'Mole balance' diaporamas de présentation

Lecture 1

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Professor De Chen Institutt for kjemisk prosessteknologi, NTNU Gruppe for katalyse og petrokjemi

Professor De Chen Institutt for kjemisk prosessteknologi, NTNU Gruppe for katalyse og petrokjemi Kjemiblokk V, rom 407 chen@nt.ntnu.no. Kjemisk reaksjonsteknikk Chemical Reaction Engineering H. Scott Fogler: Elements of Chemical Engineering www.engin.umich.edu/~cre

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Lecture 22

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CHEMICAL QUANTITIES

CHEMICAL QUANTITIES. All Roads Lead to the Mole. Measuring doughnuts: 1 dozen = 12 doughnuts (count) 1 dozen = 500 g doughnuts (mass) 1 dozen = 1 box doughnuts (volume). Measuring steam (H 2 O gas): 1 mole = 6.02 x 10 23 H 2 O molecules (count) 1 mole = 18.0 g H 2 O (mass)

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Lecture 2

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Lecture 2

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ERT 316: REACTION ENGINEERING CHAPTER 1 MOLE BALANCES

ERT 316: REACTION ENGINEERING CHAPTER 1 MOLE BALANCES. Lecturer: Miss Anis Atikah Ahmad Email: anisatikah@unimap.edu.my Tel: +604-976 3245. OUTLINE. Introduction Chemical Species Chemical Reaction Rate of Reaction General Mole Balance Equation Batch Reactor Continuous-Flow Reactors

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ERT 316: REACTION ENGINEERING CHAPTER 1 MOLE BALANCES

ERT 316: REACTION ENGINEERING CHAPTER 1 MOLE BALANCES. Lecturer: Miss Anis Atikah Ahmad Email: anisatikah@unimap.edu.my Tel: +604-976 3245. OUTLINE. Introduction Chemical Species Chemical Reaction Rate of Reaction General Mole Balance Equation Batch Reactor Continuous-Flow Reactors

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Lecture 12 Tuesday 2/12/08

Lecture 12 Tuesday 2/12/08. Multiple Reactions Selectivety and Yield Series Reactions Complex Reactions. Blood Coagulation.

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Lecture 19 Tuesday 3/18/08 Gas Phase Reactions Trends and Optimuns

Lecture 19 Tuesday 3/18/08 Gas Phase Reactions Trends and Optimuns. User Friendly Equations Relate T and X or F i. User Friendly Equations Relate T and X or F i. Heat Exchange. Elementary liquid phase reaction carried out in a PFR

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Lecture 19 Tuesday 3/18/08 Gas Phase Reactions Trends and Optimuns

Lecture 19 Tuesday 3/18/08 Gas Phase Reactions Trends and Optimuns. User Friendly Equations Relate T and X or F i. User Friendly Equations Relate T and X or F i. Heat Exchange. Elementary liquid phase reaction carried out in a PFR

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Lecture 6

Lecture 6. Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. Previous Lectures. Reactor Mole Balances in terms of conversion. X. Batch. t. X. CSTR. W. PFR. PBR.

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Lecture 5 Kjemisk reaksjonsteknikk Chemical Reaction Engineering

Lecture 5 Kjemisk reaksjonsteknikk Chemical Reaction Engineering. Isothermal reaction design algorithm Algorithm to estimate the time or conversion for different reactor Examples. Reaction Engineering. Isothermal reactor design. Mole Balance. Rate Laws. Stoichiometry.

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Lecture 5 Thursday 1/17/08

Lecture 5 Thursday 1/17/08. Block 1: Mole Balances Block 2: Rate Laws Block 3: Stoichiometry Stoichiometric Table: Flow Definitions of Concentration: Flow Gas Phase Volumetric Flow rate Calculate the Equilibirum Conversion X e.

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Mole balance for chemical reaction engineering (Design Equations for reactors)

Mole balance for chemical reaction engineering (Design Equations for reactors). Lec 3 week 3. The General Mole Balance Equation. To perform a mole balance on any system, the system boundaries must first be specified. The volume enclosed by these boundaries is referred to as the system volume.

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Chemical Reaction Engineering Asynchronous Video Series

Chemical Reaction Engineering Asynchronous Video Series. Chapter 5: Finding the Rate Law H. Scott Fogler, Ph.D. Algorithm. Consider the following reaction that occurs in a constant volume batch reactor: (We will withdraw samples and record the concentration of A as a function of time.).

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Chemical Reaction Engineering Asynchronous Video Series

Chemical Reaction Engineering Asynchronous Video Series. Chapter 5: Finding the Rate Law H. Scott Fogler, Ph.D. Algorithm. Consider the following reaction that occurs in a constant volume batch reactor: (We will withdraw samples and record the concentration of A as a function of time.).

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Chapter 2

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Chapter 4

Chapter 4. Isothermal Reactor Design. Overview. Chapter 1 and 2 focus on mole balances on reactors to predict the volume Chapter 3 focuses on reactions Cahpter 4 combine previous chapters to obtain optimum reactor design . Design Algorithm. Mole balance (reactor type)

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