Lecture 1 Biochemical Engineering

Slides:



Advertisements
Similar presentations
Water Management in a Petroleum Refinery
Advertisements

ORDINARY DIFFERENTIAL EQUATIONS (ODE)
Hierarchy of decisions
Modelling & Simulation of Chemical Engineering Systems
Biological waste water treatment
Lecture 13: Introduction to Environmental Engineering
Volumetric Analysis Frequently, we will react 2 solutions with each other These reactions are called titrations: Water analysis Environmental Sciences.
CH 3: Stoichiometry Moles.
Chemical Stoichiometry
PTT108/108 MATERIAL AND ENERGY BALANCE
SOLUTIONS & CONCENTRATIONS WHAT IS A SOLUTION ? WHAT IS CONCENTRATION & HOW IS IT MEASURED ?
Introduction to Chemical Engineering CHE-201
Advanced Bioprocess Engineering Material Balances
Exergy: A Measure of Work Potential Study Guide in PowerPoint
Dr. F. Iskanderani Spring 2003/2004 Example C : Component.
Development of Dynamic Models Illustrative Example: A Blending Process
Development of Dynamic Models Illustrative Example: A Blending Process
Material balance on single unit process
THEORETICAL MODELS OF CHEMICAL PROCESSES
Accounting for Mass Chapter 18.
Advanced Bioprocess Engineering Material Balances
Food Process Engineering
FUNDAMENTALS OF MATERIAL BALANCE
Chemical Engineering Plant Design Lek Wantha Lecture 05 Input-Output Structure of the Flowsheet.
Chapter 3: Matter and Energy Chemistry 1020: Interpretive chemistry Andy Aspaas, Instructor.
Chapter 3 Mass Balance.
Matter and Change.
Prentice Hall © 2003Chapter 3 Chapter 3 Stoichiometry: Calculations with Chemical Formulas and Equations FAYETTEVILLE STATE UNIVERSITY COLLEGE OF BASIC.
Reading Materials: Chapter 4
Wastewater Treatment Processes
An Investigation Into Advanced Life Support system for Mars Thursday 9 th February, AM Chemical Engineering Design Projects 4 Red Planet Recycle.
Materials Balances with Multiple Materials Only one equation can be written for each black box unless there is more than one material in the flow Example.
Pure Substances Elements
Atomic theory Odds and ends. AMU 1.6 x Kg Mass of 1/12 of carbon – 12 isotope.
Lecture 1: Kinetics of Substrate Utilization and Product Formation
Material balance and Energy balance steady state reaction systems.
Lecture 3 – Materials Balances Introduction to Environmental Engineering Lecture3 Dr. Jawad Al-rifai.
Liquid-Liquid Extraction
Assignment 1 submitted via moodle within 31 Aug 11.
Prentice Hall © 2003Chapter 3 Chapter 3 Stoichiometry: Calculations with Chemical Formulas and Equations CHEMISTRY The Central Science 9th Edition David.
Food Process Engineering
Miss :Salsabeel H. AL-Joujou
Microbial growth in:- Closed Cultivation Systems Open Cultivation Systems Semi-Open Cultivation Systems.
Concentration of Solutions What is Concentration? What is Concentration? The amount of solute dissolved in a specified amount of solution The amount of.
Chemistry 111 for Engineering students Dr. Ayman H. Kamel Office: 33.
Ch61: Industrial Chemistry The Material Balance E. Abenojar 10 November 2010.
Additional Problems (1) A wet paper pulp is found to contain 71% water. After drying it is found that 60% of the original water has been removed. Calculate.
Lecture 7. Single Units without Reaction. Units without Reaction Fermentation broth Membrane separator Continuous distillation column Mixing of battery.
Energy. Energy is classified: Kinetic energy – energy of motion Potential energy – energy of position Both energies can be transferred from one object.
CHAPTER 3 material balance part iI
FACULTY OF ENGINEERING TECHNOLOGY AND RESEARCH
Lecture 9. Material Balance for Processes Involving Reaction.
© 2016 Carl Lund, all rights reserved A First Course on Kinetics and Reaction Engineering Class 40.
Properties of Matter. What is Matter Anything that has mass and takes up space.
Prepared By: Group.5( to 47) B.E. Sem-III(Chemical) Guided By:
MASS BALANCE REACTOR THEORY
Ert 455 manufacturing & production of biological product
Is this process continuous, batch, or semi-batch?
Dissolved Oxygen and Biochemical Oxygen Demand Analyses
Material Balances w/ Chemical Reactions
Filtration Reading Materials:
Chapter 4 Material Balances.
Mass Balance- in Non-Reactive System Multi unit system
Mass Balance- in Non-Reactive System Multi unit system
Environmental Engineering
4. Basis Operations in Food Fermentations (Biotechnology)
Mass Balance- in Non-Reactive System Multi unit system
EXAMPLE 1 – Diluting a Toxic Water Supply (Elementary)
Environmental Engineering
PROCESS AND PROCESS VARIABLE
Presentation transcript:

Lecture 1 Biochemical Engineering Material Balances Lecture 1 Biochemical Engineering

Review of Thermodynamics System – any matter identified for investigation Surroundings – the remainder of the universe Boundary – separates system from surroundings May be real and tangible or virtual and nominal

Types of System

Process – causes changes in the system or surroundings Batch process – operates in a closed system Semi-batch process – allows either input or output of mass Fed-batch process – allows input of material to the system but not output Continuous processs – allows matter to flow in and out of the system Batch process – all materials are provided at the start, and the products are removed only when the process is complete Semi batch – all other process that does not fit in the other three If input and output rates of continuous process is equal, it can continue on indefinitely

Equilibrium vs Steady-state Describes a process in which the properties of the system (T, p, V, …) doesn’t vary with time Equilibrium Describes a system in which all opposing forces are counter-balanced, leading to insignificant changes in the properties of the system

Law of Conservation of Mass Mass in = Mass out Given component A, what if Mass in ≠ Mass out? Something is wrong with the measurements The system has a leak Component A is consumed/generated within the system Component A accumulates in the system

General Mass Balance For component A Mass in Mass out Mass generated Mass consumed Mass accumulated

Sample Problem A continuous process is set up for treatment of waste water. Each day, 105 kg cellulose and 103 kg bacteria enter the feed stream, while 104 kg cellulose and 1.5 x 104 kg bacteria leave the effluent. The rate of cellulose digestion by the bacteria is 7 x 104 kg/day. The rate of bacterial growth is 2 x 104 kg/day; the rate of bacterial lysis is 5 x 102 kg/day. Write balances for cellulose and bacteria in the system Cellulose: 2x104 accumulation Bacteria: 5.5x103 accumulation

Types of Material Balance Differential Balance Used for continuous processes Based on flow rates Integral Balance Used for batch, semi-batch and fed-batch Based on the quantity or mass, usualy over a specified time period

Simplified General Mass Balance: the Steady-state Material At steady-state, does mass in = mass out? With reaction Without reaction Total mass Yes Total moles No Mass of a molecular specie Moles of a molecular specie Mass of an atomic specie Moles of an atomic specie 𝑚𝑎𝑠𝑠 𝑖𝑛+𝑚𝑎𝑠𝑠 𝑔𝑒𝑛𝑒𝑟𝑎𝑡𝑒𝑑=𝑚𝑎𝑠𝑠 𝑜𝑢𝑡+𝑚𝑎𝑠𝑠 𝑐𝑜𝑛𝑠𝑢𝑚𝑒𝑑

Procedure for material balance calculation Draw a clear process flow diagram Select a set of units and state it clearly Select a basis for calculation and state it clearly State all assumptions applied to the problem Identify which components of the system are involved in reaction

What percentage water is in the filter cake? A fermentation slurry containing Streptomyces kanamyceticus cells is filtered using a continuous rotary vacuum filter. Slurry is fed to the filter at the rate of 120 kg/h; 1 kg slurry contains 60 g cell solids. To improve filtration rates, particles of diatomaceous aerth filter aid are added at a rate of 10 kg/h. the concentration of kanamycin in the slurry is 0.05% by weight. Liquid filtrate is collected at a rate of 112 kg/h; the concentration of the kanamycin in the filtrate is 0.045% (w/w). Filter cake containing cells and filter aid is removed continuously from the filter cloth. What percentage water is in the filter cake? If the concentration of kanamycin dissolved in the liquid within the filter cake is the same as that in the filtrate, how much kanamycin is absorbed per kg filter aid? Draw a clear process flow diagram Select a set of units and state it clearly Select a basis for calculation and state it clearly State all assumptions applied to the problem Identify which components of the system are involved in reaction 4.4% 9.6x10-4 kg/kg

How much glucose and ammonia are required? Xanthan gum is produced using Xanthomonas campestris in batch culture. Laboratory experiments have shown that for each gram of glucoses utilized by the bacteria 0.23 g of oxygen and 0.01 g ammonia are consumed, while 0.75 g gum, 0.09 g cells, and 0.27 g gaseous CO2 and 0.13 g H2O are formed. Other components of the system such as phosphate can be neglected. Medium containing glucose and ammonia dissolved in 20,000 L water is pumped into a stirred fermenter and innoculated with X. campestris. Air is sparged into the fermenter; the total amount of off- gas recovered during the entire batch culture is 1250 kg. because xanthan gum solutions have high viscosity and are difficult to handle, the final gum concentration should not be allowed to exceed 3.5% wt. How much glucose and ammonia are required? What percentage air is provided? Draw a clear process flow diagram Select a set of units and state it clearly Select a basis for calculation and state it clearly State all assumptions applied to the problem Identify which components of the system are involved in reaction 980 kg glucose; 9.8 kg NH3 25% excess air

Material Balance w/ Recycle, Purge and Bypass