What are the operating conditions of ( plug flow reactor - CSTR - plug bed reactor...

What are the operating conditions of ( plug flow reactor - CSTR - plug bed reactor - batch reactor - semi-batch reactor ) ?

Expert Solution

Amanda K answered 2 years ago

With two possible reactions in parallel, which type of reactor (CSTR, Batch, or Plug Flow) will...

With two possible reactions in parallel, which type of reactor (CSTR, Batch, or Plug Flow) will you choose to maximize selectivity? F-->P1 r1= k1(CF)^a1 F-->P2 r2= k2(CF)^a2

What is a fluidized bed reactor? Explain the working of fluidized bed reactor in refineries with...

What is a fluidized bed reactor? Explain the working of fluidized bed reactor in refineries with a neat diagram? Mention the advantages and disadvantage of fluidized bed reactor.

1). A plug-flow reactor has a flow pattern of uniform velocity and concentration in the axial (longitudinal)...

1). A plug-flow reactor has a flow pattern of uniform velocity and concentration in the axial (longitudinal) direction. (T), (F) 2). For natural water (pH around 6−8), alkalinity is equal to the concentration of HCO3-. (T), (F) 3). Unit operation means a treatment unit in which “treatment” is accomplished through chemical/biological means. (T), (F) 4). Based on the law of mass action, the reaction rate is proportional to the remaining concentration of the products (T), (F) 5). Strict household use from public water supply systems is...

-Working of batch and continuous stirrer tankreactor And plug flow reactor - examples of distillation components...

-Working of batch and continuous stirrer tankreactor And plug flow reactor - examples of distillation components - Definition if fluid package & five example of fluid package

A packed bed reactor is also known as a fluidized bed reactor? Only when using an...

A packed bed reactor is also known as a fluidized bed reactor? Only when using an alias Depends on the catalyst used True Always false

A CSTR is used in production of A → R Feed enters the reactor at a...

A CSTR is used in production of A → R Feed enters the reactor at a rate of vo(L/s), and the concentration of the reactant in the feed is CAo (mol A/L) The volume of the tank is V(L). Assume that the process is a well-mixed process, so that the concentration of A in product stream equals that in the tank. For this process, the rate of consumption of A equals kCA[mol/ (s L of reaction volume)] Assume that all...

Confirm Continuous-Flow Stirred Tank Reactors (CFSTRs) in-series approximate a Plug-Flow Reactor (PFR). 1) Assume steady-state and...

Confirm Continuous-Flow Stirred Tank Reactors (CFSTRs) in-series approximate a Plug-Flow Reactor (PFR). 1) Assume steady-state and 1st order reaction kinetics 2) The total volume of the CSFTRs in-series is equal to the volume of the PFR. 3) Also, the total Hydraulic Retention time (HRT) of the CFSTRs in-series is equal to the HRT of the PFR.

A packed bed reactor is 2 m long with 0.2 m diameter. The reactor is filled...

A packed bed reactor is 2 m long with 0.2 m diameter. The reactor is filled with 1000 spherical particles with a diameter of 5 mm. Air enters the reactor at a volumetric flow rate of 0.0X m3/s. At these conditions, density of air is 1.2 kg/m3 with a viscosity y of 3.0 x 10-5 Pa.s. Calculate: - Porosity of the bed reactor. - The gas mass velocity, G. - Re number, at this value of Re would kinetics or...

An isothermic reaction is carried out adiabatically and the CSTR reactor design algorithm is shown as...

An isothermic reaction is carried out adiabatically and the CSTR reactor design algorithm is shown as below: The reaction is second order in A. The feed which is equimolar in a solvent and A, and its enters the reactor at a total volumetric flow rate, v0 of 10 dm3/min with the initial concentration of A being 4 M. The rate constant, k given as 0.1 dm3/mol.min at 380 K. Determine the conversion can be achieved in 600 dm3 CSTR by...

Experiment data taken in a batch reactor predicted the CSTR conversion should be 50%. However, the...

Experiment data taken in a batch reactor predicted the CSTR conversion should be 50%. However, the concentration measured in the actual CSTR was 57%. Suggest a reason for the discrepancy between the predicted and measured conversion.

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