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CHAPTER 6

CHAPTER 6

CHAPTER 6. RECYCLE STRUCTURE OF THE FLOWSHEET. 6.1 DECISIONS THAT DETERMINE THE RECYCLE STRUCTURE. The decisions that fix the recycle structure of the flowsheet are listed in Table 6.1-1. TABLE 6.1-1 Decision for recycle structure.

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Introduction to DESIGN II for Windows

Introduction to DESIGN II for Windows

Introduction to DESIGN II for Windows. Instructor: Murugan Selvan. Scopes Covered. The DESIGN II for Windows interface Tutorial 1: How DESIGN II works How to draw a flowsheet Component selection & input Equipment specification Execute the simulation The simulation results interface.

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ASPEN DYNAMICS

ASPEN DYNAMICS

ASPEN DYNAMICS. EXAMPLES. PRESENTED BY. UBAID UR REHMAN 2008-CHEM-19 ANAM ASIF 2008-CHEM-107. PRESENTATION LAYOUT. INTRODUCTION. This is an example of a batch column simulation and illustrates these features of Aspen Dynamics:

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DIP_09

DIP_09

DIP_09.ppt. Extractive Distillation Balance PFD Report Heat/Work streams Heat Exchangers Stream properties. Balance. Extraction distillation of the mixture ETOH + WATER (ETGL) using ethyleneglycol (ETGL) as solvent. Property method: NRTL

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Dr Saad Al-Shahrani

Dr Saad Al-Shahrani

Multiple Feed and Side Stream. Multiple Feed. F 1 + F 2 = B + D, F 1 x F1 + F 2 x F2 = Bx B + Dx D. There are three operating lines. a) Rectifying section. n. x D. D x D. L. V. n+1. F 1 x F1. q 1. k. b) Intermediate line. k+1. F 2 x F2. q 2. m. m+1. B x B.

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DS-2 controls the flow in the feed stream to give 75 MW

DS-2 controls the flow in the feed stream to give 75 MW

Note that I broke the recycle after the boiler. While not really necessary, it does make life easier. I used three design specs in this problem.

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103 views • 4 slides

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