• Title/Summary/Keyword: Bromate

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Formation behaviour of Bromate in Processes of Advanced Water Treatment System using Nakdong river water (고도정수처리 공정에서 브로메이트의 거동 평가)

  • Kim, Young-Jin;Hyun, Kil-Soo
    • Journal of Korean Society of Water and Wastewater
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    • v.25 no.4
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    • pp.605-610
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    • 2011
  • The objectives of this study are to investigate a bromate behaviour in the processes of advanced water treatment system (AWTS: preozonation, coagulator-settler, rapid sand filter, postozonation, biological activated carbon (BAC) beds) and to investigate the effects of ozonation, pH and ammonia nitrogen on bromate (${BrO^-}_3$) formation. As a result, $BrO_3$ was not detected in the processes of the AWTS without ozonation, while it was detected in a preozonated and postozonated water. For $BrO_3$ formation during June to November, the $BrO_3$ concentration of <9.4${\mu}g/L$ was observed in postozonated water, while it was reduced to about 46% by BAC beds. When applied ozone dosage and ozone contact time for influent with $Br^-$ of <0.3mg/L were 0.5-2.0mg/L.min and 10 min., $BrO_3$ concentration increased with increasing ozone dosage. Longer contact time and lower ozone level also was needed to inhibit the formation of $BrO_3$. At ozone dosage of 1.4 mg/L.min, the formation rate of $BrO_3$ increased with increase of pH value. When $NH_4-N$ concentration increased from 0.1mg/L to 0.4mg/L, $BrO_3$ concentration decreased to about 38%. These results revealed that $BrO_3$ concentration increased with increasing Br level, ozone dosage, and pH value, while it decreased with increase of $NH_4-N$ concentration.

Design Optimization of an Ozone Contactor Using Ozone Contactor Model (OCM) Software

  • Kim, Doo-Il;Lee, Chae-Young;Joe, Woo-Hyeun;Lee, Seock-Heon
    • Environmental Engineering Research
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    • v.14 no.4
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    • pp.244-249
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    • 2009
  • Designing an ozone contactor is complicated because the residual ozone, log C. parvum inactivation, and bromate formation should be optimized with fluctuating water quality. OCM software was developed to assist a plant designer or an operator to fulfill the sophisticated optimization required in the design or operation of a new or an existing plant. In this article, numerical simulations were carried out using the OCM software for the design of a new ozone contactor under diverse design factors (i.e., three pHs, three temperatures, low and high dispersion numbers, and four and ten cells with complete mixing) with kinetic parameters obtained from the sand-filter effluent of a water treatment plant treating water from the Paldang impoundment. The results of the simulation suggested that a high residual ozone concentration at low pH and low temperature would be challenging, and PFR-like hydrodynamics could lower the residual ozone concentration. The inactivation of C. parvum oocysts increased at a lower pH. A lower dispersion number and more cell division increased the inactivation efficiency. Bromate was instantaneously formed during the initial ozonation stage. The effluent concentration was much lower than the regulatory levels imposed by the USEPA because of the low bromide level in raw water.

Quantification of sulfur from organic and inorganic materials for determination of 35C (35C 측정을 위한 유기물과 무기물에서 황의 정량)

  • Lee, H.N.;Kang, S.H.;Song, B.C.;Sohn, S.C.;Jee, K.Y.
    • Analytical Science and Technology
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    • v.22 no.2
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    • pp.186-190
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    • 2009
  • The oxidation studies of a sulfur to a sulfate ion by various oxyhalide oxidants in organic (thiourea, methionine) and inorganic (sulfate, thiophosphate) compounds were carried out in an acidic solution. The optimized result of the oxidation reaction was obtained when a bromate compound (${BrO_3}^-$) as an oxidant and a 3 M $HNO_3$ solvent were used. The chemical yield for the oxidation of the organic and inorganic sulfur compounds to a sulfate ion was monitored as 80% for thiophosphate, 87% for methionine, and 100% for thiourea and sulfate within 5% RSD. The oxidations of thiourea required at least 1.6 equivalents of the bromate in an acidic solution. In the case of the oxidation of methionine and thiophosphate, the oxidation yields were above 80% if the bromate was used at 20 times higher than that of the substrates. The sulfate ion was quantitatively measured by using a GPC counting of $^{35}S$ followed by precipitates of $BaSO_4$. A quenching correction curve for the $^{35}S$ counting was obtained to use the difference via the precipitate weight result.

Effect of Certain Additives on Bread-Making Quality of Wheat-Purple Sweet Potato Flours (밀 및 자색고구마 가루의 제빵성에 대한 첨가제의 영향)

  • 김선영;유정희
    • Korean journal of food and cookery science
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    • v.13 no.4
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    • pp.492-499
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    • 1997
  • The effect of oxidants, gluten and gums on breadmaking quality of wheat-purple sweet potato(Ipomoea batatas) composite flour were studied. Alveograph tests of doughs showed that all additives increased the P, L and W values. Of these additives, L-Ascorbic acid, gluten, carboxy methyl cellulose have a significant effect on alveogram indexes. SEM showed that the dough added with additives changed some what in appearance when compared with the control. When oxidants was added, the doughs discontinuous gluten film were observed. No significant differences ,were evident in bread crumb color among the additives. And textural characteristics of bread crumb were influened by adding additives. Breads containing additives showed an increase in max weight, strength and hardness and a decrease in springness and cohesiveness. Average enthalpy values for all bread crumb after 7days increased with storage time. However, addition of additives decrease the rate of staling slightly more than that of the control. Addition of L-Ascorbic acid, L-Cystine, carboxy methyl cellulose and hydroxy propyl methyl cellulose increased the loaf volume significantly, and with except potassium bromate bread scores were acceptable.

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Determination of bromide in bottled mineral water and ground water in Korea (먹는 샘물 및 지하수 원수 중 bromide 분석연구)

  • Ahn, Hye-Sil;Seo, Kyoung-Ae;Park, Ju-Hyun;Lee, Jun-Bae;Kim, Tae-Seung;Han, Jin-Seok;Kwon, Oh-Sang
    • Analytical Science and Technology
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    • v.24 no.1
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    • pp.10-14
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    • 2011
  • This study was performed to compare international analytical methods of bromide and applied to determine bromide in bottled mineral water and raw ground water in Korea. Bromide in water was eluted by 10~50 mM potassium hydroxide (KOH) and determined by ion chromatography-suppressed conductivity detector (IC-CD). Sample was purified with Ba- and H-on-guard cartridge and $0.2\;{\mu}m$ membrane filter. The method detection limit (MDL) and the limit of quantitation (LOQ) of bromide were 0.2 and $0.5\;{\mu}g/L$, respectively. The calibration curve showed good lineality above 0.9993 in the ranges of the $0.5\sim80\;{\mu}g/L$. A correlation coefficient of bromide in ground water and sum of bromide and bromate in bottled mineral water is 0.808.

Peroxone ($O_3/H_2O_2$) Process in Drinking Water Treatment (정수처리에서의 Peroxone ($O_3/H_2O_2$) 공정)

  • Son, Hee-Jong;Yoom, Hoon-Sik;Bin, Jae-Hoon
    • Journal of Korean Society of Environmental Engineers
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    • v.32 no.3
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    • pp.296-308
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    • 2010
  • The peroxone process overcomes many of the limitations associated with conventional and advanced water treatment systems using chlorine disinfection and ozone oxidation processes. Ozone and hydrogen peroxide generate highly reactive hydroxyl free radical which oxidize various organic compounds and has highly removal efficiency. The key issue to operate peroxone process is developing the method to achieve high process effectiveness when scavengers that inhibit generation of OH radicals or consume OH radicals are co-existing in the process. Also many studies, to minimize inorganic oxidative by-products such as bromate and to reduce disinfection by-products after chlorination behind peroxone process, are needed. And we should consider the excess residual hydrogen peroxide in the water. On-line instruments and control strategies need to be developed to ensure effective and robust operation under conditions of varying load. If problems above mentioned are solved, peroxone process will be applied diversely for water treatment.