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Application of Pressure-Driven Membrane Processes in Treatment of Swimming Pool Water System

Edyta ŁASKAWIEC

Edyta ŁASKAWIEC

MSc Eng. (PhD Study); Institute of Water and Wastewater Engineering, Faculty of Energy and Environmental Engineering, Silesian University of TechnologyGliwice, Poland
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ŁASKAWIEC, Edyta
, 
Mariusz DUDZIAK

Mariusz DUDZIAK

Associate Prof. DSc PhD Eng.; Institute of Water and Wastewater Engineering, Faculty of Energy and Environmental Engineering, Silesian University of TechnologyGliwice, Poland
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DUDZIAK, Mariusz
 y 
Joanna WYCZARSKA-KOKOT

Joanna WYCZARSKA-KOKOT

PhD Eng.; Institute of Water and Wastewater Engineering, Faculty of Energy and Environmental Engineering, Silesian University of TechnologyGliwice, Poland
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WYCZARSKA-KOKOT, Joanna
  
01 abr 2019
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Publicado en línea: 01 abr 2019
Páginas: 141 - 148
Recibido: 28 ago 2017
Aceptado: 13 oct 2017
DOI: https://doi.org/10.21307/acee-2018-014
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© 2018 Edyta łaskawiec et al., published by Sciendo
This work is licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International License.

Figure 1.

Hydraulic performance of the MW and V5 ultrafiltration membranes (ΔP=0.5 MPa) during filtration of washings from SP and RP swimming pool systems
Hydraulic performance of the MW and V5 ultrafiltration membranes (ΔP=0.5 MPa) during filtration of washings from SP and RP swimming pool systems

Figure 2.

Hydraulic performance of the V5 ultrafiltration membrane at ΔP = 0.2 and 0.5 MPa during filtration of washings from the JB system
Hydraulic performance of the V5 ultrafiltration membrane at ΔP = 0.2 and 0.5 MPa during filtration of washings from the JB system

Figure 3.

Hydraulic performance of nanofiltration membranes (DK and HL) at ΔP=3 MPa for washings from the SP and RP systems
Hydraulic performance of nanofiltration membranes (DK and HL) at ΔP=3 MPa for washings from the SP and RP systems

Figure 4.

Separation properties of ultrafiltration membranes MW and V5 (ΔP=0.5 MPa) in relation to reduction of a) absorbance RUV254 b) turbidity Rturbidity of washings from the SP and RP systems
Separation properties of ultrafiltration membranes MW and V5 (ΔP=0.5 MPa) in relation to reduction of a) absorbance RUV254 b) turbidity Rturbidity of washings from the SP and RP systems

Figure 5.

Separation properties of the V5 membrane at different transmembrane pressure values (0.2 MPa and 0.5 MPa) defined by the values of the average retention coefficients a) absorbance RUV254 and b) turbidity Rturbidity of washings from the JB system
Separation properties of the V5 membrane at different transmembrane pressure values (0.2 MPa and 0.5 MPa) defined by the values of the average retention coefficients a) absorbance RUV254 and b) turbidity Rturbidity of washings from the JB system

Figure 6.

Separation properties of nanofiltration membranes (DK and HL) defined by the retention average ratio for a) absorbance RUV254 b) turbidity Rturbidity of the washings from the SP and RP systems
Separation properties of nanofiltration membranes (DK and HL) defined by the retention average ratio for a) absorbance RUV254 b) turbidity Rturbidity of the washings from the SP and RP systems

Figure 7.

Changes in the value of inhibition of bioluminescence of samples of washings before and after a) ultrafiltration for the V5 and MW membranes (ΔP=0.5 MPa) and b) nanofiltration for the HL and DK membranes (ΔP=3 MPa)
Changes in the value of inhibition of bioluminescence of samples of washings before and after a) ultrafiltration for the V5 and MW membranes (ΔP=0.5 MPa) and b) nanofiltration for the HL and DK membranes (ΔP=3 MPa)
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