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    REMOVAL OF RHODAMINE B FROM AQUEOUS

    SOLUTION USING COCONUT COIR PITH AS ANADSORBENT

    under the guidance of

    Dr. R.Gandhimathi

    Done by :

    1.Billa Manasa Reddy

    2.Kavya sharma

    3. Mainowshree Boro

    4. Shamma Anna Jacob

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    OBJECTIVES

    To investigate the efficiency of coconut coir pith for theremoval of Rhodamine B dye from waste water.

    To investigate the effects of contact time, adsorbent

    dosage, pH on dye removal efficiency.

    To investigate the adsorption mechanisms throughkinetic models.

    To quantify the adsorption equilibrium through Langmuir

    and Freundlich isotherms.

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    Introduction

    Materials used

    Adsorbate: Rhodamine B dye

    Adsorbent: Coconut Coir Pith

    What is Rhodamine B? What are its uses?

    Why the removal of Rhodamine B?

    Ref: Wikipedia.org

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    Materials used contd

    Why Coconut Coir pith is used as adsorbent?

    The coir pith is sieved through a 300 micron sieve and

    retained on a 150 micron sieve.

    Unsieved Sieved

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    Work Done

    Performed Trials for phosphate removal by adsorption

    using various adsorbents .

    Removal Efficiency not sufficient .

    Started new project on Removal of Rhodamine B dyefrom aqueous solution using adsorption by coconut coir

    pith.

    Experiments performed :

    Effect of contact time

    Effect of Dosage

    Kinetic models for contact time

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    Experimental Procedure

    Preparation of stock solution:

    Take 1g of Rhodamine B and add it to 1000 ml of

    distilled water. A solution of concentration 1000 mg/l is

    obtained.

    Preparation of Reference samples:

    Take 10 ml of 1 g/l solution and dilute it to 100 ml. This

    solution has a concentration of 100 mg/l.

    Further take 50 ml of this solution and dilute it to 500 ml.A solution of 10 mg/l is obtained.

    Similarly, samples of concentration 2,4,6,8 mg/l are

    prepared and a calibration curve is obtained.

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    Peak Wavelength Graph

    for Rhodamine B

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    CALIBRATION CURVE

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    Effect of contact time

    25 mg of coconut coir pith is added to 50 ml of the 10

    mg/l solution. 11 such samples are prepared.

    All samples are put in the shaker for the respective

    timings-5,10,15,20,30,45,60,90,120,150 and 180 mins.

    They are later centrifuged at 1000 rpm and the obtained

    supernatants are tested for Rhodamine B concentration

    using a UV Spectrophotometer.

    The equilibrium contact time is established.

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    Effect of contact time

    Adsorption increases with

    increase in the contact time

    Initially adsorption was low

    but increases with time

    quickly.

    Optimum contact time : 60

    min (Qe )

    Removal efficiency at Qe =

    83.85 %

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    Effect of dosage of theadsorbent

    Prepare samples with different doses of coconut coir

    pith-10,20,30,40,50,60,70,80,90,100 mg/ 50 ml.

    Put these samples in the shaker for 60 min (equilibrium

    contact time).

    Centrifuge the samples at 1000 rpm and measure the

    concentration of the supernatants using a UV

    Spectrophotometer.

    The optimum dosage of the adsorbent is obtained.

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    Effect of dosage

    Removal efficiency

    increases with the

    increase in Coir pith

    dosage.

    Optimum dosage : 2.5

    gm/L with Removal

    efficiency of 98%.

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    Colour change in the sample

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    ADSORPTION KINETICS

    In order to clarify the adsorption process, adsorptionmodels were applied to evaluate the experimental data.

    Adsorption Models :

    1. Lagergrens pseudo first order kinetic model

    2. Lagergrens pseudo second order kinetic model.

    The pseudo first order equation is generally expressedas :

    log(Qe-Qt) = log Qe (k1/2.303)t

    Where Qe and Qt are the adsorption capacity atequilibrium and at time t, respectively(mg/g), k1 is therate constant of pseudo first order.

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    The pseudo second order equation is expressed as :

    (t/Qt) = (1/(k2Qe) + (t/Qe)

    Where k2 is the rate constant of pseudo second order.

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    Kinetic Models

    Pseudo 1st Order Kinetics Pseudo 2nd Order Kinetics

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    Kinetic Constants

    Dye Pseudo 1st order

    coefficients

    Pseudo 2ndorder

    Coefficients

    Qe exp

    (mg/g)

    Qe

    (mg/g)

    k

    (1/min)

    R Qe

    (mg/g)

    k

    (g/mg/m

    in )

    R

    Rhoda

    mineB

    19.7 0.0368 0.914 18.4 0.021 0.999 17.61

    Conclusion : It follows Pseudo 2nd order kinetics.

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    Future Plans

    Experiments to be conducted :

    Effect of pH

    Adsorption Isotherms

    Properties of Adsorbents :1. Zero point charge

    2. Specific gravity

    3. Particle size

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    REFERENCES

    1. Residual oil and suspended solid removal using natural adsorbents

    chitosan, bentonite and activated carbon: A comparative study by

    A.L. Ahmad, S. Sumathi, B.H. Hameed.

    2. Removal and Recovery of the Hazardous Azo Dye Acid Orange 7

    through adsorption over Waste Materials: Bottom Ash and De-Oiled

    Soya by Alok Mittal, Vibha Gajbe, and Jyoti Mittal.

    3. Adsorption of basic dye (methylene blue) onto activated carbon

    prepared from rattan sawdust by B.H. Hameed*, A.L. Ahmad,

    K.N.A. Latiff.

    4. A novel agricultural waste adsorbent for the removal of cationic dyefrom aqueous solutions by B.H. Hameed, R.R. Krishni, S.A. Sata.

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    THANK YOU