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. 2023 Jul 17;9(8):e18344. doi: 10.1016/j.heliyon.2023.e18344

Table 9.

Economic Feasibility of Spent Acid Regeneration and Metal Ion Recovery DD runs, at 5500 kg/d, in the textile industry.


Water Input (kg/d)a
Feed (kg/d)
Spent Solutionb (kg/d)
Recovered Acid (kg/d)c
3300.00 5500.00 5277.15 3522.85
H2SO4 4041.02 549.37 3491.66d
H2O 3300.00 1458.98 4727.78 31.19

Note: Operation time: 8.5 h, equiv. To one (working) day.

a

Feed/Water = 0.6.

b

Mass Balance: F + W Created by potrace 1.16, written by Peter Selinger 2001-2019 R + S.

c

Also called ‘Depleted’ Solution.

d

Worth US $83,799 of technical-grade H2SO4 used.