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Suppose the reaction PhilHead --P2H20 is carried out at pH-400 and at a hydrogen gas pressure...
Suppose you carried out the decomposition reaction using 30.0 mL of reaction solution (i.e. 15.0 mL...
Suppose you carried out the decomposition reaction using 30.0 mL of reaction solution (i.e. 15.0 mL of 6.10% hydrogen peroxide and 15.0 mL of the solvent, water). Assume that you observed the pressure increase by 0.148 atm over a period of 20.0 seconds at a constant temperature, 20.5ºC. A. How many moles of oxygen gas are produced in 20.0 seconds? (Conversion factor = 0.1545 M/atm) B. What would be the concentration of oxygen (in molarity units) if the gas had...
An isothermal (170 °C) isobaric (6 atm) catalytic gas-phase reaction is carried out in a fluidized...
An isothermal (170 °C) isobaric (6 atm) catalytic gas-phase reaction is carried out in a fluidized CSTR: Assume that the reaction is elementary. The feed (benzene and hydrogen) is stoichiometric with θ。= 50-. The rate constant defined wrt benzene is 53 mol / (kgcat * min * atm) at 300 K with activation energy of 80 kJ/mol. What catalyst weight is required to reach 80% conversion? Hint: Use ideal gas law to relate pressure to concentrations (note the units of...
The second order gas phase irreversible reaction: 2.4-B is carried out in an isothermal batch reactor...
The second order gas phase irreversible reaction: 2.4-B is carried out in an isothermal batch reactor containing 40 kg of catalyst and with an initial volume of 60-liter. The reactor is initially filled with equal molar quantities of A and inert I at 300 K and 2.5 atm. Calculate the time needed for the concentration of product (B) to be 0.02 mole/liter if: a) the reaction takes in a constant pressure batch reactor (3 points) b) the reaction takes place...
energy il Camor P5-30 Pressure Drop. The gas phase reaction A+B C+D is carried out isothermally...
energy il Camor P5-30 Pressure Drop. The gas phase reaction A+B C+D is carried out isothermally at 227 C in a packed-bed reactor with 100 kg of catalyst. The reaction is first order in A and first order in B. The entering pres- sure was 20 atm and the exit pressure is 1 atm. The feed is equal molar in A onigA and B and the flow is in the turbulent regime with FA0 10 mol/min and CAO= 0.25 mol/dm3....
A common way to make hydrogen gas in the laboratory is to react a metal such...
A common way to make hydrogen gas in the laboratory is to react a metal such as zinc with hydrochloric acid. Suppose this reaction was carried out in a sealed flask with a pressure sensor connected. Before the reaction, the pressure sensor read 39.82 mmHg. After the reaction was complete, the pressure sensor read 705.89 mmHg. The volume of the flask was 155.2 mL and the temperature was 29.2ºC. What is the density (in g/L) of this gas? Enter only...
An aqueous phase reversible reaction ? ⇌ ? + ? is carried out in a batch...
An aqueous phase reversible reaction ? ⇌ ? + ? is carried out in a batch reactor. The forward reaction is first order wrt A and the backward reaction is first order wrt each component. Initial concentration of A is 1 mol/litre and no R and S are present initially. Derive an expression for ?? ⁄??. What is the maximum allowable conversion in the reactor? If this reaction happens in gas phase (constant pressure), derive an expression for ?? ⁄??....
The elementary gas phase reaction (A <--> 2B) is to be carried out in an adiabatic...
The elementary gas phase reaction (A <--> 2B) is to be carried out in an adiabatic CSTR. The feed which is at a temperature of 27oC, consists of 80% of A and the remainder inerts. The volumetric flow rate entering the reactor at this temperature is 100 l/min. The concentration of A in the feed at 27oC is 0.5 mol/liter. For 80% of the adiabatic equilibrium conversion, calculate the required reactor volume. DATA: CpA=12 J/mol.K; CpB=10 J/mol.K; CpI=15 J/mol.K deltaHrxn=-75000...
2. The irreversible gas phase reaction A B is carried out isothermally in a fluidized catalytic...
2. The irreversible gas phase reaction A B is carried out isothermally in a fluidized catalytic CSTR. The reaction rate is first orderw.r.t.the partial pressure of A (-rA KA PA). With arn entering pressure 20 atm, an negligible pressure drop in CSTR, and 50 kg of catalyst, a conversion of 50% was realized for pure A feed. |-Fluidized hal oooo -catalyst o ojo | |,'-/ pellets Now, a PBR is connected to the downstream of this CSTR with a same...
The reaction below, carried out at 272.67 K and 1.00 bar, carried out at constant pressure...
The reaction below, carried out at 272.67 K and 1.00 bar, carried out at constant pressure was found to release 329 kJ of heat and consume 21.8 g of oxygen. Calculate the internal energy change associated with this reaction. 2H2(g) + O2(g) → 2H2O(g) a. 331 kJ b. 329 kJ c. -331 kJ d. -327 kJ e. -329 kJ
The reaction below, carried out at 252.57 K and 1.00 bar, carried out at constant pressure...
The reaction below, carried out at 252.57 K and 1.00 bar, carried out at constant pressure was found to release 907 kJ of heat and consume 60.0 g of oxygen. Calculate the internal energy change associated with this reaction. 2H2(g) + O2(g) → 2H2O(g) a. -911 kJ b. 911 kJ c. -907 kJ d. -903 kJ e. 907 kJ
An isothermal (170 °C) isobaric (6 atm) catalytic gas-phase reaction is carried out in a fluidized CSTR: Assume that the reaction is elementary. The feed (benzene and hydrogen) is stoichiometric with θ。= 50-. The rate constant defined wrt benzene is 53 mol / (kgcat * min * atm) at 300 K with activation energy of 80 kJ/mol. What catalyst weight is required to reach 80% conversion? Hint: Use ideal gas law to relate pressure to concentrations (note the units of...
The second order gas phase irreversible reaction: 2.4-B is carried out in an isothermal batch reactor containing 40 kg of catalyst and with an initial volume of 60-liter. The reactor is initially filled with equal molar quantities of A and inert I at 300 K and 2.5 atm. Calculate the time needed for the concentration of product (B) to be 0.02 mole/liter if: a) the reaction takes in a constant pressure batch reactor (3 points) b) the reaction takes place...
energy il Camor P5-30 Pressure Drop. The gas phase reaction A+B C+D is carried out isothermally at 227 C in a packed-bed reactor with 100 kg of catalyst. The reaction is first order in A and first order in B. The entering pres- sure was 20 atm and the exit pressure is 1 atm. The feed is equal molar in A onigA and B and the flow is in the turbulent regime with FA0 10 mol/min and CAO= 0.25 mol/dm3....
2. The irreversible gas phase reaction A B is carried out isothermally in a fluidized catalytic CSTR. The reaction rate is first orderw.r.t.the partial pressure of A (-rA KA PA). With arn entering pressure 20 atm, an negligible pressure drop in CSTR, and 50 kg of catalyst, a conversion of 50% was realized for pure A feed. |-Fluidized hal oooo -catalyst o ojo | |,'-/ pellets Now, a PBR is connected to the downstream of this CSTR with a same...
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