利用活化粉煤灰处理造纸废水的研究

通过正交试验,对粉煤灰处理造纸废水的影响因素进行了研究。研究结果表明：对粉煤灰进行活化,能增加其对造纸废水COD的去除效果;最佳的试验设计方案为：粉煤灰经40％硫酸活化、粒度160—200目、投加量为30g／100ml;影响COD去除率的大小顺序为：投加量影响最大,粒度次之,活化方式影响最小。     

麦秸制浆造纸废水深度处理中试研究

采用催化氧化—絮凝—沉淀工艺深度处理麦秸制浆造纸废水,处理规模为200 m3/d.在进水COD为150 ～ 263 mg/L、色度为64～128倍、SS为50～ 88 mg/L的水质情况下,处理后出水水质稳定,COD为38～ 52mg/L,色度为2～8倍,SS为12～23 mg/L,出水水质达到GB3544-2008《制浆造纸工业水污染物排放标准》的要求.采用该工艺深度处理麦秸制浆造纸废水的费用不超过0.55元/m3.     

交流变频磁化聚合硫酸铁混凝处理造纸废水

采用交流变频磁场预处理聚合硫酸铁(PFS),用于混凝处理造纸废水。考察了有无磁化作用、PFS加入量、磁化强度、磁化频率、磁化时间等因素对造纸废水的COD去除率和色度去除率的影响。实验结果表明:磁化PFS对造纸废水的处理效果较未磁化时明显提高;在PFS加入量为1 000 mg/L、磁化强度为6 mT、磁化频率为90 Hz、磁化时间为3 min的条件下,处理初始COD为650 mg/L、初始色度为180倍的造纸废水,COD去除率为93.22%,色度去除率为88.89%。     

用白泥和赤泥制备烟气脱硫剂

以碱厂白泥和钢厂赤泥为主要原料,研究了制备复合金属氧化物成型烟气脱硫剂的工艺;考察了m（白泥）：m（赤泥）、白泥和赤泥平均粒径、黏结剂、造孔剂对脱硫剂活性的影响。脱硫剂最佳制备工艺条件为m（白泥）：m（赤泥）=2：1,白泥和赤泥粒径越小越好,黏结剂为Na,造孔剂为Zb,加水混匀,挤条成型,烘干后高温焙烧制得;脱硫剂的最高脱硫率为99．83％,脱硫剂脱硫12．30h后穿透硫容为15．20％。     

晶析辅助化学沉淀法处理高含磷废水

在常温条件下,将价格低廉的氯化镁、碳酸氢铵加入到高浓度含磷废水中,不仅有较高的除磷率,且可兼得缓效复合肥MgNH4PO4·6H2O。为了使一次处理液能达标排放,以MgNH4PO4·6H2O作为晶种,采用晶析辅助化学沉淀法进一步除磷。在一次处理液放置时间为2.7h、水力停留时间维持0.1h左右的条件下,处理后的废水可达到Ⅱ类水排放标准(磷质量浓度不超过2.0mg/L)。     

粉煤灰,聚合硫酸铁处理瓦楞纸生产废水的研究

本文介绍了以粉煤灰、聚合硫酸铁为水处理剂，处理瓦楞纸生产废水的试验研究。结果表明；该方法成本低，操作简便，处理效果好，废水可全部回用。     

脱硫增效剂与白泥在湿式FGD系统中的应用分析

介绍了脱硫增效剂和纯碱厂生产的废渣白泥在石灰石-石膏湿法脱硫系统中的应用,以已经实施投加增效剂和使用白泥为脱硫剂的电厂案例为基础进行技术经济分析与比较,对工艺改造方案选择给出了建议。     

T酸一次洗水初步处理的研究

采用重氮化－偶合－混凝沉淀和重氮化－混凝沉淀两种方法对Ｔ酸一次洗水的初步处理进步了研究。Ｔ酸一次洗水经两种方法处理后,ＣＯＤ去除率分别为６１．３％、５０．５％,色度去除率分别为７４．６％、７１％。     

铁屑／炭电化学反应—混凝沉淀法处理制罐废水

研究了用铁屑／炭电化学反应－混凝沉淀法处理铝质量易拉罐生产废水的流程和工艺条件。废水经铸铁屑／焦炭反应柱处理后再经混凝沉淀处理,ＣＯＤｃｒ去除率可达９０％以上。     

超临界水氧化法处理造纸黑液

采用自制的超临界水氧化反应装置,对造纸工业排放的黑液进行处理。考察了反应温度、反应压力、反应时间、过氧量(初始反应时所加氧气的量与废水完全氧化所需氧气的理论量的比,%)等对黑液中COD去除率的影响。实验结果表明,处理黑液的最佳反应条件为:反应温度500℃,压力26M Pa,过氧量500%,反应时间120s。在此最佳条件下处理COD为85 000m g/L的造纸黑液,COD去除率可达99.9%。     

Environmental assessment of supercritical water oxidation and other sewage sludge handling options.

Sustainable development relies on the eco-efficient use of all flows in society; more value created out of each resource unit. Supercritical water oxidation (SCWO) can be used for treatment of wet organic waste. The technology has been under development for over 20 years but has not yet been fully commercialized. SCWO allows for complete oxidation of all organics in sewage sludge and almost complete recovery of the inherent energy, essentially without harmful emissions. In this paper, a life-cycle assessment (LCA) of sewage sludge SCWO (Aqua-Critox) is presented and the results are compared with LCA results for other sludge handling options: agricultural use, co-incineration with municipal solid waste, incineration with subsequent phosphorus extraction (Bio-Con) and sludge fractionation with phosphorus recovery (Cambi-KREPRO). For SCWO, beneficial utilization of the heat of reaction is of crucial importance for the outcome. The electricity consumed by pumping and the nitrous oxide produced are other important parameters. The best sludge handling option from an environmental point of view depends on what aspect is considered more important in the impact assessment. Regarding global warming, the energy recovery methods perform better than agricultural use.     

Utilization of solar energy in sewage sludge composting: Fertilizer effect and application

Three reactors, ordinary, greenhouse, and solar, were constructed and tested to compare their impacts on the composting of municipal sewage sludge. Greenhouse and solar reactors were designed to evaluate the use of solar energy in sludge composting, including their effects on temperature and compost quality. After 40 days of composting, it was found that the solar reactor could provide more stable heat for the composting process. The average temperature of the solar reactor was higher than that of the other two systems, and only the solar reactor could maintain the temperature above 55 °C for more than 3 days. Composting with the solar reactor resulted in 31.3% decrease in the total organic carbon, increased the germination index to 91%, decreased the total nitrogen loss, and produced a good effect on pot experiments.     

Mercury emission from sewage sludge incineration in Japan

Sewage sludge contains trace amounts of mercury, and sewage sludge incineration is a major source of mercury emissions. However, relatively few studies have reported on mercury emissions from sewage sludge incineration. Consequently, data on emissions from sewage sludge incinerators must be updated to estimate current emissions of mercury. In this study, we examined mercury emissions and speciation using continuous mercury analyzers in two incinerators. The mercury concentrations in stack gas from facilities A and B were 36.6 and 21.1???g/Nm³, respectively. As a result, the emission rate was calculated to be 0.282?C0.750?g/ton-dry sludge. Considering the total amount of sewage sludge incinerated in Japan, the mercury emissions from sewage sludge incinerators were estimated to be 0.49?C1.31?tons/year.     

Behavior of PAHs from sewage sludge incinerators in Korea

Although production of sewage sludge increases every year, its proper treatment has only been recently raised as a new issue, as current landfill and ocean dumping arrangements are expected to become increasingly difficult to manage in the future. The Korean Ministry of Environment plans to diversify its processing facilities and expand its processing systems by 2011, with the purpose of processing all sludge produced in Korea. According to this plan, incineration (including incineration of municipal wastes) will process 30% of the entire sewage sludge throughout the country in 2011. This study reviews the characteristics of PAH, which is one of the organic substances found in sewage sludge during the incinerating process. The total amount of PAH produced from sewage sludge incineration was found to be 6.103 mg/kg on average, and investigation performed on 16 PAHs of inlets and outlets of the air control devices at five full-scale incineration facilities showed that concentrations of the PAHs on the inlet and on the outlet ranged from 3.926 to 925.748 microg/m(3) and from 1.153 to 189.449 microg/m(3), respectively. In the case of the incineration facility fed with municipal waste (95%) and sewage sludge (5%), the total of the PAH emissions concentration was higher than that found at the incineration facilities used exclusively to treat sewage. The combustion of waste vinyl and plastics contained in municipal waste fed into the facility might contribute to the high levels of PAHs in the stack gas. However more investigation is needed on the production mechanism of PAHs at different operating conditions of the incineration facilities, such as the types of waste, and other relevant factors.     

Characteristic of heavy metals in biochar derived from sewage sludge

This study investigates the characteristic of heavy metals (Pb, Zn, Cu, Cd, Cr, Ni and As) in biochar derived from sewage sludge at different pyrolysis temperatures (300, 400, 500, 600 and 700 °C). The heavy metal concentrations, chemical speciation distribution, leaching toxicity, and bio-available contents were investigated using ICP-OES after microwave digestion, a sequential extraction procedure recommended by the Community Bureau of Reference (BCR), an improved nitric acid–sulphuric acid method, and diethylenetriamine pentaacetic acid (DTPA) extraction method, respectively. The results showed that a great percentage of the heavy metals remained in biochar, the concentrations of heavy metals in biochar (except Cd in B7) were higher than that in sludge, and the enrichment of the heavy metals in biochar enhanced with the pyrolysis temperature. Although the effect of pyrolysis temperature on the chemical speciation distribution, the leaching toxicity and the bio-available contents of heavy metals in biochar was inconsistent, the potential risk of biochar on soil and groundwater contamination was lower than sewage sludge.     

Utilization of river sediment,sewage sludge and wheat straw as the primary raw material in sintered-shale bricks

Journal of Material Cycles and Waste Management - China produces large amounts of sewage sludge and agricultural waste every year. In line with the concepts of economic and environmental...     

Recovery of biomass cellulose from waste sewage sludge

In our previous work, the primary sludge from wastewater treatment plants was shown to contain a considerable amount of cellulose (about 20%, based on suspended solids) owing to the discharge of toilet paper. For the purpose of using the cellulose as a biomass resource, this study examined a simple method for its recovery. When fibrous cellulose was suspended in 0.3% sulfuric acid and autoclaved at 130°C for 60 min, 85%–88% of the initial solids remained without dissolving. Under these conditions, an activated sludge sample not containing cellulose was strongly hydrolyzed and only 7% of the initial solids remained. The prescribed amounts of cellulose added to the activated sludge sample were quantitatively recovered by the autoclaving treatment. In the treatment of primary sludge containing >20% cellulose, residual solids with relatively high levels of cellulose (>69%) could be obtained. The results indicate that the method proposed here could recover cellulose practically from waste sewage sludge for biomass utilization. Received: July 17, 2000 / Accepted: July 4, 2001     

Acidic bioleaching of heavy metals from sewage sludge

The overall objective of this study was to evaluate the use of controlled bio-acidification prior to land application as a decontamination process to remove heavy metals from sludge. The sulfur-oxidizing bacteria were naturally available in the sludge samples and were activated by providing sulfur and aeration at 28°C–30°C. Activation resulted in bio-acidification to pH 2 within 5–11 days. Successive inoculation of fresh sludges with 5% acidified samples reduced the acidification time to 2–3 days in most samples. Bio-acidification resulted in dissolving significant quantities of heavy metals from all sludge types tested. The maximum solubilization results were: 86%–97% for Ni; 48%–98% for Pb; 26%–71% for Cr; 18%–91% for Zn; 16%–90% for Cu; 7%–60% for Cd. Limited metal solubilization results were observed in the various control samples that accompanied the bio-acidified samples. The leaching results in the control samples were limited to 2%–19% for Ni, 0%–7% for Pb, 0%–5% for Cr, 0.3%–4% for Zn, 0.2%–4% for Cu and 0%–3% for Cd. The results confirmed that Ni and Pb were the easiest metals to dissolve from the various sludge types. On the other hand, the lowest solubilization results were observed for Cu and Cd, and moderate solubilization results were achieved for Cr. The bio-acidification process resulted in moderate gains in terms of improving the suitability of tested sludges for land application. Received: April 19, 1999 / Accepted: November 4, 1999     

油田污油池VOCs源强核算

以油田两处污油池为研究对象开展VOCs浓度监测,结合社会科学统计软件包（Statistical Package for the Social Science,SPSS）的Pearson相关分析对监测数据进行了分析;并利用地面浓度反推法核算污油池的VOCs排放源强,将结果与排放系数法计算值进行对比;最后对下风向不同距离采样线监测数据反推源强逐渐减小的原因进行了讨论。结果表明：污油池B各采样线监测数据间的相关性好,反推出的源强较为准确,VOCs年排放量为17.6 t/a;而污油池A监测数据间的相关性不佳,可能是由于其他无组织排放源相距较近影响所致,不适合直接应用地面浓度反推法计算其源强,需要结合其他排放源的情况进行修正。