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Isothermal Semi Batch Reactor

Isothermal Semi Batch Reactor

2018年10月2日

Inherently Safer Reactor Design: Challenges in the Changeover from Semi-Batch to Continuous

Inherently Safer Reactor Design: Challenges in the Changeover from Semi-Batch to Continuous

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Pure butanol is to be fed into a semi-batch reactor containing pure ethyl acetate to produce butyl acetate and ethanol. The reaction is elementary and reversible:The reaction is carried out isothermally at 300K. At this temperature, the equilibrium constant is 1.08 and the specific rate is 9 Ã— 10^-5 dm^3.mol^-1.s^-1. Initially, there is 200 dm^3 of ethyl acetate in the vat and butanol is fed at a rate of 0.05 dm^3.s^-1. The feed and initial concentrations of butanol and ethyl acetate are 10.93

Pure butanol is to be fed into a semi-batch reactor containing pure ethyl acetate to produce butyl acetate and ethanol. The reaction is elementary and reversible:The reaction is carried out isothermally at 300K. At this temperature, the equilibrium constant is 1.08 and the specific rate is 9 Ã— 10^-5 dm^3.mol^-1.s^-1. Initially, there is 200 dm^3 of ethyl acetate in the vat and butanol is fed at a rate of 0.05 dm^3.s^-1. The feed and initial concentrations of butanol and ethyl acetate are 10.93

2021年12月20日

pure butanol c4h9ohis fed into a semi batch reactor containing pure ethyl acetate ch3cooc2h5to produce butyl acetate ch3cooc4h9 and ethanol c2h5ohaccording to the following elementary and re 82913

pure butanol c4h9ohis fed into a semi batch reactor containing pure ethyl acetate ch3cooc2h5to produce butyl acetate ch3cooc4h9 and ethanol c2h5ohaccording to the following elementary and re 82913

2023年6月20日

Modelamiento, simulaci�n y propuesta de un esquema de control regulatorio de un reactor semibatch para la producci�n de polivinil acetato

Modelamiento, simulaci�n y propuesta de un esquema de control regulatorio de un reactor semibatch para la producci�n de polivinil acetato

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