CN102826646A - Catalytic iron internal electrolysis biological fluidization filler and preparation method thereof - Google Patents
Catalytic iron internal electrolysis biological fluidization filler and preparation method thereof Download PDFInfo
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 240
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 118
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 92
- 239000000945 filler Substances 0.000 title claims abstract description 68
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 29
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 238000005243 fluidization Methods 0.000 title claims abstract description 10
- 239000000463 material Substances 0.000 claims abstract description 69
- 230000005484 gravity Effects 0.000 claims abstract description 57
- 238000003825 pressing Methods 0.000 claims abstract description 3
- 230000001105 regulatory effect Effects 0.000 claims abstract description 3
- 238000012856 packing Methods 0.000 claims description 32
- 239000011257 shell material Substances 0.000 claims description 30
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 18
- 229910052802 copper Inorganic materials 0.000 claims description 18
- 239000010949 copper Substances 0.000 claims description 18
- -1 polyethylene Polymers 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 239000004698 Polyethylene Substances 0.000 claims description 7
- 229920000573 polyethylene Polymers 0.000 claims description 7
- 239000004743 Polypropylene Substances 0.000 claims description 6
- 239000004033 plastic Substances 0.000 claims description 6
- 229920003023 plastic Polymers 0.000 claims description 6
- 239000002861 polymer material Substances 0.000 claims description 6
- 229920001155 polypropylene Polymers 0.000 claims description 6
- 229910001018 Cast iron Inorganic materials 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 239000012535 impurity Substances 0.000 claims description 5
- 239000000969 carrier Substances 0.000 claims description 4
- 239000000725 suspension Substances 0.000 claims description 4
- 238000012545 processing Methods 0.000 claims description 3
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 2
- 229910052709 silver Inorganic materials 0.000 claims description 2
- 239000004332 silver Substances 0.000 claims description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims 2
- 229910052763 palladium Inorganic materials 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 9
- 230000008901 benefit Effects 0.000 abstract description 3
- 238000004065 wastewater treatment Methods 0.000 abstract description 3
- 238000011282 treatment Methods 0.000 description 12
- 230000006870 function Effects 0.000 description 8
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- 238000005516 engineering process Methods 0.000 description 6
- 239000006260 foam Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000005273 aeration Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 230000007774 longterm Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000020477 pH reduction Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 239000005562 Glyphosate Substances 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000004699 Ultra-high molecular weight polyethylene Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000227 bioadhesive Substances 0.000 description 1
- 230000002210 biocatalytic effect Effects 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 230000007227 biological adhesion Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- XDDAORKBJWWYJS-UHFFFAOYSA-N glyphosate Chemical compound OC(=O)CNCP(O)(O)=O XDDAORKBJWWYJS-UHFFFAOYSA-N 0.000 description 1
- 229940097068 glyphosate Drugs 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 235000021190 leftovers Nutrition 0.000 description 1
- 238000011866 long-term treatment Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 230000037323 metabolic rate Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
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- 231100000331 toxic Toxicity 0.000 description 1
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- 229920000785 ultra high molecular weight polyethylene Polymers 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
本发明属于废水处理领域,公开了一种催化铁内电解生物流化填料及其制备方法。本发明公开的催化铁内电解生物流化填料,包括以下组分和重量百分含量:10-15%的外壳、80-90%的催化铁和0-5%比重调节材料。本发明公开的催化铁内电解生物流化填料制备方法,包括以下步骤:将催化铁压制成一定形状的催化铁内电解材料,将催化铁内电解材料和比重调节材料填充到外壳中,或者将催化铁内电解材料直接填充到具有调节功能的外壳中,从而制成可流化的生物填料。本发明解决了催化铁内电解容易堵塞的缺点,又充分保留了催化铁内电解填料的技术优点,如价廉易得、对环境无害、还原能力强、效果好、适用pH范围广等。The invention belongs to the field of waste water treatment, and discloses a biological fluidization filler for catalytic iron internal electrolysis and a preparation method thereof. The biological fluidized filler for internal electrolysis of catalytic iron disclosed by the invention comprises the following components and percentage by weight: 10-15% of shell, 80-90% of catalytic iron and 0-5% of specific gravity adjusting material. The preparation method of the catalytic iron internal electrolysis biological fluidized filler disclosed by the invention comprises the following steps: pressing the catalytic iron into a catalytic iron internal electrolytic material of a certain shape, filling the catalytic iron internal electrolytic material and the specific gravity adjustment material into the shell, or The electrolytic material in the catalytic iron is directly filled into the housing with regulating function, thus making a fluidizable biofiller. The invention solves the shortcoming that the inner electrolysis of the catalytic iron is easily blocked, and fully retains the technical advantages of the inner electrolytic filling of the catalytic iron, such as cheap and easy to obtain, harmless to the environment, strong reducing ability, good effect, and wide applicable pH range.
Description
技术领域 technical field
本发明属于废水处理领域,具体涉及一种催化铁内电解生物流化填料及其制备方法。The invention belongs to the field of waste water treatment, and in particular relates to a catalytic iron internal electrolysis biological fluidization filler and a preparation method thereof.
背景技术 Background technique
为了提高废水生物处理系统中的微生物量和活性,科技和工程人员开发了多种生物载体填料。根据填料的安装方式不同,可以分为固定式和流化式。前者如软性、半软性填料、组合填料、弹性填料等,这些填料虽然价格较低,但是安装需要对应的填料架,不止增加了投资和填料更换的困难,而且也影响填料下的相关水处理设备(如曝气、搅拌、配水等设备)的维护和更换。而流化填料使用、更换方便,可以根据实际需要随时调整投加量,因此目前流化填料成为生物载体的研究和应用热点,也开发了多种不同形式的流化填料,如“一种循环式水处理流化填料”(专利申请号:200720128864.7)、“一种高效脱氮水处理流化填料”(专利申请号:200720128865.1)、“空心齿形流化填料”(专利申请号:200510116790.0)、“多面流化填料”(专利申请号:200610137088.7)、“改良的生物流化填料”(专利申请号:200520128198.85)等,开发这些填料的主要目的为了是增加填料的比表面积、减少流化所需动力、提高填料的使用效率等,而其他作用相对较少。为了进一步提高流化载体填料对污染物去除效率,开发出了具有生物催化作用的流化填料,如“用于生物流化床的生物催化组合填料的制备方法”(专利申请号:200410018319.3),该填料将一定比例的活性炭、超高分子聚乙烯、铁、锰四种材料通过500-560℃高温焙烧制成。由于铁、锰的存在,一方面增加了电子传递功能,提高了生物的新陈代谢速度;另一方面还可以促使生化过程在无氧条件下高效完成,扩大了填料的使用范围。可以看出,该类填料制作条件要求较高,限制了其推广应用。In order to improve the microbial biomass and activity in wastewater biological treatment systems, scientists and engineers have developed a variety of biological carrier fillers. According to the different installation methods of packing, it can be divided into fixed type and fluidized type. The former includes soft, semi-soft packing, composite packing, elastic packing, etc. Although these packings are relatively cheap, they require corresponding packing frames for installation, which not only increases the investment and the difficulty of packing replacement, but also affects the related water under the packing. Maintenance and replacement of processing equipment (such as aeration, stirring, water distribution, etc.). The fluidized packing is easy to use and replace, and the dosage can be adjusted at any time according to the actual needs. Therefore, the current fluidized packing has become a hot spot in the research and application of biological carriers, and a variety of different forms of fluidized packing have also been developed, such as "a cycle Type water treatment fluidized packing" (patent application number: 200720128864.7), "a high-efficiency denitrification water treatment fluidized packing" (patent application number: 200720128865.1), "hollow tooth-shaped fluidized packing" (patent application number: 200510116790.0) , "multi-surface fluidized packing" (patent application number: 200610137088.7), "improved biological fluidized packing" (patent application number: 200520128198.85), etc. The main purpose of developing these packings is to increase the specific surface area of the packing and reduce the fluidization time. It needs power, improves the use efficiency of fillers, etc., while other functions are relatively small. In order to further improve the removal efficiency of fluidized carrier packing for pollutants, a fluidized packing with biocatalysis has been developed, such as "Preparation method of biocatalytic composite packing for biological fluidized bed" (patent application number: 200410018319.3), The filler is made of a certain proportion of activated carbon, ultra-high molecular weight polyethylene, iron, and manganese through high-temperature roasting at 500-560°C. Due to the existence of iron and manganese, on the one hand, it increases the electron transfer function and improves the metabolic rate of organisms; on the other hand, it can also promote the efficient completion of biochemical processes under anaerobic conditions, expanding the use range of fillers. It can be seen that the production conditions of this type of filler are relatively high, which limits its popularization and application.
催化铁内电解技术可以通过还原的方法将废水中的有毒有害的难降解有机污染物转化为低毒或无毒的易生物降解物质,同时产生的铁离子可以将磷酸盐沉淀,刺激微生物的新陈代谢,增强传统生物载体的挂膜性能,促进硝化细菌的增殖,因此既可以作为单独处理单元,也可以与生物处理技术组合使用,如“一种催化铁内电解污水处理方法及其使用的填料”(专利申请号:200510029765.9)、“催化铁还原与厌氧水解酸化协同处理工业废水的方法”(专利申请号:20081019601.0)。该方法对pH等外部条件要求低,应用方便,因此已经在工程中应用,取得了理想的效果。但是在实际应用中,由于催化铁内电解填料较重,在系统中通常以静止状态存在,因此尽管所采用的填料堆积比重较小,填料空隙率达到95%以上,但随着运行时间的延长,不可避免的出现堵塞现象,妨碍了废水与填料的直接接触,降低处理效果。此外,传统催化铁填料安装需要专门的支撑架,安装、更换困难。所以在使用该类催化铁内电解填料的同时,不得不考虑如何减少该类现象的发生而采取种种措施,这在一定程度上影响了该技术的推广应用。Catalytic iron internal electrolysis technology can convert toxic and harmful refractory organic pollutants in wastewater into low-toxic or non-toxic biodegradable substances by reduction method, and the iron ions produced at the same time can precipitate phosphate and stimulate the metabolism of microorganisms , enhance the film-hanging performance of traditional biological carriers, and promote the proliferation of nitrifying bacteria, so it can be used as a single treatment unit or in combination with biological treatment technologies, such as "a catalytic iron electrolysis sewage treatment method and the filler used therein" (Patent Application No.: 200510029765.9), "A Method for Cooperative Treatment of Industrial Wastewater by Catalytic Iron Reduction and Anaerobic Hydrolysis and Acidification" (Patent Application No.: 20081019601.0). The method has low requirements on external conditions such as pH and is easy to apply, so it has been applied in engineering and achieved ideal results. However, in practical applications, due to the heavy electrolytic filler in the catalytic iron, it usually exists in a static state in the system. Therefore, although the bulk density of the filler used is small and the void ratio of the filler reaches more than 95%, with the extension of the operating time , the inevitable clogging phenomenon hinders the direct contact between the waste water and the filler and reduces the treatment effect. In addition, the installation of traditional catalytic iron packing requires a special support frame, which is difficult to install and replace. Therefore, when using this kind of catalytic iron inner electrolytic filler, we have to consider how to reduce the occurrence of this kind of phenomenon and take various measures, which affects the popularization and application of this technology to a certain extent.
发明内容 Contents of the invention
本发明的目的是提供一种催化铁内电解生物流化填料。The purpose of the present invention is to provide a catalytic iron internal electrolysis biological fluidization filler.
本发明的另一个目的是提供一种上述催化铁内电解生物流化填料的制备方法。Another object of the present invention is to provide a preparation method of the above-mentioned internal electrolysis biological fluidized filler in catalytic iron.
本发明的技术方案如下:Technical scheme of the present invention is as follows:
本发明提供了一种催化铁内电解生物流化填料,该催化铁内电解生物流化填料包括以下组分和重量百分含量:The invention provides a catalytic iron internal electrolysis biofluidization filler, which comprises the following components and weight percentages:
外壳 10-15%,Shell 10-15%,
催化铁 80-90%,Catalytic iron 80-90%,
比重调节材料 0-5%。Specific gravity adjustment material 0-5%.
所述的外壳为现有悬浮生物载体所能采用的高分子材料,选自聚乙烯或聚丙烯材料。The shell is a polymer material that can be used in existing suspended biological carriers, and is selected from polyethylene or polypropylene materials.
所述的催化铁选自铁刨花或铜刨花中的一种或两种;其中,铁刨花为铸铁加工后的边角料,铁中含碳量0.05-0.5%,铁刨花厚度1.0-2.0mm,具有延展性和抗拉强度,除铁刨花外,其他杂质(如尘土、杂物等)≤2%;铜刨花为紫铜材料,厚度0.5-1.0mm,长度5-150mm,平均长度为60mm,宽度为2-20mm。The catalytic iron is selected from one or both of iron shavings or copper shavings; wherein, the iron shavings are scraps after cast iron processing, the carbon content in the iron is 0.05-0.5%, and the thickness of the iron shavings is 1.0-2.0mm. Ductility and tensile strength, except iron shavings, other impurities (such as dust, sundries, etc.) ≤ 2%; copper shavings are made of copper material, with a thickness of 0.5-1.0mm, a length of 5-150mm, an average length of 60mm, and a width of 2-20mm.
所述的比重调节材料选自泡沫塑料或空心塑料球等表观比重小于水的材料,或者是直接利用聚乙烯或聚丙烯材料加工成网状的半球球冠作为外壳,每个半球球冠制作时非孔隙部分中空,形成气囊,能够产生浮力,得到具有比重调节功能的外壳。The specific gravity adjustment material is selected from foamed plastics or hollow plastic balls and other materials whose apparent specific gravity is smaller than water, or the hemispherical caps directly processed into mesh using polyethylene or polypropylene materials as shells, and each hemispherical cap is made When the non-porous part is hollow, it forms an air bag, which can generate buoyancy, and obtain a shell with a specific gravity adjustment function.
本发明还提供了一种上述催化铁内电解生物流化填料的制备方法,该方法包括以下步骤:The present invention also provides a method for preparing the above-mentioned catalytic iron internal electrolysis biological fluidized filler, the method comprising the following steps:
将催化铁压制成一定形状的催化铁内电解材料,将催化铁内电解材料和比重调节材料填充到外壳中,或者将催化铁内电解材料直接填充到具有调节功能的外壳中,从而制成可流化的生物填料。The catalytic iron is pressed into a certain shape of the catalytic iron inner electrolytic material, and the catalytic iron inner electrolytic material and the specific gravity adjustment material are filled into the shell, or the catalytic iron inner electrolytic material is directly filled into the outer shell with the adjustment function, thus making it possible Fluidized biofill.
所述的催化铁压制成一定形状的催化铁内电解材料,包括以下步骤:将铁刨花和铜刨花按照质量比10∶1~20∶1的比例混合,并压制成堆积比重为0.15~0.30、直径为35~145mm的球状或半球冠状催化铁内电解材料;或先将铁刨花压制成同样堆积比重、直径、形状的单元块,然后按照质量比0.2%~1.0%的比例镀铜、镀钯或镀银等,即可制得催化铁内电解材料。The catalytic iron is pressed into a catalytic iron inner electrolytic material of a certain shape, comprising the following steps: mixing iron shavings and copper shavings according to a mass ratio of 10:1 to 20:1, and pressing them into a bulk specific gravity of 0.15 to 0.30, Spherical or hemispherical crown catalytic iron inner electrolytic material with a diameter of 35-145mm; or first press iron shavings into unit blocks with the same bulk specific gravity, diameter and shape, and then copper-plated and palladium-plated according to the mass ratio of 0.2%-1.0% Or silver plating, etc., can be prepared in the catalytic iron electrolytic material.
所述的外壳为两个半球冠的球形生物悬浮填料,或将高分子材料加工制作成外直径为40-150mm和内直径为35-145mm的两个网状半球球冠,孔隙率为35-65%,每个半球球冠非孔隙部分中空,形成气囊;其中,高分子材料选自聚乙烯或聚丙烯材料。The shell is two hemispherical spherical bio-suspension fillers, or the polymer material is processed into two reticular hemispherical spherical caps with an outer diameter of 40-150mm and an inner diameter of 35-145mm, with a porosity of 35- 65%, the non-porous part of each hemispherical crown is hollow to form an air bag; wherein, the polymer material is selected from polyethylene or polypropylene material.
所述的气囊在水中所形成的浮力等于组合填料产生重力的0.95-1.05倍,组合填料产生的重力包括:填料外壳本身产生的重力与内部催化铁内电解材料产生的重力,从而使得填料本身能够直接悬浮或者在微小紊动条件下悬浮于水中;以此类方法所得到的催化铁内电解生物流化填料,外壳同时起到了比重调节功能,因此该类催化铁内电解生物流化填料中的催化铁材料部分占总重量的85%-90%,外壳材料占总重量的10%-15%,比重调节材料为0%。The buoyancy formed by the airbag in water is equal to 0.95-1.05 times of the gravity generated by the combined filler, and the gravity generated by the combined filler includes: the gravity generated by the filler shell itself and the gravity generated by the electrolytic material in the internal catalytic iron, so that the filler itself can Directly suspended or suspended in water under slight turbulent conditions; the shell of the catalytic iron inner electrolysis biofluidization filler obtained by this method also plays the function of adjusting the specific gravity, so the catalytic iron inner electrolysis biofluidization filler The catalytic iron material accounts for 85%-90% of the total weight, the shell material accounts for 10%-15% of the total weight, and the specific gravity adjustment material accounts for 0%.
所述的比重调节材料加入比例以其在水中形成的浮力等于组合填料产生重力的0.95-1.05倍,组合填料产生的重力包括:外壳产生的重力、内部催化铁内电解材料产生的重力和比重调节材料本身产生的重力,从而使得填料本身能够直接悬浮或者在微小紊动条件下悬浮于水中。以此类方法制作所得到催化铁内电解生物流化填料其催化铁材料占整个填料重量的85%-90%之间,比重调节材料占1%-5%之间,而外壳材料占10%-15%之间。The addition ratio of the specific gravity adjustment material is equal to 0.95-1.05 times of the gravity generated by the combined filler in terms of the buoyancy formed in water. The gravity generated by the combined filler includes: the gravity generated by the outer shell, the gravity generated by the electrolytic material in the internal catalytic iron, and the specific gravity adjustment The gravity generated by the material itself enables the filler itself to be suspended directly or suspended in water under slightly turbulent conditions. The catalytic iron inner electrolysis biofluidized packing obtained by this method has a catalytic iron material that accounts for 85%-90% of the weight of the entire packing, a specific gravity adjustment material that accounts for 1%-5%, and a shell material that accounts for 10%. -15% between.
如上所述,催化铁内电解填料块与外壳材料以及比重调节材料结合必须牢固,且要遵循生物附着材料(作为组合填料外壳)在外,而催化铁内电解填料在内的原则,以充分发挥各自的功能。此外,外壳材料必须有足够大的空隙(35%~65%),即使在生物膜形成后,也能使得废水顺利进入催化铁内电解填料内部。As mentioned above, the electrolytic filler block in the catalytic iron must be firmly combined with the shell material and the specific gravity adjustment material, and the principle of bio-adhesive material (as a combined filler shell) outside and the electrolytic filler inside the catalytic iron must be followed to give full play to their respective functions. function. In addition, the shell material must have a large enough gap (35%-65%), even after the biofilm is formed, it can also make the waste water smoothly enter the interior of the electrolytic filler in the catalytic iron.
该发明通过巧妙地使用比重调节材料,使得催化铁内电解填料能够悬浮、流化,在保证催化铁内电解处理效果下,有效解决了传统催化铁内电解填料在使用过程中可能出现的堵塞问题。此外和现有生物载体结合,既强化了现有生物附着材料的挂膜性能,从而增加生物量和活性,同时生物的作用也确保了催化铁内电解的还原条件,减少了铁的消耗量。The invention makes the electrolytic filler in the catalytic iron suspend and fluidize through the clever use of the specific gravity adjustment material, and effectively solves the problem of blockage that may occur during the use of the traditional catalytic iron inner electrolytic filler while ensuring the electrolytic treatment effect in the catalytic iron . In addition, the combination with the existing biological carrier not only strengthens the film-hanging performance of the existing biological adhesion materials, thereby increasing the biomass and activity, but also ensures the reducing conditions for catalyzing the internal electrolysis of iron and reduces the consumption of iron.
该发明的关键技术是比重调节材料的控制,即在制作过程中,要求比重调节材料所产生的浮力等于0.95~1.05倍的整体组合填料的重力。The key technology of the invention is the control of the specific gravity adjusting material, that is, in the production process, the buoyancy produced by the specific gravity adjusting material is required to be equal to 0.95 to 1.05 times the gravity of the overall combined packing.
本发明同现有技术相比,具有如下优点和有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:
1.本发明解决了催化铁内电解容易堵塞的缺点,又充分保留了催化铁内电解填料的技术优点,如价廉易得、对环境无害、还原能力强、效果好、适用pH范围广等。1. The present invention solves the shortcoming that the electrolysis in the catalytic iron is easy to block, and fully retains the technical advantages of the electrolytic filling in the catalytic iron, such as cheap and easy to obtain, harmless to the environment, strong reducing ability, good effect, and a wide range of applicable pH wait.
2.本发明填料载体制作方法简单,材料易得,既可以利用一些废料,也可以充分利用现有填料或填料制作技术,而无需特殊设备或技术。2. The preparation method of the filler carrier of the present invention is simple, and the materials are easy to obtain. Some waste materials can be used, and the existing filler or filler manufacturing technology can be fully utilized without special equipment or technology.
3.本发明填料载体使用、更换方便,可以用于不同的池形,也可用于厌氧、缺氧、好氧等不同的环境条件。3. The packing carrier of the present invention is easy to use and replace, and can be used in different pool shapes, and can also be used in different environmental conditions such as anaerobic, anoxic, and aerobic.
4.本发明实现了催化铁内电解与生物的相互耦合,发挥了两者的协同作用。催化铁内电解产生的铁离子可以直接改变外部生物附着载体的挂膜性能,因此无需对现有生物载体进行表面活化处理,而且对外部生物也有强化作用。而外部由于覆盖生物膜,保证了内部催化铁内电解处于厌、缺氧状态,充分发挥其还原能力,减少了铁的消耗量。4. The present invention realizes the mutual coupling between catalytic iron electrolysis and biology, and exerts the synergistic effect of the two. The iron ions produced by catalyzing the internal electrolysis of iron can directly change the film-hanging performance of the external biological attachment carrier, so there is no need to perform surface activation treatment on the existing biological carrier, and it also has a strengthening effect on the external organisms. However, because the outside is covered with biofilm, it ensures that the internal catalytic iron electrolysis is in anaerobic and anoxic state, fully exerts its reducing ability, and reduces the consumption of iron.
具体实施方式 Detailed ways
以下结合实施例对本发明作进一步的说明。The present invention will be further described below in conjunction with embodiment.
实施例1Example 1
将铸铁加工后的边角料-铁刨花和铜刨花按照比例10∶1制成直径为95mm的球状催化铁单元材料,堆积比重为0.15,其中所用的铁刨花含碳量为0.5%,铁刨花厚度为2.0mm,具有延展性和抗拉强度,除铁刨花外,其它杂质为2%,所用的铜刨花采用铜片加工而成,厚度为1.0mm,长度为100mm,宽度为15mm。另外利用聚乙烯材料,制作外直径为100mm,内直径95mm的网状半球球冠,其孔隙率为55%,每个半球球冠非孔隙部分中空,形成气囊,该壳体的浮力等于壳体本身重力与球状催化铁单元材料重力和的0.95倍。把球状催化铁单元材料放置于两个半球冠状壳体内,合并固定,最终获得的催化铁内电解生物流化填料中的催化铁材料部分占总重量的90%,外壳(本身具有调节功能)占总重量的10%,比重调节材料0%。将获得的填料投放在处理化工园区废水的中试CAST池中处于悬浮状态,在有曝气情况下可以实现流化。经过7d后,生物填料表面布满生物膜,镜检发现其生物相及其丰富,而内部处于缺氧状态。长期运行发现内部催化铁内电解填料仍然过水性能良好,没有出现堵塞现象。Leftovers after cast iron processing-iron shavings and copper shavings are made into a spherical catalytic iron unit material with a diameter of 95mm according to a ratio of 10:1, and the bulk specific gravity is 0.15. The carbon content of the iron shavings used is 0.5%, and the thickness of the iron shavings is 2.0mm, with ductility and tensile strength, except for iron shavings, other impurities are 2%, the copper shavings used are processed from copper sheets, the thickness is 1.0mm, the length is 100mm, and the width is 15mm. In addition, polyethylene material is used to make a mesh hemispherical cap with an outer diameter of 100 mm and an inner diameter of 95 mm. Its porosity is 55%. The non-porous part of each hemispherical cap is hollow to form an air bag. The buoyancy of the shell is equal to the shell Its gravity is 0.95 times the sum of the gravity of the spherical catalytic iron unit material. The spherical catalytic iron unit material is placed in two hemispherical crown shells, combined and fixed, and the catalytic iron material in the electrolytic biofluidized filler in the finally obtained catalytic iron accounts for 90% of the total weight, and the outer shell (which itself has a regulating function) accounts for 90% of the total weight. 10% of the total weight, 0% of the specific gravity adjustment material. The obtained filler is placed in a suspended state in the pilot CAST tank for treating wastewater in chemical industry parks, and fluidization can be achieved with aeration. After 7 days, the surface of the biofiller was covered with biofilm, and the microscopic examination found that the biophase was extremely rich, while the interior was in an anoxic state. After long-term operation, it is found that the electrolytic filler in the internal catalytic iron still has good water-passing performance, and there is no clogging phenomenon.
实施例2Example 2
将将铸铁加工后的边角料-铁刨花和铜刨花按照比例15∶1制成直径为145mm的半球冠状催化铁单元材料,堆积比重为0.2,其中所用的铁刨花含碳量为0.05%,铁刨花厚度为1.0mm,具有延展性和抗拉强度,除铁刨花外,其它杂质为2%,所用的铜刨花采用铜片加工而成,厚度为0.5mm,长度为150mm,宽度为5mm。将催化铁内电解材料放置到现有直径为150mm的球形悬浮填料中,在催化铁单元材料中心处放置泡沫塑料,使得泡沫塑料的浮力等于整个催化铁内电解生物流化填料重力的1.0倍。最终形成的催化铁内电解生物流化填料催化铁部分占总重量的80%,外壳占13%,比重调节材料为2%。将此填料直接投放在处理化工园区废水的中试CAST池中处于悬浮状态,在曝气情况下可以实现流化。经过7d后,生物填料表面布满生物膜,镜检发现其生物相及其丰富,而内部处于缺氧状态。长期运行发现内部催化铁内电解填料仍然过水性能良好,没有出现堵塞现象。同样的悬浮载体直接投放在处理化工园区废水的中试水解酸化池中,使其处于悬浮流化状态,经过10d后,填料外部也长满微生物。长期运行发现内部没有出现堵塞现象。The scrap iron shavings and copper shavings processed by cast iron will be made into a hemispherical crown catalytic iron unit material with a diameter of 145mm according to a ratio of 15:1. The bulk specific gravity is 0.2, and the carbon content of the iron shavings used is 0.05%. The thickness is 1.0mm, with ductility and tensile strength. Except for iron shavings, the other impurities are 2%. The copper shavings used are processed from copper sheets. The thickness is 0.5mm, the length is 150mm, and the width is 5mm. The electrolytic material in the catalytic iron is placed in the existing spherical suspension filler with a diameter of 150 mm, and foam plastic is placed at the center of the catalytic iron unit material, so that the buoyancy of the foam plastic is equal to 1.0 times the gravity of the electrolytic biofluidized filler in the entire catalytic iron. The catalytic iron part of the electrolytic biological fluidized filler in the finally formed catalytic iron accounts for 80% of the total weight, the shell accounts for 13%, and the specific gravity adjustment material accounts for 2%. Put this filler directly in the pilot CAST tank for wastewater treatment in chemical industrial parks in a suspended state, and fluidization can be achieved under aeration. After 7 days, the surface of the biofiller was covered with biofilm, and the microscopic examination found that the biophase was extremely rich, while the interior was in an anoxic state. After long-term operation, it is found that the electrolytic filler in the internal catalytic iron still has good water-passing performance, and there is no clogging phenomenon. The same suspension carrier was directly placed in the pilot test hydrolysis acidification tank for the treatment of wastewater in the chemical industry park, making it in a suspended fluidized state. After 10 days, the outside of the filler was also covered with microorganisms. Long-term operation found that there is no blockage inside.
实施例3Example 3
将将铸铁加工后的边角料-铁刨花和铜刨花按照比例20∶1制成直径为36mm的半球冠状催化铁单元材料,堆积比重为0.3,其中所用的铁刨花含碳量为0.1%,铁刨花厚度为1.5mm,具有延展性和抗拉强度,除铁刨花外,其它杂质为1%,所用的铜刨花采用铜片加工而成,厚度为0.5mm,长度为50mm,宽度为10mm。将该内电解材料放入直径为38mm的外壳内,添加以泡沫做成的比重调节材料(泡沫产生的浮力等于最终形成的整个组合填料重力的0.95倍),将外壳固定,形成可以悬浮于水中的催化铁内电解生物流化填料,该流化填料中的催化铁载体部分占总重量的85%,外壳占10%,比重调节材料占5%。将该填料用于处理草甘膦废水,在水力搅拌的条件下实现流化,其长期处理效果要好于固定式催化铁内电解填料系统,除磷率提高了20%左右。且1个月的运行,未发现堵塞现象,其处理效果也没有下降。The scrap iron shavings and copper shavings processed by the cast iron will be made into a hemispherical crown catalytic iron unit material with a diameter of 36mm according to the ratio of 20:1, the bulk specific gravity is 0.3, and the carbon content of the iron shavings used is 0.1%. The thickness is 1.5mm, with ductility and tensile strength. Except for iron shavings, other impurities are 1%. The copper shavings used are processed from copper sheets. The thickness is 0.5mm, the length is 50mm, and the width is 10mm. Put the inner electrolytic material into a shell with a diameter of 38mm, add a specific gravity adjustment material made of foam (the buoyancy generated by the foam is equal to 0.95 times the gravity of the entire combined packing that is finally formed), and fix the shell to form a material that can be suspended in water. The catalytic iron internal electrolysis biological fluidized packing, the catalytic iron carrier in the fluidized packing accounts for 85% of the total weight, the shell accounts for 10%, and the specific gravity adjustment material accounts for 5%. The filler is used to treat glyphosate wastewater, and fluidization is realized under the condition of hydraulic agitation, and its long-term treatment effect is better than that of the fixed catalytic iron internal electrolysis filler system, and the phosphorus removal rate is increased by about 20%. And after one month of operation, no clogging phenomenon was found, and the treatment effect did not decline.
上述的对实施例的描述是为便于该技术领域的普通技术人员能理解和应用本发明。熟悉本领域技术的人员显然可以容易地对这些实施例做出各种修改,并把在此说明的一般原理应用到其他实施例中而不必经过创造性的劳动。因此,本发明不限于这里的实施例,本领域技术人员根据本发明的揭示,不脱离本发明范畴所做出的改进和修改都应该在本发明的保护范围之内。The above description of the embodiments is for those of ordinary skill in the art to understand and apply the present invention. It is obvious that those skilled in the art can easily make various modifications to these embodiments, and apply the general principles described here to other embodiments without creative efforts. Therefore, the present invention is not limited to the embodiments herein. Improvements and modifications made by those skilled in the art according to the disclosure of the present invention without departing from the scope of the present invention should fall within the protection scope of the present invention.
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CN108503150A (en) * | 2018-06-06 | 2018-09-07 | 湖南航天凯天水务有限公司 | A kind of optimization integrated sewage treating apparatus |
CN109748380A (en) * | 2018-08-29 | 2019-05-14 | 郑州轻工业学院 | A kind of combined biological filler of foamed nickel and iron carbon and preparation method thereof |
CN109748380B (en) * | 2018-08-29 | 2021-07-06 | 郑州轻工业学院 | A kind of combined biological filler of foamed nickel and iron carbon and preparation method thereof |
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