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 ) ?

Solutions

Expert Solution

Amanda K answered 1 year ago

Next > < Previous

Related Solutions

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.

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.

(a) Explain briefly in what circumstances you would require a Packed Bed Reactor (PBR) in a...

(a) Explain briefly in what circumstances you would require a Packed Bed Reactor (PBR) in a chemical process. How is a PBR different from an ordinary Plug Flow Reactor (PFR). Use sketches and design equations to justify your answers. [8 marks] (b) The data in Table Q1 were obtained for the photochemical decay of liquid bromine dissolved in water when placed in sunlight: TABLE Q1 Time (min) 10 20 30 40 50 60 Bromine (ppm) 2.45 1.74 1.23 0.88 0.62...

Assume a biological process can be performed in either a plug flow or completely mixed flow reactor, and the process has a first-order reaction rate K of 0.5 hr-1.

Assume a biological process can be performed in either a plug flow or completely mixed flow reactor, and the process has a first-order reaction rate K of 0.5 hr-1. Assume an influent concentration of 100 mg/L, a regulatory required effluent concentration of 10 mg/L, and a flow rate of 100 m3/hr. a. What reactor volume (m3) is required if one completely mixed reactor is used? HINT: use the equation for a first order reaction with a CMR. b. What...

Subjects