How Cellular Information is Altered Flashcards

(189 cards)

1
Q

HOW CELLULAR
INFORMATION IS ALTERED

A

Mutation and Selection
Natural Mechanisms for Gene Transfer and Rearrangement
Genetically Engineering Cells
Genomics

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2
Q

We can alter cells by using mutation or genetic engineering.

A

HOW CELLULAR
INFORMATION IS ALTERED

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3
Q

____________ is the purposeful transfer of DNA from one type of organism to another.

A

Genetic Engineering

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4
Q

_________ is subjecting the cells to stress, causing changes in the genetic make-up.

A

Mutation

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5
Q

___________ = mistakes in the genetic code (can arise from replication and/or damage)

A

Mutations

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6
Q

____________ = organism with a genetic mutation

A

Mutant

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7
Q

_________ = the organism without the genetic organism

A

Wild type

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8
Q

______________ = genetic construction of an organism

A

Genotype

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9
Q

_________ = characteristics expressed by an organism.

A

Phenotype

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10
Q

__________ = usually refers to transcription + translation + post-translation processing.

A

Expression

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11
Q

If the mutation is in the active site, there may be some _________ consequences.

A

enzyme activity

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12
Q

If the mutation changes the amino acid to a ________, the resulting _______ will be ________ and probably ___________.

A

stop codon, protein, truncated, not active

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13
Q

If the amino acid is the same as before the mutation there is _____________

A

no consequence

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14
Q

If the amino acid is different, but not in the ________ of the active site, there _________

A

region, may be no consequences.

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15
Q

confers upon the mutant an advantage for growth, survival or detection under a set of environmental conditions that the wild type does not have

A

Selectable mutation:

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16
Q

Antibiotic resistance
Ability to grow on toluene
Inability to produce lysine
Ability to produce bioluminescence
Ability to produce more of an enzyme
Inability to grow at higher temperatures

A

SELECTION

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17
Q

____________ mutations per cell conversion

A

10^-3 - 10^-9

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18
Q

10^-6 = ________________

A

1 mutation/1,000,000 divisions

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19
Q

_________: chemicals, radiation

A

Mutagens

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20
Q

Lots of growth (i.e. lots of divisions)

A

INCREASE MUTATION RATES

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21
Q

WHY DO WE WANT TO
INCREASE MUTATIONS?

A

We want a cell to develop specific characteristics that are advantageous for us.

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22
Q

_____________: uptake of free DNA by a cell. The cell membrane has to be permeable to DNA.

A

Transformation

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23
Q

_____________: DNA is carried into the call in a phage.

A

Transduction

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24
Q

_________: Cell-to-cell transfer of DNA.

A

Conjugation

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25
Also called mating.
Conjugation
26
Using ___________, engineers and microbiologists were able to increase penicillin from 0.001 g/L to 50 g/L.
mutation and selection
27
Using natural mechanisms to purposefully manipulate DNA. The DNA is manipulated outside of the cell, and then sent into the cell.
GENETIC ENGINEERING
28
__________: enzymes that cut DNA at specific sequences. Different enzymes will cut at different sequences.
Restriction enzymes
29
______________: A method to detect what sizes of DNA a sample contains.
Gel electrophoresis (Southern Blot)
30
______________: A process used to make many copies of a piece of DNA.
Polymerase chain reaction (PCR)
31
_____________: self replicating, circular piece of DNA that can survive in a cell.
Plasmid
32
________________recognition sequence cuts long DNA more frequently and produces smaller DNA fragments than a restriction enzyme with a six-nucleotide recognition sequence.
A restriction enzyme with a four-nucleotide
33
Any given __________ occurs in DNA, on average, at a distance of 256 (4^4)nucleotides.
four nucleotide long recognition site
34
Any given _________________ occurs, on average, at a distance of 4096 (4^6) nucleotides.
six nucleotide long sequence
35
Any given __________________ occurs, on average, at a distance of 65536 (48) nucleotides.
eight nucleotide long sequence
36
allows scientists to extract and analyze bits of microbial DNA from samples, meaning they don't need to find and grow whole cells.
PCR
37
is an essential element in DNA fingerprinting and in the sequencing of genes and entire genomes.
PCR
38
Basically, it's like a technique to photocopy pieces of DNA. In a matter of a few hours, a single DNA sequence can be amplified to millions of copies
PCR
39
lets scientists work with samples containing even very small starting amounts of DNA.
PCR
40
The technique makes use of the DNA repair enzyme polymerase. This enzyme, present in all living things, fixes breaks or mismatched nucleotides in the double- stranded DNA helix. These breaks or mismatches could cause genes to malfunction if left unfixed.
PCR
41
Polymerase uses the intact half of the DNA molecule as a template and attaches the right nucleotides, which circulate constantly in the cell, to the complementary nucleotide at the site of the break. (DNA consists of two strands of nucleotide bases, which are represented as A, G, C, and T. In the laws of DNA base-pairing, A joins with T and G with C.)
PCR
42
Not all polymerases are created equal, however. Many fall apart in high heat.
PCR
43
PCR was developed in ______ following the discovery of an unusual heat-loving bacterium called ________ in a hot spring in __________
1985, Thermus aquaticus, Yellowstone National Park.
44
This bacterium's polymerase, dubbed Taq, does its job of matching and attaching nucleotides even in the high heat generated by the successive_________ cycles required during PCR.
"photocopying"
45
______ made PCR possible.
Taq
46
_________: changing conditions - transient (S, X, growth rate), high initial substrate, different phases of growth.
Batch
47
________: steady-state, constant low concentration of substrate, constant growth ratethat can be set by setting the dilution rate (ie. the feed flow rate).
Chemostat
48
__________ is more efficient.·
Chemostat
49
____________ is more common.
Batch
50
CHOICE OF CONTINUOUS VS BATCH PRODUCTION
Productivity Flexibility Control Genetic stability Operability Economics Regulatory
51
_________: rate of product per time per volume. Chemostat is better for growth-associated products. Wasted time in batch process.
Productivity
52
____________: the ability to make more than one product with the same reactor. Batch better.
Flexibility
53
___________: maintaining the same conditions for all of the products produced. In theory, the chemostat is better, steady state. In reality???
Control
54
____________: maintaining the organism with the desired characteristics. Chemostat selects for fast-growing mutants that may not have the desired characteristics.
Genetic stability
55
___________: maintaining a sterile system. Batch better.
Operability
56
____________: validating the process. Initially, many process batch, too expensive to re-validate after clinical trials.
Regulatory
57
Consider the production of a growth-associated product (like cell mass) in _________.
suspension culture
58
__________ of a chemostat is detrimental to engineered organisms.
Selective pressure
59
______ is more mechanically reliable.
Batch
60
________ system is more more flexible.
Batch
61
SPECIALIZED REACTORS
Chemostat with recycle Multistage chemostat Fed-batch Perfusion
62
_________ under the control of an inducible promoter
Recombinant product
63
________ at the same rate if the recombinant product is not expressed.
Recombinant strain and wild type grow
64
If the __________is expressed, the _____________ grows much slower.
recombinant product, recombinant strain
65
First chemostat is fed with a non-inducing growth substrate, allowing the recombinant strain to be produced.
MULTISTAGE CHEMOSTAT
66
The effluent from the first chemostat feeds a second chemostat that is fed inducer, and the product is produced.
MULTISTAGE CHEMOSTAT
67
Note: new recombinant cells are continually added to the second chemostat not allowing take-over by a fast growing mutant.
MULTISTAGE CHEMOSTAT
68
_________ reactors gain some advantages of a CSTR, retain some disadvantages of batch
Fed-batch
69
Reduces substrate inhibition or catabolic repression, allows for high conversion, and the extension of stationary phase.
Fed-batch
70
______ nature usually leads to higher operation cost and batch variability.
Semi-batch
71
________ cultures are started as batch cultures and grown to an initial cell concentration X, after which fed-batch operation begins.
Fed-batch
72
Substrate is consumed at the same rate it is added.
QUASI-STEADY STATE
73
Usually, fed-batch cultures are taken through many feedings cycles, with each feeding cycle followed by a harvest cycle during which the volume is drawn back down to V0 and the cycle begun again.
REPEATED FED-BATCH
74
PERFUSION CULTURE
Animal Cell culture Constat medium flow Cell retention Selective removal of dead cells Removal of cell debris, inhibitory by products High medium use, costs raw materials and sterilization.
75
IMMOBILIZED CELL SYSTEMS
High cell concentrations Cell reuse Eliminates cell washout at high dilution rates High volumetric productivities May provide favorable microenvironment Genetic stability Protection from shear damage
76
Mass transfer (diffusional) resistance
MAJOR LIMITATION
77
Whole cells provide cofactors, reducing power, energy that many enzymatic reactions require.
ADVANTAGE OVER IMMOBILIZED ENZYMES
78
_____________: similar to enzyme immbolization. Entrapment and binding.
Active Immobilization
79
_____________: Biofil-multilater growth on solid surfaces.
Passive Immobilization
80
PHYSICAL ENTRAPMENT
Widely used method of cell immobilization. Various matrices: porous polymers (agar, alginate, carrageenan, polyacrylamide. Chitosan, gelatin, collagen) Porous metal screens Polyurethane Silica gel Polystyrene Cellulose triacetate Polymer beads are also typically used Encapsulation Macroscopic membrane-based reactors (hallow fiber)
81
Method of preparing polymer beads:
Gelation of polymers Precipitation of polymers Ion exchange gelation Polycondensation Polymerization
82
There is direct contact between nutrient and suppor materials.
PHYSICAL ADSORPTION
83
High cell loadings
PHYSICAL ADSORPTION
84
Disadvantages: porous support materials causes intraparticle pore diffusion (at high cell densities) and hard to control microenvironmental conditions
PHYSICAL ADSORPTION
85
Selective of suitable support materials is highly based on adsorption capacity and strength of binding
PHYSICAL ADSORPTION
86
In general, good support materials should be rigid and chemically inert, should bind cells firmly, high loading capacity.
COVALENT BINDING
87
Widely used for enzymes but not for cells.
COVALENT BINDING
88
Multilayer growth of cells on solid support surfaces
PASSIVE IMMOBILIZATION: BIOLOGICAL FILMS
89
Support materials can be biologically active or inert
PASSIVE IMMOBILIZATION: BIOLOGICAL FILMS
90
Common in waste water treatment and mold fermentations
PASSIVE IMMOBILIZATION: BIOLOGICAL FILMS
91
DIFFUSIONAL LIMITATION
Analysis similar to immobilized enzymes. Damkoler number Effectiveness factor Thiele modulus.
92
___________: feed flows through a column packed with immobilized cells. Similar to a plug flow reactor. Can be recycles chamber.
Packed-column
93
_________: feed flows up through a bed of immobilized cells, fluidizing the immobilized cell particles.
Fluidized-bed
94
________: air bubbles suspend the immobilized cell particles in a reactor.
Airlift
95
SOLID-STATE FERMENTATIONS
Fermentation of solid materials Low moisture levels or water activities Agricultural products or foods Smaller reactor volume Low contamination due to low moisture Easy product separation Energy efficiency Differentiate microbiological structures
96
Cellular metabolism produces heat, removed by internal coils or reactor jackets.
Heat Removal
97
Cellular metabolism produces compounds that promote foaming. Controlled by mechanical foam breakers and chemical additives.
Foam Control
98
Cellular respiration requires oxygen. Sparged air, impeller makes smaller bubbles and increases residence time.
Providing Oxygen
99
Single organism desired. Steam and filtering.
Sterilization
100
Good oxygen mass transfer High energy requirement for mixing Seal to maintain, keep sterile.
Agitated Tank
101
Low shea environment No seal needed Restricted to low viscosity Less mixing than agitated tank Bubble coalescence limits air flow rate
Bubble Column
102
Better mixing than bubble column with same low shear and energy requirements and lack of seal. Work with higher viscosity liquids than bubble columns. Still less mixing than agitated tank
Loop reactors
103
WHAT FACTORS LIMIT SIZE OF REACTORS
Ability to provide oxygen and remove heat.
104
REACTOR TYPES
Stirred-tank Bubble Column Airlift Propeller Loop Jet Loop
105
Impeller breaks bubbles into smaller ones to provide for better oxygen mass transfer
AGITATED TANKS
106
are typically glass, commercial fermentors are typically stainless steel
Bench-top tanks
107
Heat removal/addition is typically by coils along the wall, or a water jacket around the tank
AGITATED TANKS
108
prevents foaming problems, but can cause additional mass transfer resistance
Antifoam
109
volume of liquid in tank; does not include head space
"working volume"
110
must not allow contamination
Seal for agitator shaft
111
are used to augment mixing and gas dispersion
Baffles
112
__________: disc with 6 to 8 blades. Pumps fluid in a radial direction. Compartmentalization with multiple impellers on a shaft.
Rushton impellers
113
_______________: pumps liquid in a vertical direction. Lower energy for the same oxygen mass transfer. Lower shear rates.
Axial flow impeller
114
OXYGEN MASS TRANSFER
Bulk gas phase oxygen concentration Tranfer across stagnan gas layer Partitioning into the liquid phase (C* at saturation) Transfer actress stagnant liquid layer Bulk liquid concentration ( CL) Transfer across stagnan liquid layer to cell.
115
Transfer rate at _________ is determined by the slowest rate (just like on a highway)
steady state
116
______ is not the rate at which you provide air to the reactor. You will actually provide much more oxygen to the reactor than is transferred to the cells.
OTR
117
Utilizes a ________ with actively growing cells.
fermentor
118
The air to the fermentor is shut off, and the DO decreases due to consumption by the microorganisms. The air is then turned on, and the the DO increases.
DYNAMIC METHOD
119
Make the controlling regime the same on the small scale as on the large scale.
SCALE-UP
120
Empirical
SCALE-UP
121
SCALE-UP CRITERION
Power Input - OTR Liquid circulation rate - mixing time Tip speed - shear Reynolds number - geometry
122
________ by requiring characteristic times to be constant between the small and large scale.
Scale-up
123
Many types of characteristic times are related to mixing, diffusion, oxygen mass transfer, reaction, and growth.
ANOTHER METHOD
124
COMMON ON-LINE INSTRUMENTATION
pH Temperature Dissolved oxygen Foam Flow Rates Level Off-gas composition (CO2,O2,VOCs)
125
is generally not as sophisticated as chemical production process control due to a lack of on-line sensors.
Fermentation process control
126
Each probe into the ____________ the probability of contamination, difficult to sterilize some probes, probe fouling, probe placement (gradients within the fermentor).
fermentorincreases
127
Form a group of three and describe 5 control loops based on the most common instrumentation.
TYPICAL FERMENTOR CONTROL SCHEMES
128
Identify the measured variable, and the controlled variable-specifying what is the final control element (ie. valve, pump, etc.)
TYPICAL FERMENTOR CONTROL SCHEMES
129
the absence of detectable, viable organisms.
Sterilization
130
reduction in the amount of detectable, viable organisms.
Disinfection
131
__________: some portion of the population is more resistant to sterilizing agents than other portions.
Sterilization is probabilistic
132
______: Heat-sensitive liquids and gases. Most common for gases - P important.
Filter
133
_______: Most common for liquids and equipment. Steam. Typically 121°C.Time and T are important. Risk degrading medium components.
Heat
134
_____: Surfaces.
Radiation
135
_____: Risk of toxic residues.
Chemical
136
______ - a faster growing contaminating organism can outgrow the desired organism and cause a washout of the desired organism.
Chemostat
137
_________ - the product can be biologically contaminated (could be lethal) or the purity profile could be significantly effected (indust. fermentations 100 kl).
Batch
138
to clean with the purpose of removing possible biological and nonbiological threats to human health.
Sanitize
139
to greatly reduce the number of living organisms.
Disinfect
140
to eliminate all viable organisms present (often our goal).
Sterilize
141
(filtration equipment, reactors, etc.) can be sterilized by heat, microfiltration, radiation, chemical agents, and UV light.
Fluids and process equipment
142
a cell, spore, or virus that is dead will not reproduce (cells and viruses) or germinate (spores) under conditions favorable for growth (opposite is “viable”)
Death
143
is a common method.
Thermal sterilization
144
is common for the insides of reactors that can't be heat or steam sterilized.
Ethylene oxide
145
(heat labile vitamins, proteins, sugars) must be filter sterilized using filters with narrow pore-size distributions.
Media that can't be heat sterilized
146
70% v/v ETOH in water with HCl to pH 2 is a ____________________.
good sterilizing fluid
147
is commonly used to sterilize filtration equipment.
Weak (3%) sodium hypochlorite solution
148
GENERAL APPROACH
1.Separation of insoluble products or Components. 2.Primary isolation or concentration and removal of water. 3.Purification and removal of contaminated chemicals. 4.Product preparation.
149
FACTORS THAT IMPACT DIFFICULTY AND COST OF RECOVERY
1.Product can be biomass, intracellular, or extracellular components. 2.Fragile or heat sensitive. 3.Concentration or titer in the broth. 4.Typically, recovery and purification are more than 50% of total manufacturing costs.
150
INSOLUBLE PRODUCTS OR COMPONENTS
Filtration Centrifugation Coagulation and Flocculation
151
Most cost-effective, most common in industrial biotechnology.
Filtration
152
Rotary vacuum precoat filters: traditional. Penicillin mold.
Filtration
153
Cross-flow ultrafiltration: 0.02-0.2 um bacterial separations.
Filtration
154
Cross-flow microporous filtration 0.2-2 um for yeast.
Filtration
155
Used to separate solids of size. 01 um to 100 um using centrifugal forces.
Centrifugation
156
Being replaced by microfiltration
Centrifugation
157
Pretreatment to centrifugation, gravity settling, or filtration to improve separation.
Coagulation and Flocculation
158
________: formation of small flocs of cells using coagulating agents electrolytes.
Coagulation
159
________: formation of agglomeration of flocs into settleable particles using flocculating agents, polyelectrolytes, or CaCl2
Flocculation
160
Used wastewater treatment processes to improve clarification.
Coagulation and Flocculation
161
Mechanical Methods
Sonication Bead beating Pressing
162
Non-Mechanical Methods
Osmotic shock Freeze-thaw Enzymatic
163
_______: disrupts cell membrane. Mostly used at the laboratory scale.
Ultrasound
164
_________: extrude cell paste at high pressure.
Pressing
165
__________: grind cells with glass, metal beads.
Bead beating
166
________ is a problem with all of these methods.
Heat dissipation
167
____________: salt differences to cause the membrane to rupture. Common.
Osmotic shock
168
________: Causes cell membrane to rupture. Common.
Freeze-thaw
169
_________: Lysozyme attacks the cell wall.
Enzymatic
170
SEPARATION OF SOLUBLE PRODUCTS
Liquid-liquid extraction Aqueous two-phase extraction Precipitation Adsorption Dialysis Reverse osmosis Ultrafiltration and microfiltration Cross-flow filtration and microfiltration Chromatography Electrophoresis Electrodialysis
171
Separate inhibitory fermentation products from broth.
LIQUID-LIQUID EXTRACTION
172
Based on the solubility difference for the compound between the phases.
LIQUID-LIQUID EXTRACTION
173
PRECIPITATION
Solubility reduction at low temperatures (less than - 5°C) by adding organic solvents.
174
- inorganic salts (NH4)2SO4 at high ionic strength.
Salting out
175
Membrane separation is used to remove low molecular weight solutes.
DIALYSIS
176
Used to remove salts from protein solutions.
DIALYSIS
177
Transport occurs due to a concentration gradient driving force.
DIALYSIS
178
Sal phase becomes more concentrated.
REVERSE OSMOSIS (RO)
179
pressure is applied to the salt phase, causing water to move against a concentration gradient.
REVERSE OSMOSIS (RO)
180
_________: Transport of water molecules from a high to a low concentration of pure water to salt water.
Osmosis
181
Pressure-driven molecular sieve to separate molecules of different sizes.
ULTRAFILTRATION AND MICROFILTRATION
182
____________: retained components accumulate on the filter. Gel layer formed on the filter.
Dead end filtration
183
_____________: retained components flow tangentially across the filter.
Cross filtration
184
Separates mixtures into components by passing the mixture through a bed of adsorbent particles.
CHROMATOGRAPHY
185
Solutes travel at different speeds through the column resulting in the separation of the solutes.
CHROMATOGRAPHY
186
Highly specific interaction between a ligand on the particle and a component in the mixture. Often based on antibodies.
AFFINITY CHROMATOGRAPHY
187
Separation of molecules based on size and charge in an electric field.
ELECTROPHORESIS
188
Membrane separation to separate charged molecules from a solution.
ELECTRODIALYSIS
189
FINISHING STEPS
Crystallization Drying