TW201016619A - A process for a fly ash contaminated with a hazardous material be solidificated and stabilizated - Google Patents

A process for a fly ash contaminated with a hazardous material be solidificated and stabilizated Download PDF

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TW201016619A
TW201016619A TW97140773A TW97140773A TW201016619A TW 201016619 A TW201016619 A TW 201016619A TW 97140773 A TW97140773 A TW 97140773A TW 97140773 A TW97140773 A TW 97140773A TW 201016619 A TW201016619 A TW 201016619A
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ratio
fly ash
sludge
heavy metal
solidified body
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TW97140773A
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Chinese (zh)
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Ming-Sheng Ko
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Ying Cheng Environmental Technology Co Ltd
Ming-Sheng Ko
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Abstract

A process for a fly ash contaminated with a hazardous material such as a heavy metal be solidificated and stabilizated. The process is added a classificated incinerator ash, Kaolin and alkali liquer to the fly ash, mixed all of it for 30 minutes as sludge and put the sludge under the circumstance of 45 centigrade degree/100%. Relative Humidity for 2 days, then move it to circumstance of nature for 5 days to solidificated and stabilizated the Lead and Cadmium contaminated in the fly ash.

Description

201016619 九、發明說明: 【發明所屬之技術領域】 鉻 【先前技術】 化為㉗里=垃垃圾以 %。而廢錄㈣焚化觀職,達98.93 物,而其中焚化飛灰中船、鑛等重金屬等副產 ”定標準,而被t歧為有害廢棄物屬廢棄 ^飛t處理方式主要以波特蘭水泥辅以f合劑進行固。』/ ;ΐ"^ ❿ 原2無機聚合物之主要原料化學:成相::二 約產生5%之飛灰,並中所知聽A、獻^廢棄物經焚化處理後 有的另以水泥並添加螯合劑進行固化/釋定彳I 因此, 體之機械強度降低,不利於後續資材化之運用,“: 5 201016619 ϊίίί/ί定有再溶出之虞。而目且其前亦有單獨 口口抗愿強度部無法達到法規標準,且因螫合劑多屈糞剎甚口 ’處ίΐ費用為錢固化/穩定化法之2〜3倍,又部人^ 會/生劣化或腐敗_絲,處^後 之長期穩定性亦有再溶出之疑慮。201016619 IX. Description of the invention: [Technical field to which the invention belongs] Chromium [Prior Art] It is 27 liters = garbage is %. And the waste record (4) incineration and duty, up to 98.93 things, and among them incineration fly ash in the ship, mine and other heavy metal and other by-products set standards, and is classified as hazardous waste is a waste ^ fly t treatment mainly in Portland The cement is supplemented with a mixture of F. 』/ ;ΐ"^ ❿ The main raw material of the original 2 inorganic chemistry: phase:: about 5% of the fly ash, and the knowledge of the A, the contribution of waste After incineration, some cements and chelating agents are added to cure/release 彳I. Therefore, the mechanical strength of the body is reduced, which is not conducive to the subsequent application of materials. “: 5 201016619 ϊ ί ί ί 虞 虞 虞 虞 虞 虞 虞 虞 虞 虞 虞 虞 虞However, there is also a separate oral anti-intentional strength department that cannot meet the regulatory standards, and because the sputum mixture is more sturdy, the sputum is more than 2 to 3 times the cost of the solidification/stabilization method. Will / raw deterioration or corruption _ silk, the long-term stability after the ^ also has doubts about re-dissolution.

CaO及CO 县水/尼時生料中CaC〇3將因高溫分解成 量的二氧化碳,估計每生產—公侧水泥, ijif i、^Hc〇2 ’故利用水泥固化/穩定化焚化飛灰不僅有重 念。而严機聚合物的主姜特性為節能、低三氧化碳排放應高抗壓強 且不須經過高溫的燒結,只需以低於loot 機^合化技術製造出類似陶究結構的材料,可大 ί 幾聚合材料亦可運用於固化及穩定化重金 ,機^合材料固化重金屬的機制包含物理吸附及化學包覆。因 2*二ϋΐ3ί親,污泥資源化做為無機聚合材料,並加以固化/ 理廢棄物」的資源化目標’落實焚化底潰全資源化、零 之目知。 八 ㈣號「廢棄物處理方法」係於廢棄物中加入水 玻,和水進行振盪攪拌將廢棄物中的鉛形成矽酸鉛沉澱令鉛安定化 而達到穩疋化有害重金屬船的目的,惟此發明乃結合水玻璃和水即 矽酸鈉溶液及水與含重金屬廢棄物混合攪拌進行養護固化者,其固 化體之機械強度亦低,不利後續固化體資材化之應用。、 另發明專利第301697號「灰燼之穩定與利用」係有關穩定焚 化器灰燼之方法,步驟為1.將焚化之灰燼由一分離器分離成乾灰 燼,2.導入分離之乾灰燼進入一酸水貯槽與酸水反應洗提出重金屬, 3·取出重金屬溶液經過一重金屬溶液焚化器予以焚化處理收集重金 屬,屬洗提重金屬之專利並未有將重金屬固化或穩定化之機轉報 ^。且在其内容中提及之先前技術方法為丨·送焚化之灰燼至一分離 ,分出雜質及廢鐵,2.轉移分出之灰燼渣至一螯合反應器,將具有定 篁之表面活化劑及乙二胺四乙酸聚合物(ethyieneciiamine tetra acetic acid簡稱EDTA)作為重金屬螯合劑攪拌混合物,固定灰燼渣中重金 201016619 屬以抽離重金屬,4.饋送固定之重金屬至螯合物分離反應容器攪拌混 合由EDTA分出重金屬,5.饋送由螫合物分離反應容器中分出之重 金屬溶液以鹼處理而轉換酸性EDTA,並送回螯合容器回收。其缺 點為1.成本效益不高,2.準備螯合絡合劑極為費時,3.須將分離^酉^ 性EDTA轉成4NaEDTA故設備成本極大。 【發明内容】In CaO and CO County water/Nissan raw materials, CaC〇3 will be decomposed into carbon dioxide by high temperature, and it is estimated that each production-male side cement, ijif i, ^Hc〇2', uses cement to solidify/stabilize incineration fly ash. Have a good thought. The main ginger characteristic of Yanji polymer is energy saving, low carbon monoxide emission should be high pressure resistance and does not need to be sintered at high temperature, and only need to produce a material similar to ceramic structure with lower loot machine technology. A large number of polymeric materials can also be used to cure and stabilize heavy gold. The mechanism for curing heavy metals by mechanical materials includes physical adsorption and chemical coating. Because of 2*2ϋΐ3ί, the resource utilization of sludge recycling as an inorganic polymer material and solidification/remediation of wastes has been implemented. No. VIII (4) "Waste Disposal Method" is to add water glass to the waste, and stir it with water to form a lead bismuth sulphate precipitate in the waste to stabilize the lead and stabilize the harmful heavy metal ship. The invention combines water glass and water, that is, sodium citrate solution and water and heavy metal waste, to cure and solidify, and the solidified body has low mechanical strength, which is unfavorable for subsequent application of the solidified material. Another invention patent No. 301697 "Stabilization and Utilization of Ash" is a method for stabilizing the incinerator ash. The steps are as follows: 1. The incinerated ash is separated into a dry ash by a separator, 2. The separated dry ash is introduced into an acid. The water storage tank reacts with the acid water to wash out the heavy metal. 3. The heavy metal solution is taken out and incinerated by a heavy metal solution incinerator to collect heavy metals. The patent for the heavy metal extraction does not have a machine for solidifying or stabilizing heavy metals. And the prior art method mentioned in the content is: the ash from the incineration to a separation, the separation of impurities and scrap iron, 2. the transfer of the separated ash slag to a chelation reactor, which will have a defined surface Activator and ethyieneciiamine tetra acetic acid (EDTA) as a heavy metal chelating agent to stir the mixture, fix the heavy ash in the ash residue 201016619 genus to extract heavy metals, 4. Feed the fixed heavy metal to the chelate separation reaction vessel The heavy metal is separated by EDTA by stirring and mixing. 5. The heavy metal solution separated from the reaction vessel by the chelating agent is fed with alkali to convert the acidic EDTA, and sent back to the chelating vessel for recovery. The disadvantages are: 1. The cost-effectiveness is not high. 2. It is extremely time-consuming to prepare the chelating complexing agent. 3. The separation of EDTA into 4NaEDTA is extremely costly. [Summary of the Invention]

❿ 本發明所採用之固化劑基材係取自都市廢棄物焚化底渣濕筛污 泥’欲藉由濕篩污泥摻配變高嶺土及鹼性活化液製作無機聚合物, 以固化/穩定化焚化飛灰中Pb、Cd等重金屬,並探討不同Si/Al莫耳 (mole)比、Si02/M20莫耳(mole)比(M=Na、K)及水灰由,對於濕篩污 泥固化/穩定化飛灰中重金屬溶出特性及抗壓強度之影響時^,當 SJ/A1J:匕固定時,飛灰固化體中Pb、cd溶出濃度隨水灰比越大而減 抗壓強度則是隨水灰比越大而減少,當Si/Al比變化時,重金屬 溶^漢度隨Si/Al比增加而減少,抗壓強度則隨Si/A1比增加而增加, 且當Si/Al比為2.93、SiCVMzO比為〇.8〇及水灰比為0.59時,飛灰 〒亡苎中Pb的溶出濃度為3.44mg/l ’ Cd的溶出濃度為〇.84mg/l,遠 始飛灰Pb溶出濃度為49.33mg/l及Cd溶出濃度為3.68mg/l, 固ΐ?之抗壓強度可達89.53kg/cm2。由此結果顯示,利用焚 g底渣濕4污泥固化/穩定化焚化飛灰中重金屬是具有其功效及實用 一 了,聚合物主要是一種似天然沸石之結構,為一由矽、氧及鋁 璃相三元架構,以[也0^1-0-]11之P〇Wsial此)’ 夕:rSl_〇_]n 之 P〇ly(Sialate-Sil〇XO) ’ [-Si-0-A1-〇-Si-〇-Si-〇-li 種架構為主要形式,和水泥最大的不同 之ϊ子平衡之角色。而無機聚合物因具有質 可倣火強Λ大4物理特性’因此能廣泛應用於建材方面, 見好ΐ彳卜裝汊材料等。此外,無機聚合物對於重金屬具有 高嶺土 化學特性潛勢,如Jaarsveld使用燃煤飛灰參配變 機添加咖的銅和_子—同反應,將 錯離ϋ屮忍合出试驗,當產物粒徑破碎至以2/600!^111時, ^間子2=ρριη,銅離子溶出濃度則介於12/30ppm 因=物對於錯離子的固化、敎化效果很好。 發月利用夂化底渣濕篩污泥摻配固定比例的變高嶺土 7 201016619固化 The curing agent substrate used in the present invention is taken from municipal waste incinerated bottom slag wet sifting sludge. 'Inorganic polymer is prepared by mixing wet kaolin with alkaline kaolin and alkaline activation liquid to cure/stabilize. Incineration of heavy metals such as Pb and Cd in fly ash, and discussion of different Si/Al mole ratio, SiO2/M20 mole ratio (M=Na, K) and water ash, for wet sieve sludge solidification / When stabilizing the influence of the dissolution characteristics and compressive strength of heavy metals in fly ash ^, when SJ/A1J: 匕 is fixed, the dissolution concentration of Pb and cd in the fly ash solidified body is larger with the water-cement ratio and the compressive strength is As the water-cement ratio increases, the heavy metal solubility decreases with increasing Si/Al ratio, and the compressive strength increases with the Si/A1 ratio, and when the Si/Al ratio increases. When the ratio of SiCVMzO is 〇.8〇 and the water-cement ratio is 0.59, the dissolution concentration of Pb in the fly ash is 3.44mg/l 'The dissolution concentration of Cd is 84.84mg/l, far-flying ash Pb The dissolution concentration was 49.33 mg/l and the dissolution concentration of Cd was 3.68 mg/l, and the compressive strength of the solid solution was 89.53 kg/cm2. The results show that the use of incineration g-sludge wet 4 sludge solidification / stabilization of heavy metals in the incineration fly ash has its efficacy and practicality. The polymer is mainly a natural zeolite structure, which is composed of bismuth, oxygen and Aluminum glass phase ternary structure, [also 0^1-0-]11 P〇Wsial this) '夕: rSl_〇_]n P〇ly(Sialate-Sil〇XO) ' [-Si-0 The -A1-〇-Si-〇-Si-〇-li structure is the main form, and the role of cement is the biggest difference in the balance of the dice. However, the inorganic polymer can be widely used in building materials because of its high quality and can be used as a building material. In addition, inorganic polymers have the potential for kaolin chemical properties for heavy metals. For example, Jaarsveld uses a coal-fired fly ash blending machine to add copper and _ sub-synthesis, which will be mismatched and tested. When the diameter is broken to 2/600!^111, the ^2 is ρριη, and the copper ion elution concentration is between 12/30ppm. The effect of solidification and deuteration on the wrong ions is good. Using a sulphurized bottom slag wet sieve sludge to mix a fixed ratio of metakaolin 7 201016619

作為無機聚合物之反應基材,並添加鹼性活化液進行聚合反應固化/ 穩定化焚化飛灰令重金屬’以不同Si/Al比、Si02/M20比及水灰比 對飛灰固化體重金屬溶出特性及抗壓強度之影響探討時發現,以其 Si / A1比為2.93 ’ Si(VM2〇比為〇.8〇所得之飛灰固化體之重金屬 =;谷出濃度最低’而以Si / A1比為2.93,Si〇2/M2〇比為0.93所 才寸之飛灰固化體之重金屬Cd溶出濃度最低。顯示於本發明反應參數 之設定下,Si/A1比最大2.93之飛灰固化體,有最佳之重金f Pb、 固化/穩定化效果,而si〇2/M2〇比過大反而會使重金屬pb溶 出?辰度有微幅增加之趨勢’而重金屬Cd溶出濃度,則隨si〇2/M20比 增加,其固化/穩定化效果隨之增加。至於其他重金屬之固化/穩定化 千果,隨著飛灰固化體之配比不同,重金屬Cu&Cr溶出濃度有微 t Ϊ規則之變化,但以整體而言,於Si /A1比相同時,隨著Si02/M20 而微幅增加,但隨著水灰比增加而微幅減少。重金屬Β&之溶 g濃度則大致皆相同,未有隨飛灰固化體配比不同有明顯變化之趨 據此 夕考::土本?!係關於以底渣濕筛污泥固化/穩定化飛灰中重金屬 之所含之有害重金屬,特 枯目ϊ係提供一種—種以底潰濕篩污泥固化/穩定化 H金屬之處理方法’以賴汚泥13〜i4wt%加人焚化飛灰 駐粒應紐聽餘錄,_3。以 再宫=,,、'度100 % (Relative Humidity 簡稱 r.h.)之環境下兩天 再於置放五天以固化/穩定化焚化飛灰中pb、Cd等重金 灰中種以底賴1$污關彳_定化飛 f方法’其反應基材之Si/A1比為2.93者。。 【實施方式】 飛灰ϊί i 污泥、焚化 义底渣濕師巧·泥為南部某焚化底渣濕篩分選廠,經過渴 8 201016619 飛灰為殿分離程序所得之濕篩污泥,焚化 收廒產生之最終混合飛灰。 將其石夕、銘組成比例盥文AJA、Fe2〇3等氧化物。 相,因此將焚化底料篩污泥Sl〇2為主要組成晶 而焚化飛灰特性分析結果則以C 應=。 序為Si〇2、ΑΙΑ、κ20及Na7〇,右最多’其次依 0.37% ’另由基本晶相分析結果$量則佔有 筛污泥相較,雖U飛灰1有飛灰f變,土及濕 有易與無機聚合物原料物種U應之仏而可推知焚化飛灰應具As a reaction substrate of an inorganic polymer, an alkaline activation solution is added to carry out polymerization reaction solidification/stabilization of incineration fly ash to make heavy metal 'dissolve the fly ash solidified metal with different Si/Al ratio, SiO 2 /M 20 ratio and water cement ratio The influence of the characteristics and compressive strength was found to be Si/A1 with a Si / A1 ratio of 2.93 'Si (the heavy metal of the fly ash solidified body obtained by VM2 〇.8〇; the lowest bark concentration) The ratio of the heavy metal Cd dissolution of the fly ash solidified body with a ratio of 2.93 and Si〇2/M2 〇 is 0.93, which is the lowest, and shows the fly ash solidified body with a Si/A1 ratio of 2.93 at the setting of the reaction parameters of the present invention. There is the best heavy gold f Pb, curing / stabilizing effect, and the si〇2/M2 〇 ratio is too large, but will make the heavy metal pb dissolve? The degree of slight increase in the 'thickness' and the heavy metal Cd dissolution concentration, then with si〇2 As the ratio of /M20 increases, the curing/stabilizing effect increases. As for the solidification/stabilization of other heavy metals, the dissolution ratio of heavy metal Cu&Cr has micro-t Ϊ rule change with the different ratio of fly ash solidified body. , but overall, when the ratio of Si / A1 is the same, with Si02/M 20 and slightly increased, but decreased slightly with the increase of water-cement ratio. The concentration of dissolved metal in heavy metal Β & is almost the same, there is no obvious change with the proportion of fly ash solidified body. : 土本?!About the harmful heavy metals contained in the solids in the bottom slag wet-sludge sludge solidification/stabilized fly ash, the special chlorpyrifos provides a kind of bottom-cracking sludge solidification/stabilization H The metal treatment method 'to the sludge 13~i4wt% plus incineration fly ash granules should be heard, _3. In the environment of Remiya =,,, '100% (Relative Humidity referred to rh) for two days After placing for five days to solidify/stabilize the incineration fly ash, the heavy gold ash such as pb and Cd is the same as the base material. The Si/A1 ratio of the reaction substrate is 2.93. [Embodiment] Fly ash ϊ i i sludge, incineration slag slag wet teacher Qiao · mud for the southern incineration bottom slag wet sifting and sorting plant, through the thirst 8 201016619 fly ash for the wet separation sludge obtained from the separation process, The final mixed fly ash produced by incineration and enrichment. The composition of Shi Xi and Ming is composed of oxides such as AJA and Fe2〇3. The incineration primer sludge Sl2 is the main constituent crystal and the incineration fly ash characteristic analysis results are as follows: C should be =. The order is Si〇2, ΑΙΑ, κ20 and Na7〇, and the right is the most 'secondary according to 0.37%' The results of the basic crystal phase analysis are compared with the amount of sieve sludge. Although the U fly ash 1 has fly ash f change, the soil and wet easily react with the inorganic polymer raw material species U, and it can be inferred that the incineration fly ash should be

Cd 49.33 一 1 Μ 1.23 0.90 - 5.0 1.0 PPm 焚化飛灰 濕篩污泥 _ TCLP管制標準 1〇〇 註:’’-”表示濃度低於O.lppm 201016619 主要始ίίίϊίί及f相分析可知,濕筛污泥以_為 之潛勢,焚化飛灰雖 γ CaO為主但因具有少置矽、鋁,而推測焚 合物原料物㈣產生反應之特性4由原 結果顯示,焚化灰重金屬溶出濃度以出2 ft應能對焚化飛灰中重金屬/穩定化^ϊίίί ilrn^ 物,取^污泥、焚化飛灰及變高嶺土相體反應 參 實驗程圖(詳參第1圖)之步驟製作固 抑ΐ固化體置於45c/i〇〇%r.h.下兩天以及室溫下五天後,再 將製作完成之固化體移入乾燥箱中保存以待後續分析。 …斗f種毒性特性溶出試驗(tclp)、结果發現,濕 師巧尼之浴出试驗結果中,只以Cr、〇1及pb有少量溶出,但豆溶 f,並不具環境危害性。而焚化飛灰則心匕 及Cd之洛出濃度为別為49.33mg/l及1.23mg/l超過法規標準,J:中 以Pb超出法規標準甚多,應進行固化/穩定化處理。 八 以下以實施例詳細說明本發明; 實施例一Cd 49.33 一1 Μ 1.23 0.90 - 5.0 1.0 PPm Incineration fly ash wet sieve sludge _ TCLP control standard 1 〇〇 Note: ''-' indicates that the concentration is lower than O.lppm 201016619 Mainly ίίίίίί and f phase analysis shows that wet sieve The sludge has a potential of _, and the incineration fly ash is mainly γ CaO, but because of the low bismuth and aluminum, it is speculated that the characteristics of the reaction of the incineration raw material (4) are shown by the original results, and the dissolved concentration of the incinerated ash heavy metal is 2 ft should be able to produce heavy solids in the incineration fly ash heavy metal / stabilized ^ ϊ ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί After the solidified body is placed at 45c/i〇〇%rh for two days and at room temperature for five days, the finished solidified body is transferred to a dry box for later analysis. The toxic characteristic dissolution test (tclp) The results showed that in the test results of the wet teacher's bath, only a small amount of Cr, 〇1 and pb were dissolved, but the bean soluble f was not environmentally harmful. The incineration fly ash was palpitations and Cd. The concentration is 49.33mg/l and 1.23mg/l exceeding the regulatory standards, J: Pb very much higher than the legal standards, should solidification / stabilization process in the following eight embodiments of the present invention will be described in detail; Example a

以46wt°/〇焚化飛灰、17wt%濕篩汚泥及變高嶺土等再加入矽酸 納及NaOH溶液混合攪拌,其si/Al比、Si02/M20比各如表3。 實施例二 以40wt%焚化飛灰、15wt%濕篩汚泥及變高嶺土等再加入矽酸 納及NaOH溶液混合攪拌,其&/Α1比、si〇2/M2〇比及水灰比各如 表3 〇 實施例三 以36加%焚化飛灰、14wt%濕篩汚泥及變高嶺土等再加入石夕酸 納及NaOH溶液混合攪拌,其si/Al比、Si02/M20比及水灰比各如 表3。 實施例四 201016619 以43wt%焚化飛灰、i6wt%濕篩汚泥及變高嶺土等再加入石夕酸 納及NaOH溶液混合攪拌,其Si/Ai比、Si〇2/M2〇比及水灰比各如 表3。 實施例五 以38wt%焚化飛灰、i5wt%濕篩汚泥及變高嶺土等再加入矽酸 納及NaOH溶液混合攪拌,其Si/Al比、Si02/M2〇比及水灰比各如 表3。 實施例六The mixture of 46 wt%/〇 incineration fly ash, 17 wt% wet sieve sludge and metakaolin was added with sodium citrate and NaOH solution, and the ratio of si/Al ratio and SiO 2 /M20 was as shown in Table 3. In the second embodiment, 40 wt% incineration fly ash, 15 wt% wet sieve sludge and metakaolin are added and mixed with sodium citrate and NaOH solution, and the ratio of &/Α1 ratio, si〇2/M2 ratio and water-cement ratio are as follows. Table 3 〇 Example 3 with 36%% incineration fly ash, 14wt% wet sieve sludge and metakaolin, etc. and then added with sodium silicate and NaOH solution mixed with stirring, its si/Al ratio, SiO2/M20 ratio and water-cement ratio As shown in Table 3. Example 4 201016619 43 wt% incineration fly ash, i6 wt% wet sieve sludge and metakaolin, etc., and then mixed with sodium silicate and NaOH solution, the Si/Ai ratio, Si〇2/M2 ratio and water-cement ratio As shown in Table 3. Example 5 38 wt% incineration fly ash, i5 wt% wet sieve sludge and metakaolin were added and mixed with sodium citrate and NaOH solution, and the Si/Al ratio, the SiO 2 /M 2 enthalpy ratio and the water-cement ratio were as shown in Table 3. Embodiment 6

以34wt°/〇焚化飛灰、I3wt%濕篩汚泥及變高嶺土等再加入矽酸 納及NaOH溶液混合攪拌,其Si/Al比、Si〇2/M2〇比及水灰比各如 表3。 實施例七 以42wt%焚化飛灰、I6wt%濕篩汚泥及變高嶺土等再加入矽酸 納及NaOH溶液混合攪拌,其Si/Al比、Si02/M20比及水灰比各如 表3。 實施例八 以37wt%焚化飛灰、l4wt%濕篩污泥及變高嶺土等再加入矽酸 納及NaOH溶液混合攪拌,其Si/Al比、Si02/M2〇比及水灰比各如 表3。 實施例九 以33wt%焚化飛灰、13wt%濕篩污泥及變高嶺土等再加入石夕酸 納及NaOH溶液混合攪拌,其Si/Al比、Si〇2/M2〇比及水灰比各如 201016619 -... -.......飛灰固化體之凝 诚_)ΐ 樣品 焚化飛灰(知 濕篩污泥(%) Si/Al 比 Si(VM20 比 水灰比 實施例1 46 ] 17 1.88 0.54 0.33 眚施例2 40 H 15 2.40 0.93 0.39 實施例3 36 14 2.93 1.22 0.45 實施例4 43 16 1.88 0.38 0.40 實施例5 38 _ 15 2.40 0.68 0.46 實施例6 34 13 2.93 0.93 0.51 實施例7 42 16 1.88 0.32 0.47 實施例8 「37 14 2.40 0.58 0.53 實施例9 33 13 2.93 0.80 0.59 录3 ,3,、第4圖及第5圖以及表4分別為Si / A1比a組中之 1 t f2.40及C組中之2·93的飛灰固化體,於不同Si〇2/M20 度變化趨勢圖。經過比較後發現,#飛灰固化 Si/A1比=1·88為例(請參第3圖),重金屬 Γ之广2度USlCVM2°比增加由6mg/1增加為19喊’ Cd、 員,但仍可看出cd&cu有略為增加, ^及Ba财略為減少趨勢,且隨Si/A1比越大,此變化趨勢越 明顯° 樣品 固化體; 焚涵灰(%] 乙組成(Si/Al) [1篩污泥(%)j t固定 —Si/Al 卜 h Si〇2/M20 比 a 實施例1 46 17 1.88 〇 54 實施例4 _ 43 16 1 88 π QQ 實施例7 .42 — 0.32 b 實施例2 —40 15 2.4Π 0〇3 實施例5 __ 38 15 24-D 〇6R 實施例8 37 14 Lmj 0.58 c 實施例3 _ 36 14 293 1 99 實施例6 34 13 2^3 〇g^ 實施例9 33 13 L-2.93 V/ mJ 0.80 表4 12 201016619 此外,當飛灰固化體之Si/Al比改變時,以實施例1/實施例2/ 實施例3之飛灰固化體於si/A1比由1.88增加至2.93為例,重金屬 Pb 及 Cd 溶出量分別為 18.99 / 16.90 / 13.90mg/l 以及 2.98 / 2.66 / 2.15mg/卜皆有隨Si / A1比越大,溶出濃度越低之趨勢。上述重金 屬溶出濃度變化趨勢於實施例4〜實施例6以及實施例〜實施例9皆 有相同結果。The mixture of 34wt ° / 〇 incinerated fly ash, I3wt% wet sieve sludge and metakaolin was added with sodium citrate and NaOH solution, and the Si/Al ratio, Si〇2/M2 ratio and water-cement ratio were as shown in Table 3. . Example 7 42 wt% incineration fly ash, I6 wt% wet sieve sludge and metakaolin were added and mixed with sodium citrate and NaOH solution, and the Si/Al ratio, the SiO 2 /M 20 ratio and the water-cement ratio were as shown in Table 3. In the eighth embodiment, 37 wt% incineration fly ash, 14 wt% wet sieve sludge and metakaolin are added and mixed with sodium citrate and NaOH solution, and the Si/Al ratio, the SiO 2 /M 2 enthalpy ratio and the water-cement ratio are as shown in Table 3. . In the ninth embodiment, 33 wt% incineration fly ash, 13 wt% wet sieve sludge and metakaolin are added and mixed with sodium silicate and NaOH solution, and the Si/Al ratio, Si〇2/M2 ratio and water-cement ratio are respectively mixed. For example, 201016619 -... -....... ash solidified body _ _ ΐ sample incineration fly ash (known wet sieve sludge (%) Si / Al ratio Si (VM20 than water cement ratio example 1 46 ] 17 1.88 0.54 0.33 眚 Example 2 40 H 15 2.40 0.93 0.39 Example 3 36 14 2.93 1.22 0.45 Example 4 43 16 1.88 0.38 0.40 Example 5 38 _ 15 2.40 0.68 0.46 Example 6 34 13 2.93 0.93 0.51 Example 7 42 16 1.88 0.32 0.47 Example 8 "37 14 2.40 0.58 0.53 Example 9 33 13 2.93 0.80 0.59 Record 3, 3, 4 and 5 and Table 4 are respectively in the Si / A1 ratio a group 1 t f2.40 and the 2.93 fly ash solidified body in the C group showed different trend trends in different Si〇2/M20 degrees. After comparison, it was found that #fly ash solidified Si/A1 ratio=1·88 was For example (please refer to Figure 3), the weight of the heavy metal US 2 degree USlCVM2 ° increase from 6mg / 1 increased to 19 shout 'Cd, member, but still can be seen that cd & cu has a slight increase, ^ and Ba financial slightly reduced trend, The larger the ratio of Si/A1, the more obvious this trend is. The sample solidified body; the burned ash (%) B composition (Si/Al) [1 sieve sludge (%) jt fixed - Si / Al Bu h Si〇 2 /M20 ratio a Example 1 46 17 1.88 〇 54 Example 4 _ 43 16 1 88 π QQ Example 7.42 - 0.32 b Example 2 - 40 15 2.4 Π 0 〇 3 Example 5 __ 38 15 24-D 〇6R Example 8 37 14 Lmj 0.58 c Example 3 _ 36 14 293 1 99 Example 6 34 13 2^3 〇g^ Example 9 33 13 L-2.93 V/ mJ 0.80 Table 4 12 201016619 In addition, when flying When the Si/Al ratio of the ash-cured body is changed, the fly ash solidified body of Example 1/Example 2/Example 3 is increased from 1.88 to 2.93 in the si/A1 ratio, and the amount of heavy metal Pb and Cd eluted is 18.99, respectively. / 16.90 / 13.90mg / l and 2.98 / 2.66 / 2.15mg / b have a tendency to decrease with the Si / A1 ratio, the lower the dissolution concentration. The above-mentioned heavy metal dissolution concentration change tendency was the same as in Examples 4 to 6 and Examples to Example 9.

因此’由飛灰固化體之重金屬溶出實驗結果可知,濕篩污泥製 作之飛灰固化體,對於焚化飛灰中重金屬之固化/穩定化效率,是受 固化體組成之Si/A1比之影響較為顯著,重金屬溶出濃度於固化體 之Si/Al比固定時,會隨著Si02/M20比增加而增加,若固化體之 Si/Al比改變時’則會隨Si/Al比增加而減少,且不同重金屬也有 不同之變化趨勢。 再比較飛灰固化體在不同水灰比之重金屬溶出濃度變化趨勢, 如第6圖、第7圓及第8圖分別為Si / A1比a組中之1.88、b組中 之2.40及c組中之2.93之飛灰固化體於不同水灰比對各重金屬溶出 濃度變化趨勢圖,當飛灰固化體中Si / A1比相同時,以Si / A1比=1.88 為例,重金屬Pb之溶出濃度隨著水灰比增加由Dmg/丨減少為 6mg/卜Cd、Cu、Cr及Ba雖然變化不明顯,但仍可看出Cd及Cu 有略為減少趨勢而Cr及Ba則有略為增加之趨勢,且變化趨勢同樣 隨Si/Al比越大而越明顯,與飛灰固化體於不同si〇2/M2〇比之重金 屬溶出濃度變化圖(第6圖、第7圖及第8圖)相同。 而當飛灰固化體之Si / A1比改變時,以實施例丨/實施例2/實施 例3之飛灰固化體於Si/Al比由1.88增加至2.93為例,Pb及Cd溶 出量分別為 18.99/16.90/13.90mg/l 以及 2.98/2.66/2.15mg/l,皆有 隨Si/A1比越大’溶出濃度越低之趨勢,且當Si/Ai比為2 時, 重金屬Pb由原始溶出值為49.33mg/l降至i3.9〇mg/卜隨著水灰比辦 加,再降至3.95及3.44,低於法規限值(5mg/1),已確實逵丨^ 飛灰中重金屬固化/穩定化之效果。 a 因此,經由整體比較之結果發現,以實施例9配比,其Si /A1 士 為2.93,SKVMzO比為0.80所得之飛灰固化體之重金屬'p 度最低,而以實施例6配比,其Si/Al比為2.93,Si02/M,0 ί 〇.l所得之飛灰隨體之重金屬〇i溶出濃度最低。“本2發比;J 應參數設定下,Si/Al比最大(2.93)之飛灰固化體’有最佳 13 201016619Therefore, it can be seen from the results of the heavy metal dissolution test of the fly ash solidified body that the solidification/stabilization efficiency of the heavy metal in the incineration fly ash is affected by the Si/A1 ratio of the solidified body composition. It is more remarkable that the concentration of heavy metal dissolved in the solidified body increases with the Si/Al ratio, and increases as the Si/Al ratio of the solidified body decreases as the Si/Al ratio changes. And different heavy metals also have different trends. Then compare the trend of the dissolution concentration of heavy metals in the fly ash solidified body at different water-cement ratios. For example, Figure 6, Figure 7, and Figure 8 are respectively 1.88 of the Si / A1 ratio a group, 2.40 and the group c of the b group. In the case of 2.93 fly ash solidified body, the concentration trend of each heavy metal dissolution concentration is different. When the Si / A1 ratio in the fly ash solidified body is the same, the dissolution ratio of heavy metal Pb is taken as Si / A1 ratio = 1.88. As the water-cement ratio increased from Dmg/丨 to 6 mg/b Cd, Cu, Cr and Ba, although the change was not obvious, it can be seen that Cd and Cu have a slight decrease trend, while Cr and Ba have a slight increase trend. The change trend is also more obvious as the Si/Al ratio is larger, which is the same as the heavy metal dissolution concentration change diagram (Fig. 6, Fig. 7, and Fig. 8) of the fly ash solidified body at different si〇2/M2 turns ratio. When the Si / A1 ratio of the fly ash solidified body is changed, the fly ash solidified body of Example 丨 / Example 2 / Example 3 is increased from 1.88 to 2.93 in the Si/Al ratio, and the Pb and Cd elution amounts are respectively The ratio of 18.99/16.90/13.90 mg/l and 2.98/2.66/2.15 mg/l has a tendency to decrease as the ratio of Si/A1 increases, and when the Si/Ai ratio is 2, the heavy metal Pb is original. The dissolution value is 49.33mg/l and down to i3.9〇mg/b. With the water-cement ratio, it drops to 3.95 and 3.44, which is lower than the regulatory limit (5mg/1). Heavy metal curing / stabilization effect. a Therefore, as a result of the overall comparison, it was found that the Si/A1 of the composition of Example 9 was 2.93, and the fly ash solidified body obtained by the SKVMzO ratio of 0.80 had the lowest 'p degree, and the ratio of Example 6 was The Si/Al ratio is 2.93, and the concentration of the heavy metal 〇i dissolved in the fly ash with SiO2/M,0 ί 〇.l is the lowest. "This 2 round ratio; J is the best setting for the fly ash solidified body with the largest Si/Al ratio (2.93) according to the parameter setting. 13 201016619

Pb、Cd之固化/穩定化效果,而Si〇2/M20比過大反而會使重金屬 Pb溶出濃度有微幅增加之趨勢,而重金屬cd溶出濃度,則隨 SiCVl^O比增加’其固化/穩定化效果隨之增加。 至於其他重金屬之固化/穩定化效果,隨著飛灰固化體之配比不 同,重金屬Cu及Cr溶出濃度有微小不規則之變化。但以整體而言, 於Si/Al比相同時,隨著Si〇2/M2〇比增加而微幅增加,但隨著水 灰比增加反而微幅減少。重金屬Ba之溶出濃度則大致皆相同,未有 隨飛灰固化體配比不同有明顯變化之趨勢。 次由第9圖可知,當Si/Al比相同時,以Si/Al比=1.88為例(實 施例1、實施例4及實施例7相較),隨著Si02/M20比越大,固化 體之抗壓強度越A ’ Si/Al比為2.4〇及Z93時,抗壓強皮於實施例 2、實施例5、實施例8及實施例3、實施例6、實施例9隨著Si02/M20 β 比越大而增加。若以Si/Al比之變化進行比較,則發現當si/Ai比由 1.88增加至2.93,抗壓強度由最低之8.87 Kg/cm2增加至最高值89.53The curing/stabilizing effect of Pb and Cd, while the Si〇2/M20 ratio is too large, the concentration of heavy metal Pb will increase slightly, while the concentration of heavy metal cd will increase with the ratio of SiCVlO. The effect is increased. As for the solidification/stabilization effect of other heavy metals, as the ratio of the fly ash solidified bodies is different, there are slight irregular changes in the dissolution concentrations of heavy metals Cu and Cr. However, as a whole, when the Si/Al ratio is the same, it increases slightly as the Si〇2/M2 ratio increases, but decreases slightly as the water-cement ratio increases. The dissolution concentration of heavy metal Ba is almost the same, and there is no obvious change with the ratio of fly ash solidified body. As can be seen from Fig. 9, when the Si/Al ratio is the same, the Si/Al ratio = 1.88 is taken as an example (comparison of Example 1, Example 4 and Example 7), and the solidification is performed as the ratio of SiO 2 / M 20 is larger. When the compressive strength of the body is A'Si/Al ratio is 2.4〇 and Z93, the compressive skin is in the embodiment 2, the embodiment 5, the embodiment 8 and the embodiment 3, the embodiment 6, and the embodiment 9 along with the SiO 2 . The /M20 β ratio increases as the ratio increases. If the Si/Al ratio is compared, it is found that when the si/Ai ratio is increased from 1.88 to 2.93, the compressive strength is increased from the lowest of 8.87 Kg/cm2 to the highest value of 89.53.

Kg/cm2,顯示飛灰固化體之抗壓強度有隨Si/A1比增加而增加之趨 ° 另由第10圖可見’當Si/Al比相同時,以Si/Al比=1.88為例(實 施例1、實施例4及實施例7相較),隨著水灰比越大,抗壓強度卻 越小’ Si/Al比=2.40及2.93時,抗壓強度於實施例2、實施例5、 實施例8及實施例3、實施例6、實施例9卻有隨水灰比先減後辦之 趨勢。若以Si/Al比之變化進行比較,則發現當Si/A1比由188曰妗 加至2 93 ’抗壓強度於最大水灰比(0.59)時有最大抗壓強度值(89g Kg/cm),此結果與固化體於不同Si02/M20比之變化結果相同,顯 灣 示飛灰固化體之抗壓強度有隨Si/Al比增加而增加之趨勢。此外二 當固化體SiCVl^O比相同(實施例2與實施例6)時,水灰比較大 (0.51>0.39)之固化體抗壓強度值略大(55.98Kg/cm2>55.178 Kg/em2)。Kg/cm2, which shows that the compressive strength of the fly ash solidified body increases with the increase of the Si/A1 ratio. It can be seen from Fig. 10 'When the Si/Al ratio is the same, the Si/Al ratio = 1.88 is taken as an example ( In the first embodiment, the fourth embodiment and the seventh embodiment, the compressive strength is smaller as the water-cement ratio is larger. When the Si/Al ratio is 2.40 and 2.93, the compressive strength is in the second embodiment. 5. Example 8 and Example 3, Example 6, and Example 9 have a tendency to decrease after the water-cement ratio is first reduced. If the Si/Al ratio is compared, it is found that the maximum compressive strength value (89 g Kg/cm) is obtained when the Si/A1 ratio is increased from 188 2 to 2 93 ′ at the maximum water-cement ratio (0.59). The result is the same as that of the cured body at different ratios of SiO 2 / M 20 , and the pressure resistance of the fly ash solidified body increases with the increase of the Si/Al ratio. In addition, when the ratio of the solidified body SiCVlO is the same (Example 2 and Example 6), the compressive strength of the cured body having a relatively large water ash (0.51 > 0.39) is slightly larger (55.98 Kg/cm2 > 55.178 Kg/em2). ).

由以上結果顯示,固化體之抗壓強度值於相同Si/Al比時整體 趨勢隨SiCVl^O比增加而減少’但隨水灰比增加而增加;不同Si/A1 比時,整體趨勢隨Si/Al比增加而增加;相同si〇2/M20比時,水灰 比較大之固化體抗壓強度值略大。因此推測若固化體製作時之g 比越大,或是Si/Al比越大時’反應原始物種中所含;g夕、銘量隨 多’使得固化體結構越易形成,固化體之聚合程度也隨之辦 此飛灰固化體抗壓強度值隨之增加。 a U 綜合飛灰固化體於重金屬溶出濃度及抗壓強度之結果可知,飛 14 201016619 灰固化體之重金屬固化/穩定化,於相同Si/Al比時,受到s 比及水灰比影響’當水灰比越大’反應原始物種中石夕、六2 2 多,飛灰固化體之結構強度(抗壓強度)越大,因而較無鸶 力或f外在環境之破壞影響飛灰固化體之特性,對於播 重金屬固化、穩定化能力則越大。而Si/A1比 強度越大所造J。 屬為辰度越小’廷是因為固化體的結構 201016619 【圖式簡單說明】 第1圖. 本發明以紐闕污朗化/狱化驗巾f金廣之處理 概略流程圖。 第2圖. 本發明之底>查濕_污泥,飛灰之晶相分析圖。 第3圖. 本發明以底渣濕篩污泥固化/穩定化飛灰中重金屬之處理 - 方法Si/Al比為188之a組中飛灰固化體於不同From the above results, the overall compressive strength of the cured body decreases with the increase of SiCVlO ratio at the same Si/Al ratio, but increases with the increase of water-cement ratio; when Si/A1 ratio is different, the overall trend follows Si. The ratio of /Al increases with the increase; when the ratio of si〇2/M20 is the same, the compressive strength of the solidified body with a larger water ash is slightly larger. Therefore, it is presumed that if the ratio of g at the time of production of the solidified body is larger, or the ratio of Si/Al is larger, the content of the reaction is contained in the original species, and the amount of the cured body is more easily formed. The degree of compressive strength of the fly ash solidified body is also increased accordingly. a U composite fly ash solidified body results in heavy metal dissolution concentration and compressive strength. It can be seen that the heavy metal solidification/stabilization of the fly ash 2010 201019 ash solidified body is affected by the s ratio and the water-cement ratio at the same Si/Al ratio. The larger the water-cement ratio is, the more the structural strength (compressive strength) of the fly ash solidified body is, the more the structural strength (compressive strength) of the fly ash solidified body is, so the damage of the fly ash solidified body is affected by the damage of the external environment. The characteristics are greater for the curing and stabilization of the heavy metal. The Si/A1 ratio is stronger than that of the J. The smaller the Chen is, the smaller the court is because of the structure of the solidified body. 201016619 [Simple description of the drawing] Fig. 1. The present invention is a rough flow chart of the treatment of the smear of the smear. Fig. 2. The bottom of the present invention> The wet phase _ sludge, fly ash crystal phase analysis chart. Figure 3. Treatment of heavy metals in solid ash sludge solidification/stabilized fly ash by bottom slag - Method for the formation of fly ash solidified body in group 148 with Si/Al ratio of 188

SiCVMzO比對各重金屬溶出濃度變化趨勢圖。 β 第4圖. 本發明以底渣濕篩污泥固化/穩定化飛灰中重金屬之處理 方法之Si/Α1比為2.4〇之〇組中飛灰固化體於不同SiCVMzO compares the trend of the dissolution concentration of each heavy metal. β Figure 4. The present invention uses a bottom slag wet sieve sludge solidification/stabilization of heavy metals in fly ash. The Si/Α1 ratio of the method is 2.4 〇.

SiCVM2。比對各重金屬溶出濃度變化趨勢圖。 第5圖. 本發明以底渣濕篩污泥固化/穩定化飛灰中重金屬之處理 方法Si/Al比為2.93之e組中飛灰固化體於不同SiCVM2. Compare the trends of the concentration of each heavy metal dissolution concentration. Figure 5. Treatment of heavy metals in fly ash solidified sludge solidification/stabilized fly ash according to the present invention. The fly ash solidified body in the e group with a Si/Al ratio of 2.93 is different.

SiCVlvtO比對各重金屬溶出濃度變化趨勢圖β 第6圖. φ 本發明以底渣濕篩污泥固化/穩定化飛灰中重金屬之處理 方法Si/Α1比為1.88之b組中飛灰固化體於不同水灰 比對各重金屬溶出濃度變化趨勢圖。 第7圖. 本發明以底渣濕篩污泥固化/穩定化飛灰中重金屬之處理 方法Si/Al比為2.40之d組中飛灰固化體於不同水灰 比對各重金屬溶出濃度變化趨勢圖。 第8圖. 本發明以底漬濕篩污泥固化/穩定化飛灰中重金屬之處理 方法Si/Al比為2.93之f組中飛灰固化體於不同水灰 201016619 比對各重金屬溶出濃度變化趨勢囷。 第9圖. 本發明以底渣濕篩污泥固化/穩定化飛灰中重金屬之處理 方法之為飛灰固化體七天的抗壓強度值於不同Si〇2/j^2〇 比之變化趨勢圖。 第10圖. 本發明以底渣濕篩污泥固化/穩定化飛灰中重金屬之處理 方法之為飛灰固化體七天的抗壓強度值於不同水灰比之 變化趨勢圖。_ - 【主要元件符號說明】 ❹ 17SiCVlvtO aligns the concentration trend of each heavy metal dissolution concentration. Fig. 6 Fig. φ The method for treating heavy metals in the bottom slag wet sieve sludge solidification/stabilized fly ash according to the invention The Si/Α1 ratio is 1.88 b in the fly ash solidified body A plot of the change in the concentration of each heavy metal in different water-cement ratios. Fig. 7. The treatment method of the heavy metal in the bottom slag wet sieve sludge solidification/stabilized fly ash The variation trend of the dissolution concentration of each heavy metal in the water-cement ratio of the fly ash solidified body in the d/Al ratio of 2.40 Figure. Fig. 8. The treatment method for the heavy metal in the solidification/stabilized fly ash of the bottom wet staining sludge in the present invention. The fly ash solidified body in the f group with the Si/Al ratio of 2.93 is compared with the different gold metal dissolution concentration in different water ash 201016619. Trends are rampant. Figure 9. The treatment method of the heavy metal in the solid residue sludge solidification/stabilized fly ash according to the present invention is the change trend of the compressive strength value of the fly ash solidified body for seven days in different Si〇2/j^2 ratio. Figure. Fig. 10 is a diagram showing the change of the compressive strength value of the fly ash solidified body in the fly ash solidified body in different water-cement ratios by the method of treating the heavy metal in the fly ash sludge solidification/stabilized fly ash. _ - [Main component symbol description] ❹ 17

Claims (1)

201016619 十、申請專利範圍: 1. 一種以底渣濕篩污泥固化/穩定化焚化飛灰中重金屬之處理方 法,其特徵在於; 在濕篩汚泥13〜14wt%加入焚化飛灰33〜36wt%中添加變高 嶺土等反應基材及驗性活化液,混拌3〇分鐘置於451/10()0/^ r.h.兩天,再於室溫置放五天以固化、穩定化焚化飛灰中孙、 Cd等重金屬。 2. 如申清專利範圍第1項所述之以底渣濕篩污泥固化、穩定化 飛灰中重金屬之處理方法,其反應基材之別/八丨比為f93者。 3. 如申請專利範圍第丨項所述之底渣濕篩污泥固化、穩定化飛 ❿ 灰中重金屬之處理方法,其反應基材之Si02/M20 ^兔 0.80〜0.93者。 待 圍Ϊ 1項所述ί以底渣_污泥固化、穩定化 f中重金屬之處理方法,其反絲材之水灰比為Q 5i〜〇 59 者"〇201016619 X. The scope of application for patents: 1. A method for treating heavy metals in a solidified sludge in a bottom slag wet-sludge sludge stabilization/stabilization incineration fly ash, characterized in that: 13~14wt% of the wet-sludge sludge is added to the incineration fly ash 33~36wt% The reaction substrate such as metakaolin and the test activation liquid were added, mixed for 3 minutes, placed at 451/10()0/^ rh for two days, and then placed at room temperature for five days to solidify and stabilize the incineration fly ash. Sun, Cd and other heavy metals. 2. For the treatment of heavy metals in the bottom slag wet-sludge sludge solidified and stabilized fly ash as described in item 1 of the patent scope, the reaction substrate/eighth ratio is f93. 3. For the treatment of the bottom slag wet-sludge sludge solidification and stabilization of the heavy metals in the fly ash as described in the scope of the patent application, the reaction substrate is SiO 2 / M 20 ^ rabbit 0.80 to 0.93. The method of treating the heavy metal in the bottom slag_sludge solidification and stabilization f, the water-cement ratio of the reverse wire material is Q 5i~〇 59
TW97140773A 2008-10-24 2008-10-24 A process for a fly ash contaminated with a hazardous material be solidificated and stabilizated TW201016619A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI413627B (en) * 2010-09-07 2013-11-01 Univ Nat Taipei Technology Alkali activated pulp
CN113371807A (en) * 2021-06-24 2021-09-10 安徽海螺建材设计研究院有限责任公司 Treatment system and method for desulfurization wastewater for full absorption and full degradation of materials

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI413627B (en) * 2010-09-07 2013-11-01 Univ Nat Taipei Technology Alkali activated pulp
CN113371807A (en) * 2021-06-24 2021-09-10 安徽海螺建材设计研究院有限责任公司 Treatment system and method for desulfurization wastewater for full absorption and full degradation of materials

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