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WASTEWATER TREATMENT, ENERGY PRODUCTION, AND ENERGY CONSERVATION IN AN ALGAL-BACTERIAL SYSTEM.

机译:藻类细菌系统中的废水处理,能源生产和节能。

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摘要

Quantitative data on the operation of an integrated photosynthetic wastewater treatment system are presented. The system was designed to treat wastewater concurrent with the production of microalgae biomass from waste nutrients and the conversion of that biomass to fuel. The proposed system involves retention of nutrients within the system to increase the biomass production potential of a given rate of nutrient inflow. The components investigated in this study were the algae growth ponds, harvesting ponds, anaerobic digesters, and algae regrowth on effluents from the anaerobic digesters.;Two 32 m('3) settling ponds were operated for the same 16-month period. The ponds were operated on a fill and draw basis to recover biomass from the growth pond effluents. The settling data collected in these ponds were augmented by 24-hour settling tests in Imhoff cones in the laboratory and by settling rate measurements in plastic cylinders in the laboratory. With some exceptions, suspended solids removals of 70 to 85% were achieved by 24-hour settling in Imhoff cones. The removal efficiency in the large settling ponds was consistently less than in the Imhoff cones. Mean settling rates were typically 10 to 30 cm/hr, but rates from 0 to 74 cm/hr were observed on isolated occasions. The dissolved BOD concentration in the settling pond effluent was generaly less than 10 mg/l. Total BOD was roughly proportional to suspended solids concentration.;The algal-bacterial solids recovered in the settling ponds were subjected to anaerobic digestion in bench scale (16 L) digesters to determine methane yield and volatile solids destruction under various conditions of temperature, feed solids concentration, and hydraulic detention time. The specific gas production obtained from the fresh algal-bacterial sludge was found to be 0.39 liters of total gas/gram of volatile matter added. At 30 days detention time a 17% reduction in gas production was observed at 25(DEGREES)C compared to 35(DEGREES)C. . . . (Author's abstract exceeds stipulated maximum length. Discontinued here with permission of school.) UMI;Two 1080 m('2) high rate algae growth ponds were operated for 16 months at detention times of 2.0 to 8.0 days and depths of 20 to 50 cm. BOD loadings ranged from 25 to 350 kg/HA-day. The growth medium was settled municipal wastewater. The biomass production in the most productive pond averaged 38.33 g/m('2)-day during the most productive 30-day period. The measured volatile solids production in that pond was 79.3 metric tons during one calendar year (Jan. to Jan.). Peak productivity was found to be limited by the availability of carbon, even in heavily loaded ponds.
机译:介绍了有关光合废水综合处理系统运行的定量数据。该系统旨在处理废水,同时利用废养分生产微藻生物质并将该生物质转化为燃料。拟议的系统涉及将营养物保留在系统中,以在给定的营养物流入速率下增加生物质的生产潜力。在这项研究中调查的组件是藻类生长池,收获池,厌氧消化池以及厌氧消化池废水中的藻类再生长。;两个32 m('3)沉降池在相同的16个月内运行。池塘在充填和抽取的基础上进行操作,以从生长池塘的废水中回收生物量。在这些池塘中收集的沉降数据通过在实验室的Imhoff锥盆中进行24小时沉降测试以及在实验室中的塑料瓶中进行沉降速率测量得到了增强。除某些例外,通过在Imhoff锥体中进行24小时沉降,可以去除70%到85%的悬浮固体。大型沉降池的去除效率始终低于Imhoff锥。平均沉降速度通常为10至30 cm / hr,但在个别情况下观察到的沉降速度为0至74 cm / hr。沉淀池废水中溶解的BOD浓度通常小于10 mg / l。总BOD大致与悬浮固体浓度成正比;在沉降池中回收的藻类细菌固体在台式规模(16 L)消化池中进行厌氧消化,以确定甲烷产量和在各种温度,进料固体条件下的挥发性固体破坏浓度和水力滞留时间。从新鲜的藻类细菌污泥获得的比气产量为0.39升总气体/每克添加的挥发性物质。在滞留时间30天,观察到25(摄氏)C的产气量比35(摄氏)C减少了17%。 。 。 。 (作者的摘要超出了规定的最大长度。在学校允许的情况下在此停产。)UMI;两个1080 m('2)高速藻类生长池在20到8.0天的拘留时间和20到50厘米的深度下操作了16个月。每天的BOD装载量为25至350 kg / HA。生长培养基是沉降的城市废水。在生产力最高的30天期间,生产力最高的池塘中生物量的平均产量为38.33 g / m('2)天。在一个日历年(1月至1月),该池塘中测得的挥发性固体产量为79.3公吨。发现即使在重负荷的池塘中,最高生产力也受到碳供应的限制。

著录项

  • 作者

    EISENBERG, DON MAURY.;

  • 作者单位

    University of California, Berkeley.;

  • 授予单位 University of California, Berkeley.;
  • 学科 Engineering Sanitary and Municipal.
  • 学位 Ph.D.
  • 年度 1981
  • 页码 307 p.
  • 总页数 307
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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