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Introduction

The retrieval of color from industrial effluent is a major problem as restriction become more stringent. Effluents from textile pulp and paper industries are highly colored due to residual dyes, and thus lower the aesthetic value structure and are toxic and harmful for aquatic and human life. The presence of color in water inhibits the growth of aquatic fauna and flora by reducing light penetration. Various techniques such as chemical Coagulation Bio – sorption, Oxidation using ozone and adsorption have been generally employed for ret rival of color, Adsorption is one of the most effective physical process and has a great potential for the removal of dyes from wastewater. The aim of this study was to prepare activated carbon fromFerronia elephantumFruit Shell and adsorptionisotherm was developed for Congo red cycle. Which can be readily used to designing purpose in pollution amendment and control.

Material and Methods

Adsorbent Preparation

The adsorbentFerronia elephantumFruit shell (FEFS) was collected from the Pandhari forest situated in between warud and Padhurna. TheFerronia elephantumFruit Shell was first dried at atemperature of 160°C for six hours. After grinding it was then soaked overnight in 0.1 N NaOH solution to remove the lignin content, excess alkalinity was then neutralized with 0.1 N HCI solution. It was washed with distilled water several time till the wash water become colorless. Then it was kept in muffle furnace at 130°C for 6 hrs. it was sieved to obtain average particle size of 200 mesh. Finally it was dried again in an over at 50°C for hours. The adsorbent was then stored in desiccators for final studies.

Adsorbate Preparation and Batch Study

Stock solution (1000mg/L) of Congo Red was prepared by dissolving 1 gm of dye in 1000 ml of double distilled water. The stock solution were diluted with double distilled water to obtain required standard solution. The dried amount of 0.2gm. of FEF. Shell was take in 250 ml reagent bottle and standard solution (100ml) containing various concentration of Congo Red dye was added and system is equilibrated by shaking the contents of the flask at room temperature. The adsorbent and adsorbent were separated by filtration and filtrate was determined by spectrophotometer at 495 nm a against a reagent blank. The spectrophotometer systrornic(model 104) was used to measure the concentration of Congo Red.

Table 1: Kinetic model value for adsorption of Congo Red on FEFS Click here to view table

Effect of pH on the scavenging the dye was studied using 100ml dye solution having 40 mg/L initial concentration. Effect of initial concentration. Agitating time and adsorbent dose was also studied.

Result and Discussion

Effect of Initial Dye Concentration & Contact Time

The initial concentration of Congo Red solution was varied from 20,30,40,60 mg/L and batch experiments were carried out by taking 200 ml of this solution with dried 200mg on the adsorbent and the system is equilibrated by shaking the contents of the flask at room temperature equilibrium reached in 2 hours. Final concentration of Congo Red was determined by spectrophotometer at 495 n.m. the percentage removal of Congo Red was observed to be 87%. To establish equilibrium time for maximum uptake and to know the kinetics of adsorption process. The adsorption of Congo Red on adsorbent was studied as a function of contact time. Percentage removal of dye is found to decrease with increase in dye concentration. From contact time data it may be seen that dye removal is very rapid during initial period of contact and the maximum are reached within the first 30 minutes removal.

Table 2: Isothermal Constants Click here to view table

Effect on pH

The adsorption capacity of Congo Red as a function of pH. It was observed that percentage removal of Congo Red is maximum of pH = 8 and then decrease with increase of pH.

Effect on Sorbent Dosage

Batch sorption studies were performed to determine the effect of sorbent dosage on Congo red removal. The percent removal increase rapidly and reaches about 95% For 100% removal of the Congo Red the dosage required is 300mg/50ml for the initial concentration of 50mg/L at pH = 8.0

Sorption Kinetics

The rate of adsorption of Congo Red onFerronia elephantumFruit Shell was studied byusing the first order kinetic model, Pseudo second order kinetic and Elovich models are used to test the experiment data.

First Order Kinetics

The rate of adsorption of Congo Red onFerronia elephantumFruit Shell was studied byusing the first order rate equation proposed by Lagergren. It is found that as initial dye concentration increase Lagergren rate constant decrease, This indicates that, adsorption does not follow the 1^storder kinetics.

Table 3: Thermodynamics Parameters Click here to view table

Pseudo Second Order Models

伪二阶模型表明,速率常数ant K₂is almost constant at different initial concentration which is shown in Table 1. this indicate that adsorption of Congo Red. OnFerroniaelephantumFruit Shell obey the 2^ndorder kinetics.Also the concentration of Congo Red increasing from 20mg/L to 60mg/L equilibrium sorption capacity q^eincrease.

Elovich Model

Adsorption of Congo Red anFerroniaelephantumFruit Shell are shown. A linearrelationship is obtained betⁿthe amount of Congo Red, Adsorbed q_tand Int. from the table 1, show that value∝and β varied as a function fo Congo Red concentration. As the concentration of Congo Red increase from 20mg/L. to 6mg/L. value of∝increase and β decrease. This favored the adsorption phenomenon.

Isotherm Modeling

Langmuir Adsorption Isotherm

The Langmuir sorption isotherm is shown in Table 2. Q^ovalues found be comparable with commercial activated carbon. Value of R^Llies between 0 and 1 indicate the favorable adsorption. It indicates the applicability of Langmuir adsorption isotherm. The calculated value r²confirm the applicability of Langmuir adsorption isotherm.

Freundlich Adsorption isotherm

Freundlich plot for the adsorption of Congo Red onFerronia elephantumFruit Shell is given in table 2. it was that the values of adsorption intensity 1/n <1, reveal the applicability of freundlich adsorption.

Thermodynamics Parameters

The influence of temperature upon the adsorption rate was investigated at 30°C 40°C and 50°C it is observed that mass of the Congo Red. Adsorbed per unit mass of adsorbent increase with increasing temperature. The negative value of free energy change G indicates the feasibility and spontaneous nature of adsorption of Congo Red.

H value suggests endothermic nature of Congo Red onFerronia elephantumFruit Shell. Positive value is Sis due to increase randomness during adsorption of Congo Red.

Conclusion