2. Reaction Energy Calculations for Metabolic Process change of the reaction The standard free-energy phosphoenolpyruvate + ADP pyruvate + ATP is AG = -7.50 kcal/mol. If the reaction is initiated with 8.0 millimole/L of ADP, 8.0 millimole/L of phosphoenolpyruvate, 4.0 millimole/L of ATP, and 0.0 millimole/L of pyruvate, what will the final concentrations of the reactants and the products be if the reaction goes to completion?

Discuss challenges and obstacles to implementation of microservices architecture in the enterprise.

What is meant by a group method?

Briefly explain what is meant by “Control for Operability”.

AutoSave Document1 - Word O Search (Alt+Q) ff RICAMAE SALADAGA RS File Home Insert Draw Design Layout References Mailings Review View Help P Comments B Share X Cut O Find v Calibri (Body) - A A Aa v A AаBЬСcDd AaBbСcDd AaBbC AаBЬСc[ Аа B АавьссD v 11 LE Copy Replace Paste BIUV ab x, x A . I v A - I Normal 1 No Spac. Heading 1 Heading 2 Title Subtitle Dictate Sensitivity Editor Reuse S Format Painter A Select v Files Clipboard Font Paragraph Styles Editing Voice Sensitivity Editor Reuse Files |· 2: 1 1 |· ·1: 3.1. 4 5.. 6 . I 7.1· 8.I 10.1 11.| 12:1 13. 14. I 15. 16 17.1 18 | 19 II. The adiabatic exothermic irreversible gas-phase reaction 2A + B → 20 is to be carried out in a flow reactor for an equimolar feed of A and B. A Levenspiel plot for this reaction is shown in the figure: 500,000 400,000 300,000 FAO -rA 200,000 100,000 0.3 0.6 0.9 1. What PFR volume is necessary to achieve 50% conversion? 2. What CSTR volume is necessary to achieve 50% conversion? 3. What is the volume of a…

What are the disadvantages of pfr used in Chemical processing

What is the best method for estimating the distribution of nonkey components at the actual (operating) reflux?

2. A 1 L, 100 g (dry weight) sample is removed from a continuous crystallizer which is operated with a residence time of 1000 s. The following particle size distribution is obtained for the sample: i) Size range (um) Mass (g) 200- 300- 400 500 600-700- 800- 300 400 500 600 700 800 900 0- 100- 100 200 2.5 26.0 30.0 21.0 12.0 6.0 2.0 0.5 0.0 Microscopy based on the sieve fractions has found that a volumetric shape correction factor, ky, of 0.52, for the crystal population and the crystal density has been found to be 2000 kg/m³ Determine whether the MSMPR model describes the system. If it does so, then determine the growth and nucleation rates for this system; if it does not, suggest why reasons that may cause deviation of this CSTR type crystallizer from the MSMPR model.

this isnt what was asked. also copied and pasted from other question could someone show clearer working for 1 and 2 please   i am not sure where the (4v+1) comes from

reverse osmosis desalination Cartridge filters i need step by step please