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41.
采用HZ-16型大孔树脂对含三(三溴苯氧基)三嗪(RDT-8)废水进行吸附及脱附处理。实验结果表明:在废水流量为4.0 BV/h的条件下,树脂最佳吸附工艺条件为出水体积88.0 BV,此条件下出水COD小于291 mg/L,挥发酚质量浓度小于0.08 mg/L;在脱附液流量为0.5 BV/h的条件下,树脂最佳脱附工艺条件为脱附液体积3.0 BV,此条件下脱附液中挥发酚质量浓度为30.6 mg/L,挥发酚脱附率高达76.4%。在最佳吸附-脱附工艺条件下,连续进行10次动态吸附-脱附实验,吸附出水中COD为137~294 mg/L,COD去除率为72.5%~89.1%,挥发酚质量浓度稳定在0.05 mg/L以下,挥发酚去除率为99.8%~100%,说明HZ-16型大孔树脂的吸附-脱附性能稳定。 相似文献
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Patrick A. Mower J. Philip J. O'Kane Jerry D.F. Sherrif Tim Wyatt J. David Barrett 《Journal of the American Water Resources Association》1971,7(4):831-843
ABSTRACT .Operating rule procedures are developed for the optimal use of desalination in conjunction with surface water impoundments. Results obtained from the use of hill-climbing and dynamic programming methods are compared. Benefits to be obtained from the integrated use of desalination are demonstrated through a case study for the Barcelona area of Spain. 相似文献
45.
Irving Spiewak 《Journal of the American Water Resources Association》1971,7(4):844-855
ABSTRACT The selection of an evaporator design must reflect the balancing of captial cost (primarily in heat exchanger surface and vessels) against operating cost (primarily steam cost) to achieve minimum cost. In a conjunctive plant the tendency is to select a low-capital cost, high-operating cost plant. In addition, it is advantageous to use a high-capacity plant which needs to be operated much less of the time than a plant which is sized just at the needed rate. For example, in the study of a possible system to satisfy a future increase of 450 MGD in water supply to New York Qty, a plant of 750 MGD capacity was selected as optimum. This plant, of the advanced VTE-MSF process type, would have a performance ratio of 9 lb product/1000 Btu as compared to 10-13 normally used for base-loaded plants. Steam would be supplied by a multi-unit dual-purpose nuclear power plant. The most economical type of energy supply would be “interruptible”; the steam would be used by a low pressure turbine to generate electricity during periods of peak electrical demand but would be available to the desalting plant at other times. The low pressure turbine would be available as spinning reserve during desalting plant operation. It is estimated that the desalting plant would have a load factor of 27 per cent over its life. 相似文献
46.
Gideon Fishelson 《Journal of the American Water Resources Association》1973,9(4):801-815
The study contains the methodology of finding the optimal time to start the operation of a desalting plant or any other non conventional source of water for agricultural use in Israel. The essence of the methodology is the moving equilibrium price and quantity of agricultural products. The market of agricultural products is represented by a single demand curve and a supply curve which is derived from the agricultural sector production function. Both the demand for and the supply of agricultural products functions are shifting over time. The marginal value product of water is the critical value that determines the optimal time of a desalting plant. The study is static in the sense that dynamic aspects per se are not dealt with-e.g. learning by doing of building and operating desalting plants. The empirical results although used for illustrative purposes can be used as reference points for other detailed and more ‘exact’ studies on water desalination. 相似文献
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O. Phillips Agboola U. Atikol Hossein Assefi 《International Journal of Green Energy》2015,12(2):139-147
The present study assesses the feasibility of exploiting single- and double-basin solar stills in our daily lives. An investigation is carried out to determine the thermal performance and economic viability of making use of solar stills in water desalination. The climatic conditions of Tehran (35°44?N, 51°30?E) are considered to assess the feasibility of the basins. Transient energy and mass balance equations are utilized for modeling the thermal performance. The equations are solved by using fourth-order Runge–Kutta method in FORTRAN. The daily productivities of single- and double-basin solar stills are found to be 5.22 kg/m2 and 7.73 kg/m2, respectively, while the effect of different water masses (20–100 kg) on the productivity of each system was found to be optimum at 20 kg/m2. The results are compared with experimental work performed under different climatic conditions to examine the validity of the feasibility of basins in general. A life cycle cost analysis performed for Tehran, yields that single- and double-basin solar stills have savings-to-investment ratios of 4.2 and 4.8, respectively, indicating that they are economically feasible. 相似文献
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以江苏某印染废水处理厂反渗透(RO)浓水为研究对象,采用多种分析手段分析了RO浓水的水质特征.首先采用IC和ICP-MS对水中的无机离子进行了定性和定量分析,采用GC-MS对废水中的半挥发性有机物进行定性和定量分析.结果表明,RO浓水中无机离子以Na+、Cl-和SO42-为主,半挥发性有机物邻苯二甲酸二(2-乙基己)酯(DEHP)为主要成分,其浓度为1.452mg/L.为分析RO浓水中的溶解性有机物(DOM)特征,进一步采用超滤膜分子量分级法和树脂亲疏水分离技术对废水中的DOM进行分离解析,分析了不同组分的溶解性有机碳(DOC)、UV254、SUVA含量和分布情况,应用三维荧光光谱对各组分物质进行了定性分析.超滤分级表明,RO浓水中相对分子量<1k的有机物占56.98%,相对分子质量5~10k有机物仅占2.19%,但其芳香化程度较高.树脂分离结果表明,RO浓水中亲水性物质(HPI*)、疏水性物质(HPO*)和过渡性物质(TPI*)的DOC含量差异不大,其中HPO*的芳香构造化程度最高,含有较多的色氨酸类芳香族蛋白质,而HPI*中含有较多的溶解性微生物代谢产物类物质. 相似文献