Modelling anaerobic biofilm reactors--a review

Anaerobic treatment has become a technically as well as economically feasible option for treatment of liquid effluents after the development of reactors such as the upflow anaerobic sludge blanket (UASB) reactor, expanded granular sludge bed (EGSB) reactor, anaerobic biofilter and anaerobic fluidized bed reactor (AFBR). Considerable effort has gone into developing mathematical models for these reactors in order to optimize their design, design the process control systems used in their operation and enhance their operational efficiency. This article presents a critical review of the different mathematical models available for these reactors. The unified anaerobic digestion model (ADM1) and its application to anaerobic biofilm reactors are also outlined.     

太阳光催化反应器的研究进展

以太阳光为光源的光催化氧化技术是一种清洁和节能的污水处理技术。对廉价和高效的太阳光催化反应器的设计和放大是这项技术研究的关键,也是实现工业化应用的重要因素。结合近几年国外对太阳光催化反应器的研究,详细地讨论了目前几种太阳光催化反应器的发展及应用研究,比较了不同反应器的优缺点,同时提出一些建议和今后的研究方向。     

消毒技术去除饮用水中病原微生物的研究进展

饮用水中存在着不同种类的病原微生物,这些病原微生物给人体健康带来危害。本文简要介绍常规消毒技术去除饮用水中病原微生物的研究现状;常规消毒剂仍然是现代饮用水处理工艺使用的主要消毒剂;近些年来,对常规消毒剂联合消毒的协同作用和联合消毒剂的概念提出了探讨,认为联合消毒荆是今后饮用水去除病原微生物的发展趋势;膜技术这种物理消毒技术,由于其高效性而得到广泛关注,膜消毒去除病原微生物也成为当今消毒技术研究的热点。     

Design study of a 150 kWth double loop circulating fluidized bed reactor system for chemical looping combustion with focus on industrial applicability and pressurization

Nowadays the lab scale feasibility of the chemical looping combustion technology has been proved. This article deals with many of the design requirements that need to be fulfilled to make this technology applicable at industrial scale. A design for a 150 kW_th chemical looping combustion reactor system is proposed. In the base case it is supposed to work with gaseous fuels and inexpensive oxygen carriers derived from industrial by-products or natural minerals. More specifically the fuel will be methane and a manganese ore will be the basis for the oxygen carrier. It is a double loop circulating fluidized bed where both the air reactor and the fuel reactor are capable to work in the fast fluidization regime in order to increase the gas solids contact along the reactor body. High operational flexibility is aimed, in this way it will be possible to run with different fuels and oxygen carriers as well as different operating conditions such as variation in air excess. Compactness is a major goal in order to reduce the required solid material and possibly to enclose the reactor body into a pressurized vessel to investigate the chemical looping combustion under pressurized conditions. The mass and heat balance are described, as well as the hydrodynamic investigations performed. Most design solutions presented are taken from industrial standards as one main objective is to meet commercial requirements.     

Steam demand reduction of water–gas shift reaction in IGCC power plants with pre-combustion CO2 capture

This paper presents the results of system assessments that were conducted to compare conventional and advanced water–gas shift reactor sections. The latter are specifically tailored for Integrated Gasification Combined Cycles (IGCC) power plants with pre-combustion CO₂ capture. The advanced shift reactor section comprises four staged reactors with distributed feeds of synthesis gas and quench water in between the reactors. Conventional shift reactor sections consist of two sequential reactors with intermediate cooling, where the entire synthesis gas stream passes both reactors.The advanced shift reactor section reduces the steam requirement of the water–gas shift reaction up to 70% in comparison with conventional configurations, at carbon dioxide capture ratios of approximately 85%. This reduction allows for lower electric efficiency penalties, thus higher net electric outputs for IGCC power plants with CO₂ capture. For each case, the CO₂ capture ratio was optimised for the lowest specific lost work per amount of captured CO₂. Both the number of reactors and the total catalyst volume are higher for the advanced shift reactor sections, resulting in increased capital expenses. In case of four staged reactors, the additional expenses are expected to be outperformed by the increased revenues associated with the higher net electric output.     

废液处理新工艺超临界水氧化（SCWO）评述

超临界水氧化是一项对有机废液焚烧处理最有潜力的替代技术,在过去的20多年里,这项技术引起了广泛的关注。然而,作为一项管端技术,超临界水氧化仍存在许多不足,这些不足阻碍了它的工业应用。除了反应器腐蚀和盐析导致的技术问题外,超临界水氧化经常被认为是一项处理所有废液的“通用”技术,然而也是无法实现的“通用”技术。本文介绍了作为管端处理技术的超临界水氧化技术存在的问题,讨论了可能的解决办法,介绍了不同反应器的概念,提出了在超临界水氧化领域里开展进一步研究和发展新工艺流程的建议。此外,评价了超临界水氧化技术涉及到的自身能源供应问题。     

A NOVEL CHLORAMINE COMPOUND FOR WATER DISINFECTION1

A new chloramine agent, 3-chloio-4, 4-dimethyl-2-oxazolidinone, has been tested in a laboratory scale water treatment plant as to its efficacy in water disinfection. The agent seems to be equally effective as compared to chlorine gas in this application. The results of preliminary toxicity studies on the agent are very encouraging. The agent has a long shelf life both in water solution and in the solid state. Being a solid, the agent is clearly less hazardous to handle than chlorine gas. The agent appears to inhibit oxidative corrosion of metals as well. The agent is less likely to produce toxic halocarbons (e.g., chloroform) in water than is chlorine gas. Possibly most important from the standpoint of water disinfection, the agent is a “slow release” one for its positive chlorine, which provides prolonged bactericidal activity.     

Grey water reclamation by decentralized MBR prototype

Grey water treatment and reuse for non-drinking water requirements has become of great interest in arid and semi-arid zones where water resources are becoming both quantitatively and qualitatively scarce. In this study a decentralized and automatic MBR prototype has been designed and installed in the REMOSA facilities for treatment of low-load grey water to be recycled in flushing-toilet application. The recycling treatment of grey water comprises four stages: screening, biological oxidation, filtration and a final disinfection by chlorination. The influent and effluent were monitored in order to determine the treatment efficiency and assessment of the quality potential of treated grey water. The results obtained indicate that recycling of grey water allows an effluent of excellent quality with organic, surfactants and microbial parameters under the limits defined by Spanish legislation for urban water reuse. The disinfection of treated grey water is required to ensure compliance with microbial standards and to avoid the health risk in storage and application of recycled water.     

A comparative analysis of methods to represent uncertainty in estimating the cost of constructing wastewater treatment plants

Prediction of construction cost of wastewater treatment facilities could be influential for the economic feasibility of various levels of water pollution control programs. However, construction cost estimation is difficult to precisely evaluate in an uncertain environment and measured quantities are always burdened with different types of cost structures. Therefore, an understanding of the previous development of wastewater treatment plants and of the related construction cost structures of those facilities becomes essential for dealing with an effective regional water pollution control program. But deviations between the observed values and the estimated values are supposed to be due to measurement errors only in the conventional regression models. The inherent uncertainties of the underlying cost structure, where the human estimation is influential, are rarely explored. This paper is designed to recast a well-known problem of construction cost estimation for both domestic and industrial wastewater treatment plants via a comparative framework. Comparisons were made for three technologies of regression analyses, including the conventional least squares regression method, the fuzzy linear regression method, and the newly derived fuzzy goal regression method. The case study, incorporating a complete database with 48 domestic wastewater treatment plants and 29 industrial wastewater treatment plants being collected in Taiwan, implements such a cost estimation procedure in an uncertain environment. Given that the fuzzy structure in regression estimation may account for the inherent human complexity in cost estimation, the fuzzy goal regression method does exhibit more robust results in terms of some criteria. Moderate economy of scale exists in constructing both the domestic and industrial wastewater treatment plants. Findings indicate that the optimal size of a domestic wastewater treatment plant is approximately equivalent to 15,000 m3/day (CMD) and higher in Taiwan. Yet the optimal size of an industrial wastewater treatment plant could fall in between 6000 CMD and 20,000 CMD.     

High temperature membrane reactors for clean productions

The coupling of reaction and separation in the same device (membrane reactor) has been demonstrated to be an interesting way to enhance the performance of several reactions. In particular, by-products can be separated, side-reactions can be avoided and higher yields and conversions can be achieved. This means that the same conversions of traditional reactors can be obtained at more mild conditions (e.g. lower temperatures and pressures) with consequent energy saving and, thus, environmental benefits. Low temperatures are preferred also because they increase the life-time of the catalyst (it can be used for much longer time before it has to be regenerated) and reduce the tendency of both products and reactants to degrade (to avoid undesired side-reactions), which might lead to a loss of yield. Membrane reactors, then, seem to constitute a possible means for reducing waste production. In this paper the potential role of high temperature membrane reactors in clean productions is presented and discussed.     

Phenol degradation using combined effects of hydrodynamic cavitation and oxidant: Doehlert matrix

Hydrodynamic cavitation (HC)-based treatments have been proposed for the degradation of phenol as a toxic pollutant. The present work aimed to optimize the degradation of phenol using HC by means of Doehlert experimental design, which has not been previously addressed. Initially, operational parameters of hydraulic characteristics of the pump, inlet pressure, solution pH, and initial concentration were optimized; later, the effects of pH solution and H₂O₂ loading or initial pollutant concentration on phenol degradation were explored using the Doehlert experimental design. It was observed that phenol degradation is strongly dependent on the pH of the solution. Also, the acidic condition favors the formation of hydroxyl radicals and thus, the degradation of phenol. Based on the Doehlert matrix, the 94.1% phenol degradation and 68.60% total organic carbon (TOC) were obtained in 180 min at 304.5 mg/L of hydrogen peroxide at an initial concentration of 20 mg/L, 2.0 pH, and 90 psi inlet pressure, providing a cavitational yield of 6.33 × 10⁻⁶ mg/J and minimum treatment cost of US$/L 0.13. Overall, it has been observed that HC can be a promising route for the removal of pollutants (phenol) effectively using hydrogen peroxide as an additive.     

新型循环水处理系统的设计及应用

简介了软包装印刷工业复合生产过程中产生的VOCs污染物,探讨了现有ACF咐附回收有机溶剂设备存在的技术问题;结合软包装复合生产工艺特点,提出一种闭式循环的改良工艺,以解决能量浪费问题。     

基于常规处理的微污染水源水处理工艺改进措施简

我国大部分给水处理厂主要采用混凝-沉淀-过滤-消毒的常规处理工艺,该工艺对有机物、氨氮等去除效果有限,同时存在消毒副产物残留等问题。根据我国经济发展现状,分析了常规处理工艺的改进措施,包括对常规工艺进行强化,在常规处理工艺之前增加预吸附和预氧化,在常规处理工艺之后增加臭氧-生物活性炭吸附、膜处理等。这些措施在保留原处理工艺的基础上,通过调整操作条件或增加处理设施来改善出水水质,具有投资少、见效快的特点。     

Influence of support material on the immobilization of biomass for the degradation of linear alkylbenzene sulfonate in anaerobic reactors

Two horizontal-flow anaerobic immobilized biomass reactors (HAIB) were used to study the degradation of the LAS surfactant: one filled with charcoal (HAIB1) and the other with a mixed bed of expanded clay and polyurethane foam (HAIB2). The reactors were fed with synthetic substrate supplemented with 14 mg l(-1)of LAS, kept at 30+/-2 degrees C and operated with a hydraulic retention time (HRT) of 12h. The surfactant was quantified by HPLC. Spatial variation analyses were done to quantify organic matter and LAS consumption along the reactor length. The presence of the surfactant in the load did not affect the removal of organic matter (COD), which was close to 90% in both reactors for an influent COD of 550 mg l(-1). The results of a mass balance indicated that 28% of all LAS added to HAIB1 was removed by degradation. HAIB2 presented 27% degradation. Molecular biology techniques revealed microorganisms belonging the uncultured Holophaga sp., uncultured delta Proteobacterium, uncultured Verrucomicrobium sp., Bacteroides sp. and uncultured gamma Proteobacterium sp. The reactor with biomass immobilized on charcoal presented lower adsorption and a higher kinetic degradation coefficient. So, it was the most suitable support for LAS anaerobic treatment.     

Formulation,calibration, and validation of hybrid and coupled models for the design of upflow anaerobic filters in multiple separated stages for organic matter removal from sanitary landfill leachates

In this paper, the formulation, calibration, and validation of hybrid and coupled models for the design of upflow anaerobic filters in multiple separated stages were developed for organic matter removal from sanitary landfill leachates. Three novelties were presented, the type of reactor, design models, and kinetic coefficients. The upflow anaerobic filters were separated into two and three stages identified as UAF-2SS (DI-FAFS, in Spanish) and UAF-3SS (TRI-FAFS, in Spanish). The formulation, calibration, and validation of mathematical structures of hybrid models and five coupled models are proposed for each reactor. The hybrid models are based on the law of mass conservation, with the organic matter transformation component within the UAF-2SS and UAF-3SS reactors, being estimated from empirical equations that have been tested in aerobic culture reactors, adapted to the experimental factors, including among these, those under a non-stationary—advective conditions based on Velz's Law, Phelps's Law, and Monod's equation. The coupled models combine the components of the molecular transport by biosorption and molecular diffusion processes, with adaptations of the Stack's equation and Fick's Law, as well as transformation of organic substrates by biomass, whose kinetic coefficients contribute to explain the fraction, in which, the processes of mobility and biochemical transformation of the organic matter are occurring in the biomass within the bioreactors.     

臭氧消毒中水前后挥发性有机物的GC/MS分析研究

文章研究在不同消毒时间下,臭氧消毒中水前后挥发性有机物的变化。得出:消毒时间30 s和60 s后GC/MS检测有机物的种类较10 s时有明显增多,种类由10 s时的65种增到30 s时的98种,再增到60 s时的101种,最后到3 min时的135种。臭氧消毒法的快速、高效无二次污染、适用范围广。     

Integrated management of radioactive strontium contamination in aqueous stream systems

A combination of biomass treatment, fluidized bed/membrane reactor, and a minimum-suspension fluidized bed reactor is proposed to remove strontium cations from aqueous solutions, such as those generated by nuclear reactors. After conducting a series of screening tests, three adsorbents were selected for their suitability and high adsorptive capacity. The proposed combination uses Chlorella vulgaris in a packed column, followed by the fluidized bed/membrane reactor with bentonite powder in suspension. The membrane is primarily used to retain bentonite powder in the reactor. However, the same can be designed to remove additional amount of contaminant from the aqueous stream. The final separation is carried out in a fluidized bed containing resins that are suspended with minimal airflow. In laboratory scale, a flow rate of 600 ml/h was achieved for 30 min during which period the inlet concentration of 100 mg/l was reduced to 2.5 mg/l at the outlet. Bio-encapsulation with thermophilic bacteria and subsequent separation is proposed at this point in order to reduce the concentration to an even lower level. The proposed separation scheme offers an acceptable solution to removing strontium while minimizing the generation of secondary waste.     

油田采出系统中空化防垢技术室内研究

以大庆油田采出污水为母液,配置不同硅离子浓度的采出液,考察了起始硅离子浓度不同时油田采出液中的结垢因子经过空化防垢装置处理后的变化规律。结果表明:在经过空化防垢装置处理后,Ca2+、Mg2+浓度的下降得到一定的抑制;该装置对硅垢有一定的防垢作用,特别是对中、高浓度硅体系的防垢效果明显。     

饮用水消毒副产物控制工艺研究进展

通过对氯、二氧化氯、紫外线等常见消毒工艺以及去除已生成消毒副产物的深度处理工艺进行了分析,探讨了各种消毒工艺的消毒性能和对消毒副产物的控制效果以及各种深度处理工艺对消毒副产物的去除性能,为实际水处理中消毒以及深度处理工艺的选择提供了参考。     

DBO模式在污水处理行业的应用研究

DBO模式是PPP模式之一,在国家大力推进PPP模式之际,尝试开展DBO模式在污水处理行业的应用研究,分析污水处理行业发展趋势与问题,DBO模式在污水处理行业应用的适用领域与适用条件、优点,提出DBO模式在污水处理行业的推行路径,希望通过DBO模式解决污水处理行业的问题,促进行业健康发展。本文认为,城镇、乡镇与村庄生活污水处理、工业企业废水治理等领域具有项目设计与建设非标准化、项目需求明确、责任边界清晰、项目运营服务质量和成本容易监测等特点,应用DBO模式具有可行性。这些领域内的项目若有可靠的建设资金来源、稳定的运行费用保障机制、急于改善的区域水环境质量及严格的环保设施运行需求,适合采用DBO模式。DBO模式可以提高这些项目的建设质量和运营质量,节约成本,缩短建设周期,提高抗风险能力。同时,在行业层面,能够解决这些领域面临的项目设计不合理、建设质量不高、运行费用高、运行管理不善、闲置等诸多问题,可以促进先进实用技术和管理经验的应用,提高行业技术和运营管理水平的整体进步。因此,建议政府从开展实施试点、制定行业规范、加大宣传和推广、颁布政策文件等方面大力推进DBO模式在污水处理行业的应用。