IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology
Rapid Industrialization specially in developing industry in recent years causes the heavy waste water pollution due to release of heavy metal into water stream.
Chromium and lead being carcinogenic in high dosage represent threat to human health as well as flora and fauna of various water bodies.
Pollution of river stream, lakes by Heavy metal industry poses a threat to human as well as aquatic flora and fauna.
Heavy metals like lead comes under toxic category while chromium though comes under micronutrient category its excess intake is toxic to human. In human body, metals enter through animal feed, green fodder, drinking water, pharmaceutical medicines, etc.
Excessive intake of chromium by humans leads to hepatic and renal damage, capillary damage, gastrointestinal irritation and central nervous system irritation.
Maximum acceptable concentration of lead and chromium in drinking water recommended by WHO is 0.05 mg/lit respectively.
Because of above said reasons it is very much required to remove these metals before discharge into surrounding.
Chemical precipitation, ion-exchange, electro flotation, membrane separation, reverse osmosis, electro dialysis, adsorption, biological separation are various types of removal method of heavy metals. Out of these methods we will review about adsorption.
Chromium is a metal that exists in several oxidation
• Chromium is a metal that exists in several oxidation or valence states, ranging from chromium (-II) to chromium (+VI).
• Chromium compounds are very stable in the trivalent state and occur naturally in this state in ores such as ferrochromite, or chromite ore.
• Chrome III is an essential nutrient for maintaining blood glucose levels
• The hexavalent, Cr(VI) or chromate, is the second most stable state. It rarely occurs naturally.
Rapid Industrialization specially in developing industry in recent years causes the heavy waste water pollution due to release of heavy metal into water stream.
Chromium and lead being carcinogenic in high dosage represent threat to human health as well as flora and fauna of various water bodies.
Pollution of river stream, lakes by Heavy metal industry poses a threat to human as well as aquatic flora and fauna.
Heavy metals like lead comes under toxic category while chromium though comes under micronutrient category its excess intake is toxic to human. In human body, metals enter through animal feed, green fodder, drinking water, pharmaceutical medicines, etc.
Excessive intake of chromium by humans leads to hepatic and renal damage, capillary damage, gastrointestinal irritation and central nervous system irritation.
Maximum acceptable concentration of lead and chromium in drinking water recommended by WHO is 0.05 mg/lit respectively.
Because of above said reasons it is very much required to remove these metals before discharge into surrounding.
Chemical precipitation, ion-exchange, electro flotation, membrane separation, reverse osmosis, electro dialysis, adsorption, biological separation are various types of removal method of heavy metals. Out of these methods we will review about adsorption.
Chromium is a metal that exists in several oxidation
• Chromium is a metal that exists in several oxidation or valence states, ranging from chromium (-II) to chromium (+VI).
• Chromium compounds are very stable in the trivalent state and occur naturally in this state in ores such as ferrochromite, or chromite ore.
• Chrome III is an essential nutrient for maintaining blood glucose levels
• The hexavalent, Cr(VI) or chromate, is the second most stable state. It rarely occurs naturally.
It is our group presentation.
topic on effluent treatment plant.
From this presentation, you will be able to know elaborately about the ETP. And i hope, this presentation will be very helpful for your presentation, related this topic.
Moreover, from this content you can easily understand how to management wastewater, wastewater treatment etc.
Quantitative measurements of water pollution, Water Analysis, Measurement of water quality by chemical and physical examination of water, BACTERIOLOGICAL EXAMINATION OF WATER,
Deals with the biological removal of nitrogen and phosphorus, Nitrification-denitrification removal of nitrogen, and Phosphate accumulating organisms and poly-hydroxibutirate in the phosphorus removal.
تعد هذه الأنظمة هى الأقوى تجاريا فى معالجة مياه صرف المنازل و الصرف الصحى فهى صديقة للبيئة و من خلالها يتم التخلص مباشرة من ملوثات المياه, المواد الملونه, الروائح و الكائنات الحية الدقيقة فهى تأتى لتحل محل الكلورين و تتفوق عليه بخفض إستخدام المواد الكيميائية الخطيرة فى عملية المعالجة, مولد الأوزون يلعب الدور الرئيسى فى إنتاج الأوزون من غاز الأكسجين فى مكان التشغيل
http://rheoserve.com/index.html#portfolio
Biochemical Oxygen Demand and its Industrial SignificanceAdnan Murad Bhayo
BOD is the amount of dissolved oxygen needed by aerobic biological organism in a body of water to breakdown organic material present in a given water sample at certain temperature over a specific time period .
Most of Bacteria in the aquatic columns are aerobic. Escherichia coli, Bacillus subtilis, Vibrio cholera.
Atmosphere contains 21% oxygen (210000 mg/dm3)
Higher the temperature of water higher will be the rate of respiration. So, concentration of oxygen decreases.
Many Animal species can grow and reproduce normally when dissolved oxygen level is ~ 5.0 mg/L.
HYPOXIA: When dissolve oxygen content below 3.0 mg/L. Many Species move elsewhere and immobile species may die
ANOXIA: When dissolve oxygen content below 0.5 mg/L. All aerobic species will die
Fertilizer contains Nitrate contributes to high BOD
Phosphate present in Soap and detergent that enhances the growth of algal blooms. As a result depletion of oxygen occur.
In a body of water with large amount of decaying organic material , the dissolved oxygen level may drop by 90 %, this would represent High BOD
In a body of water with small amount of decaying organic material , the dissolved oxygen level may drop by 10 %, this would represent Low BOD
ANALYSIS OF BOD OF WATER
Use glass bottles having 60 mL or greater capacity. Take samples of water.
Turn on the constant temperature chamber to allow the
controlled temperature to stabilize at 20°C ±1°C.
Record the DO level (ppm) of one immediately.
Place water sample in an incubator in complete darkness at 20 C for 5 days. Exclude all light to prevent possibility of photosynthetic production of DO
If don't have an incubator, wrap the water sample bottle in aluminum foil or black electrical tape and store in a dark place at room temperature (20o C or 68 °F).
DILUTION OF SAMPLE
Most relatively unpolluted streams have a BOD5 that ranges from 1 to 8 mg/L
Dilution is necessary when the amount of DO consumed by microorganisms is greater than the amount of DO available in the air-saturated.
If the BOD5 value of a sample is less than 7 mg/L, sample dilution is not needed.
The DO concentration after 5 days must be at least 1 mg/L and at least 2 mg/L lower in concentration than the initial DO
(American Public Health Association and others, 1995).
BOD of the dilution water is less than 0.2 mg/L.
Discard dilution water if there is any sign of biological growth.
pH of the dilution water needs to be maintained in a range suitable for bacterial growth
Bacterial growth is very good between 6.5 to 7.5
Sulfuric acid or sodium hydroxide may need to be added to the dilution water to lower or raise the pH, respectively.
CALCULATION:
The general equation for the determination of a BOD5 value is:
BOD = D1-D2/P
Where
D1 = initial DO of the sample,
D2 = final DO of the sample after 5 days, and
P = decimal volumetric fraction of sample used.
If 100 mL of sample a
Generally soaps create foam in water, but in present of some materials the foam creation is reduced and need more soap for producing foam, and this condition of water is called water hardness.
The presence of Calcium, Magnesium salt i.e. bicarbonates, sulphates, chloride in water is called causes of hardness of water. The water which contains these salts is called hard water. Hard water does not easily form lather with soap as the salt of Calcium and Magnesium react with soap to form insoluble organic salts.
It is our group presentation.
topic on effluent treatment plant.
From this presentation, you will be able to know elaborately about the ETP. And i hope, this presentation will be very helpful for your presentation, related this topic.
Moreover, from this content you can easily understand how to management wastewater, wastewater treatment etc.
Quantitative measurements of water pollution, Water Analysis, Measurement of water quality by chemical and physical examination of water, BACTERIOLOGICAL EXAMINATION OF WATER,
Deals with the biological removal of nitrogen and phosphorus, Nitrification-denitrification removal of nitrogen, and Phosphate accumulating organisms and poly-hydroxibutirate in the phosphorus removal.
تعد هذه الأنظمة هى الأقوى تجاريا فى معالجة مياه صرف المنازل و الصرف الصحى فهى صديقة للبيئة و من خلالها يتم التخلص مباشرة من ملوثات المياه, المواد الملونه, الروائح و الكائنات الحية الدقيقة فهى تأتى لتحل محل الكلورين و تتفوق عليه بخفض إستخدام المواد الكيميائية الخطيرة فى عملية المعالجة, مولد الأوزون يلعب الدور الرئيسى فى إنتاج الأوزون من غاز الأكسجين فى مكان التشغيل
http://rheoserve.com/index.html#portfolio
Biochemical Oxygen Demand and its Industrial SignificanceAdnan Murad Bhayo
BOD is the amount of dissolved oxygen needed by aerobic biological organism in a body of water to breakdown organic material present in a given water sample at certain temperature over a specific time period .
Most of Bacteria in the aquatic columns are aerobic. Escherichia coli, Bacillus subtilis, Vibrio cholera.
Atmosphere contains 21% oxygen (210000 mg/dm3)
Higher the temperature of water higher will be the rate of respiration. So, concentration of oxygen decreases.
Many Animal species can grow and reproduce normally when dissolved oxygen level is ~ 5.0 mg/L.
HYPOXIA: When dissolve oxygen content below 3.0 mg/L. Many Species move elsewhere and immobile species may die
ANOXIA: When dissolve oxygen content below 0.5 mg/L. All aerobic species will die
Fertilizer contains Nitrate contributes to high BOD
Phosphate present in Soap and detergent that enhances the growth of algal blooms. As a result depletion of oxygen occur.
In a body of water with large amount of decaying organic material , the dissolved oxygen level may drop by 90 %, this would represent High BOD
In a body of water with small amount of decaying organic material , the dissolved oxygen level may drop by 10 %, this would represent Low BOD
ANALYSIS OF BOD OF WATER
Use glass bottles having 60 mL or greater capacity. Take samples of water.
Turn on the constant temperature chamber to allow the
controlled temperature to stabilize at 20°C ±1°C.
Record the DO level (ppm) of one immediately.
Place water sample in an incubator in complete darkness at 20 C for 5 days. Exclude all light to prevent possibility of photosynthetic production of DO
If don't have an incubator, wrap the water sample bottle in aluminum foil or black electrical tape and store in a dark place at room temperature (20o C or 68 °F).
DILUTION OF SAMPLE
Most relatively unpolluted streams have a BOD5 that ranges from 1 to 8 mg/L
Dilution is necessary when the amount of DO consumed by microorganisms is greater than the amount of DO available in the air-saturated.
If the BOD5 value of a sample is less than 7 mg/L, sample dilution is not needed.
The DO concentration after 5 days must be at least 1 mg/L and at least 2 mg/L lower in concentration than the initial DO
(American Public Health Association and others, 1995).
BOD of the dilution water is less than 0.2 mg/L.
Discard dilution water if there is any sign of biological growth.
pH of the dilution water needs to be maintained in a range suitable for bacterial growth
Bacterial growth is very good between 6.5 to 7.5
Sulfuric acid or sodium hydroxide may need to be added to the dilution water to lower or raise the pH, respectively.
CALCULATION:
The general equation for the determination of a BOD5 value is:
BOD = D1-D2/P
Where
D1 = initial DO of the sample,
D2 = final DO of the sample after 5 days, and
P = decimal volumetric fraction of sample used.
If 100 mL of sample a
Generally soaps create foam in water, but in present of some materials the foam creation is reduced and need more soap for producing foam, and this condition of water is called water hardness.
The presence of Calcium, Magnesium salt i.e. bicarbonates, sulphates, chloride in water is called causes of hardness of water. The water which contains these salts is called hard water. Hard water does not easily form lather with soap as the salt of Calcium and Magnesium react with soap to form insoluble organic salts.
Asopos is a river that rises in Viotia and discharges into the South Euboea Gulf in Greece, about 60 km north of Athens.Forty years ago, in 1969, through a Presidential Decree, issued by the Military Government (Junta) that ruled Greece at the time, Asopos was proclaimed a Processed Industrial Waste receiver. The river the Ancient Greeks worshiped as a god (Asopos was Poseidon’s son) was unfortunate enough to run through areas that turn out almost 20% of Greece’s total industrial production.
Today, Asopos’ waters receive waste from hundreds of industries, situated at a nearby Industrial area. Nevertheless, only a slight amount of water reaches its estuary. The texture of the soil absorbs the largest part of the water, including all the industrial waste, and spreads it to the whole underground water. This results to a possibly irreversible pollution of a huge area with various waste, amongst which heavy metals, including the renowned due to recent publicity, Hexavalent Chromium. This is an element that causes cancer and/or mutations.
The water from the springs, the fountains and the drillings in this whole area is no longer suitable for any human use, neither drinking nor cooking, bathing and washing clothes, not even for watering plants!
Hundreds of thousands of residents inhabit the area, especially during the summer. All these people have been consuming water for years, without ever having been officially informed of the hazards, until early this summer (2007).
Recently, after 3 adjournments and a delay of 6 years, a trial took place. 10 out of 18 defendants were acquitted due to misrecorded data! For those convicted, the highest punishment was the ridiculous amount of EURO 5000 as a fine!
Various reportings have revealed that some industries open up drillings and convey inside all their waste- directly into the underground water!
We request that the Greek Government, the Greek Parliament, the European Community Authorities and every other qualified service take all necessary measures and actions in order to insure the restoration of Asopos river, as well as the indemnification of all the problems (health related, economical, environmental) the residents are facing due to this situation.
Project Management Challenges in an Effluent Treatment Plant Construction PRABHASH GOKARN
Tata Steel operates India’s largest chromite mines at the Sukinda Valley in Odisha producing chrome ore which is subsequently converted it to Ferro Chrome and sold to customers across the world. A large quantity of water, generated during mining and due to rainfall, needs to be handled during the mining operations. Chrome Ore mainly contains tri-valent Chromic oxide and a very small fraction of hexavalent di-chromate. Water coming in contact with chromium ore preferentially leaches out soluble hexavalent chromium from the ore body, as a result, water from the mine contains 0.2 – 4 mg/l of hexavalent chromium against a safe limit of 0.005 mg/l for human consumption; requiring all water to be treated before its release from the mines. Thus, Tata Steel is setting up an effluent plant at Sukinda with a capacity of 108 million litres/day; perhaps one of the largest in the region; which will be complete by end June 2015.
Worked with different particle size of coffee as an antioxidant to find which size creates a reaction at a faster rate in the reduction of Chromium IV to Chromium III.
Removal of heavy metal lead (pb) from electrochemical industry waste water us...eSAT Journals
Abstract Electrochemical industries generates a wastewater that has a potential hazard for our environment as it contains various heavy metals such as Lead, Cadmium, Nickel etc. If this wastewater left untreated, will pollute soil and water resources. Out of the above heavy metals, in this project work, only removal of Lead (Pb) from electrochemical industrial wastewater has been investigated by using low cost adsorbent such as charcoal along with coconut shell powder as a natural adsorbent. The project is a bench scale experimental type i.e. Batch mode technique and analyses have performed by using different amounts of adsorbent in solutions with different concentrations of Lead metal. Beside the effect of various amounts of adsorbent used in adsorption efficiency experiments has been investigated. Result indicates that the maximum removal efficiency for Lead is about 94% by using 0.25 gm/L amount of activated coconut shell carbon powder (ACSCP) and charcoal powder (ACP) mixed in equal amount for particular pH and contact time. Keywords: Adsorption, batch mode technique, battery industry waste water, Coconut shell powder, Charcoal carbon powder, Economic, Heavy Metal.
Assessment of heavy metal concentrations in surface water sourcesManoj Kumar Tiwari
Rapid industrialisation and resulting industrial solid waste from power plants and integrated iron and steel industries, have
imposed an enormous environmental pressure on water resources of Chhattisgarh, a state in Central India. Rural population living
nearby the study area is mainly depended on the available surface water in the form of lakes or pond in their vicinity. Therefore it is
necessary to look after the surface water through leachate pollution caused by dumping and disposal of industrial solid waste. In the
present study, ten surface water samples each for pre monsoon and post monsoon were collected for analysis from the surrounding
areas of a major industrial region of Chhattisgarh. The AAS analysis of the surface water samples shows higher concentration of
certain heavy metals above the permissible limits. In the pre monsoon samples the metals Mn and Cr resulted higher concentration
and at the same time metals; Cu, Fe and Pb resulted in lower concentrations. Similarly, for the post monsoon samples, Mn, Cr and Fe
found with higher concentration, while Cu and Pb resulted with lower concentration. The high amount of heavy metals were found
in the analyzed samples shows that there is a real risk for population living in the nearby areas of the industrial region of
Chhattisgarh. Therefore a huge amount of industrial wastes produced needs a proper disposal. Unscientific and poorly-managed
disposal of industrial solid wastes containing heavy metals needs remediation before discharging into the environment.
Suitability of leaching test methods for fly ash and slag a reviewManoj Kumar Tiwari
Fly ash and slag leachate pollution can be of great environmental concern due to generation
of these wastes in huge quantities from their respective industrial units, mainly coalbased
thermal power plants and iron and steel plants. For simulation of natural leaching in
laboratory, various leaching methods are available, but selection of a method that can
exactly simulate the real-life scenario for accurate estimation of various pollutants is
challenging; particularly, the heavy metals present and impact due to reuse or disposal of
these wastes. For choosing the most suitable leaching method according to specific situation,
one must primarily consider the chemical and physical properties of wastes, the
composition of the source, age of waste disposal, and the climatic conditions of the
disposal area. Since these factors may not be specified, a variety of leaching methods with
relevant equipment have been proposed by researchers; that are based on their required
information to particular conditions in absence of a prescribed protocol and non standardization
of equipment. The present review is an attempt to investigate the suitable
leaching method for coal fly ash and slag.
Kinetic, thermodynamic and equilibrium studies on removal of hexavalent chrom...Ratnakaram Venkata Nadh
Removal of Cr(VI) by biosorption on two agro waste materials, casuarinas fruit powder (CFP) and sorghum
stem powder (SSP), has been investigated. The prepared adsorbent materials were characterized by SEM, EDX,
FTIR and BET. These biomaterials effectively removed Cr(VI) with a maximum removal of 93.35% and 63.75% using
15 gL−1 and 5 gL−1 of CFP and SSP, respectively, at 60 oC with 20mgL−1 initial Cr(VI) concentration in solution. In both
cases of adsorbents, kinetic data of adsorption fitted well in pseudo-second-order in terms of correlation coefficient
(R2). This helps in proposing the process of adsorption as chemical coordination, which is correlated with the thermodynamic
study results conducted at different values of temperature. Langmuir, Freundlich and D-R models were evaluated
for description of metal sorption isotherms. Values of coefficients of intra-particle diffusion and mass transfer have
also been determined at different values of temperature.
IRJET-Fixed Bed Column Study for Removal of Hexavalent Chromium From Aqueous ...IRJET Journal
Subitha V , Vanathi M " Fixed Bed Column Study for Removal of Hexavalent Chromium From Aqueous Solution by using Denolix Regia Pods (Flamboyant Pods) ",International Research Journal of Engineering and Technology (IRJET), Volume2,issue-01 April 2015.e-ISSN:2395-0056, p-ISSN:2395-0072. www.irjet.net .published by Fast Track Publications
Abstract
The contamination of chromium (VI) in water posed severe health issues throughout the world. Several methods are available to remove chromium from aqueous environment but they are not feasible in all places and conditions due to various reasons. Some of the processes are electrochemical precipitation, ion exchange, solvent extraction, reverse osmosis, etc from contaminated water. The development of low cost adsorbent is essential for benefit of the society. In present work, the study on performance of low cost adsorbent such as Denolix regia pods were used in removal of toxic heavy metal hexavalent chromium from aqueous solution was performed. The adsorbent material adopted was found to be efficient media for removal of Chromium (VI) using fixed bed column which was having the total column height of 40cm, diameter of 7cm and a bed height of 30cm. The removal percentage has achieved 49% at optimum condition with the initial concentration of Cr (VI) as 500 mg/ml. The extend of adsorption was investigated as a function of pH, contact time, adsorbent dosage and adsorption of Cr (VI) was found to be time and concentration dependent.
Removal of Lead Ion Using Maize Cob as a BioadsorbentIJERA Editor
The intensification of industrial activity and environmental stress greatly contributes to the significant rise of
heavy metal pollution in water resources making threats on terrestrial and aquatic life. The toxicity of metal
pollution is slow and interminable, as these metal ions are non bio-degradable. The most appropriate solution for
controlling the biogeochemistry of metal contaminants is sorption technique, to produce high quality treated
effluents from polluted wastewater. Maize cob readily available was used as sorbent for the removal of lead ions
from aqueous media. Adsorption studies were performed by batch experiments as a function of process
parameters such as sorption 500ppm,2.5g, 400minutes, 400 rpm and 5 PH. Concentration, Dosage, time, rpm,
and pH. I have found that the optimized parameters are Freundlich model fits best with the experimental
equilibrium data among the three tested adsorption isotherm models. The kinetic data correlated well with the
Lagergren first order kinetic model for the adsorption studies of lead using maize cob. It was concluded that
adsorbent prepared from maize cob as to be a favorable adsorbent and easily available to remove the heavy
metal lead (II) is 95 % and can be used for the treatment of heavy metals in wastewater.
Metal ion and contaminant sorption onto aluminium oxide-based materials: A re...Dr. Md. Aminul Islam
Nanosized aluminium oxides (NAOs) are an important class of minerals widely found in soil, sediment, aquifer,
and aquatic environments. Over the decades, these minerals have been explored as sorbents for the removal of
wastewater contaminated with metal ions, anions, organic dyes, humic substances, phenolic compounds, pesticides, and pharmaceuticals from contaminated wastewater. This review summarizes the reported research of
NAOs as sorbents and provides details on their sorption capacities including maximum removal capacity under
various experimental conditions. Information on the composition, synthesis, characterization and experimental
parameters together with sorption mechanisms is provided. A compilation of such information is not currently
available and so this review should enable workers in the area to make more informed choices on suitable
sorbents for large-scale environmental samples and be able to develop more efficient processes for environmental pollutant clean-up
Statistical optimization of adsorption variables for biosorption of chromium ...eSAT Publishing House
IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology
Agricultural by-Products/Waste as Dye and Metal Ions Adsorbents: A Reviewresearchinventy
A major treat to the comfort of human life has been imposed by the unintentional and great increased industrialization and urbanization. Their generations and land disposals of huge amounts of toxic materials and pollutants have contributed in contaminating our environment frighteningly. Synthetic dyes (SD) and heavy metals (HM) are becoming increasingly prevalent in soil and surface water environments, as the most dangerous pollutants. They are present a great concern worldwide, due to their toxicity to many life forms. Environment-friendly utilization of agricultural by-products/waste materials either as raw materials or in production of the so-called activated carbons (AC) is an important issue. Because, it is apparent from our literature review that the main factors characterizing these materials are the inexpensiveness, the local availability and their efficiencies in removal of heavy metals and dyes from contaminated water. A number of different agricultural by-product/wastes as renewable and potential sources for green adsorbent production has been listed in this review. Additionally, the paper has provided the reader with an overview of a number of case studies which were conducted by scientists and researchers. These case studies have pointed out to the efficient removal of SD/HM ions from aqueous solutions by the agricultural by-products/wastes in the form of a raw material, spent tea leaves (STL), spent coffee ground(SCG), and rice husk (RH) wastes were selected as a good examples. Besides, the efficient removal of such ions by AC produced from the same raw materials has been also reviewed. Both kinds are widely used adsorbents in the treatment of wastewaters. High adsorption capacity, cost effectiveness, and environmentally friendly, and their abundance in nature are the important factors which explain why the adsorbent materials derived from an agricultural by-product/wastes is economical for the removal of dye and metal ions from contaminated water. Comparison of different technologies of wastewater treatment especially heavy metals and dyes were also listed in this review
Understanding Inductive Bias in Machine LearningSUTEJAS
This presentation explores the concept of inductive bias in machine learning. It explains how algorithms come with built-in assumptions and preferences that guide the learning process. You'll learn about the different types of inductive bias and how they can impact the performance and generalizability of machine learning models.
The presentation also covers the positive and negative aspects of inductive bias, along with strategies for mitigating potential drawbacks. We'll explore examples of how bias manifests in algorithms like neural networks and decision trees.
By understanding inductive bias, you can gain valuable insights into how machine learning models work and make informed decisions when building and deploying them.
Harnessing WebAssembly for Real-time Stateless Streaming PipelinesChristina Lin
Traditionally, dealing with real-time data pipelines has involved significant overhead, even for straightforward tasks like data transformation or masking. However, in this talk, we’ll venture into the dynamic realm of WebAssembly (WASM) and discover how it can revolutionize the creation of stateless streaming pipelines within a Kafka (Redpanda) broker. These pipelines are adept at managing low-latency, high-data-volume scenarios.
Low power architecture of logic gates using adiabatic techniquesnooriasukmaningtyas
The growing significance of portable systems to limit power consumption in ultra-large-scale-integration chips of very high density, has recently led to rapid and inventive progresses in low-power design. The most effective technique is adiabatic logic circuit design in energy-efficient hardware. This paper presents two adiabatic approaches for the design of low power circuits, modified positive feedback adiabatic logic (modified PFAL) and the other is direct current diode based positive feedback adiabatic logic (DC-DB PFAL). Logic gates are the preliminary components in any digital circuit design. By improving the performance of basic gates, one can improvise the whole system performance. In this paper proposed circuit design of the low power architecture of OR/NOR, AND/NAND, and XOR/XNOR gates are presented using the said approaches and their results are analyzed for powerdissipation, delay, power-delay-product and rise time and compared with the other adiabatic techniques along with the conventional complementary metal oxide semiconductor (CMOS) designs reported in the literature. It has been found that the designs with DC-DB PFAL technique outperform with the percentage improvement of 65% for NOR gate and 7% for NAND gate and 34% for XNOR gate over the modified PFAL techniques at 10 MHz respectively.
6th International Conference on Machine Learning & Applications (CMLA 2024)ClaraZara1
6th International Conference on Machine Learning & Applications (CMLA 2024) will provide an excellent international forum for sharing knowledge and results in theory, methodology and applications of on Machine Learning & Applications.
Using recycled concrete aggregates (RCA) for pavements is crucial to achieving sustainability. Implementing RCA for new pavement can minimize carbon footprint, conserve natural resources, reduce harmful emissions, and lower life cycle costs. Compared to natural aggregate (NA), RCA pavement has fewer comprehensive studies and sustainability assessments.
Literature Review Basics and Understanding Reference Management.pptxDr Ramhari Poudyal
Three-day training on academic research focuses on analytical tools at United Technical College, supported by the University Grant Commission, Nepal. 24-26 May 2024
5214-1693458878915-Unit 6 2023 to 2024 academic year assignment (AutoRecovere...
Adsorption of cr (vi) from aqueous environment using neem leaves powder
1. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
_______________________________________________________________________________________
Volume: 03 Special Issue: 09 | NCETCE-2014 | June-2014, Available @ http://www.ijret.org 25
ADSORPTION OF CR-(VI) FROM AQUEOUS ENVIRONMENT USING NEEM LEAVES POWDER Rahul N. Jain1, S. B. Patil2, D. S. Lal3 1ME (Environmental Engineering), Department of Civil Engineering, S.S.B.T.’s COET, Bambhori- Jalgaon, Maharashtra 2Assistant Professor, Department of Civil Engineering, S.S.B.T.’s COET, Bambhori- Jalgaon, Maharashtra 3Assistant Professor, Department of Civil Engineering, RCPIT, Shirpur Maharashtra Abstract This study is aimed at utilizing Neem Leaves powder as low cost adsorbent material for removal of Cr-(VI) from aqueous solution. Adsorption is an important process used for removal of colour, odour, turbidity, metal ions and reduction of COD. In adsorption, the solute present in dilute concentration in liquid or gas phase is extracted by contacting with suitable solid adsorbent so that the transfer of the component first takes place on the surface of solid and then into the pore of the solid. Neem Leaves powder Adsorbent used in present study is prepared at Laboratory scale which is very effective to remove chromium from its aqueous solution. This study describes the detailed experimental procedure to obtain Adsorption Equilibrium and the Effect of various parameters such pH, agitation time, initial metal ion concentration & adsorbent doses on batch technique. Keywords: Hexa-valent Chromium, Neem Leaf Powder, Adsorption, Batch process, UV-Vis Spectrophotometer.
---------------------------------------------------------------------***--------------------------------------------------------------------- 1. INTRODUCTION Due to increased urbanization as well as industrialization, generation of large amount of toxic contaminants especially heavy metals are to be produced. These received widespread attention because of their persistent nature, toxicity, carcinogenicity or mutagenicity even at very low concentrations. Among these heavy metals chromium is more toxic. Chromium ion in industrial wastewater occurs in two forms; trivalent Cr3+ and hexa-valent Cr6+. The increase in concentration levels of heavy metals in the environment particularly in water is a cause for concern. The major contributor for this rise in the concentration level is in the extensive development of heavy & manufacturing industries that uses metals & related compounds. Discharge of treated industrial wastewater containing metal ions such as nickel, lead, copper, zinc, chromium and aluminium are common in nearby water sources like river. This may result in affecting the quality of aquatic & human life. Therefore, the removal of heavy metals from wastewater is essential. 1.1 Sources of Cr-(VI)
Main sources of chromium-(VI) pollution are 1) Mining industry 2) Leather Tanning industry 3) Cement industry 4) Electroplating industry 5) Production of steel and other metal alloys industry 6) Photographic material and corrosive paints 7) Nuclear Power-plants 8) Textile industries. Chromium is the naturally occurring element which is found in the volcanic-ash, volcanic-gases, soil and rocks (Abbasi and Soni, 1985). Chrome plating, leather tanning, combustion of natural fuels (gas, oil, coal), catalysts, fertilizers, dye manufacturing industries, battery making, printers, emission from cooling towers, air condensers and incineration of sewage sludge, municipal refuse and other solid wastes, are the anthropogenic sources of chromium emission in the environment (Faisal and Hasnain, 2004). More than 1, 70,000 metric tonnes of chromium wastes are discharged annually in environment as a result of industrial and manufacturing activities (Abassi et al, 1998). The leather industry is the major cause for the high influx of chromium to the biosphere, accounting for 40% of the total industrial use (Baruhart, 1997). Chromium exists in food, air, water and soil, mostly in the trivalent form. It is only as a result of human activities that substantial amounts of Cr- (VI) become present in environment. Cr-(III) is comparatively insoluble while Cr-(VI) is quite soluble and is readily leached from soil to groundwater or surface water. 1.2 Cr-(VI) Metal Impacts on Health The hexa-valent form is 500 times more toxic than the trivalent (Kowalski, 1994). It is toxic to micro-organisms, plants, animals and humans. Human toxicity includes lung cancer as well as kidney, liver, and gastric damage (US Department of Health and Human Services, 1991; Cieslak- Golonka, 1995). The tanning process is one of the largest polluters of chromium all over the world. Most of the tanneries in India adopt the chromium tanning process because of its processing speed, low costs, and light color of leather and greater stability of the resulting leather.
In the chromium tanning process, the leather takes up only 60–80% of applied chromium, and the rest is usually discharged into the sewage system causing serious environmental impact. Chromium ion in liquid tanning wastes occurs mainly in trivalent form, which gets further oxidized to hexa-valent Cr-(VI) form, due to the presence of
2. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
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Volume: 03 Special Issue: 09 | NCETCE-2014 | June-2014, Available @ http://www.ijret.org 26
organics. For nearly a century, heavy metal-laden wastewater discharged from industries, are posing a serious challenge to environmental, public health, scientists and Engineers. Numerous investigations on effects of heavy metal on environment and human have been carried out. Unlike organic pollutants, which in most cases can be destroyed, heavy metal discharged into environment tend to persist indefinitely, circularly and eventually throughout the food chain thus causing a series of threats to human and organisms (Cooke et al, 1990; Deniseger et al, 1990;Sag et al, 1995b; Chua and Hua, 1996). Even if the heavy metal ions in water present in dilute, undetectable quantities, their recalcitrance and consequent persistence in water bodies imply that through natural processes, such as biomagnification, concentrations may become elevated to such an extent that they begin exhibiting toxic characteristics (Atkinson et al, 1998). 1.3 Permissible Limits of Cr-(VI) The maximum levels permitted in waste-water are 5 mg/L for trivalent chromium and 0.05 mg/L for hexavalent chromium (Acar and Malkoc, 2004). With this limit, it is essential for industries to treat their effluents to reduce the Cr to acceptable levels. The Ministry of Environment and Forest (MOEF), Government of India has set mini-mal national standards (MINAS) of 0.1 mg/L for safe discharge of effluent containing Cr(VI) in surface water and in potable water is 0.05 mg/L . 2. BATCH ADSORPTION EXPERIMENT ANALYSIS Study reports the use of Neem leaves powder as a low cost adsorbent and investigation of various parameters such as pH, metal ion concentration, adsorbent dose and contact time by using batch adsorption technique.
1. Using Neem Leaves adsorbents in 250 ml stopper conical flask containing 100 ml of Cr (VI) solution batch adsorption were carried out. pH of the solution adjusted by adding H2SO4 or NaOH or HCL solution as required. Then the flasks were shaken for the desired contact time.
2. The time required to reach the equilibrium was estimated by withdrawing conical flask containing treated solution at regular intervals of time. The content flasks were filtered through filter paper (Whatman no.1).
3. UV-visible Spectrophotometer employed to determine the remaining Cr (VI) concentration in the sample solution using 1, 5-diphenylcarbazide method as laid down in standard methods for examination of water and wastewater, APHA, AWWA, WEF, 1998 edition.
4. The removal percentage (R %) of chromium was calculated for each run by following expression:
R (%) = [(Ci – Ce)/ Ci] x 100 Where,
Ci- initial concentration of chromium in the solution. Ce- final concentration of chromium in the solution
3. CHEMICALS & INSTRUMENTS
3.1 Chemicals/ Materials Required
1. Distilled water/ De-ionized water
2. Standard buffer solution-For pH meter calibration
3. H2SO4 / NaOH/ HCL- For adjusting pH of Solution
4. 1,5-Diphenyl Carbazide (DPC)
5. Neem leaves
6. Potassium chromate/ Potassium dichromate
3.2 Equipments Required
pH meter/ pH paper
UV-VIS Spectrophotometer
250 ml Stopper Conical flask
What-man Filter Paper
Muffle furnace
Digital Weighing Balance
Glass Beakers
Measuring Cylinders
Burettes & Pipettes
4. EXPERIMENTAL METHOD 4.1 Adsorbent Preparation 1. Neem leaves were collected from local nearby area & washed with several times to remove dust particles. 2. Adsorbents were oven dried to remove the adherent moisture content. 3. Dried leaves were crushed with domestic mixture. 4. Adsorbent in a powder form was obtained. After drying, adsorbent sieved to obtain particle size of 250 - 350 μm prior to being used for adsorption studies.
4.2 Preparation of Standard CR-(VI) Solution The stock solution containing 1000 mg/L of Cr-(VI) was prepared by dissolving 2.828 g of A. R. grade potassium dichromate(K2Cr2O7) in 1000 ml double-distilled water. Required initial concentrations of Cr-(VI) standards were prepared by appropriate dilution of the stock Cr-(VI) solution.
3. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
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Volume: 03 Special Issue: 09 | NCETCE-2014 | June-2014, Available @ http://www.ijret.org 27
4.3 Determination of Maximum Absorptive Wavelength for Operation Absorbances were recorded at different wavelengths by using UV-vis Spectrophotometer. Up to certain wavelength absorption increases and then decreases, at the point where the % absorption is maximum that point is considered as maximum wavelength of operation. 4.4 Construction of Standard Calibration Curve for Chromium For this purpose, solution of chromium of different concentrations were prepared and their absorbance recorded by using UV Spectrophotometer. The Spectrophotometer is set to Zero absorbance with the reference solution (Distilled water) and then the absorbance of standard solution was measured. With the help of these Reading standard calibration curve plotted between Absorbance and standard chromium solution of various concentrations. Table-1 Standard Calibration Curve For Cr+6
Concentration (ppm)
Absorbance
Concentration (ppm)
Absorbance 1 0.1 6 0.5
2
0.19
7
0.64 3 0.32 8 0.7
4
0.38
9
0.87 5 0.48 10 0.99
Fig. 1- Standard Calibration Curve For Cr+6 Graph shows as chromium concentration increases absorbance also increases. Curve to be used as a standard curve for determining concentration of an unknown Cr solution by observing Absorbance with the help of UV-VIS Spectrophotometer.
5.0 RESULTS & DISCUSSIONS
5.1 Effect of pH
Fig.2- Effect of pH on removal of Cr (VI) ion pH affects the solubility of chromium ion to a great extent. The pH of aqueous solution is the controlling factor in the adsorption process; hence it become necessary to determine at what pH, max adsorption will takes place. Percentage removal of Chromium goes on decreasing with increase in pH values. The maximum removal efficiency was 67.5% at 2 pH value. The Chromium removal was higher at lower pH values. 5.2 Effect of Contact Time Graph shows that Removal efficiency of Cr-(VI) ion increases with respect to increase in contact time (in min.) of adsorbent.
Fig.3-Effect of contact time on removal of Cr- (VI) ion 5.3 Effect of Initial Metal Ion Concentration It was observed that the activity of adsorbent material falls sharply with an increase in initial concentration of chromium ion. The max Cr removal efficiency for all the set of optimized parameter was found to be 98% for Neem Leaves at initial concentration of 30mg/100ml.
Fig.4-Effect of initial concentration on removal of Cr-(VI) ion
0
10
20
1
3
5
7
9
Absorbance
Concentration (ppm)
Standard Calibration Curve For Chromium
Concentration (ppm)
Absorbance
0
100
1
2
3
4
5
% Removal
pH
Effect of pH
pH
% Removal
0
200
20
40
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% Removal
Time (min)
Effect of Contact Time
Time (min.)
% Removal
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30
% Removal
Initial Concentration (mg/l)
Effect of Concentration
Initial Concentration (mg/l)
% Removal