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Control of membrane fouling by Hydrogen Sulfide (H2S) diffusion ...

Control of membrane fouling by Hydrogen Sulfide (H2S) diffusion ...

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Soluble Microbial Products (SMP)SMP is soluble EPS in feed water. It ismainly composed <strong>of</strong> protein, carbohydrateand total organic carbon. In our experiment,four samples were used to determine theconcentration protein and carbohydrate andfive samples for total organic carbon.Obtained results are given below:ProteinTable 1: Protein conc. (mg/l) in SMPRun C D F GNo H 2 S 38.8 8.3 0 025 ppm H 2 S 25.3 4.3 1.5 4.250 ppm H 2 S 46.3 0 0 0100 ppm H 2 S 33.8 0 14.1 0Concentration <strong>of</strong> protein in SMP has beendetermined after sparing <strong>of</strong> H 2 S in fourdifferent concentrations. Most results showthat protein concentration is very low and itdoes not vary with H 2 S concentration.CarbohydrateTable 2: Carbohydrate conc. (mg/l) in SMPRun C D F GNo H 2 S 0 7.3 6.2 23.625 ppm H 2 S 10.8 11.0 4.8 14.450 ppm H 2 S 8.3 10.9 10.3 14.8100 ppm H 2 S 12.2 13.9 13.9 16.2After <strong>diffusion</strong> <strong>of</strong> H 2 S it was not found asignificant variation <strong>of</strong> carbohydrateconcentration in SMP sample and accordingto obtained result, effect <strong>of</strong> H 2 S onconcentration <strong>of</strong> carbohydrate in SMP is notcountable.Total Organic CarbonTOC, mg/l180160140120100806040200Effect <strong>of</strong> H 2 S on TOCD F G H ISampleNo <strong>H2S</strong> sparging25 ppm <strong>H2S</strong>sparging50 ppm <strong>H2S</strong>sparging100 ppm <strong>H2S</strong>spargingTOC has been measured for five set <strong>of</strong>samples and in two test results, TOC wasnot vary significantly when applied H 2 S insludge but other three set <strong>of</strong> results showthat TOC decreases with the increase <strong>of</strong> H 2 S<strong>diffusion</strong>. As total organic carbon play animportant role <strong>of</strong> in <strong>fouling</strong> resistance,application <strong>of</strong> H 2 S in feed water deduce theTOC and consequently help to increase thefilterability <strong>of</strong> <strong>membrane</strong> in MBRs.ConclusionThis research works have focused on theimpact <strong>of</strong> H 2 S <strong>diffusion</strong> on <strong>membrane</strong><strong>fouling</strong> in MBR operation. ZP, pH, SMP,eEPS have been used to investigate theeffect <strong>of</strong> H 2 S application on <strong>membrane</strong><strong>fouling</strong> behavior. From the obtained result,following specific conclusions could bedrawn out:1. Application <strong>of</strong> H 2 S in feed waterassisted significantly to decrease theconcentration <strong>of</strong> eEPS and SMP TOCin sludge. It was found other studiesthat eEPS and SMP have a vital roleto enlarge the <strong>fouling</strong> resistance(Liang et al., 2007). Therefore,<strong>diffusion</strong> <strong>of</strong> H 2 S enhancedpermeability <strong>of</strong> <strong>membrane</strong> in MBRoperation <strong>by</strong> limiting <strong>fouling</strong>resistance as it reduced theconcentration <strong>of</strong> eEPS and SMPcompounds.2. It is quite clear from obtained resultsthat pH <strong>of</strong> biomass increased withthe increase <strong>of</strong> H 2 S concentration.This elevated pH value facilitates theactivities <strong>of</strong> the livingmicroorganisms which couldimprove the whole treatmentperformance.3. ZP <strong>of</strong> virgin <strong>membrane</strong> is lower thanthe <strong>fouling</strong> <strong>membrane</strong> but the effect<strong>of</strong> H 2 S application on zeta potentialis dubious because it unevenlyvaried with different concentration<strong>of</strong> H 2 S.Fig 9: TOC <strong>of</strong> SMP at different H 2 S conc6

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