introduction to engineering calculations - bio-engineering

40
Lecture 2: INTRODUCTION TO ENGINEERING CALCULATIONS by Listowel Abugri Anaba AEN7201 BIO-ENGINEERING

Upload: listowel-abugri-anaba

Post on 11-Apr-2017

765 views

Category:

Engineering


10 download

TRANSCRIPT

Page 1: Introduction to Engineering Calculations - Bio-Engineering

Lecture 2: INTRODUCTION TO ENGINEERING CALCULATIONS

by

Listowel Abugri Anaba

AEN7201 BIO-ENGINEERING

Page 2: Introduction to Engineering Calculations - Bio-Engineering

Learning Outcomes• To learn conventions and definitions which form the backbone

of engineering analysis

• To know the nature of physical variables, dimensions and units

• Get to understand dimensionality and be able to convert units with ease

• How physical and chemical processes are translated into mathematics

Page 3: Introduction to Engineering Calculations - Bio-Engineering

Physical Variables, Dimensions and Units

Calculations used in bioprocess engineering require a systematic approach with well-defined methods and rules

The first step in quantitative analysis of systems is to express the system properties using mathematical language

Page 4: Introduction to Engineering Calculations - Bio-Engineering

1.1 Physical Variables

•A physical property of a body or substance that can be quantified by measurement e.g. length, velocity, viscosity etc.

• Seven out of all physical variables are accepted internationally as basis for measurement

• The base quantities are called dimensions, from which the dimensions of other physical variables are derived

e.g. velocity is LT-1 , force is LMT-2 etc.

Page 5: Introduction to Engineering Calculations - Bio-Engineering

Base quantitiesBase quantity Dimensional

symbolBase SI unit Unit symbol American Eng.

Length L metre m foot (ft)Mass M kilogram kg pound mass (lbm)Time T second s secondElectric current I ampere A ampereTemperature Θ kelvin K Rankine (R)Amount of substance N gram-mole gmol (mol) lbm-mole (lbmmol)Luminous intensity J candela cd candela

Supplementary fundamental units

Plane angle - radian radSolid angle - steradian sr

Page 6: Introduction to Engineering Calculations - Bio-Engineering

1.1.1 Substantial variables (1)

• Examples of substantial variables are mass, length, volume,viscosity, temperature etc.

• Expression of the magnitude of substantial variables requires a precise physical standard against which measurement is made

• These standards are called units

Page 7: Introduction to Engineering Calculations - Bio-Engineering

1.1.1 Substantial variables (2)

• The magnitude of substantial variables are in two parts: the number and the unit used for measurement

• The values of two or more substantial variables may be added or subtracted only if their units are the same

• the values and units of any substantial variables can be combined by multiplication or division

Page 8: Introduction to Engineering Calculations - Bio-Engineering

Dimensional quantities (1)Derived quantity Dimension SI unitAcceleration LT-2 ms-2

Angular velocity T-1 rads-1

Area L2 m2

Concentration L-3N moldm-3

Conductance (electric) L-2M-1T3I2 m-2kg-1s3A2 (Siemens)Density L-3M kgm-3

Energy L2MT-2 Nm or J (Joule)Enthalpy L2MT-2 JEntropy L2MT-2θ-1 J/KForce LMT-2 m·kg·s-2 or N (Newton)Fouling factor M T-3θ-1 Wm-2 K-I Frequency T-1 s-1 or Hz (Hertz)Half life T sHeat L2MT-2 JHeat flux MT-3 W m-2

Page 9: Introduction to Engineering Calculations - Bio-Engineering

Dimensional quantities (2)Derived quantity Dimension SI unitHeat-transfer coefficient MT-3θ-I Wm-2K-1

Illuminance L-2J Cdm-2 (lux)Mass flux L-2MT-1 kgm-2s-1

Momentum LMT-1 Kgms-1Molar mass MN-1 Gmol-1

Osmotic pressure L-1MT-2 Kgm-1s-2

Power L2MT-3 m2kgs-3 or Js-1 or W (Watt)Pressure/stress L-1MT-2 m-1kgs-2 or Nm-2 or Pa(Pascal)Specific death constant T-l S-1

Specific growth rate T-l S-1

Specific production rate T-l S-1

Specific volume L3M-1 Kg-1m3

Surface tension MT-2 Nm-l

Viscosity (dynamic) L-1MT-1 Pa.sViscosity (kinematic) L2T-1 m2s-1

Page 10: Introduction to Engineering Calculations - Bio-Engineering

1.1.2 Natural Variables (1)

• Dimensionless variables, dimensionless groups or dimensionless numbers

• No unit(s) or any standard of measurement is required for their magnitudes

e.g. the aspect ratio of a cylinder

• Other natural variables involve combinations of substantial variables that do not have the same dimensions

• Engineers make frequent use of dimensionless numbers for succinct representation of physical phenomena

e.g.

Page 11: Introduction to Engineering Calculations - Bio-Engineering

1.1.2 Natural Variables (2)• Other dimensionless variables relevant to bioprocess engineering are the

Schmidt number, Prandtl number, Sherwood number, Peclet number, Nusselt number, Grashof number, power number etc.

• Rotational phenomena;

• Degrees, which are subdivisions of a revolution, are converted into revolutions or radians before application in engineering calculations

Page 12: Introduction to Engineering Calculations - Bio-Engineering

1.1.3 Dimensional Homogeneity in Equations (1)• Equations representing relationships between physical variables must

be dimensionally homogeneous

Margules equation for evaluating fluid viscosity:

• The argument of any transcendental function, such as a logarithmic, trigonometric, exponential function, must be dimensionless ;

e.g. cell growth is: where x = cell concentration at time t, xo = initial cell concentration, and = specific growth rate

Page 13: Introduction to Engineering Calculations - Bio-Engineering

1.1.3 Dimensional Homogeneity in Equations (2)• The displacement y due to action of a progressive wave with

Amplitude A, frequency ω/2π and velocity v is given by the equation:

• The relationship between α the mutation rate of Escherichia coli and temperature T, can be described using an Arrhenius-type equation:

• Integration and differentiation of terms affect dimensionality

Page 14: Introduction to Engineering Calculations - Bio-Engineering

1.1.4 Equations Without Dimensional Homogeneity

• Equations in numeric or empirical equations

• Equations derived from observation rather than from theoretical principles

•Richards' correlation for the dimensionless gas hold-up ϵ in a stirred fermenter

P (hp)V = ungassed liquid volume(ft3)u = linear gas velocity(ft/s)ϵ = fractional gas hold-up (dimensionless)

Page 15: Introduction to Engineering Calculations - Bio-Engineering

1.2 Units (1)

•Unit names and their abbreviations have been standardised according to SI convention

• SI convention - unit abbreviations are the same for both singular and plural and are not followed by a period

• SI prefixes are used to indicate multiples and sub-multiples of units

•No single system of units has universal application

Page 16: Introduction to Engineering Calculations - Bio-Engineering

1.2 Units (2)

• Base Units - units for base quantities

•Multiple units - multiples or fraction of base unit e.g. minutes, hours, milliseconds or all in term of base unit second

•Derived units - obtained in one of two ways;

Multiplying and dividing base units (m2, ft/min, kgm/s2)

Defined as equivalents of compound units ( 1 erg = 1 g. cm/s2, 1 lbf = 32. 1 74 lbm. ft/s2)

Page 17: Introduction to Engineering Calculations - Bio-Engineering

1.2 Units (3)• Familiarity with both metric and non-metric units is necessary

• In calculations it is often necessary to convert units

• Units are changed using conversion factors

1 in = 2.54 cm ; 2.20 lb = 1 kg ; 1 slug = 14.5939kg

• Unit conversions are not only necessary to convert imperial units to metric; some physical variables have several metric units in common use e.g. (centipoise, kgh-1m-1), (Pa, atm, mmHg), (km/h, m/s, cm/s)

• Unity bracket e.g. 1lb = 453.6g

;

Page 18: Introduction to Engineering Calculations - Bio-Engineering

1.2.1 SI PrefixesFactor Prefix Symbol Factor Prefix Symbol1024 yotta Y 10-1 deci d1021 zetta Z 10-2 centi c1018 exa E 10-3 milli m1015 Peta P 10-6 micro μ1012 Tera T 10-9 nano n109 Giga G 10-12 pico p106 Mega M 10-15 femto f103 Kilo k 10-18 atto a102 Hecto h 10-21 zepto z101 Deca da 10-24 yocto y

Page 19: Introduction to Engineering Calculations - Bio-Engineering

1.2.2 UNIT CONVERSION DEVICES

THE CALCULATOR

Page 20: Introduction to Engineering Calculations - Bio-Engineering

1.3 Force and Weight• In the British or imperial system, pound-force (lbf) = (1 lb mass) x

(gravitational acceleration at sea level and 45o latitude)

Units N, kgms-2, gcms-2, lbfts-2 ; 1N = 1kgms-2, 1lbf = 32.174lbmfts-2

Calculate the kinetic energy of 250 Ibm liquid flowing through a pipe at 35 ft s-I. Express your answer in units of ft-lbf

• Weight changes according to the value of the gravitational acceleration

Page 21: Introduction to Engineering Calculations - Bio-Engineering

MEASUREMENT CONVENTIONS

Page 22: Introduction to Engineering Calculations - Bio-Engineering

1.4 Density, Specific Weight and Specific Volume

•Densities of solids and liquids vary slightly with temperature

• Specific gravity a dimensionless variable also known as relative density

• Specific volume is the inverse of density

• The density of solutions is a function of both concentration and temperature

•Gas densities are highly dependent on temperature and pressure

Page 23: Introduction to Engineering Calculations - Bio-Engineering

1.5 Mole

•Amount of a substance containing the same number of atoms, molecules, or ions as the number of atoms in 12 grams of 12C

• There are 6.022 × 1023 (Avogadro’s Constant) atoms of carbon in 12 grams of 12C

Page 24: Introduction to Engineering Calculations - Bio-Engineering

1.5.1 Molar mass• It is the mass of one mole of substance, and has dimensions MN-l

• Unit: g/mol

• Examples

H2 hydrogen 2.02 g/mol

He helium 4.0 g/mol

N2 nitrogen 28.0 g/mol

O2 oxygen 32.0 g/mol

CO2 carbon dioxide 44.0 g/mol

• Molar mass also referred to us molecular weighte.g. How many atoms of Cu are present in 35.4 g of Cu? (Cu = 63.5)

Page 25: Introduction to Engineering Calculations - Bio-Engineering

1.6 Chemical compositions

•Mole fraction•Mass fraction•Mass percent e.g. sucrose solution with a concentration of

40% w/w•Volume fraction

•Volume percent e.g. H2SO4(aq) mixture of 30% (v/v) solution

•Molarity•Molality•Normality

Page 26: Introduction to Engineering Calculations - Bio-Engineering

1.7 Temperature• Two most common temperature scales are defined using the freezing point (Tf )

and boiling point (Tb ) of water at 1 atm.

Celsius(or centigrade) scale Tf = 0oC and Tb = 100oC Absolute zero on this scale falls at -273.15oC

Fahrenheit scale Tf = 32oF and Tb = 212oF Absolute zero on this scale falls at - 459.67oF

The Kelvin and Rankin scale are defined at absolute value of Celsius and Fahrenheit;

T(K) = T(oC) + 273.15 T(oR) = T(oF) + 459.67 T(oR) = 1.8 T(K) T(oF) = 1.8T (oC) + 32

Page 27: Introduction to Engineering Calculations - Bio-Engineering

1.8 Pressure

•Units - psi, mmHg, atm, bar, Nm-2 etc.

• Absolute pressure is pressure relative to a complete vacuum

• It is independent of location, temperature and weather, absolute pressure is a precise and invariant quantity

• Pressure-measuring devices give relative pressure, also called gauge pressure

Absolute pressure = gauge pressure + atmospheric pressure

Page 28: Introduction to Engineering Calculations - Bio-Engineering

1.9 Standard Conditions and Ideal Gases

• Ideal gas - a hypothetical gas that obeys the gas laws perfectly at all temperatures and pressures

• A standard state of temperature and pressure is used when specifying properties of gases, particularly molar volumes

• Volume of a gas depends on the quantity present, temperature and pressure

• 1gmol of a gas at standard conditions of 1atm and 0°C occupies a volume of 22.4 litres

Page 29: Introduction to Engineering Calculations - Bio-Engineering

Boyle’s lawAt fixed n and T,

PV = constant or

P1V

n = number of moles of gas molecules

1.9.1 Ideal gas equation(1)

Page 30: Introduction to Engineering Calculations - Bio-Engineering

1.9.1 Ideal gas equation (2)

At fixed n and P,

Charles’ law

TVT is the absolute temperature in Kelvin, K

Page 31: Introduction to Engineering Calculations - Bio-Engineering

1.9.1 Ideal gas equation (3)

PV = nRT

PRnTV R is the same for all gases

R is known as the universal gas constant

nV Avogadro’s law

P1V Boyle’s law

Charles’ lawTV

Ideal gas equation

Page 32: Introduction to Engineering Calculations - Bio-Engineering

1.10 Chemical Equation and Stoichiometry

• What can we learn from a chemical equation?

C7H16 + 11O2 7CO2 + 8H2O

1. What information can we get from this equation?

2. What is the first thing we need to check when using a chemical equation?

3. What do you call the number that precedes each chemical formula?

4. How do we interpret those numbers?

Page 33: Introduction to Engineering Calculations - Bio-Engineering

1.11 Stoichiometry• It’s concerned with measuring the proportions of elements that

combine during chemical reactions

• Atoms and molecules rearrange to form new groups in chemical or biochemical reactions

C6H12O6 2C2H5OH + 2CO2

• Total mass is conserved

• Number of atoms of each element remains the same

• Moles of reactants ≠ moles of products

Page 34: Introduction to Engineering Calculations - Bio-Engineering

C7H16 + 11O2 7CO2 + 8H2O

If 10 kg of C7H16 react completely with the stoichiometric quantity, how many kg of CO2 will be produced? = 30.8 kg

Example

Page 35: Introduction to Engineering Calculations - Bio-Engineering

1.11.1 Stoichiometry Terminologies (1)

• Limiting reactant is the reactant present in the smallest stoichiometric amount. It is the compound that will be consumed first if the reaction proceeds to completion

• Excess reactant is a reactant present in an amount in excess of that required to combine with all of the limiting reactant

Page 36: Introduction to Engineering Calculations - Bio-Engineering

1.11.1 Stoichiometry Terminologies (2)

• Limiting and Excess Reactants

Consider a balanced chemical reaction: aA +bB cC +dD

• Suppose x moles of A and y moles of B are present and they react according to the above reaction,

Page 37: Introduction to Engineering Calculations - Bio-Engineering

1.11.1 Stoichiometry Terminologies (3)• Conversion is the fraction or percentage of a reactant converted into

products

• Degree of completion is usually the fraction or percentage of the limiting reactant converted into products

Page 38: Introduction to Engineering Calculations - Bio-Engineering

1.11.1 Stoichiometry Terminologies (4)• Selectivity is the ratio of the moles of the desired product produced to

the moles of undesired product (by-product)

• Yield is the ratio of mass or moles of product formed to the mass or moles of reactant consumed

Page 39: Introduction to Engineering Calculations - Bio-Engineering

2CH3OH C2H4 + 2H2O

3CH3OH C3H6 + 3H2O

If the desired product is ethylene, then the selectivity is

Example

Page 40: Introduction to Engineering Calculations - Bio-Engineering

THANK YOU VERY MUCH