TW201838936A - Method of converting sewage sludge to improved soil material converting the sewage sludge containing heavy metals which reduces contamination - Google Patents

Method of converting sewage sludge to improved soil material converting the sewage sludge containing heavy metals which reduces contamination Download PDF

Info

Publication number
TW201838936A
TW201838936A TW106112798A TW106112798A TW201838936A TW 201838936 A TW201838936 A TW 201838936A TW 106112798 A TW106112798 A TW 106112798A TW 106112798 A TW106112798 A TW 106112798A TW 201838936 A TW201838936 A TW 201838936A
Authority
TW
Taiwan
Prior art keywords
sewage sludge
sludge
heavy metals
sewage
converting
Prior art date
Application number
TW106112798A
Other languages
Chinese (zh)
Other versions
TWI648227B (en
Inventor
章日行
張喬揚
Original Assignee
朝陽科技大學
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 朝陽科技大學 filed Critical 朝陽科技大學
Priority to TW106112798A priority Critical patent/TWI648227B/en
Publication of TW201838936A publication Critical patent/TW201838936A/en
Application granted granted Critical
Publication of TWI648227B publication Critical patent/TWI648227B/en

Links

Classifications

    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Landscapes

  • Treatment Of Sludge (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

Disclosed is a method of converting sewage sludge to improved soil material, which includes sequential steps: preparation, mixing, high temperature fermentation, turning and decomposition, and finish. The disclosed method is to remove impurities from the sewage sludge, remove heavy metals by means of using an electric power reaction tank, then mix the sewage sludge up with an organic additive in order to form a first mixture. The first mixture is fermented at high temperature and turns into a second mixture; then the second mixture is turned and decomposed, and finally converts into an improved soil material. Accordingly, the disclosed has advantages of being able to completely convert the sewage sludge containing heavy metals which reduces contamination, and being environmental-friendly to mix plural wastes for reuse and recycle purpose.

Description

下水污泥轉製土壤改良材料之方法Method for converting sewage sludge into soil improvement material

本發明係有關一種下水污泥轉製土壤改良材料之方法,尤指一種兼具充分轉用含重金屬之下水污泥可減少污染,與混合數種廢棄物回收再利用相當環保之下水污泥轉製土壤改良材料之方法。The invention relates to a method for converting sewage sludge into soil improvement materials, in particular to a method for fully converting heavy sewage containing sewage sludge to reduce pollution, and mixing with several kinds of wastes to recycle and reuse recycled sewage sludge to convert soil Methods of improving materials.

一般情況下,下水污泥被視為污水處理場常見的污染來源,除了產生不良氣味,還含有重金屬及致病性微生物等物質,除此之外,下水污泥中含有大量植物生長所需的有機物質及豐富的營養素(如氮、磷、鉀等)。 另外,在不影響工程品質的要求之下,經處理後的下水污泥,也可作替代原料使用,如水泥摻料、瀝青混合料,及透水磁磚等建材之應用。 下水污泥就是下水道系統中之沉積物,其中當然包含許多經化糞池處理後之排出物。由於下水污泥中含有高營養物質(對農作物而言)和有機物,可作為農業之土壤改良劑、建築材料等,具有相當的經濟效益。 但是,污水處理場所產生之下水污泥,除了含有上述經濟價值成分外,尚含有重金屬與其他有毒性物質。若無法將下水污泥中這些危害物質移除,不僅無法用於農業堆肥,且需以有害廢棄物方式處理,後續處理成本亦大幅提升。若不慎排放至環境中,即導致土壤或地下水污染,影響層面極廣,後果不堪設想。 重金屬在今日工業中使用很普遍,一旦造成污染可能經年累月也無法予以改善。重金屬不像有機物會經微生物分解而消滅,使本來之毒害作用完全消失。重金屬污染環境可利用物理、化學及生物方式去除,而選擇處理方法的考慮因素有:處理成本、污染物特性、技術可行性及下水污泥特性等。處理的程度也因後續使用需求不同而有所差異。近年來已有許多研究探討去除含重金屬下水污泥之技術應用,而且也證實其可行性。 電動力技術應用於處理環境污染上,主要為修復受污染之土壤、污泥、固體廢棄物等,亦可應用於處理飽和、非飽和之污染土壤、污泥及地下水,且對於低滲透性之待處理樣品有更好之整治成效(如文獻Guedes et al., 2014)。此技術係在受污染的區域兩端插入正負電極施加直流電後,在施加電場作用下,多數帶正電荷的重金屬陽離子會朝陰極移動,而下水污泥中之陰離子則朝陽極方向移動,藉由正負電極之間電場產生電化學原理之電滲透流及離子遷移等作用機制,引導下水污泥中之電解質溶液流動,將污染物去除或濃縮至有限的範圍,以方便後續之處理,而達到去除污染物的目的(如文献Choi and Luib, 1995)。 又,有關電動力技術之原理與反應機制,由於下水污泥表面帶負電荷,且為一多孔性介質,當加入電場時,電解液流體與下水污泥間之相對運動隨之產生,此皆屬電動力學的範圍,利用電動力法處理下水污泥過程中會發生各種電化學反應,其電動力技術之原理及反應機制包括:電雙層、電解作用、電滲透流、離子遷移,由於此電動力技術與反應機制均為習知技術,恕不贅述。 此外,現有許多家禽糞材(例如雞糞、鴨糞、鵝糞)、種植香菇後之廢棄太空包、廢棄木屑…等有機廢棄物很難處理,若直接丟棄也十分浪費。 因此,有必要開發新技術,以解決前述下水污泥與有機廢棄物之處理問題。In general, sewage sludge is regarded as a common source of pollution in sewage treatment plants. In addition to producing bad odors, it also contains heavy metals and pathogenic microorganisms. In addition, sewage sludge contains a large amount of plant growth. Organic substances and rich nutrients (such as nitrogen, phosphorus, potassium, etc.). In addition, without affecting the quality of the project, the treated sewage sludge can also be used as a substitute for raw materials, such as cement admixtures, asphalt mixtures, and construction materials such as permeable tiles. Sewer sludge is the sediment in the sewer system, which of course contains many effluents that have been treated by the septic tank. Since the sewage sludge contains high nutrients (for crops) and organic matter, it can be used as an agricultural soil improver, building material, etc., and has considerable economic benefits. However, the sewage sludge produced in sewage treatment sites contains heavy metals and other toxic substances in addition to the above-mentioned components of economic value. If these hazardous substances in sewage sludge cannot be removed, not only can they not be used for agricultural composting, but also need to be treated in the form of hazardous waste, and the cost of subsequent treatment will also increase significantly. If it is accidentally discharged into the environment, it will lead to soil or groundwater pollution, the impact level is extremely wide, and the consequences are unimaginable. Heavy metals are commonly used in industry today, and once they cause pollution, they may not improve over time. Unlike organic matter, heavy metals are destroyed by microorganisms and destroyed, so that the original toxic effects disappear completely. Heavy metal pollution environment can be removed by physical, chemical and biological methods, and the considerations for the selection of treatment methods are: treatment cost, pollutant characteristics, technical feasibility and sewage sludge characteristics. The degree of processing also varies depending on the subsequent use requirements. In recent years, there have been many studies to explore the application of technology to remove sewage sludge containing heavy metals, and it has also proved its feasibility. Electric power technology is used to treat environmental pollution, mainly to repair contaminated soil, sewage, solid waste, etc. It can also be applied to saturated, unsaturated, and contaminated soil, sewage, and groundwater, and for low permeability The samples to be processed have a good remediation effect (eg Guedes et al., 2014). This technique is to insert positive and negative electrodes at both ends of the contaminated area and apply direct current. Under the action of the applied electric field, the more positively charged heavy yang will move toward the cathode, and the yin in the sewage sludge will move toward the anode. The electric field between the positive and negative electrodes generates the electroosmotic flow and ion migration mechanism of the electrochemical principle to guide the flow of the electrolyte solution in the sewage sludge to remove or concentrate the pollutants to a limited range to facilitate subsequent treatment and achieve the removal The purpose of the pollutant (eg Choi and Luib, 1995). In addition, the principle and reaction mechanism of electrodynamic technology, because the surface of the sewage sludge is negatively charged and is a porous medium, when an electric field is added, the relative movement between the electrolyte fluid and the sewage sludge is generated. All belong to the scope of electrodynamics, and various electrochemical reactions will occur during the treatment of sewage sludge by the electrodynamic method. The principles and reaction mechanisms of the electrodynamic technology include: electric double layer, electrolysis, electroosmotic flow, and ion migration. This electric power technology and reaction mechanism are conventional technologies and will not be repeated here. In addition, many existing poultry manure materials (such as chicken manure, duck manure, goose manure), waste space bags after shiitake mushroom cultivation, waste wood chips, etc. are difficult to dispose of, and it is also wasteful if directly discarded. Therefore, it is necessary to develop new technologies to solve the aforementioned disposal problems of sewage sludge and organic waste.

本發明之目的,在於提供一種下水污泥轉製土壤改良材料之方法,其兼具充分轉用含重金屬之下水污泥可減少污染,與混合數種廢棄物回收再利用相當環保等優點。特別是,本發明所欲解決之問題係在於傳統下水污泥及有機廢棄物無法被有效再利用等問題。 解決上述問題之技術手段係提供一種下水污泥轉製土壤改良材料之方法,其包括下列步驟: 一.準備步驟; 二.混合步驟; 三.高溫發酵步驟; 四.翻堆腐熟步驟;與 五.完成步驟。 本發明之上述目的與優點,不難從下述所選用實施例之詳細說明與附圖中,獲得深入瞭解。 茲以下列實施例並配合圖式詳細說明本發明於後:The purpose of the present invention is to provide a method for converting sewage sludge into soil improvement materials, which has the advantages of sufficiently converting sewage sludge containing heavy metals to reduce pollution, and is quite environmentally friendly with the recycling of several kinds of waste. In particular, the problem to be solved by the present invention is that the traditional sewage sludge and organic waste cannot be effectively reused. The technical means to solve the above problem is to provide a method for converting sewage sludge into soil improvement materials, which includes the following steps: 1. Preparation steps; 2. Mixing step; three. High temperature fermentation steps; 4. Steps of turning the pile into rot; and V. Complete the steps. The above objects and advantages of the present invention are not difficult to gain an in-depth understanding from the following detailed description and drawings of selected embodiments. The following examples and drawings are used to explain the present invention in detail:

參閱第1及第2圖,本發明係為一下水污泥轉製土壤改良材料之方法,於開始後包括下列步驟: 一.準備步驟S1:將來自下水系統之污水處理場91之下水污泥取出,此被定義為一第一下水污泥81,將該第一下水污泥81除去雜質後,成為一第二下水污泥82;接著將該第二下水污泥82中之重金屬去除,而形成一第三下水污泥83。 二.混合步驟S2:將去除重金屬後之該第三下水污泥83與一有機添加物71混合,而形成一第一混合物61。 三.高溫發酵步驟S3:將該第一混合物61置入一高溫發酵裝置92中,進行高溫發酵後形成一第二混合物62,該高溫發酵裝置92之發酵溫度係介於攝氏100至160度之間,且發酵時間係介於1至24小時之間。 四.翻堆腐熟步驟S4:將該第二混合物63進行翻堆腐熟之程序至少3天。 五.完成步驟S5:最後轉製成一土壤改良材料63。 實務上,關於該準備步驟S1,進一步可再細分為: [a]下水污泥前處理步驟S11:於室溫下,將該第一下水污泥81鋪平風乾至少24小時,並除去雜質後,研磨破碎再過篩網,而成為該第二下水污泥82。 [b] 去除重金屬步驟S12:參閱第3圖,設一電動力反應槽93(例如中華民國發明專利第I249441號之『電動力整治重金屬污染土壤之系統與方法』所述),將該第二下水污泥82置於其內;該電動力反應槽93內係設一對電極板93A,並供入一電解液93B(如第4圖所示),則該第二下水污泥82與該電解液93B混合。另於分佈重金屬區域A(參閱第4圖,不規則團狀僅為示意)之兩端,分別接設一直流正極端部931與一直流負極端部932,其間具有一介於0至100V之預定電壓(或0至200mA之預定電流)。當進行電動力反應時,多數帶正電荷的重金屬陽離子會朝該直流負極端部932移動,而污泥中之陰離子則朝該直流正極端部931移動,藉由正負電極之間電場產生電化學原理之電滲透流及離子遷移等作用機制,引導該第二下水污泥82中之電解質溶液流動,最後可於該直流負極端部932得到較集中之重金屬B(如第4圖所示,團狀僅為示意,並可能包括其他污染物),而達到去除污染物(將該第二下水污泥82所包含之重金屬移除)的目的。 該重金屬係包含鎘、鎳、銅、鉛、鉻、鋅其中至少一者。 該有機添加物71係選自種植香菇後之廢棄太空包、廢棄家禽糞材、廢棄木屑其中至少一項。 本技術以含重金屬之下水污泥為整治試驗之主要標的污染物,利用電動力技術將下水污泥之重金屬移除,並探討不同操作條件之影響,冀使對污泥中之重金屬達到移除之成效,並使用移除重金屬後之下水污泥,保留其高營養物及有機物,結合高溫發酵技術,將其轉製成土壤改良材。 茲舉例說明如下: 本試驗使用之樣品採自某水資源回收中心所產生之污泥(亦即該第一下水污泥81)。採集回來之污泥樣品先進行前處理,將樣品鋪平並於室溫下風乾至少24小時,除去污泥中紙屑、礫石、雜草及毛髮等雜質後,以陶瓷材質之研磨器具進行破碎並通過ASTM 10號(2 mm)之標準篩網,以作為後續試驗使用。並依標準方法對污泥進行基本性質分析,分析項目包括:污泥pH值、污泥導電度、含水率、有機質含量及重金屬之全量分析。各項污泥基本性質分析方法依據及結果列於下表一。本研究污泥樣品之pH值為6.11,含水量為78%,污泥有機質含量為47%,重金屬鎘濃度為5.60mg/kg、鉻濃度為317mg/kg、鎳濃度為830mg/kg、銅濃度為533mg/kg、鉛濃度為147mg/kg、鋅濃度為2501mg/kg。             (表一) 關於試驗所使用之相關儀器設備如下表二所示: (表二) 其中,酸鹼度計與導電度計分別用來測量污泥樣品、電解液之pH值及導電度。火焰式原子吸收光譜儀為重金屬濃度的分析量測;多段變速振盪器為污泥振盪萃取之使用。離心機為污泥振盪萃取後,以離心方式將污泥固液體分離,以便後續分析使用。抽氣幫浦則用於污泥重金屬之萃取,將污泥顆粒完全過濾乾淨,以便後續樣品上機分析使用。直流電源供應器提供本試驗之電動力處理系統操作所需之直流電源;電子天平則提供試驗藥品及污泥樣品之秤量所使用;去離子水製造機則作為配製試驗藥品、樣品分析及實驗儀器設備清洗使用。電磁攪拌器主要用於配製系統中之電解液,使試驗藥品與試劑水均勻混合;超音波洗淨器用來洗滌實驗玻璃器皿及不易清洗之實驗器具;烘箱則為污泥樣品中含水率分析使用。   本研究所使用之試驗藥品如下表三所示:          (表三) 碳酸鈉配製成0.01 M濃度,做為電動力系統中之電解液所用,製造商為Sigma-Alorich,純度為99.8%;硝酸及鹽酸製造商皆為Merck公司出品,純度分別為65%、37%,主要用於重金屬檢測方法-王水消化法(NIEA S321.63B, 2003)之王水配製。 關於電動力技術去除下水污泥中重金屬試驗,本研究電動力處理系統皆以0.01 M碳酸鈉電解液條件下進行試驗,以石墨電極板(Graphite)、二氧化銥極板(Dimensionally Stable Anode,簡稱DSA)、不鏽鋼極板(Stainless Steel)作為電極,以不同電壓梯度之操作因子:1.0V/cm、1.5V/cm及2V/cm、2.5V/cm。 關於電動力技術設備與材料,本試驗設計之電動力處理系統(如第3圖所示)係設置電動力處理系統槽體(即該電動力反應槽93)以聚氯乙烯(PVC)製作,規格為長26cm×寬11cm×高11cm(內徑),槽體中以PVC隔板將樣品儲槽分隔,規格為長15cm×寬11cm×高6cm(內徑)。處理系統由直流電源供應器供應直流電,在極板與污泥樣品之間以紗布包覆多孔PVC板做為間隔,填入待處理之污泥樣品及操作之電解液後,最後通以定電壓之直流電進行操作。 關於電動力技術試驗流程(如第2圖所示),先進行污泥的前處理及基本物理化學特性分析,包括污泥的pH值、含水率、有機質含量及重金屬濃度之全量分析,將污泥樣品放置於模場之樣品儲槽中(約450 g污泥),並將0.01 M 碳酸鈉電解液注入電解液儲存槽周圍,配合不同操作電極板(石墨電極板、二氧化銥極板與不鏽鋼極板)進行試驗,目的是為了找出較理想的極板種類作為系統之操作參數。選定其操作效果較佳之極板後,再以不同電壓梯度之操作參數進行試驗。 試驗期間每日記錄系統電壓、電流之變化並測量電解液的pH值、導電度,每日亦需注入適量的電解液。此外,每日採取污泥樣品一次(約3 g),採集點分別為靠近陽極端(即該直流正極端部931)、儲槽中央及靠近陰極端(即該直流負極端部932)三處,採取污泥樣品經烘乾後,得以進行污泥之重金屬含量分析。經由找出電動力技術處理系統之適當參數的程序,對系統中所發生的電化學反應傳輸機制進行更深入之探討。 移除污泥重金屬並做為後需高溫發酵的原料,再搭配種植香茹用之廢棄太空包(或是廢棄家禽糞材、廢棄木屑),經過高溫發酵130o C的加熱,並加入耐高溫菌於2小時內即完成轉製,發展無毒、無害的土壤改良資材。 重點在於,本試驗為藉由不同種類之電極板與施加不同之電壓梯度等參數,探討電動力技術去除下水污泥中重金屬之試驗,依據各試驗結果與相關理論,尋求出適當之操作條件以達到有效之去除下水污泥中重金屬。得到較佳之結果如下: [a] 經由電動力技術處理之污泥中重金屬濃度,隨著距離陽極板越遠濃度越高,由此可知藉由正負電極之間電場產生電化學原理之電滲透流及離子遷移等作用機制,可有效地將重金屬污染物去除或濃縮至有限的範圍。 [b] 本研究以不同電極板為電動力技術之操作參數時,使用二氧化銥極板為電極板時有較佳之去除效率,其中重金屬鎳、鎘和鉻去除效率最為顯著,分別為72.22%、56.76%及38.59%。 [c] 本研究在不同電壓梯度下,進行5天之電動力試驗,鎘、鎳、銅和鉛於電壓梯度2.0V/cm時有較好之去除率,分別為100%、96.67%、17.89%及52.88%;鉻及鋅則於2.5V/cm時去除效果較顯著,去除率為80.07%和44.09%。 [d] 本試驗以0.01 M碳酸鈉為電解操作液,二氧化銥極板為陽極板,不鏽鋼為陰極板,進行電動力技術去除下水污泥中重金屬之試驗,鎘與鎳有較高之去除率,其中鎘於電壓梯度2.0V/cm操作下之去除率可達100%。 [e] 利用電動力技術處理下水污泥中重金屬,以不同操作電壓梯度(2.0V/cm及2.5V/cm)進行1天之試驗,若移除100mg/kg重金屬所需用電量之費用約為0.93-99.6元。 [f] 本產品協助霧峰國小進行校地綠化,成果獲得該校肯定。 本發明之優點及功效係如下所述: [1] 充分轉用含重金屬之下水污泥可減少污染。本發明利用電動力技術將下水污泥之重金屬移除,再經混合、高溫發酵、翻堆腐熟等步驟,轉變成土壤改良材料,可減少污染。故,充分轉用含重金屬之下水污泥可減少污染。 [2] 混合數種廢棄物回收再利用相當環保。本發明係將下水污泥之重金屬移除後,混入種植香菇後之廢棄太空包、廢棄家禽糞材、廢棄木屑其中至少一種的廢棄物(有機添加物)。再經高溫發酵及翻堆腐熟等步驟,即可予以回收再利用。故,混合數種廢棄物回收再利用相當環保。 以上僅是藉由較佳實施例詳細說明本發明,對於該實施例所做的任何簡單修改與變化,皆不脫離本發明之精神與範圍。Referring to Figures 1 and 2, the present invention is a method for converting water sludge into soil improvement materials, which includes the following steps after the start: 1. Preparation Step S1: Take out the sewage sludge from the sewage treatment plant 91 of the sewage system, which is defined as a first sewage sludge 81, and after removing impurities from the first sewage sludge 81, it becomes a second sewage Sludge 82; The heavy metals in the second sewage sludge 82 are then removed to form a third sewage sludge 83. two. Mixing step S2: The third sewage sludge 83 after removing heavy metals is mixed with an organic additive 71 to form a first mixture 61. three. High-temperature fermentation step S3: Put the first mixture 61 into a high-temperature fermentation device 92 to form a second mixture 62 after high-temperature fermentation. The fermentation temperature of the high-temperature fermentation device 92 is between 100 and 160 degrees Celsius. And the fermentation time is between 1 and 24 hours. four. Step S4: The second mixture 63 is subjected to a process of turning and maturing for at least 3 days. Fives. Step S5 is completed: finally converted into a soil improvement material 63. In practice, the preparation step S1 can be further subdivided into: [a] Pre-treatment of sewage sludge Step S11: At room temperature, flatten the first sewage sludge 81 for at least 24 hours and remove impurities After grinding and crushing, it passes through the screen to become the second sewage sludge 82. [b] Step S12 of removing heavy metals: refer to FIG. 3, and set up an electrodynamic reaction tank 93 (for example, as described in the "System and Method of Electrodynamic Power Remediation of Heavy Metal Contaminated Soil by the Republic of China Invention Patent No. I249441"). The sewage sludge 82 is placed therein; a pair of electrode plates 93A are provided in the electrodynamic reaction tank 93, and an electrolyte 93B (as shown in FIG. 4) is supplied, then the second sewage sludge 82 and the Electrolyte 93B is mixed. In addition, at both ends of the distributed heavy metal region A (see FIG. 4, the irregular clusters are only for illustration), a DC positive terminal 931 and a DC negative terminal 932 are respectively connected, with a predetermined interval between 0 and 100V Voltage (or predetermined current from 0 to 200mA). When carrying out electrokinetic reactions, many positively charged heavy positive ions will move towards the DC negative terminal 932, while the negative ions in the sludge will move toward the positive DC terminal 931, and the electrochemistry is generated by the electric field between the positive and negative electrodes The principle of electroosmotic flow and ion migration and other action mechanisms guide the flow of the electrolyte solution in the second sewage sludge 82, and finally the concentrated heavy metal B can be obtained at the DC negative electrode end 932 (as shown in Figure 4 The state is only for indication, and may include other pollutants), and the purpose of removing pollutants (removing heavy metals contained in the second sewage sludge 82) is achieved. The heavy metal system includes at least one of cadmium, nickel, copper, lead, chromium, and zinc. The organic additive 71 is at least one item selected from the group consisting of waste space bags after planting shiitake mushrooms, waste poultry dung, and waste wood chips. This technology uses water sludge under heavy metals as the main target pollutant in the remediation test. It uses electric power technology to remove heavy metals from sewage sludge, and discusses the impact of different operating conditions to achieve the removal of heavy metals in sludge. The results, and the use of sewage sludge after removing heavy metals to retain its high nutrients and organic matter, combined with high-temperature fermentation technology, convert it into soil improvement materials. Here are some examples: The samples used in this experiment were collected from the sludge produced by a water resource recovery center (that is, the first sewage sludge 81). The collected sludge sample is pre-treated, and the sample is flattened and air-dried at room temperature for at least 24 hours. After removing impurities such as paper dust, gravel, weeds and hair from the sludge, it is crushed with ceramic grinding equipment and Pass the standard screen of ASTM No. 10 (2 mm) for subsequent tests. The basic properties of sludge are analyzed according to standard methods. The analysis items include: sludge pH, sludge conductivity, water content, organic matter content, and full-scale analysis of heavy metals. The basis and results of various basic analysis methods of sludge are listed in Table 1 below. The pH value of the sludge sample in this study was 6.11, the moisture content was 78%, the sludge organic content was 47%, the heavy metal cadmium concentration was 5.60 mg/kg, the chromium concentration was 317 mg/kg, the nickel concentration was 830 mg/kg, and the copper concentration It is 533mg/kg, the lead concentration is 147mg/kg, and the zinc concentration is 2501mg/kg. (Table I) The relevant instruments and equipment used in the test are shown in Table 2 below: (Table 2) Among them, the pH meter and the conductivity meter are used to measure the pH value and conductivity of the sludge sample and the electrolyte, respectively. The flame atomic absorption spectrometer is used for the analysis and measurement of heavy metal concentration; the multi-stage variable-speed oscillator is used for sludge oscillation extraction. After the centrifuge oscillates and extracts the sludge, the solid and liquid of the sludge are separated by centrifugation for subsequent analysis and use. The pumping pump is used for the extraction of heavy metals in the sludge, and the sludge particles are completely filtered out, so that the subsequent samples can be analyzed on the machine. The DC power supply provides the DC power required for the operation of the electrodynamic treatment system for this test; the electronic balance provides the weighing of the test drugs and sludge samples; the deionized water manufacturing machine serves as the preparation of test drugs, sample analysis and experimental instruments Equipment cleaning and use. The electromagnetic stirrer is mainly used to prepare the electrolyte in the system, so that the test drugs and reagent water are evenly mixed; the ultrasonic cleaner is used to wash experimental glassware and laboratory instruments that are not easy to clean; the oven is used for the analysis of moisture content in sludge samples . The test drugs used in this institute are shown in Table 3 below: (Table 3) Sodium carbonate is formulated to a concentration of 0.01 M and used as an electrolyte in the electric power system. The manufacturer is Sigma-Alorich with a purity of 99.8%. The manufacturers of nitric acid and hydrochloric acid are all produced by Merck with purity of 65% and 37, respectively. %, mainly used for the preparation of aqua regia of heavy metal detection method-aqua regia digestion method (NIEA S321.63B, 2003). Regarding the test of the removal of heavy metals in sewage sludge by electrodynamic technology, the electrodynamic treatment system in this study was tested under the conditions of 0.01 M sodium carbonate electrolyte, with graphite electrode plates (Graphite) and iridium dioxide plate (Dimensionally Stable Anode, referred to as DSA), Stainless Steel plate (Stainless Steel) as electrodes, with different voltage gradient operating factors: 1.0V/cm, 1.5V/cm and 2V/cm, 2.5V/cm. Regarding electromotive technology equipment and materials, the electromotive treatment system (as shown in Figure 3) designed in this experiment is equipped with an electromotive treatment system tank (ie, the electromotive reaction tank 93) made of polyvinyl chloride (PVC). The specifications are 26cm in length × 11cm in width × 11cm in height (inner diameter), and the sample storage tank is separated by a PVC separator in the tank body. The treatment system is supplied with DC power by a DC power supply, and a gauze-covered porous PVC plate is used as an interval between the polar plate and the sludge sample. After filling in the sludge sample to be processed and the operating electrolyte, the final voltage is passed Direct current. Regarding the test process of electrodynamic technology (as shown in Figure 2), the pretreatment of sludge and the analysis of basic physical and chemical characteristics, including the full analysis of the pH value, water content, organic matter content and heavy metal concentration of the sludge, will be carried out. The mud sample is placed in the sample storage tank of the mold field (about 450 g of sludge), and 0.01 M sodium carbonate electrolyte is injected around the electrolyte storage tank, with different operation electrode plates (graphite electrode plate, iridium dioxide electrode plate and (Stainless steel plates) The purpose of the test is to find the ideal plate type as the operating parameter of the system. After selecting the electrode plate with better operation effect, the experiment is conducted with the operation parameters of different voltage gradients. During the test, the system voltage and current changes are recorded daily and the pH value and conductivity of the electrolyte are measured. An appropriate amount of electrolyte is also injected daily. In addition, the sludge samples are taken once a day (about 3 g), and the collection points are respectively near the anode end (that is, the DC positive pole end 931), the center of the storage tank, and near the cathode end (that is, the DC negative pole end 932). After the sludge sample is dried, the heavy metal content of the sludge can be analyzed. Through the process of finding out the appropriate parameters of the electrodynamic technology processing system, the transmission mechanism of the electrochemical reaction occurring in the system is discussed in more depth. Remove heavy metal from the sludge and use it as a raw material for high temperature fermentation, then use it with the waste space bag (or waste poultry manure, waste wood chips) for planting Xiangru, heat it at 130 o C under high temperature fermentation, and add high temperature resistance The bacterium completes the transformation within 2 hours and develops non-toxic and harmless soil improvement materials. The key point is that this test is to explore the test of removing heavy metals in sewage sludge by using different types of electrode plates and applying different voltage gradients and other parameters. Based on the test results and related theories, appropriate operating conditions are sought to To achieve effective removal of heavy metals in sewage sludge. The best results are obtained as follows: [a] The concentration of heavy metals in the sludge treated by electrodynamic technology increases with the distance from the anode plate, and it can be seen that the electroosmotic flow of the electrochemical principle is generated by the electric field between the positive and negative electrodes And ion migration and other action mechanisms can effectively remove or concentrate heavy metal contaminants to a limited range. [b] In this study, when different electrode plates are used as the operating parameters of electrodynamic technology, the removal efficiency is better when using iridium dioxide electrode plates as electrode plates, among which the removal efficiency of heavy metals nickel, cadmium and chromium is the most significant, respectively 72.22% , 56.76% and 38.59%. [c] In this study, a five-day electrodynamic test was conducted under different voltage gradients. Cadmium, nickel, copper and lead had good removal rates at a voltage gradient of 2.0V/cm, which were 100%, 96.67%, and 17.89, respectively. % And 52.88%; the removal effect of chromium and zinc at 2.5V/cm is more significant, the removal rate is 80.07% and 44.09%. [d] In this test, 0.01 M sodium carbonate was used as the electrolysis operating fluid, iridium dioxide electrode plate was used as the anode plate, and stainless steel was used as the cathode plate. The test for removing heavy metals in sewage sludge by electrodynamic technology was performed. Cadmium and nickel were removed at a higher level The removal rate of cadmium can reach 100% under the voltage gradient of 2.0V/cm. [e] Use electrodynamic technology to treat heavy metals in sewage sludge, conduct a one-day test with different operating voltage gradients (2.0V/cm and 2.5V/cm), and the cost of electricity consumption if 100mg/kg heavy metals are removed About 0.93-99.6 yuan. [f] This product assists Wufeng Elementary School in greening the campus, and the results have been affirmed by the school. The advantages and effects of the present invention are as follows: [1] Full conversion to water sludge containing heavy metals can reduce pollution. The invention uses electric power technology to remove heavy metals from sewage sludge, and then converts them into soil improvement materials through steps such as mixing, high-temperature fermentation, and pile-over rot, to reduce pollution. Therefore, full conversion to water sludge containing heavy metals can reduce pollution. [2] Mixing several kinds of wastes for recycling is quite environmentally friendly. The invention removes the heavy metal from the sewage sludge and mixes it with waste (organic additives) of at least one of the discarded space bag, discarded poultry dung material and discarded sawdust after planting shiitake mushrooms. It can be recycled and reused after the steps of high temperature fermentation and pile rot. Therefore, it is quite environmentally friendly to mix and recycle several types of waste. The above is only a detailed description of the present invention through the preferred embodiment. Any simple modifications and changes made to this embodiment will not deviate from the spirit and scope of the present invention.

S1‧‧‧準備步驟 S1‧‧‧Preparation steps

S11‧‧‧下水污泥前處理步驟 S11‧‧‧Pretreatment steps of sewage sludge

S12‧‧‧去除重金屬步驟 S12‧‧‧Step of removing heavy metals

S2‧‧‧混合步驟 S2‧‧‧Mix step

S3‧‧‧高溫發酵步驟 S3‧‧‧High temperature fermentation step

S4‧‧‧翻堆腐熟步驟 S4‧‧‧ Steps of rot

S5‧‧‧完成步驟 S5‧‧‧Complete steps

61‧‧‧第一混合物 61‧‧‧The first mixture

62‧‧‧第二混合物 62‧‧‧Second mixture

63‧‧‧土壤改良材料 63‧‧‧ Soil improvement materials

71‧‧‧有機添加物 71‧‧‧ organic additives

81‧‧‧第一下水污泥 81‧‧‧First sludge

82‧‧‧第二下水污泥 82‧‧‧Second sewage sludge

83‧‧‧第三下水污泥 83‧‧‧The third sewage sludge

91‧‧‧污水處理場 91‧‧‧Sewage treatment plant

92‧‧‧高溫發酵裝置 92‧‧‧High temperature fermentation device

93‧‧‧電動力反應槽 93‧‧‧Electrodynamic reaction tank

93A‧‧‧電極板 93A‧‧‧electrode plate

93B‧‧‧電解液 93B‧‧‧Electrolyte

931‧‧‧直流正極端部 931‧‧‧DC positive pole

932‧‧‧直流負極端部 932‧‧‧DC negative terminal

A‧‧‧分佈重金屬區域 A‧‧‧Heavy metal distribution area

B‧‧‧較集中之重金屬 B‧‧‧ more concentrated heavy metals

第1圖係本發明之流程圖 第2圖係本發明之下水污泥處理成土壤改良材料過程之方塊圖 第3圖係電動力反應槽之示意圖 第4圖係第3圖之下水污泥包含之重金屬處理前與處理後之示意圖Figure 1 is a flow chart of the present invention. Figure 2 is a block diagram of the process of processing water sludge into soil improvement materials under the present invention. Figure 3 is a schematic diagram of an electrodynamic reaction tank. Figure 4 is a water sludge under Figure 3. Schematic diagram before and after heavy metal treatment

Claims (4)

一種下水污泥轉製土壤改良材料之方法,係包括:  一.準備步驟:將來自下水系統之污水處理場之下水污泥取出,此被定義為一第一下水污泥,將該第一下水污泥除去雜質後,成為一第二下水污泥;接著將該第二下水污泥中之重金屬去除,而形成一第三下水污泥;  二.混合步驟:將去除重金屬後之該第三下水污泥與一有機添加物混合,而形成一第一混合物;  三.高溫發酵步驟:將該第一混合物置入一高溫發酵裝置中,進行高溫發酵後形成一第二混合物,該高溫發酵裝置之發酵溫度係介於攝氏100至160度之間,且發酵時間係介於1至24小時之間;  四.翻堆腐熟步驟:將該第二混合物進行翻堆腐熟之程序至少3天;  五.完成步驟:最後轉製成一土壤改良材料。A method for converting sewage sludge into soil improvement materials includes:  一. Preparation steps: Take out the sewage sludge from the sewage treatment plant of the sewage system. This is defined as a first sewage sludge. After removing impurities from the first sewage sludge, it becomes a second sewage sludge; then Heavy metals in the second sewage sludge are removed to form a third sewage sludge;  二. Mixing step: mixing the third sewage sludge after removing heavy metals with an organic additive to form a first mixture;  三. High-temperature fermentation step: Put the first mixture into a high-temperature fermentation device to form a second mixture after high-temperature fermentation. The fermentation temperature of the high-temperature fermentation device is between 100 and 160 degrees Celsius, and the fermentation time is between Between 1 and 24 hours;  四. Step of turning and composing: the procedure of turning and composing the second mixture for at least 3 days;  Five. Completion steps: Finally converted into a soil improvement material. 如申請專利範圍第1項所述之下水污泥轉製土壤改良材料之方法,其中,該準備步驟係包括:  [a]下水污泥前處理步驟:於室溫下,將該第一下水污泥鋪平風乾至少24小時,並除去雜質後,研磨破碎再過篩網,而成為該第二下水污泥;  [b]去除重金屬步驟:設一電動力反應槽,將該第二下水污泥置於其內;該電動力反應槽內係設一對電極板,並供入一電解液,則該第二下水污泥與該電解液混合。另於分佈重金屬區域之兩端,分別接設一直流正極端部與一直流負極端部,其間具有一介於0至100V之預定電壓;當進行電動力反應時,多數帶正電荷的重金屬陽離子會朝該直流負極端部移動,而污泥中之陰離子則朝該直流正極端部移動,藉由正負電極之間電場產生電化學原理之電滲透流及離子遷移等作用機制,引導該第二下水污泥中之電解質溶液流動,最後可於該直流負極端部得到較集中之重金屬,而達到去除污染物的目的。The method for converting sewage sludge into soil improvement materials as described in item 1 of the scope of patent application, wherein the preparation steps include:  [a] Pretreatment step of sewage sludge: at room temperature, the first sewage sludge The mud is flat and air-dried for at least 24 hours, and after removing impurities, it is ground and crushed and then passed through a screen to become the second sewage sludge;  [b] Step of removing heavy metals: setting up an electrodynamic reaction tank, the second sewage sludge Placed in it; a pair of electrode plates are arranged in the electrodynamic reaction tank, and an electrolyte is fed, then the second sewage sludge is mixed with the electrolyte. In addition, at both ends of the distributed heavy metal region, a DC positive terminal and a DC negative terminal are respectively connected, and there is a predetermined voltage between 0 and 100V; when electrodynamic reaction is performed, more than positively charged heavy 金 is positive Move toward the negative end of the DC, and the yin in the sludge moves toward the positive and negative end of the DC. The electro-osmotic flow and ion migration of the electrochemical principle are generated by the electric field between the positive and negative electrodes to guide the second launch. The electrolyte solution in the sludge flows, and finally concentrated heavy metals can be obtained at the end of the DC negative electrode to achieve the purpose of removing pollutants. 如申請專利範圍第2項所述之下水污泥轉製土壤改良材料之方法,其中,該重金屬係包含鎘、鎳、銅、鉛、鉻、鋅其中至少一者。The method for converting water sludge into soil improvement materials as described in item 2 of the patent application scope, wherein the heavy metal includes at least one of cadmium, nickel, copper, lead, chromium, and zinc. 如申請專利範圍第1項所述之下水污泥轉製土壤改良材料之方法,其中,該有機添加物係選自種植香菇後之廢棄太空包、廢棄家禽糞材、廢棄木屑其中至少一項。The method for converting water sludge into soil improvement materials as described in item 1 of the patent application scope, wherein the organic additive is at least one selected from the group consisting of waste space bags after planting shiitake mushrooms, waste poultry manure, and waste wood chips.
TW106112798A 2017-04-17 2017-04-17 Method for converting sewage sludge into soil improvement material TWI648227B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW106112798A TWI648227B (en) 2017-04-17 2017-04-17 Method for converting sewage sludge into soil improvement material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW106112798A TWI648227B (en) 2017-04-17 2017-04-17 Method for converting sewage sludge into soil improvement material

Publications (2)

Publication Number Publication Date
TW201838936A true TW201838936A (en) 2018-11-01
TWI648227B TWI648227B (en) 2019-01-21

Family

ID=65033891

Family Applications (1)

Application Number Title Priority Date Filing Date
TW106112798A TWI648227B (en) 2017-04-17 2017-04-17 Method for converting sewage sludge into soil improvement material

Country Status (1)

Country Link
TW (1) TWI648227B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109320030A (en) * 2018-08-31 2019-02-12 中国石油化工股份有限公司 A kind of excess sludge small molecule reactor of petrochemical wastewater treatment process
CN111592201A (en) * 2020-05-28 2020-08-28 湖北华德莱节能减排科技有限公司 Electrochemical decomposition method for sludge solid waste

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101333123B (en) * 2007-10-12 2011-03-30 东莞市圣茵生物有机肥有限公司 Process for reclaiming city domestic sludge
CN101618977B (en) * 2008-07-03 2013-01-09 城市污染控制国家工程研究中心 High-temperature aerobic fermentation process for sludge with low energy consumption and no pollution
CN102887736B (en) * 2012-10-15 2015-02-04 熊汉夫 Method for preparing special fertilizer by treating kitchen waste, sludge and domestic waste in one machine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109320030A (en) * 2018-08-31 2019-02-12 中国石油化工股份有限公司 A kind of excess sludge small molecule reactor of petrochemical wastewater treatment process
CN111592201A (en) * 2020-05-28 2020-08-28 湖北华德莱节能减排科技有限公司 Electrochemical decomposition method for sludge solid waste

Also Published As

Publication number Publication date
TWI648227B (en) 2019-01-21

Similar Documents

Publication Publication Date Title
CN203380185U (en) Device for restoring polluted soil by using electrodynamic force
CN102886375B (en) Method for processing heavy metal Cd (Cadmium) contaminated soil
Avsar et al. Comparison of classical chemical and electrochemical processes for treating rose processing wastewater
CN105665437B (en) A kind of device using Electroremediation contaminated soil
CN102886374B (en) Method for electrically repairing heavy metal As (Arsenic) contaminated soil by using rhamnolipid
CN103241737A (en) Sludge bagasse active carbon and preparation method thereof
CN105126749A (en) Domestic sludge-based charcoal preparation method, and application of charcoal
CN102503059B (en) Method for removing heavy metal from sludge and device thereof
CN103406347A (en) Method for enriching heavy metals and organic matters in soil
US20220219212A1 (en) Stacked circulatable microbial electrochemical reactor and degradation method of petroleum hydrocarbon contaminated soil
CN109926447A (en) A variety of contaminated soil advanced oxidation collaboration electrodynamics in-situ remediation systems and method
TWI648227B (en) Method for converting sewage sludge into soil improvement material
WO2013170555A1 (en) Method for treating saline and alkali land and device therefor
CN107639108A (en) A kind of Ex-situ washing remediation of heavy-metal contaminated soil
CN105417928B (en) A method of using Fenton sludge to municipal sludge dehydrated in situ
CN104829076B (en) A kind of method of black smelly bed mud recycling treatment in polluted water body
CN105597676B (en) The preparation method of Metal Substrate charcoal and its application in heavy metal passivation
CN205701842U (en) A kind of device utilizing Electroremediation contaminated soil
Yilmaz et al. An empirical model for parameters affecting energy consumption in boron removal from boron-containing wastewaters by electrocoagulation
CN106424116B (en) A kind of anode electro catalytic electrode of electro reclamation cyanide polluted soil, electro reclamation device and restorative procedure
CN104668280A (en) Soil restoration method based on bioleaching and electrodynamics
CN107384977B (en) Method for enhancing lactic acid production efficiency of sludge fermentation organic waste by using positive voltage
Ghimire et al. Energy and nutrient recovery from dairy and municipal wastewater sources in a terracotta-biochar bioelectrochemical system
JP2006339132A (en) Method and apparatus for restoring electricity using soil fuel cell generation system
CN209318419U (en) A kind of plate shaped graphite electrode electric power contaminated soil remediation device