When.com Web Search

  1. Ad

    related to: continuous stirred tank reactor in series experiment

Search results

  1. Results From The WOW.Com Content Network
  2. Continuous stirred-tank reactor - Wikipedia

    en.wikipedia.org/.../Continuous_stirred-tank_reactor

    The continuous stirred-tank reactor (CSTR), also known as vat-or backmix reactor, mixed flow reactor (MFR), or a continuous-flow stirred-tank reactor (CFSTR), is a common model for a chemical reactor in chemical engineering and environmental engineering. A CSTR often refers to a model used to estimate the key unit operation variables when using ...

  3. Continuous reactor - Wikipedia

    en.wikipedia.org/wiki/Continuous_reactor

    Reactors can be divided into two broad categories, batch reactors and continuous reactors. [1] Batch reactors are stirred tanks sufficiently large to handle the full inventory of a complete batch cycle. In some cases, batch reactors may be operated in semi batch mode where one chemical is charged to the vessel and a second chemical is added slowly.

  4. Damköhler numbers - Wikipedia

    en.wikipedia.org/wiki/Damköhler_numbers

    The residence time scale can take the form of a convection time scale, such as volumetric flow rate through the reactor for continuous (plug flow or stirred tank) or semibatch chemical processes: D a I = reaction rate convective mass transport rate {\displaystyle \mathrm {Da_{\mathrm {I} }} ={\frac {\text{reaction rate}}{\text{convective mass ...

  5. Plug flow reactor model - Wikipedia

    en.wikipedia.org/wiki/Plug_flow_reactor_model

    Each plug of differential volume is considered as a separate entity, effectively an infinitesimally small continuous stirred tank reactor, limiting to zero volume. As it flows down the tubular PFR, the residence time ( τ {\displaystyle \tau } ) of the plug is a function of its position in the reactor.

  6. Chemical reactor - Wikipedia

    en.wikipedia.org/wiki/Chemical_reactor

    When a reactor is brought into operation, either for the first time or after a shutdown, it is in a transient state, and key process variables change with time. There are three idealised models used to estimate the most important process variables of different chemical reactors: Batch reactor model, Continuous stirred-tank reactor model (CSTR), and

  7. Residence time - Wikipedia

    en.wikipedia.org/wiki/Residence_time

    The concept of residence time originated in models of chemical reactors. The first such model was an axial dispersion model by Irving Langmuir in 1908. This received little attention for 45 years; other models were developed such as the plug flow reactor model and the continuous stirred-tank reactor, and the concept of a washout function (representing the response to a sudden change in the ...

  8. Levenspiel plot - Wikipedia

    en.wikipedia.org/wiki/Levenspiel_plot

    For a continuous stirred-tank reactor (CSTR), the following relationship applies: [1] [2] = where: is the reactor volume; is the molar flow rate per unit time of the entering reactant A; is the conversion of reactant A

  9. Attainable region theory - Wikipedia

    en.wikipedia.org/wiki/Attainable_Region_Theory

    A combination of reactors is often termed a reactor structure. An example of the reactors that are considered for this theory are Continuous flow stirred-tank reactor (CSTR) and a Plug flow reactor model (PFR). Knowledge of the AR helps to address two areas in chemical reactor design: