采用絮凝—接触氧化法处理酿酒行业废水

采用絮凝-接触氧化法处理酿酒行业废水，原废水CODcr浓度为1627-2334mg/L，SS浓度为2095-2301mg/L，BOD5浓度为981-1005mg/L，色度为80-110倍，用絮凝-接触氧化法处理后，CODer浓度为280-295mg/L，SS浓度为178-199mg/L,CODcr浓度为145-150mg/L，色度为20-25倍，CODcr平均去除率为85%。悬浮物平均去除率为91%，BOD5平均去除率为85%，色度平均去除率为77%，各项指标符合国家排废标准。     

Ca(OH)_2絮凝沉淀-臭氧氧化垃圾渗滤液生化出水提高反渗透性能

为了提高生化出水的反渗透性能,本文提出采用Ca(OH)_2絮凝沉淀预处理生化出水,再经O_3氧化后,用于反渗透膜的深度处理工艺.研究表明,Ca(OH)_2絮凝沉淀可以有效地去除垃圾渗滤液生化出水中的大分子有机物及Ca~(2+)、Mg~(2+)离子.当废水絮凝沉淀出水的电导率最低时,废水中的Ca~(2+)和Mg~(2+)离子浓度降到最低,同时也去除了较大比例的COD.对电导率最低条件下的Ca(OH)_2絮凝沉淀出水再经O_3处理后,废水中的Ca~(2+)和Mg~(2+)离子浓度和COD进一步降低,其反渗透膜通量比MBR出水的通量增高25%—35%,膜污染明显减轻,可延长膜清洗周期.臭氧氧化Ca(OH)_2絮凝沉淀出水涉及到臭氧分子直接氧化和氢氧根催化臭氧氧化两种机理,但前者起主导作用.臭氧氧化处理进一步降低了废水中的COD和Ca~(2+)、Mg~(2+)离子浓度,是提高反渗透膜通量的主要原因.     

受酸性矿山废水影响河流悬浮物中重金属污染特征分析与生态风险评价

受酸性矿山废水影响河流水体与沉积物中重金属污染及评价的研究已有大量报道,而缺乏对这类水体悬浮物重金属污染研究.选择受广东大宝山采矿废水影响的横石河为研究对象,研究该河流悬浮物中6种重金属元素(Mn、Cu、Zn、As、Cd和Pb)的浓度空间分布,采用地累积指数法和潜在生态危害指数法评价重金属生态风险,结合悬浮物组分SEM/XRD表征来进一步解析污染特征及迁移转化机理.结果表明,横石河悬浮物重金属污染严重,主要来源于大宝山采矿废水,Mn、Cu、Zn、As、Cd、Pb起始浓度分别高达1470、101.6、12169、174.9、412.2、873.7 mg·kg~(-1),且重金属浓度沿程呈逐渐降低趋势,与悬浮物含量呈显著正相关;悬浮物中重金属污染处于极强风险等级,单个元素Cd严重污染频率为83.33%,对RI贡献平均超90%,各元素潜在风险大小为:CdZnAsPbCuMn;横石河悬浮物初始矿物成分以施氏矿物为主,随着河流的迁移,其逐渐向更为稳定的针铁矿和水铁矿转化,这种矿物组成及转化决定了重金属的分布特征.     

絮凝-光催化处理实际染料废水的研究

采用絮凝-光催化氧化工艺成功地处理了实际染料废水;研究了COD光催化降解动力学。COD和BOD5浓度分别为2169mg／L、295mg／L的染料废水,经絮凝-光催化处理后,出水COD和BOD5分别为214mg／L、18．5mg／L,去除率分别为90．1％、93．7％。向光催化体系中加入H2O2,可促进COD与BOD5的去除。该工艺可处理高浓度染料废水。     

铝铁改性淀粉复合絮凝剂对甲基紫的絮凝机理

以模拟甲基紫染料废水为处理对象,通过测定絮凝R值、Zeta电位、脱色率与CODCr去除率,研究了自配铝铁改性淀粉复合絮凝剂(CAFS)的絮凝特性,初步探讨了其絮凝机理.结果表明,该复合絮凝剂为阳离子型高分子絮凝剂,絮凝初期作用机理趋于"吸附电中和",絮凝后期作用机理以"絮凝架桥"和"卷扫网捕"为主,絮凝性能受pH值影响显著.在pH=11.0,投加量为0.330 mg·L-1时,甲基紫处理效果最优,CODCr去除率达41.0%,色度去除率高达98.0%,其絮体形态密实、含水率低.     

一锅法溶液缩聚制备高效阳离子絮凝剂及其絮凝性能

以丙酮、二甲胺和甲醛为原料,采用一锅法溶液缩聚制备了一种新型阳离子高分子絮凝剂CPF.通过红外、核磁共振氢谱、凝胶渗透色谱和元素分析对CPF的分子结构进行了表征,通过絮凝实验研究了CPF对水中阴离子染料的絮凝脱色效果并探讨了絮凝机理.研究表明,CPF重均分子量为1.81×10~4,拥有胺基、醇羟基、羰基和醚键等极性官能团,大量质子化胺基赋予其很高的阳离子度.CPF对酸性、直接和活性阴离子染料的絮凝脱色率均达95%以上,脱色率随溶液pH降低而升高且不受水中无机盐的影响.该絮凝行为是"吸附电中和"与"吸附架桥"效应共同作用的结果.CPF对实际印染废水同样具有良好的絮凝脱色效果,但对组分复杂的混合印染废水化学需氧量(COD)的去除率较低,因此可作为一种高效的物化处理手段与生化处理配合用于印染废水的工业化处理.     

壳聚糖/膨润土复合絮凝剂处理染料废水的研究

利用壳聚糖/钠基膨润土复合絮凝剂对活性艳红X3B等11种染料模拟废水及实际印染废水进行絮凝脱色处理。考察了复合絮凝剂投加量、pH值、搅拌速率、搅拌时间等因素对模拟染料废水絮凝脱色的影响。结果表明,在染料浓度为100 mg.L-1,pH为5的条件下,复合絮凝剂投加量为1.25 g.L-1时,3种质量比的复合絮凝剂对活性艳红X3B的脱色率分别达到75%、90%和97%以上;质量比为1∶10的壳聚糖/钠基膨润土复合絮凝剂,对其它活性、还原性、分散性、水溶性等8种印染厂常用染料也具有很好的絮凝脱色作用,脱色率均可达94%以上。对印染废水处理厂进水口废水和经过A/O处理后废水的色度去除率和COD去除率分别可以达到81.05%、83.74%和53.21%、41.22%,具有一定的应用前景。     

微生物絮凝剂产生菌的筛选及相关废水絮凝效果试验

用常规的细菌分高纯化方法从废水、土壤、活性污泥中分离出42株细菌，将单株菌培养于特殊的产絮凝剂液体培养基中，培养物离心后上液对高岭土县液絮凝效果作为指标衡量其絮凝活性及产絮凝剂能力，由此初步获得6株微生物絮凝剂产生菌：Ⅰ－23，Ⅰ－24，Ⅱ－4，Ⅲ－2，Ⅲ－8，Ⅲ-12．其发酵离心上液对造纸黑液、皮革废水、偶氮染料废水、硫化染料废水、电镀废水、彩印制板废水、石油化工废水、造币废水及蓝墨水、碳素墨水等进行的絮凝试验表明，废水固液分离效果良好，CODCr去除率55％～98％，悬浮物、色度、浊度去除率90％以上．     

阳离子聚电解质强化絮凝去除活性染料的研究

选用三种活性染料分别配成模拟染料废水,用阳离子聚电解质(PDADMAC)强化絮凝去除活性染料.结果表明,PDADMAC去除活性染料的机理为聚电解质络合絮凝.PDADMAC的阳离子度高,分子量低,疏水性大,脱色去除效果较好.而且,活性染料的脱色去除率随活性染料色度的深浅而不同,表现为活性黑K-BG＞活性艳红K-2BP＞活性嫩黄K-6G.     

论造纸中段废水和废纸造纸废水的处理原则

从造纸中段废水絮凝法处理和生化处理效果的实验研究结果出发,讨论了造纸中段废水处理的技术路线,指出絮凝法与好氧生化法联用是该废水处理的适宜方法。根据废纸造纸产生的两股废水（打浆洗涤废水和抄纸废水）的污染物特性,提出了废纸造纸废水处理的５条设计原则。     

Suspended solid abatement in a conical fluidized bed flocculator

With the random movement of silica gel beads in a conical fluidized bed, micro-vortices resulting from the fluidization promoted the collision and aggregation of suspended fine kaolin powders. The abatement efficiencies of the suspended fine solids under several hydrodynamic conditions were studied, and a suitable control strategy for operating the conical fluidized bed flocculators was identified. The suspended solids abatement efficiency was found to increase with increasing Camp Number and flocculation time (T), but decreased with the increase of velocity gradient (G) within the range studied in this research (165.1–189.6 s^-1). The abatement efficiencies were all more than 60% at the range of G = 165–180 s^-1 and T = 15–33 s at an initial kaolin solid concentration of 150 mg·L^-1, polymer aluminum chloride dosage of 60 mg·L^-1 and sedimentation time of 20 min. However, the formation of flocs was influenced by the liquid backmixing. Excessive backmixing caused the breakup of flocs and resulted in difficulty for the fine powders to aggregate and sediment to the reactor bottom. The results of the calculated fractal dimension and measured free sedimentation velocity of flocs obtained at different runs showed similar flocs properties, and indicated an easy control strategy for sedimentation of the flocs.     

高效絮凝反应器处理生活污水试验研究

本文采用高效絮凝模拟反应器进一步对实际生活污水进行连续运行处理试验，结果表明，直接絮凝沉淀处理后的出水浊度去除率和ＣＯＤ去除率分别达到９３．４％和７９．２％，可完全达到排放标准。絮凝处理后再经纤维过滤柱过滤处理，可控制出水浊度在１．０ＮＴＵ以下，ＣＯＤ去除率增加５．０￣７．０％，试验结果进一步验证了这种高效絮凝装置具有高效处理效能及实际工程应用推广价值。     

垃圾填埋场渗滤液中NH3-N的处理

阐述垃圾渗滤液的产生及危害,重点介绍现有垃圾渗滤液中高浓度NH3-N处理的现状及发展方向.垃圾填埋场渗滤液是一种成分复杂的废水,目前还没有特别有效的治理办法,传统的生化处理办法虽然常常用来处理渗滤液,但是由于渗滤液中含有高浓度NH3-N,其处理效果不及城市污水的处理.     

悬浮填料生物膜工艺的研究进展

悬浮填料生物膜工艺又称为移动床生物膜反应器工艺，是上世纪90年代初迅猛发展起来的一种新型水处理工艺．它既可以作为独立的生物处理系统，也能够与活性污泥法组合以增加后者的处理效能，还可以作为中高浓度工业废水的生物预处理手段．本文总结了悬浮填料生物膜工艺的流体力学、生化动力学规律、悬浮填料的开发现状，探讨了此工艺在市政生活污水、工业废水、低污染物浓度的水处理领域的研究和应用进展．进一步开发高效、廉价的功能型悬浮填料，提高填料的有效比表面积，优化与确定工艺和运行参数，将推动悬浮填料生物膜工艺在我国的全面应用．图3表1参64     

Verhalten von Nanosilber in Kläranlagen und dessen Einfluss auf die Nitrifikationsleistung in Belebtschlamm

Background, aim and scope The application of nanosilver is increasing. Knowledge on the fate and behavior of nanosilver in wastewater and wastewater treatment plants is scarce. Studies under real world conditions are completely lacking. We studied (1) the impact of nanosilver on the nitrification of sewage sludge, (2) quantified the mass flow of nanosilver in a pilot-plant, and (3) verified the mass balance in a full-scale municipal wastewater treatment plant where nanosilver is introduced to the municipal plant by an indirect discharger. Materials and Methods The addition of four different nanosilver additives on ammonia oxidation in activated sludge has been studied in batch-reactors at two concentrations (1, 100?mg/L Ag) with two exposure times (2?h, 6?days). The pilot-plant treating 70 population equivalents of domestic wastewater is operated with a 12?day sludge age. Nanosilver was applied to the activated sludge tank within two sludge ages. The silver concentrations were measured in sludge and effluent samples during dosing and the following two sludge ages. The adsorption and speciation of silver particles has been analyzed using scanning electron microscopy (SEM) coupled with energy dispersive X-ray spectroscopy (EDX). Influent, effluent and sludge were sampled on a full-scale plant (60?000 equivalent inhabitants) and analyzed for silver. Results Silver nitrate, metallic nanosilver, nano-scaled silver chloride and microcomposite silver did not show any effect on ammonia oxidation after the addition of 1?mg/L Ag to the activated sludge (corresponding to 250?mg Ag per kg solids). In contrast, 100?mg/L Ag inhibited the nitrification process by 100?% after the addition of silver nitrate and 20–30?% after addition of colloidal polymer-coated nanosilver. A complete mass balance of the pilot-plant, a steady-state system with known fluxes, demonstrates significant enrichment of silver in the sewage sludge (96?%) after the addition of silver chloride to the plant and small losses of silver into the secondary effluent (4?%). The mass fluxes are similar to metallic colloidal nanosilver investigated under the same conditions. The mass balance has been consistently confirmed by the full-scale study in a municipal wastewater treatment plant. The silver fluxes correspond to the fluxes of the suspended solids in sludge and effluent. Overall, it is estimated that from public wastewater treatment plants about 4–40?mg/a Ag per inhabitant equivalent are discharged annually to the receiving water. The analysis by SEM-EDX demonstrates adsorption and incorporation of nanosilver on biological flocs. This method yields first insight into complex building and transformation of silver associated with sulfide after adding metallic nanosilver and silver chloride to wastewater. Discussion Silver ions released from nanosilver react immediately with large amounts of chloride present in wastewater to form silver chloride. Silver ions may react with organic ligands or sulfide groups additionally. Consequently, even silver nitrate added with 1?mg/L Ag (250?mg Ag/kg TS) to activated sludge did not inhibit nitrification activity. Very high amounts of nanosilver, i.?e. 100?mg/L Ag, overburdened the system and equilibrium condition between silver ion release and ligands was not reached. The mass balance reflects the excellent attachment of nanosilver to activated sludge and biological flocs. Therefore, the main elimination process of nanosilver is attachment to the activated sludge. The elimination of nanosilver is high compared to organic and inorganic micro pollutants omnipresent in wastewater. Any further reduction of suspended solids in the effluent water will reduce the silver load. Conclusions Generally, in wastewater nanosilver occurs bonded to activated sludge flocs and therefore the elimination of nanosilver is efficient under operation conditions typical for wastewater treatment plants. The major fraction of nanosilver is removed from the system by the excess sludge withdrawal. Nonetheless, the efficiency may be further improved by a tertiary filtration step. All analyses of influent, effluent and sludge confirmed that silver exists as silver sulfide. Due to a negligible water solubility of this silver species, silver ions are not subsequently released. Recommendations and perspectives Nanosilver research should be driven to the identification of transformation processes in real environmental matrices and the influence of coatings on the adsorption behavior. There is no need for action to take special measures for nanosilver removal in the area of municipal wastewater treatment plants compared to ubiquitous hazardous organic pollutants may present in wastewater. Nevertheless, source control measures following the precautionary principle should be performed.     

Formation of ferric flocks to remove for the removal of Zn and Cu from dockyard wastewater

Wastewater from wash down of boat hulls contains typically Cu, Zn and organometallic biocides, e.g. tributyltin (TBT). In some cases this wastewater is led directly into the marine system. In the present paper, a cheap flocculation method (iron flocculants) for removal of Cu and Zn from the wastewater is investigated and the method was shown successful. TBT concentration in a sample from a German dockyard was also decreased during flocculation, but the TBT removed was already associated with small particulates in the original sample. Low concentrations of heavy metals were obtained by flocculation: <0.05 mg Cu/l and 0.2 mg Zn/l. An erratum to this article can be found at     

Planktonic bacteria in the Humber Estuary; Seasonal variation in population density and heterotrophic activity

Seasonal variation in population density and heterotrophic activity (as maximum potential rate, V _max, for glucose mineralization) of bacteria attached to suspended solids, of free bacteria and of total bacteria was examined in the water of the Humber Estuary, north-east England. At the principal site, which was studied over 2 yr, values of density and activity of attached and total bacteria showed marked seasonal periodicity, being low in summer and high from autumn to spring. This was a consequence of density of attached bacteria being dependent on the concentration of suspended solids, which was high in winter and low during summer. Values of density and activity of free bacteria, which were less than those of attached bacteria, showed no seasonal pattern but fluctuated irregularly and were independent of concentration of suspended solids. At two further sites, which were studied over 1 yr only, the density of bacteria varied seasonally in a similar manner, but the activity of attached and total bacteria showed no distinct seasonal pattern — this may, however, be due to limitations of the data rather than to fundamental differences between the sites studied.     

糖精钠生产废水的铁氧体法除铜研究

对糖精钠生产废水实施铁置换法除铜后，废水中仍含有较高浓度的Ｃｕ＾２＋。本研究进一步以铁氧体法除铜。试验条件下，Ｃｕ６２＋的去除率达９８％Ｔ以上，出水Ｃｕ＾２＋浓度低于２．５ｍｇ／Ｌ。通过正交试验，找出最佳工艺及操作参数，从而为该类废水的预处理设计及运行管理提供屯依据。     

Interaction of carbonaceous nanomaterials with wastewater biomass

Increasing production and use of carbonaceous nanomaterials (NMs) will increase their release to the sewer system and to municipal wastewater treatment plants. There is little quantitative knowledge on the removal of multi-walled carbon nanotubes (MWCNTs), graphene oxide (GO), or few-layer graphene (FLG) from wastewater into the wastewater biomass. As such, we investigated the quantification of GO and MWCNTs by UV-Vis spectrophotometry, and FLG using programmable thermal analysis (PTA), respectively. We further explored the removal of pristine and oxidized MWCNTs (O-MWCNTs), GO, and FLG in a biomass suspension. At least 96% of pristine and O-MWCNTs were removed from the water phase through aggregation and 30-min settling in presence or absence of biomass with an initial MWCNT concentration of 25 mg·L⁻¹. Only 65% of GO was removed with biomass concentration at or above 1,000 mg·L⁻¹ as total suspended solids (TSS) with the initial GO concentration of 25 mg·L⁻¹. As UV-Vis spectrophotometry does not work well on quantification of FLG, we studied the removal of FLG at a lower biomass concentration (50 mg TSS·L⁻¹) using PTA, which showed a 16% removal of FLG with an initial concentration of 1 mg·L⁻¹. The removal data for GO and FLG were fitted using the Freundlich equation (R² = 0.55, 0.94, respectively). The data presented in this study for carbonaceous NM removal from wastewater provides quantitative information for environmental exposure modeling and life cycle assessment.