Problem Solving in Chemical Reactor Design (eBook)

Juan A. Conesa (Autor)

eBook Download: EPUB

2024
691 Seiten
Wiley-VCH (Verlag)
978-3-527-84801-0 (ISBN)

Infos

Extensive workbook with more than 200 up-to-date solved problems on advanced chemical reactors for deeper understanding of chemical reactor design

Problem Solving in Chemical Reactor Design provides in-depth coverage of more than 200 solved complex reactor design problems extracted from core chemical engineering subject areas. The problems in this book cover the design of non-ideal, catalytic, multiphase, heterogeneous, and biochemical reactors rather than focusing on basic Chemical Reactor Engineering concepts.

Each complex problem is solved using simple procedures and mathematical tools, enabling readers to better understand the correct procedure for solving problems and solve them faster, more conveniently, and more accurately.

This book is inspired by more than two decades of the author's teaching experience in chemical reactor engineering. Accompanying electronic materials include spreadsheets and easily understandable Matlab^® programs, which can both be downloaded from the Wiley website.

Some of the topics covered in Problem Solving in Chemical Reactor Design include:

• Optimization, operation, and complexities of reactor design in the face of non-idealities such as mixing issues and residence time distributions
• Utilization of the tanks-in-series model, dispersion model, and intricate combinations of ideal reactors to elucidate the impact on conversion rates
• Signal processing within the domain of chemical reactor engineering, specifically focusing on convolution and deconvolution methodologies
• Reaction kinetics, diffusion dynamics, and catalyst efficiency in catalytic reactor design, and design of gas-catalytic and gas-liquid-solid catalyst systems in multiphase reactors

Problem Solving in Chemical Reactor Design is an excellent learning resource for students and professionals in the fields of chemical engineering, pharmaceuticals, biotechnology, and fine chemistry.

Juan A. Conesa, PhD, is a distinguished Professor of Chemical Engineering at the University of Alicante, Spain. With over 30 years of experience, his research focuses on decomposition kinetics, waste degradation, and pollutant analysis under various conditions. He is particularly renowned for his work on dioxins and furans analysis in waste treatment processes. Since 2015, he has led the research group 'Waste, Energy, Environment and Nanotechnology (WEEN)' at the University of Alicante.

Textauszug

1
Non-ideal Flow and Reactor Characterization

Summary of Residence Time Distribution Properties and Most Important Models

Residence Time Distribution

In a reactor, C(t) is obtained by injecting pulse of tracer. From that:

Total amount of tracer injected is:

In a step tracer run:

Mean residence time:

Variance of the residence time distribution (RTD):

The square root of the variance, σ, is called standard deviation.

Average residence time:

RTD in Ideal Reactors

For the plug flow reactor (PFR):

For the continuous stirred tank reactor (CSTR):

Tanks-in-series (TIS) Model

Dispersion Model

Bo < 0.01

Bo > 0.01, Closed–Closed Recipient

E(t) is only integrable by numerical methods.

Bo > 0.01, Open–Open Recipient

Designing E1 to the E(t) given by the first expression (valid for Bo < 0.01) and E2 to the one predicted by the open–open (o–o) assumption, the differences between these RTDs are small at low Bo, but at a high Bo number, E1 is not valid (for more details, consult spreadsheet “dispersion model Bo fitting.xls”):

Problem 1.1 A solution of potassium permanganate (KMnO4) was rapidly injected into a water stream flowing through a circular tube at a linear velocity of 35.70 cm/s. A photoelectric cell located 2.74 m downstream from the injection point was utilized to monitor the local concentration of KMnO4.

1. (a) By using the given effluent KMnO4 concentrations, calculate the average residence time of the fluid as well as the variance, E(t), F(t), and I(t).
2. (b) Determine the number of ideal tanks (nt), the variance, the dispersion number, and the Peclet number.

Time (s)	KMnO4 concentration

0.0

0.0

2.0

11.0

4.0

53.0

6.0

64.0

8.0

58.0

10.0

48.0

12.0

39.0

14.0

29.0

16.0

22.0

18.0

16.0

20.0

11.0

22.0

9.0

24.0

7.0

26.0

5.0

28.0

4.0

30.0

2.0

32.0

2.0

34.0

2.0

36.0

1.0

38.0

1.0

40.0

1.0

42.0

1.0

Solution to Problem 1.1

For details refer the Wiley website at http://www.wiley-vch.de/ISBN9783527354115

1. (a) To solve this problem, we should use a spreadsheet. First, data given in the statement are introduced, and then we should do the following calculations:

   t (s)	C(t)	C(t)dt	E(t)	t·E(t)	t·E(t)·Δt	(t − tm)2·E(t)	(t − tm)2·E(t)·Δt	F(t)	I(t)

   0

   0

   0

   0.000

   0.000

   0.000

   0.000

   0.000

   0.000

   1.000

   2

   11

   11

   0.014

   0.029

   0.029

   1.149

   1.149

   0.029

   0.971

   4

   53

   64

   0.069

   0.275

   0.304

   3.345

   4.494

   0.166

   0.834

   6

   64

   117

   0.083

   0.498

   0.773

   2.055

   5.399

   0.332

   0.668

   8

   58

   122

   0.075

   0.602

   1.100

   0.666

   2.721

   0.482

   0.518

   10

   48

   106

   0.062

   0.623

   1.224

   0.059

   0.725

   0.607

   0.393

   12

   39

   87

   0.051

   0.607

   1.230

   0.053

   0.112

   0.708

   0.292

   14

   29

   68

   0.038

   0.527

   1.134

   0.344

   0.397

   0.783

   0.217

   16

   22

   51

   0.029

   0.457

   0.983

   0.720

   1.065

   0.840

   0.160

   18

   16

   38

   0.021

   0.374

   0.830

   1.024

   1.744

   0.882

   0.118

   20

   11

   27

   0.014

   0.285

   0.659

   1.162

   2.186

   0.911

   0.089

   22

   9

   20

   0.012

   0.257

   0.542

   1.419

   2.581

   0.934

   0.066

   24

   7

   16

   0.009

   0.218

   0.475

   1.540

   2.959

   0.952

   0.048

   26

   5

   12

   0.006

   0.169

   0.387

   1.464

   3.004

   0.965

   0.035

   28

   4

   9

   0.005

   0.145

   0.314

   1.504

   2.968

   0.975

   0.025

   30

   2

   6

   0.003

   0.078

   0.223

   0.939

   2.443

   0.981

   0.019

   32

   2

   4

   0.003

   0.083

   0.161

   1.147

   2.086

   0.986

   0.014

   34

   2

   4

   0.003

   0.088

   0.171

   1.375

   2.522

   0.991

   0.009

   36

   1

   3

   0.001

   0.047

   0.135

   0.812

   2.187

   0.994

   0.006

   38

   1

   2

   0.001

   0.049

   0.096

   0.947

   1.759

   0.996

   0.004

   40

   1

   2

   0.001

   0.052

   0.101

   1.093

   2.040

   0.999

   0.001

   42

   1

   2

   0.001

   0.054

   0.106

   1.248

   2.341

   Σ(C(t)dt) = 771tm = 10.98 sσ2 = 46.88 s2

   We can calculate time increment as the difference between time in two experimental data; in the third column, concentration and time increment are multiplied. For a better calculation, instead of calculating C(t)·Δt for each time directly, we can use the average value of C(t) between two consecutive data. This is called Simpson’s rule for evaluating areas graphically. The sum of the values in this column would give the area of the C(t) curve, so in the fourth column, the following relationship is applied to calculate E(t):

   In the next columns, the average value of E(t) between two consecutive data is multiplied by time, by time increment, and the sum would represent mean time, as we have:

   In a similar way, variance is calculated:

   Finally, we can calculate F(t) and I(t) according to their definitions:

   We can check the form of the graphs showing the distributions:

2. (b) From the calculated parameters, it is easy to find the number of tanks in the TIS model:

   For the dispersion model to be applied, first we should assume Bo < 0.01, and then:

   We obtain Bo = 11.24 ≫ 0.01, so this assumption is not valid.

   Assuming now...

Produkt-Details

• Erscheint lt. Verlag: 4.9.2024
• Sprache: englisch
• Themenwelt: Naturwissenschaften ► Chemie
• Schlagworte: biochemical reactors • Catalyst Systems • catalytic reactors • Chemical Reactor Engineering • Heterogeneous Reactors • Multiphase Reactors • non-ideal reactors • Reaction kinetics • Reactor Design • reactor operation • reactor optimization
• ISBN-10: 3-527-84801-0 / 3527848010
• ISBN-13: 978-3-527-84801-0 / 9783527848010