t 更、、貝之選原步驟中被利用為觸媒。In the aforementioned pulverization and selection, a β 钤 side is sprinkled to remove the metal and impurities from the original ash, and the LV pulverizer is used to pulverize the ash. Go back to the crusher again. The particle size of the fire becomes the predetermined particle size, so that the original T is only [the crushing processing step]. The various genus contained in the original ash Iron, copper, steel, cadmium, and mercury4, these metals are used as catalysts in the original steps of 螗 ′, Μ, M 锤, and 贝.
將ϊίϊίΐ 積小與做為觸媒之能力亦小,L 為高。所以,▲此所謂之表面ΐ ’觸媒活性必 處理步驟之活性等的差去::’因為在後續之還原 X西处& 1ΛΛ 較佳為50〜200篩孔(mesh ),更佳為100〜150篩孔。 、meSh 又,為了微粉化作為粉碎處理 屬的結晶中虧損原+,本發 J在原灰中各有之金 與觸媒進行。以,用最小限的熱與衝擊力 忒泰碎處理步驟之粉碎處理, 第9頁 2036-4563-PF(N);phoebe.ptdThe ability to make ϊίϊί 小 small and use as a catalyst is also small, L is high. Therefore, ▲ this so-called surface ΐ 'catalyst activity must be treated with the difference of the activity and the like ::' Because in the subsequent reduction X West & 1ΛΛ is preferably 50 ~ 200 mesh, more preferably 100 ~ 150 mesh. In addition, in order to micronize the original + in the crystal, which is a pulverizing treatment, the present invention J carries gold and catalyst each in the original ash. Therefore, using the minimum heat and impact force, the crushing treatment of the Putai crushing treatment step, page 9 2036-4563-PF (N); phoebe.ptd
為3G以上,以5G之衝擊條件 驟使用之粉碎處理機並無特 (hammer miller) 〇 進行為佳。在此,粉碎處理步 別限制,例如有錘碎機 在經·過前 添加劑(無機 °C,進行40分 該還原反 濃度。再者, 依場合以該等 該等毒性物質 如戴奥辛類) 下。為了更有 %以下。 述粉碎處理 質等),投 鐘的還原反 應爐,係以 原灰中含有 做為觸媒亦 之中特別是 的生成,該 效防止有害 入還原 應(還 I入氮 之金屬 產生毒 氧素為 爐内的 物質的 原灰中添加p t等的觸媒和 反應爐,加熱原灰至6 0 0 原反應步驟)。 素等惰性氣體調節低氧素 和非金屬元素之氧化物, 性物質。藉此,為了壓抑 媒體而成之有害物質(例 氧素濃度較佳為6 %以 生成,氧素濃度更佳為3It is 3G or more, and the crushing processor used under the impact condition of 5G does not have to be performed by a hammer mill. Here, the crushing process steps are limited. For example, there are additives such as hammer crusher before the pass (inorganic ° C, the reduction inverse concentration of 40 minutes. Moreover, depending on the occasion, these toxic substances such as dioxins) . In order to be more than%. (Such as pulverization treatment quality, etc.), the reduction reaction furnace of the clock, is based on the formation of raw ash as a catalyst, especially the formation of this effect, the effect to prevent harmful reduction into the metal Add a catalyst such as pt and a reaction furnace to the raw ash of the material in the furnace, and heat the raw ash to 600 original reaction steps). Inert gases, such as pigments, regulate low-oxygen and oxides of non-metallic elements and sexual substances. In this way, in order to suppress the harmful substances created by the media (for example, the oxygen concentration is preferably 6% to generate, and the oxygen concentration is more preferably 3
在此,成為觸媒之物質不拘為氣體、液體、固體各種 樣式。 一般來說,戴奥辛類在95〇它以下的燒成溫度是無法 分解的。但是,使用本發明之方法,原灰在前述粉碎處理 步驟微粉化’且金屬結晶格子中的金屬原子虧損,以及藉 由原子的擴散現象被活性化,因此可以在5 〇 〇〜6 t之低 溫度分解。 * 又,在其中混入氧化鈣時,可生成以更低溫度起始分 解戴奥辛的氯化鈣。 77 藉此’戴奥辛類在與外氣絕緣之低氧濃度雾圍的空 間,藉由維持一定的溫度以及一定時間,以擴散現象活性Here, the materials used as catalysts are not limited to gas, liquid, and solid. In general, dioxins cannot be decomposed at a firing temperature below 95 ° C. However, using the method of the present invention, the raw ash is micronized in the aforementioned pulverization treatment step, and the metal atoms in the metal crystal lattice are depleted and activated by the atom diffusion phenomenon, so it can be as low as 5000 to 6 t. Temperature decomposition. * In addition, when calcium oxide is mixed therein, calcium chloride that decomposes dioxin at a lower temperature can be generated. 77 In this way, the dioxins are active in the space surrounded by a low-oxygen concentration mist insulated from the outside air by maintaining a certain temperature and a certain time to diffuse the activity
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五、發明說明(8) 而被 化,以觸媒以及添加藥劑(無機質)被脫氣/氫化 分解。 接著,經過還原反應步 雰1圍下於爐内溫度300〜600 進行20〜30分鐘加熱處理( 在該步驟,利用含有重 灰原子的擴散現象,使其有 類和金屬氧化物、金屬單體 其結晶化而穩定化。 在此’擴散是指固體金 就是在結晶之中原子自由活 在物質的存在樣式之一 成結晶,在該結晶,多數的 晶格子。在本發明,由於在 擊而使結晶格子中金屬原子 產生空孔和變形,成為不穩 然而,加上熱能量使原 之中原子自由地來回活動的 中新原子虧損而消除結晶格 易在結晶中的空孔容納原子 變換金屬至穩定的化合物( 再者,該穩定化步驟中 金屬的種類,得到氧化物 物、磷氧化物、等 〔驟後之原灰,在該低氧素濃度 C ’更佳調節為4〇〇〜5〇〇〇c, 穩定化處理步驟)。 金屬、異種金屬之混合物之原 效地相互分解,利用重金屬鹽 為觸媒,解離金屬鹽,藉由使 屬(結晶)中原子的移動,也 動。 的固體狀態,大部分的物質形 原子係作三次元規則配列為結 粉碎處理步驟給予慣性力5 G衝 雇亏損,因此金屬在結晶袼子中 定狀態。 子的熱振動活絡,做出在結晶 狀態(擴散狀態),結晶格子 子的變形(脫鹵化),或,容 而消除結晶格子的變形,同時 穩定化)。 金屬成為化合物之穩定化,依 氫氧化物、硫氧化物、硫化 各種型態。例如,驗金屬與驗5. Description of the invention (8) It is chemically decomposed, and the catalyst and the additive (inorganic substance) are degassed / hydrogenated and decomposed. Next, after the reduction reaction step 1 is carried out, the furnace is heated at a temperature of 300 to 600 for 20 to 30 minutes. (At this step, the diffusion phenomenon containing heavy gray atoms is used to make it similar to metal oxides and metal monomers. It crystallizes and stabilizes. Here, 'diffusion' means that solid gold is one of the existence patterns of substances in which crystals freely crystallize. In this crystal, most crystal lattices. In the present invention, due to Make the metal atoms in the crystal lattice produce voids and deformation, and become unstable. However, the addition of thermal energy makes the atoms in the original freely move back and forth, and the new and new atoms are depleted, eliminating the crystal lattice. The holes in the crystal easily contain the atomic transformation metal. To the stable compound (moreover, the kind of metal in the stabilization step, to obtain oxides, phosphorus oxides, etc. [the original ash after the step, the low oxygen concentration C 'is more preferably adjusted to 400 ~ 50000c, stabilizing treatment step). The original mixture of metals and dissimilar metals decomposes to each other, and the heavy metal salt is used as a catalyst to dissociate the metal salt. In the solid state, most of the material atomic systems are arranged in a three-dimensional rule as a knot crushing process step, which gives inertia force 5 G and a loss of employment, so the metal is in a crystalline state. The thermal vibration is active, and in the crystalline state (diffused state), the deformation of the crystal lattice (dehalogenation), or, to eliminate the deformation of the crystal lattice while stabilizing). Metals become compounds for stabilization, depending on various types of hydroxides, sulfur oxides, and sulfides. For example, metal inspection and inspection
512077 五、發明説明(9) 土族金屬以外的金屬,大多穩定化為不溶於水的氫氧化 物。又,Pb等則被穩定化為氫氧化物[Pb(〇H)2 ],該氫氧 化物由於在強酸條件下顯示有水溶性,使其穩地化為硫化 物。又,As和P係反應被穩定化為CaO。 該等的金屬元素密度高,主要為屬於遷移金屬之金屬 與該等的離子。原灰含有成分中任一元素,是在普通土壤 中比較少量不存在者。但是,該等之中亦含有作為植物生 長不可欠缺之微量元素。 又,有時會牵涉到未含有非金屬之有害指定物質之微 量元素的污染問題。 金屬化合物被埋藏於地下,土壤中的微生物慢慢無機 化為構成元素的大部分,以C〇2、、%等的形式還原至 大氣中。 又,Ca2+、Mg2+、K+等的無機陽離子被吸著於腐蝕和黏 土。在腐蝕,係作為有機酸的官能基,在黏土,於黏土石产 物的層間位置和格子空孔的陰電荷則吸著於該等陽離子二 c Γ、so/荨的陰離子亦因腐姓和黏土的部分陽電荷 被吸著。穩定化之金屬化合物,大部分以組成一次礦^、 黏土礦物以及腐#的内部構造的形式存在,以離子的形 於溶液中’或被吸者保持於黏土和腐钕的表面的離子交換 部位。 乂、 又,原灰鹽基度Cs 0 / S i 〇2兩,具有慢慢冷卻結晶化之 性質,急速冷卻則成為玻璃質。即難溶於水的物暂 成穩定、且安全的物質。 ' 生512077 V. Description of the invention (9) Most metals other than the earth metals are stabilized into water-insoluble hydroxides. In addition, Pb and the like are stabilized into a hydroxide [Pb (OH) 2], and this hydroxide is stably converted to a sulfide because it shows water solubility under strong acid conditions. In addition, the reaction between As and P is stabilized to CaO. These metal elements have high density, mainly the metals that belong to the migrating metal and these ions. Raw ash contains any element in the composition, and it is a relatively small amount that does not exist in ordinary soil. However, these also contain trace elements that are essential for plant growth. In addition, it sometimes involves the problem of contamination by trace elements that do not contain harmful designated substances other than metals. The metal compounds are buried underground, and the microorganisms in the soil are slowly mineralized into most of the constituent elements, and are reduced to the atmosphere in the form of C02,%, etc. In addition, inorganic cations such as Ca2 +, Mg2 +, and K + are attracted to corrosion and clay. In corrosion, it is a functional group of organic acids. In clay, the anionic charge in the interlayer position of the clay stone product and the lattice pores attracts the anions of these cations c Γ, so / net. Part of the positive charge is attracted. Most of the stabilized metal compounds exist in the form of internal structures that make up primary minerals, clay minerals, and rots. They are in the form of ions in solution, or are held on the surface of clay and neodymium by ion exchange sites. . In addition, the basic degree of the original ash, Cs 0 / S i 〇2, has the characteristics of slow cooling and crystallization, and rapid cooling becomes glassy. That is, substances that are difficult to dissolve in water become temporarily stable and safe substances. 'Health
五、發明說明(10) 不溶性金屬的因為f變化合物的性質作為 的添加劑由於沒有毒性可作為:::二:二’㈣系、磷系 ^加劑的場合,原灰中:ϊί=丨定=氣:用 物。,化物係無公害物質不會造成么4…-化 (以下ί 用本發明之方法,㉟明從原灰得到之生成物 因為是有機成分和重金屬類的、曰二f \原灰3水率高’ 場合,最難固化。“的“物,使用水硬性水泥的 機質=化具有該固化阻礙原因之金屬,卩及促進有 物的硬化’本發明之處理後的職,藉由微粒子 + ί f 擴散分解,與觸媒反應與還原反應的相乘結果 去除阻礙原因。 一般來說,水泥與水反應,析出水和物的結晶,由於 其凝結固化,該水和物結晶在常溫是穩地的。構成水泥之 疋素,組成最多為鈣,接著為氧、矽、鋁、鐵、硫磺、 鎮、納等,但化學組成係以Ca〇、Si〇2、Al2〇3、Fe2〇3、 S〇3、MgO的氧化物存在,佔全體的92%。 ^ 另一方面’處理後之原灰的品質並無一定,但鈣CaO 最多25〜27%,接著,鋁Al2〇3為22〜24%,矽Si02為15〜 17% ’鐵Fe2 03為9〜11%,硫酸根s〇3為2%,鎂MgO為2 % ’雖含有水泥的三成分石灰、矽、鋁,但沒有作為水硬 性的水泥的效力。 但是’具有潛在的水硬性,藉由鹼或硫酸鹽等中性以V. Description of the invention (10) Because of the nature of the compound of insoluble metal, the additive can be used as an additive because it has no toxicity. = Qi: things. Will the chemical system be harmless? 4…-化 (The following uses the method of the present invention, because the product obtained from the original ash is organic components and heavy metals. High 'occasions, the most difficult to cure. "", The use of hydraulic cement of the organic substance = the metal that has the cause of the curing hindrance, and promote the hardening of the material. "After the treatment of the present invention, the fine particles + ί f Diffusion decomposition, multiplication with catalyst reaction and reduction reaction results in removal of obstacles. Generally, cement reacts with water to precipitate crystals of water and substances. Due to its solidification, the water and substance crystals are stable at room temperature. The element of cement that constitutes cement is composed of calcium at most, followed by oxygen, silicon, aluminum, iron, sulfur, sulfur, sodium, etc., but the chemical composition is CaO, Si〇2, Al203, Fe203 , S03, and MgO oxides account for 92% of the total. ^ On the other hand, the quality of the raw ash after treatment is not constant, but the calcium CaO is 25 to 27% at most, and then the aluminum Al2O3 is 22 ~ 24%, silicon Si02 is 15 ~ 17% 'iron Fe2 03 is 9 ~ 11%, sulfate s03 is 2%, Magnesium MgO is 2% ’Although it contains three components of cement—lime, silicon, and aluminum—it has no effect as a hydraulic cement. However, it has potential hydraulic properties.
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外的刺激作用慢慢地、經年地發揮水硬性。 •又,顯示化學成分的鹽基度的值(Ca0+Al2〇3+Mg〇) /Si〇2,處理後的原灰的場合為135〜145,比水泥 1 · 0 0 〇 與水泥比較的場合,處理後之原灰的優點,不會因為 水蒸氣和碳酸氣體反應而被風化固結。 9 # 並且’處理後的原灰,大量含有反應激烈的鋁和鎂、 妈成分,由於其含有量比水泥成分中之含有量多,因此具 有反應速度快且膨脹係數高的特徵。 又’一般來說水泥被混凝土(concrete)化,其構造物 容易破壞’硫酸鹽化合為混凝土中的以⑺。2,成為硫酸 約成為CaS〇4 ’且與鋁酸三石灰水合物3Ca〇Al2〇3nH2〇結 合’成為水泥約釁土(eHringite)。 本發明之處理後的燃燒灰燼,由於反應速度快,膨脹 係數高,反應開始初期,很快生成Ca(〇H)2,因為硬化物 中沒有Ca(OH)2亦沒有csA,所以構造物的抵抗性增大。 從該等性質,與水泥並用固化時必要的氣泡能力,與 分散能力優良,具有流動性,亦可使黏性度強的土與 變化為砂質。 、匕予 並且’具有地盤改良等透水性優良、強度維持的特 性。 、 接著說明用以實施本發明之方法的裝置。 本發明之裝置,具備用以將燃燒灰燼等的原灰含有之 水分’以熱風進行脫水乾燥處理同時,將原灰中含有之未The external stimulating effect is slowly and hydraulically exerted over the years. • The value of the salinity of the chemical composition (Ca0 + Al2〇3 + Mg〇) / Si〇2. The value of the treated raw ash is 135 ~ 145, which is higher than that of cement 1 · 0 0 〇 compared with cement. On the occasion, the advantages of the treated ash will not be weathered and consolidated due to the reaction of water vapor and carbonic acid gas. 9 # In addition, the treated raw ash contains a large number of components such as aluminum, magnesium, and magnesium which are violently reactive. Since the content is more than that in the cement component, it has the characteristics of fast reaction speed and high expansion coefficient. In general, cement is concreted, and its structure is easily damaged. Sulfate is combined into concrete in concrete. 2. It becomes sulfuric acid. It becomes approximately CaS04 'and combines with aluminate trilime hydrate 3Ca〇Al203nH2O' to become cement eHringite. The treated combustion ash of the present invention has a fast reaction rate and a high expansion coefficient, and Ca (〇H) 2 is formed quickly in the initial stage of the reaction. Because there is no Ca (OH) 2 or csA in the hardened material, Increased resistance. From these properties, it is necessary to use it together with cement to solidify the necessary air bubble ability and dispersing ability, and it has fluidity. It can also change the viscosity of the soil and sand to sandy. And dagger, and it has the characteristics of excellent water permeability and strength maintenance such as site improvement. Next, the apparatus for implementing the method of the present invention will be described. The device of the present invention includes a method for dehydrating and drying the moisture contained in the raw ash such as burning ashes with hot air, and simultaneously
五、發明說明(12) 燃成分以高溫完全燃燒的脫水乾燥處理 ,混入被脫水乾燥之燃燒灰燼等的原 石吸著而從原灰中選出’再於振動篩子J出:的鐵類以磁 破璃類以及粗大雜質,將選出之玻璃類二原灰中含有之 原灰進行粉碎,破碎•選擇之破碎•選、^篩子後的 對破碎•選擇後之燃燒灰爐等的原灰仏 將原灰的粒徑成為既定之粒徑以下你Ί慣性力5G而 J理步驟之氯素和其他的雜f原子的游離原 加入Pt於破碎處理後的燃燒灰燼,作 故=,在氮素氣體等的惰性氣二二 有害物置用以還原處理原灰中… 將還原反應處理後之燃燒灰燼等的原灰中 類變換成無害的化合物之穩定化處理裝置, j用:利用觸媒將脫水乾燥、還原反應處理、以及穩 處理時產生之排煙中所含之有害物質無害化 煙處理裝置。 藉著使用該裝置,燃燒灰燼等的原灰中含有之戴奥辛 類等的有害物質,以還原處理被無害化,金屬類以穩定化 處理被無害化,又,排出氣體中含有之有害物質以排煙處 理裝置被無害化。 藉此’利用本發明之裝置處理之燃燒灰燼,比習知的〜 燃燒灰燼掩埋處理更不會對土壤造成污染。 第15頁 2036-4563-PF(N);phoebe.ptd 凝 成 五、發明說明(13)V. Description of the invention (12) The dehydration and drying treatment of the combustible component is completely burned at high temperature, mixed with the raw stones that are dehydrated and dried by burning ash, etc., and selected from the raw ash. For the glass and coarse impurities, the original ash contained in the selected glass two primary ash is crushed, crushed • selected and crushed • selected, ^ screened and crushed • selected burned ash furnace, etc. The particle size of the ash becomes below the predetermined particle size. Your inertial force is 5G, and the free atoms of chlorine and other hetero-f atoms in the J step are added to Pt after the crushing treatment of the burning ash, for the sake of =, in nitrogen gas, etc. The inert gas 222 harmful substances are used to reduce and treat the raw ash ... A stabilization treatment device that converts the types of raw ash such as burning ash after reduction reaction treatment into harmless compounds, and is used for dehydration and drying using a catalyst, Harmless substance treatment device for harmful substances contained in exhaust smoke generated during reduction reaction and stable treatment. By using this device, hazardous substances such as dioxin contained in raw ash such as ashes are burned to be detoxified by reduction treatment, metals are detoxified by stabilization treatment, and harmful substances contained in the exhaust gas are discharged. The smoke treatment device is rendered harmless. By this means, the burned ash treated by the device of the present invention will cause less pollution to the soil than the conventional ~ burned ash landfill treatment. Page 15 2036-4563-PF (N); phoebe.ptd Condensation V. Description of the invention (13)
又,利用本發明之裝置處 土荨的骨材之回收資源。 理之燃燒灰燼 可利用為混 再者,該等各裝置並 了增加燃燒灰燼的處理 =限疋為單獨設置而構成,亦可 罝而以複數台相同装置並列而構 實施例1 以下顯示進行燃燒灰 接著,實際使用本發明之方法 燼的處理之結果。 _ 燃燒灰燼係使用從司爐(stoker)方式的燃燒場以及流 動床爐方式的燃燒場採得者,每天的實證頓數為3〇t,進 行3年。 再者’燃燒灰燼再資源化場系統(plant system)的破 碎•粉碎反應·還原反應穩定化反應排煙反應各個設備的 形式’設定條件如下。 (1) 原灰進入槽:5〇m3 供給灰起重機 13t/h 接受槽 l〇m3 進料機 15t/h (2) 選擇破碎裝置 振動篩(篩(screen) 50 mm) 選擇機(除鐵之外磁選機) (3) 乾燥設備 3t/hx2 乾燥溫度 5 0 0。(:In addition, using the device of the present invention, the resources of the bones of the earth net are recovered. The combustion ash can be used as a remixer. These devices are combined with a treatment to increase the combustion ash = the limit is configured separately, or multiple identical devices can be arranged in parallel. Example 1 The combustion is shown below. Next, the results of the embers treatment using the method of the present invention are actually used. _ Combustion ash is obtained from a stoker-type combustion field and a fluid-bed furnace-type combustion field, and the actual number of proofs per day is 30t for 3 years. In addition, 'the form of each device of the crushing, pulverizing reaction, reduction reaction stabilizing reaction, and fume exhausting reaction' of the plant system for burning ash re-recycling field system 'is set as follows. (1) Raw ash enters trough: 50m3 ash crane supplies 13t / h receiving trough 10m3 feeder 15t / h (2) Selection crusher vibrating screen (screen 50 mm) selection machine (except iron External magnetic separator) (3) Drying equipment 3t / hx2 Drying temperature 5 0 0. (:
2036-4563-PF(N);ph〇ebe.ptd2036-4563-PF (N); ph〇ebe.ptd
512077 五、發明說明(14) ----- 處理時間 3 0分鐘 添加劑(妈系3 % ) 氧素濃度 約6 %以下 (4) 粉碎裝置 給予微粉末(微粒子)5G的衝擊 添加磷礦石0.03% ’添加磷化物或硫化鐵〇 〇3%製 硫化物。 (5) 還原反應處理裝置 爐處理量:3t/h X 2 反應溫度:500〜400 °C _ 反應時間:2 0〜3 0分鐘 酸性濃度·· 3 0 %以下 (6) 穩定化反應處理裝置 爐處理量:3t/h X 2 反應溫度:200〜300 °c 反應時間:1 0分鐘 (7) 製品料斗(hopper)攪拌機:3〇m3 (8 )排煙處理裝置 考慮綜合排氣處理,使用濾過式集塵器(bag filter)。檢測該濾過層濾布的壓力損出,控制在一定壓 _ (60 〜150 mmAg ) 〇 〈處理後之原灰中的有害物質量> 燃燒灰燼以及飛灰的混合物之燃燒殘渣,以本設備無512077 V. Description of the invention (14) ----- Processing time 30 minutes Additive (Ma 3%) Oxygen concentration is less than about 6% (4) Crushing device gives 5G impact of fine powder (fine particles) Adding phosphate ore 0.03 % 'Adding phosphide or iron sulfide 003% to make sulfide. (5) Furnace processing capacity of reduction reaction processing device: 3t / h X 2 Reaction temperature: 500 ~ 400 ° C _ Reaction time: 20 to 30 minutes Acidic concentration · 30% or less (6) Stabilization reaction processing device Furnace processing capacity: 3t / h X 2 Reaction temperature: 200 ~ 300 ° c Reaction time: 10 minutes (7) Product hopper (hopper) mixer: 30m3 (8) Exhaust treatment device considers comprehensive exhaust treatment, use Filter-type dust collector (bag filter). Detect the pressure loss of the filter layer filter cloth, and control it at a certain pressure _ (60 ~ 150 mmAg) 〇 <mass of harmful substances in the raw ash after treatment> Burning residue of the mixture of burning ash and fly ash, using this equipment no
512077 五、發明說明(15) 害化之生成物燃燒灰燼處理物混練水泥2 0 %作為固化物而 檢查有害指定金屬的溶出之結果,如表1所示之基準值。 表1 計量的對象 計量白 彌果 pH=7 pH=4 鈣 0.01(mg/L)未滿 0-01(mg/L)未滿 鉛 0-01(mg/L)未滿 0_01(mg/L)未滿 — 六價銘 0.05(mg/L)未滿 0.05(mg/L)未滿 砒素 OOl(mg/L)未滿 0.01(mg/L)未滿 總水銀 0.00005(mg/L)未滿 0.00005(mg/L)未滿 硒 0.01(mg/L)未滿 0.01(m2/L)未滿512077 V. Description of the invention (15) 20% of the burnt ash treatment mixture of the harmful products, mixed cement, as a solidified product, and the results of checking the dissolution of harmful specified metals are shown in Table 1 as the reference values. Table 1 Objects to be measured pH: 7 pH = 4 Calcium 0.01 (mg / L) less than 0-01 (mg / L) Less than lead 0-01 (mg / L) Less than 0_01 (mg / L ) Unfilled — Hexavalent 0.05 (mg / L) less than 0.05 (mg / L) less than 0.1 mg (mg / L) less than 0.01 (mg / L) less than total mercury 0.00005 (mg / L) less than 0.00005 (mg / L) less than selenium 0.01 (mg / L) less than 0.01 (m2 / L) less than
再者’溶出檢查,係以pH = 7與pH = 4之2水準進行。 又’各計量對象的計量,鎘係以JIS κ 01 02 55. 1為基 準,鉛以】18 1(0102 51.4為基準,六價鉻以了13|^〇1〇2 65· 2.1為基準,砒素係以JIS κ 〇1〇2 612為基準,總; 銀係以昭46環告第59號附表1為基準,硒係以JIS κ 〇1〇2 67·2為基準分別進行。 又’燃燒爐排氣中的戴奥辛類的濃度之結果示於表 %^、#、°1果,如表2所示,可判斷排氣中的各氣體濃度係 基準值以下,且戴奥辛類的、遭#Furthermore, the dissolution test was performed at a level of 2 of pH = 7 and pH = 4. Also, for the measurement of each measurement object, cadmium is based on JIS κ 01 02 55.1, lead is based on] 18 1 (0102 51.4, and hexavalent chromium is based on 13 | ^ 〇1〇2 65 · 2.1, The halogens are based on JIS κ 〇〇〇〇2 612, the total; the silver system is based on Zhao 46 ring report No. 59 Schedule 1 as the basis, and the selenium system is based on JIS κ 〇〇〇2 67 · 2 respectively. The results of the concentration of dioxin in the exhaust gas of the combustion furnace are shown in the table% ^, #, ° 1. As shown in Table 2, it can be determined that the concentration of each gas in the exhaust gas is below the reference value. #
, 度亦顯示未滿ND值(定量 宝铷哲尨务甘 +I月之裝置排出之排氣氣體中所含 害物質係在基準值以下。 & 表2The degree also shows the under-ND value (quantitative of the harmful substances contained in the exhaust gas discharged by the Breguet philosophical service + I month device is below the reference value. &Amp; Table 2
512077 五、發明說明(16) 計量的對象 計量白 猫果 測定値 〇2 12%換算値 戴奧辛濃度(ng-TEQ/m3N) — <0.016 麈濃度(g/m3N) 0.05 0.06 氮素氧化物農度(v/v ppm) 46 56 硫磺氧化物濃度⑽ppm) <5 — 硫磺氧化物量(m3_ <0.006 ―― 氯化氫濃度(v/v ppm) 0.7 0.9 一氧化碳濃度(Wv ppm) 8 10 再者,各測定對象的濃度測定法,戴奥辛類濃度係以 厚生省公示第234號(1 997 ) 「戴奥辛類濃度之計算方 法」為基準,灰塵濃度係以JIS Z 8808 ( 1 995 ) 「排氣氣 _ 體中的灰塵濃度的測定法」為基準,氮素氧化物濃度係以 JIS K 0104 (1984) 「排氣氣體中的氮素氧化物濃度的 測定法」為基準,硫確氧化物濃度係以J I S K 0 1 〇 3 (1 995 ) 「排氣氣體中的硫磺氧化物濃度的測定法」為基 準,氯化氫濃度係以JIS K 0107 ( 1 995 ) 「排氣氣體中 的氣化氫濃度的測定法」為基準,一氧化碳濃度係以j IS K 0 0 9 8 ( 1 9 8 8 ) 「排氣氣體中的一氧化碳濃度的測定 法」為基準分別進行。512077 V. Description of the invention (16) Object of measurement Measurement of white cat fruit 〇2 12% conversion 値 Dioxin concentration (ng-TEQ / m3N) — < 0.016 麈 concentration (g / m3N) 0.05 0.06 Nitrogen oxide agricultural (V / v ppm) 46 56 Sulfur oxide concentration (ppm) < 5 — Sulfur oxide content (m3_ < 0.006 —— Hydrogen chloride concentration (v / v ppm) 0.7 0.9 Carbon monoxide concentration (Wv ppm) 8 10 Furthermore, For the concentration measurement method of each measurement object, the dioxin concentration is based on the Ministry of Health, Labour and Welfare Publication No. 234 (1 997) "Calculation method of dioxin concentration", and the dust concentration is based on JIS Z 8808 (1 995) "Exhaust gas _ body The method for measuring the concentration of dust in water ”is based on JIS K 0104 (1984)“ The method for measuring the concentration of nitrogen oxides in exhaust gas ”as the standard, and the concentration of sulfur oxides is based on JISK 0 1 〇3 (1 995) "Measurement method of sulfur oxide concentration in exhaust gas" as reference, and hydrogen chloride concentration based on JIS K 0107 (1 995) "Measurement method of hydrogen gas concentration in exhaust gas" As a benchmark, the carbon monoxide concentration is based on j IS K 0 0 9 8 (1 9 8 8) "Measurement method of carbon monoxide concentration in exhaust gas" as a reference.
【發明效果】 根據申請專利範圍第1項所記載之發明,由於能做出 使結晶格子中虧損原子,而在被活性化狀態之金屬原子中 所含之燃燒灰燼中添加熱能量使原子之熱振動活絡,在結、 晶之中原子自由地來回活動之狀態(擴散狀態),[Effect of the invention] According to the invention described in the first item of the scope of the patent application, because the atom in the crystal lattice can be made deficient, thermal energy is added to the burning ashes contained in the activated metal atom to make the atom heat Vibration active, the state in which atoms move freely back and forth between the junction and crystal (diffusion state),
2036-4563-PF(N);ph〇ebe.ptd "一"一: 第19頁 " 五、發明說明(17) 二,ί:解決結晶格子的變形,從結晶格子φ· 子(齒原子等),能將燃燒灰燼中所含之=損新的原 害物質無害化。 戴奥辛類等的有 又為了解決結晶格子的變形,藉由 二孔收納原子時引起原子的替換,燃婷在結晶中的 屬類等穩定變換為無害的化合物。…所含之重金 申請專利範圍第2項所記載之發明, f燼中含有之水分,將其濕潤化流動性差由於^ :性變好。藉此’能容易進行脫水乾燥步驟= 擇:驟之選擇、粉碎…燃燒灰爐中含有之 氧素的存在下以高溫使其完全燃燒。# 分產生戴奥辛類。 J防止未燃成 又,申請專利範圍第3項所記載之發明,能將 水乾燥之燃燒灰燼等的原灰中的釘子等的鐵類以磁石磁 而從原灰選出。又,通過振動篩子可選擇原灰中含有之 :类員::粗大雜質’將選擇之玻璃類粉碎處理,能混入經 過師子後之原灰。其結果,可除去釘等的處理雜質,又、、 在後續之粉碎處理步驟,可容易粉碎處理燃燒灰燼。 、 又’根據申請專利範圍第4項所記載之發明,對破碎 ^擇後之燃燒灰燼等的原灰給予慣性力5 (j而成為既定的粒 €以下。在該原灰中’含有在後續步驟之還原處理步驟做 為觸媒之金屬類。該等在經過慣性力破碎處理之結果,由 於被微細化、被活性化做為觸媒,可促進在還原處理步驟 的反應。 。2036-4563-PF (N); ph〇ebe.ptd " 一 " 一: page 19 " V. Description of the invention (17) Second, ί: Solve the deformation of the crystal lattice, from the crystal lattice φ · 子 ( Tooth atoms, etc.), can detoxify the original harmful substances contained in the burning ashes. Dioxins and the like In order to solve the crystal lattice deformation, by replacing the atoms when the atoms are stored in the two holes, the genus and the like in the crystal are stably transformed into harmless compounds. … Contained heavy gold The invention described in item 2 of the scope of patent application, f the moisture contained in the embers, moisturizes it and has poor fluidity due to ^: better properties. In this way, the dehydration and drying step can be easily carried out = selection: sudden selection, pulverization ... combustion at high temperature in the presence of oxygen contained in the combustion ash furnace. # Points to generate dioxins. JPrevention of Unburned In addition, the invention described in claim 3 of the scope of patent application can select iron from nails such as nails in raw ashes of water-dried burning ashes and the like. In addition, the vibrating sieve can be used to select the original ash: Class member :: coarse impurities' The selected glass is crushed and can be mixed into the original ash after passing through the teacher. As a result, processing impurities such as nails can be removed, and in the subsequent pulverization processing step, the ash can be easily pulverized and treated. According to the invention described in item 4 of the scope of the patent application, the inertia force 5 (j becomes the predetermined grains or less is given to the original ashes of the crushed ash and other burning ashes. The original ash is included in the subsequent The reduction treatment step of the step is used as the metal of the catalyst. As a result of the inertial force crushing treatment, these are refined and activated as the catalyst, which can promote the reaction in the reduction treatment step.
2036-4563-PF(N);phoebe.p t d 第20頁 512077 五、發明說明(18) 又’根據申請專利範圍 入惰性氣體於還原反應,能 果,可抑制以氧素為媒介之 又,使用申請專利範圍 藉由還原反應處理裝置將燃 無害化。並且,將原灰中含 物理處理並用使其穩定,成 污染環境之安全成分。 並且,處理後的原灰成 (Portland)水泥等的並用, 藉此,在最終處分場無 材,也就是構成循環型社會 又,使用本發明之處理 比使用高溫溶融的場合,費 第5項所記栽 在低氧素條件下务進明’藉由導 有害物質的生成仃。…结 第6項所記載之發 燒灰燼中人古 的裝置’ 有=中含有之有害指定物質 ^ ^ ^ 匕學處理,與 、θ以重金屬類和戴奥辛類 為土壤成分,藉由與普通 ’亦可使用為水和固化資材。 須掩埋,可再資源化為新素 〇 裂置處理每曰排出之垃圾時, 用為3分之1。2036-4563-PF (N); phoebe.ptd Page 20 512077 V. Description of the invention (18) In addition, the inert gas is used for the reduction reaction according to the scope of the patent application. It can be effective and can inhibit the use of oxygen as a medium. The scope of the patent application is to make the combustion harmless by the reduction reaction processing device. In addition, the raw ash contains physical treatment and is used to stabilize it and become a safe ingredient that pollutes the environment. In addition, the treated raw ash is used in combination with Portland cement, etc. By this, there is no material in the final disposal field, that is, forming a recycling-type society. The use of the treatment of the present invention is more expensive than the use of high-temperature melting. It is noted that under the conditions of low oxygen, Wujinming 'will lead to the generation of harmful substances. … The ancient device of fever in the ashes described in item 6 'has a harmful designated substance contained in ^ ^ ^ dagger treatment, and θ uses heavy metals and dioxins as soil components, and with ordinary' also Can be used as water and curing materials. It must be buried, and it can be re-resourced into a new element. 〇 Splitting treatment is used for one-third of every waste discharged.
2036-4563-PF(N);phoebe.ptd2036-4563-PF (N); phoebe.ptd
512077 圖式簡單說明 第1圖係本發明之燃燒灰燼的原子以擴散分解而無害 化處理方法的流程圖。 iiii 2036-4563-PF(N);phoebe.ptd 第22頁512077 Brief Description of Drawings Figure 1 is a flow chart of the method for treating the ash-burning atoms of the present invention by diffusion and decomposition without harm. iiii 2036-4563-PF (N); phoebe.ptd page 22
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CN102657925B (en) * | 2012-04-12 | 2018-01-05 | 广东省生态环境技术研究所 | The method of heavy metal thermal curing agents and its curing heavy metal based on clay |
CN103042022B (en) * | 2012-12-05 | 2015-11-25 | 广东德诚环保科技有限公司 | A kind of flyash treatment method |
JP5983849B2 (en) * | 2014-12-10 | 2016-09-06 | 栗田工業株式会社 | Automatic sampling apparatus and automatic sampling method for fly ash |
CN107413815A (en) * | 2017-05-11 | 2017-12-01 | 深圳泛科环保产业发展有限公司 | A kind of dechlorination method of chloride material |
CN108526200B (en) * | 2018-04-08 | 2021-07-23 | 成都中节能再生能源有限公司 | Step-by-step fly ash solidification process |
CN109570185B (en) * | 2018-10-19 | 2020-11-27 | 同济大学 | Waste incineration fly ash reduction dechlorination method and device based on water vapor induction |
CN111495520A (en) * | 2019-07-19 | 2020-08-07 | 河北燕岛环保科技股份有限公司 | Waste incineration flue gas treatment device |
CN111359136A (en) * | 2020-04-03 | 2020-07-03 | 连云港新江环保材料有限公司 | Dioxin detoxification chelating agent for fly ash and preparation method thereof |
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