This document outlines the objectives and key concepts of bacterial growth. It discusses the fastest and slowest known doubling times for bacteria under different conditions. It also explains the different phases of a bacterial growth curve (lag, exponential, stationary, death), including the mathematical equations that describe each phase. Additionally, it covers factors that influence growth rates like temperature, substrates, and environmental conditions. The Monod equation is presented which models bacterial growth in relation to substrate concentration.
its about the microbial kinetics of growth and substrate utilization.
Growth of a typical microbial culture in batch conditions.
Effect of substrate concentration on microbial growth .
Monad Equation
Fermentation
Scale up of fermentation
Steps in scale up
Scale up fermentation process
Optimizing scale up of fermentation process
Rules followed while doing scale up
Studies carried out during scale up
Reference
its about the microbial kinetics of growth and substrate utilization.
Growth of a typical microbial culture in batch conditions.
Effect of substrate concentration on microbial growth .
Monad Equation
Fermentation
Scale up of fermentation
Steps in scale up
Scale up fermentation process
Optimizing scale up of fermentation process
Rules followed while doing scale up
Studies carried out during scale up
Reference
Microbial Kinetics in Batch Culture
Culture system containing a limited amount of nutrient, which is inoculated with the microorganism. Cells grow until some component is exhausted or until the environment changes so as to inhibit growth. Biomass concentration defined in terms of cell dry weight measurements (g/l) or total cell number (cells/ml).
Lineweaver-Burke Equation.....We remember the Monod Equation
Invert…
The equation now has the form of a straight line with intercept.
Y = MX + C
By plotting as a function of
You get a straight line, where the slope is , and the y–axis intercept is .
Product Yield Coefficient
Maintenance:
Cells use energy and raw materials for two functions, production of new cells and the maintenance of existing cells. In general, consumption of materials for maintenance is small w.r.t. the amount of materials used in the synthesis of new biomass.
Generally it is assumed that the use of materials for maintenance is proportional to the amount of cells present.
“Bioleaching" or "bio-oxidation" employs the use of naturally occurring bacteria, harmless to both humans and the environment, to extract of metals from their ores.
Conversion of insoluble metal sulfides into water-soluble metal sulfates.
It is mainly used to recover certain metals from sulfide ores. This is much cleaner than the traditional leaching.
A fluidized bed reactor (FBR) is a type of reactor device that can be used to carry out a variety of multiphase chemical reactions.
In this type of reactor, a fluid (gas or liquid) is passed through a solid granular material (usually a catalyst possibly shaped as tiny spheres) at high enough velocities to suspend the solid and cause it to behave as though it were a fluid.
This process, known as fluidization, imparts many important advantages to the FBR.
As a result, the fluidized bed reactor is now used in many industrial applications
Basic Knowledge about industrial microorganism. why industry choose microorganism rather than chemical. isolation technique of microorganism. source of microorganisms. Process of using microorganism. Disadvantages of using microorganisms in industry. Process of genetic modification of microorganisms. Storage process of microorganism. preservation methods of microorganism. Reculture methods of microorganism.
Microbial Kinetics in Batch Culture
Culture system containing a limited amount of nutrient, which is inoculated with the microorganism. Cells grow until some component is exhausted or until the environment changes so as to inhibit growth. Biomass concentration defined in terms of cell dry weight measurements (g/l) or total cell number (cells/ml).
Lineweaver-Burke Equation.....We remember the Monod Equation
Invert…
The equation now has the form of a straight line with intercept.
Y = MX + C
By plotting as a function of
You get a straight line, where the slope is , and the y–axis intercept is .
Product Yield Coefficient
Maintenance:
Cells use energy and raw materials for two functions, production of new cells and the maintenance of existing cells. In general, consumption of materials for maintenance is small w.r.t. the amount of materials used in the synthesis of new biomass.
Generally it is assumed that the use of materials for maintenance is proportional to the amount of cells present.
“Bioleaching" or "bio-oxidation" employs the use of naturally occurring bacteria, harmless to both humans and the environment, to extract of metals from their ores.
Conversion of insoluble metal sulfides into water-soluble metal sulfates.
It is mainly used to recover certain metals from sulfide ores. This is much cleaner than the traditional leaching.
A fluidized bed reactor (FBR) is a type of reactor device that can be used to carry out a variety of multiphase chemical reactions.
In this type of reactor, a fluid (gas or liquid) is passed through a solid granular material (usually a catalyst possibly shaped as tiny spheres) at high enough velocities to suspend the solid and cause it to behave as though it were a fluid.
This process, known as fluidization, imparts many important advantages to the FBR.
As a result, the fluidized bed reactor is now used in many industrial applications
Basic Knowledge about industrial microorganism. why industry choose microorganism rather than chemical. isolation technique of microorganism. source of microorganisms. Process of using microorganism. Disadvantages of using microorganisms in industry. Process of genetic modification of microorganisms. Storage process of microorganism. preservation methods of microorganism. Reculture methods of microorganism.
The term “fermentation” is derived from the Latin verb fervere, to boil, thus describing the appearance of the action of yeast on extracts of fruit or malted grain. The boiling appearance is due to the production of carbon dioxide bubbles caused by the anaerobic catabolism of the sugars present in the extract. However, fermentation has come to have different meanings to biochemists and to industrial microbiologists. Its biochemical meaning relates to the generation of energy by the catabolism of organic compounds, whereas its meaning in industrial microbiology tends to be much broader. Fermentation is a word that has many meanings for the microbiologist: 1 Any process involving the mass culture of microorganisims, either aerobic or anaerobic. 2 Any biological process that occurs in the absence of O2. 3 Food spoilage. 4 The production of
1 Objectives • Measure carbon dioxide evolution and .docxjoyjonna282
1
Objectives
• Measure carbon dioxide evolution and
uptake in plants and animals.
• Study the effect of temperature on cell
respiration.
• compare respiration rates in germinating
and non-germinating peas.
Introduction
Energy is required by living organisms for
movement, transport, and growth. Nothing
happens without energy! The Sun is the
ultimate source of virtually all energy on the
planet Earth. Solar energy is captured by
plants through the process of photosynthesis.
The glucose molecules holding this energy are
broken down by metabolic processes, creating
usable energy for living systems.
Cellular respiration is a series of reactions in
which glucose molecules are broken down,
releasing stored chemical bond energy
(Figure 6.1). The released energy is used to
make the energy rich molecule ATP
(adenosine triphosphate). Carbon dioxide is
released as a by-product of the breakdown of
glucose. It is a crucial by-product from the
perspective of plants, because they need CO2
to perform photosynthesis.
Glycolysis is the first step in cellular
respiration, and it results in the net production
of two ATP molecules. In glycolysis, the 6-
carbon glucose molecules are “split” into two,
3-carbon pyruvate (pyruvic acid) molecules.
LAB TOPIC 6: RESPIRATION
Pyruvate has two potential routes – aerobic
respiration or anaerobic respiration [as either
lactate fermentation or alcohol fermentation]
(Figure 6.1).
1
In laboratory today, you will be examining
respiration in organisms that use aerobic
respiration, which makes use of oxygen. In
this pathway, pyruvate is broken down
completely, and h igh-energy electrons are
stripped away and passed through a series of
electron carriers. Energy is released at each
transfer, and is used to make a net 34 ATP
molecules. Oxygen is the final electron
acceptor in the electron transport system,
hence the name aerobic cellular respiration. In
lecture you will compare this process to
anaerobic respiration, which occurs in the
absence of oxygen or under low oxygen
conditions. The equation below summarizes
the process of aerobic respiration:
C6H12O6
+
6
O2
à 6
CO2
+
6
H2O
+
ATP
+
Heat
Glucose
Oxygen
Carbon
Water
Dioxide
Considering the equation for aerobic
respiration what variables could you measure
to monitor respiration rate?
Figure
6.1
Glycolysis
and
the
potential
fates
of
pyruvate
during
cellular
respiration.
2
2
Oxygen Consumption during Aerobic
Respiration
Aerobic respiration uses oxygen as the
terminal electron‐acceptor in the electron
transport chain and produces carbon dioxide
(see equation above). You can, therefore,
monitor the respiration rate of an organism by
measuring its uptake of oxygen or evo ...
Expt. 5 Bioassay of oxytocin using rat uterine horn by interpolation methodVISHALJADHAV100
Objective
Principle
Requirements
Experimental specifications (conditions)
Preparation of oxytocin standard solution
Preparation of De Jalon solution (PSS)
Procedure
Kymograph recording of contractions
Observation table
Graphical presentation of DRC
Calculation
Result and interpretation
Question 1. Two parallel flocculation basins are to be used to tre.docxIRESH3
Question 1. Two parallel flocculation basins are to be used to treat water flow of 150m3/s. If the design detention time is 20minute, what is the volume of each tank? If the average velocity gradient in these two tanks is 124/s, calculate the velocity gradient is each basin if the gradient in second basin is half of the first one.
Question 2. Determine the volume of the aeration tank for the following operating conditions:
Influent BOD5 concentration after the primary is = 150mg/L
Wastewater flow rate = 10MGD
F/M ratio = 0.2/d
Mixed Liquor volatile suspended solid concentration = 2200mg/L
Question 3. Given below is the wastewater characteristics, determine the F/M ratio? (10 Points)
Influent BOD5 concentration = 84mg/L
Wastewater flow rate = 0.150m3/s
Volume of the aeration tanks = 970m3
Mixed Liquor volatile suspended solid concentration = 2000mg/L
Question 4. What is the terminal settling velocity of a particle with a specific gravity of 1.4 and a diameter of 0.010mm in 20oC water? Would this particle be completely removed in a settling basin with a width of 10.0m, depth of 3.0m, a length of 30.0m, and a flow rate of 7500m3/d? What is the smallest diameter particle of specific gravity 1.4 that would be removed in the sedimentation basin described above?
Question 5. Will grit particle with a radius of 0.04mm and a specific gravity of 2.65 be collected in a horizontal grit chamber that is 13.5m in length if the average grit-chamber flow is 0.15m3/s, the width of the chamber is 0.56m, and the horizontal velocity is 0.25m/s? The wastewater temperature is 22oC.
Question 6. Wastewater treatment plant flow rate is 20MGD. Chlorine dosage is 10mg/L. Determine chlorine requirement (lb/day)
Question 7. If a particle having a 0.0170-cm radius and density of 1.95g/cm3 is allowed to fall into quiescent water having a temperature of 4oC, what will be the terminal settling velocity? Assume the density of water = 1000kg/m3. Assume Stoke’s law applies?
Question 8. If the terminal settling velocity of a particle falling in quiescent water having a temperature of 15oC is 0.0950cm/s, what is its diameter? Assume a particle density of 2.05g/cm3 and density of water equal to 1000kg/m3.
µ@15oC = 1.139 mPa-s
ρ @15oC = 999.103kg/m3
Question 9. Determine the diameter of a single-stage rock media filter to reduce an applied BOD5 of 125mg/L to 25mg/L. Use a flow rate of 0.14m3/s, a recirculation ratio of 12.0 and a filter depth of 1.83m. Assume the NRC equations apply and that the wastewater temperature is 20oC?
Question 10. Bacterial kill rate typically follows Chick’s law. If the first-order kill rate for a certain weak disinfectant is 0.067/h. Determine the time it will take to reduce the bacterial population to half of its original concentration?
Question 11. A town discharges 17,360 m3/d of treated wastewater into the Creek. The Creek has a flow rate of 0.43m3/s and the DO of the creek is 6.5 mg/L and DO of the wastewater is 1.0 mg/L. Compute the DO?
Questio ...
A workshop hosted by the South African Journal of Science aimed at postgraduate students and early career researchers with little or no experience in writing and publishing journal articles.
This slide is special for master students (MIBS & MIFB) in UUM. Also useful for readers who are interested in the topic of contemporary Islamic banking.
Synthetic Fiber Construction in lab .pptxPavel ( NSTU)
Synthetic fiber production is a fascinating and complex field that blends chemistry, engineering, and environmental science. By understanding these aspects, students can gain a comprehensive view of synthetic fiber production, its impact on society and the environment, and the potential for future innovations. Synthetic fibers play a crucial role in modern society, impacting various aspects of daily life, industry, and the environment. ynthetic fibers are integral to modern life, offering a range of benefits from cost-effectiveness and versatility to innovative applications and performance characteristics. While they pose environmental challenges, ongoing research and development aim to create more sustainable and eco-friendly alternatives. Understanding the importance of synthetic fibers helps in appreciating their role in the economy, industry, and daily life, while also emphasizing the need for sustainable practices and innovation.
Read| The latest issue of The Challenger is here! We are thrilled to announce that our school paper has qualified for the NATIONAL SCHOOLS PRESS CONFERENCE (NSPC) 2024. Thank you for your unwavering support and trust. Dive into the stories that made us stand out!
Safalta Digital marketing institute in Noida, provide complete applications that encompass a huge range of virtual advertising and marketing additives, which includes search engine optimization, virtual communication advertising, pay-per-click on marketing, content material advertising, internet analytics, and greater. These university courses are designed for students who possess a comprehensive understanding of virtual marketing strategies and attributes.Safalta Digital Marketing Institute in Noida is a first choice for young individuals or students who are looking to start their careers in the field of digital advertising. The institute gives specialized courses designed and certification.
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Exploiting Artificial Intelligence for Empowering Researchers and Faculty, In...Dr. Vinod Kumar Kanvaria
Exploiting Artificial Intelligence for Empowering Researchers and Faculty,
International FDP on Fundamentals of Research in Social Sciences
at Integral University, Lucknow, 06.06.2024
By Dr. Vinod Kumar Kanvaria
Normal Labour/ Stages of Labour/ Mechanism of LabourWasim Ak
Normal labor is also termed spontaneous labor, defined as the natural physiological process through which the fetus, placenta, and membranes are expelled from the uterus through the birth canal at term (37 to 42 weeks
Acetabularia Information For Class 9 .docxvaibhavrinwa19
Acetabularia acetabulum is a single-celled green alga that in its vegetative state is morphologically differentiated into a basal rhizoid and an axially elongated stalk, which bears whorls of branching hairs. The single diploid nucleus resides in the rhizoid.
2. Objectives
1.
The fastest known doubling time for a bacterium and under what
conditions this occurs
2.
The slowest estimated doubling time for a bacterium and under
what conditions this occurs
3.
Calculate a growth rate, u, from the slope of a growth curve
4.
Compare and contrast growth in pure culture with growth in the
environment
5.
The growth curve and the parts of the curve
6.
A mathematical equation for each part of the curve as well as the
Monod equation
7.
At least two electron acceptors that can be used under anaerobic
conditions in place of oxygen
8.
Whether aerobic or anaerobic metabolism yields more energy and
why
9.
The mass balance equation for aerobic metabolism
3. Growth Curve
S t a t io n a r y
7 .0
De
Expo
nent
ia l
10
Log CFU/ml
L o g C F U /m l
8 .0
6 .0
5 .0
4 .0
Lag
Lag
T im e
a th
O p tic l d e n s it y
Opticala Density
T u r b i d i t y ( o p t i c a l d e n s it y )
9 .0
4. Lag phase
Three causes for lag:
physiological lag
low initial numbers
appropriate gene(s) absent
growth approx. = 0
(dX/dt = 0)
5. Exponential phase
Nutrients and conditions are not limiting
growth = 2n
or
X = 2 nX 0
Where X0 = initial number of cells
X = final number of cells
n = number of generations
20
20
21
21
22
22
23
23
24
24
2n
2n
6. Viable Count (CFU/ml)
1.0e+8
1.0e+7
Example: An experiment was performed in a lab flask growing cells on
0.1% salicylate and starting with 2.21.0e+6 4 cells. As the experiment
x 10
below shows, at the end there were 3.8 x 109 cells.
1.0e+5
This is an increase is 5 orders of magnitude!!
1.0e+4
0
20
How many doublings or generations occurred?
40
60
80
Time (Hours)
X = 2nX0
3.8 x 109 = 2n(2.2 x 104)
1.73 x 10 = 2
5
n
log(1.73 x 105) = nlog2
17.4 = n
Cells grown on salicylate, 0.1%
100
7. How does this compare to growth in the soil?
Response of culturable microbial community to addition of a
carbon source.
Unamended
CFU/g soil
Soil
Pima
Brazito
Clover Springs
Mt. Lemmon
1% Glucose
CFU/g soil
Log Increase
5.6 x 105
1.1 x 106
1.4 x 107
1.4 x 106
4.6 x 107
1.1 x 108
1.9 x 108
8.3 x 107
1.9
2.0
1.1
1.7
Only a 1 to 2 order of increase!!
8. Now compare how environmental conditions
can impact metabolism in soil
Degradation of straw under different conditions
Residue
Wheat straw, laboratory
Rye straw, Nigeria
Rye straw, England
Wheat straw, Saskatoon
Half-life
Days
u
Days-1
Relative rate
9
17
75
160
0.008
0.04
0.01
0.003
1
0.5
0.125
0.05
9. Calculating growth rate during exponential growth
dX/dt = uX
where u = specific growth rate (h-1)
Rearrange: dX/X = udt
Integrate: lnX = ut + C, where C = lnX0
dX/dt = uX
where u = specific growth rate (h-1)
lnX = ut + ln X0 or
X = X0eut
y = mx + b (equation for a straight line)
Note that u, the growth rate, is the slope of this straight line
10. Calculating growth rate during exponential growth
dX/dt = uX
where u = specific growth rate (h-1)
Rearrange: dX/X = udt
Integrate: lnX = ut + C,
where C = lnX0
lnX = ut + ln X0 or
X = X0eut
y = mx + b (equation for a straight line)
Note that u, the growth rate, is the slope of this straight line
11. 0
20
40
60
80
100
Time (Hours)
Find the slope of this growth curve
lnX = ut + ln X0
or u = lnX – lnX0
t – t0
u = ln 5.5 x 108 – ln 1.7 x 105
8.2 - 4.2
= 2 hr-1
12. Now calculate the doubling time
If you know the growth rate, u, you can calculate the doubling time
for the culture.
lnX = ut + ln X0
For X to be doubled: X/X0 = 2
or: 2 = eut
From the previous problem, u = 2 hr-1,
2 = e2(t)
t = 0.34 hr = 20.4 min
What is fastest known doubling time? Slowest?
13. How can you change the growth rate???
When under ideal, nonlimiting conditions, the growth rate can only be
changed by changing the temperature (growth increases with increasing
temp.). Otherwise to change the growth rate, you must obtain a different
microbe or use a different substrate.
In the environment (non-ideal conditions), the growth rate can be
changed by figuring out what the limiting condition in that environment is.
Question: Is exponential growth a frequent occurrence in the
environment?
14. Growth Curve
T u r b i d i t y ( o p t i c a l d e n s it y )
9 .0
7 .0
De
6 .0
5 .0
4 .0
Lag
T im e
a th
O p tic a l d e n s it y
S t a t io n a r y
Stationary
Expo
nent
ia l
Log
10
C F U /m l
8 .0
15. Stationary phase
nutrients become limiting and/or toxic waste products accumulate
growth = death
(dX/dt = 0)
Death phase
death > growth
(dX/dt = -kdX)
16. Viable Coun
1.0e+6
Monod Equation
1.0e+5
The exponential growth equation describes only a part of the growth
curve as shown in the graph below.
1.0e+4
0
20
40
60
80
100
The Monod equation describes the dependence of the growth rate on the
Time (Hours)
substrate concentration:
u =
.
um S
Ks + S
u = specific growth rate (h-1)
um = maximal growth rate (h-1)
S = substrate concentration (mg L-1)
Ks = half saturation constant (mg L-1)
17. 1.0e+10
1.0e+9
Viable Count (CFU/ml)
Combining the Monod equation and the exponential growth equation allows
1.0e+8
expression of an equation that describes the increase in cell mass through
the lag, exponential, and stationary phases of growth:
1.0e+7
u =
um . S
Ks + S
Monod equation
1.0e+6
dX/dt = uX
1.0e+5
u = dX/Xdt
1.0e+4
0
20
40
60
80
Time (Hours)
Exponential growth equation
dX/dt = um. S . X
Ks + S
Does not describe death phase!
100
18. There are two special cases for the Monod growth equation
1.
At high substrate concentration when S>>Ks, the Monod equation
simplifies to:
dX/dt = umX
growth will occur at the
maximal growth rate.
2.
Ks
At low substrate concentration
when S<< Ks, the Monod equation
simplifies to:
dX/dt = um. S . X
Ks
growth will have a first order dependence on substrate concentration
(growth rate is very sensitive to S).
Which of the above two cases is the norm for environmental samples?
19. Growth in terms of substrate loss
In this case the growth equation must be expressed in terms of substrate
concentration. The equations for cell increase and substrate loss can be
related by the cell yield:
dS/dt = -1/Y (dX/dt)
where Y = cell yield
Y = g cell mass produced
g substrate consumed
Glucose (C6H12O6)
0.4
Pentachlorophenol (C6Cl5OH)
0.05
Octadecane (C18H38)
1.49
20. Growth in terms of substrate loss
dS/dt = -1/Y (dX/dt)
Combine with: dX/dt = um. S . X
dS/dt = - um (S . X)
Ks + S
Y (Ks + S)
R e m a in in g
p h e n a n th re n e (% )
Which parts of this curve does the equation describe?
0
1
2
3
4
T im e ( d a y s )
5
6
7
8
Editor's Notes
Nigeria hot all year round with a rainy season and a dry season
England is a warm summer and cold winter and plenty of rainfall
Saskatoon cold winters and summers in the high 60s. Plenty of rainfall