Term 1 Flashcards
applications of biotechnology
AB production, Ab production, transgenic animals, gene therapy, vaccines, protein pharmaceuticals
do animal growth hormones have therapeutic value in humans
no
what happened when cadaver isolated growth hormones were used? What was done?
transfer of diseases such as creutzfeldt jacob disease and a shortage in availability. In 1980s, human growth hormone was produced using bacterial cells
pharmacists’ role in biotech
1) product evaluation and selection 2) patient education and counselling 3)provision of drug info 4) assistance in patient monitoring 5) drug control and prep
what plant cells have that animals don’t
cell wall, chloroplasts, and centriole
what has DNA/nucleus
chloroplasts, mitochondria and and nucleus all have DNA and nucleus (all double membraned)
how many nucleotides are in the human and mouse genome?
3 x 10^9
A pairs with
T (2 bonds)
G pairs with
C (3 bonds)
do introns or exons code for protein
exons
do higher organisms have more junk DNA (non coding, or “intron” regions)?
yes (only about 1.5% codes for proteins)
mRNA
duplication of genetic material
tRNA
translation of genetic material
rRNA
site for protein synthesis on ribosomes
what differs in RNA in base paits
U instead of T
nucleotide contains
sugar, phosphate, base
where does protein synthesis occur
cytoplasm
what enzyme initiates transcription
RNA polymerase
start codon
AUG
order of translation
initiation, elongation, termination
stop codons
UAA, UAG, UGA (has to be U and then at least one A)
there is at least one unique tRNA for each of the ___ (#) AAs
20
how to sequence DNA (what must we start with)
primer**, need before enzymes work
what kind of DNA do bacteria have
both plasmid and genomic
why manipulate plasmids?
easy to grow and maintain bacterial cells, plasmid DNA is easy to isolate
3 important sections of plasmid
promoter, reporter gene, multiple cloning site
2 key enzymes that made it possible to manipulate sequences of plasmids
restriction endonucleases (cut DNA by recognizing specific BPs), and DNA ligases (link DNA fragments)
what was the first biopharmaceutical
insulin
phases of bacterial growth
lag, log, stationary, death
explain lag phase
number of bacteria does not change with time
explain log phase
number of bacteria increases exponentially
explain stationary phase
no net change in number of bacteria- grow and divide at same rate and die. Happens when overcrowded and nutrients are depleting)Most important biological products (especially secondary metabolites like ABs) are produced here
explain death phase
bacteria decrease with time
any protein can be produced using genetically engineered organisms, but not every type of protein can be produced by any cell type
true
bacteria are not capable of post translational modifications
true- cannot glycosylate, etc
limitations to using bacterial expression systems
no post translational modification (mammalian can), proteolytic cleavage can degrade product, must break/lyse cell to get protein out (are secreted into media in mammalian cells)
animal cells have limits to dividing. How do you overcome this
hybridomas (genetically engineered animal cells with no limits on dividing- this is what cancer cells produce)
other name for bioreactor
fermentor (type where biocatalyst is a living cell)
step one in production of biopharms (synthesis)
cell culture started in small bottles, then small bioreactor, eventually large
types of cultivation systems
-free in suspension, -attached to microspheres or entrapped in matrices that are usually solidified agar, -or immobilized state as monolayers)
types of bioreactors
liquid (aka submerged) (most-saves space and more ammmenable to design, cost effective, easier to maintain, don’t have to worry about monolayers or microspheres are free in suspension)) or solid state (surface)
monitoring of bioreactors
temperature, sufficient substrate (usually carbon source), sugars/proteins.lipids, water, salts, vitamins, oxygen, optimum pH, product and by product removal
types of submerged (liquid) bioreactor operation types
batch, continuous, fed-batch
forms of biocatalyst for submerged (liquid) bioreactors
free cell (enzyme), immobilized cell (enzyme) (packed bed, membrane reactor)
bioreactor systems
stirred tank, airlift, microcarrier (ie fixed bed reactors)
stirred tank bioreactors
-air enters at bottoms, baffles range from 4-8, key factors controlled are pH/temp/oxygen, mixing method is mechanical agitation, requires energy input, bubbles are reduces by an agitator, exhaust gas flows out top
baffle purpose
used to reduce vortexing
what is mixing necessary for
maintain homogeneity, attain rapid dispersion and mixing of components injected into the fermentor, enhance heat transfer and temp control, enhance mass transfer
airlift bioreactors
reaction medium kept mixed and gassed by air or another gas at the base of reactor, seperated into gassed and ungassed regions generating a vertically circulating glow
advantages of airlift bioreactor
simple, no moving parts, less maintenance, less risk of defects and easier sterilization, lower shear rate, both plant and bacterial cells, well controlled flow and efficient mixing, large volume tanks possible which increases the output, enhances oxygen solubility achieved in large tanks with greater pressures, greater heat removal
disadvantages of airlift bioreactor
higher initial investment, greater air and higher pressures needed, impossible to maintain consistent levels of substrate, nutrients and oxygen with circulation and changing conditions, inefficient gas and liquid separation when foaming occurs
micro carrier bioreactors
can have extremely high productivity within a compact size, used for culture of immobilized mammalian cells, us porous glass beads to give large SA,
batch operations
everything put in vessel together, let it grow, watch for products, harvest. Once started, no inlet or outlet unless aerobic system and gas inlet and outlet should be there. Between batches, down time to harvest, empty, clean, sterilize and refill- lowers efficiency)
continuous operation
don’t add substrate all at once, remove throughout. Continuous medium flow- incoming stream (feed) contains substrate and leaving stream (effluent) contains product. Good to maintain bacteria in log phase (keep there longer), contamination more likely
2 assumptions with continuous operations
mixing is vigorous (concentrations are uniform throughout the reactor), effluent concentration is same with reactor contents (chemostat=continuous configurations for cultivation of microorganisms) (conditions don’t change through time=steady state-no accumulation of components ie too much feed, and no depletion of source ie too much effluent)
advantages of batch
-most commonly used because reduced contamination or mutation (due to relatively brief growing period), lower investment, more flexible, higher raw material conversion, easy to operate
disadvantages of batch
lower productivity (maintenance) (down time), increased focus on instrumentation, greater expense in preparing several subcultures for inoculation, higher labor and process control costs, batch to batch variability, accumulation of inhibitory products
continuous reactors advantages
increased opportunities for system investigation and analysis, higher degree of control, results are more reliable and reproducible (quality), efficient, higher productivity, uniform product, no accumulation of inhibitory proteins
disadvantage of continuous reactors
higher contamination and cell mutation risk (long growing periods and continuous reactions, higher investment, less flexible
fed batch
modification of batch cultivation in which nutrient is added intermittently
cell bank (and 2 types)
when cell line is to be used over many cycles- master cell (expanded to WCB) and working bank (ones currently use and experiment with)
cell banks must be tested for
contaminents, and some for viruses
higher speed centrifuge is required for separation of smaller particles
true
inclusion bodies
bacterial proteins aggregate - often occur when bacterial cells overproduce proteins through the use of plasmid expression
advantages and disadvantages of inclusion bodies
A- relatively simple to recover, protected from proteolytic cleavage D- biologically inactive- must be denatured first to be solubilized then refolded for activity, inaccurate assessment of recovery-can’t directly measure, recovery of proteins requires cell breakage/protein sedimentation/pellet washing.
disrupting cells can be 2 ways
-mechanical (sonication and liquid shear homogenization) and non (autolysis, osmotic shock)
if proteolytic degradation will occur, purification should be carried out at ___degrees celsius
4
inclusion bodies dissolve in denaturing agents such as
SDS, urea, guanidine HCl
if molecules are interlinked by disulfide bonds, must add ___ agents such as
reducing- mercaptoethanol, dithiothreitol (DTT)- they may enhance or facilitate the solubilization of protein inclusion bodies
presence of glycosylation can affect
solubility, stability, serum half life, pharmacological fx, immunogenicity
protein glycosylation is directly determined by DNA sequence
false
why can’t most proteins be sterilized by the standard methods
denaturation at high temperatures
components of parenteral formulations
solubility enhancers, anti adsorption and anti aggregation agents, buffer, antioxidants, preservatives, osmotic agents, carrier systems, active ingredient
why are solubility enhancers needed in parenteral formulations
generally a high concentration is used in biotech drugs, and this can cause proteins to aggregate and precipitate out (lowers potency, increasing change of immunogenicity). Interaction with excipients instead of other proteins= MOA
when does aggregation of proteins occur
hydrophobic or electrostatic interactions between different proteins
approaches to enhance solubility
proper pH and ionic conditions, additions of AA like lysine and arginine (tend to solubilize t-PA), adding surfactants (SDS), sugars like glucose and sucrose
what is used to prevent insulin adsorption
albumin- has higher affinity for surfaces (competition)
what is likely to form fibrillar precipitates
(long rod shaped structures); low concentrations of phopholipids and sufactants, insulin; solve by selecting proper pH often
common buffer system components in biotech
phosphate, citrate, acetate