This experiment aims to discover the effect of initial concentration and initial height on sedimentation characteristics of calcium carbonate particles suspended in water. Data was collected for calcium carbonate suspensions at different concentrations (2-10%) and initial heights, measuring the settling velocity over time. The results show an inverse relationship between concentration and settling velocity, with higher concentrations settling more slowly. Higher initial heights also resulted in higher settling velocities compared to the same concentration at a lower initial height. Graphs of settling velocity versus limiting concentration were similar for all cases tested.
Sedimentation is the process where particles in suspension settle out of the fluid they are entrained in, due to forces like gravity, centrifugal force, and drag. It is widely used in industries like food, water treatment, and wastewater treatment. The document discusses the principles and mechanisms of sedimentation through equations of motion and graphical representations of particle settling. An experiment is described that examines the relationship between calcium carbonate concentration, initial suspension height, and settling velocity, though it has some errors. The results show higher concentrations and lower initial heights increase settling velocity. Recommendations to improve experimental control and reduce errors are provided.
This experiment aimed to determine how concentration affects the weight and volume of cake obtained from a plate and frame filter press, as well as the length of time needed to obtain a certain volume of filtrate. The results showed that as concentration increased, the time required to collect a set volume of filtrate also increased. A linear relationship was observed between volume of filtrate and time per volume of filtrate, with an r-squared value of 0.95, indicating these variables increased proportionally. Sources of error included possible equipment defects and variability in cake weights.
FULL COURSE:
https://courses.chemicalengineeringguy.com/p/flash-distillation-in-chemical-process-engineering/
Introduction:
Binary Distillation is one of the most important Mass Transfer Operations used extensively in the Chemical industry.
Understanding the concept behind Gas-Gas, Liquid-Liquid and the Gas-Liquid mass transfer interaction will allow you to understand and model Distillation Columns, Flashes, Batch Distillator, Tray Columns and Packed column, etc...
We will cover:
REVIEW: Of Mass Transfer Basics (Equilibrium VLE Diagrams, Volatility, Raoult's Law, Azeotropes, etc..)
Distillation Theory - Concepts and Principles
Application of Distillation in the Industry
Equipment for Flashing Systems such as Flash Drums
Design & Operation of Flash Drums
Material and Energy Balances for flash systems
Adiabatic and Isothermal Operation
Animations and Software Simulation for Flash Distillation Systems (ASPEN PLUS/HYSYS)
Theory + Solved Problem Approach:
All theory is taught and backed with exercises, solved problems, and proposed problems for homework/individual study.
At the end of the course:
You will be able to understand mass transfer mechanism and processes behind Flash Distillation.
You will be able to continue with Batch Distillation, Fractional Distillation, Continuous Distillation and further courses such as Multi-Component Distillation, Reactive Distillation and Azeotropic Distillation.
About your instructor:
I majored in Chemical Engineering with a minor in Industrial Engineering back in 2012.
I worked as a Process Design/Operation Engineer in INEOS Koln, mostly on the petrochemical area relating to naphtha treating.
There I designed and modeled several processes relating separation of isopentane/pentane mixtures, catalytic reactors and separation processes such as distillation columns, flash separation devices and transportation of tank-trucks of product.
1) Distillation is a method used to separate components of a liquid solution based on differences in how the components distribute between the vapor and liquid phases when heated to their boiling points.
2) Raoult's law describes vapor-liquid equilibrium for ideal solutions, relating the partial pressure of a component in vapor phase to its mole fraction in the liquid phase. Boiling point diagrams can be constructed using vapor pressure data.
3) Equilibrium or flash distillation involves heating a liquid mixture to partially vaporize it in a single stage, separating the vapor and liquid which approach equilibrium compositions.
This experiment involves conducting a saponification reaction between sodium hydroxide (NaOH) and ethyl acetate (Et(Ac)) in a continuous stirred tank reactor (CSTR) to determine the effect of residence time on conversion. A calibration curve will be prepared to relate conductivity measurements to conversion values for the 0.1M NaOH and 0.1M Et(Ac) reaction. The objectives are to determine conversion, the reaction rate constant, and the effect of residence time on conversion.
The McCabe-Thiele method is a graphical technique for determining the minimum number of stages required for distillation. It involves plotting the equilibrium relationship between liquid and vapor phases on a diagram and constructing operating lines to represent the mass balances in the rectifying and stripping sections. Intersections between the lines indicate the number of ideal stages. The method was developed in 1925 and remains useful for preliminary column design. Key considerations include the feed composition and enthalpy, reflux ratio, and use of partial condensers or reboilers.
This experiment aimed to determine the Reynolds number (NRe) as a function of flow rate for liquid flowing through a circular pipe. NRe was calculated for 6 trials with increasing flow rates. All trials had NRe below 2100, indicating laminar flow as observed by the smooth movement of dye in the pipe. As flow rate increased, NRe also increased but remained in the laminar flow regime. The results show that flow type depends on NRe, with laminar flow occurring at low velocities (NRe < 2100).
This document discusses an experiment on agitation and determining the relationship between speed of rotation, impeller diameter, and power requirement for baffled tanks. It also examines the relationship between power number and Reynold's number. The experiment used a baffled tank and found that power requirement increased with speed. While it could not directly compare baffled and unbaffled tanks, literature shows power numbers are higher for baffled tanks as Reynold's number increases. Greater impeller diameters also require more power.
Sedimentation is the process where particles in suspension settle out of the fluid they are entrained in, due to forces like gravity, centrifugal force, and drag. It is widely used in industries like food, water treatment, and wastewater treatment. The document discusses the principles and mechanisms of sedimentation through equations of motion and graphical representations of particle settling. An experiment is described that examines the relationship between calcium carbonate concentration, initial suspension height, and settling velocity, though it has some errors. The results show higher concentrations and lower initial heights increase settling velocity. Recommendations to improve experimental control and reduce errors are provided.
This experiment aimed to determine how concentration affects the weight and volume of cake obtained from a plate and frame filter press, as well as the length of time needed to obtain a certain volume of filtrate. The results showed that as concentration increased, the time required to collect a set volume of filtrate also increased. A linear relationship was observed between volume of filtrate and time per volume of filtrate, with an r-squared value of 0.95, indicating these variables increased proportionally. Sources of error included possible equipment defects and variability in cake weights.
FULL COURSE:
https://courses.chemicalengineeringguy.com/p/flash-distillation-in-chemical-process-engineering/
Introduction:
Binary Distillation is one of the most important Mass Transfer Operations used extensively in the Chemical industry.
Understanding the concept behind Gas-Gas, Liquid-Liquid and the Gas-Liquid mass transfer interaction will allow you to understand and model Distillation Columns, Flashes, Batch Distillator, Tray Columns and Packed column, etc...
We will cover:
REVIEW: Of Mass Transfer Basics (Equilibrium VLE Diagrams, Volatility, Raoult's Law, Azeotropes, etc..)
Distillation Theory - Concepts and Principles
Application of Distillation in the Industry
Equipment for Flashing Systems such as Flash Drums
Design & Operation of Flash Drums
Material and Energy Balances for flash systems
Adiabatic and Isothermal Operation
Animations and Software Simulation for Flash Distillation Systems (ASPEN PLUS/HYSYS)
Theory + Solved Problem Approach:
All theory is taught and backed with exercises, solved problems, and proposed problems for homework/individual study.
At the end of the course:
You will be able to understand mass transfer mechanism and processes behind Flash Distillation.
You will be able to continue with Batch Distillation, Fractional Distillation, Continuous Distillation and further courses such as Multi-Component Distillation, Reactive Distillation and Azeotropic Distillation.
About your instructor:
I majored in Chemical Engineering with a minor in Industrial Engineering back in 2012.
I worked as a Process Design/Operation Engineer in INEOS Koln, mostly on the petrochemical area relating to naphtha treating.
There I designed and modeled several processes relating separation of isopentane/pentane mixtures, catalytic reactors and separation processes such as distillation columns, flash separation devices and transportation of tank-trucks of product.
1) Distillation is a method used to separate components of a liquid solution based on differences in how the components distribute between the vapor and liquid phases when heated to their boiling points.
2) Raoult's law describes vapor-liquid equilibrium for ideal solutions, relating the partial pressure of a component in vapor phase to its mole fraction in the liquid phase. Boiling point diagrams can be constructed using vapor pressure data.
3) Equilibrium or flash distillation involves heating a liquid mixture to partially vaporize it in a single stage, separating the vapor and liquid which approach equilibrium compositions.
This experiment involves conducting a saponification reaction between sodium hydroxide (NaOH) and ethyl acetate (Et(Ac)) in a continuous stirred tank reactor (CSTR) to determine the effect of residence time on conversion. A calibration curve will be prepared to relate conductivity measurements to conversion values for the 0.1M NaOH and 0.1M Et(Ac) reaction. The objectives are to determine conversion, the reaction rate constant, and the effect of residence time on conversion.
The McCabe-Thiele method is a graphical technique for determining the minimum number of stages required for distillation. It involves plotting the equilibrium relationship between liquid and vapor phases on a diagram and constructing operating lines to represent the mass balances in the rectifying and stripping sections. Intersections between the lines indicate the number of ideal stages. The method was developed in 1925 and remains useful for preliminary column design. Key considerations include the feed composition and enthalpy, reflux ratio, and use of partial condensers or reboilers.
This experiment aimed to determine the Reynolds number (NRe) as a function of flow rate for liquid flowing through a circular pipe. NRe was calculated for 6 trials with increasing flow rates. All trials had NRe below 2100, indicating laminar flow as observed by the smooth movement of dye in the pipe. As flow rate increased, NRe also increased but remained in the laminar flow regime. The results show that flow type depends on NRe, with laminar flow occurring at low velocities (NRe < 2100).
This document discusses an experiment on agitation and determining the relationship between speed of rotation, impeller diameter, and power requirement for baffled tanks. It also examines the relationship between power number and Reynold's number. The experiment used a baffled tank and found that power requirement increased with speed. While it could not directly compare baffled and unbaffled tanks, literature shows power numbers are higher for baffled tanks as Reynold's number increases. Greater impeller diameters also require more power.
This document contains lecture slides from Dr. M. Subas Chandra Bose and Mrs. Sabarunisha Begum on the topic of mass transfer operations. It discusses various mass transfer concepts like diffusion, gas absorption principles, and vapor-liquid operations including distillation. The slides provide definitions and examples of different mass transfer processes and operations. They also describe concepts like the transfer unit, differential distillation, flash distillation, and continuous rectification in binary systems.
This document describes the single effect evaporation desalination process. It discusses the process components and flow, including an evaporator, condenser, and heating steam. Mathematical models are developed for the process, including material and energy balances. The models account for variables like salt concentration, mass flow rates, temperatures, heat of evaporation, and heat transfer between components. The goal of the models is to analyze the thermal performance of the single effect evaporation process.
This experiment studied the effect of step change input on the concentration in a continuous stirred tank reactor (CSTR) system consisting of three reactors in series. Sodium chloride solution was introduced to the first reactor and deionized water was pumped through the system. Conductivity readings were taken from each reactor every 3 minutes. The results showed that the conductivity increased over time as the salt solution spread through the reactors. After 84 minutes, the conductivity values equalized across the three reactors, indicating the input had achieved steady state distribution. Issues with data recording affected the smoothness of the plotted results graph.
This Presentation gives an overview about the multiple effect evaporators. The intention is also focused on designing principles of Single and Multiple Effect Evaporators
Packed columns are used for distillation, gas absorption, and liquid-liquid extraction. They have continuous gas-liquid contact through a packed bed, unlike plate columns which have stage-wise contact. Packed columns depend on good liquid and gas distribution, and have lower holdup but higher pressure drop than plate columns. This document provides details on packed column components, design procedures such as selecting packing and determining height, and examples of absorption and stripping processes in packed columns.
The objective of this experiment is to study spray dryers and spray drying operation. In industry, spray drying is used to separate liquid from solid. In a spray dryer, a liquid solution is dispersed into a stream of hot gas in the form of a mist of fine droplets. Moisture is rapidly vaporized from droplets and leaves residue particles of dry solid. These are then separated from the gas stream by the separator. In this experiment, dry milk was used for dry solid. The milk solution was used as liquid feed and the performance of spray dryer is observed.
This document discusses various mass transfer separation processes used in chemical industries. It describes core separation processes like distillation, gas absorption, liquid-liquid extraction, drying, adsorption, crystallization and membrane separation. These processes are classified based on the phases involved (gas, liquid, solid) and the mechanism of separation - contact of immiscible phases, indirect contact of miscible phases through a membrane, direct contact of miscible phases, or use of surface phenomena. Examples of typical applications and separation processes are provided for different combinations of phases.
Feed conditions in distillation column with respect to feed plate and refluxIhsan Wassan
This document discusses feed conditions in distillation columns with respect to the feed plate and reflux. It defines key terms like distillation, relative volatility, and reflux. It explains that the condition of the feed stream determines the relation between flows above and below the feed plate. The amount of saturated liquid versus vapor in the feed is quantified by a variable q. Feed can be saturated liquid/vapor or a mixture, determining the slope of the q-line. Feed plates help separate mixtures, and more reflux improves separation efficiency, allowing fewer plates for a given separation. Total reflux passes vapor and liquid without product removal, while minimum reflux is the lowest ratio enabling separation with infinite plates.
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
1) Drying curves plot drying rate versus remaining water content and can describe the drying process in steps with changing drying rates.
2) There is an initial constant rate period where unbound surface water is removed, followed by a falling rate period where the drying rate decreases as water moves internally through the material.
3) Drying rates determined experimentally can be used to calculate drying times to design drying equipment and operations. Simplified calculations can provide useful estimates by assuming constant temperature and humidity.
Gas absorption is a process used to separate gases by contacting a gas mixture with a liquid solvent. The key principles are the solubility of the absorbed gas and the rate of mass transfer as the gas dissolves into the liquid. Absorption is usually carried out counter-currently in vertical columns. The solvent is fed at the top while the gas enters at the bottom, allowing the absorbed substances to be washed out in the downward flowing liquid. Proper selection of solvent considers factors like gas solubility, volatility, cost, and viscosity. Rate of absorption is determined by volumetric mass transfer coefficients, which can be calculated from operating line and equilibrium curve diagrams.
This document discusses non-ideal flow and residence time distribution (RTD) analysis for non-ideal reactors. It begins by describing deviations from ideal reactor behavior, such as dead zones and bypassing, and how these affect residence times. It then covers RTD concepts like E(t), F(t), and normalized E(θ) curves. Measurement of RTD using tracers is described. Ideal reactor RTDs and models for non-ideal reactors like segregation and tanks-in-series are presented. The document stresses that RTD alone may not characterize non-ideal reactors and that flow models are also needed to analyze performance.
Batch sedimentation
What is sedimentation…?
Goals of gravity s sedimentation
Applications of sedimentation
zone settling velocity
Factors affecting zone settling velocity
Design of Zone Settling Tanks
What is Thickener and Clarifiers…?
Thickener Area Calculation
Types of clarifier
(No "Download lock")........... Study it, Download it, Understand it, Apply it and Serve the community.
رَبِّ زدْنيِ عِلْماً (Arabic)..............Ameen.
Here are the steps to solve this problem:
(a) Surface area of cuboid = 2*(5*3 + 5*1 + 3*1) = 38 mm^2
Surface area of sphere = 4*π*r^2
Equating the two: 38 = 4*π*r1^2
r1 = √(38/4/π) = 3 mm
Surface diameter = 2*r1 = 6 mm
(b) Surface area of cuboid = 38 mm^2
Volume of cuboid = 5*3*1 = 15 mm^3
Surface area to volume ratio of cuboid = 38/15 = 2.53 mm^-1
Surface
Difference between batch,mixed flow & plug-flow reactorUsman Shah
This slide completely describes you about the stuff include in it and also everything about chemical engineering. Fluid Mechanics. Thermodynamics. Mass Transfer Chemical Engineering. Energy Engineering, Mass Transfer 2, Heat Transfer,
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project (https://www.spire2030.eu/impress).
Section: Mass transfer processes
Subject: 2.4 Interphase mass transfer
This experiment aims to plot the friction factor against the Reynolds Number for a fixed bed and determine the critical velocity and superficial velocity of particles. Fluidization occurs when the upward drag force from the fluid equals the apparent weight of particles, lifting them. The experiment obtains bed expansion, pressure drop, and flow rate at different superficial velocities. The fanning friction factor is then plotted against the Reynolds number. Results show the friction factor was around 0.15, with 0.16 in the first trial and 0.14 in the second as the pressure drop increased and critical velocity and superficial velocity rose proportionally to the gas supply rate.
This document outlines the procedures and results from an experiment on gas absorption using an absorption column. The experiment examined the air pressure drop across the column as air flow rate was increased for different fixed water flow rates. Pressure drop was recorded and plotted against air flow rate. The experimental flooding points where compared to theoretical calculations, with errors ranging from 11.1% to 20%. The results showed that pressure drop increased with air flow rate as expected, identifying the flooding points where liquid could no longer flow down the column.
ASSIGNMNET-2 (10)Project submission with presentation-This.docxrock73
ASSIGNMNET-2 (10)
Project submission with presentation-
This activity is based on group work (3 students per group). Students is responsible to write a report about a given company, business idea or any other course related topics.
STEP 1- GROUPS CREATION:
Students may choose their mates and give a list of the members per group to the faculty member who will create a group wiki using that list. Those who did not choose their group members will be assigned automatically.
Step 2-- project theme
Each group will propose a project theme:
· case study about logistics and supply chain management in a company in Saudi Arabia ( to be precised)
· a new concept or innovation in the field of logistics management.
· The creation of a new project and the presentation of the logistics strategies, plans and practices.
Step 3- information gathering:
All the collected information has to be submitted in the wiki of the group.
The group work has to be continuous by updating the information in wikis that are specially created for the assignment (at least 5 updates per student).
Step 4: report submission week 12.
At the end of the semester, each student will submit the final report to concerned faculty members and present it to class with the help of a PowerPoint presentation with group members.
***************************************
Sheet1AveragesAverages with bad data thrown outStandard Deviation of AveragesStandard Deviation of Corrected DataTrial 1 (oC)Ecell (mV)Trial 2 (oC)Ecell (mV)Trial 3 (oC)Ecell (mV)Temperature (oC)Voltage (mV)Average TemperatureTemperatureVoltage (mV)TemperatureVoltage5.011613.113535.013064.412734.412731.0969655115100.08163334661.0969655115100.081633346610.011919.2137310.014239.713299.713290.4618802154122.09832103680.4618802154122.098321036820.0136621.8137920.9129020.9134520.913450.948.07286136690.948.072861366930.9119030.0131932.1138031.0129631.113501.053565375397.00687260881.484924240543.133513652440.0111840.4141140.1143940.2132340.314250.2081665999177.79857517240.212132034419.798989873249.0141450.6142450.1145949.9143249.914320.818535277223.62907813130.818535277223.629078131360.0136760.0134960.7145060.2138960.213890.404145188453.87330817140.404145188453.8733081714Average1341
Average Temperature (oC) vs Average Voltage (mV)
100.08163334665025122.0983210367775648.07286136688765897.006872608765875177.7985751723941223.62907813126304353.873308171425052100.08163334665025122.0983210367775648.07286136688765897.006872608765875177.7985751723941223.62907813126304353.8733081714250521.09696551146029050.461880215351701040.900000000000000361.05356537528527470.208166599946612240.818535277187245720.404145188432739671.09696551146029050.461880215351701040.900000000000000361.05356537528527470.208166599946612240.818535277187245720.404145188432739674.36666666666666639.733333333333332520.93140.16666666666666449.960.2333333333333271273.3333333333333132913451296.33333333333331322.66666666666671432.3333333333333 ...
This document describes an experiment to determine the residence time distribution for a continuous stirred-tank reactor (CSTR) at different flow rates. Sodium hydroxide is injected as a tracer and samples are collected and titrated over time. Curves are constructed for concentration C(t), normalized concentration E(t), cumulative distribution F(t), and others. The dispersion number D/uL is calculated from these curves and found to initially decrease then increase with flow rate.
This document contains lecture slides from Dr. M. Subas Chandra Bose and Mrs. Sabarunisha Begum on the topic of mass transfer operations. It discusses various mass transfer concepts like diffusion, gas absorption principles, and vapor-liquid operations including distillation. The slides provide definitions and examples of different mass transfer processes and operations. They also describe concepts like the transfer unit, differential distillation, flash distillation, and continuous rectification in binary systems.
This document describes the single effect evaporation desalination process. It discusses the process components and flow, including an evaporator, condenser, and heating steam. Mathematical models are developed for the process, including material and energy balances. The models account for variables like salt concentration, mass flow rates, temperatures, heat of evaporation, and heat transfer between components. The goal of the models is to analyze the thermal performance of the single effect evaporation process.
This experiment studied the effect of step change input on the concentration in a continuous stirred tank reactor (CSTR) system consisting of three reactors in series. Sodium chloride solution was introduced to the first reactor and deionized water was pumped through the system. Conductivity readings were taken from each reactor every 3 minutes. The results showed that the conductivity increased over time as the salt solution spread through the reactors. After 84 minutes, the conductivity values equalized across the three reactors, indicating the input had achieved steady state distribution. Issues with data recording affected the smoothness of the plotted results graph.
This Presentation gives an overview about the multiple effect evaporators. The intention is also focused on designing principles of Single and Multiple Effect Evaporators
Packed columns are used for distillation, gas absorption, and liquid-liquid extraction. They have continuous gas-liquid contact through a packed bed, unlike plate columns which have stage-wise contact. Packed columns depend on good liquid and gas distribution, and have lower holdup but higher pressure drop than plate columns. This document provides details on packed column components, design procedures such as selecting packing and determining height, and examples of absorption and stripping processes in packed columns.
The objective of this experiment is to study spray dryers and spray drying operation. In industry, spray drying is used to separate liquid from solid. In a spray dryer, a liquid solution is dispersed into a stream of hot gas in the form of a mist of fine droplets. Moisture is rapidly vaporized from droplets and leaves residue particles of dry solid. These are then separated from the gas stream by the separator. In this experiment, dry milk was used for dry solid. The milk solution was used as liquid feed and the performance of spray dryer is observed.
This document discusses various mass transfer separation processes used in chemical industries. It describes core separation processes like distillation, gas absorption, liquid-liquid extraction, drying, adsorption, crystallization and membrane separation. These processes are classified based on the phases involved (gas, liquid, solid) and the mechanism of separation - contact of immiscible phases, indirect contact of miscible phases through a membrane, direct contact of miscible phases, or use of surface phenomena. Examples of typical applications and separation processes are provided for different combinations of phases.
Feed conditions in distillation column with respect to feed plate and refluxIhsan Wassan
This document discusses feed conditions in distillation columns with respect to the feed plate and reflux. It defines key terms like distillation, relative volatility, and reflux. It explains that the condition of the feed stream determines the relation between flows above and below the feed plate. The amount of saturated liquid versus vapor in the feed is quantified by a variable q. Feed can be saturated liquid/vapor or a mixture, determining the slope of the q-line. Feed plates help separate mixtures, and more reflux improves separation efficiency, allowing fewer plates for a given separation. Total reflux passes vapor and liquid without product removal, while minimum reflux is the lowest ratio enabling separation with infinite plates.
An Overview to the most common Industrial Mass Transfer Operations & Process Separation Technologies
Course Description
In this course we will cover the most basic processes involved in Mass Transfer Operations. This is an overview of what type of processes, methods and units are used in the industry. This is mostly an introductory course which will allow you to learn, understand and know the approach towards separation processes involving mass transfer phenomena.
It is an excellent course before any Mass Transfer Process or Unit Operation Course such as Distillations, Extractions, Leaching, Membranes, Absorption, etc...
This course is extremely recommended if you will continue with the following:
Flash Distillation, Simple Distillation, Batch Distillation
Gas Absorption, Desorption & Stripping
Binary Distillation, Fractional Distillation
Scrubbers, Gas Treating
Sprayers / Spray Towers
Bubble Columns / Sparged Vessels
Agitation Vessels
Packed Towers, Tray Towers
Membranes
Liquid Extraction
Dryers / Humidifiers
Adsorbers
Evaporators/Sublimators
Crystallizers
Centrifugations
And many other Separation Technology!
At the end of the Course:
You will be able to understand the mass transfer operations concepts. You will be able to identify Mass Transfer Unit Operations. You will be also able to ensure the type of method of separation technology used.
You will be able to apply this theory in further Unit Operations.
Theory-Based Course
This is a very theoretical course, some calculations and exercises are present, but overall, expect mostly theoretical concepts.
1) Drying curves plot drying rate versus remaining water content and can describe the drying process in steps with changing drying rates.
2) There is an initial constant rate period where unbound surface water is removed, followed by a falling rate period where the drying rate decreases as water moves internally through the material.
3) Drying rates determined experimentally can be used to calculate drying times to design drying equipment and operations. Simplified calculations can provide useful estimates by assuming constant temperature and humidity.
Gas absorption is a process used to separate gases by contacting a gas mixture with a liquid solvent. The key principles are the solubility of the absorbed gas and the rate of mass transfer as the gas dissolves into the liquid. Absorption is usually carried out counter-currently in vertical columns. The solvent is fed at the top while the gas enters at the bottom, allowing the absorbed substances to be washed out in the downward flowing liquid. Proper selection of solvent considers factors like gas solubility, volatility, cost, and viscosity. Rate of absorption is determined by volumetric mass transfer coefficients, which can be calculated from operating line and equilibrium curve diagrams.
This document discusses non-ideal flow and residence time distribution (RTD) analysis for non-ideal reactors. It begins by describing deviations from ideal reactor behavior, such as dead zones and bypassing, and how these affect residence times. It then covers RTD concepts like E(t), F(t), and normalized E(θ) curves. Measurement of RTD using tracers is described. Ideal reactor RTDs and models for non-ideal reactors like segregation and tanks-in-series are presented. The document stresses that RTD alone may not characterize non-ideal reactors and that flow models are also needed to analyze performance.
Batch sedimentation
What is sedimentation…?
Goals of gravity s sedimentation
Applications of sedimentation
zone settling velocity
Factors affecting zone settling velocity
Design of Zone Settling Tanks
What is Thickener and Clarifiers…?
Thickener Area Calculation
Types of clarifier
(No "Download lock")........... Study it, Download it, Understand it, Apply it and Serve the community.
رَبِّ زدْنيِ عِلْماً (Arabic)..............Ameen.
Here are the steps to solve this problem:
(a) Surface area of cuboid = 2*(5*3 + 5*1 + 3*1) = 38 mm^2
Surface area of sphere = 4*π*r^2
Equating the two: 38 = 4*π*r1^2
r1 = √(38/4/π) = 3 mm
Surface diameter = 2*r1 = 6 mm
(b) Surface area of cuboid = 38 mm^2
Volume of cuboid = 5*3*1 = 15 mm^3
Surface area to volume ratio of cuboid = 38/15 = 2.53 mm^-1
Surface
Difference between batch,mixed flow & plug-flow reactorUsman Shah
This slide completely describes you about the stuff include in it and also everything about chemical engineering. Fluid Mechanics. Thermodynamics. Mass Transfer Chemical Engineering. Energy Engineering, Mass Transfer 2, Heat Transfer,
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project (https://www.spire2030.eu/impress).
Section: Mass transfer processes
Subject: 2.4 Interphase mass transfer
This experiment aims to plot the friction factor against the Reynolds Number for a fixed bed and determine the critical velocity and superficial velocity of particles. Fluidization occurs when the upward drag force from the fluid equals the apparent weight of particles, lifting them. The experiment obtains bed expansion, pressure drop, and flow rate at different superficial velocities. The fanning friction factor is then plotted against the Reynolds number. Results show the friction factor was around 0.15, with 0.16 in the first trial and 0.14 in the second as the pressure drop increased and critical velocity and superficial velocity rose proportionally to the gas supply rate.
This document outlines the procedures and results from an experiment on gas absorption using an absorption column. The experiment examined the air pressure drop across the column as air flow rate was increased for different fixed water flow rates. Pressure drop was recorded and plotted against air flow rate. The experimental flooding points where compared to theoretical calculations, with errors ranging from 11.1% to 20%. The results showed that pressure drop increased with air flow rate as expected, identifying the flooding points where liquid could no longer flow down the column.
ASSIGNMNET-2 (10)Project submission with presentation-This.docxrock73
ASSIGNMNET-2 (10)
Project submission with presentation-
This activity is based on group work (3 students per group). Students is responsible to write a report about a given company, business idea or any other course related topics.
STEP 1- GROUPS CREATION:
Students may choose their mates and give a list of the members per group to the faculty member who will create a group wiki using that list. Those who did not choose their group members will be assigned automatically.
Step 2-- project theme
Each group will propose a project theme:
· case study about logistics and supply chain management in a company in Saudi Arabia ( to be precised)
· a new concept or innovation in the field of logistics management.
· The creation of a new project and the presentation of the logistics strategies, plans and practices.
Step 3- information gathering:
All the collected information has to be submitted in the wiki of the group.
The group work has to be continuous by updating the information in wikis that are specially created for the assignment (at least 5 updates per student).
Step 4: report submission week 12.
At the end of the semester, each student will submit the final report to concerned faculty members and present it to class with the help of a PowerPoint presentation with group members.
***************************************
Sheet1AveragesAverages with bad data thrown outStandard Deviation of AveragesStandard Deviation of Corrected DataTrial 1 (oC)Ecell (mV)Trial 2 (oC)Ecell (mV)Trial 3 (oC)Ecell (mV)Temperature (oC)Voltage (mV)Average TemperatureTemperatureVoltage (mV)TemperatureVoltage5.011613.113535.013064.412734.412731.0969655115100.08163334661.0969655115100.081633346610.011919.2137310.014239.713299.713290.4618802154122.09832103680.4618802154122.098321036820.0136621.8137920.9129020.9134520.913450.948.07286136690.948.072861366930.9119030.0131932.1138031.0129631.113501.053565375397.00687260881.484924240543.133513652440.0111840.4141140.1143940.2132340.314250.2081665999177.79857517240.212132034419.798989873249.0141450.6142450.1145949.9143249.914320.818535277223.62907813130.818535277223.629078131360.0136760.0134960.7145060.2138960.213890.404145188453.87330817140.404145188453.8733081714Average1341
Average Temperature (oC) vs Average Voltage (mV)
100.08163334665025122.0983210367775648.07286136688765897.006872608765875177.7985751723941223.62907813126304353.873308171425052100.08163334665025122.0983210367775648.07286136688765897.006872608765875177.7985751723941223.62907813126304353.8733081714250521.09696551146029050.461880215351701040.900000000000000361.05356537528527470.208166599946612240.818535277187245720.404145188432739671.09696551146029050.461880215351701040.900000000000000361.05356537528527470.208166599946612240.818535277187245720.404145188432739674.36666666666666639.733333333333332520.93140.16666666666666449.960.2333333333333271273.3333333333333132913451296.33333333333331322.66666666666671432.3333333333333 ...
This document describes an experiment to determine the residence time distribution for a continuous stirred-tank reactor (CSTR) at different flow rates. Sodium hydroxide is injected as a tracer and samples are collected and titrated over time. Curves are constructed for concentration C(t), normalized concentration E(t), cumulative distribution F(t), and others. The dispersion number D/uL is calculated from these curves and found to initially decrease then increase with flow rate.
The document discusses design procedures for ion exchange columns. The breakthrough curves for ion exchange and adsorption columns are similar. The same design procedures can be used for both, including the scale-up and kinetic approaches. A laboratory or pilot-scale breakthrough curve is required to determine design parameters like the rate constant and maximum solid phase concentration. The breakthrough curve shows effluent concentration versus throughput volume, and the area above the curve represents the amount of solute/ions removed.
The document presents calculations and data from a copper flotation process. It includes equations for the various flotation circuits (rougher, scavenger, cleaner, etc.). Mass balances are provided showing the distribution of copper, silver, and iron throughout the process, from the feed to each cell to the final concentrate. Assays are given for the feed and outputs from each cell, along with calculated flow rates and recoveries.
The document presents the final year project of several students on optimizing the concentration of surfactant in nanofluid for boiling applications. The objective is to study the effect of surfactant concentration on the heat transfer of base fluids containing various proportions of methanol and water. Experiments are conducted to determine the optimum surfactant concentration for a nanofluid made of alumina nanoparticles dispersed in water. Results show that heat transfer increases with increasing surfactant concentration up to an optimum level, beyond which it decreases due to higher viscosity outweighing reductions in surface tension.
This document contains information about engineering simulations of fluid reservoirs including:
- Basic plots used to model fluid height over time using the Euler integration method
- A schematic layout of a fluid reservoir showing fluid inflow and outflow
- An equation relating the change in fluid height over time to the inlet and outlet mass flows
- A sample simulation run with results showing fluid height decreasing over time as inlet flow stops and outlet flow continues
Welcome to International Journal of Engineering Research and Development (IJERD)IJERD Editor
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yahoo journals, bing journals, International Journal of Engineering Research and Development, google journals, hard copy of journal
The World Bank project proposal aims to improve water quality in Lake Taihu through dredging contaminated sediments, testing improved dewatering methods, and treating discharge water with ClearBlue 104 to reduce bacteria. The proposal outlines objectives to map dredge areas, evaluate new dredging and dewatering technologies, and make recommendations to support long-term water quality monitoring. Pilot tests will dredge sediments, measure water quality impacts, and evaluate dewatering options like geotextile bags to inform full-scale implementation plans.
Accidental Releases Analysis for Toxic Aqueous SolutionsBREEZE Software
This document discusses methodologies for modeling the evaporation rates and downwind dispersion of accidental releases of chlorine dioxide (ClO2) and ammonia (NH3) aqueous solutions. It presents a heat and mass transfer model to calculate time-dependent evaporation rates that considers variables such as liquid temperature, vapor pressure, and concentration. Example calculations show that this model estimates lower evaporation rates than the EPA guidance method. Three dispersion models (DEGADIS, ALOHA, SLAB) are applied to benchmark example releases of ClO2 and NH3, with ClO2 modeled as a dense gas and NH3 as neutrally buoyant. The maximum distances to toxic endpoints are reported.
Bernoulli equation Determination through LAB work.pdfBapi Mondal
Applying Bernoulli equation to determine the orifice throat diameter of the
given orifice meter and plotting the following curves.
a) Pressure difference vs Reynolds number.
b) Log pressure difference vs Log velocity
c) Log average velocity vs manometer reading and find the slope of the line.
This document summarizes a student research project investigating the use of coal fly ash as an adsorbent for removing color from pulp mill effluent. The research team analyzed how factors like ash dosage, shake speed, contact time, and pH affected color removal efficiency. Equilibrium was reached within 12 hours, and dosage optimization found 175g/L of ash most effective. Adsorption models showed the process was more complicated than simple physical adsorption. The team received a research grant and plans to present findings at conferences. Further studies include analyzing COD levels and running continuous column tests.
This document provides data from a gas chromatography experiment analyzing the peaks of pentafluorobenzene. It includes the relative retention times and peak areas of pentafluorobenzene and an internal standard, as well as calibration curves constructed from these data. It directs the student to calculate linear regression statistics, determine concentrations from the calibration curves, and calculate standard deviations. The key information is that relative retention times and peak area ratios to an internal standard were used to identify an unknown compound and calculate its concentration through linear calibration curves.
The document summarizes the design of a septic tank. It calculates the required volumes for sedimentation (1.8 m3), sludge digestion (1.06 m3), and sludge storage (15 m3). The total volume is determined to be 1.8 + 1.06 + 1.4 * 15 = 27.24 m3. The suitable dimensions of the septic tank are determined to be 6 m x 4 m x 1.5 m, with the first compartment being 4 m x 4 m x 1.5 m and the second being 2 m x 4 m x 1.5 m. Diagrams of the plan and elevation views of the septic tank are also provided.
The document discusses flowmetering steam. It begins by quoting Lord Kelvin about the importance of measurement. Many businesses now recognize the value of energy cost accounting, conservation, and monitoring techniques using tools like flowmetering. Steam is difficult to measure accurately. Flowmeters designed for liquids and gases don't always work well for steam. The document then discusses fundamentals of fluid mechanics including density, viscosity, Reynolds number, and flow regimes as they relate to measuring steam flow. Accurately measuring steam use allows optimizing plant efficiency and energy efficiency through monitoring steam demand and identifying major steam users.
1) The document describes an experiment measuring the impact force of a water jet on flat and hemispherical surfaces.
2) The experiment calculates the theoretical and actual jet forces using formulas involving discharge rate, velocity, and surface area.
3) The results show that the force on a hemispherical surface is larger than a flat surface for the same amount of water, and that actual and theoretical forces are linearly related.
A short project to find out Critical Micellar Concentration of reverse micelle in non-polar environment. the instrument used is obviously Dynamic Light Scattering Machine.
The document discusses phase equilibrium studies of impure carbon dioxide systems relevant to carbon capture and storage technologies. It presents new vapor-liquid equilibrium and solubility data for binary and ternary mixtures of CO2, N2, H2, and H2O measured using high-pressure facilities. The data aims to expand understanding of thermodynamic properties to inform the design of CO2 compression, pipeline transport, and the presence of impurities like H2 which increase the pressure required for a homogeneous CO2 phase. Equations of state are evaluated against the experimental data.
This document provides information about Caltra's cement products and castable refractories. It includes:
1. An introduction and overview of Caltra's product development, quality control processes, and product offerings.
2. Details on Caltra's main cement product, CAC-70F, including its chemical composition and physical properties compared to other cements. Test data shows CAC-70F performs well.
3. Information on castable formulations using different cements, water-cement ratios, and additives, along with corresponding test results for properties like strength and permeability. CAC-70F-containing castables demonstrate good high-temperature resistance.
Episode 5 : Liquid-Solid
Separation
There are many solid/liquid separation techniques which have established general application within the process industries
The selection of appropriate equipment is thus a challenge to the design engineer and it is often difficult to identify the most appropriate separator without extensive previous knowledge of a similar separation problem
Don't forget to leave a comment! I would like to know if this helped you in any way possible and if there's any mistakes or corrections I can make 'em right.
Water Pollution in Lakes (causes, effects, sources)
Rule 1080: Personal Protective Equipment (PPE) OSH Standards Nicely Jane Eleccion
Personal protective equipment (PPE) provides an important barrier between workers and environmental hazards. PPE includes equipment that protects the eyes and face, head, respiratory system, hands and arms, and feet. Proper PPE must be approved, maintained, and used correctly. Eye and face protection includes safety glasses and goggles to protect from flying particles or splashes. Respirators are required when workers are exposed to harmful dusts, fumes, mists or gases. Hard hats protect the head from impact or penetration. Gloves and sleeves protect hands and arms based on the specific hazards. Safety shoes protect the feet from hazards such as heavy objects, sharp objects, molten metal, electricity or hot/wet surfaces.
1. Sieve analysis was performed on a sample of calcium carbonate to determine its particle size distribution. The sample was shaken in a mechanical shaker through a series of sieves with decreasing mesh sizes for different time intervals.
2. The mass of the sample retained on each sieve was measured and the cumulative percentage passing and particle size distribution curves were plotted.
3. The results showed that increasing the shaking time decreased the particle size, following a bell-shaped curve distribution rather than a direct proportional relationship between particle size and mass fraction.
This experiment aims to calibrate venturi and orifice flow meters by plotting the coefficient of discharge against Reynolds number for each and measuring the pressure drop across them at various flow rates. A known volume of water is passed through the meters and the flow rate is calculated. For both meters, the coefficient of discharge increases as the Reynolds number decreases, and the pressure drop increases non-linearly with flow rate, with a greater pressure drop observed for the orifice meter.
This document describes a student laboratory experiment to produce fruit wine. It provides details of the wine production process including objectives, materials, equipment, process steps from fruit preparation to aging, observations recorded over 8 weeks, and conclusions. The production of wine was found to take 2 months and require careful control and monitoring of temperature, sugar levels, and other factors to produce a quality product without waste. Suggestions are made to explore using local fruits and aging in oak barrels.
This document discusses the causes and effects of soil pollution. It identifies various sources of soil pollution including industrial wastes, urban wastes, agricultural practices, radioactive pollutants, and biological agents. Industrial pollutants come from industries like paper mills, oil refineries, and fertilizer plants. Urban wastes include garbage and refuse from cities. Modern agriculture releases large amounts of fertilizers and pesticides. Radioactive substances from nuclear activities can also pollute soil. The pollutants affect the chemical and biological properties of soil. The document also outlines physical, chemical, biological, and thermal treatments that can be used to remediate contaminated soil.
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KuberTENes Birthday Bash Guadalajara - K8sGPT first impressionsVictor Morales
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International Conference on NLP, Artificial Intelligence, Machine Learning an...gerogepatton
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population health. The study explores stakeholders' perceptions on critical success factors, identifying
challenges such as insufficiently trained personnel, organizational silos, and structural barriers to data
exchange. Facilitators for integration include cost reduction initiatives and interoperability policies.
Technologies like IoT, Big Data, AI, Machine Learning, and robotics enhance diagnostics, treatment
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Introduction- e - waste – definition - sources of e-waste– hazardous substances in e-waste - effects of e-waste on environment and human health- need for e-waste management– e-waste handling rules - waste minimization techniques for managing e-waste – recycling of e-waste - disposal treatment methods of e- waste – mechanism of extraction of precious metal from leaching solution-global Scenario of E-waste – E-waste in India- case studies.
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CHINA’S GEO-ECONOMIC OUTREACH IN CENTRAL ASIAN COUNTRIES AND FUTURE PROSPECTjpsjournal1
The rivalry between prominent international actors for dominance over Central Asia's hydrocarbon
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ISPM 15 Heat Treated Wood Stamps and why your shipping must have one
Sedimentation
1. SEDIMENTATION
ELECCION, NICELY JANE R.
Department of Chemical Engineering
College of Engineering and Architecture
Cebu Institute of Technology – University
N. Bacalso Ave., Cebu City 6000
This experiment wants to discover the effect of the initial concentration and the initial
height on sedimentation characteristics specifically to plot the initial mass settling rate
against concentration, the rate of sedimentation at final consolidation on semi – log paper,
the settling velocity against the limiting concentration and to deduce that the graphs of
settling velocity against limiting concentration are similar for all cases. Sedimentation is
the process of letting suspended particles or solids settle through gravity. A particle in a
fluid settles eventually due to its higher density compared to the fluid in which it is
suspended. In the first part, different concentrations of the slurry were allowed to settle in
different cylinders. Data showed an inverse relationship between the concentration and
settling velocity. As the concentration increases, the rate of settling decreases. In the
second part, a certain concentration of slurry was allowed to settle in the cylinders but
varied in the initial heights. Data showed a direct relationship between the change in initial
heights and the settling velocity compared in the first part which was inverse.
2. 1. Introduction
Sedimentation, or clarification, is the process of allowing particles in suspension in
water to settle out of the suspension through gravity. Suspended material may be
particles, such as clay or silts, originally present in the source water. More commonly,
suspended material or floc is created from material in the water and the chemical used in
coagulation or in other treatment processes, such as lime softening. It is timely to note
that development of the theory of sedimentation is based on the initial assumption that
the particles to be removed from suspension are spherical and solid, whereas in practice,
they are irregular in shape, exist as a wide range in size and can be permeable to flow of
water.
This process is accomplished by decreasing the velocity of the water being treated
to a point below which the particles will no longer remain in suspension. When the velocity
no longer supports the transport of the particles, gravity will remove them from the flow.
Several factors affect the separation of settle-able solids from water. Some of the more
common types of factors to consider are: particle size, water temperature, currents, and
sedimentation basin zones.
This experiment aims to discover the effect of the initial concentration and the
initial height on sedimentation characteristics specifically to plot the initial mass settling
rate against concentration, the rate of sedimentation at final consolidation on semi – log
paper, the settling velocity against the limiting concentration and to deduce that the
graphs of settling velocity against limiting concentration are similar for all cases
3. 2. Materials and Methods
2.1 Equipment and Materials
sedimentation apparatus
mesh
beaker
spatula
stirring rod
powder of calcium carbonate.
2.2 Methods
The calcium carbonate was first sieved in order to achieve a uniform particle size
using a mesh. The calcium carbonate is then mixed with water in 5 different
concentration levels in 2%, 4%, 6%, 8%, and 10% by weight. Each of the slurry is then
placed in the sedimentation tubes at the same height. The readings were noted at
different time intervals until all calcium carbonates are completely settled down. The
slurries were then left for 24 hours to record the final compaction readings.
15. 5. Discussion
Sedimentation, or clarification, is the process of letting suspended material settle
by gravity. Sedimentation is characterized through the following parameters, which relate
to how they have been transported and weathered and how far from their original source
they have been deposited: (a) porosity – volume of voids within a bed which can contain
liquid, (b) permeability - the ability of water or other liquids (e.g. oil) to pass freely through
a material, (c) roundness - measure of the roughness of the surface of the sedimentary
grain, (d) sorting - relates to the range of particle sizes in a sediment, and (e) matrix - fine-
grained material (usually clays or silt) that is deposited originally with the coarser-grained
material.
Based on the gathered data in Part A, the change in the concentration of the slurry
affects the value of the settling velocity. It is observed that the height of the sludge
decreases slowly as the concentration of the slurry increases. The settling velocities were
obtained by getting the difference of the initial height of the sludge (calcium carbonate)
and the interphase height over the time interval recorded. It is also observed that the final
concentration recorded is lesser than the original concentration and this is because some
of the calcium carbonate are dissolved in water. In part B, the different initial heights
affects the values of the settling velocity. It is observed in tables 6 – 10 that the settling
velocity values increases as the initial height increases in the different trials.
16. 6. Conclusion
One of the commonly used unit operation in the industry is sedimentation because
it’s cheap and is efficient in separating solid and liquid phases. The change in
concentration of the slurry has a great impact on the settling velocity due to a greater
velocity gradient in the fluid surrounding the particles whereby a closer proximity of the
particles is evident. The rise of the initial heights also affects the settling velocity due
again to velocity gradients in the fluid surrounding the particles, this time, lesser compared
to part A. The change in initial height explains that the particles in the slurry are even
more scattered and the amount of particles is constant compared to part A. This would
mean that free settling is more favorable. Stokes law can be applied for this experiment
because of the very low settling velocities gathered and would mean the settling of
particles is having a laminar behavior.
7. Recommendation
In this experiment, there are several precaution we must take to avoid and prevent
errors to occur. Ensure the clarity of the glass apparatus since the one present in the
laboratory is not that clear anymore and the markings are also not clear which may result
to erroneous reading of values. The cylinders also are needed to be replaced. The lights
are not that bright enough to see the tip of the height of the sludge so make sure there is
a good lighting in the area in order to visibly see the height of the sludge.
17. 8. References
[1] Geankoplis, C.J. (2009) Principles of Transport Processes and Separation
Processes. 1st edition. Pearson Education South Asia PTE. LTD.
9. Web References
[1] Graham, I. (2010, January 27). Characteristic of Sediments. Retrieved March 12,
2018, from https://australianmuseum.net.au/characteristics-of-sediments
[2] Britannica, T. E. (2017, December 05). Sedimentation. Retrieved March 12,
2018, from https://www.britannica.com/science/sedimentation-geology