Welcome to Answerclub.org
Questions | Answers | Discussions | Knowledge sharing | Communities & more.
Sign Up to our social questions and Answers Engine to ask questions, answer people’s questions, and connect with other people.
Login to our social questions & Answers Engine to ask questions answer people’s questions & connect with other people.
Lost your password? Please enter your email address. You will receive a link and will create a new password via email.
Please briefly explain why you feel this question should be reported.
Please briefly explain why you feel this answer should be reported.
Please briefly explain why you feel this user should be reported.
Questions | Answers | Discussions | Knowledge sharing | Communities & more.
In batch culture, protogon is produced from peptone during the stationary phase with a yield of 0.4 protogon mg per g of peptone. If it is to be produced in a chemostat at a dilution rate of 0.5 h-1 from a medium containing 10 g.l-1 of peptone, then the rate of protogon synthesis would be
In batch culture, protogon is produced from peptone during the stationary phase with a yield of 0.4 protogon mg per g of peptone. 1 answer · Top answer: 0 g.l-1h-1.
In batch culture, protogon is produced from peptone during the stationary phase with a yield of 0.4 protogon mg per g of peptone.
1 answer
·
Top answer:
See less0 g.l-1h-1.
Mixing in an anaerobic sludge blanket reactor is due to
The sludge bed consists of biologically formed granules or thick flocculent sludge. Treatment occurs as the wastewater is exposed to the granular and or thick flocculent sludge. The gases produced causes internal mixing in the reactor.
The sludge bed consists of biologically formed granules or thick flocculent sludge. Treatment occurs as the wastewater is exposed to the granular and or thick flocculent sludge. The gases produced causes internal mixing in the reactor.
See lessThe lowest yield of ATP /is in
The order of potential ATP yield, from greatest to least, would be glucose, pyruvate, NADH, and acetyl CoA.
The order of potential ATP yield, from greatest to least, would be glucose, pyruvate, NADH, and acetyl CoA.
See lessThe continuous cultures are not widely used in industry because
Continuous fermentation is a superior tool in research, but the number of industrial applications is limited. Reasons for this include an increased risk for contamination, risk for genetic drift in the culture, and difficulties to control the process.
Continuous fermentation is a superior tool in research, but the number of industrial applications is limited. Reasons for this include an increased risk for contamination, risk for genetic drift in the culture, and difficulties to control the process.
See lessWhen two populations compete for a single growth limiting substrate in a continuous fermenter, which organism would not be washed out?
This is because of limitation of one or more of the essential nutrients. In continuous fermentation, the substrate is added to the fermenter
This is because of limitation of one or more of the essential nutrients. In continuous fermentation, the substrate is added to the fermenter
See lessThe lowest biomass yield in a culture of Escherichia coli will be in
The determined yield coefficients Y X,S were in the reported range of 0.35–0.5 g g−1 for E.
The determined yield coefficients Y X,S were in the reported range of 0.35–0.5 g g−1 for E.
See lessYield coefficient represents
The yield coefficient is commonly known as the substrate to biomass ratio to calculate the rate of cell growth of a microorganism within a product and also the calculation of the mass of the product with the increase in the cell growth.
The yield coefficient is commonly known as the substrate to biomass ratio to calculate the rate of cell growth of a microorganism within a product and also the calculation of the mass of the product with the increase in the cell growth.
See lessCommonly employed water insoluble supports for the covalent attachment of enzyme include
Some common water-insoluble supports used for covalent immobilization of enzymes are synthetic supports such as acrylamide-based polymers, maleic anhydride-based polymers, methacrylic acid-based polymers, styrene-based polymers, and polypeptides, and natural supports such as agarose, cellulose, dextRead more
Some common water-insoluble supports used for covalent immobilization of enzymes are synthetic supports such as acrylamide-based polymers, maleic anhydride-based polymers, methacrylic acid-based polymers, styrene-based polymers, and polypeptides, and natural supports such as agarose, cellulose, dextran, glass,
See lessThe most commonly employed cross-linked polymer is the
The matrix can be composed of particles, membranes, or fibers. The most commonly employed cross-linker polymer is the polyacrylamide gel system.
The matrix can be composed of particles, membranes, or fibers. The most commonly employed cross-linker polymer is the polyacrylamide gel system.
See lessIf Damkohler number, NDa >>1, the reaction rate is much greater than the mass transfer rate and the overall reaction is controlled by the rate of mass transfer. In this case, the enzyme reaction can be described as (where Csb and Cs are the substrate concentration in bulk of solution and at the immobilized enzyme surface respectively. ks mass transfer coefficient, and a is the surface area of an immobilized enzyme particles)
Damköhler's numbers ( D a and D a I I ) are dimensionless numbers used to relate the intrinsic reaction rate to the mass transport rate [11]. D a is the ratio of the reaction rate to the global movement rate of the fluid (see supporting information S1).
Damköhler’s numbers ( D a and D a I I ) are dimensionless numbers used to relate the intrinsic reaction rate to the mass transport rate [11]. D a is the ratio of the reaction rate to the global movement rate of the fluid (see supporting information S1).
See less