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![Match the following kinetics variables with appropriate units.
Specificity Constant
Turnover number
Michaelis Constant
Maximum Velocity
1. []/s
2. []
3. s-1
4. [1-1.s-1
5. S
6. [1-1
7. s/[]](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Ffd4de583-e4d3-492c-a5f4-de371541259a%2F7df1580d-d62c-4e84-9c08-1c4416db73f9%2Fl1rbcbn_processed.jpeg&w=3840&q=75)
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- Based on your residing of this chapter, what would you expect to be the most immediate effect oil glycolysis, if the steady-state concentration of gJucose-6-P were 8.3 mM instead of 0.083 mM?calculate the reaction velocity at saturating substrate concentrations. Your numerical answer is assumed to be in units of M sec-1. [S] = 100 mM k1 = 10 sec-1 k2 = 3000 sec-1 k-1 = 20 sec-1 [E]T = 1 \muμMThe Ki for a competitive inhibitor pyrrole-2-carboxylate is 0.05M.Calculate the initial velocity if the substrate concentration is 0.25M and 1.0 mole/liter of the inhibitor is added to thereaction.
- The equation of the double reciprocal plot is y = 0.5294 x + 1.4960. What is the value of vmax (in M/s)? The substrate concentration is given in units of molarity (M) and reaction velocity has units of molarity per second (M/s). (Report to three significant figures)At steady state,[Es} stays the same although substrate concentraion is steadily decreasing and product concentraion is increasing .how do you explain this?An enzymatic reaction follows M-M kinetics with Vmax= 2.5 mol m-3s-1and Km = 5 mM.Calculate the time required for 50% conversion of the substrate in a batch reactor if theinitial substrate concentration is0.2 M.Show your calculation steps.
- With a ∆G°´ of -16.7 kJ/mol, the reaction catalyzed by hexokinase is considered to be _____. at equilibrium substrate and product concentration dependent freely reversible metabolically irreversible none of the aboveCalculate for the water activity of the soy sauce in 80.3% ERH. Suppose the soy sauce is subjected to a storage area with RH of 95.9%. What will be the water activity of the soy sauce?As a reference model, a 7 L baffled stirred-tank reactor with a 3:1 (H:D) aspect was employed to scale down to a 7 mL tiny bioreactor.Dt = 0.16 m; Di = 0.07 m; N = 100 rpm are the dimensions of the huge tank.1)Using geometric similarities, determine the dimensions of the micro bioreactor (Dt, Di, and H).
- Hi, if I have the substrate concentration as 20, 40 , 65 and the V(mol/min) no inhibitor 602, 690, 833 and with inhibitor 370, 476, 526. How would I plot these numbers on both a MMplot and an LB plot and How would I claulate the Km and Vmax for each graphDetermine the extent of advantage in terms of G factor reduction if a kraft cooking temperature is reduced from 1700C to 1650C, keeping the target H factor constant at1200 (at the cooking temperature) in both cases. The activation energies for the two processes are 32 and 40.3 kcal/mole.Calculate the percentage efficiency of extraction of phycocyanin in sample y, if the amount of phycocyanin is 57.8 mg, and the starting amount in sample x was 118.1 mg. Your answer should have one decimal place.
