Ñòóäåíò Áóäûêèíà Ä.Â.,
ñòóäåíò Ðàçèíüêîâ Ä.Þ., ê.õ.í. Áóðûêèíà Î.Â.
Þãî-Çàïàäíûé ãîñóäàðñòâåííûé óíèâåðñèòåò
The use of agrowaste as the absorbing agent for
different classes of industrial dyes
Creating effective ways of
toxic waste treatment and disposal, including different technological
wastewater is an important environmental problem. Sorbents that could be used to solve this problem, more often
than not, are expensive or ineffective. Therefore, special attention should be
paid to finding new innovative materials with high sorption properties
including industrial waste and natural
materials.
It was interesting to
investigate the sorption ability of corn's residues not used as fodder to purify
water from organic dyes.
Specially provided for this purpose
sorption capacity and sorption percent of corn was determined.
To
determine the sorption capacity and
sorption percent of corncobs it was necessary to prepare solutions with four
classes of dyes: acid ( acid dye bright blue), cationic ( cationic dye red), chromium (chromium dye
blue 2 K) and active ( active dye orange) concentration of 0.005 to 0.1 g/l.
The sorption of dye solutions was
carried out under the same conditions (msorbent=2g, tcontact=30
min, vsolution=50 ml). To determine the residual concentration after
sorption the photometric method, the method of calibration curve A=F(due) was
used. The results of this research are shown in Tables 1-4. The data in Tables
1-4 show that complete sorption was achieved within 30 minutes only for active
orange dye and acid bright blue dye with
concentration 0.005 g/l.
Tables 1 – Sorption cationic dye
red
|
Ñ source, g/l |
Ñ residual, g/l |
À |
G,10-3 |
G,% |
|
0,100 |
0,009 |
0,238 |
2,275 |
91 |
|
0,050 |
0,014 |
0,375 |
0,900 |
72 |
|
0,010 |
0,004 |
0,109 |
0,150 |
60 |
|
0,005 |
0,004 |
0,041 |
0,025 |
20 |
Tables 2 – Sorption active dye orange
|
Ñ source, g/l |
Ñ residual, g/l |
À |
G,10-3 |
G,% |
|
0,100 |
0,086 |
1,886 |
0,350 |
14 |
|
0,050 |
0,006 |
0,138 |
0,100 |
40 |
|
0,010 |
0,003 |
0,071 |
0,050 |
40 |
|
0,005 |
0 |
0,110 |
0,025 |
100 |
Tables
3 – Sorption acid dye bright blue
|
Ñ source, g/l |
Ñ residual, g/l |
À |
G,10-3 |
G,% |
|
0,100 |
0,006 |
0,121 |
2,350 |
94 |
|
0,050 |
0,003 |
0,056 |
1,175 |
94 |
|
0,010 |
0,002 |
0,041 |
0,200 |
80 |
|
0,005 |
0 |
0 |
0,125 |
100 |
Tables
4 – Sorption chromium dye blue
|
Ñ source, g/l |
Ñ residual, g/l |
À |
G,10-3 |
G,% |
|
0,100 |
0,021 |
0,501 |
1,980 |
79 |
|
0,050 |
0,007 |
0,169 |
1,075 |
86 |
|
0,010 |
0,003 |
0,059 |
0,180 |
75 |
|
0,005 |
0,003 |
0,102 |
0,040 |
32 |
Sorption
isotherm of active orange dye is similar to
isotherm of the 4th type according to the classification of the
Brunauer, Emmet and Teller. This S - shaped isotherm refers to the isotherm
transition-porous sorbents . Convex portions of sorption isotherms specify the
presence of micropores in the sorbents, concave portions indicate the presence
of macropores.
Sorption
isotherms of acid dye bright blue, chromium dye blue, cationic dye red are similar to the isotherm of the 3rd type
and describe strong intermolecular interaction in the sorbate's substance.
The research has shown that corncobs
have good sorption capacity. During a short period of contact maximal level of
sorption is achieved for almost all
dyes used in the experiment, which indicates their high sorption capacity.