STUDY OF ADSORPTION ON DIFFERENT TYPES OF CHARCOALS
ABSTRACT
The present
investigation has been so designed as to provide some insight on various
aspects of adsorption power of carbon materials. In this investigation we use
various types of charcoal of approximately same particle size, namely
activated charcoal, wood charcoal, coconut shell charcoal, paddy shell charcoal
and studied their power using oxalic acid as adsorbate.
INTRODUCTION
In recent years research in the field
of adsorbents and adsorption has gained considerable importance because of its
wide applications. Activated charcoal is used as adsorbent in gas masks in
which all toxic gases and vapors are adsorbed by the charcoal and pure air is
passed through it. Silica and alumina gel are used as adsorbents for removing
moisture and for controlling humidity in closed bottles, bottles, boxes and
rooms. Adsorption also plays an important role in heterogeneous catalysis. For
example the role of finely divided iron in the manufacture of ammonia by Haber
process .Animal charcoal is used as a decolorize in the manufacture of cane sugar.
Various aspects of
the phenomenon of Adsorption
Adhesion of atoms,
ions, biomolecules or molecules of gas, liquid or dissolved solids to a surface
is called adsorption. Adsorption is different from absorption. In adsorption
process two substances are involved.
Adsorbent : The
substance on whose surface the adsorption occurs is known as adsorbent.
Adsorbate : The
substance whose molecules get adsorbed on the surface of the adsorbent ( i.e.
solid or liquid ) is known as adsorbate.
Types of adsorption:
Depending upon the nature of forces
existing between adsorbate molecules and adsorbent, the adsorption can be
classified into two types:
1. Physical adsorption (physisorption): If
the force of attraction existing between adsorbate and adsorbent are Vander
Waal’s forces, the adsorption is called physical adsorption. It is also known
as Vander Waal’s adsorption. In physical adsorption the force of attraction
between the adsorbate and adsorbent are very weak, therefore this type of
adsorption can be easily reversed by heating or by decreasing the pressure.
2. Chemical adsorption (chemisorption): If
the force of attraction existing between adsorbate and adsorbent are
almost same strength as chemical bonds, the adsorption is called chemical
adsorption. It is also known as Langmuir adsorption. In chemisorption the force
of attraction is very strong, therefore adsorption cannot be easily reversed.
Adsorption process is usually studied through graphs known as adsorption
isotherm. That is the amount of adsorbate on the adsorbent as a
function if its pressure or concentration at constant temperature .The quantity
adsorbed is nearly always normalized by the mass of the adsorbent to allow
comparison of different materials.
Adsorbents
The material upon whose surface the adsorption takes place is called an
adsorbent .Activated carbon is used as an adsorbent. Adsorbents are used
usually in the form of spherical pellets, rods, moldings, or monoliths with
hydrodynamic diameters between 0.5 and 10 mm. They must have high abrasion
resistance, high thermal stability and small pore diameters, which results in
higher exposed surface area and hence high surface capacity for adsorption. The
adsorbents must also have a distinct pore structure which enables fast
transport of the gaseous vapours. Most industrial adsorbents fall into one of
three classes:
Oxygen-containing compounds - Are typically hydrophilic and polar,
including materials such as silica gel and zeolites.
Carbon-based compounds - Are typically hydrophobic and non-polar,
including materials such as activated carbon and graphite.
Polymer-based compounds - Are polar or non-polar functional groups in a
porous polymer matrix.
Activated carbon is used for adsorption of organic substances and
non-polar adsorbates and it is also usually used for waste gas (and waste
water) treatment. It is the most widely used adsorbent since most of its
chemical (eg. surface groups) and physical properties (eg. pore size
distribution and surface area) can be tuned according to what is needed. Its
usefulness also derives from its large microspore (and sometimes mesopore)
volume and the resulting high surface area.
Mechanism of
Adsorption Using Adsorbent
SIGNIFICANCE OF WORK
This study is based on important topic adsorption
which has application in various fields of industries. Different varieties of
charcoal considered in this investigation have showed considerable adsorption
power. It is found that ordinary varieties of charcoal are highly active and
they can be used for removing impurities of metal ions even from drinking
water.
OBJECTIVES
·
To understand the adsorption
power of ordinary varieties of charcoal.
· To make sure that ordinary charcoals are highly active in removing
impurities
METHODOLOGY
One litre of 1 N Oxalic acid solution was prepared by weighing from
which 500 ml of .5N,0.25N, 0.125N oxalic acid solutions were
prepared. Charcoals were labelled as Sample I (Activated charcoal ),Sample II
(Wood charcoal), Sample III (Paddy shell charcoal) ,Sample IV (Coconut shell charcoal)
. 32 well cleaned and dried bottles were taken and labelled .For
each sample of charcoals 4 different concentrations of oxalic acid were allowed
to adsorb. Duplicates were also prepared .1 gram of charcoal was accurately
weighed and completely transferred into each bottle 50 ml of oxalic acid of
particular concentration as per label was also pipette into each bottle. The
bottles were tightly stoppered and shaken for 1.30 hour.
Then the bottles were placed in a water bath for about half an hour in
order to attain equilibrium temperature .Then the supernatant liquid was
filtered through a dry filter paper .The initial 5 to 10ml solution was
rejected and the remaining solution was collected . The first
fraction was rejected since adsorption of the solution to the filter
paper may occur which decrease the concentration of the solution .The
same procedure was followed for all the 18 bottles . Then 10ml of the solution
was pipette out and titrated against standard KMnO4 solution.
A graph was
plotted for each type of charcoal by taking ce /(x/m) values along Y axis
and Ce along X axis. Here Ce is the equilibrium concentration of
oxalic acid after adsorption .A straight line wil indicate the verification of
Langmuir adsorption .The different graphs will also indicate highest adsorbing
charcoal.
RESULTS &
DISCUSSION
All the charcoal samples we are made uniform size by using serves. The
charcoal samples we are uniformly activated by heating.
According to Langmuir Adsorption theorem
Verification of Langmuir Adsorption theory ; x/m=abCe/1+aCe
Where ‘Ce’ is the
equilibrium concentration of the adsorbate . ’x’ is the amount of oxalic acid
adsorbed .It is calculated from the titre values .Here ‘a’ and ‘b’ constants .
A plot
of Ce/(x/m) values against Ce must give a
straight line with slope 1/b and intercept 1/ab. Here samples are labeled
according to the charcoal sample used and concentration of oxalic acid after
adsorption the equilibrium concentration of oxalic acid was determined by titrating
10 ml of solution with KMnO4 of known concentration.

Then x/m is calculated,
where m is the mass of charcoal added in each case Ce/(x/m) is
calculated .A graph was ploted by taking Ce/(x/m) values
Y axis and Ce along x axis .A straight line was obtained which verifies
Langmuir Theorem.
CALCULATION OF EQUILIBRIUM ON
CONCENTRATION OF OXALIC ACID
|
Charcoal Used |
Bottle No |
C0 Concentration of oxalic acid before adsorption |
VKMnO4 [10 ml filtrate against KMnO4] |
C0=(N KMnO4 * VKMnO4)/10 Concentration of oxalic acid after adsorption |
|
Sample 1 Activated charcoal |
1 a1 |
1 |
89 |
.89 |
|
1a2 |
89 |
.89 |
||
|
1b1 |
.5 |
45.7 |
.457 |
|
|
1b2 |
45.7 |
.457 |
||
|
1c1 |
.25 |
20.8 |
.208 |
|
|
1c2 |
20.8 |
.208 |
||
|
1d1 |
.125 |
10.3 |
.103 |
|
|
1d2 |
10.3 |
.103 |
||
|
Sample 2 Wood charcoal |
IIa1 |
1 |
49.6 |
.992 |
|
IIa2 |
49.6 |
.992 |
||
|
IIb1 |
.5 |
46.5 |
.465 |
|
|
IIb2 |
46.5 |
.465 |
||
|
IIc1 |
.25 |
22.1 |
.221 |
|
|
IIc2 |
22.1 |
.221 |
||
|
IId1 |
.125 |
19.6 |
.098 |
|
|
IId2 |
19.6 |
.098 |
||
|
Sample 3 Paddy shell charcoal |
IIIa1 |
1 |
49 |
.98 |
|
IIIa2 |
49 |
.98 |
||
|
IIIb1 |
.5 |
47.3 |
.473 |
|
|
IIIb2 |
47.3 |
.473 |
||
|
IIIc1 |
.25 |
23.1 |
.231 |
|
|
IIIc2 |
23.1 |
.231 |
||
|
IIId1 |
.125 |
21.5 |
.1075 |
|
|
IIId2 |
21.5 |
.1075 |
||
|
Sample IV Coconut shell charcoal |
Iv a1 |
1 |
49 |
.98 |
|
Iva2 |
49 |
.98 |
||
|
IVb1 |
.5 |
40.6 |
.466 |
|
|
IVb2 |
40.6 |
.466 |
||
|
IVc1 |
.25 |
22 |
.22 |
|
|
IVc2 |
22 |
.22 |
||
|
IVd1 |
.125 |
21.1 |
.211 |
|
|
IVd2 |
21.1 |
.211 |
CALCULATION OF Ce/(x/m)VALUES FOR
DIFFERENT SAMPLES
|
Charcoal used |
Bottle No |
C0 –C e |
|
x/m |
Ce/(x/m) |
||
|
Charcoal I |
1 a1 |
.11 |
.3465 |
.3465 |
2.568 |
||
|
I a2 |
.11 |
.3465 |
.3465 |
2.568 |
|||
|
I b1 |
.043 |
.13545 |
.13545 |
3.373 |
|||
|
I b2 |
.043 |
.13545 |
.13545 |
3.373 |
|||
|
I c1 |
.042 |
.1323 |
.1323 |
1.572 |
|||
|
I c2 |
.042 |
.1323 |
.1323 |
1.572 |
|||
|
I d1 |
.022 |
.0693 |
.0693 |
1.486 |
|||
|
I d2 |
.022 |
.0693 |
.0693 |
1.486 |
|||
|
Charcoal 2 |
II a1 |
.008 |
.0252 |
.0252 |
39.3 |
||
|
IIa2 |
.008 |
.0252 |
.0252 |
39.3 |
|||
|
IIb1 |
.035 |
.1102 |
.1102 |
4.219 |
|||
|
II b2 |
.035 |
.1102 |
.1102 |
4.219 |
|||
|
II c1 |
.029 |
.0913 |
.0913 |
5.09 |
|||
|
II c2 |
.029 |
.0913 |
.0913 |
5.09 |
|||
|
II d1 |
.027 |
.08505 |
.0852 |
1.1522 |
|||
|
II d2 |
.027 |
.08505 |
.0852 |
1.1522 |
|||
|
Charcoal 3 |
IIIa1 |
.02 |
.063 |
.063 |
15.55 |
||
|
IIIa2 |
.02 |
.063 |
.063 |
15.55 |
|||
|
IIb1 |
.027 |
.08505 |
.08505 |
5.5614 |
|||
|
IIIb2 |
.027 |
.08505 |
.08505 |
5.5614 |
|||
|
III c1 |
.019 |
.05985 |
.05985 |
3.859 |
|||
|
IIIc2 |
.019 |
.05985 |
.05985 |
3.859 |
|||
|
IIId1 |
.0175 |
.055125 |
.055125 |
1.950 |
|||
|
IIId2 |
.0175 |
.055125 |
.055125 |
1.950 |
|||
|
Charcoal 4 |
IV a1 |
.02 |
.063 |
.063 |
15.55 |
||
|
IV a2 |
.02 |
.063 |
.063 |
15.55 |
|||
|
IV b1 |
.034 |
.1071 |
.1071 |
4.3510 |
|||
|
IV b2 |
.034 |
.1071 |
.1071 |
4.3510 |
|||
|
IVc1 |
.03 |
.0945 |
.0945 |
2.328 |
|||
|
IV c2 |
.03 |
.0945 |
.0945 |
2.328 |
|||
|
Iv d1 |
.0195 |
.061425 |
.061425 |
1.7175 |
|||
|
IV d2 |
.0195 |
.061425 |
.061425 |
1.7175 |
|||
Table showing adsorption of oxalic acid per gram
of charcoal ( with different
concentration of oxalic acid)
|
1 N
Oxalic acid |
.5 N Oxalic acid |
.25 N Oxalic acid |
.125 N Oxalic acid |
||||||||||
|
Bottle NO. |
x |
x/m |
Bottle No |
x |
x/m |
Bottle No. |
x |
x/m |
Bottle No. |
x |
x/m |
||
|
Ia1 |
.3465 |
.465 |
I b1 |
.1354 |
.1354 |
Ic1 |
.1323 |
.1323 |
Id1 |
.0693 |
.0693 |
||
|
Ia2 |
.3465 |
.3465 |
Ib2 |
.1354 |
.1354 |
Ic2 |
.1323 |
.1323 |
Id2 |
.0693 |
.0693 |
||
|
IIa1 |
.0252 |
.0252 |
IIb1 |
.1102 |
.1102 |
IIc1 |
.0913 |
.0913 |
IId1 |
.08505 |
.08505 |
||
|
IIa2 |
.0252 |
.0252 |
IIB2 |
.1102 |
.1102 |
IIc2 |
.0913 |
.0913 |
IId2 |
.08505 |
.08505 |
||
|
IIIa1 |
.063 |
.063 |
IIIb1 |
.0850 |
.0850 |
IIIc1 |
.05985 |
.0598 |
IIId1 |
.05512 |
.05512 |
||
|
III a2 |
.063 |
.063 |
IIIb2 |
.08505 |
.08505 |
IIIc2 |
.05985 |
.05985 |
IIId2 |
.055125 |
.055125 |
||
|
IVa1 |
.063 |
.063 |
IVb1 |
.1071 |
.1071 |
IVc1 |
.0945 |
.0945 |
IVd1 |
.061425 |
.061425 |
||
|
IVa2 |
.063 |
.063 |
IVb2 |
.1071 |
.1071 |
IVc2 |
.0945 |
.0945 |
IVd2 |
.061425 |
.061425 |
||
CONCLUSION
The different
varieties of charcoal considered in this investigation have showed considerable
adsorption power. It is found that ordinary varieties of charcoal are highly
active and they can be used for removing impurities of metal ions even from
drinking water.
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