TW200426130A - Manufacturing method and product of resource regenerated cement for construction material - Google Patents

Manufacturing method and product of resource regenerated cement for construction material Download PDF

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Publication number
TW200426130A
TW200426130A TW093120583A TW93120583A TW200426130A TW 200426130 A TW200426130 A TW 200426130A TW 093120583 A TW093120583 A TW 093120583A TW 93120583 A TW93120583 A TW 93120583A TW 200426130 A TW200426130 A TW 200426130A
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TW
Taiwan
Prior art keywords
cement
resource
manufacturing
recycling
item
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TW093120583A
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Chinese (zh)
Inventor
Jin-Shou Chang
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Jin-Shou Chang
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Priority to TW093120583A priority Critical patent/TW200426130A/en
Publication of TW200426130A publication Critical patent/TW200426130A/en

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding

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  • Processing Of Solid Wastes (AREA)

Abstract

This invention relates to a manufacturing method and product of resource regenerated cement for construction material. The method mainly uses bottom ash and fly ash generated from garbage cremation and sludge generated from waste water treatment as regeneration raw material and combines with a regeneration pretreatment process, a homogenizing process, a sintering process, a recycling process and a crushing grinding process, which comprises manufacturing metal-free granular raw material from the regenerated raw material, preparing raw material chemical composition, manufacturing dechlorinated and detoxicated clinker, recycling toxic material and grinding to produce powdery cement so that regenerated construction cement article with the same quality as conventional Portland cement can be obtained for the application on general civil engineering work such as park path paving, retaining wall construction, sea bank construction, wave breaking block production, concrete brick, conduit cover and side ditch, as well as construction material for conventional architectural structure.

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200426130 九、發明說明: 【發明所屬之技術領域】 本發明係涉及一種資源再生建材水泥之製造方法及其製成 品,乃係涉及利用廢棄灰、泥再生製作水泥的技術領域,特別是指 一種利用垃圾焚化所產生之底灰、飛灰以及污水處理產生之污泥為 主要再生原料,經本方法之技術製程,得製作獲得無毒性、去除氣 化物與金屬物質,且可獲得與普通波特蘭水泥同等品質之再生建材 水泥製造方法及其製成品。 【先前技術】 按,目前對於國民日常生活所產生之垃圾,在處理上可分為掩 埋法與焚化法。其中該掩埋法,必需具備有一相當大的掩埋地域位 置,將垃圾直接依序的傾倒後,在進行一層的覆土掩埋,如此重複 的疊埋,但此種方式需求於相當大的掩埋空間,且在掩埋過程中稍 有不慎,即可能造成二次的環境污染等公害問題,並有因掩埋所產 生之沼氣引起火災之可能與危險,且最嚴重的問題是可適於作為掩 埋場的地點取得不易;因此,政府也大力的提倡垃圾的焚化處理, 一方面則以透過焚化方式獲得減量化,因焚化後所產生殘存之底 灰,約為焚化垃圾量之2 〇〜3 0%,而飛灰量約為底灰量之1〇 %左右’確可達到有效的減量效果;但這些焚化所產生之底灰與飛 灰,其最終的處理方式仍必需以掩埋方式來處理,且為防止底灰與 飛灰這類輕質量之灰燼飄飛造成環境空氣的污染,還必需進一步的 5 利用水泥予以固化後才進行掩埋處理,因此同樣仍必需面臨掩埋場 取得不易與住民抗爭的問題,因焚化後殘餘之底灰與飛灰中,仍含 存有戴奥辛、有害重金屬與多氯聯苯等污染性與有毒性物質,在未 經去除下進行掩埋,仍因其無法分解且埋設在地下,而造成二次環 境污染的問題,因此如何得以在有效的利用這些焚化所產生之底灰 與飛灰,並能去除各種有毒或有害物質下為再生運用,將是一個重 要的發展課題。 另關於前污水處理所產生之污泥,在最終的處置上仍無法擺脫籲 掩埋一途,當然也就面臨與焚化後底灰與飛灰之掩埋相同的窘境, 仍有待於詢求其它可適用之終極處理方法。 又習知的水泥製作,其原料多使用經開採適用以製造水泥之天 然礦物,如石灰質原料、黏土質原料及含鐵原料等,依比例混合、 煅燒熔融成為水泥熟料,再經研磨為適當的粉狀即成;換言之,該 水泥的製作必需不斷的進行天然礦石開採,且並非任一種礦石均可 適用,透過不斷的開採,將使得天然礦石資源相對不斷的減少,且修 在開採過程中’也會對周遭的環境與自然生態造成破壞,因此急待 尋求得以替代天然礦石原料之其他原料來製作水泥,一方面可降低 原料開採成本,又可維護自然環境與生態的保護。 又查該水泥原料之化學成份,不外為Si〇2、AhOa、Fe2〇3、(:ao 等,而前述焚化後之底灰、飛灰以及污泥等,除有毒與有害物質之 外也都含存這些Si〇2、Ah〇3、Fe2〇3、CaO化學成份,是若能透過適 200426130 虽的製造方法,能去除有害敍毒物,即可作祕生之原料,或作 為水泥使用之天然礦物之替代原料,而這個製造方法現已為本發明 人所研發,亦為本發明所要揭示之主要技術内容。 【發明内容】 本發明之主要目的之一,是提供一種資源再生建材水泥之製造 方法,其主要在·垃域化所產生之底灰、歧魏污水處理產 生之污泥為主要再生原料,替代天然礦物原料,透過再生原料之前 置製程、均質製程、煅燒製程與粉碎磨粉製程來製作;並配合環保_ 回收製程進行排放之處置,利用本發明前述製程獲得之水泥製成 时,在依波特蘭水泥之組成比例計算下製作,係為具有與普通波特 蘭水泥同等品質之再生建材水泥製成品。 本發明之另一主要目的之一,是提供一種資源再生建材水泥之 製造方法’其主要在透過前置製程、均質製程、緞賴程、環保回 收製程與粉碎磨粉製程,結合脫鹽技術、熱分解毒性物技術與去金 屬質技術,進而將垃圾焚化產生之底灰、飛灰以及污水處理產生之籲 污泥為主要原料,製作不含有害物質與毒性物質且符合含氣量規定 之再生水泥。 本發明之再一主要目的之一,是提供一種資源再生建材水泥之 製造方法,其主要在利用垃圾焚化所產生之底灰、飛灰以及污水處 理產生之污泥為主要再生原料,製作出不含有害物質與毒性物質且 符合含氣量規定,並能使用於一般工程,如公園路面舖裝工程、擁 壁工程、海洋護岸工程'消波石製作、混凝土碑、溝蓋側溝等,亦 τ 200426130 能用於一般建築構造之施工建材之再生水泥製成品。 本發明之又一主要目的之一,是提供一種資源再生建材水泥之 製造方法,其主要補躲圾焚靖產生之絲、歧以及污水處 理產生之污泥,為再生水泥製成品之主要礦石替代成分原料,如此 得以解決前述底灰、飛灰與污泥之掩埋及二次公害問題;同時降低 天然礦石開採使用以維護環境生態保護與天然資源保存。 根據本發明而提供一種資源再生建材水泥之製造方法,該方法 步驟包括: 鲁 提供經儲存之礦石替代原料之廢棄再生原料; 將前述再生原料利用前置製程去除金屬質形成粒狀生料; 執行一原料均質製程,根據水泥組成比例係數,進行化學組成 之比例調合,以及與前述再生原料製成之生料進行調合,組成待製 原料; 將前述調合後原料送入一熏燒設備進行緞燒製程,結合緞燒技 術形成結晶型態之化合為近似液態水泥,在此製程中,進一步結合鲁 脫鹽技術進行脫氣工程,以及毒物分解技術來除去有毒物含量,並 透過去金屬質技術除去原料中之重金屬物質,形成熟料製作; 利用環保回收設備,將前述熱分解之有毒物質與重金屬經環保 回收設備進行二次處理與棑放; 執行一粉碎磨粉製程,將前述水泥熟料冷卻後,透過研磨設備 予以粉碎磨粉,形成再生水泥製成品。 8 在一較佳具體的製造方法實施例中,該再生原料,係採用垃圾 焚化所產生之底灰、飛灰以及污水處理產生之污泥為主要再生原 料。 在一較佳具體的製造方法實施例中,該前置製程,係將前述再 生原料進行粉碎成粒狀體,並透過電磁設備進行金屬物去除作業, 以行成適於進行均質製程調合之生料。 在一較佳具體的製造方法實施例中,該均質製程,主要係根據 水泥組成比例係數,進行化學組成之調和,以決定製成品水泥之品_ 質;並進行與前述生料的調合組成待製原料。 在一較佳具體的製造方法實施例中,該含有生料之待製原料係 在一窯燒設備中,結合煅燒技術形成水泥化合之結晶型態;同時透 過煅燒技術之高熱,將生料中所含之有機鹽類、戴奥辛、有害重金 屬類等有還或有毒物質,蒸發分解成為微細顆粒之熔融飛灰,並可 進一步的利用脫鹽技術進行脫氣工程,以及毒物分解技術來除去有 毒物含量,並透過去金屬質技術除去原料中之重金屬物質。 孀 在一較佳具體的製造方法實施例中,該脫氣工程主要係利用於 前述均質製程中所添加之鈉化合物,如碳酸鈉等組群之一採用;藉 由锻燒製程,使生料中所含之多量氣離子(CI—)與鈉離子(Na+) 結合成氣化鈉(NaCI),並揮發於煅燒製程的瓦斯中,而使製成品 之水泥含氣量可符合〇· 1%水泥質量規定之要求。 在一較佳具體的製造方法實施例中,該毒物分解技術,主要在 200426130 去除戴奥辛類有機毒物類,藉由锻燒製程之高熱,使有機毒物類之 戴奥辛類發生脫鹽素反應之氣與氫置換,而完全分解於瓦斯中,嗣 配合前述環保回收設備,即利用急速冷卻塔將高溫排放瓦斯急速降 溫至戴奥辛之新合成反應溫度(約3〇〇它)以下,使戴奥辛完全達 到分解消除。 在一較佳具體的製造方法實施例中,該去金屬質技術,主要係 將前述生料中所含之有害重金屬Hg、Cd、Pb、As等於高溫煅燒中, 熱分解為金屬離子蒸發並揮發於瓦斯中與HCI結合而濃縮於熔解籲 飛灰成微細粒子之金屬鹽,隨瓦斯排放配合前述環保回收設備,即 利用旋風集塵機將含有濃縮重金屬之鹽微細顆粒熔解飛灰進行捕 集。此含有濃縮重金屬之鹽微細顆粒熔解飛灰得進一步由重金屬工 廠再生提煉。 【實施方式】 本發明之内容,主要在揭示一種可具有與普通波特蘭水泥同等 化學組成與品質之廢棄物資源再生建材水泥,係以垃圾焚化所產生春 之底灰、飛灰以及污水處理產生之污泥為主要再生原料,替代天然 確物製成之生料。其較佳的製成品製作方法,係-種由前述再生原 料’透過均質製程獲得與普通波特蘭水泥同等化學組成之化合物調 合’結合緞燒製程製作水泥熟料中,同時將再生原料所製成之生料 中含存之有害物質’結合環伽收製程與去除有害物質之相關技術 進行完全的去除,以獲得無害之再生水泥製成品現已發明,這個製 成之水泥製成品係為一種與普通波特蘭水泥同等或類同規格之水 10 200426130 泥;並能使用於-般工程,如公園路面舖裝工程、擁壁工程、海洋 護岸工程、消波石製作、混凝土碑、溝蓋姆等,亦制於一般建 築構造之施工建材之再生水泥製成品。 本發明之較佳實施例將前述的資源再生建材水泥之製造方法 及其製成品的主要技術内容適當揭示於以下所列舉的一較佳實施 例中,並利用該較佳實施例裝置將本發明之主要技術内容予以適當 實施。 第一〜二圖揭示本發明一較佳實施例資源再生建材水泥之製籲 造方法的製造步驟方塊圖,以及製造流程路徑圖。前述資源再生建 材水泥之具體製造方法,至少包括: 步驟10,提供經儲存之破石替代原料。該礦石替代原料包括 垃圾焚化所產生之底灰、飛灰、污水處理產生之污泥以及石灰石等 原料。 步驟1 1,&供經别置製程處理之前述礦石替代原料,並儲置 於一生料儲槽中,為水泥生料界定。該前置製程主要在進行對各礦魯 石替代原料,如底灰、飛灰、污泥以及石灰石等原料,係在一設定 之粒別規格範圍之前置加工,以便利進行下一步驟之均質製程之調 和,同時也在去除前述各礦石替代原料中含存之金屬物。 步驟1 2 ’將前述由確石替代原料所組成之水泥生料,進行一 原料均質製程,並將經均質完成之水泥生料送到一入窯生料槽(為 一般已知設備,故未進一步繪示說明),採自動且定量之送入窯燒 11 200426130 設備進行緞燒製程。此均質製程之執行,主要在對水泥生料之組成 成分,根據所要獲得之水泥製成品品質與規格之成分比例與係數計 算,進行符合該計算結果之化學成分Si〇2、Ah〇3、Fe2〇3、Ca〇等與 調合各化合物GS、GS、GA、GAF、水泥生料;並在均質製程中加 入適量納化合物,如碳酸納等為最佳,以中和氣化物離子。 步驟13,將前述步驟12,經均質完成之水泥生料,透過入 窯生料槽自動且定量之送入窯燒設備(為一般已知設備,故未進一 步繪示說明)進行煅燒製程,以完成水泥生料之放熱反應化合為結籲 晶型態形成之水泥熟料。且在此烺燒製程中將進一步的將水泥生料 中含存之有害物質,如有機類重金屬、戴奥辛類及氯化物等,透過 南溫缎燒環境進行分解於窯内含存之瓦斯中,經冷卻並結合環保回 收設備進行回收與去除處理。 步驟1 4,將前述步驟1 3緞燒所得之水泥熟料,經冷卻後加 入3〜5%石膏等固形添加物,透過研磨設備(為一般已知設備, 故未進一步繪示說明)予以粉碎磨粉,形成再生水泥製成品。 · 步驟15,於步驟13煅燒製程中所分解之有害物質,如有機 類重金屬、戴奥辛類及氣化物等,則結合脫鹽技術進行脫氣工程, 以及配合環保回收設備結合毒物分解技術與去金屬質技術,而進行 有毒物質與重金屬物質之去除處理。 根據本發明前述資源再生建材水泥之製造方法,得以利用應掩 埋廢棄之垃圾焚化所產生之底灰、飛灰以及污水處理產生之污泥, 200426130 作為水泥主要成分之天然礦石原料的替代原料,透過本發明前述製 造方法暨步驟,得以製成完全不具有害物纽氣含量在規定之〇· 1 %以下之再生水泥製成品;相較於習知水泥暨普通波特蘭水泥,可 以獲得同等之品質,並能使用於-般X程,如公園路面舖裝工程、 擁壁工程、海洋護岸工程、消波石製作、混凝土碑、溝蓋側溝等, 亦忐用於一般建築構造之施工建材。但卻不需開採與使用天然破物 來製作’不僅能有效的降低使用原料之成本,更具有解決前述底 灰、飛灰與污泥等廢棄物之掩埋及二次公害問題;同時降低天然礦_ 石開採使用以維護環境生態保護與天然資源保存。 在一較佳具體的製造方法實施例中,該用以替代天然礦石使用 製作水泥製成品之再生原料,係採用垃圾焚化所產生之底灰、飛灰 以及污水處理產生之污泥為主要再生原料,並與石灰石等原料組成 水泥生料。其中該焚化爐底灰與污水處理產生之污泥,係分別置於 一儲存場中;而飛灰則必須儲放於一密閉儲存槽中 該前述礦石替代原料之前置製程,在一較佳的製造方法具體實春 施例中,包括前述礦石替代原料之破解、乾燥、金屬物清除、粗碎、 細碎及篩別粒度等製程,並進行多次的製程重覆執行,以取得適於 進行均質製程調和之礦石替代原料組成之生料。其中該礦石替代原 料之破解、粗碎、細碎等製程,係透過破碎設備,如粗碎機、細碎 機之採用執行;而金屬物清除則係透過電磁選別機進行一次或以上 之金屬物清除。 13 200426130 本發明資源再生建材水泥之製造方法中之均質製程,用以製造 水泥之原料的化學成分不外Si〇2、Al2〇3、Fe2〇3、CaO等,即使如本 發明採用垃圾焚化所產生之底灰、飛灰以及污水處理產生之污泥, 配合石灰石組成替代天然破石使用之原料’其原料之化學成分組成 亦不外乎為Si〇2、Al2〇3、Fe2〇3、CaO等,但在一較佳之具體實例中, 為使利用本發明製造方法所製成之水泥製成品,係具有與普通波特 蘭水泥同等品質,因此在進行水泥組成原料之比例係數與化學組成 暨化合物調合製程時,仍必需根據波特蘭水泥標準,按照各化學成φ 分之比例係數及限度允許範圍内進行精確計算調配,其計算調配方 式包括: 水泥組成比例係數: 水硬率(EM)=CaO(%) -S〇2(%)x0.7/Si〇2(%) +Al2〇3(%) +Fe2〇3 (% ) 矽氧率(S.M· ) =Si〇2 (%) /Al2〇3 (%) +Fe2〇3 (%) * 鐵率(Ι·Μ· ) =Ah〇3 (%) /Fe2〇3 (%) 活動係數(A· I· ) =Si〇2 (%) /AI2O3 (%) 水硬係數(Η· I· ) =Si〇2 (%) +Al2〇3 (%) /CaO (%) 石灰比(L.R· ) =CaO (%) /Si〇2 (%) -Al2〇3 (%) 鐵釁土比(I.A.R· ) =Fe2〇3 (%) /Al2〇3 (%) n 200426130 水泥組成比例係數及限唐: 水硬率(Η·Μ· ) Hydraulic Modulus 1·7 〜2·4 石夕氧率(S·Μ· ) Silica Modulus 1.8 〜3·2 鐵率(Ι·Μ· ) Iron Modulus 0· 7 〜2· 0 活動係數(Α· Ι· ) Activity Index 2· 5〜6· 0 水硬係數(Η· Ι· ) Hydraulic Index 0· 42〜0· 48 石灰比(L.R· ) Lime Ratio < 2·85 鐵釁土比(I.A.R· ) Iron Oxide / Alumina 1·4 〜0·5 在一較佳具體的製造方法實施例中,該前述經均質完成之水泥 生料的煅燒製程,係在一窯燒設備中進行,該窯燒設備以旋窯使用 為最佳,且得依據實際要求選別採用燒成帶較大或煅燒帶、化合帶 較大之旋窯使用;利用旋窯内具有不同之溫度帶,包括100°C〜600 °〇為預熱帶,當水泥生料進入此預熱帶,發生吸熱反應,水份開始 蒸發並釋放出水泥生料中之結晶水;然後進入900°C〜1000°C之煅 燒帶,經不同之溫度下,水泥生料開始放熱反應,此時使得非結晶 型態之水泥生料開始轉變成為結晶型態,同時,水泥生料中之石灰 石等吸熱反應放出二氧化碳變成氧化鈣;最後進入1100°c〜1400°c 之化合帶,水泥生料於南溫下放熱反應化合’進而完成水泥的反應 成為近似液態的水泥熟料,其化學變化為:CaC〇3與MgC〇3分解;%2〇 與Μ揮發;FeO氧化成Fe〇3; CaO、MsO、AhO3、Fe2〇3化合產生 矽酸、鋁酸等鹽類。而水泥生料中所含有之有機鹽類、戴奥辛及有 15 200426130 害重金屬類’將於高溫下蒸發分解成為微細顆粒之熔融飛灰,得結 合脫鹽技術進行脫氣工程,以及配合環保回收設備結合毒物分解技 術與去金屬質技标’將戴奥辛及有害重金屬類從水泥生料中去除。 前述對於水泥生料中所含有之有機鹽類的去除,由於該水泥生 料中所使用之S生原料為垃圾焚化所產生之底灰、飛灰以及污水處 理產生之污泥,而含有較天然礦物較多量之氣化物離子,為達到水 泥熟料中之氣化物離子分量必需在水泥質量之〇· 1%以下之規定, 而必須將多餘之氣化物離子進行去除;該有機鹽類的去除,主要係 結合脫鹽技術進行脫氣工程,在一具體實施例方法中,利用在水泥 生料之均質製程中,添加適量之納化合物,如碳酸納等組群之一採 用;藉由緞燒製程,使生料中所含之多量氣離子(CI-)與鈉離子 (Na )結合成氣化納(就1),並揮發於瓦斯中,進而隨瓦斯排出, 而使製成品之水泥含氣量可符合0· 1%水泥質量規定之要求。 又水泥生料中之再生原料,因係由垃圾焚化所產生之底灰、飛 灰以及污水處理產生之污泥,而相對含有些有害重金屬取、⑺、 Pb、As等成分必需進行去除,該去除之方法係結合去金屬質技術 與環保回收设備來進行,即藉由前述水泥生料中所含之有害重金屬 Hg、Cd、Pb、As等於煅燒製程之化合帶高溫煅燒中,發生熱分解 為金屬離子蒸發,並揮發於瓦斯中與HCI結合,而濃縮於炼解飛灰 成微細粒子之金屬鹽,隨瓦斯排放配合前述環保回收設備,即利用 旋風集塵機之筛選,而將粗粒回收並送入窯内再次煅燒,至於含有 26 200426130 漠縮重金屬之鹽微細顆粒轉飛灰,再經袋式捕塵猶設備完全捕 集,即可完成水泥生料中之含存重金屬之去除;所產生之濃縮重金 屬之鹽微_姆解驗,得進—步由重金屬讀再生提練。 同樣的水泥生财之再生顧所含存之錢毒性物之 PCDDs 、 PCDFs戴奥辛類,亦必須進行去除作業,並抑止戴奥辛之新合成反 應Synthesis)合成更具毒性之戴奥辛。此毒物分解技術, 係利用刖述锻燒製程之化合帶高溫锻燒中,戴奥辛類發生脫鹽素反 應’氣與氫置換而完全分解為^〜沁…以^”並揮發於瓦斯中’籲 又戴奥辛類之新合成反應(DoNoVo Synthesis)適溫約為30(TC左 右’因此,在瓦斯排放中接經急速冷卻塔,將高溫排放瓦斯急速降 溫至戴奥辛之新合成反應溫度(約3〇〇〇c)以下,例如2〇(rc,而 使得戴奥辛可被完全達到分解消除。而排放之瓦斯,再經脫硝設備 去除NOx與SOx,達到瓦斯排放標準經煙_排放大氣中。 實施例: 以垃圾焚化所產生之底灰、飛灰、污水處理產生之污泥以及石 ® 灰石等原料,經前置製程後混合組成礦石替代原料之水泥生料。 將前述之水泥生料,以前述波特蘭水泥標準之化學組成之比例 係數及限度允許範圍進行精確計算調配,如 水泥組成比例係數: 水硬率(Η· M·)=CaO (%) —S〇2 (%) xO· 7/Si〇2 (% ) + Al2〇3 (%) +F62O3 (%) 17 200426130 矽氧率(S.M· ) =Si〇2 (%) /Al2〇3 (%) +Fe2〇3 (%) 鐵率(Ι·Μ· ) =Al2〇3 (%) /Fe2〇3 (%) 活動係數(A· I. ) =Si〇2 (%) /Al2〇3 (%) 水硬係數(Η· I· ) =Si〇2 (%) +Al2〇3 (%) /CaO (%) 石灰比(L.R· ) =CaO (%) /Si〇2 (%) — AI2O3 (%) 鐵礬土比(I.A.R· ) =Fe2〇3 (%) /Al2〇3 (%) 水泥組成比例係數及限度: · 水硬率(Η·Μ· ) Hydraulic Modulus 1·7 〜2·4 石夕氧率(S·Μ· ) Silica Modulus 1·8 〜3·2 鐵率(Ι· Μ· ) Iron Modulus 0· 7 〜2· 0 活動係數(Α· Ι· ) Activity Index 2· 5〜6· 0 水硬係數(Η· Ι· ) Hydraulic Index 0.42〜0.48 石灰比(L.R· ) Lime Ratio < 2·85 鐵礬土比(Ι· A· R· ) Iron Oxide / Alumina 1· 4 〜0.5 f 本發明之水泥生料根據前述化學成分配比確定後,原料於锻繞 製程時,其中所含之揮發成分如飛灰、石灰石中之二氧化碳及污泥 底灰中之水份釋出,故重量錢損為此各祕讀4,按Cac〇= 燒分解時之反應計算··200426130 IX. Description of the invention: [Technical field to which the invention belongs] The present invention relates to a method for manufacturing cement from resource-recycling building materials and its finished products, and relates to the technical field of recycling cement by using waste ash and mud, and in particular, refers to a kind of utilization of Bottom ash, fly ash from sewage incineration, and sludge from sewage treatment are the main recycled raw materials. After the technical process of this method, non-toxic, gaseous and metal substances can be removed, and it can be obtained with ordinary Portland cement. Method for manufacturing recycled building material cement of the same quality and its finished products. [Previous technology] According to the current, the garbage generated by the daily life of citizens can be divided into landfill method and incineration method. Among them, the burial method must have a relatively large burial area location. After the garbage is dumped directly and sequentially, it is buried in a layer of soil, which is repeated. However, this method requires a large burial space, and There is a little carelessness during the landfill process, which may cause secondary environmental pollution and other pollution problems, and the possibility and danger of fire caused by the biogas produced by the landfill. The most serious problem is that it can be used as a landfill site. It is not easy to obtain; therefore, the government also vigorously promotes the incineration of waste. On the one hand, it is reduced by incineration. The residual bottom ash generated after incineration is about 20 to 30% of the amount of incinerated waste, and The amount of fly ash is about 10% of the amount of bottom ash. It can indeed achieve an effective reduction effect; however, the final treatment method of the bottom ash and fly ash produced by these incinerations must still be disposed of in a landfill manner, and to prevent Light-weight ashes such as bottom ash and fly ash cause environmental air pollution, and further 5 must be cured by cement before being buried, so the same It is necessary to face the problem that the landfill is not easy to fight with the residents. The residual bottom ash and fly ash after incineration still contain contaminating and toxic substances such as dioxin, harmful heavy metals and polychlorinated biphenyls. When it is buried, it still cannot be decomposed and buried in the ground, which causes the problem of secondary environmental pollution. Therefore, how can the bottom ash and fly ash generated by these incineration be effectively used, and various toxic or harmful substances can be removed? Recycling will be an important development issue. In addition, regarding the sludge generated from the previous sewage treatment, it is still impossible to get rid of the landfill in the final disposal. Of course, it also faces the same dilemma as that of the bottom ash and fly ash after incineration. It remains to be inquired about other applicable The ultimate approach. Also known for cement production, the raw materials are mostly natural minerals that are suitable for cement production, such as lime raw materials, clay raw materials, and iron-containing raw materials. They are mixed in proportion, calcined and melted into cement clinker, and then ground as appropriate. In other words, the production of this cement requires continuous natural ore mining, and not all types of ore can be applied. Through continuous mining, the natural ore resources will be relatively reduced, and repaired during the mining process. 'It will also cause damage to the surrounding environment and natural ecology. Therefore, it is urgent to find other materials that can replace natural ore raw materials to make cement. On the one hand, it can reduce the cost of raw material mining and maintain the natural environment and ecological protection. Also check the chemical composition of the cement raw materials, except for Si02, AhOa, Fe203, (ao, etc.), and the above-mentioned incinerated bottom ash, fly ash and sludge, etc., are all toxic and harmful substances. Containing these Si02, Ah03, Fe203, and CaO chemical components, if it can remove harmful poisons through a manufacturing method suitable for 200426130, it can be used as a secret raw material or as a natural cement use Mineral is an alternative raw material, and this manufacturing method has been developed by the inventors and is also the main technical content to be disclosed by the present invention. [Summary] One of the main objects of the present invention is to provide a resource-recycling building material cement manufacturing Method, which mainly uses the bottom ash produced by wastelandization and the sludge produced by Qiwei wastewater treatment as the main recycled raw materials, instead of natural mineral raw materials, through the pre-process, homogeneous process, calcination process and pulverization milling of the recycled raw materials It is produced by the manufacturing process; and is disposed of in accordance with the environmental protection _ recycling process for the disposal of emissions. When using the cement obtained by the aforementioned process of the present invention, it is produced under the calculation of the Portland cement composition ratio. It is a recycled building material cement product with the same quality as ordinary Portland cement. One of the other main purposes of the present invention is to provide a manufacturing method of resource recycled building material cement, which mainly uses pre-processing, homogenization, The satin process, the environmentally friendly recycling process, and the pulverizing and milling process combine demineralization technology, thermal decomposition of toxic materials technology, and demetallization technology, and then use the bottom ash, fly ash, and sewage sludge produced by incineration as the main raw materials , To produce recycled cement that does not contain harmful substances and toxic substances and meets the requirements for gas content. One of the other main objectives of the present invention is to provide a method for manufacturing a resource-recycling building material cement, which mainly uses the bottom ash generated by waste incineration. Fly ash and sludge from sewage treatment are the main raw materials for regeneration. They are produced without harmful and toxic substances and meet the gas content requirements. They can be used in general projects, such as park pavement works, wall works, and marine revetments. Engineering 'wave-making stone, concrete monument, trench cover side trench, etc., also τ 200426130 can be used for general construction Recycled cement made of construction materials for construction. One of the other main objects of the present invention is to provide a method for manufacturing a resource-recycling building material cement, which mainly supplements the silk and slag produced by waste incineration and sludge produced by sewage treatment. It is the main ore substitute component raw material for recycled cement products, which can solve the aforementioned landfill, fly ash and sludge burial and secondary pollution problems; meanwhile, reduce the use of natural ore mining to maintain environmental protection and natural resource conservation. The present invention provides a method for manufacturing a resource-recycling building material cement. The method includes the steps of: providing a discarded recycled raw material for the stored ore substitute raw material; removing the metallic material into a granular raw material by using a pre-processing process; Raw material homogenization process, according to the cement composition ratio coefficient, chemical composition ratio blending, and blending with the raw materials made of the aforementioned recycled raw materials to form the raw materials to be prepared; the aforementioned blended raw materials are sent to a fumigation equipment for satin firing process The combination of satin firing technology to form a crystalline form is similar State cement, in this process, further combined with Lu desalination technology for degassing project, and toxic substance decomposition technology to remove toxic substances content, and demetallic technology to remove heavy metal substances in raw materials to form clinker production; use environmental protection recycling equipment The above-mentioned thermally decomposed toxic substances and heavy metals are subjected to secondary treatment and release by environmental protection recovery equipment; a pulverization and milling process is performed, the aforementioned cement clinker is cooled, and the pulverization and milling are performed through the grinding equipment to form a recycled cement finished product . 8 In a preferred embodiment of the specific manufacturing method, the recycled raw materials are bottom ash, fly ash and sewage sludge generated from waste incineration as the main recycled raw materials. In a preferred embodiment of the manufacturing method, the pre-process is to pulverize the aforementioned recycled raw materials into granules, and perform metal object removal operations through electromagnetic equipment to form a suitable product for homogeneous process blending. material. In a preferred specific embodiment of the manufacturing method, the homogeneous manufacturing process is mainly based on the chemical composition ratio coefficient to adjust the chemical composition to determine the quality of the finished product cement;制 材料。 Manufacturing raw materials. In a preferred specific embodiment of the manufacturing method, the raw material to be prepared containing raw meal is combined in a kiln firing equipment, which is combined with a calcination technique to form a crystalline form of cementation. At the same time, the raw material is passed through the high heat of the calcination technique. The contained organic salts, dioxin, harmful heavy metals and other toxic or toxic substances can be evaporated and decomposed into fine particles of molten fly ash, and the desalination technology can be further used for degassing projects, and the toxic substance decomposition technology can be used to remove toxic substances. , And remove the heavy metal substances in the raw materials through demetallic technology.孀 In a preferred embodiment of the specific manufacturing method, the degassing project is mainly used by the sodium compound added in the aforementioned homogenization process, such as one of the groups such as sodium carbonate; the raw material is made by the calcination process A large amount of gas ions (CI-) and sodium ions (Na +) are combined to form sodium gasification (NaCI), and volatilized in the gas in the calcination process, so that the gas content of the finished product can meet the 0.1% cement Requirements for quality regulations. In a preferred specific embodiment of the manufacturing method, the poison decomposition technology mainly removes dioxin-type organic poisons in 200426130. By the high heat of the calcination process, the dioxin-type gases and hydrogen of the organic poisons are desalinated. Displacement and complete decomposition in gas, combined with the aforementioned environmental protection recovery equipment, that is, using a rapid cooling tower, the high temperature exhaust gas is rapidly cooled to below the new synthesis reaction temperature of dioxin (about 300 ° C), so that dioxin can be completely decomposed and eliminated. In a preferred specific embodiment of the manufacturing method, the demetallization technology is mainly to decompose the harmful heavy metals Hg, Cd, Pb, and As contained in the aforementioned raw meal during high-temperature calcination, and thermal decomposition decomposes into metal ions to evaporate and volatilize. Combined with HCI in gas, it is concentrated in the metal salt that melts into the fly ash to become fine particles. With the gas emission, it cooperates with the aforementioned environmental protection recycling equipment, that is, the cyclone dust collector is used to capture the fine particles of salt containing concentrated heavy metals by melting the fly ash. The fine particles of salt containing concentrated heavy metals melt the fly ash and can be further refined by the heavy metal factory. [Embodiment] The content of the present invention mainly discloses a waste resource regeneration building material cement which can have the same chemical composition and quality as ordinary Portland cement, which is produced by spring bottom ash, fly ash and sewage treatment generated from waste incineration. The sludge is the main renewable raw material, replacing the raw material made from natural materials. Its preferred method for making finished products is a kind of compound made from the aforementioned recycled raw materials 'obtaining a compound with the same chemical composition as that of ordinary Portland cement through a homogeneous process' combined with a satin firing process to produce cement clinker, and at the same time made of recycled raw materials Harmful substances contained in Chengzhi raw materials' combined with cyclogamous harvesting process and related technologies for removing harmful substances are completely removed to obtain harmless recycled cement products. This cement product is a kind of Water with the same or similar specifications as ordinary Portland cement 10 200426130 mud; and can be used in ordinary projects, such as park pavement works, wall-supporting works, marine revetment works, wave-making stones, concrete monuments, trench covers Mu, etc., also made of recycled cement made of construction materials for general building construction. The preferred embodiment of the present invention appropriately discloses the above-mentioned manufacturing method of the resource-recycling building material cement and the main technical contents of the finished product thereof in a preferred embodiment listed below, and utilizes the preferred embodiment device to translate the present invention The main technical content shall be properly implemented. The first and second figures disclose a block diagram of manufacturing steps and a manufacturing process path diagram of a method for manufacturing a resource-recycling building material cement according to a preferred embodiment of the present invention. The specific method for manufacturing the resource-recycling building material cement includes at least: Step 10, providing stored raw materials for broken stone replacement. The ore substitute raw materials include bottom ash, fly ash, sewage sludge and limestone from waste incineration. Step 11: & The aforementioned ore substitute raw material for processing by another process is stored in a raw material storage tank to define the cement raw material. The pre-processing process is mainly to replace raw materials such as bottom ash, fly ash, sludge, and limestone in various mines. The raw materials are processed before a set range of grain specifications to facilitate the next step. The reconciliation of the homogenization process also removes the metal substances contained in the aforementioned various ore substitute raw materials. Step 1 2 'Put the aforementioned cement raw material composed of solid stone substitute raw materials into a raw material homogenizing process, and send the homogenized cement raw material to a raw kiln raw material trough (which is generally known equipment, so Further illustrations), automatic and quantitative feeding into the kiln firing 11 200426130 equipment for satin firing process. The implementation of this homogeneous process is mainly to calculate the composition of the cement raw material according to the composition ratio and coefficient of the quality and specifications of the cement finished product to be obtained, and carry out the chemical composition Si02, Ah03, and Fe2 that meet the calculation results. 〇3, Ca〇 and other compounds GS, GS, GA, GAF, cement raw materials; and in the homogeneous process by adding an appropriate amount of sodium compounds, such as sodium carbonate, etc. is best to neutralize gaseous ions. Step 13. The homogenized cement raw material from the previous step 12 is automatically and quantitatively fed into the kiln firing equipment (which is a generally known equipment, so it is not further illustrated) through a kiln raw material tank to perform a calcination process to The exothermic reaction of the finished cement raw material is combined into cement clinker with the formation of crystalline forms. And in this firing process, harmful substances contained in the cement raw material, such as organic heavy metals, dioxins and chlorides, will be decomposed into the gas contained in the kiln through the south temperature satin firing environment. It is cooled and combined with environmental protection recycling equipment for recycling and removal. Step 14: The cement clinker obtained from the satin firing in the previous step 13 is cooled and added with solid additives such as 3 to 5% gypsum, and then pulverized by a grinding device (which is a generally known device, so no further description is shown). Milled to form recycled cement products. · Step 15, harmful substances decomposed during the calcination process in step 13, such as organic heavy metals, dioxins and gaseous substances, etc., combined with desalination technology for degassing project, and with environmental protection recycling equipment combined with toxicological decomposition technology and demetallicity Technology to remove toxic substances and heavy metal substances. According to the aforementioned method for manufacturing a resource-recycling building material cement according to the present invention, the bottom ash, fly ash, and sewage sludge generated from the waste incineration that should be disposed of can be buried. 200426130 is used as a substitute for natural ore raw materials for the main component of cement. The foregoing manufacturing method and steps of the present invention can be made into recycled cement products with no harmful gas content below 0.1%. Compared with conventional cement and ordinary Portland cement, it can obtain the same quality. It can also be used in general X-paths, such as park pavement works, wall-supporting works, marine revetment works, wave-making stones, concrete monuments, ditch-covering side ditches, etc. It is also used as a building material for general building construction. However, it does not require mining and use of natural broken materials to make 'not only can effectively reduce the cost of using raw materials, but also solve the landfill and secondary pollution problems of the aforementioned bottom ash, fly ash and sludge; at the same time, reduce natural ore _ Stone mining is used to maintain environmental protection and natural resource conservation. In a preferred embodiment of the specific manufacturing method, the recycled raw materials used to make cement products instead of natural ore are made of ground ash, fly ash and sewage sludge generated from waste incineration as the main recycled raw materials. And, with limestone and other raw materials to make cement raw materials. The bottom ash of the incinerator and the sludge generated from sewage treatment are separately placed in a storage yard; and the fly ash must be stored in a closed storage tank before the aforementioned ore substitute raw material is placed in a process. In the specific embodiment of the manufacturing method, the processes include cracking, drying, metal removal, coarse crushing, fine crushing and sieving particle size of the aforementioned ore substitute raw materials, and repeating the process multiple times to obtain a suitable process. Homogenization of the homogenization process to replace raw materials consisting of raw materials. The process of cracking, coarse crushing, and fine crushing of the ore instead of the raw materials is performed through the use of crushing equipment, such as coarse crushers and fine crushers; and the removal of metal objects is performed once or more by using an electromagnetic separator. 13 200426130 The homogeneous process in the manufacturing method of the resource-recycling building material cement of the present invention, the chemical composition of the raw materials used to make the cement is not only Si02, Al2 03, Fe2 03, CaO, etc., even if the waste incineration plant is used as the present invention The generated bottom ash, fly ash, and sludge generated from sewage treatment are combined with limestone to replace the raw materials used in natural stone breaking. The chemical composition of its raw materials is nothing more than Si02, Al203, Fe203, and CaO. Etc., but in a preferred specific example, in order to make the cement products manufactured by the manufacturing method of the present invention have the same quality as ordinary Portland cement, the proportion coefficient and chemical composition of the raw materials of the cement composition are being processed. During compound compounding process, it is still necessary to accurately calculate and blend according to the Portland cement standard according to the proportion coefficient and limit of each chemical composition φ. The calculation and blending methods include: Cement composition proportion coefficient: Hydraulic set ratio (EM) = CaO (%) -S〇2 (%) x0.7 / Si〇2 (%) + Al2〇3 (%) + Fe2〇3 (%) Silicon Oxide Rate (SM ·) = Si〇2 (%) / Al2〇3 (%) + Fe2〇3 (%) * Iron rate (I · M ·) = Ah. 3 (%) / Fe2〇3 (%) Activity coefficient (A · I ·) = Si〇2 (%) / AI2O3 (%) Hydraulic coefficient (Η · I ·) = Si〇2 (%) + Al2〇 3 (%) / CaO (%) Lime ratio (LR ·) = CaO (%) / Si〇2 (%) -Al2〇3 (%) Iron-to-earth ratio (IAR ·) = Fe2〇3 (%) / Al2〇3 (%) n 200426130 Cement composition ratio coefficient and limit: hydraulic modulus (Η · Μ ·) Hydraulic Modulus 1 · 7 ~ 2 · 4 Shi Xi oxygen rate (S · Μ ·) Silica Modulus 1.8 ~ 3 · 2 Iron rate (Ι · Μ ·) Iron Modulus 0 · 7 ~ 2 · 0 Activity coefficient (Α · Ι ·) Activity Index 2 · 5 ~ 6 · 0 Hydraulic coefficient (Η · Ι ·) Hydraulic Index 0 · 42 ~ 0 · 48 Lime Ratio (LR ·) Lime Ratio < 2 · 85 Iron Oxide / Alumina 1 · 4 ~ 0 · 5 In a preferred embodiment of the manufacturing method, the aforementioned The homogeneous completion of the cement raw material calcination process is carried out in a kiln firing equipment. The kiln firing equipment is best used in a rotary kiln. According to the actual requirements, it is necessary to choose a larger firing zone or a calcining zone. Dazhi rotary kiln is used; it has different temperature zones in the rotary kiln, including 100 ° C ~ 600 °. Preheating zone. When the cement raw material enters this preheating zone, an endothermic reaction occurs, and the water begins to evaporate and release the crystallization water in the cement raw material. Then it enters the calcination zone at 900 ° C ~ 1000 ° C. After different temperatures, The cement raw meal begins to exothermic, at this time, the non-crystalline cement raw meal begins to change into a crystalline form. At the same time, the endothermic reaction of limestone in the cement raw meal releases carbon dioxide into calcium oxide; finally it enters 1100 ° c ~ 1400 ° c. In the compounding zone, the cement raw material exothermicly reacts at south temperature to complete the reaction of the cement to become a nearly liquid cement clinker. The chemical changes are: CaC03 and MgC03 are decomposed;% 20 and M are volatile; FeO is oxidized to FeO3; CaO, MsO, AhO3, and Fe203 are combined to produce salts such as silicic acid and aluminate. The organic salt, dioxin and 15 200426130 heavy metals contained in the cement raw material will evaporate and decompose into molten fly ash with fine particles at high temperature, which can be combined with desalination technology for degassing project and environmental protection recycling equipment. Detoxification technology and demetallization technology standard 'remove dioxin and harmful heavy metals from cement raw materials. The removal of the organic salts contained in the cement raw material is because the raw raw materials used in the cement raw material are bottom ash, fly ash generated from waste incineration, and sludge generated from sewage treatment. In order to achieve the gaseous ion content in the cement clinker which is less than 0.1% of the mass of the cement, the excess gaseous ion must be removed; the removal of the organic salts, It is mainly used in combination with desalination technology for degassing. In a specific embodiment method, it is used in the homogeneous process of cement raw materials to add an appropriate amount of sodium compounds, such as one of the groups such as sodium carbonate; through the satin firing process, The large amount of gas ions (CI-) and sodium ions (Na) contained in the raw material are combined to form sodium gasification (as 1), which is volatilized in the gas, and then discharged with the gas, so that the gas content of the cement in the finished product can be Meet the requirements of 0.1% cement quality regulations. The recycled raw materials in the cement raw meal are the bottom ash, fly ash and sewage sludge generated from the waste incineration, and relatively harmful heavy metals such as extract, plutonium, Pb, As must be removed. The The removal method is carried out in combination with demetalization technology and environmentally friendly recycling equipment, that is, the thermal decomposition occurs in the high-temperature calcination of the compound zone in which the harmful heavy metals Hg, Cd, Pb, and As contained in the aforementioned cement raw material are equal to the calcination process. The metal ions evaporate and volatilize in the gas and combine with HCI, and are concentrated in the metal salt of the refining fly ash into fine particles. With the gas discharge, the aforementioned environmental protection recovery equipment is used, that is, the coarse dust is collected by the cyclone dust collector to recover the coarse particles. And sent to the kiln for calcination again. As for 26 200426130, the fine particles of salt containing indifferent heavy metals are converted to fly ash, and then completely captured by the bag-type dust-collecting equipment, the removal of the heavy metals in the cement raw meal can be completed; The produced concentrated heavy metal salt is micro-tested, which can be further improved by reading and regenerating heavy metals. In the same way, the regeneration of cement fortunes and PCDDs and PCDFs dioxins contained in toxic substances stored in money must also be removed, and the new synthesis of dioxin by synthesis of dioxin should be prevented to synthesize the more toxic dioxin. This poison decomposition technology is based on the high-temperature calcination of the compounding zone of the described calcination process. Dioxins undergo a desalination reaction, which is replaced by gas and hydrogen, and completely decomposed into ^ ~ qin ... and ^ "and volatilized in gas. The suitable temperature for the new synthesis of Dioxin (DoNoVo Synthesis) is about 30 (TC). Therefore, in the gas emission, a rapid cooling tower is connected to rapidly cool the high-temperature exhaust gas to the temperature of the new synthesis reaction of Dioxin (about 3,000). c) The following, for example, 20 (rc), so that dioxin can be completely decomposed and eliminated. The emitted gas is then removed by the denitration equipment to remove NOx and SOx to reach the gas emission standard and discharged into the atmosphere through smoke. Example: The raw materials such as bottom ash, fly ash, sewage sludge generated from waste incineration, and stone® limestone are mixed in a pre-process to form cement raw materials that replace the raw materials of the ore. The proportion coefficient and limit of chemical composition of Tran cement standard allow accurate calculation and deployment, such as the proportion coefficient of cement composition: hydraulic rate (Η · M ·) = CaO (%) —S〇2 (%) xO · 7 / Si〇2 (%) + Al2〇3 (%) + F62O3 (%) 17 200426130 Silicon Oxide Rate (SM ·) = Si〇2 (%) / Al2〇3 (%) + Fe2〇3 (%) Iron Rate (Ι · Μ ·) = Al2〇3 (%) / Fe2〇3 (%) Activity coefficient (A · I.) = Si〇2 (%) / Al2〇3 (%) Hydraulic coefficient (Η · I · ) = Si〇2 (%) + Al2〇3 (%) / CaO (%) Lime ratio (LR ·) = CaO (%) / Si〇2 (%) — AI2O3 (%) Iron bauxite ratio (IAR · ) = Fe2〇3 (%) / Al2〇3 (%) Cement composition ratio coefficient and limit: · Hydraulic set rate (Η · Μ ·) Hydraulic Modulus 1 · 7 ~ 2 · 4 Shixi oxygen rate (S · Μ · ) Silica Modulus 1 · 8 ~ 3 · 2 Ferrite rate (I · M ·) Iron Modulus 0 · 7 ~ 2 · 0 Activity coefficient (Α · Ι ·) Activity Index 2 · 5 ~ 6 · 0 Hydraulic coefficient (Η · Ι ·) Hydraulic Index 0.42 ~ 0.48 Lime Ratio (LR ·) Lime Ratio < 2.85 Iron bauxite ratio (Ι · A · R ·) Iron Oxide / Alumina 1.4 · 0.5 ~ 0.5 f After the aforementioned chemical composition distribution ratio is determined, the volatile components contained in the raw materials such as fly ash, carbon dioxide in limestone and water in sludge bottom ash are released during the forging process, so the weight loss is 4 each read secret, by reaction of burning decomposition calculation Cac〇 = ··

CaC〇3 =>Ca0 + CO2----------------- 即 100 份 CaC〇3 =56 份 CaO + 44 份 C〇2 18 200426130 污泥底灰中將有6%之水份蒸發-----------------------(2) 水泥生料中含75%之石灰石,其燒損量依(1)可求得c〇2之 量為 0· 44x0· 75=0· 3344 kg。 而依(2)式可得水份量為〇·〇6χ〇· 25=0. 〇15〇 kg。 故總燒相量為 0· 3344 kg + 0· 0150 kg=〇· 3494 kg 即一公斤水泥生料(CaC〇3含量75%)可產生〇· 65呔之水泥熟 料,至於CaC〇3含量不同時,可以依下式得水泥生料量: a= Cl-〇.44xCaC〇3 (%)/100) +0. 〇6x (l〇〇-CaC〇3 (%) /100)--------------------------------------------(i) 每公斤生料所產生之熟料公斤熟料/公斤生料------(2) b=l/2 生料/熟料---------------------------(3) c=CaC〇3 (%) x56/2xl00------------------------(4) 由(1) (3) (4)或計算並依統計可知每生產一公斤熟料約需 生產1· 55〜1· 60公斤水泥生料,配合比例之概算可採用化學比例 法’由各原料中Si〇2、Al2〇3、Fe2〇3等成分緞燒時,所耗之CaO與提 供之CaO量直接求得原料配比。 2.3 Si〇2 + 1.7 (Al2〇3+Fe2〇3X〇.6) =CaO+l. 4Mg+0. 7S〇3 Si〇2x2· 8=燒成3CaO· Si〇2時所耗之CaO量CaC〇3 => Ca0 + CO2 ----------------- 100 parts CaC〇3 = 56 parts CaO + 44 parts C〇2 18 200426130 6% of the water is evaporated ----------------------- (2) 75% of limestone is contained in the cement raw material, and the burning loss depends on (1 ) The amount of co2 can be found to be 0.444x0. 75 = 0. 3344 kg. According to the formula (2), the water content can be obtained as 0.06 × 0.25 · 0.15 = 0 kg. Therefore, the total amount of burnt phase is 0.3344 kg + 0.3150 kg = 0.3494 kg, that is, one kilogram of cement raw material (CaC03 content 75%) can produce cement clinker of 65.5%, as for the content of CaC03 At different times, the amount of cement raw material can be obtained according to the following formula: a = Cl-0.44xCaC〇3 (%) / 100) + 0.06x (100-CaC〇3 (%) / 100) --- ----------------------------------------- (i) per kilogram of raw material Kg of clinker / kg of clinker ------ (2) b = l / 2 clinker / clinker --------------------- ------ (3) c = CaC〇3 (%) x56 / 2xl00 ------------------------ (4) consists of (1 ) (3) (4) Or it can be calculated and calculated that each kilogram of clinker needs to produce about 1.55 to 1.60 kilograms of cement raw material. The approximate ratio of the proportion can be calculated using the chemical ratio method 'Si from each raw material. 2. When the components such as Al2O3 and Fe2O3 are sintered, the amount of CaO consumed and the amount of CaO provided directly determine the raw material ratio. 2.3 Si〇2 + 1.7 (Al2〇3 + Fe2〇3X〇.6) = CaO + 1.4 Mg + 0.7S〇3 Si〇2x2 · 8 = CaO amount consumed when firing 3CaO · Si〇2

Si〇2xl.9=燒成 2CaO· Si〇2時所耗之 CaO 量=>2·3= (2.8 + 1.9) /2 Αΐ2〇3χ1· 7=燒成 3CaO. Si〇2 時所耗之 CaO 量 19 200426130Si〇2xl.9 = CaO consumed when firing 2CaO · Si〇2 = > 2 · 3 = (2.8 + 1.9) / 2 Αΐ2〇3χ1 · 7 = consumed when firing 3CaO. Si〇2 CaO content 19 200426130

Fe2〇3X〇· 6 =同Ah〇3之相當量 MgOxl· 4=同CaO之相當量 S〇3X〇. 7 =同CaO之相當量 將前述均質製程的精確計算與調合後的水泥生料,自動依定量 的進入煅燒製程之窯燒設備中,進行各煅燒帶的煅燒製作,以及將 水泥生料中含存之有害物質,如有機類重金屬、戴奥辛類及氣化物 等,透過高溫煅燒環境進行分解於窯内含存之瓦斯中,經冷卻後結 合脫鹽技術、毒物分解技術與去金屬物技術,配合環保回收設備進籲 行回收與去除處理;經煅燒製程製成之水泥熟料,進一步經冷卻後 加入3〜5 %石膏,透過研磨設備粉碎磨粉,形成再生水泥製成品。 經前述均質製程的精確計算與調合後經本發明步驟製作之水 泥製程品,本發明之再生水泥化學成份比例(%)為(此數值將因 水泥生料之調配而有所變動): 熱減量 Si〇2 AI2O3 Fe2〇3 CaO MgO S〇3 Na2〇 K20 Cl 1.05 16. 95 7. 96 4. 40 61.04 1.84 3. 86 0. 28 0. 02 0. 053 本發明再生水泥之礦物組成比例(%)為(此數值將因水泥生 料之調配而有所變動):Fe2〇3X〇 · 6 = equivalent to Ah〇3 MgOxl · 4 = equivalent to CaO S〇3X0.7. = Equivalent to CaO Accurate calculation of the aforementioned homogeneous process and blended cement raw materials, Automatically and quantitatively enter the kiln firing equipment of the calcination process to perform the calcination of each calcination zone, and the harmful substances such as organic heavy metals, dioxins and gaseous substances contained in the cement raw material are carried out through a high-temperature calcination environment. It is decomposed in the gas contained in the kiln. After cooling, it combines desalination technology, poison decomposition technology and demetalization technology, and cooperates with environmental protection recycling equipment for recycling and removal. The cement clinker made by the calcination process is further processed by After cooling, 3 ~ 5% gypsum is added, and the grinding powder is pulverized through a grinding device to form a recycled cement product. After the precise calculation and blending of the aforementioned homogeneous process, the cement process product produced by the steps of the present invention after the homogeneous process, the chemical composition ratio (%) of the recycled cement of the present invention is (this value will vary due to the preparation of the cement raw material): heat reduction Si 〇2 AI2O3 Fe2〇3 CaO MgO S〇3 Na2〇K20 Cl 1.05 16. 95 7. 96 4. 40 61.04 1.84 3. 86 0. 28 0. 02 0. 053 Mineral composition ratio (%) For (this value will vary due to the deployment of cement raw materials):

CaS C2S CaA QAf _ 49 12 14 13 20 200426130 經前述本發明製造方法所製程之再生水泥製成品,可獲得之一 例值品質規格(此數值將因水泥生料之調配而有所變動):CaS C2S CaA QAf _ 49 12 14 13 20 200426130 An example of quality specifications can be obtained for recycled cement products manufactured by the aforementioned manufacturing method of the present invention (this value will vary due to the deployment of cement raw materials):

比表面積cm2 / g 凝結 4-100 夺刀凝hi --—-- 、終凝h-mSpecific surface area cm2 / g Condensation 4-100 Concentrated knife -----, final condensation h-m

安定性 壓縮強度 N/mm2Stability compressive strength N / mm2

5 2 · 4 氧化鎂% —-———. •氧化硫% -——__ 總驗% 斤—-——- 氣化物離子5 2 · 4 Magnesium Oxide% ———————. • Sulfur Oxide% -——__ Total Test% jin —-——- Vapor ion

3 · 863 · 86

熱減量% 1-05 、生方、、具體製造實例,根據本發明前述資源再生建材水泥之製 污水處理传以利用應掩埋廢棄之垃圾焚化所產生之底灰 、飛灰以及 生之/Τ泥’作為水泥主要成分之天鋪石原料的替代原 21 200426130 料’透過本發明前述製造方法暨步驟,得以製成完全不具有害物質 且氣含量在規定之G· 1%以下之再生水泥製成品;相較於習知水泥 暨普通波特蘭水泥,可以獲得料之品f ,並能使用於―般工程, 如公園路面舖裝工程、擁壁X程、料護岸王程、消波石製作、混 凝土碑、溝蓋側溝等,亦能用於一般建築構造之施工建材。但卻不 需開採與使用天然礦物來製作,不僅能有效的降低使用原料之成 本,更具有解決前述底灰、飛灰與污泥等廢棄物之掩埋及二次公害 問題;同時降低天然礦石開採使用以維護環境生態保護與天然資源_ 保存。 本發明所提供的資源再生建材水泥之製造方法及其製成品,務 須確實瞭解此處所宣佈的實施例係用來解釋而非用來過度限制本 發明的申請專利範圍,未在此處所述的其它實施例與申請,均視為 在本發明的範圍内。在此亦務須確實瞭解,雖然已經討論了本案資 源再生建材水泥之製造方法及其製成品的特定實施方式,但執行大 部份類似功能的這些實施結構暨仍為本發明的申請專利範圍所要 _ 保護的範_内。 【圖式簡單說明】 第一圖係本發明方法之流程圖。 第二圖係本發明方法之流程步驟方塊圖。 【主要元件符號說明】 步驟1 0 步驟1 1 步驟1 2 步驟1 3 步驟1 4 步驟1 5 22Heat reduction% 1-05, concrete, and specific manufacturing examples. According to the aforementioned invention, the waste water treatment of resource-recycling building materials and cement is transferred to the bottom ash, fly ash, and raw / T mud produced by incineration of waste that should be buried. 'Replacement of the original raw material of the sky pavement as the main component of cement 21 200426130' Through the aforementioned manufacturing method and steps of the present invention, it is possible to produce a recycled cement finished product that is completely free of harmful substances and has a gas content below the specified G · 1%; Compared with the conventional cement and ordinary Portland cement, the product f can be obtained, and can be used in general projects, such as park pavement engineering, wall-supporting X-process, material revetment process, wave-making stone manufacturing, Concrete monuments, ditch covers, side trenches, etc. can also be used as construction materials for general building structures. However, it does not require mining and production using natural minerals, which not only can effectively reduce the cost of using raw materials, but also solves the aforementioned landfill and secondary pollution problems of wastes such as bottom ash, fly ash and sludge; meanwhile, it reduces natural ore mining Use to maintain environmental protection and natural resources_ Preservation. The method for manufacturing the resource-recycling building material cement provided by the present invention and its finished products must be surely understood that the embodiments announced herein are intended to explain rather than to excessively limit the scope of patent application of the present invention. Other embodiments and applications are considered to be within the scope of the present invention. It is also important to understand here that although the specific method of manufacturing the resource-recycling building material cement and its finished products have been discussed in this case, these implementation structures that perform most of the similar functions are still required by the scope of the patent application of the present invention_ Within the scope of protection. [Schematic description] The first diagram is a flowchart of the method of the present invention. The second figure is a block diagram of the process steps of the method of the present invention. [Description of main component symbols] Step 1 0 Step 1 1 Step 1 2 Step 1 3 Step 1 4 Step 1 5 22

Claims (1)

200426130 十、申請專利範圍: 1·一種資源再生建材水泥之製造方法,包括: 提供經儲存的替帶天然礦物之礦石替代原料; 將該礦石替代原料利用前置製程,進行去金屬物並形成混合組 成之水泥生料儲置; 根據水泥製成品標準,利用均質製程,將前述水泥生料進行化 學成分與組成比例係數及限度之調合; 將經均質製程調合之水泥生料,輸入窯燒設備進行煅燒製程, 以化合反應取得水泥熟料;並透過緞燒製程之高溫環境,進行水泥 生料中含存之有害物質,進行分解於窯内含存之瓦斯中,以排放進 行環保處理; 再將前述水泥熟料冷卻並加入石膏等固形添加物,透過研磨設 備粉碎磨粉,形成再生水泥製成品。 2·如申請專利範圍第1項所述的資源再生建材水泥之製造方法, 其中該確石替代原料,係為廢棄之再生原料與石灰石原料所組成。 3 ·如申請專利制第1項所述的資源再生建材水泥之製造方法, 其中該礦石替代原料’係為賴焚倾產生之底灰、飛灰污水處 理產生之污泥以及石灰石等原料所組成。 4.如申請專利範圍第!項所述的資源再生建材水泥之製造方法, 其中知置製程更包括:將絲、污泥及石灰石等原料進行設定粒 度篩別之破碎處理,以及所含存金屬物之清除。 5·如申請專利範圍第!項所述的資源再生建材水泥之製造方法, 23 200426130 其中該均質製程,更包括,將礦石替代原料之再生原料組成之水泥 生料,根據水泥化學成分進行與其它天然原料之調合,與各化學成 分之比例係數及限度允許範圍,進行精確計算調配。 6·如申請專利範圍第1項所述的資源再生建材水泥之製造方法, 其中該煅燒製程係透過一窯燒設備進行,該窯燒設備係為一旋窯採 用。 7·如申請專利範圍第1項所述的資源再生建材水泥之製造方法, 其中該烺燒製程係透過一窯燒設備進行,該窯燒設備包括不同溫度籲 提供煅燒之預熱帶、煅燒帶與化合帶。 8·如申請專利範圍第1項所述的資源再生建材水泥之製造方法, 其中該緞燒製程中之水泥生料含存有害物質的分解排放,進一步結 合環保回收設備進行回收與去除處理。 9·如申請專利範圍第8項所述的資源再生建材水泥之製造方法, 其中S亥環保回收設備’包括用以進行有害重金屬處理之旋風集塵機 與袋式捕塵過濾設備;用以進行戴奥辛分解消除處理之急速冷卻籲 塔;以及用以進行瓦斯排放處理之脫硝設備。 10·如申請專利範圍第1項所述的資源再生建材水泥之製造方 法,其中該煅燒製程中之水泥生料含存有害物質的分解排放處理, 包括有機鹽類的氯化物離子、有害重金屬以及戴奥辛等有害物質的 分解排放。 1 1 ·如申請專利範圍第1〇項所述的資源再生建材水泥之製造方 2冬 200426130 法,其中該有機鹽類的氣化物離子的去除,係利用脫鹽技術進行脫 氣工程;即利用在水泥生料之均質製程中,添加適量之納化合物; 藉由锻燒製程,使生料中所含之多量氣離子(Gr)與鈉離子⑽ )結合成氣化鈉(NaCI),並揮發於瓦斯中,進而隨瓦斯排出,而 使製成品之水泥含㈣可符合G· 1%水泥質量規定之要求。 1 2如申請專利範圍第11項所述的資源再生建材水泥之製造方 法其中。亥於均質製程中添力口適量之納化合物,係為碳酸鈉等組群 之其一採用。 Φ 1 3 ·如”補細帛! Q項所述的資源再生雜水泥之製造方 法’其中該有害重金屬之去除,係結合去金屬質技術進行,即藉由 锻燒製程之回⑽锻燒,發生有害重金屬之熱分解為金屬離子蒸發, 並揮發於瓦斯中與HCI結合,而濃縮於熔解飛灰成微細粒子之金屬 鹽,隨瓦斯排放配合前述環保回收設備進行處理。 1 4 ·如申請專利範圍第i 3項所述的資源再生建材水泥之製造方 法’其中該隨瓦斯排放於環保回收設備之微細粒子之金屬帛,利用肇 旋風集塵機之_選,而將粗粒回收並送人如再次煅燒,至於含有 濃縮重金屬之鹽微細顆粒溶解飛灰,再經袋式捕塵過遽設備完全捕 集’即可完成水泥生料中之含存重金屬之去除;所產生之濃縮重金 屬之鹽微細雛雜歧,得進-步由重金屬工廠再生提煉。 1 5 ·如申請專利範圍第1〇項所述的資源再生建材水泥之製造方 法’其中該戴奥辛之去除,係利用毒物分解技術進行;即利用煅燒 25 200426130 製程之咼溫锻燒環境’使戴奥辛類發生脫鹽素反應之氣與氫置換, 而完全分解為C〇2、H2〇、CaCL·,並揮發於瓦斯中,並透過將高溫 排放瓦斯急速降溫至戴奥辛之新合成反應溫度(約3〇〇ϊ)以下, 抑止戴奥辛之新合成反應,使戴奥辛可被完全達到分解消除。 1 6 · —種資源再生建材水泥之製造方法,包括·· 提供經儲存之再生原料; 將該再生原料搭配石灰石利用前置製程,分別進行去金屬物, 進而混合組成水泥生料儲置; Φ 根據水泥製成品標準,利用均質製程,將前述水泥生料進行化 學成分與組成比例係數及限度之調合; 將經均質製程調合之水泥生料,輸入窯燒設備進行煅燒製程, 以化合反應取得水泥熟料;並透過煅燒製程之高溫環境,進行水泥 生料中含存之有害物質’進行分解於窯内含存之瓦斯中,以排放進 行環保處理; 再將前述水泥熟料冷卻並加入石膏等固形添加物,透過研磨設_ 備粉碎磨粉,形成再生水泥製成品。 1 7 ·如申請專利範圍第16項所述的資源再生建材水泥之製造方 法’其中該再生原料,係為垃圾焚化所產生之底灰、飛灰、污水處 理產生之污泥。 1 8 ·如申請專利範圍第16項所述的資源再生建材水泥之製造方 法,其中該前置製程更包括··將再生原料之底灰與污泥,以及石灰 26 200426130 石等原料進行設定粒度篩別之破碎處理,以及所含存金屬物之清 除。 1 9·如申請專利範圍第16項所述的資源再生建材水泥之製造方 法,其中該均質製程,更包括:將再生原料與石灰石組成之水泥生 料,根據水泥化學成分進行與其它天然原料之調合,與各化學成分 之比例係數及限度允許範圍,進行精確計算調配。 2 0 ·如申請專利範圍第丄6項所述的資源再生建材水泥之製造方 法,其中該煅燒製程係透過一窯燒設備進行,該窯燒設備係為一旋籲 熏採用。 2 1 ·如申請專利範圍第i 6項所述的資源再生建材水泥之製造方 法,其中該煅燒製程係透過一窯燒設備進行,該窯燒設備包括不同 溫度提供煅燒之預熱帶、緞燒帶與化合帶。 2 2·如申請專利範圍第16項所述的資源再生建材水泥之製造方 法,其中該緞燒製程中之水泥生料含存有害物質的分解排放,進一 步結合環保回收設備進行回收與去除處理。 _ 2 3·如申請專利範圍第2 2項所述的資源再生建材水泥之製造方 法,其中該環保回收設備,包括用以進行有害重金屬處理之旋風集 塵機與袋式捕塵過濾設備;用以進行戴奥辛分解消除處理之急速冷 卻塔;以及用以進行瓦斯排放處理之脫硝設備。 2 4 ·如申請專利範圍第16項所述的資源再生建材水泥之製造方 法’其中該烺燒製程中之水泥生料含存有害物質的分解排放處理, 27 200426130 包括有機鹽類的氣化物離子、有害重金屬以及戴奥辛等有害物質的 分解排放。 2 5·如申請專利範圍第2 4項所述的資源再生建材水泥之製造方 法,其中該有機鹽類的氣化物離子的去除,係利用脫鹽技術進行脫 氯工程;即利用在水泥生料之均質製程中,添加適量之鈉化合物; 藉由煅燒製程,使前述生料中所含之多量氣離子(CI-)與鈉離子 (Na+)結合成氣化納(NaCI),並揮發於瓦斯中,進而隨瓦斯排出, 而使製成品之水泥含氣量可符合〇· 1%水泥質量規定之要求。 籲 2 6 ·如申請專利範圍第2 5項所述的資源再生建材水泥之製造方 法,其中該於均質製程中添加適量之鈉化合物,係為碳酸納等組群 之其一採用。 2 7 ·如申請專利範圍第2 4項所述的資源再生建材水泥之製造方 法,其中該有害重金屬之去除,係結合去金屬質技術進行,即藉由 煅燒製程之高溫煅燒,發生有害重金屬之熱分解為金屬離子蒸發, 並揮發於瓦斯中與HCI結合,而濃縮於熔解飛灰成微細粒子之金屬· 鹽,隨瓦斯排放配合前述環保回收設備進行處理。 2 8·如申請專利範圍第2 7項所述的資源再生建材水泥之製造方 法,其中該隨瓦斯排放於環保回收設備之微細粒子之金屬鹽,利用 旋風集塵機之篩選,而將粗粒回收並送入窯内再次緞燒,至於含有 漠縮重金屬之鹽微細顆粒熔解飛灰,再經袋式捕塵過濾設備完全捕 集’即可完成水泥生料中之含存重金屬之去除;所產生之濃縮重金 28 200426130 屬之鹽微細顆粒熔解飛灰,得進一步由重金屬工廠再生提煉。 2 9·如申請專利範圍第2 4項所述的資源再生建材水泥之製造方 法,其中S亥戴奥辛之去除,係利用毒物分解技術進行;即利用煅燒 製程之高溫煅燒環境,使戴奥辛類發生脫鹽素反應之氣與氫置換, 而7G全分解為C〇2、H2〇、CaCl2 ,並揮發於瓦斯中,並透過將高溫 排放瓦斯急速降溫至戴奥辛之新合成反應溫度(約3〇〇。〇以下, 抑止戴奥辛之新合成反應,使戴奥辛可被完全達到分解消除。 3 0 · —種資源再生建材水泥製成品,其組成包括·· 籲 以再生原料為主要原料,搭配石灰石組成水泥生料,透過均質 製程、锻燒製程的製作,加入固形添加物,研磨形成再生水泥製成 品0 3 1 ·如申請專利範圍第3〇項所述的資源再生建材水泥製成品, 其中该再生原料,係為垃圾焚化所產生之底灰、飛灰、污水處理產 生之污泥採用。 3 2·如申請專利範圍第3 〇項所述的資源再生建材水泥製成品,籲 其中該再生原料,係透過前置製程,形成設定之粒別篩選與去金屬 物之原料。 3 3·如申請專利範圍第3 〇項所述的資源再生建材水泥製成品, 其中該石灰石,係透過前置製程,形成設定之粒別篩選與去金屬物 之原料。 34·如申請專利範圍第3〇項所述的資源再生建材水泥製成品, 29 200426130 其中該再生原料所含存之有害物質,係於般燒製程的高溫環境進行 熱分解,配合環保回收設備為回收與去除,以獲得無害之再生水泥 製成品。 3 5·如申請專利範圍第3 4項所述的資源再生建材水泥之製造方 法,其中該環保回收設備,包括用以進行有害重金屬處理之旋風集 塵機與袋式捕塵過濾設備;用以進行戴奥辛分解消除處理之急速冷 卻塔;以及用以進行瓦斯排放處理之脫硝設備。 3 6·如申請專利範圍第3 4項所述的資源再生建材水泥之製造方鲁 法,其中該缎燒製程中之水泥生料含存之有害物質的分解排放處 理,包括有機鹽類的氣化物離子、有害重金屬以及戴奥辛等有害物 質的分解排放。 3 7 ·如申請專利範圍第3 β項所述的資源再生建材水泥之製造方 法,其中該有機鹽類的氣化物離子的去除,係利用脫鹽技術進行脫 氣工程;即利用在水泥生料之均質製程中,添加適量之鈉化合物; 藉由煅燒製程,使前述生料中所含之多量氣離子(Ci-)與納離子 _ (Na+)結合成氣化鈉(NaCI),並揮發於瓦斯中,進而隨瓦斯排出, 而使製成品之水泥含氣量可符合〇· 1%水泥質量規定之要求。 3 8 ·如申請專利範圍第3 7項所述的資源再生建材水泥之製造方 法,其中該於均質製程中添加適量之鈉化合物,係為碳酸納等組群 之其一採用。 3 9·如申請專利範圍第3 6項所述的資源再生建材水泥之製造方 30 200426130 法’其中該有害重金屬之去除,係結合去金屬質技術進行,即藉由 煅燒製程之高溫缎燒,發生有害重金屬之熱分解為金屬離子蒸發, 並揮發於瓦斯中與HCI結合,而濃縮於熔解飛灰成微細粒子之金屬 鹽,隨瓦斯排放配合前述環保回收設備進行處理。 4 0·如申請專利範圍第3 9項所述的資源再生建材水泥之製造方 法’其中該隨瓦斯排放於環保回收設備之微細粒子之金屬鹽,利用 方疋風集塵機之篩選,而將粗粒回收並送入窯内再次煅燒,至於含有 濃縮重金屬之鹽微細顆粒熔解飛灰,再經袋式捕塵過濾設備完全捕鲁 集’即可完成水泥生料中之含存重金屬之去除;所產生之濃縮重金 屬之鹽微細顆粒熔解飛灰,得進一步由重金屬工廠再生提煉。 4 1 ·如申請專利範圍第36項所述的資源再生建材水泥之製造方 法’其中該戴奥辛之去除,係利用毒物分解技術進行;即利用煅燒 製程之高溫煅燒環境,使戴奥辛類發生脫鹽素反應之氣與氫置換, 而完全分解為C 〇2、H2〇、CaCL·,並揮發於瓦斯中,並透過將高溫 排放瓦斯急速降溫至戴奥辛之新合成反應溫度(約3〇〇〇c )以下, 抑止戴奥辛之新合成反應,使戴奥辛可被完全達到分解消除。 4 2·如申請專利範圍第3 〇項所述的資源再生建材水泥製成品, 其中該固形添加物係為石膏採用添加。 31200426130 10. Scope of patent application: 1. A method for manufacturing resource-recycling building material cement, including: providing a stored raw material to replace the natural mineral ore; using the pre-process to remove the metal and form a mixture Storage of the cement raw material composition; According to the standards of cement products, the homogeneous process is used to blend the aforementioned chemical raw materials with the composition ratio coefficients and limits; the cement raw material blended through the homogeneous process is input to the kiln firing equipment. The calcination process obtains the cement clinker through the combination reaction; and through the high-temperature environment of the satin firing process, the harmful substances contained in the cement raw meal are decomposed into the gas contained in the kiln and discharged for environmental protection treatment; The cement clinker is cooled, solid additives such as gypsum are added, and the grinding powder is pulverized by a grinding device to form a recycled cement finished product. 2. The method for manufacturing a resource-recycling building material cement as described in item 1 of the scope of the patent application, wherein the solid stone substitute raw material is composed of waste recycled raw materials and limestone raw materials. 3. The manufacturing method of the resource-recycling building material cement according to item 1 of the patent application system, wherein the ore substitute raw material is composed of raw materials such as bottom ash produced by Lai Ping, sludge produced from fly ash sewage treatment, and limestone. . 4. If the scope of patent application is the first! The method for manufacturing a resource-recycling building material cement as described in the above item, wherein the knowing process further includes: performing a crushing treatment of setting the size of the raw materials such as silk, sludge, and limestone, and removing the contained metal objects. 5 · If the scope of patent application is the first! The production method of the resource-recycling building material cement as described in the item, 23 200426130. The homogeneous process further includes a cement raw material composed of recycled raw materials of ore substitute raw materials, and blending with other natural raw materials according to the chemical composition of the cement. The proportion coefficient and limit allowable range of ingredients are accurately calculated and allocated. 6. The manufacturing method of the resource-recycling building material cement according to item 1 of the scope of the patent application, wherein the calcination process is performed by a kiln firing equipment, which is adopted by a rotary kiln. 7. The manufacturing method of resource-recycling building material cement as described in item 1 of the scope of patent application, wherein the sintering process is performed through a kiln firing equipment, which includes preheating zones, calcining zones and Chemical band. 8. The manufacturing method of the resource-recycling building material cement as described in item 1 of the scope of the patent application, wherein the cement raw material in the satin firing process contains decomposition and discharge of harmful substances, and is further combined with environmental protection recycling equipment for recycling and removal treatment. 9. The manufacturing method of the resource-recycling building material cement as described in item 8 of the scope of the patent application, wherein the environmental protection recycling equipment of the Hai 'includes a cyclone dust collector and a bag-type dust filtering device for the treatment of harmful heavy metals; used for dioxin decomposition Elimination of rapid cooling towers; and denitration equipment for gas emission treatment. 10. The method for manufacturing a resource-recycling building material cement as described in item 1 of the scope of the patent application, wherein the cement raw material in the calcination process contains decomposition and discharge treatment of harmful substances, including chloride ions of organic salts, harmful heavy metals, and Decomposition and release of hazardous substances such as dioxin. 1 1 · The method for manufacturing the resource-recycling building materials and cement as described in item 10 of the scope of the patent application, the winter method 200426130, wherein the removal of the gaseous ion of the organic salt is a degassing project using a desalination technology; In the homogeneous production process of cement raw material, an appropriate amount of sodium compound is added; by the calcination process, a large amount of gas ions (Gr) and sodium ions ()) contained in the raw material are combined to form sodium vaporized (NaCI), which is volatilized in In the gas, and then discharged with the gas, the cement content of the finished product can meet the requirements of G · 1% cement quality regulations. 1 2 The manufacturing method of the resource-recycling building material cement according to item 11 of the scope of patent application. Hai added a suitable amount of sodium compounds in the homogenization process, which is one of the groups used by sodium carbonate. Φ 1 3 · As described in the “refining process!” The production method of resource-recycling miscellaneous cement as described in item Q ', wherein the removal of the harmful heavy metal is carried out in combination with demetalization technology, that is, by the re-calcination and calcination of the calcination process, When the thermal decomposition of harmful heavy metals occurs, the metal ions evaporate, and they are volatilized in the gas and combined with HCI, and are concentrated in the metal salt that melts into the fly ash to become fine particles, and are processed with the aforementioned environmental protection recycling equipment as the gas is discharged. 1 4 · If you apply for a patent The manufacturing method of the resource-recycling building material cement described in the item i 3 of the scope 'where the metal particles of the fine particles discharged with the gas in the environmental protection recycling equipment are collected by the Zhao cyclone dust collector, and the coarse particles are recovered and sent to another person. Calcining, as for the fine particles of salt containing concentrated heavy metals dissolve fly ash, and then completely capture it by a bag-type dust catcher, the removal of stored heavy metals in the cement raw meal can be completed; the salts of concentrated heavy metal salts are produced finely Miscellaneous, can be further-refined by heavy metal factories. 1 5 · The manufacturing method of the resource-recycling building materials cement as described in the scope of patent application No. 10 ' The removal of dioxin is carried out using toxicant decomposition technology; that is, the dioxin reaction gas and hydrogen are replaced by the calcination environment of the calcination 25 200426130 process, and completely decomposed into C02, H2〇, CaCL · is volatilized in the gas, and the temperature of the high-temperature exhaust gas is rapidly reduced to below the temperature of the new synthesis reaction of dioxin (about 300 ° F), which suppresses the new synthesis reaction of dioxin, so that dioxin can be completely decomposed and eliminated. 1 6 · A manufacturing method of resource-recycling building materials and cement, including: · Providing stored recycled raw materials; using the pre-process with the recycled raw materials in combination with limestone, separately removing metals, and then mixing to form cement raw material storage; Φ according to Standards for cement finished products. The homogeneous process is used to blend the aforementioned cement raw materials with chemical components and composition ratio coefficients and limits. The cement raw materials blended through the homogeneous process are input to the kiln firing equipment for the calcination process. And through the high temperature environment of the calcination process, the harmfulness contained in the cement raw material is carried out The quality is decomposed into the gas contained in the kiln, and it is discharged for environmental protection treatment; the aforementioned cement clinker is cooled and solid additives such as gypsum are added, and the grinding powder is pulverized through the grinding equipment to form a recycled cement product. 1 7 · The manufacturing method of the resource-recycling building material cement as described in item 16 of the scope of the applied patent ', wherein the recycled raw materials are bottom ash, fly ash and sewage sludge generated from waste incineration. 1 8 · If applied The method for manufacturing a resource-recycling building material cement as described in item 16 of the patent scope, wherein the pre-processing process further includes the crushing treatment of setting the particle size of the raw materials such as the bottom ash and sludge of the recycled raw materials, and lime 26 200426130 stone. And the removal of the contained metal objects. 19 · The manufacturing method of the resource-recycling building material cement as described in item 16 of the patent application scope, wherein the homogeneous process further includes: a cement raw material composed of recycled raw materials and limestone, Blend with other natural raw materials according to the chemical composition of the cement, and the proportionality coefficient and limit allowable range of each chemical composition for accurate calculation Deployment. 20 • The method for manufacturing a resource-recycling building material cement as described in item 26 of the scope of application for a patent, wherein the calcination process is performed by a kiln firing equipment, which is adopted by a spin-fume process. 2 1 · The method for manufacturing a resource-recycling building material cement as described in item i 6 of the scope of patent application, wherein the calcination process is performed by a kiln firing equipment, which includes preheated and satin ribbons that are calcined at different temperatures. And chemical band. 2 2. The manufacturing method of the resource-recycling building material cement as described in item 16 of the scope of the patent application, wherein the cement raw material in the satin firing process contains the decomposition and discharge of harmful substances, and is further combined with environmental protection recycling equipment for recycling and removal treatment. _ 2 3 · The method for manufacturing a resource-recycling building material cement as described in item 22 of the scope of the patent application, wherein the environmentally-friendly recycling equipment includes a cyclone dust collector and a bag-type dust-collecting filter device for processing harmful heavy metals; Rapid cooling tower for dioxin decomposition and elimination treatment; and denitration equipment for gas emission treatment. 2 4 · The manufacturing method of resource-recycling building material cement as described in item 16 of the scope of the patent application, wherein the cement raw material in the sintering process contains decomposition and discharge treatment of harmful substances, 27 200426130 including gaseous ion of organic salts , Harmful heavy metals, and the release of hazardous substances such as dioxin. 25. The method for manufacturing a resource-recycling building material cement as described in item 24 of the scope of the patent application, wherein the removal of the gaseous ion of the organic salt is a dechlorination project using a desalination technology; In the homogenization process, an appropriate amount of sodium compound is added; through the calcination process, a large amount of gas ions (CI-) and sodium ions (Na +) contained in the aforementioned raw material are combined to form sodium gasification (NaCI) and volatilized in gas. , And then discharged with the gas, so that the cement gas content of finished products can meet the requirements of 0.1% cement quality regulations. Call 26. The method for manufacturing the resource-recycling building material cement as described in item 25 of the scope of patent application, wherein the addition of an appropriate amount of sodium compound in the homogeneous process is one of the groups of sodium carbonate and the like. 2 7 · The manufacturing method of the resource-recycling building material cement as described in item 24 of the scope of the patent application, wherein the removal of the harmful heavy metals is performed in combination with demetallization technology, that is, the high-temperature calcination of the calcination process causes the occurrence of harmful heavy metals. Thermal decomposition is the evaporation of metal ions, which is volatilized in gas and combined with HCI, and is concentrated in the molten metal ash that is formed into fine particles, and is processed with the aforementioned environmental protection recycling equipment as the gas is discharged. 28. The method for manufacturing a resource-recycling building material cement as described in item 27 of the scope of the patent application, wherein the metal salt of the fine particles discharged with the gas to the environmental protection recovery equipment is screened by a cyclone dust collector, and the coarse particles are recovered and combined. Sent into the kiln for satin firing again. As for the fine particles of salt containing indifferent heavy metals, the fly ash will be melted and then fully captured by the bag-type dust filter equipment to complete the removal of the stored heavy metals in the cement raw meal. Concentrated heavy gold 28 200426130 The fine particles of the salt are melted and the fly ash can be further regenerated from the heavy metal factory. 29. The manufacturing method of the resource-recycling building material cement as described in item 24 of the scope of the patent application, wherein the removal of Schiothosin is carried out using poison decomposition technology; that is, the high-temperature calcination environment of the calcination process is used to desalinate the dioxin The gas of the reaction is replaced with hydrogen, and 7G is completely decomposed into CO2, H2O, CaCl2, and volatilizes in the gas, and the high-temperature exhaust gas is rapidly cooled to the new synthesis reaction temperature of dioxin (about 300. In the following, the new synthetic reaction of dioxin is suppressed, so that dioxin can be completely decomposed and eliminated. 3 0 · A kind of resource-recycling building materials made of cement, the composition of which includes: · Recycling raw materials are used as the main raw materials, and limestone is used to make cement raw materials. Through the production of homogeneous process and calcination process, adding solid additives, grinding to form recycled cement products 0 3 1 · Recycling building materials cement products as described in item 30 of the patent application scope, where the recycled raw materials are The bottom ash, fly ash and sewage sludge generated from waste incineration are used. 3 2 · If the scope of patent application is No. 30 The resource-recycling building material cement manufactured product mentioned above, it is appealed that the recycled raw material is formed through the pre-process to form the set granular screening and demetallized raw material. 3 3. Resource recycling as described in item 30 of the scope of patent application Cement products made of building materials, in which the limestone is formed through a pre-process to form a set of granular screening and demetallizing raw materials. 34. Cement products made of resource-recycling building materials as described in item 30 of the scope of patent application, 29 200426130 Among them, the harmful substances contained in the recycled raw materials are thermally decomposed in the high-temperature environment of the general firing process, and are recycled and removed with environmental protection recycling equipment to obtain harmless recycled cement products. 3 5 · If the scope of patent application is the third The method for manufacturing a resource-recycling building material cement according to item 4, wherein the environmentally-friendly recycling equipment includes a cyclone dust collector and a bag-type dust collection and filtering device for treating harmful heavy metals; a rapid cooling tower for performing dioxin decomposition and elimination treatment; and Denitration equipment used for gas emission treatment. 3 6 · Resources as described in item 34 of the scope of patent application The manufacturing method of recycled building material cement, in which the decomposition and emission treatment of harmful substances contained in the cement raw material in the satin firing process includes the decomposition and emission of organic salt gaseous ions, harmful heavy metals, and dioxin. 3 7 · The method for manufacturing a resource-recycling building material cement as described in item 3 β of the scope of the patent application, wherein the removal of the gaseous ion of the organic salt is a degassing project using a desalination technology; that is, the homogeneity of the raw material in the cement is used In the process, an appropriate amount of sodium compound is added; by the calcination process, a large amount of gas ions (Ci-) and nano-ions (Na +) contained in the aforementioned raw material are combined to form sodium gasification (NaCI) and volatilized in gas. , And then discharged with the gas, so that the cement gas content of finished products can meet the requirements of 0.1% cement quality regulations. 38. The method for manufacturing a resource-recycling building material cement as described in item 37 of the scope of the patent application, wherein an appropriate amount of sodium compound is added to the homogenization process, which is one of the groups such as sodium carbonate. 3 9 · According to Article 36 of the scope of patent application, the manufacturer of the resource-recycling building material cement 30 200426130 method, wherein the removal of the harmful heavy metal is performed in combination with demetalization technology, that is, by high-temperature satin firing in the calcination process, The thermal decomposition of harmful heavy metals occurs as metal ions evaporate, and volatilizes in the gas to combine with HCI, and is concentrated in the molten fly ash to form fine particles of metal salts, which are processed with the aforementioned environmental protection recycling equipment as the gas is discharged. 40. The method for manufacturing a resource-recycling building material cement as described in Item 39 of the scope of the patent application, wherein the metal salt of the fine particles discharged to the environmental protection recovery equipment with the gas is screened by the Fangfeng dust collector, and the coarse particles are Recovered and sent to the kiln for re-calcination. As for the fine particles of salt containing concentrated heavy metals, the fly ash is melted and then completely collected by a bag-type dust-collection filtering device to complete the removal of the heavy metals in the cement raw meal. The fine particles of concentrated heavy metal salt melt the fly ash, which can be further refined by the heavy metal factory. 4 1 · The manufacturing method of the resource-recycling building material cement as described in item 36 of the scope of the patent application, wherein the dioxin is removed using poison decomposition technology; that is, the high-temperature calcination environment of the calcination process is used to cause the desalination reaction of the dioxin The gas is replaced with hydrogen, and it is completely decomposed into C02, H2O, CaCL, and volatilizes in the gas, and the temperature of the high-temperature exhaust gas is rapidly reduced to below the new synthesis reaction temperature (about 300c) of dioxin. Inhibit the new synthetic reaction of dioxin, so that dioxin can be completely decomposed and eliminated. 4 2. The cement recyclables for building materials as described in item 30 of the scope of patent application, wherein the solid additive is gypsum. 31
TW093120583A 2004-07-09 2004-07-09 Manufacturing method and product of resource regenerated cement for construction material TW200426130A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI460143B (en) * 2010-09-14 2014-11-11 Univ Nat Ilan Method for producing eco-cement by using tft-lcd waste glass
TWI631091B (en) * 2017-03-03 2018-08-01 蔣本基 A method of modifying alkaline solid wastes as green construction materials
CN110357510A (en) * 2019-08-30 2019-10-22 江西鑫泉固废处理有限公司 A kind of environmentally friendly process for producing bricks of the object containing waste incineration

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI460143B (en) * 2010-09-14 2014-11-11 Univ Nat Ilan Method for producing eco-cement by using tft-lcd waste glass
TWI631091B (en) * 2017-03-03 2018-08-01 蔣本基 A method of modifying alkaline solid wastes as green construction materials
CN110357510A (en) * 2019-08-30 2019-10-22 江西鑫泉固废处理有限公司 A kind of environmentally friendly process for producing bricks of the object containing waste incineration

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