Research Article

Hexavalent Chromium Removal from Model Water and Car Shock Absorber Factory Effluent by Nanofiltration and Reverse Osmosis Membrane

Table 2

Transport parameters ( and ), diffusive flux and of hexavalent chromium in presence of different salts ( = 50 mg , = 50%, pH = 8, and θ = 25°C).

C (mol L−1) (L h−1 m−2)SD
(%)
(mg L−1)SD
(%)
SD
(%)
SD
(%)

KClNF-HL05.090.174.1950.0950.9160.040.71021.06
0.001240.304.8890.0940.9030.0171.48793.68
0.0128.170.065.0880.010.9016 10−51.63842.65
0.127.140.216.8840.10.8655 10−61.75174.75

KClRO-SG05.330.070.3980.0920.9930.00950.1680.06
0.0017.820.150.7160.0350.9870.0490.2690.04
0.017.800.010.8010.010.9850.10.2671.09
0.120.400.041.54310−40.9760.1520.5450.09

KNO3NF-HL05.090.094.1950.0040.9160.380.71020.003
0.00111.970.025.7150.00140.8860.011.03660.09
0.0124.910.185.9630.0980.8850.031.52741.63
0.147.170.088.0810.020.8480.12.52620.08

KNO3RO-SG05.330.070.3980.00030.9930.030.1680.007
0.0016.430.090.4020.00070.9920.040.1840.0034
0.018.430.040.5090.00040.9900.080.2490.002
0.112.520.031.7390.00130.9680.010.3880.09

K2SO4NF-HL05.090.084.1950.0150.9164 10−30.71020.008
0.00112.800.106.9710.10.8690.251.23330.001
0.0132.1570.016.8010.0010.8710.1451.82420.001
0.1116.830.187.7800.005ndndndnd

K2SO4RO-SG05.330.110.3980.000230.9930.0490.1681.78
0.0019.820.10.70010−40.9860.010.3141.02
0.018.240.20.8840.00050.9820.070.2930.008
0.121.770.22.7461.14 10−50.9570.230.6520.09