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To determine the biosorbent quantity for a maximal removal of diazinon, the effect of the PCW dose on the biosorption equilibrium is illustrated in Fig. 5 which shows the uptake of diazinon for five doses over the range (0.2 1.2 g L−1).
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Biosorption of metal ion from aqueous solution depends on the functional groups present on the biosorbent, their quantity and affinity for the metal ion.
Batch biosorption experiments were performed to optimize the conditions of environmental parameters (pH, biosorbent quantity, heavy metal concentration and contact time).
Few researchers were interested in desorption processes for either regeneration of the biosorbent for reuse and/or for recovery of the sorbate material.
The biosorbent efficiency for the dyes was determined after 3 h of treatment at 30 °C using suitable size of biosorbent (0.255 mm).
The use of microorganisms to regenerate the surface of the biosorbent for more removal is known as bioregeneration/bioaccumulation.
The data can be used to compare the kinetics of the biosorbent for different pollutants.
The data can be used to compare the biosorptive capacities of the biosorbent for different pollutants.
Further study is warranted to evaluate the potentiality of the biosorbent for heavy metal removal from the real environment.
H2O2 along with thermal treatment was used to treat wine processing sludge in order to remove organic matter before using the biosorbent for the removal of Cr (VI) [ 73].
As shown in the figure, as the quantity of the biosorbent increased from 0.1 to 0.2 g the % Cu2+ ion removed increases from 64to79%9 % for RAWB while the increase is from 80 to 97 % for OAMB.
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