Project Title:

Nowadays,water pollution problem is becoming more and more serious.One
possible method to remove pollutants from water is adsorption.Among many
known adsorbents,activated carbons are most widely used because of its
high adsorption ability.Activated carbon have been produced from
carbonaceous matterials(such as coconut shell,coconut fibre,peat,wood…)by
carbonization at 800-1000 0 C and activation at over 1000 0 C with CO2 or
steam.Another way to produce activated carbon is chemical activation with
Scrap-coir is a kind of waste from coconut fibre production process.In
Vietnam,there is about 200 000-500 000 tons of scrap-coir eliminated every
year.A little them is used as organic soil for agriculture. Almost other scrapcoir quantity has been thrown into rivers. This cause a big polution problem.
So, it is essential to study applying the scrap-coir as raw material for
production of activated carbon.
1.Pretreatment of raw scrap-coir
The material is first pretreated in deionized water to remove soil,sand and
other inorganic impurities at pH 5.0,mscrap-coir/mwater=1/10 and temperature at
about 80-100 0C.Then,the pretreated scrap-coir is washed by deionized water
until the pH of solution reached about 7.0.Finally,it is dried at 105 0C for
many hours.
This water pretreated scrap-coir sample (WP) will be used as initial material
in this study.
2.Preparation of activated carbon (AC) from WP
Chemical activation with sulfuric acid or phosphoric acid are carried out
using an impregnation method.For each impregnation experiment,15.0
grams of WP is mixed with 1M,2M of 3M solutions of H2SO4 or H3PO4 for
24 h at stirring rate of 200 rpm.
The resultingmixture is filtered and dried at 105 0C overnight.Then
impregnated WP is carbonized in a horizontal furnace,under a nitrogen gas
flow(2.51 min -1).The furnace temperature is increased from room
temperature to 400 0C,500 0C or 600 0C with heating rate of 20 0C.min -1 and
held at this temperature for different ti mesof 30 min,90 min or 180 min.
To estimated the effect or sulfuric acid on the characteristic of resulting
materials,WPsample without impregnated H2SO4 or H3PO4 solution should
be carbonized at 400 0C,500 0C or 600 0C for 30 min.The other
carbonization conditions are as in the chemical activation process.
A)Characterization of the materials
1.Ash content (%) is determined by the method of Ahmedna.According to
that,approximately 2 grams of sample is placed into weighed ceramic
crucibles.Sample and crucibles are dried overnight at 80 0C and reweighed
to obtain the dry material weight.Then,they are heated at 760 0C for at least
6 h.The crucibles are cooled in a desicator and ash are weighed.
2.Porous characteristics
-Mesopore (2nm-50nm) and macropore (>50nm)size distributions are
estimated with a MICROMERITICS AUTOPORE VI 9500 mercury
porosimeter up to 2,000 atm,to estimate the volume constituted by all pores
with a diameter from 100 000 nm down to 8.5 nm.
-To determine specific surface area and micropore characteristics,nitrogen
adsorption/desorption isotherms are performed at 77k with a CHEMBET
3000 surface area analyzer.The specific surface area is calculated by
Brunauer-Emmett-Teller equation.The mesopore (2nm-50nm) and
micropore (<2nm) volumes are estimated according to Barrett Joyner
Halenda and Horvath Kawazoe theories,rspectively.
-Size and morphological features was studied by Scanning electron
microscopy (S-4800 UHR-FE-SEM-Hitachi,Japan)after fibers metallization
with 100 0A platinum.
3.Surface chemistry
-The pH of point of zero charge is measured following Franz
method.Titrations by 0.1N solutions of NaOH or HCl are carried out at 298
K,after stirring during 24 h of 500 mg AC product in 50 ml of NaCl
electrolyte solutions(0.1N,0.05N and 0.01N)
-The surface acidic oxygen functional groups of AC product are determined
by the Boehm titration method.500 mg of AC is stirred for 24 h in 25 ml of
0.1 N solutions of base with different strengths:sodium ethoxide
(NaOC2H5),sodium hydroxide (NaOH),sodium carbonate (Na2CO3) or
sodium bicarbonate (NaHCO3).After this time,the slurry is filtered and a 10
ml aliquot is titrated with 0.1 N HCl.The results of titration are expressed as
mol H+ equivalent/g carbon.
B)Adsorption of organic compounds or metallic ions in water
Phenolic compounds and Cu +2 ion (from CuSO4)are selected to test
pollutant adsorption ability of AC products.They are chosen because of their
popularity in municipal and industrial wastewater.
The method used in this study is performed in stoppered glass reactor,kept in
a temperature-controlled water bath at 25±1.0 0C with contant stirring rate of
300 rpm.
For each pollutant,isotherm experiments are performed at 293 K.Given
weights of are stirred in 0.250 L of an aqueous solution containing the
pollutant with an initial concentration ranging from 5 to 100 mg L-1.The
contact time needed to reach equilibrium is set to 48 h for phenol and 120 h
for copper on the basis of kinetic experiments carried out in previous
works.In the case of copper adsorption,pH is maintained at a value of 5.0 by
adding 0.1N NaOH.
To produce activated carbon powder from waste coconut fibre in
Vietnam,with application for pollutants removal from water.