scholarly journals Washing Batch Test of Contaminated Sediment: The Case of Augusta Bay (SR, Italy)

2020 ◽  
Vol 10 (2) ◽  
pp. 473
Author(s):  
Lucia Lumia ◽  
Maria Gabriella Giustra ◽  
Gaspare Viviani ◽  
Gaetano Di Bella

Two experimental campaigns were conducted to optimize the applicability of the Sediment Washing treatment on the marine sediments of Augusta Bay contaminated with heavy metals and total petroleum hydrocarbons (TPH). In the first campaign were used EDTA, citric acid, and acetic acid to removal only heavy metals (Ni, Cu, Zn, Cr, and Hg) from the sediments, while in the second campaign EDTA, citric acid, and EDDS were used to removal heavy metals (Ni, Cu, Cr, and Pb) and TPH. The tests were conducted at different pH values and contact times with 1:10 solid:liquid weight ratio. In the first experimental, at pH values 4, contact time 3 h, and citric acid, high removal efficiencies (78–82%) have been obtained for Ni, Cu, Zn, and Cr metals, while, in the second experimental campaign, at pH value 4, contact time 0.5 h, and citric acid, high removal efficiencies have been achieved especially for Pb and TPH. Finally, on the basis of the results obtained, a conceptual sediment washing treatment layout was proposed and the related costs estimated.

2017 ◽  
Vol 17 (12) ◽  
pp. 2873-2886 ◽  
Author(s):  
Analy Quiñonez-Plaza ◽  
Fernando Toyohiko Wakida ◽  
Juan Temores-Peña ◽  
Diana Dolores Rodriguez-Mendivil ◽  
Enrique Garcia-Flores ◽  
...  

1978 ◽  
Vol 13 (1) ◽  
pp. 149-160
Author(s):  
W.K. Oldham ◽  
B.H. MacLean

Abstract The research described in this paper is directed toward optimizing conventional lime precipitation of heavy metals by the addition of small quantities of magnesium. Specifically, jar tests were performed to evaluate the effectiveness of adding various concentrations of Mg2+ to both raw sewage and primary effluent to improve the precipitation of metal ions at various reaction pH values. The desired pH levels (10.0, 10.6 and 11.4) were obtained by the addition of lime. General results of the study, using Cr3+, Cu2+, Pb2+, Ni2+ and Zn2+ in concentrations of 0.5, 2.5 and 5.0 mg/l, indicated the following: 1. as expected, the higher the reaction pH, the greater the removal efficiency; 2. for a given reaction pH, the presence of some added Mg++ increased the removal efficiency for all metals tested except Ni2+; 3. on the average, a lime dosage of 220 mg/l (reaction pH=10.6) coupled with an Mg2+ concentration of 30 mg/l, give equivalent removals to high lime treatment at 400 mg/l (reaction pH=11.4); 4. the removal efficiencies varied between 10% and 35% for Ni2+, while the other metals gave results of 35% to 95%, depending upon treatment conditions. It can be concluded that the addition of Mg2+ does indeed enhance the removal of many heavy metals although more work is needed to optimize the combinations for a given type of sewage and to subsequently investigate relative economics.


1982 ◽  
Vol 14 (12) ◽  
pp. 87-105 ◽  
Author(s):  
B Regnier ◽  
C Goblet ◽  
J Genot ◽  
W J Masschelein

Mineral micropollutants in waste waters and drinking water are essentially composed of heavy metal salts. Their elimination, when present in trace quantities, is discussed in this paper. The techniques, which water treatment facilities can use, necessitate preclarification in open basins (efficiency varying between 20 and 90%), elimination by filtration, with efficiencies depending largely on preoxidation but particularly on coagulation-precipitation and related techniques. Our investigations, as well as certain literature data, demonstrate the predominating importance of contact between water and sludges in decanters-clarificators. Thus, Jar tests often yield only a poorly representative result of the elimination of heavy metals by coagulation-flocculation-decantation. As to the use of aluminium sulphate, for example, the elimination rates mentioned relating to the elimination rate or % removal in laboratory experiments, in pilot tests with sludge beds and in treatment plants respectively are as follows: Fe: 100, 95, 100; Mn: 4, 38, 97; Cu: 91, 83, 85; Cr: 29, 8, 83; Cd: 21, 29, 96; Ni: 0, 20, 50; Co: 0, 16, 51; Pb; -, 52, 61. It should be noted that treatment in plants is much more elaborate (oxidation by chlorine dioxide, application of activated silica and a one hour contact time with the sludge bed) than in pilot experiments (15 minutes contact time and a sludge bed without activated carbon). The oxidation state of metals plays an important role in techniques for their elimination by the usual methods such as coagulation-flocculation-decantation as well as in coprecipitation phenomena of Fe and Mn for example. The method of alkaline precipitation, in which the pH value needed is obtained by addition of lime, results in elimination rates over 80% and generally far over 90%. This method uses at the same time direct precipitation and coprecipitation in a calcium carbonate/magnesium oxide matrix. Ion exchange gives highly variable elimination results according to the ion present and its concentration. In practice, strong cation exchange resin are generally applied. In treatment plants, adsorption on carbon allows an overall yield of 50-100% removal of the metal concerned, provided that preoxidation and sufficient contact times are allowed. The experimental distinction of the specific effect due to adsorption is difficult, but according to our studies, adsorption occurs to a small extent only in the majority of cases. 30-50% of the remaining traces are eliminated by infiltration of purified waters underground, where a levelling of concentrations also occurs. In addition to the investigations presented, studies still being carried out demonstrate a sufficient stabilization of heavy metals immobilized with lime in order to allow them to be dumped in the environment without risk. This method seems confirmed as a method of choice in treatment of waste waters loaded with heavy metals.


2020 ◽  
pp. 371-383
Author(s):  
Hassan Elgharbi ◽  
Fatma Aloulou ◽  
Wajdi Haj Ali ◽  
Subrata Borgohain Gogoi ◽  
Monem Kallel

2009 ◽  
Vol 36 (4) ◽  
pp. 709-719 ◽  
Author(s):  
Siranee Sreesai ◽  
Suthipong Sthiannopkao

Utilization of zeolite industrial wastewater as a sorbent and (or) precipitant to remove Cu and Zn from copper-brass pipe industrial wastewater was conducted. These wastewaters were sampled and values for pH, temperature, biochemical oxygen demand (BOD5), chemical oxygen demand (COD), total solids (TS), total dissolved solids (TDS), total suspended solids (TSS), and heavy metals were determined. In addition, the sorption isotherms of Cu and Zn in copper-brass pipe industrial wastewater onto solids of zeolite industrial wastewater at various dilutions of copper-brass pipe industrial wastewater were explored. The relationship between Cu and Zn concentrations and their removal efficiencies under different conditions of wastewater pH, contact times, and ratios between copper-brass pipe industrial wastewater and zeolite industrial wastewater was examined. Zeolite industrial wastewater contained various carbonate compounds that contributed to high pH and TDS values, and low heavy metals contamination whereas copper-brass pipe industrial wastewater had a low pH value and was contaminated with heavy metals, especially Cu and Zn. Application of zeolite industrial wastewater significantly increased the pH of copper-brass pipe industrial wastewater and consequently removed Cu and Zn. The increase in pH of the wastewater mixture significantly enhanced the heavy metals removal. The Langmuir equation described sorption isotherms of Cu and Zn onto solids of zeolite industrial wastewater at neutral pH (6–7) while the Freundlich equation fitted well at pH > 12. The maximum Cu (97%–98%) and Zn (92%–96%) removal efficiencies occurred at the original pH 12.8 of zeolite industrial wastewater, at the ratio of copper-brass pipe industrial wastewater to zeolite industrial wastewater 3:1 (vol.:vol.) and at 30 min contact time.


2020 ◽  
Vol 81 (6) ◽  
pp. 1130-1136 ◽  
Author(s):  
Yue Zhang ◽  
Xiumei Duan

Abstract Heavy metal pollution has become one of the most serious environmental problems today. The preparation of magnesium hydroxy carbonate from low-grade magnesite, and the chemical precipitation of heavy metal wastewater with magnesium hydroxy carbonate as precipitating agent were undertaken. The removal efficiencies of heavy metals were improved by increasing the dose of magnesium hydroxy carbonate, and the applicable dose of magnesium hydroxy carbonate was 0.30 g for 50 mL of the wastewater (6,000 mg/L). The precipitation reactions proceeded thoroughly within 20 min. At this time, the removal efficiencies of heavy metals were above 99.9%. The final pH value was 7.1, the residual VO2+, Cr3+ and Fe3+ concentrations were 0.01, 0.05 and 1.12 mg/L, respectively, which conformed to the limit of discharge set by China (0.5–2.0 mg/L, GB 8978–1996). The precipitate was mainly composed of Fe2O3, V2O5 and Cr2O3, which can be recycled as secondary raw material for metallurgical industry. The treatment of the heavy metal wastewater with magnesium hydroxy carbonate was successful in decreasing the concentrations of VO2+, Cr3+ and Fe3+ in wastewater.


2018 ◽  
Vol 7 (3.34) ◽  
pp. 160
Author(s):  
D Sivakumar ◽  
R Anand ◽  
Asanammal Saral

The influence of various nutrient dosages, dilution ratios and pH values was evaluated with different contact time against colour removal from textile industry wastewater using Lemna minor L and Lemna minuta L.  The optimum nutrient dosage, dilution ratio, and pH value was found to be 50 mg, 8 and 8 respectively. The maximum colour removal corresponding to the optimum process parameters value observed using Lemna minor L as 82.85 % and using Lemna minuta L as 89.5 %. Further, verification was done and showed that the maximum colour removal percentage from textile industry wastewater is lower than colour removal from an aqueous solution.  The results of this study concluded that Lemna minuta L removed more colour than Lemna minor L and both were identified to reproduce the obtained optimum process parameters and for removing colour in a textile industry wastewater.  


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