TW201634400A - Preparation of a composition for removing wastewater and restoring river course, and application method thereof - Google Patents

Preparation of a composition for removing wastewater and restoring river course, and application method thereof Download PDF

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TW201634400A
TW201634400A TW104108413A TW104108413A TW201634400A TW 201634400 A TW201634400 A TW 201634400A TW 104108413 A TW104108413 A TW 104108413A TW 104108413 A TW104108413 A TW 104108413A TW 201634400 A TW201634400 A TW 201634400A
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sewage
composition
zeolite
water
wastewater
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TW104108413A
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zhen-gang Lu
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Nanjing Shafeite Biotechnology Co Ltd
zhen-gang Lu
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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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/40Protecting water resources
    • Y02A20/402River restoration

Abstract

The present invention is a composition of the porous substance and microbe for removing wastewater and restoring river course and its application method. The fixed embedded biological catalyst in the present invention is not easy to be washed away after being added into the polluted river. Not only can the catalyst be used in the degradation of wastewater and channel water body pollutant, but the fixed material can also have the adsorption and fixation function for releasing the pollutant from the bottom mud of a river course, thereby achieving the purpose of reducing pollution of the bottom mud towards the covering water body.

Description

一種用於清除汙水與復育河道的組合物之製備與應用方法 Preparation and application method of composition for removing sewage and re-cultivating river channel

本發明係為一種用於清除汙水與復育河道的多孔洞物質與微生物組合物,該組合物係用於控制河道汙染、城市汙水、與養殖廢水。 The invention relates to a porous hole substance and microbial composition for removing sewage and re-cultivating river channels, and the composition is used for controlling river pollution, urban sewage, and aquaculture wastewater.

由於生活污染物的長期沉降、累積,導致城市河道黑臭底泥淤積,城市河道底泥污染是水體黑臭的重要來源,黑臭河道水體的外源污染與底泥污染兩者成為河道水體污染的主要來源。 Due to the long-term settlement and accumulation of domestic pollutants, black muddy sediments in urban rivers are deposited. Urban river channel sediment pollution is an important source of black body odor. The external pollution and sediment pollution of black and odor river waters become river water pollution. The main source.

城市河道黑臭主要是過量納汙導致水體供氧和耗氧失衡的結果,水體缺氧乃至厭氧條件下污染物轉化並產生氨氮、硫化氫、揮發性有機酸等臭惡臭物質以及鐵、錳硫化物等黑色物質。生活污水是導致城市河道黑臭的最普遍和最主要的污染源。其他污染源還有:生活垃圾、有機工業廢水、合流制管網溢流污水、污水廠尾水、畜禽養殖場糞便污水等。 The black odor of urban rivers is mainly the result of excessive oxygen pollution and oxygen imbalance and oxygen consumption. The water body is under oxygen and even anaerobic conditions convert pollutants and produce ammonia nitrogen, hydrogen sulfide, volatile organic acids and other stench substances and iron and manganese. Black substance such as sulfide. Domestic sewage is the most common and major source of pollution that causes black odor in urban rivers. Other sources of pollution include: domestic waste, organic industrial wastewater, overflow sewage from confluent pipe network, tail water from sewage plants, and sewage from livestock and poultry farms.

水體中的有機汙染是造成黑臭水最主要的因素,水體中的汙染物又大部分為有機性汙染物質,有機汙染物質為水體中最主要的耗氧物質,這些有機汙染物質排放入河川,前期在好氧微生物的分解作用下,將有機物質分解成CO2、H2O,造成水中的溶氧量大幅降低導致缺氧,厭氧微生物即取而代之繼續分解水中的有機物質,產生硫化物使水體變黑,厭氧作用分解有機物質產生的H2S、NH3和CH4多種小分子化合物的氣味混和飄出水面,使水體飄散臭味。也有研究指出,當水體當中還有大量的有機碳、 有機氮及有機磷汙染時,不管水中的溶氧量的多寡,在適宜的溫度下都會被好氧的放線菌以及厭氧的微生物的降解,並且生成不同類型的物質來導致水體變黑發臭。 Organic pollution in water is the most important factor causing black odor water. Most of the pollutants in water are organic pollutants. Organic pollutants are the most important oxygen-consuming substances in water. These organic pollutants are discharged into rivers. In the early stage, under the decomposition of aerobic microorganisms, the organic matter was decomposed into CO 2 and H 2 O, causing the oxygen dissolved in the water to be greatly reduced, resulting in anoxic. The anaerobic microorganisms then replaced the organic matter in the water and produced sulfides. The water body turns black, and the odor of various small molecule compounds of H 2 S, NH 3 and CH 4 produced by anaerobic decomposition of organic substances mixes and floats out of the water surface, causing the water body to scatter the odor. Some studies have also pointed out that when there is a large amount of organic carbon, organic nitrogen and organic phosphorus in the water, no matter the amount of dissolved oxygen in the water, it will be degraded by aerobic actinomycetes and anaerobic microorganisms at a suitable temperature. And generate different types of substances to cause the body of water to become black and smelly.

含有大量有機物質、營養物質,耗氧速率高,一般處於強還原環境,河道底泥二次污染易導致水體中氨氮、亞硝酸鹽、硫化物、糞臭等有害物質含量過高,造成水體黑臭,影響城市景觀和居民生活。河道污染底泥對上覆水體水質產生大的影響,底泥的治理能有效控制和減少其COD(化學需氧量Chemical oxygen demand)、氮、磷營養鹽等污染的釋放和對上覆水體的污染,因此控制河道底泥污染,是城市河道水環境改良的重要環節。 Contains a large amount of organic substances, nutrients, high oxygen consumption rate, generally in a strong reducing environment, secondary pollution of river bottom sediments easily lead to excessive levels of harmful substances such as ammonia nitrogen, nitrite, sulfide, fecal odor in water bodies, resulting in black body water Stinky, affecting urban landscapes and residents' lives. River polluted sediment has a great impact on the water quality of the overlying water. The treatment of sediment can effectively control and reduce the release of COD (Chemical Oxygen Demand), nitrogen and phosphorus nutrients, and the overlying water. Pollution, therefore controlling the sediment pollution of rivers, is an important part of the improvement of urban river water environment.

以往用於控制底泥污染的措施主要是疏竣清淤,這種方法成本較高,底泥的再處置也是一個複雜環保難題:通過水體曝氣增氧,可一定程度減少底泥污染,但對較淺的河道易導致底泥再懸浮:在河道中添加微生物製劑,這種方法對增強水體自淨能力有一定作用,缺點是在河道中微生物製劑易流失,頻繁投放,成本過高。 In the past, the measures used to control sediment pollution were mainly dredging and dredging. The cost of this method is relatively high. The re-disposal of sediment is also a complicated environmental protection problem: the aeration of water can increase the sediment pollution to a certain extent, but For shallow rivers, it is easy to resuspend the sediment: adding microbial preparations in the river channel, this method has a certain effect on enhancing the self-purification ability of the water body. The disadvantage is that the microbial preparations in the river channel are easily lost, frequently placed, and the cost is too high.

生物修復是指生物、特別是微生物催化降解有機污染物,從而修復被污染環境或消除環境中污染物的過程。水體中的微生物種類多、代謝類型多樣、適應能力強,利用水體中原先存在的微生物修復污染水體,強化自然界的淨化能力治理被污染的水體,具有投入少、耗能低、管理方便、安全等優點,符合建立經濟節約、資源迴圈、可持續發展社會理念。 Bioremediation refers to the process by which organisms, especially microbes, catalyze the degradation of organic pollutants to repair contaminated environments or eliminate pollutants in the environment. There are many types of microorganisms in the water body, various types of metabolism, and strong adaptability. The original microorganisms in the water body are used to repair the polluted water bodies, and the purification ability of the natural environment is strengthened to control the polluted water bodies, which has less investment, low energy consumption, convenient management, safety, etc. The advantages are in line with the concept of establishing economic savings, resource recycling and sustainable development.

微生物固定化方法是指利用化學或物理的方法,將游離微生物定位於限定的空間區域內,並保持完整性,且能反覆使用的基本技術。 固定化技術可對完整細胞進行固定,可最大限度地維持生物酶完整性和穩定性,提高單位元體積內微生物密度和流動速率,修復過程不受稀釋率高於微生物生長率的限制,固定化微環境有利於遮罩外界環境的不利影響,固定化顆粒的水力性質和沉降性能可靈活控制,是一項高效實用的污染環境修復技術。 Microbial immobilization refers to the basic technique of using chemical or physical methods to locate free microorganisms in a defined spatial region and maintain integrity and can be used repeatedly. Immobilization technology can immobilize intact cells, maximally maintain the integrity and stability of biological enzymes, increase microbial density and flow rate per unit volume, and the repair process is not limited by the dilution rate higher than the growth rate of microorganisms. The micro-environment is conducive to masking the adverse effects of the external environment. The hydraulic properties and sedimentation performance of the immobilized particles can be flexibly controlled, and it is an efficient and practical pollution-remediation technology.

目前微生物的固定化方法在國內外尚沒有統一的分類標準,方法也多種多樣,但主要有表面吸附(結合)固定化、交聯(鍵聯)固定化、(多聚體)包埋固定化和自身固定化(微生物細胞間自交聯固定化)等幾種方法。固定化微生物技術中,以包埋法最為常見。包埋法是將微生物封閉在天然高分子多糖類或合成高分子凝膠的網路中,從而使微生物固定化。其特點是能將固定化微生物製備成各種形狀(球狀、塊狀、圓柱狀、膜狀、布狀、管狀等),並且固定化後的微生物能增值,所以對它的研究最多,應用也最廣。包埋法中使用的材料主要有海藻酸鈉、聚乙烯醇、三醋酸纖維、瓊脂等,並添加輔助材料如活性炭、累托石、石灰石等以提高包埋材料的性能。在廢水的微生物處理過程中,主要利用微生物的生物化學作用,廢水中的有機污染物作為微生物生命活動過程中所需要的營養物質,並在微生物的生命活動過程中被吸收利用,並被轉化為易於分離或無害的物質。微生物在水體中具有改良水質、生物自淨、抑制藻類過度繁殖、控制水體富營養化、增加溶氧、降低COD、降低氨氮、降低磷含量、改善水環境生態平衡等功能。有研究表明,在未對河道底泥進行治理的情況下,經過氧化塘預處理、河道水體增氧、水體原位強化生物修復等措施的治理,河道下游水體又逐漸恢復黑臭。在對河道底泥進行生物強化氧化修復後,河道 污染水體水質得到顯著的改善和提高。 At present, there are no unified classification standards for immobilization methods of microorganisms at home and abroad, and there are various methods, but mainly surface adsorption (binding) immobilization, cross-linking (bonding) immobilization, (multimer) embedding immobilization. Several methods such as self-immobilization (self-crosslinking immobilization between microbial cells). Among the immobilized microbial techniques, the embedding method is the most common. The embedding method is to immobilize microorganisms by blocking microorganisms in a network of natural polymer polysaccharides or synthetic polymer gels. It is characterized in that the immobilized microorganisms can be prepared into various shapes (spherical, massive, cylindrical, membrane, cloth, tubular, etc.), and the immobilized microorganisms can be added, so the research on it is the most, and the application is also The widest. The materials used in the embedding method mainly include sodium alginate, polyvinyl alcohol, triacetate, agar, etc., and auxiliary materials such as activated carbon, rectorite, limestone, etc. are added to improve the performance of the embedding material. In the microbial treatment process of wastewater, the biochemical action of microorganisms is mainly utilized, and the organic pollutants in the wastewater are used as nutrients required for the life activities of microorganisms, and are absorbed and utilized in the life activities of microorganisms, and are converted into A substance that is easy to separate or harmless. Microorganisms have functions of improving water quality, self-purification, inhibiting algae overgrowth, controlling water eutrophication, increasing dissolved oxygen, reducing COD, reducing ammonia nitrogen, reducing phosphorus content, and improving ecological balance of water environment. Studies have shown that in the absence of treatment of river sediments, through the treatment of oxidation pond pretreatment, river water aeration, water body in situ enhanced bioremediation, the water body downstream of the river gradually recovers black odor. After the bio-enhanced oxidation repair of the river sediment, the river channel The quality of polluted water has been significantly improved and improved.

包埋固定化生物催化劑(IBC,immobilized biocatalysts)的優點包括:成本低、固定化容易操作並可製成各種形狀,可於常溫常壓下進行固定化、固定化對微生物無害、固定化後載體內細胞漏出少,環境中其他微生物不易進入、基質通透性佳、物理強度與化學穩定度佳(王建龍,2002)。 The advantages of embedding immobilized biocatalysts (IBC) include: low cost, easy immobilization, and various shapes, which can be immobilized at normal temperature and pressure, and immobilized to microorganisms, and immobilized. In vivo, the cells leak less, other microorganisms in the environment are not easy to enter, the matrix permeability is good, physical strength and chemical stability are good (Wang Jianlong, 2002).

生物催化劑(Biocatalyst)是指具有催化能力的蛋白酶或是生物活細胞,在特殊情況下也可能是核酸(Cech,1993),酶是在所有生命體中必要的物質,酶可以有效率並且有選擇性的催化各種生命體中的化學轉換。1839年,Payen和Persozu研究了處於發芽狀態的大麥水解澱粉為糊精和糖的過程,並純化出澱粉酶(Payen,1839)。在1973年時日本千煙一郎利用聚丙烯醯胺凝膠包埋固定化具有高活性天門冬氨酸酶的大腸桿菌(Escherichia coli)天門冬氨酸(千煙一郎,1975)。在此之後固定化生物催化劑(Immobilized biocatalyst)的相關研究並迅速的發展。 Biocatalyst refers to proteases or biological living cells with catalytic ability. In special cases, it may also be nucleic acids (Cech, 1993). Enzymes are essential substances in all living organisms. Enzymes can be efficient and selective. Sexually catalyzes the chemical transformation in various living organisms. In 1839, Payen and Persozu studied the process of germinated barley hydrolyzed starch as dextrin and sugar, and purified amylase (Payen, 1839). In 1973, Japanese Chihiro Ichiro was immobilized with Escherichia coli aspartic acid (H. Ichiro, 1975) with high activity aspartase. After that, related research on immobilized biocatalyst (Immobilized biocatalyst) has been rapidly developed.

沸石為一種常見生物催化劑的載體,透過固體吸附法將微生物細胞吸附到沸石表面,沸石的結構是以矽或鋁氧化物的四面體骨架結構(SiO4或AlO4)作為基本單位,透過氧原子連結矽、鋁的四面體形成一種三度空間骨架結構(Oliveira and Rubio,2007,Malekian et al.,2011)。因為鋁原子帶三價電荷,與氧原子結合成AlO4四面體骨架結構時,整個結構呈現帶負電荷的狀態,因此會吸附周遭附近的負電荷離子來中和其電性,也因為這樣的一種骨架構造產生了許多孔穴和空洞,沸石具有其他礦物還大的表面積(400-800m2/g),這樣的結構使得沸石擁有強大的吸附力以及離子交換能力,沸石表面的孔洞大小均勻,平均在0.3mm-1.0mm,小於此直徑的物質都會被吸附 (Popov et al.,2012)。利用沸石做生物催化劑載體,除了沸石表面擁有許多孔洞表積大、對微生物細胞沒有傷害性,在生物脫氮工藝中,一方面沸石自身也可以經由離子交換的過程中吸附水中的氨氮,另一方面透過沸石靜電作用將硝化菌固定並在沸石表面形成一層生物膜,生物膜會將沸石自身吸附水中的氨氮經由化學轉化為硝酸鹽,一種自我吸收並且自我硝化的循環發生在沸石的表面,沸石氨氮的能力因為表面微生物的作用不斷的再生,所以利用沸石做微生物催化劑載體在生物脫氮的工藝中,過程中為同時兼賦了物理吸附、離子交換以及生物硝化三個過程(Bai et al.,2010)。 Zeolite is a common biocatalyst carrier. The microbial cells are adsorbed to the surface of the zeolite by solid adsorption. The structure of the zeolite is based on the tetrahedral framework structure of yttrium or aluminum oxide (SiO 4 or AlO 4 ) as the basic unit. The tetrahedrons of tantalum and aluminum form a three-dimensional skeleton structure (Oliveira and Rubio, 2007, Malekian et al., 2011). Because the aluminum atom carries a trivalent charge and combines with the oxygen atom to form an AlO 4 tetrahedral skeleton structure, the entire structure exhibits a negatively charged state, so it adsorbs negatively charged ions in the vicinity to neutralize its electrical properties, and also because of such A skeleton structure produces a large number of cavities and voids. The zeolite has a large surface area (400-800 m 2 /g) of other minerals. This structure gives the zeolite a strong adsorption capacity and ion exchange capacity, and the pore size of the zeolite surface is uniform and average. At 0.3mm-1.0mm, substances smaller than this diameter are adsorbed (Popov et al., 2012). The use of zeolite as a biocatalyst carrier, in addition to the surface of the zeolite has a large number of pores and no damage to microbial cells. In the biological nitrogen removal process, on the one hand, the zeolite itself can also adsorb ammonia nitrogen in the water through ion exchange, another In the aspect, the nitrifying bacteria are fixed by the electrostatic action of the zeolite and form a biofilm on the surface of the zeolite. The biofilm converts the ammonia nitrogen adsorbed by the zeolite itself into a nitrate by chemical conversion. A self-absorption and self-nitration cycle occurs on the surface of the zeolite. The ability of ammonia nitrogen is continuously regenerated by the action of surface microorganisms. Therefore, the use of zeolite as a microbial catalyst carrier in the process of biological nitrogen removal has simultaneously resulted in three processes of physical adsorption, ion exchange and biological nitrification (Bai et al. , 2010).

本發明的固定化複合益生菌劑(CBM,complex beneficial microorganism)投入污染河道後,不易流失,不僅加強微生物菌劑對污染物的降解作用,其固定化基質還可促進對底泥釋放污染物的吸附固定作用,進一步達到減少底泥對上覆水體污染。 The immobilized composite probiotics (CBM) of the present invention are not easily lost after being put into a polluted river channel, and not only enhance the degradation of pollutants by microbial agents, but also the immobilized matrix can promote the release of pollutants from the sediment. Adsorption and fixation can further reduce the pollution of the overlying water by the sediment.

本發明選擇沸石為載體,沸石平均比重為2.12,體積在0.05-0.15cm3範圍較合適,其孔隙度適合微牛傘物的吸附固定,可對完整的微生物細胞進行固定,避免人為破壞生物酶的完整性和生化反應的穩定性;增殖速度快、效果好。沸石為載體的固定化細胞顆粒對於靜止或緩流污染水體中的底泥,可根據污染程度直接投加,操作簡單,無需改變自然環境和修築大規模構築物,不產生二次污染。沸石來源豐富,價格便宜。節省投資,簡化流程,實踐上安全可靠,經濟上費用低廉,工程投資僅為物理法、化學法修復的30-50%。 The invention selects zeolite as the carrier, the average specific gravity of the zeolite is 2.12, and the volume is suitable in the range of 0.05-0.15 cm 3 , and the porosity is suitable for adsorption fixation of the micro-bulb, and the intact microbial cells can be fixed to avoid artificial destruction of the biological enzyme. The integrity and stability of biochemical reactions; rapid proliferation and good results. The immobilized cell particles with zeolite as the carrier can directly add to the sediment in the water body of static or slow-flow pollution according to the degree of pollution, and the operation is simple, and it is not necessary to change the natural environment and build a large-scale structure, and no secondary pollution is generated. Zeolite is rich in source and cheap. Save investment, simplify the process, safe and reliable in practice, low in economic cost, engineering investment is only 30-50% of physical and chemical repair.

本發明所使用之載體可以球形藻膠代替。採用複合菌(硝化菌與反硝化菌),加上使用兩相(有氧與缺氧)的藻膠包埋,其原理為利用該 球形藻膠內部的氧氣分布不同,由於氧氣之滲透力,藻膠內部為缺氧區(anaerobic zone);藻膠外部為有氧區(aerobic zone)。有效去除污水中氨氮分為兩個步驟:硝化作用(nitrification;有氧狀態)產物為硝酸(NO3),與亞硝酸(NO2);反硝化作用(denitrification;厭氧狀態)產物為氮氣(N2)。有氧環境,只能進行硝化作用;反之,只能進行反硝化作用。一般污染河道或污水處理池,很難同地點同時維持有氧與厭氧狀態,或僅是包埋單一硝化菌種,其除氨氮效果均不佳;本發明採用之藻膠具有兩相(有氧和缺氧)的藻膠包埋複合菌組合物,對於污水中氨氮更有效率 The carrier used in the present invention may be replaced by a spherical algin. The use of composite bacteria (nitrifying bacteria and denitrifying bacteria), coupled with the use of two-phase (aerobic and anoxic) algae embedding, the principle is to use the oxygen distribution inside the spherical algae, due to the penetration of oxygen, The interior of the algin is an anaerobic zone; the exterior of the algin is an aerobic zone. Effective removal of ammonia nitrogen from wastewater is divided into two steps: nitrification (aerobic state) product is nitric acid (NO 3 ), and nitrous acid (NO 2 ); denitrification (denitrification; anaerobic state) product is nitrogen ( N 2 ). In an aerobic environment, nitrification can only be carried out; conversely, denitrification can only be carried out. Generally, polluted rivers or sewage treatment tanks are difficult to maintain aerobic and anaerobic conditions at the same time, or only a single nitrifying strain is embedded, and the effect of removing ammonia nitrogen is not good; the algin rubber used in the present invention has two phases (there are Oxygen and anoxic) algae-embedded composite bacteria composition, more efficient for ammonia nitrogen in sewage

本發明選擇的微生物為兼性厭氧混合菌,固定化後的微生物能長期保持清潔;固定化細胞顆粒的微環境有利於遮罩土著原生菌、毒性物質對微生物體的惡性競爭、吞噬和毒害,使其在複雜環境條件下穩定地發揮高效能。本發明採用生物修復主要指微生物修復,具體為無機載體沸石吸附固定微生物,對複合菌吸附速度快、增殖效果好。 The microorganism selected by the invention is a facultative anaerobic mixed bacteria, and the immobilized microorganism can be kept clean for a long time; the microenvironment of the immobilized cell particles is favorable for masking the vicious competition, phagocytosis and poisoning of the indigenous protozoa and toxic substances to the microorganisms, It enables high performance in a stable environment under complex environmental conditions. The invention adopts bioremediation mainly refers to microbial remediation, specifically adsorption and immobilization of microorganisms by inorganic carrier zeolite, and the adsorption speed of the composite bacteria is fast and the proliferation effect is good.

本發明也屬於底泥生物修復劑,由複合微生物菌劑、增氧劑和固定化載體組成,還可包含生物營養劑和生物解毒劑輔助藥物,達到高效去除污水中污染物的目的。由於多數河道污染區域大、具流動性,原生型微生物很難形成優勢降解菌群,污染底泥的特殊性質無疑對生物修復提出更高的要求,必須篩選組合優勢降解菌群,而且微生物固定化顆粒其密度,才能使優勢降解微生物菌群接觸到污染底泥,達到去除有機污染物的目的。 The invention also belongs to a sediment biological repairing agent, which is composed of a composite microbial agent, an oxygenating agent and an immobilized carrier, and can also comprise a biological nutrient and a biological antidote auxiliary drug, so as to achieve the purpose of efficiently removing pollutants in the sewage. Because most rivers have large pollution areas and are fluid, it is difficult for primary microorganisms to form dominant degradation bacteria. The special nature of contaminated sediments undoubtedly puts forward higher requirements for bioremediation. It is necessary to screen combined dominant degradation bacteria and microbial immobilization. The density of the particles can make the dominant degrading microbial flora contact the contaminated sediment and achieve the purpose of removing organic pollutants.

生態清淤劑是一種性能優異的環境淨化劑,通過提高水體的生命力和自淨能力,迅速地改善水質,是一種經濟的淨化方法。生態清淤 劑具有沉澱的功能,其本身及其附著的微生物不易流失,即使在水流動的河道、湖沼、水庫和漲退潮的海灘、港灣等地方,都可以有效的起作用。即便在很深的水域裡,都能沉入到底部,把淤泥裡的有機物吸收分解掉,並達到淨水、增氧、消除惡臭等效果。實際應用中,其它生物載體在河道需要固定才能起作用,而且往往會被水流沖垮需進行整復,而使用生態清淤劑則不會有此現象。 The ecological dredging agent is an environmental purifying agent with excellent performance. It is an economical purification method by improving the vitality and self-purification ability of the water body and rapidly improving the water quality. Ecological dredging The agent has the function of sedimentation, and the microorganism itself and its attached microorganisms are not easily lost, even in the rivers, lakes, reservoirs, and beaches and harbors where water flows, which can effectively function. Even in deep waters, you can sink to the bottom, absorb and decompose the organic matter in the mud, and achieve the effects of purifying water, increasing oxygen, and eliminating malodor. In practical applications, other biological carriers need to be fixed in the river to function, and they are often washed away by water, and this phenomenon is not the case with ecological dredging agents.

施放生態清淤劑,不用清淤機械、清運污泥,沒有散發臭氣的清淤場面。由於污染情況和污泥情況不同,根據已往的應用實例,施放一次生態清淤劑,河道的淤泥4-6個月可以減少20-30公分。施放生態清淤劑後,不需要曝氣充氧設備,原來缺氧黑臭的河道很快淨化。水質得到淨化後可以看到很多水生動物,促進水生生物的食物鏈修復。這個過程無需投放魚苗和其它物種,幾十天就長了許多水生生物與魚群,因此很適合淨化底質污染和水體生態修復。 The application of the ecological dredging agent does not require dredging machinery, clearing and transporting sludge, and there is no dredging scene with odor. Due to different pollution conditions and sludge conditions, according to the previous application examples, an ecological dredging agent is applied, and the sludge in the river can be reduced by 20-30 cm in 4-6 months. After the application of the ecological dredging agent, there is no need for aeration and oxygenation equipment, and the original oxygen-deficient black and odorous river channel is quickly purified. After the water is purified, many aquatic animals can be seen to promote the restoration of the food chain of aquatic organisms. This process eliminates the need to release fry and other species, and has grown many aquatic organisms and fish stocks for decades, making it ideal for purifying sedimentary and ecological restorations.

用生態清淤劑消除污泥替代清淤同時修復水生生態,可以與原有河道綜合治理任務對接,大大減少治理難度,提高治理效果,而且無二次污染。施放生態清淤劑之後,淨化劑及其吸附固著的微生物生物量巨大,可以吸收分解水體和淤泥裡含有的氨氮、硝酸鹽、亞硝酸鹽、硫化氫、硫化合物以及其它營養成分、致臭物。生態清淤劑的作用是吸收分解淤泥裡含有的有機物,當有機物被完全吸收分解之後,底泥表面就是一層不被吸收分解的砂石無機物,泥面變為灰白色。生態清淤劑還可以投放到汙水處理池、污泥池裡,可以分解除去剩餘淤泥、淨化水質、消除惡臭等。生態清淤劑在淨化海灘淤泥、分解水產養殖場淤泥、改善汙水處理的水質, 去除臭味、去除有毒的藻類和淨化湖泊水體等,都有出色的淨化能力。 The use of ecological dredging agent to eliminate sludge instead of dredging and repair aquatic ecology can be docked with the original river comprehensive management task, greatly reducing the difficulty of treatment, improving the treatment effect, and no secondary pollution. After the application of the ecological dredging agent, the purifying agent and the microorganisms adsorbed and immobilized are huge in biomass, and can absorb ammonia nitrogen, nitrate, nitrite, hydrogen sulfide, sulfur compounds and other nutrients contained in the decomposed water and sludge, and cause odor. Things. The function of the ecological dredging agent is to absorb and decompose the organic matter contained in the sludge. When the organic matter is completely absorbed and decomposed, the surface of the sediment is a layer of sandstone inorganic matter that is not absorbed and decomposed, and the mud surface becomes grayish white. The ecological dredging agent can also be placed in the sewage treatment tank and the sludge tank, which can decompose and remove the remaining sludge, purify the water, and eliminate the foul odor. The ecological dredging agent purifies the beach sludge, decomposes the silt of the aquaculture farm, and improves the water quality of the sewage treatment. It has excellent purification ability to remove odor, remove toxic algae and purify lake water.

一種用於清除汙水與復育河道的組合物,該組合物係包括改性沸石與微生物組合物。 A composition for removing sewage from a reforestation channel, the composition comprising a modified zeolite and a microbial composition.

一種用於清除汙水與復育河道的組合物,該組合物係包括藻膠與微生物組合物。 A composition for removing sewage and a reforestation channel, the composition comprising an algin and a microbial composition.

該微生物組合物之共同培養條件為以28℃、轉速200rpm、光照強度為1000lux之光照下,連續培養7天;再加入5%糖蜜、0.4%尿素及0.15%磷酸二氫鉀後,溫度控制於28℃並以發酵槽連續發酵5天。 The co-culture condition of the microbial composition is continuous culture for 7 days under the illumination of 28 ° C, 200 rpm, and light intensity of 1000 lux; after adding 5% molasses, 0.4% urea and 0.15% potassium dihydrogen phosphate, the temperature is controlled. The fermentation was continued for 5 days at 28 ° C in a fermentation tank.

該改性沸石製作方法為將絲光沸石(mordenite,化學式為(Ca,Na2,K2)Al2Si10O24‧7H2O)以蒸餾水洗淨烘乾,再將沸石浸泡於5%鹽酸中2小時;再以蒸餾水洗淨至pH值為中性並烘乾,並將沸石浸泡於5%氫氧化鈉中2小時,以蒸餾水洗淨至pH值為中性並烘乾。 The modified zeolite is prepared by washing mordenite (mordenite, chemical formula (Ca, Na 2 , K 2 ) Al 2 Si 10 O24‧7H 2 O) with distilled water, and then immersing the zeolite in 5% hydrochloric acid. After 2 hours; wash with distilled water until the pH is neutral and dry, and soak the zeolite in 5% sodium hydroxide for 2 hours, wash with distilled water until the pH is neutral and dry.

一種使用組合物清除汙水與復育河道的方法,該組合物係包括改性沸石與微生物組合物。 A method of using a composition to remove sewage and a reforestation channel, the composition comprising a modified zeolite and a microbial composition.

將該組合物投入汙水中或河道中,即可降解水中汙染物。 By putting the composition into sewage or a river, the pollutants in the water can be degraded.

該組合物添加於汙水量為每公升汙水加3-8克。 The composition is added to the amount of sewage plus 3-8 grams per liter of sewage.

該組合物添加於河道量為每平方公尺河水面積加400-750 克。 The composition is added to the river channel with an area of 400-750 per square meter of river water. Gram.

第1圖 掃描式電子顯微鏡拍攝改性沸石與沸石包覆CBM; 第2圖 以朗模等溫吸附方程式分析改性沸石對於氨氮吸附;第3圖 複合生物催化劑與沸石吸附氨氮的能力;第4圖 固定化生物催化劑處理淡水廢水之(A)氨氮濃度、(B)亞硝酸離子濃度;第5圖 固定化生物催化劑處理海水廢水之(A)氨氮濃度、(B)亞硝酸離子濃度;第6圖 固定化生物催化劑處理海水養殖汙水之(A)氨氮濃度、(B)亞硝酸離子濃度、(C)COD濃度、(D)含硫分子濃度;第7圖 固定化生物催化劑處理河道底黑臭汙水之(A)氨氮濃度、(B)亞硝酸離子濃度、(C)COD濃度、(D)懸浮固態粒子濃度、(E)含磷分子濃度、(F)含硫分子濃度。 Figure 1 Scanning electron microscope to capture modified zeolite and zeolite coated CBM; Figure 2 analyzes the adsorption of modified zeolite on ammonia nitrogen by the Langmode isotherm adsorption equation; Figure 3 shows the ability of composite biocatalyst to adsorb ammonia nitrogen with zeolite; Figure 4 shows the concentration of ammonia nitrogen in freshwater wastewater treated by immobilized biocatalyst (B)亚 nitrite ion concentration; Figure 5 immobilized biocatalyst treatment of seawater wastewater (A) ammonia nitrogen concentration, (B) nitrite ion concentration; Figure 6 immobilized biocatalyst treatment of marine aquaculture wastewater (A) ammonia nitrogen concentration, (B) nitrite ion concentration, (C) COD concentration, (D) sulfur-containing molecular concentration; Figure 7 immobilized biocatalyst for treatment of black odorous wastewater at the bottom of the channel (A) ammonia nitrogen concentration, (B) nitrite ion concentration (C) COD concentration, (D) suspended solid particle concentration, (E) phosphorus-containing molecular concentration, and (F) sulfur-containing molecular concentration.

CBM複合益生菌發酵製備 Preparation of CBM compound probiotics by fermentation

使用購自新竹食品工業研究所生物資源及保存中心(BCRC)之純種菌株,富集擴大培養光合細菌、枯草芽孢桿菌、硝化菌、乳酸菌、黴菌類、放線菌、酵母菌,7大類菌株以共棲培養製備複合益生菌(CBM),該複合菌係包括以下菌種:Rhodopseudomonas palustrisRhodospirillum rubrumRhodobacter sphaeroidesLactobacillus pentosusLactococcus lactisBacillus subtilisSaccharomycopsis fibuligeraOchrobactrum anthropiThiosphaera pantotrophaAchromobacter denitrificansPseudomonas stutzeriPenicillium citrinumChaetomium globosumAspergillus oryzaeAspergillus nigerMyrothecium verrucariaPichia psedopastorisStreptomyces albulus。依據各菌株之培養基以及最佳生長條件進行培養;培養基配方如下所示: YM MEDIUM(Saccharomycopsis fibuligera) Enrichment and cultivation of photosynthetic bacteria, Bacillus subtilis, nitrifying bacteria, lactic acid bacteria, molds, actinomycetes, yeasts, and 7 major strains using pure strains purchased from the Bioresources and Preservation Center (BCRC) of the Hsinchu Food Industry Research Institute Co-cultured composite probiotics (CBM), including the following species: Rhodopseudomonas palustris , Rhodospirillum rubrum , Rhodobacter sphaeroides , Lactobacillus pentosus , Lactococcus lactis , Bacillus subtilis , Saccharomycopsis fibuligera , Ochrobactrum anthropi , Thiosphaera pantotropha , Achromobacter denitrificans , Pseudomonas Stutzeri , Penicillium citrinum , Chaetomium globosum , Aspergillus oryzae , Aspergillus niger , Myrothecium verrucaria , Pichia psedopastoris , Streptomyces albulus . The culture was carried out according to the culture medium of each strain and the optimal growth conditions; the medium formula was as follows: YM MEDIUM ( Saccharomycopsis fibuligera )

YPD MEDIUM(Pichia psedopastoris) YPD MEDIUM( Pichia psedopastoris )

YEAST STARCH MEDIUM II(Streptomyces albulus) YEAST STARCH MEDIUM II ( Streptomyces albulus )

LACTOBACILLI MRS BROTH(Lactobacillus pentosusLactococcus lactis) LACTOBACILLI MRS BROTH( Lactobacillus pentosus , Lactococcus lactis )

NURIENT MEDIUM(Rhodopseudomonas palustrisRhodospirillum rubrumRhodobacter sphaeroidesAchromobacter denitrificansOchrobactrum anthropiPichia psedopastorisBacillus subtilis) NURIENT MEDIUM ( Rhodopseudomonas palustris , Rhodospirillum rubrum , Rhodobacter sphaeroides , Achromobacter denitrificans , Ochrobactrum anthropi , Pichia psedopastoris , Bacillus subtilis )

NS(non-sulfur)MEDIUM(Rhodopseudomonas palustrisRhodospirillum rubrumRhodobacter sphaeroides) Mineral solution:MgSO4‧H2O:0.2g,K2HPO4:1.0g FeSO4‧H2O:0.5g CaCl2:0.02g MnCl2‧H2O:0.002g NaMoO4‧H2O:0.001g最後加蒸餾水至1.0L NS (non-sulfur) MEDIUM ( Rhodopseudomonas palustris , Rhodospirillum rubrum , Rhodobacter sphaeroides ) Mineral solution: MgSO 4 ‧ H 2 O: 0.2 g, K 2 HPO 4 : 1.0 g FeSO 4 ‧ H 2 O: 0.5 g CaCl 2 : 0.02 g MnCl 2 ‧ H 2 O: 0.002 g NaMoO 4 ‧ H 2 O: 0.001 g Finally add distilled water to 1.0L

MALT EXTRACT MEDIUM I(Blakeslaa’s Formula)(Aspergillus oryzaeChaetomium globosumPenicillium citrinum) MALT EXTRACT MEDIUM I (Blakeslaa's Formula) ( Aspergillus oryzae , Chaetomium globosum , Penicillium citrinum )

POTATO DEXTROSE MEDIUM(PDA)(Aspergillus niger) POTATO DEXTROSE MEDIUM (PDA) ( Aspergillus niger )

待上述各純種菌株達109cfu/ml後,經將各純種菌液等量混合,再以厭氧與60Lux光照、攪動50rpm方式培養5~7天共存培養(symbiotic culture),此目的是使混合厭氧菌與好氧菌的培養液提供給不同菌群的所需物質(包括:碳源與氮源;氨基酸、糖類、脂肪、維他命),這些營養基質, 可確保這些微生物菌群形成一個互利共生,共棲生存的穩定的微生物生態系。 After the above pure seed strains reached 109 cfu/ml, the pure seed culture liquids were mixed in equal amounts, and then cultured for 5-7 days by anaerobic irradiation with 60 Lux light and agitation at 50 rpm for the purpose of symbiotic culture. The mixed anaerobic bacteria and aerobic bacteria culture medium are supplied to different bacteria (including carbon source and nitrogen source; amino acid, sugar, fat, vitamin), and these nutrient substrates can ensure the formation of these microbial flora. A stable microbial ecosystem that is mutually beneficial and symbiotic.

前步驟共棲混合培養菌群再以28℃、轉速200rpm、光照強度為1000lux之光照下,連續培養7天。此步驟為第一次放大(first amplification)。 The pre-step eucommia mixed culture group was continuously cultured for 7 days at 28 ° C, a rotation speed of 200 rpm, and an illumination intensity of 1000 lux. This step is the first amplification.

前步驟共棲混合培養菌群再加入5%糖蜜、0.4%尿素及0.15%磷酸二氫鉀後,溫度控制於28℃並以發酵槽連續發酵5天,即可得CBM複合益生菌液。此步驟為第二次放大(second amplification)。 The pre-co-mixed culture group was further added with 5% molasses, 0.4% urea and 0.15% potassium dihydrogen phosphate. The temperature was controlled at 28 ° C and the fermentation tank was continuously fermented for 5 days to obtain CBM compound probiotic liquid. This step is a second amplification.

載體用沸石製備 Carrier prepared with zeolite

HCl-NaOH改性方法:將沸石以蒸餾水洗淨並烘乾,再將沸石浸泡在5% HCl中2小時。以蒸餾水洗至pH值為中性並烘乾,最後再將沸石浸泡在5% NaOH中2小時,以蒸餾水洗至pH值為中性並烘乾備用。 HCl-NaOH modification method: The zeolite was washed with distilled water and dried, and the zeolite was immersed in 5% HCl for 2 hours. Wash with distilled water until the pH is neutral and dry. Finally, the zeolite is immersed in 5% NaOH for 2 hours, washed with distilled water until the pH is neutral and dried for use.

新型固定化複合底泥淨化劑以沸石為微生物固定化主基質、並添加緩釋增氧劑和活性炭。沸石先後經過熱改性增大比表面積和孔隙率、有機改性提高對陰離子的吸附能力。沸石經改性後其架狀結構內部充滿了微孔和通道,能為微生物群落提供巨大的生物附著表面積,內部的孔洞還具有篩選分子的作用,並可以選擇優勢微生物種群和幫助它們繁衍。為了使底泥中存在微氧條件,還可採用緩釋增氧劑過氧化鈣。其有效含量80%,理論增氧量0.22 O2 mg/mg,並可產生1.38mg/mg鹼度。本專利從本土底泥中進行菌株的篩選,富集擴大培養光合細菌、枯草芽孢桿菌、硝化反硝化細菌等8大類20多種菌株以共棲方式至製備複合益生菌(CBM)。固定化複合底質淨化劑製成顆粒狀、含水率15%,平均密度2.6。 The novel immobilized composite sediment purifying agent uses zeolite as a microorganism to immobilize the main matrix, and adds a slow-release oxygenator and activated carbon. The zeolite has been thermally modified to increase the specific surface area and porosity, and the organic modification improves the adsorption capacity of the anion. After modification, the zeolite is filled with micropores and channels inside the frame structure, which can provide a huge bio-attached surface area for the microbial community. The internal pores also have the function of screening molecules, and can select dominant microbial populations and help them to multiply. In order to provide micro-oxygen conditions in the sediment, a slow-release oxygenator calcium peroxide can also be used. Its effective content is 80%, the theoretical oxygen increase is 0.22 O 2 mg/mg, and it can produce 1.38 mg/mg alkalinity. This patent screens strains from indigenous sediments, enriches and enriches and cultures photosynthetic bacteria, Bacillus subtilis, nitrifying denitrifying bacteria and other 8 types of more than 20 strains in a commensal manner to prepare composite probiotics (CBM). The immobilized composite substrate purifying agent was made into pellets, having a water content of 15% and an average density of 2.6.

載體用藻膠製備 Carrier prepared with algin

以10%聚乙烯醇(PVA)和2%海藻酸鈉(sodium alginate)為基本載體加水至100克,於80℃加熱至PVA完全溶解後加入2克改性沸石粉,於121℃、1.5大氣壓力(atm)進行滅菌20分鐘,放置冷卻至常溫。加入10%離心後的菌泥,將混合物倒入50mL針筒中,慢慢滴入含有2%氯化鈣(CaCl2)的硼酸飽和溶液中在4℃下固定化形成直徑3毫米(mm)的小球,固定時間為24小時,取出後以生理蒸餾水沖洗2至3次即可備用。 Add water to 100 g with 10% polyvinyl alcohol (PVA) and 2% sodium alginate as the basic carrier, heat at 80 ° C until PVA is completely dissolved, then add 2 g of modified zeolite powder at 121 ° C, 1.5 atm. The force (atm) was sterilized for 20 minutes, and allowed to stand to cool to room temperature. Add 10% centrifuged slime, pour the mixture into a 50mL syringe, slowly drop it into a saturated solution of boric acid containing 2% calcium chloride (CaCl 2 ) and fix it at 4 ° C to form a diameter of 3 mm (mm). The pellets are fixed for 24 hours. After being taken out, rinse with physiological distilled water for 2 to 3 times to be used.

實施例1 改性沸石表面比較 Example 1 Comparison of Modified Zeolite Surfaces

本實驗將改性後的沸石以掃描式電子顯微鏡(SEM)拍攝表面比較未改性沸石的表面,實驗結果表示改性後的沸石表面有被強酸強鹼侵蝕的痕跡,表面明顯的延伸展開,孔洞孔徑變大,說明經過改性後的沸石表面積會增大,進而增加氨氮的吸附能力(第1圖)。有研究指出在氫氧化鈉改性的過程中會使沸石的表面積與總孔容比減少,表示沸石表面孔洞的孔徑也會增加,有利於那離子進行取代,進而提高沸石對於氨氮的吸附能力(朱豐華等,2010),孫興濱等人利用改性後的沸石研究其除磷的能力,研究結果表示未改性沸石表面呈不規則,孔洞空隙較小,雖然表面布滿了孔道,但是大部分孔道被其他物質所堵塞,改性後沸石的表面層次變得鮮明,表面的孔隙變大,形成一種珊瑚狀的表面結構,這樣的表面結構增加了沸石表面的表面積,也提高了沸石的吸附能力(孫興濱等,2010)。 In this experiment, the surface of the modified zeolite was compared with the surface of the unmodified zeolite by scanning electron microscopy (SEM). The experimental results showed that the surface of the modified zeolite had traces of strong acid and alkali corrosion, and the surface was obviously extended. The pore size increases, indicating that the surface area of the modified zeolite will increase, thereby increasing the adsorption capacity of ammonia nitrogen (Fig. 1). Studies have shown that in the process of sodium hydroxide modification, the surface area to total pore volume ratio of zeolite is reduced, indicating that the pore size of the pores on the surface of the zeolite will also increase, which is beneficial to the substitution of the ions, thereby increasing the adsorption capacity of the zeolite for ammonia nitrogen ( Zhu Fenghua et al., 2010), Sun Xingbin et al. used the modified zeolite to study its ability to remove phosphorus. The results show that the surface of the unmodified zeolite is irregular and the pores are small. Although the surface is filled with pores, most of the pores are Blocked by other substances, the surface layer of the modified zeolite becomes distinct, and the pores on the surface become larger, forming a coral-like surface structure. This surface structure increases the surface area of the zeolite surface and also increases the adsorption capacity of the zeolite ( Sun Xingbin et al., 2010).

朗模等溫吸附方程式(Langmuir isotherm)之中,方程式中qe為達到吸附平衡時單位吸附劑吸附量(mg/g),C為吸附質 之平衡濃度,qm為吸附劑飽和吸附量(mg/g),KL則為常數。將Langmuir equation取倒數:。以1/qe對1/C作圖,從截距與斜率得到吸附劑的飽和吸附量qm=17.89mg/g、吸附常數KL=3.42L/mol。 Langmuir isotherm Among them, in the equation, q e is the adsorption amount per unit of adsorbent (mg/g), C is the equilibrium concentration of the adsorbate, q m is the adsorbent saturated adsorption amount (mg/g), and K L is a constant. . Count the Langmuir equation: . The ratio of 1/q e to 1/C was plotted, and the saturated adsorption amount of the adsorbent qm=17.89 mg/g and the adsorption constant KL=3.42 L/mol were obtained from the intercept and the slope.

Langmuir等溫吸附模式的線性回歸R Spuare值高,代表改性絲光沸石對於氨氮的吸附模式,符合Langmuir等溫吸附模式,吸附常數KL愈高代表吸附劑吸附能力愈高(第2圖)。Englert等人對天然智力沸石(主要成分為斜法沸石以及絲光沸石)的特性及其對氨氮的吸附能力做研究,研究結果表示天然智利沸石表表面積為177m2/g,對氨氮離子交換容量為1.02meq/g,在對氨氮吸附能力的研究結果則說明天然智利沸石對氨氮的吸附速率相當快,吸附容量可以達0.68meq/g,且吸附模式可與Langmuir吸附模式相符(Englert and Rubio,2005)。 The linear regression of the Langmuir isotherm adsorption mode has a high R Spuare value, which represents the adsorption mode of modified mordenite for ammonia nitrogen, which is consistent with the Langmuir isotherm adsorption mode. The higher the adsorption constant K L , the higher the adsorption capacity of the adsorbent (Fig. 2). Englert et al. studied the properties of natural intellectual zeolite (mainly composed of zeolite and mordenite) and its adsorption capacity for ammonia nitrogen. The results show that the surface area of natural Chilean zeolite is 177 m 2 /g, and the exchange capacity of ammonia nitrogen is 1.02meq/g, the results of the adsorption of ammonia nitrogen showed that the natural Chilean zeolite adsorption rate of ammonia nitrogen is quite fast, the adsorption capacity can reach 0.68 meq/g, and the adsorption mode can be consistent with the Langmuir adsorption mode (Englert and Rubio, 2005). ).

實施例2 表面吸附固定化CBM複合微生物沸石處理污水分析 Example 2 Analysis of Sewage Treatment by Surface Adsorption and Immobilization of CBM Composite Microbial Zeolite

利用改性的絲光沸石及複合型生物催化劑對氨氮模擬廢水處理比較兩者與不投加沸石的控制組進行氨氮吸附能力的比較,實驗結果顯示複合型生物催化劑的氨氮吸附能力明顯比改性後絲光沸石的氨氮吸附能力強。且由實驗結果得知沸石的氨氮去除率可達52%,複合生物催化劑的氨氮去除率可達63%(第3圖)。 The modified mordenite and composite biocatalyst were used to compare the ammonia nitrogen adsorption capacity of the ammonia-nitrogen simulated wastewater treatment. The experimental results show that the ammonia-nitrogen adsorption capacity of the composite biocatalyst is significantly better than that after modification. Mordenite has a strong ammonia nitrogen adsorption capacity. The experimental results show that the ammonia nitrogen removal rate of zeolite can reach 52%, and the ammonia nitrogen removal rate of composite biocatalyst can reach 63% (Fig. 3).

CBM包埋固定化生物催化劑處理淡水廢水。氨氮淡水模擬廢水添加CBM包埋固定化生物催化劑,NH4+原濃度為4.5ppm,添加量為5g/L,控制組不添加,每日檢測NH4+濃度,進行3重複連續七日,結果顯示CBM有顯著降解水中氨離子的能力,且功效可延續7天以上(第4圖A)。亞硝 酸淡水廢水添加CBM包埋固定化生物催化劑,NO2-原濃度為0.4ppm,添加量為5g/L,控制組不添加,每日檢測NO2-濃度,進行3重複連續七日,結果顯示CBM有顯著降解水中亞硝酸離子的能力,且功效可延續7天以上(第4圖B)。 CBM is embedded in immobilized biocatalyst to treat freshwater wastewater. Ammonia nitrogen freshwater simulated wastewater was added with CBM embedded immobilized biocatalyst. The original concentration of NH 4+ was 4.5ppm, the added amount was 5g/L, the control group was not added, the NH 4+ concentration was detected daily, and 3 repeated for 7 consecutive days. It shows that CBM has the ability to significantly degrade ammonia ions in water, and the efficacy can last for more than 7 days (Fig. 4A). Adding CBM-embedded immobilized biocatalyst to nitrous acid fresh water wastewater, the original concentration of NO 2- is 0.4ppm, the addition amount is 5g/L, the control group is not added, the NO 2- concentration is detected daily, and 3 repetitions are repeated for 7 consecutive days. It shows that CBM has the ability to significantly degrade nitrite ions in water, and the efficacy can last for more than 7 days (Fig. 4B).

CBM包埋固定化生物催化劑處理海水廢水。氨氮海水廢水添加CBM包埋固定化生物催化劑,NH4+原濃度為4.5ppm,添加量為5g/L,控制組不添加,每日檢測NH4+濃度,進行3重複連續7日,結果顯示CBM有顯著降解水中氨離子的能力,且功效可延續7天以上(第5圖A)。亞硝酸海水模擬廢水添加CBM包埋固定化生物催化劑,NO2-原濃度為0.4ppm,添加量為5g/L,控制組不添加,每日檢測NO2-濃度,進行3重複連續7日,結果顯示CBM有顯著降解水中亞硝酸離子的能力,且功效可延續7天以上(第5圖B)。 CBM embeds immobilized biocatalyst to treat seawater wastewater. Ammonia-nitrogen seawater wastewater was added with CBM-embedded immobilized biocatalyst. The original concentration of NH 4+ was 4.5 ppm, the added amount was 5g/L, the control group was not added, the NH 4+ concentration was detected daily, and 3 repetitions were repeated for 7 days. The results showed CBM has the ability to significantly degrade ammonia ions in water, and its efficacy can last for more than 7 days (Fig. 5A). The nitrite seawater simulated wastewater was added with CBM embedded immobilized biocatalyst. The original concentration of NO 2- was 0.4ppm, the addition amount was 5g/L, the control group was not added, the concentration of NO 2- was detected daily, and 3 repetitions were repeated for 7 days. The results show that CBM has the ability to significantly degrade nitrite ions in water, and the efficacy can last for more than 7 days (Fig. 5B).

CBM包埋固定化生物催化劑處理海水養殖汙水。氨氮海水養殖汙水添加CBM包埋固定化生物催化劑,NH4+原濃度為1.38ppm,添加量為5g/L,控制組不添加,每日檢測NH4+濃度,進行3重複連續15日,結果顯示CBM有顯著降解水中氨離子的能力,且功效可延續15天以上(第6圖A)。亞硝酸海水模擬廢水添加CBM包埋固定化生物催化劑,NO2-原濃度為0.73ppm,添加量為5g/L,控制組不添加,每日檢測NO2-濃度,進行3重複連續15日,結果顯示CBM有顯著降解水中亞硝酸離子的能力,且功效可延續15天以上(第6圖B)。 CBM embeds immobilized biocatalyst to treat marine aquaculture wastewater. Ammonia nitrogen marine aquaculture wastewater was added with CBM embedded immobilized biocatalyst. The original concentration of NH 4+ was 1.38ppm, the addition amount was 5g/L, the control group was not added, the NH 4+ concentration was detected daily, and 3 repetitions were repeated for 15 days. The results show that CBM has the ability to significantly degrade ammonia ions in water, and the efficacy can last for more than 15 days (Fig. 6A). The nitrite seawater simulated wastewater was added with CBM embedded immobilized biocatalyst. The original concentration of NO 2- was 0.73ppm, the addition amount was 5g/L, the control group was not added, the NO 2- concentration was detected daily, and 3 repetitions were repeated for 15 days. The results show that CBM has the ability to significantly degrade nitrite ions in water, and the efficacy can last for more than 15 days (Fig. 6B).

海水養殖汙水添加CBM包埋固定化生物催化劑,COD原濃度為2.54ppm,添加量為5g/L,控制組不添加,每日檢測COD濃度,進行3重複連續15日,結果顯示CBM有顯著降解水中COD的能力,且功效可延續15天以上(第6圖C)。海水模擬廢水添加CBM包埋固定化生物催化劑,硫化物 (sulfide)原濃度為41ppb,添加量為5g/L,控制組不添加,每日檢測硫化物濃度,進行3重複連續15日,結果顯示CBM有顯著降解水中硫化物的能力,且功效可延續15天以上(第6圖D)。 CBM-embedded immobilized biocatalyst was added to marine aquaculture wastewater. The original COD concentration was 2.54ppm, the addition amount was 5g/L, the control group was not added, the COD concentration was measured daily, and 3 repetitions were repeated for 15 days. The results showed that CBM was significant. The ability to degrade COD in water, and the efficacy can last for more than 15 days (Figure 6 C). Seawater simulated wastewater added CBM embedded immobilized biocatalyst, sulfide The original concentration of (sulfide) was 41 ppb, the addition amount was 5g/L, the control group was not added, the sulfide concentration was measured every day, and 3 repetitions were repeated for 15 days. The results showed that CBM has the ability to significantly degrade sulfide in water, and the effect can be continued. More than 15 days (Fig. 6D).

實施例3 以新型CBM複合生物催化劑改善黑臭汙水 Example 3 Improving black odorous sewage with a novel CBM composite biocatalyst

CBM包埋固定化生物催化劑處理黑臭汙水。河道底部黑臭汙水添加CBM包埋固定化生物催化劑,添加固定化生物催化劑之實驗結果與添加改性後絲光沸石對於汙水中氨去除率的比較(第7圖A),以及添加固定化生物催化劑之實驗結果與添加改性後絲光沸石對於汙水中亞硝酸去除率的比較(第7圖B),各實驗組包括三重複,實驗數據以平均值與標準差表示。 CBM embeds immobilized biocatalyst to treat black odorous sewage. Adding CBM-embedded immobilized biocatalyst to the black odorous sewage at the bottom of the river, adding the experimental results of the immobilized biocatalyst and adding the modified mordenite to the ammonia removal rate in the sewage (Fig. 7A), and adding the immobilized organism The experimental results of the catalyst and the addition of the modified mordenite to the nitrite removal rate in the sewage (Fig. 7B), each experimental group consists of three repetitions, and the experimental data are expressed as mean and standard deviation.

河道底部黑臭汙水添加CBM包埋固定化生物催化劑,添加固定化生物催化劑之實驗結果與添加改性後絲光沸石對於汙水中COD去除率的比較(第7圖C),以及添加固定化生物催化劑之實驗結果與添加改性後絲光沸石對於汙水中懸浮固態粒子去除率的比較(第7圖D),懸浮粒子單位為水質濁度(NTU,nephelometric turbidity unit),各實驗組包括三重複,實驗數據以平均值與標準差表示。 Adding CBM-embedded immobilized biocatalyst to the black odorous sewage at the bottom of the river, adding the experimental results of the immobilized biocatalyst and adding the modified mordenite to the COD removal rate in the sewage (Fig. 7C), and adding the immobilized organism The experimental results of the catalyst and the addition of the modified mordenite to the removal rate of suspended solid particles in the sewage (Fig. 7D), the suspended particle unit is NTU (nephelometric turbidity unit), and each experimental group includes three repetitions. Experimental data is expressed as mean and standard deviation.

河道底部黑臭汙水添加CBM包埋固定化生物催化劑,添加固定化生物催化劑之實驗結果與添加改性後絲光沸石對於汙水中含磷分子去除率的比較(第7圖E),以及添加固定化生物催化劑之實驗結果與添加改性後絲光沸石對於汙水中含硫分子去除率的比較(第7圖F),各實驗組包括三重複,實驗數據以平均值與標準差表示。 Adding CBM-embedded immobilized biocatalyst to the black odorous sewage at the bottom of the river, adding the experimental results of the immobilized biocatalyst and adding the modified mordenite to the removal rate of phosphorus-containing molecules in the sewage (Fig. 7E), and adding and fixing The experimental results of the biocatalyst and the addition of the modified mordenite to the removal rate of sulfur-containing molecules in the sewage (Fig. 7F), each experimental group includes three repetitions, and the experimental data are expressed by the mean value and the standard deviation.

實施例4 水體與底泥同步原位生態修復應用 Example 4 Synchronous in situ ecological restoration application of water and sediment

將固定複合有益微生物(CBM)的底質淨化劑400-750g/m2,均 勻撒播在河底。並設2台功率2.2Kw提水式曝氣機,曝氣機每天運轉8小時。17天后水體消除黑臭現象,從上游至下游,呈現暗灰色-灰黃色-黃綠色的漸變過程,透明度從上游水體的12cm左右提高到下游處45cm左右,並且呈現從上游到下游逐步提高的趨勢。30天后,上游出現大量黃褐色上浮污泥。60天后底泥降解了45cm,上游漂浮褐色污泥逐漸減少。此時在水陸交界處種植0.3-0.5m沉水和挺水植物帶,並補充投加250g/m2底質淨化劑後進入水質維護期。 The substrate-purifying agent for fixing the complex beneficial microorganism (CBM) is 400-750 g/m 2 and spread evenly on the bottom of the river. There are 2 sets of 2.2Kw water-lifting aerators, and the aerator runs 8 hours a day. After 17 days, the water body eliminates the black odor phenomenon. From the upstream to the downstream, the dark gray-grey yellow-yellow-green gradient process appears. The transparency increases from about 12cm in the upstream water body to about 45cm in the downstream, and it gradually increases from upstream to downstream. . After 30 days, a large amount of yellow-brown floating sludge appeared in the upstream. After 60 days, the sediment was degraded by 45 cm, and the floating brown sludge in the upstream gradually decreased. At this time, 0.3-0.5m submerged and emergent plant belts were planted at the water and land junctions, and 250g/m 2 of substrate purifying agent was added to enter the water quality maintenance period.

比較添加底質淨化劑之後的河道水質,各項水汙染因子於第1表、第2表所列如下: Compare the water quality of the river after adding the sediment purifying agent. The water pollution factors are listed in Table 1 and Table 2 as follows:

沒有投放底質淨化劑,底泥呈黑色及有極強臭味。投放底質淨化劑後3個月,底泥得到淨化且沒有臭味,河底污泥與懸浮物SS降低45-60公分。各項造成河水臭味的生物因子於第3表所列如下: There is no primer purifying agent, and the sediment is black and has a strong odor. Three months after the release of the substrate purifying agent, the sediment was purified and had no odor, and the river bottom sludge and suspended solids SS were reduced by 45-60 cm. The biological factors that cause the smell of river water are listed in Table 3 as follows:

實施例5 複合微生物各菌種定量分析 Example 5 Quantitative Analysis of Various Microorganisms

為確認複合有益微生物(CBM)之中各菌種含量,以定量核酸聚合酶連鎖反應(quantitative PCR),定量分析複合有益微生物製劑中各個培養期(共存培養、第一次培養、第二次培養)各個菌種數量(copies)與比例。各培養期的定量彙整於第8圖。 In order to confirm the content of each species in the composite beneficial microorganism (CBM), quantitative analysis of each culture period in the complex beneficial microbial preparation (quantitative culture, first culture, second culture) by quantitative nucleic acid polymerase chain reaction (quantitative PCR) ) The number and proportion of each species. The quantitative analysis of each culture period is shown in Fig. 8.

本技術特別適合於無法開展疏浚作業的場合。克服了費用昂貴、雜訊過大、易散發臭味、難以處置問題等難題。採用複合底質淨化劑能夠對重金屬和磷起到一定穩定、無害的作用。如鉻和磷均能作為沉積物轉入底泥而減少對上覆水體的釋放。採用新型底質淨化劑能夠對嚴重污染的河道進行泥水一體化生態修復。該技術操作簡單,對河道防洪無任何不利影響,運行過程中無額外費用。 This technology is especially suitable for occasions where dredging is not possible. Overcome the problems of high cost, excessive noise, easy to smell, and difficult to handle. The use of a composite substrate purifying agent can play a stable and harmless effect on heavy metals and phosphorus. For example, both chromium and phosphorus can be transferred to the sediment as sediment to reduce the release of the overlying water. The use of a new type of substrate purifying agent can carry out muddy water integration and ecological restoration of seriously polluted rivers. The technology is simple to operate and has no adverse effects on river flood control, and there is no additional cost during operation.

上述多項功效,實屬充分符合新穎性及進步性之法定發明專利要件,爰依法提出申請,懇請 貴局核准本件發明專利申請案以勵發明。 The above-mentioned multiple functions are the statutory invention patents that fully meet the novelty and progress. If you apply in accordance with the law, you are requested to approve the invention patent application to encourage invention.

Claims (10)

一種用於清除汙水與復育河道的組合物,該組合物係包括多孔洞物質與微生物組合物。 A composition for removing sewage and a reforestation channel, the composition comprising a porous cavity material and a microbial composition. 如申請專利範圍第1項所述之組合物,該多孔洞物質為改性沸石或藻膠。 The composition according to claim 1, wherein the porous hole material is a modified zeolite or algin. 如申請專利範圍第1項所述之組合物,該微生物組合物之共同培養條件為以28℃、轉速200rpm、光照強度為1000lux之光照下,連續培養7天;再加入5%糖蜜、0.4%尿素及0.15%磷酸二氫鉀後,溫度控制於28℃並以發酵槽連續發酵5天。 The composition of the microbial composition according to claim 1, wherein the microbial composition is continuously cultured for 7 days at 28 ° C, a rotation speed of 200 rpm, and an illumination intensity of 1000 lux; and then 5% molasses, 0.4% is added. After urea and 0.15% potassium dihydrogen phosphate, the temperature was controlled at 28 ° C and the fermentation was continued for 5 days in a fermentation tank. 一種如申請專利範圍第2項所述的組合物之改性沸石製造方法,該製造方法包括將絲光沸石以蒸餾水洗淨烘乾,再將沸石浸泡於5%鹽酸中2小時;再以蒸餾水洗淨至pH值為中性並烘乾,並將沸石浸泡於5%氫氧化鈉中2小時,最後以蒸餾水洗淨至pH值為中性並烘乾。 A method for producing a modified zeolite according to the composition of claim 2, which comprises washing and drying the mordenite with distilled water, immersing the zeolite in 5% hydrochloric acid for 2 hours, and then washing with distilled water. The net to pH was neutral and dried, and the zeolite was soaked in 5% sodium hydroxide for 2 hours, and finally washed with distilled water until the pH was neutral and dried. 一種使用組合物投入汙水清除汙染的方法,係以申請專利範圍第1項所指之組合物投入汙水清除汙染。 A method for using a composition to inject sewage to remove pollution, which is to be used for sewage decontamination by the composition referred to in claim 1 of the patent application. 如申請專利範圍第5項所述之方法,該汙水係指淡水廢水、海水廢水、淡水養殖汙水、或海水養殖汙水等。 For example, in the method described in claim 5, the sewage refers to fresh water wastewater, seawater wastewater, freshwater aquaculture wastewater, or marine aquaculture sewage. 如申請專利範圍第6項所述之方法,該組合物添加於汙水量為每公升汙水投入3-8克。 The method of claim 6, wherein the composition is added in an amount of 3-8 grams per liter of sewage. 如申請專利範圍第5項所述之方法,該汙水係指水溝、蓄水池、汙水下水道、河道等處之汙水。 For example, in the method described in claim 5, the sewage refers to sewage in a ditch, a reservoir, a sewage sewer, a river, and the like. 如申請專利範圍第8項所述之方法,該組合物添加於汙水量為每平方公尺汙水面積投入400-750克。 The method of claim 8, wherein the composition is added to the sewage volume of 400-750 grams per square meter of sewage area. 如申請專利範圍第5項所述之方法,該清除汙染的方法包括降低胺離子、亞硝酸離子、含硫化合物、含磷化合物、固態懸浮粒子等濃度,與降低生物需氧量、化學需氧量。 According to the method described in claim 5, the method for removing pollution includes reducing the concentration of amine ions, nitrite ions, sulfur compounds, phosphorus compounds, solid suspended particles, etc., and reducing biological oxygen demand and chemical oxygen demand. the amount.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111807635A (en) * 2020-07-23 2020-10-23 河北林江环境科技发展有限公司 Process for removing heavy metal from sewage and drinking water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111807635A (en) * 2020-07-23 2020-10-23 河北林江环境科技发展有限公司 Process for removing heavy metal from sewage and drinking water

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