Ijraset Journal For Research in Applied Science and Engineering Technology
Authors: Vidya Bhushan, Asit Singh
DOI Link: https://doi.org/10.22214/ijraset.2022.46893
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Analysis of one dimensional solute transport of Cadmium in Dudhi region of Sonebhadra district Uttar Pradesh is presented in this study. To understand and predict the behavior of solute transport within the ground water simulation of solute transport is necessary and helpful to develop remediation for this pollution. In this study the transport behavior of contaminant transport incorporating with non-linear sorption (Freundlich) for different adsorption capacities (Freundlich adsorption coefficient) (Kf) and adsorption intensity (Freundlich exponent) (a) is numerically simulated using MT3DMS. MT3DMS is a well know simulator for simulation of solute transport problems. For the study multiple simulations were conducted with several values of Kf and a, to study the trend analysis of breakthrough curves. For the visualization of the output of simulation and to plot the BTC the observation output files were imported to M.S. EXCEL and proceeded to plot the BTCs for trend analysis.
I. INTRODUCTION
Contamination of ground water is a major emerging challenge for us. Since we rely on groundwater for source of water in major parts of world, it must be entertained well. Whenever any foreign material or contamination finds it path down to the groundwater and joins the groundwater and pollutes water inside the earth aquifers is termed as Ground water contamination. In India the responsible contaminant for ground water pollution is generally identified are salinity, fluoride, nitrate, arsenic and other heavy metals. Trace of high levels fluoride above the acceptable limits of 1.5 ppm occur in around 14 states of our India. It is also reported that around 65 % of Indian rural areas are exposed to fluoride risk. Trace of high-level salinity is also reported from several states. High levels of arsenic has been also found in the Ganga basin belt of several districts of UP, Bihar and West Bengal.
To understand and predict the behaviors of solute transport within the ground water simulation of reactive contaminants is necessary and very helpful to develop remediation for the pollution. Simulation can also be useful to predict the concentration of contaminant in any particular time at any particular space. Simulation of solute transport is done by solving the ADE (Advective-dispersive differential equation) governing the transport mechanism with the help of computer programs and codes to get the study results and findings. It reduces our effort and save time as compared to other methods of solving ADE. In this current study for one dimensional solute transport with equilibrium-controlled sorption, MT3DMS is used for the simulation. A general procedure to the simulation of reactive solute transport with groundwater in porous media like soil is by assuming it to be driven by a linear sorption isotherm (Fetter, 1993).
A. Study Area
Geographically, the district is located between 23°52' and 24°55' N latitude and 82°30' to 83°33' E longitude. For the present work, two industrial clusters present in Dudhi region of SONBHADRA district, comprising of Obra (24°26'30.3'' – 24°48'41.01'' N and 82°57'41.20'' – 83°02'48.90'' E), Renukoot (24°11'17.20'' – 24°14'21.72'' N and 83°00'22.50'' – 83°03'39.10'' E) were selected. The study area is a hub for various industrial and commercial operations. The different industries present in the area are summarized as follows: Obra (Cluster A: Thermal Power Plant, Cement Factory, Sandstone–limestone Mining), Renukoot (Cluster B: Chloro-alkali Plant, Aluminum Smelting Plant and Hi-tech Carbon Limited). The southern part of Uttar Pradesh’s Sonbhadra District and the north-eastern part of Madhya Pradesh’s Singrauli District are popularly known as the ‘‘Energy capital of India’’. It is called so because of the presence of power grade coal reserves along with availability of water resources from Govind Ballabh Pant Sagar (G.B.P.S.) water reservoir (Rihand Dam). This provides an excellent location for other coal dependent industries like thermal power stations, aluminum smelting, cement industries, chloro-alkali industry, hi-tech carbon industry and other industrial and commercial operations adjacent to the coal mines (Khan et al. Khan. 2013). The surface and groundwater of Singrauli are severely contaminated due to direct pouring of fly ash slurry and leaching of toxic trace elements like As, Se, Hg, Cd and Pb from ash disposal pond of the power plant, making the water resources unfit for uses (Pandey et al. 2011).
II. METHODOLOGY
In this study the same problem is taken as illustrated in (Grove and Stollenwerk, 1984) considering the Freundlich & Langmuir isotherms. For our simulation MT3DMS was used and for creation of Input file all the steps were taken as directed in the MT3DMS user manual (Zheng et al., 2012).
A. Model parameters
The model parameters for the problem used for the simulation are same to that of (Grove and Stollenwerk, 1984) and they are illustrated below: Grid spacing (?x) = 0.16 cm, Dispersivity (αL) = 1 cm, Groundwater seepage velocity (v) = 0.1 cm/s, Porosity (θ) = 0.37, Bulk density (ρb) =1.587 g/cm3, Freundlich equilibrium constant (Kf), Freundlich sorption exponent (a), Concentration of source fluid Co = 0.05 mg/l, Duration of source pulse (to) = 160 seconds. For our study we will now see how the behavior of these breakthrough changes and what are the impacts on contaminant transport with the change in the Freundlich adsorption coefficient/ adsorption capacity (Kf) and Freundlich exponent constant/ adsorption intensity (a). All the other parameters are considered constant for proper analysis of adsorption phenomenon of soil for the heavy metals to get breakthrough curve.
The Freundlich equilibrium constant and Freundlich sorption exponent has been calculated experimentally for the soil of particular study area. The soil sample collected from the Dudhi region of Sonbhadra district was used to calculate the adsorption capacity and adsorption intensity of Cadmium, the 20(gm) soil of all the soil sample was put in oven in a crucible dish at 105° C for 3 hours. Thereafter soil was taken out of oven and crushed finely and made to pass via 0.5mm sieve mesh, the 10(ml) standard solution of cadmium was prepared which was later diluted 10 times for our experimental work. Then 10(gm) soil was mixed with 50(ml) of standard solution of cadmium which was later put in centrifuge at 250(rpm) for different time spans, after taking it out from centrifuge the sample was tested via Atomic absorption spectrometry to know the change in concentration of cadmium in the standard solution. The data obtained was later put through analysis via Origin pro software to get the data below for the simulation of one dimensional solute transport.
Above two data sets for two parameters were taken in consideration for the study and for each consideration the simulation was run separately and the outputs for each simulation for transport model were saved in separate folders to avoid the errors in the process of data visualization. Flow field is considered in steady state. Also, here Peclet number = 0.16, so that problem is not advection dominating. Constant-head B.C for flow model are taken at both by setting arbitrary hydraulic head to get desired Darcy flux.
It can be seen as with increase in Kf value the peak of the breakthrough curve is being delayed and attenuation in the peak value is observed, the peak of breakthrough curve shows the maximum relative concentration value of the contaminant in dissolved aqueous phase. Attenuated and delayed peak for higher Kf value is observed than that of lower Kf value. At Kf value 0.7 the peak value starts to fade away and relatively lower peak values or flat graph is observed. At Kf = 0.1 we can see the peak value i.e. maximum relative concentration (C/Co) in aqueous phase is above 3.5% of the initial released contaminant concentration and gradually decreasing with increased Kf also, when Kf is 1.0 it is observed that no peak is observed ,its comparatively a flat line.
The trend and pattern obtained in both comparative analysis curve is very similar as it can be seen as with increase in Kf value the peak of the breakthrough curve is being delayed and attenuation in the peak value is observed, the peak of breakthrough curve shows the maximum relative concentration value of the contaminant in dissolved aqueous phase. Attenuated and delayed peak for higher Kf value is observed than that of lower Kf value. At Kf value 0.3 the peak value starts to fade away and relatively lower peak values or flat graph is observed. But at Kf= 0.1 we can see the peak value i.e. maximum relative concentration (C/Co) in aqueous phase is nearly 2.5% of the initial released contaminant concentration and gradually decreasing with increased Kf. As seen with trends of breakthrough curve it has been observed that Kf make same impact to the breakthrough curve peak concentration and transport rate of contaminant but it more amount of contaminant is retarded when the a value is lower as compared to SET-1. It is observed that for same Kf values with a lower a value, the relative concertation of aqueous phase is higher than that of value with higher a. The solute migration rate and amount of solute migrated is lowered in each case as compared to previous set when a = 0.70.
Table-2: Comparison of Relative concentration values at a point 8 cm from the source of different Kf and a values.
Kf |
Maximum relative concentration (C/Co) at 8 cm distance from the source in aqueous dissolved phase within the simulation time. |
|
|
When, a = 0.5 |
When, a = 0.7 |
|
|
0.1 |
0.024 |
0.036 |
|
0.2 |
0.01 |
0.025 |
|
0.3 |
0.005 |
0.017 |
|
0.4 |
0.0029 |
0.013 |
|
0.5 |
0.0016 |
0.01 |
|
0.6 |
Negligible |
0.008 |
|
0.7 |
Negligible |
0.006 |
|
0.8 |
Reversal of curve is obtained |
0.0055 |
|
It can be seen clearly from the above table how the contaminant transport is being affected by these two parameters. C/Co is relative concentration in aqueous phase within the simulation time. Maximum relative concentration means the percentage of initial concentration of initial concentration input of dissolve aqueous phase at x = 0 and t = 0.
IV. ACKNOWLEDGEMENTS
The author thank Asst. Prof. Asit Singh CED, IET Lucknow, their holistic support and Ecomen Laboratories Pvt. Ltd. Lucknow, to providing the essential facilities for conducting this research.
The solute transport of Cadmium contaminated ground water in the Dudhi region of Sonbhadra district has been analyzed. This study indicates that with the increase in adsorption capacity (Kf) the concentration of contaminant dissolved in aqueous phase decrease since the more mass of contaminant is sorbed onto the solid phase. So the attenuation in peak relative concentration has been observed with increase in Kf values. This directly indicates that more the adsorption capacity of the soil slower the pollutant migration rate as the retention capacity of porous medium increases. The Freundlich exponent (a) or adsorption intensity has adverse effect on pollution migration, with high value of Freundlich exponent the concentration in aqueous phase increases as compared to the value of concentration in aqueous phase for a lower value of Freundlich exponent for same Adsorption capacity (Kf). Also, for same Kf at lower value of Freundlich exponent more retention of contaminant is observed also the peak is delayed but as the values of exponent increases the concentration in aqueous phase increases and the peak appears early since less retention of contaminant is offered by solid in this case. Hence the study gives the analysis of general behavior of soil with respect to Freundlich adsorption capacity and intensity, only using these parameters we could understand the change concentration of pollutants in aqueous phase.
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Copyright © 2022 Vidya Bhushan, Asit Singh. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
Paper Id : IJRASET46893
Publish Date : 2022-09-26
ISSN : 2321-9653
Publisher Name : IJRASET
DOI Link : Click Here