TW201014809A - Cold bonding process for incineration bottom ash-sludge rinsing - Google Patents

Abstract

A cold bonding process for incineration bottom ash-sludge is disclosed. Sludge produced by a rinsing procedure of incineration bottom ash is processed by concentration tank and performed by mud/water separation processing to form a bottom ash-sludge. After drying, the bottom ahs-sludge is stirred with a curing agent or cement or further selected from calcium sulfate (gypsum), calcium phosphate or salt containing calcium to form a proportional mixture having proper water content. A finished product with required shape is then produced by granulating injection, injecting, granulating or die casting. The finished product is further applied to need of market like plain concrete, road grading, contaminated concrete, and base backfilling which have the utilization value in the industry. The invention does not need the high temperature treatment of sintering which have the advantage of energy saving and carbon reduction, and furthermore the bottom ash sludge can be adequately utilized which is relatively comply with the principle of environmental protection.

Description

201014809 六、發明說明： 【發明所屬之技術領域】 ，發日聽指-種焚化絲水洗污泥之冷驗程，係 ，水洗程序之水洗處理触難生之污I的再加工處库，直 5 T可^骨材成品以提供做為無筋混凝土、道路級配 ^ 土、基地回填等用途。 力貞/晃凝 【先前技術】 按，公告在先之發明第1288028號「焚化底渣水洗裎床 利案係為一種應用於處理焚化底渣並產 性 丄^ ❿ 10 渣水洗程序，而本發明則主要係以將 • 所^生之抑相再加王朗输財#，崎合環保需灰 、作設I產出骨材成品以供產業上之再利用為前提而加以研究與創 ^以本發明之主要目的乃在於提供一種焚化底渣水洗 】5 將焚化底渣水洗程序所產出之污泥經濃縮槽以2 理後形成之紐水洗污泥先經乾燥後再與固化劑或 iii步選用之硫_(石膏）或魏辆石夕酸_含敏i ΐΖίϊ而ί成適當含水率的比例混合物，再經由射出或造粒 鼉2需求提供做為無筋混凝土、道路級配、劣質混凝土、基地回 填等用途’而具有產業上之利用價值。 本，之次-目的乃在紐供-種焚絲财洗污泥之冷結 机，本發明不需要燒結成形之咼溫處理流程，進而具有 碳之優點，且又可充分利用焚化底渣水洗處理流程所產生之 25泥，而相對亦較符合環保之原則。 / 【發明内容】 種焚化底渣水洗污泥之冷結流程，係可將焚化底渣水洗程 ，所產生之污泥經濃縮槽以及泥、水分離處理後形成之底渣水洗 污泥先乾燥後再與固化劑或水泥或進—步選用硫酸約(石膏)或磷 3 201014809 ====:2=含ί率的比例混 價值、.太路ΐΐΐ 基地_等用途，而具有產業上之利用 碳之優ί 赫之高减赠程，進轉有節能減 之原則。又可充/刀利用底渣水洗污泥，而相對亦較符合環保 兹配合圖式詳加說明如后。 【實施方式】 10 15 如圖一所示係本發明之第一實施例，本發明一種焚化底渣水 ，污泥之冷結流程，係將焚化底渣（11)經破碎（12)、磁選〇^)及 篩分(14)處理後經由水洗設備之水洗（15)處理流程所產生的污泥 之再加工處理程序，係包括有下列流程： 濃縮槽（16) ’將前述水洗(15)處理流程產生的泥水導入濃縮槽 (16)，令污泥往下沈澱； 泥、水分離(Π)，將前述沈澱之濃縮污泥送入濾壓機或離心機將 污泥與廢水分離即形成底渣水洗污泥（19)，而分離後的廢水則 可進一步進行廢水處理(18)以更符合環保之原則； 乾燥(20)，將前述泥、水分離(17)流程所得之底渣水洗污泥〇9) 以自然乾燥或藉由乾燥設備進行乾燥處理，並乾燥處理後之底 渣水洗污泥(19)含水率為10〜30% ; 配方比例(21)，選用70%〜95%之底渣水洗污泥(19)、5%〜30%的水 泥(22)或進一步增加選用1%〜20%之固態（例如粉末狀）的硫酸 鈣(石膏）或磷酸鈣或矽酸鈣或含鈣之塩類（23); 25攪拌(24)，將前述底渣水洗污泥(19)、水泥(22)或進一步選用之 硫酸舞(石膏）或磷酸妈或矽酸飼或含鈣之塩類(23)—起放入攪 拌機進行攪拌； 混練(25)，前述底渣水洗污泥（19)、水泥(22)或進一步選用之硫 酸鈣(石膏）或磷酸鈣或矽酸鈣或含鈣之塩類(23)—起攪拌之後 4 201014809 再經由練土機之混練以大幅減少氣泡而成為具有均勻密度之比 例混合物，該比例混合物之含水率約5%〜25% ; 射出或造粒或壓鑄成型（26)，將前述經由混練(25)流程處理後含 水率為15%〜25%之比例混合物藉由射出成型機射出成型為所需 形狀之骨材成品（27)，或者將前述混練(25)流程處理後所得之 含水率為5%〜15%的比例混合物經由造粒設備或壓鏵設備之加 工而得到複數個粒狀或所需形狀之骨材成品（27); 另外，前述射出或造粒或壓鑄成型（26)流程中藉由射出成型 機所射出成型之骨材成品（27)係可呈條狀或其他形狀，並可進一 步藉由切斷設備將條狀之骨材成品（27)切成所需長度之塊狀體； …藉由前述流程所得之骨材成品（27)可因應市場需求提供做為 無筋混凝土、道路級配、劣質混凝土、基地回填等用途，而具有 產業上之利用價值，並由於不需經由燒結成形而相對 能 及符合環保概念之優點。 15 蠹( 請另配合參考圖二所示係本發明之第二實施行，本發明 渣水洗污泥之冷結絲，储焚化総⑴)經破碎(12)、 後經由水洗設備之水洗(15)處=所 座生的汚泥之再加工處理程序，係包括有下列流程： 濃===^(15)處理流程產生的泥水導入濃縮槽 原則； 、]了進一步進行廢水處理（18)以更符合環保之 乾乾水分離⑽流程所得之底潰水洗污泥⑽ 渣水洗污泥⑽燥處理，並麵處理後之底 30%〜10%的 選用70%〜_之底渣水洗污泥(19)、 25 201014809 攪拌«4) ’將前述底渣水洗污泥(19)與固化劑(22，）一起放入擾摔 機進行攪拌而得到含水率10%〜2〇%的比例混合物； 造粒射出成型(26)’將前述經由搜拌(24)流程處理後含水率為1〇% 二之比例混合物藉由造粒設備加工而得到複數個粒狀成品 5 \ί\) 9 另外，前述造粒射出成型(26)流程所得之複數個粒狀成品(27) 係可進一步篩分(28)流程處理，乃係藉由篩分設備篩選出所需規 格尺寸的粒狀成品； 藉由前述流程所得之成品(27)可因應市場需求提供做為盔筋 ίο混凝土、道路級配、劣質混凝土、基地回填等用途，而具有產業 上之利用價值，並由於不需經由燒結成形而相對達到節能以及符 合環保概念之優點。 綜上所述’本發明可歸納具有下列增進功效： 1·本發明可將焚化底渣水洗程序所產生之泥水經濃縮槽（16)以及 15 泥、水分離(17)處理後形成之底渣水洗污泥(19)先經乾燥(20) 處理之後再與固化劑（22，）或水泥(22)或進一步選用之硫酸鈣 (石膏）或填酸#5或矽酸飼或含舞之塩類（23)經攪拌(24)處理之 後而形成適當含水率之比例混合物，然後經由射出或造粒或壓 鑄成型（26)之處理流程即產出所需形狀的成品(27)，進而可因 應市場需求提供做為無筋混凝土、道路級配、劣質混凝土、基 地回填等用途’而具有產業上之利用價值。 2,不需要燒結成形之高溫處理流程，進而具有節能減碳之優點， 且又可充分利用底渣水洗污泥，而相對亦較符合環保之原則。 是以’本發明乃確具其產業上之利用價值，乃謹以發明專利 25申請之’懇請鈞局貴審查委員予以詳查並賜准專利，至感德便。 惟，以上所述者僅為本發明之較佳實施例而已，當不能以之 限定本發明實施之範圍，舉凡依本發明申請專利範圍所作之均等 變化與修飾皆應仍屬本發明涵蓋之專利範圍内。 【圖式簡單說明】 6 201014809 圖一係本發明第一實施例之流程圖。 圖二係本發明第二實施例之流程圖。 【主要元件符號說明】 (12)破碎 (14)(28)篩分 (16)濃縮槽 (18)廢水處理 (20)乾燥 (22)水泥 10 (11)焚化底潰 (13)磁選 (15)水洗 (17)泥、水分離 (19)底渣水洗污泥 (21)配方比例 (22’）固化劑 (23) 硫酸舞(石膏）或磷酸转或矽酸齊或含鈣之塩類 (24) 攪拌 （25)混練 (26) 射出或造粒或壓鑄成型 （26’）造粒射出 (27) 骨材成品 （27，）成品 15201014809 VI. Description of the invention: [Technical field to which the invention belongs], the daily inspection of the cold-cleaning process of the incineration silk washing sludge, the reprocessing of the washing process of the washing process 5 T can be used as a non-reinforced concrete, road grade matching soil, base backfill and other purposes.贞 晃 / 晃 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 The invention is mainly based on the suppression of the phase of the birth and the addition of Wang Lang to lose money #, Qihe environmental protection needs ash, and the production of finished I bone products for industrial reuse on the premise of research and innovation The main purpose of the present invention is to provide an incineration bottom slag washing process. 5 The sludge produced by the incineration bottom slag washing process is treated by the concentrating tank to form a new water washing sludge, which is then dried and then cured with a curing agent or iii. Use the sulfur _ (gypsum) or Wei Shishi acid _ containing sensitive i ΐΖ ϊ ϊ ί ί into a suitable mixture of moisture content, and then through the injection or granulation 鼍 2 demand as unreinforced concrete, road grade, poor quality The use of concrete, base backfilling, etc. has industrial use value. The second, the purpose is to provide a cold junction machine for the production of sludge, and the present invention does not require a temperature treatment process for sintering. Further having the advantages of carbon and sufficient The 25 sludge produced by the incineration bottom slag washing process is relatively in line with the principle of environmental protection. / [Summary of the Invention] The cold-knotting process of the incineration bottom slag washing sludge can be used to wash the incineration bottom slag. The sludge is treated by the concentration tank and the bottom slag water-washed sludge formed after the separation of the mud and water, and then dried with a curing agent or cement or a sulfuric acid (gypsum) or phosphorus 3 201014809 ====: 2= The ratio of mixed value of ί rate, .Tailu ΐΐΐ base _, etc., and the use of carbon in the industry, the high-reduction of the gift, the principle of energy saving and reduction, and the use of bottom slag Washing the sludge, and relatively speaking, it is more in line with the environmental protection. The following is a detailed description of the following. [Embodiment] 10 15 As shown in the first embodiment of the present invention, the present invention is an incineration bottom slag water, sludge. The cold-knotting process is the reprocessing of the sludge produced by the washing process (15) after the incineration bottom slag (11) is processed by crushing (12), magnetic separation 〇^) and sieving (14). The program includes the following processes: Concentration tank (16) 'Wash the aforementioned water (15) The muddy water produced by the treatment process is introduced into the concentration tank (16) to precipitate the sludge downwards; the mud and water are separated (Π), and the precipitated concentrated sludge is sent to a filter press or a centrifuge to sludge and waste water. Separation forms the bottom slag washed sludge (19), and the separated wastewater can be further subjected to wastewater treatment (18) to be more environmentally friendly; dry (20), separating the mud and water (17) Bottom slag washing sludge 〇9) Drying by natural drying or drying equipment, and drying the bottom slag washing sludge (19) water content is 10~30%; formula ratio (21), 70% ~95% of bottom slag washed sludge (19), 5%~30% of cement (22) or further increased by 1%~20% solid (eg powder) calcium sulphate (gypsum) or calcium phosphate or strontium Calcium or calcium-containing bismuth (23); 25 agitated (24), the above-mentioned bottom slag washed sludge (19), cement (22) or further selected sulfuric acid dance (gypsum) or phosphate or yoghurt feed or Calcium bismuth (23) - put into a mixer for stirring; kneading (25), the aforementioned bottom slag washing sludge (19), cement (22) or further selected sulfuric acid Calcium (gypsum) or calcium phosphate or calcium citrate or calcium-containing bismuth (23) - after agitation 4 201014809 and then through the practice of the practice machine to significantly reduce the bubbles into a mixture of ratios of uniform density, the ratio of water containing The ratio is about 5% to 25%; injection or granulation or die-casting (26), and the mixture having a water content of 15% to 25% after the treatment by the kneading (25) process is injection-molded by an injection molding machine into a desired ratio. The shaped aggregate product (27), or the mixture obtained by the above-mentioned kneading (25) process, having a water content of 5% to 15%, is processed by a granulation device or a compression device to obtain a plurality of granules or The finished bone product (27); in addition, the finished product (27) formed by injection molding machine in the above-mentioned injection or granulation or die-casting (26) process may be in the form of strips or other shapes, and The strip-shaped finished product (27) can be further cut into a block of a desired length by a cutting device; the finished product (27) obtained by the foregoing process can be provided as unreinforced concrete according to market demand. Road grade, inferior concrete, The backfilling purposes, has the industrial utility value, and by eliminating the need of a sintering molding the relative energy of the environment and comply with the concept of advantages. 15 蠹 (Please refer to the second embodiment of the present invention with reference to Figure 2, the cold slag of the slag washing sludge of the present invention, the smoldering sputum (1)) is crushed (12), and then washed by water washing equipment (15) ) = the reprocessing process of the sludge produced by the company: the following processes are included: Concentration ===^(15) The principle of introducing muddy water into the concentration tank by the treatment process; ,] further wastewater treatment (18) to further In accordance with the environmentally-friendly dry water separation (10) process, the bottom of the water washing sludge (10) slag washing sludge (10) dry treatment, the bottom of the surface after the treatment of 30% ~ 10% of the choice of 70% ~ _ bottom slag washed sludge (19 ), 25 201014809 Stirring «4) 'The above-mentioned bottom slag washed sludge (19) and the curing agent (22,) are placed in a scrambler and stirred to obtain a mixture of water having a moisture content of 10% to 2% by weight; granulation Injection molding (26) 'The above-mentioned ratio of the moisture content of 1% by weight after the treatment by the mixing process (24) is mixed by the granulation equipment to obtain a plurality of granular finished products 5 \ί\) 9 The plurality of granular finished products (27) obtained by the particle injection molding (26) process can be further sieved (28), and the process is The granulated product of the required size is screened by the screening device; the finished product (27) obtained by the foregoing process can be provided as a helmet, a road grade, a poor quality concrete, a base backfill, etc. according to market demand. It has industrial use value and is relatively energy-saving and conforms to the concept of environmental protection because it does not need to be formed by sintering. In summary, the present invention can be summarized as follows: 1. The present invention can form the bottom slag after the sludge water produced by the incineration bottom slag washing process is treated by the concentration tank (16) and 15 mud and water separation (17). The washed sludge (19) is first dried (20) and then treated with curing agent (22,) or cement (22) or further selected calcium sulfate (gypsum) or acid-filled #5 or tannic acid or danced (23) After the agitation (24) treatment, a mixture of the proportions of the appropriate moisture content is formed, and then the finished product (27) of the desired shape is produced through the process of injection or granulation or die casting (26), thereby coping with the market. The demand is provided as an industrial use value as a non-reinforced concrete, road graded, inferior concrete, base backfilling and the like. 2, the high-temperature treatment process of sintering is not required, which has the advantages of energy saving and carbon reduction, and can fully utilize the bottom slag to wash the sludge, and is relatively in line with the principle of environmental protection. Therefore, 'the invention is indeed of its industrial use value, and it is the application for the invention patent 25, please ask the review board of the bureau to examine and grant the patent, to the sense of virtue. However, the above-mentioned embodiments are only the preferred embodiments of the present invention, and the equivalent variations and modifications made by the scope of the present invention should still be the patents covered by the present invention. Within the scope. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a flow chart of a first embodiment of the present invention. Figure 2 is a flow chart of a second embodiment of the present invention. [Description of main component symbols] (12) Crushing (14) (28) Screening (16) Concentration tank (18) Wastewater treatment (20) Drying (22) Cement 10 (11) Incineration bottom collapse (13) Magnetic separation (15) Washing (17) Mud, water separation (19) Bottom slag Washing sludge (21) Formulation ratio (22') Curing agent (23) Sulfuric acid dance (gypsum) or phosphoric acid or bismuth or calcium-containing bismuth (24) Stirring (25) Mixing (26) Injection or granulation or die casting (26') granulation shot (27) Finished product (27,) Finished product 15

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Claims (1)

201014809 七、申請專利範圍： 1· 一種焚化底渣水洗污泥之冷結流程，係將焚化底渣經破碎、磁 選及篩分處理後經由水洗設備之水洗處理流程所產生的污泥之 再加工處理程序，係包括有下列流程： 5 濃縮槽，將前述水洗處理流程產生的污泥導入濃縮槽，令污泥 往下沈澱； 泥、水分離’將前述沈澱濃縮之污泥送入濾壓機或離心機將污 泥與廢水分離即形成底渣水洗污泥； 10 15 to 乾燥’將前述泥、水分離流程所得之底渣水洗污泥以自然乾燥 或藉由乾燥設備進行乾燥處理； 配方比例，選用70%〜95%之底渣水洗污泥與5%〜30%的水泥； 攪拌，將前述底渣水洗污泥與水泥放入攪拌機進行攪拌； 混練’前巧底渣水洗污泥與水泥授拌之後再經由練土機之混練 以大幅減少氣泡而成為具有均勻密度之比例混合物； 射出成型，將前述經由混練流程處理後之比例混合物藉由射出 成型機射出成型為所需形狀之骨材成品者。 2.如申請專職圍第丨項所述之焚化紐水洗污泥之冷結流程， 其中該乾燥流程處理後之底渣水洗污泥的含水率為〗〇%〜3〇% 者。 3.^申請賴麵第1顿狀焚化総水妨狀冷結流程， 其中該混練流程所得之比例混合物的含水率$ 15%〜25%者。 ，第1項所述之焚化絲水洗污泥之冷結流程， 成？流程中藉由射出成型機所射出之骨材成品係可 進一步經由切斷設備裁切成所需之長度者。 5. t 1項所述之焚化底渣水洗污泥之冷結流程， 务麵水 入碰拖决剛貧）或碟酸舞或梦酸触含舞之賴 程’然後再將前述攪拌後之底渣水洗 / /b 7 、满辦;5膏)或磷峡切峡或含狀細藉 8 25 201014809 由練土機之混練以大幅減少氣泡而成為具有均勻密度之比例混 合物，該比例混合物之含水率為15%〜25%者。 6·如申請專利範圍第1項所述之焚化底渣水洗污泥之冷結流程， 其中該泥水分離流程所分離後的廢水可進一步進行廢水處理 5 者。 7· —種焚化底渣水洗污泥之冷結流程，係將焚化底渣經破碎、磁 選及篩分處理後經由水洗設備之水洗處理流程所產生的污泥之 再加工處理程序，係包括有下列流程： 漠縮槽，將前述水洗處理流程產生的污泥導入濃縮槽，令污泥 •10 往下沈澱； 泥、水分離’將前述沈澱濃縮之污泥送入濾壓機或離心機將污 泥與廢水分離即形成底渣水洗污泥； 乾燥’將前述泥、水分離流程所得之底邊水洗污泥以自然乾燥 或藉由乾燥設備進行乾燥處理； 15 配方比例，選用70%〜95%之底渣水洗污泥與5%〜30%的水泥； 攪拌’將前述底渣水洗污泥與水泥放入攪拌機進行授拌； 混練’前述底渣水洗污泥與水泥攪拌之後再經由練土機之混練 以大幅減少氣泡而成為具有均勻密度之比例混合物； φ 造粒或壓铸成型，將前述經由混練流程處理後之比例混合物藉 ° 由造粒設備或壓鑄設備之加工而成型為粒狀或所需形狀之骨 材成品者。 8·如申請專利範圍第7項所述之焚化底渣水洗污泥之冷結流程， 其中該乾燥流程處理後之底渣水洗污泥的含水率為1 〇%〜3〇% 者。 25 9·如申請專利範圍第7項所述之焚化底渣水洗污泥之冷結流程， 其中該現練流程所得之比例混合物的含水率為5%〜15%者。 10.如申請專利範圍第7項所述之焚化底渣水洗污泥之冷結流程， 其中該配方比例係選用70%〜95%之底渣水洗污泥、5%〜3〇%的水 泥與伐〜20%的硫酸與(石膏）或磷酸每或矽酸句或含舞之塩類 9 201014809 再放入攪拌機進行攪拌流程，然後再將前述攪拌後之底渣水洗 污泥、水泥與硫酸鈣(石膏）或磷酸鈣或矽酸鈣或含鈣之塩類藉 由練土機之混練以大幅減少氣泡而成為具有均勻密度之比例混 合物’該比例混合物之含水率為15%〜25%者。 5 10 15 % 11. 如申請專利範圍第7項所述之焚化底渣水洗污泥之冷結流程， 其中該泥水分離流程所分離後的廢水可進一步進行廢水處理 者。 12. — ^化底渣水洗污泥之冷結流程’係將焚化底渣經破碎、磁 選及篩分處理後經由水洗設備之水洗處理流程所產生的污泥之 再加工處理程序，係包括有下列流程： 濃縮槽，將前述水洗處理流程產生的污泥導入濃縮槽，令污泥 往下沈澱； 泥、、水分離，將前述沈澱濃縮之污泥送入濾壓機或離心機將污 / 尼與廢水分離即形成底潰水洗污泥； 乾燥，將前述泥、水分離流程所得之底渣水洗污泥以自然乾燥 或藉由乾燥設備進行乾燥處理； 配方比例，選用70%〜90%之底潰水洗污泥與腦〜灌的固化劑； 攪拌，將則述底渣水洗污泥與固化劑放入擾拌機進行攪拌； 造粒射出，將前述經由攪拌流程處理後之比例混合物藉由造粒 設備成型為所需形狀之成品者。 13·如申凊專利範圍第12項所述之焚化底渣水洗污泥之冷結流 程，其中該乾燥流程處理後之底渣水洗污泥的含率〇%〜 25% 者。 1也如ΐ 利跑圍第12項所述之焚化底渣水洗污泥之冷結流 程’其鱗流程所得之比例混合物的含水率為⑽〜雇者。 15.，申^^專利範_第12項所述之焚化総水洗S泥之冷結流 ί Ζ中該ί粒射出流財藉由造㈣1備所得之粒狀成品係可 :Ζ經由篩分處理流轉由_纽備篩選出所需規格大小之 粒狀成品者。 10 25 201014809 16. 如申請專利範圍第12項所述之焚化底潰水洗污泥之冷結流 程，其中該泥、水分離流程處理所得之底渣水洗污泥的含水率 為20%〜55%者。 17. 如申請專利範圍第12項所述之焚化底渣水洗污泥之冷結流 5 程，其中該泥水分離流程所分離後的廢水可進一步進行廢水處 理者。201014809 VII. Patent application scope: 1. A cold-knot process of incineration bottom slag washing sludge, which is the reprocessing of sludge produced by the washing process of the washing plant after crushing, magnetic separation and sieving treatment. The processing procedure includes the following processes: 5 concentrating tank, introducing the sludge generated by the aforementioned washing process into the concentrating tank to precipitate the sludge downward; separating the mud and water, and sending the sludge concentrated by the sediment to the filter press Or the centrifuge separates the sludge from the waste water to form the bottom slag washing sludge; 10 15 to dry 'The bottom slag washed sludge obtained by the mud and water separation process is dried naturally or dried by drying equipment; 70%~95% of the bottom slag is used to wash the sludge and 5%~30% of the cement; stirring, the bottom slag washing sludge and cement are put into the mixer for stirring; mixing the 'pre-skilled slag washing sludge and cement After the mixing, the kneading machine is used to greatly reduce the bubbles to become a mixture having a uniform density; the injection molding, the proportion after the above-mentioned processing through the kneading process Composition by injection molding machine by injection molding the finished aggregates of a desired shape. 2. For the cold-knot process of incinerating new-washed sludge as described in the full-time sub-paragraph, the water content of the bottom slag washed sludge after the drying process is 〇%~3〇%. 3.^ Apply for the first-stage incineration of the water-like cold-knot process, in which the ratio of the water content of the mixture obtained by the mixing process is $15%~25%. The cold-knotting process of the incineration silk washing sludge mentioned in the first item, into? The finished product of the aggregate produced by the injection molding machine in the process can be further cut to a desired length by a cutting device. 5. The cold-knotting process of the incinerated bottom slag washing sludge mentioned in item t1, the water in the face is dragged to the limit of poverty, or the sour dance or the dream acid touches the dance process, and then the agitated Bottom slag washing / / b 7 , full; 5 cream ) or Phosphorus gorge or containing fine 8 25 201014809 by the practice of the mixer to greatly reduce the bubble and become a mixture of ratios of uniform density, the ratio of the mixture The water content is 15% to 25%. 6. The cold-knotting process of the incinerated bottom slag washing sludge according to the first aspect of the patent application, wherein the wastewater separated by the mud-water separation process can be further subjected to wastewater treatment. 7. The cold-knotting process of incineration bottom slag washing sludge is a reprocessing process of sludge generated by the washing process of the washing plant after crushing, magnetic separation and sieving treatment, including The following process: the shrinking tank, the sludge produced by the aforementioned washing process is introduced into the concentration tank, so that the sludge 10 is deposited downward; the mud and water are separated. The sludge deposited by the precipitation is sent to a filter press or a centrifuge. Separation of sludge and wastewater to form bottom slag washing sludge; drying 'The bottom side washed sludge obtained by the above mud and water separation process is dried naturally or dried by drying equipment; 15 formula ratio, 70%~95 % bottom slag washed sludge and 5%~30% cement; stirring 'the bottom slag washed sludge and cement into the mixer for mixing; mixing 'the bottom slag washed sludge and cement after mixing and then through the soil Mixing of the machine to reduce the bubbles to a mixture of uniform density; φ granulation or die-casting, the above-mentioned ratio mixture treated by the kneading process is borrowed from the granulation equipment or Casting equipment processing granular or molded into the desired shape of the finished material by a bone. 8. The cold-knotting process of the incinerated bottom slag washing sludge according to item 7 of the patent application, wherein the water content of the bottom slag washing sludge after the drying process is 1% to 3%. 25 9. The cold-knotting process of the incinerated bottom slag washing sludge according to item 7 of the patent application, wherein the ratio of the water content of the mixture obtained by the actual process is 5% to 15%. 10. The cold-knot process of incinerated bottom slag washing sludge according to item 7 of the patent application scope, wherein the proportion of the formula is 70%~95% of bottom slag washing sludge, 5%~3%% of cement and Cut ~20% sulfuric acid with (gypsum) or phosphoric acid per hydrazine or dance with 9 9 201014809 and then put it into the mixer for the mixing process, then wash the sludge, cement and calcium sulphate Gypsum) or calcium phosphate or calcium citrate or calcium-containing mashes are blended by a drill machine to substantially reduce bubbles to become a mixture having a uniform density. The moisture content of the mixture is 15% to 25%. 5 10 15 % 11. For the cold-knot process of incineration bottom slag washing sludge as described in claim 7, wherein the wastewater separated by the mud-water separation process can be further subjected to wastewater treatment. 12. — The cold-knot process of the bottom slag washing sludge is a process for reprocessing the sludge produced by the washing process of the washing equipment after crushing, magnetic separation and sieving treatment, including The following process: The concentration tank, the sludge produced by the aforementioned washing process is introduced into the concentration tank to precipitate the sludge downward; the mud and water are separated, and the sludge concentrated by the precipitation is sent to a filter press or a centrifuge to remove the sewage/ Nitrogen is separated from the wastewater to form a bottom-washed sludge; dried, and the bottom slag washed sludge obtained by the mud and water separation process is dried naturally or dried by a drying device; the proportion of the formula is 70% to 90%. Bottom-washed sludge and brain-filling curing agent; stirring, the bottom slag washing sludge and curing agent are placed in a scrambler for stirring; granulation injection, the proportion mixture after the aforementioned treatment through the stirring process is used The granulation equipment is formed into a finished product of the desired shape. 13. The cold-knotting process of the incinerated bottom slag washing sludge according to item 12 of the claim patent scope, wherein the content of the bottom slag washing sludge after the drying process is 〇% to 25%. 1 Also, as for the cold-knot process of the incinerated bottom slag washing sludge described in Item 12, the moisture content of the mixture obtained by the scale process is (10) ~ employed. 15. The cold-knot of the incineration, washing and sluicing of the invented ^ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ The processing flow is filtered by _ New Zealand to filter out the granular finished products of the required size. 10 25 201014809 16. The cold-knot process of incineration bottom-washing sludge according to item 12 of the patent application scope, wherein the moisture content of the bottom slag washing sludge obtained by the sludge and water separation process is 20% to 55% By. 17. The cold condensate of the incinerated bottom slag washed sludge as described in claim 12, wherein the wastewater separated by the sludge separation process can be further subjected to wastewater treatment.