Application of subsurface wastewater infiltration system to on-site treatment of domestic sewage under high hydraulic loading rate

In order to enhance the hydraulic loading rate （HLR） of a subsurface wastewater infiltration system （SWIS） used in treating domestic sewage, the intermittent operation mode was employed in the SWIS. The results show that the intermittent operation mode contributes to the improvement of the HLR and the pollutant removal rate. When the wetting-drying ratio （RwD） was 1.0, the pollutant removal rate increased by （13.6 ± 0.3）% for NH3-N, （20.7 ± 1.1）% for TN, （18.6± 0.4）% for TP, （12.2 ± 0.5）% for BOD, （10.1 ± 0.3）% for COD, and （36.2 ± 1.2）% for SS, compared with pollutant removal rates under the continuous operation mode. The pollutant removal rate declined with the increase of the HLR. The effluent quality met The Reuse of Urban Recycling Water - Water Quality Standard for Scenic Environment Use （GB/T 18921-2002） even when the HLR was as high as 10 cm/d. Hydraulic conductivity, oxidation reduction potential （ORP）, the quantity of nitrifying bacteria, and the pollutant removal rate of NH3-N increased with the decrease of the RWD. For the pollutant removal rates of TP, BOD, and COD, there were no significant difference （p 〈 0.05） under different RwDS. The suggested RWD was 1.0. Relative contribution of the pretreatment and SWlS to the pollutant removal was examined, and more than 80% removal of NH3-N, TN, TP, COD, and BOD occurred in the SWIS.

Fabrication of high-performance PVA/PAN composite pervaporation membranes crosslinked by PMDA for wastewater desalination

The pyromellitic dianhydride（PMDA） crosslinked poly（vinyl alcohol）（PVA） was coated on top of the PAN ultrafiltration membrane to form a PVA/PAN composite PV membranes for wastewater desalination. The composite membranes have high application value in industrial wastewater treatment. By varying the membrane fabrication parameters including the weight percent（wt%） of the PMDA, the crosslink temperature and duration, membrane with the best desalination performance was obtained. The composite membrane with a 2-lm-thick PVA selective layer containing 20 wt% of PMDA and being crosslinked at 100 °C for 2 h showed the highest Na Cl rejection of 99.98% with a water flux of 32.26 L/（m^2 h）at 70 °C using the 35,000 ppm Na Cl aqueous solution as feed. FTIR spectroscopy, wide-angle X-ray diffraction, thermogravimetric analysis and scanning electron microscope have been used to characterize the structures and properties of both the crosslinked PVA dense films and PVA/PAN composite membranes. The effects of the concentrations of PMDA,the crosslinking time and temperature to the membrane water contact angle, swelling degree, salt rejection and water flux were systematically studied.

Loosely coordinating diluted highly concentrated electrolyte toward -60℃ Li metal batteries

Lithium metal batteries(LMBs) promise energy density over 400 Wh kg^(-1).However,they suffer severe electrochemical performance deterioration at sub-zero temperatures.Such failure behavior highly correlates to inferior lithium metal anode(LMA) compatibility and sluggish Li^(+) desolvation.Here,we demonstrate that cyclopentylmethyl ether(CPME) based diluted high-concentration electrolyte(DHCE)enables-60℃ LMBs operation.By leveraging the loose coordination between Li^(+) and CPME,such developed electrolyte boosts the formation of ion clusters to derive anion-dominant interfacial chemistry for enhancing LMA compatibility and greatly accelerates Li^(+) desolvation kinetics.The resulting electrolyte demonstrates high Coulombic efficiencies(CE),providing over 99.5%,99.1%,98.5% and 95% at 25,-20,-40,and-60℃respectively.The assembled Li-S battery exhibits remarkable cyclic stability in-20,and-40℃ at 0.2 C charging and 0.5 C discharging.Even at-60℃,Li-S cell with this designed electrolyte retains> 70% of the initial capacity over 170 cycles.Besides,lithium metal coin cell and pouch cell with10 mg cm^(-2) high S cathode loading exhibit cycling stability at-20℃.This work offers an opportunity for rational designing electrolytes toward low temperature LMBs.

Treatment of Dyes Wastewater by a New Kind of Bio - Fluid Bed

A new kind of bio-fluid bed used to treat dyes wastewater is described in detail due to its several special features,such as high removal efficiency,simple struc-ture,shock load resistance,etc.By means of analyzing the experiment data,the results show that the dye wastewater’s organic matter is removed greatly after be-ing treated by this new kind of bio-fluid bed.On the other hand,the removal efficiency of chromaticity of

除氟剂HJ-DF-07用于煤化工含氟废水深度处理实验研究

采用自主研发的除氟药剂HJ-DF-07对煤化工含氟废水进行了深度除氟实验研究。比对了市场常见的几种除氟药剂和HJ-DF-07的除氟效果;考察了废水pH值、反应时间、两级除氟工艺中HJ-DF-07各自投加量等因素对除氟剂HJ-DF-07氟去除率的影响。结果表明:除氟剂HJ-DF-07对氟离子的去除率比其他几种除氟剂高出约20个百分点,其最佳操作条件为:pH值10.37,反应时间10 min,两级除氟工艺除氟剂投加量分别为3.0 mL/L和2.0 mL/L,相应的一级、二级氟去除率分别为81.74%和92.82%,最终二级除氟装置出水氟离子质量浓度可降至0.976 mg/L,总氟去除率可达98.69%。

Troubleshooting and Optimization of High-Strength Inhibitory Chemical Wastewater Treatment Process

从化学工业的废水通常具有高张力并且可以包含是的次要的禁止、不顺从的 organics 有时，不乐意地， identifiable.Thispaper 描述处理 43000 mg 中心点L~的 CODconcentration 的生物废水处理植物( WWTP )的经验(从含氧化学药品的 manufacturingplant.Stage 的-1)废水改进由导致 synergistic 进程的化学废水流完成的禁止的流入的使用其它的冲淡的植物过程，和由经由使发酸的析相作用的禁止的 organics 的移动，生产一条高质量的自河的有效地完成的进程优化。特别地，粒状淤渣的货到付款移动效率基于从 56% ～ 90%.The 期末考试自河货到付款增加的厌氧的反应堆从 250mg 中心点 L~ 减少了(-1) to50mg 中心点 L^(-1),consistently 遇见 l00 mg 中心点 L~ 的 COD 集中(-1)regulatory 分泌物限制。进程改进的成功在生物进程作为底层禁止者支持假设 thatlong 链 quaternary 羧酸行为。

Effects of hydraulic retention time, temperature, and effluent recycling on efficiency of anaerobic filter in treating rural domestic wastewater

With rural population expansion and improvement of the socio-economic standard of living, treatment of rural domestic wastewater has rapidly become a major aspect of environmental concern. Selection of a suitable method for treatment of rural domestic wastewater depends on its efficiency, simplicity, and cost-effectiveness. This study investigated the effects of hydraulic retention time （HRT）, temperature, and effluent recycling on the treatment efficiency of an anaerobic filter （AF） reactor. The first round of experimental operations was run for three months with HRTs of one, two, and three days, temperatures of 18℃, 21℃, and 24℃, and no effluent recycling. The second round of experimental operations was conducted for another three months with HRTs of three and four days; temperatures of 30.67℃, 30.57℃, and 26.91 ℃ ; and three effluent recycling ratios of 1：1, 1：2, and 2：1. The first round of operations showed removal rates of 32% to 44% for COD, 30% to 35% for TN, 32% to 36% for NH4-N, 19% to 23% for NO3-N, and 12% to 22% for TE In the second round of operations, the removal rates varied from 75% to 81% for COD, 35% to 41% for TN, 31% to 39% for NH4-N, 30% to 34% for NO3-N, and 41% to 48% for TP. The average gas production rates were 6.72 L/d and 7.26 L/d for the first and second rounds of operations, respectively. The gas production rate increased in the second round of operations as a result of applied effluent recycling. The best removal efficiency was obtained for an optimum HRT of three days, a temperature of 30℃, and an effluent recycling ratio of 2：1. The results show that the removal efficiency of the AF reactor was affected by HRT, temperature, and effluent recycling.

The Popularization and Application of Cold Storage Red Blood Cells or Whole Blood at -80 ℃ of the Rh(D) Negative Patients in Surgical Operation

Summary: The efficiency of cold storage red blood cells (CSRBC) or whole blood at -80 ℃ used in 27 Rh(D) negative patients during surgical operation was reported. The Rh(D) negative patients received the transfusion of CSRBC or whole blood stored at -80 ℃ for 180 to 360 days. The changes in the indexes, such as blood TB, DB, K +, Na +, BUN, Cr, urine protein (URPO), UOB, Hb, HCT, serum total protein, relative to hemolytic reaction and blood volume before and after transfusion were observed. The results showed that after transfusion of CSRBC or whole blood 27 cases were negative for urine protein and UOB, and the levels of BUN and Cr were normal (P>0.05). Blood TB, DB, Hb, and HCT were increased, while pH, blood K + and blood Na + was normal with the difference being not significant before and after operation (P>0.05). Plasma protein was decreased, but there was no significant difference before and after operation (P>0.05). It was suggested that CSRBC or whole blood at -80 ℃ could be safely infused to the Rh(D) negative patients without side effects during the surgical operation.

Optimization of double chamber microbial fuel cell for domestic wastewater treatment and electricity production

Microbial fuel cells(M FCs)represent a new approach for treating w aste w ater along w ith electricity production.The present study addressed electricity production from domestic w astew ater using a mediator-less double chamber M FC.The electricity production w as monitored under different operational conditions for both summer and w inter samples.Optimization of the anodic and cathodic chambers resulted in a maximal current of 0.784 and 0.645 m A w ith the maximal pow er intensity of 209 and 117 m W/m2in pow er duration of 24 h for the summer and w inter samples,respectively.Scanning electron microscopy show ed that the bacterial biofilm formation on the anode w as denser for the summer sample than that w hen the w inter sample w as used,so w as the total bacterial count.Therefore,samples taken during summer w ere considered better in electricity production and w aste w ater treatment than those taken during w inter basically because of the high microbial load during the hot season.In parallel,there w as a decrease in both biological oxygen demand(BOD5)and chemical oxygen demand(COD)values which reached 71.8%and 72.85%,respectively at the end of the operation process for the summer sample,w hile there w as no evident decrease for the w inter sample.Optimizing the operating conditions not only increased the potential of using domestic w aste w ater in microbial fuel cells to produce electricity,but also improved the quality of the domestic w aste w ater.

Treatment of Tannery Wastewater by the Application of Electrocoagulation Process Using Iron and Aluminum Electrodes

Until relatively recently, little has been done of effective technique “zero effluent” to conserve energy and water. Tannery wastewater is known as complex characteristics. In this study batch electrocoagulation experiments were carried out to assess the removal of color and chemical oxygen demand (COD) from tannery wastewater using two types of electrode materials: aluminum and iron. The effects of current density, electrolysis time and initial pH were investigated for tannery wastewater. Therefore, the operating costs for each electrode have been calculated. Based on results, it can be concluded that iron is tremendous to aluminum as electrode material, from COD removal and energy consumption views. All the conclusions of the study revealed that treatment of tannery by EC can be applied as a step of a hybrid treatment.

Occurrence and Roles of Comammox Bacteria in Water and Wastewater Treatment Systems:A Critical Review

Nitrogen removal is a critical process in water treatment plants(WIPs)and wastewater treatment plants(WWTPs).The recent discovery of a novel bacterial process,complete ammonia oxidation(comammox,CMX),has refuted a century-long perception of the two-step conversion of NH3to NO3-.Compared with canonical nitrifiers,CMX bacteria offer undeniable advantages,such as a high growth yield propensity and adaptability to nutrient-and growth-limiting conditions,which collectively draw attention to validate the aptness of CMX bacteria to wastewater treatment.As there has been no comprehensive review on the relevance of CMX bacteria for sustainable water and wastewater treatment,this review is intended to discuss the roles and applications of CMX in the removal of nitrogen and pollutants from water and wastewater.We took into account insights into the metabolic versatilities of CMX bacteria at the clade and subclade levels.We focused on the distribution of CMX bacteria in engineered systems,niche differentiation,co-occurrence and interactions with cano nical nitrifiers for a better understanding of CMX bacteria in terms of their ecophysiology.Conceptualized details on the reactor adaptability and stress response of CMX bacteria are provided.The potential of CMX bacteria to degrade micropollutants either directly or co-metabolically was evaluated,and these insights would be an indispensable advantage in opening the doors for wider applications of CMX bacteria in WWTPs.Finally,we summarized future directions of research that are imperative in improving the understanding of CMX biology.

Experimental Research on Coke Wastewater Treatment by Hybrid Biological Reactor

Phase hybrid biological reactor (HBR) was used in treating coke wastewater by adding submerging fiber-ball fillers in suspended growth activated sludge.The optimum operation parameters for the highest performance were determined.It was found that the hybrid biological reactor worked well for the coke wastewater treatment in terms of Chemical Oxygen Demand (COD),NH+4-N and other refractory organic compounds removal efficiencies.Compared with conventional activated sludge system,the removal rate of COD and NH+4-N and the nitrating rate were higher and more stable in the hybrid biological reactor.COD of effluent was less than 75 mg/L and the removal rate of COD and NH+4-N could be up to 95.0% and 92.5% when COD of influent and NH+4-N were less than 700 mg/L and 300 mg/L,respectively.In this way,the quality of effluent concentration could reach the first class of integrated wastewater discharge standard (GB8978-1996)(COD ≤100 mg/L).

<i>H</i>(.,.)<i>- φ - η -</i>Accretive Operators and Generalized Variational-Like Inclusions

In this paper, we generalize H(.,.) accretive operator introduced by Zou and Huang [1] and we call it H(.,.)- φ - η - accretive operator. We define the resolvent operator associated with H(.,.)- φ - η - accretive operator and prove its Lipschitz continuity. By using these concepts an iterative algorithm is suggested to solve a generalized variational-like inclusion problem. Some examples are given to justify the definition of H(.,.)- φ - η - accretive operator.

水解酸化+AAO+混凝沉淀+臭氧-BAF工艺在综合产业园废水处理中的应用

针对综合产业园废水处理项目进水水质成分复杂、可生化性较差、水质水量波动较大的特点,以潜江某综合产业园废水处理项目为例,介绍了该工程的废水特性、废水处理工艺、主要设计参数和运行效果,分析了不同工况下的污水处理运行费用。污水经“水解酸化+AAO+混凝沉淀+臭氧-BAF”工艺处理后,出水主要污染物指标可稳定达到《城镇污水处理厂污染物排放标准》(GB 18918—2002)一级A标准。污水处理厂投资为4826元/m^(3),设计工况下运行费用为1.399元/m^(3),实际低进水水质工况下的运行费用为0.755元/m^(3)。相关经验可为排水企业种类较多、具有相似水质特征的综合产业园污水处理厂提供参考。

Semi-Commutative Differential Operators Associated with the Dirac Opetator and Darboux Transformation

In the present paper, the semi-commutative differential oparators associated with the 1-dimensional Dirac operator are constructed. Using this results, the hierarchy of the mKdV (-) polynomials are expressed in terms of the KdV polynomials. These formulas give a new interpretation of the classical Darboux transformation and the Miura transformation. Moreover, the recursion operator associated with the hierarchy of the mKdV (-) polynomials is constructed by the algebraic method.

铁碳-芬顿-生物法处理丙烯酰胺生产废水

丙烯酰胺功能单体生产废水普遍具有COD、氨氮浓度高,可生化性差等特点。本研究利用铁碳微电解-Fenton-生物联合处理的方法对某丙烯酰胺生产企业综合废水进行处理,运行结果表明,该联合工艺对该类废水具有较强的处理能力与稳定性。Fe/C-Fenton联合预处理可使综合废水B/C从0.17提升至0.33,综合出水COD<120 mg/L,氨氮<30mg/L,满足《污水综合排放标准》(GB8978-1996)二级标准的要求,该组合处理系统综合运行成本为14.21元/m3,显著优于相似废水处理工程。

Developement of processes for nutrient removal from wastewater

This review focuses on techniques for achieving very low concentration of TN and TP in water.The 1970 Clean Water Act in the US and the Urban Waste Water Treatment Directive in Europe now provide the benchmark standards for TN and TP levels.Arden and Lockett discovered activated sludge in the 1910’s.Since then,many improvements have been made to the biological treatment process to provide various configurations that have the ability to deliver effluent concentrations between 6-8mg TN/L and 0.5-1.0mg TP/L,without external carbon addition.Typically,however,additional advanced nutrient removal technologies are used in tertiary treatment to meet more stringent effluent quality requirements.One advanced technology that has been successfully implemented in the US is denitrifying filters.For TP removal,tests showed that the BlueP RO and CoM ag systems both reliably met an effluent target as low as 0.04 mg TP/L.However,the establishment of stringent TN and TP effluent limits will dramatically increase the capital and operational costs of wastewater treatment plants.A more promising nutrient capturing process is based on the assimilation of nutrients(both N and P)during heterotrophic growth which uses a carbon source for energy.Laboratory trials of the single step process by Reach Green suggest that concentrations as low as 0.5 mg TN/L and 0.02mg TP/L are readily achievable.

A Comparative Analysis of the New -3(-n) - 1 Remer Conjecture and a Proof of the 3n + 1 Collatz Conjecture

This scientific paper is a comparative analysis of two mathematical conjectures. The newly proposed -3(-n) - 1 Remer conjecture and how it is related to and a proof of the more well known 3n + 1 Collatz conjecture. An overview of both conjectures and their respective iterative processes will be presented. Showcasing their unique properties and behavior to each other. Through a detailed comparison, we highlight the similarities and differences between these two conjectures and discuss their significance in the field of mathematics. And how they prove each other to be true.

铁基催化剂强化臭氧氧化深度处理印染废水的中试研究

针对广西玉林某工业园区污水处理厂二级工艺处理后的印染废水,利用铁刨花原位改性制备的铁基催化剂进行催化臭氧氧化中试,考察催化臭氧氧化技术对印染废水COD和色度的处理效果。实验结果表明:在本研究所使用的催化臭氧氧化反应器和反应条件下,进水COD在40~60 mg·L^(-1)范围,色度在80~120度范围,pH在6~9的印染废水,经过该工艺的处理可使出水水质稳定达到《纺织染整行业回用水水质》(FZ/T 01107—2011)标准。当进水COD维持在40 mg·L^(-1)以下时,出水COD可降至30 mg·L^(-1)甚至20 mg·L^(-1)以下,出水水质满足《地表水环境质量标准》(GB 3838—2002)Ⅳ类水标准。水力停留时间对处理效果的影响呈正态分布,建议值为60 min。铁基催化剂的活性组分和“微通道”结构,有利于臭氧与催化组分的结合以及羟基自由基的释放与作用,从而提高了臭氧利用率,使O_(3)/ΔCOD的值基本控制在2以下。

五格式净粪池与三格式化粪池处理农村生活污水效果及成本对比

针对三格式化粪池(TcST)出水COD及氮、磷浓度高,直排或溢流造成当地局部水体污染或黑臭的问题,构建了等容积五格式净粪池(FcPTR),并以实际生活污水为处理对象,对比研究2种反应器的运行特性和单位污染物去除成本。结果表明:FcPTR连续运行120 d,出水COD平均值为74 mg/L,TN、NH_(4)^(+)-N、TP平均浓度分别为26、20、1.6 mg/L,在我国进水水质相似的农村地区使用时,可满足11个省(区、市)发布的农村生活污水处理设施水污染排放地方标准二级水质要求。厌氧折流区、好氧区填料与污泥上变形菌门(Proteobacteria)的生长代谢促进了含氮和含磷物质的去除。相比于TcST,FcPTR明显增强了系统对有机物的降解和脱氮除磷效果,提高了系统的抗冲击负荷能力。经成本核算,在设计容积和运行场景相同时运行10年,FcPTR削减1 kg COD、1 kgNH_(4)^(+)-N的成本均比TcST降低19.8%。