Moran | Plant Optimization in the Process Industries | Buch | 978-1-119-70773-8 | www.sack.de

Buch, Englisch, 352 Seiten, Format (B × H): 178 mm x 254 mm, Gewicht: 826 g

Moran

Plant Optimization in the Process Industries

Incorporating Equipment/Assets in the Decision-Making Process
1. Auflage 2024
ISBN: 978-1-119-70773-8
Verlag: Wiley

Incorporating Equipment/Assets in the Decision-Making Process

Buch, Englisch, 352 Seiten, Format (B × H): 178 mm x 254 mm, Gewicht: 826 g

ISBN: 978-1-119-70773-8
Verlag: Wiley


Optimize asset decisions and improve the financial and technical operation of process plants

The process industries, particularly the refining and petrochemical industries, are comprised of capital-intensive business whose assets are valued in the trillions. Optimizing the function of refining and petrochemical plants is therefore not simply a process decision, but a business one, with even small improvements in efficiency potentially providing enormous margins. There is an urgent need for businesses to assess how the asset side of process industry production can be optimized.

Plant Optimization in the Process Industries offers a pioneering asset-focused approach to plant optimization. Optimization of operating values within a processing unit is a developed area of technology with a wide and varied literature; little attention has been paid to the asset side, making this a groundbreaking and invaluable work. Outlining a multi-tiered approach to financial optimization which adjusts the variables of a statistical asset model, this volume has the potential to revolutionize businesses and generate record profit margins.

Readers will also find: - Comparison and contrast of different technologies on the process and asset side of the industry
- Detailed discussion of constrained, non-linear optimization technology, along with basic functioning of Monte Carlo modelling

- A real-world case study followed through the book to facilitate understanding

This book is ideal for professionals who manage, design, operate, and maintain process industry facilities, particularly those in the hydrocarbon and chemical industries, as well as any asset-intensive industry.

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Autoren/Hrsg.


Weitere Infos & Material


Foreword by Ron Lambert xxi

About the Author xxiii

Acknowledgments xxviii

Disclaimer xxx

1 Optimizing a Process Plant 1

1.1 High-Level Business Goals 1

1.2 Profit 1

1.3 Each Plant Is Unique 3

1.4 Plant Optimization Nirvana 3

1.5 Process/Asset Views of the Business Need Alignment 5

1.6 Optimization Technologies on the Process Side of the Business 6

1.7 Optimization Technologies on the Asset Side of the Business 7

1.8 Conclusion 10

1.9 Future Chapters 11

2 Gen 1 – Transitioning from Reliability to Asset Management 14

2.1 Reliability’s Early Days 14

2.2 Rebranding Reliability to be Asset Management 15

2.3 Changing the Reliability Management Structure 16

2.4 Where Did Gen 1 Fall Short? 16

2.5 Adoption of Monte Carlo Simulation Technology Has Struggled 16

2.6 Asset Optimization Nirvana – The Future 17

2.7 Conclusion 19

3 Gen 2 – Plant Optimization Using Asset Modeling Methodologies 20

3.1 Gen 2 Philosophy 20

3.2 Gen 2 Asset Optimization Applications 23

3.3 Conclusion 31

4 Selecting the Best Improvement Projects – Optimal Process Unit Availability 32

4.1 Industry Challenge 34

4.2 Improvement Projects 35

4.3 Asset Optimization Technologies 38

4.4 Optimizer Definition 42

4.5 Optimization Example 45

4.6 More General Optimization 58

4.7 Does Reducing Availability Make Sense for Any of Our Process Units? 58

4.8 Conclusion 59

5 Monte Carlo Simulation Overview 61

5.1 Reliability Block Diagram (RBD) 62

5.2 Rolling the Dice 63

5.3 Histories within a Model Run 64

5.4 Results 65

5.4.1 Probability Distributions 65

5.5 Submodel – Detailed Process Unit Model 67

5.6 What Level of Detail Is Required? 68

5.7 Definitions 68

5.8 RAM Software Tools 69

5.9 Challenge to Monte Carlo Simulation Vendors 69

5.10 Conclusions 70

6 Optimizer Overview 71

6.1 Independent Variables 71

6.2 Dependent Variables 72

6.3 Constraints 72

6.4 Objective Function 72

6.5 Optimizer Problem Definitions 73

6.6 Conclusions 82

7 The Consultation Process – The Main Work Process 83

7.1 Nobody Has Excellent Data in the Process Industries 83

7.2 Why Operating Conditions Are so Important in the Process Industries 84

7.3 Tapping into Your Company’s Innate Knowledge 84

7.4 Golden Opportunity To Test the Approach 85

7.5 Consulting Meeting Details 87

7.6 Monte Carlo Modeler Software Inputs 91

7.7 Data from Asset Management Systems 92

7.8 Data Storage/Structure 93

7.9 Conclusion 94

8 Turnaround Considerations 95

8.1 Example Problem Overview 97

8.2 Results Expectations 102

8.3 Solution Approach 106

8.4 First Problem – Fixed Start Date and Duration 108

8.5 Second Problem – Fixed Start Date, but Flexible Duration 113

8.6 Last Problem – Flexible Start Date 116

8.7 Conclusion 118

9 What About Process Conditions? 119

9.1 Examples Where Feed Quality and Process Conditions Play a Major Role 119

9.2 Operating Condition Effect on Failure Data 120

9.3 Example Incorporating Process Conditions into Our Problem Definition 121

9.4 Conclusion 125

10 Opportunistic Maintenance Optimization 126

10.1 Modeling Maintenance Plan Options 127

10.2 Example Problem Data 128

10.3 Single Equipment Opportunistic Maintenance Optimization 130

10.4 Intra Unit Opportunistic Maintenance Optimization 132

10.5 Inter Unit Opportunistic Maintenance Optimization 135

10.6 Conclusion 138

11 Spare Parts Optimization 139

11.1 Spares Parts Dependence Often Masks Other Equipment Issues 139

11.2 Typical Methods for Estimating Spare Parts 140

11.3 Logistical Challenges 140

11.4 Lead Times/Price/Vendor Issues 141

11.5 Prioritization 142

11.6 Example Problem Data 144

11.7 Effect of Failure Standard Deviation 148

11.8 Optimization Problems Overview 149

11.9 Single Equipment Spares Optimization 151

11.10 Intra-Unit Spares Optimization 152

11.11 Inter-Unit Spares Optimization 154

11.12 Common Spare Across Multiple Units 157

11.13 Full-time Spare Parts Engineer Position 161

11.14 Conclusion 161

12 Task/Resource Optimization 162

12.1 Example Problem Data 163

12.2 General Approach 164

12.3 Single Equipment Task Optimization 166

12.4 Intra-Unit Equipment Task Optimization 169

12.5 Inter-Unit Equipment Task Optimization 172

12.6 Conclusion 178

13 Tankage Determination/Optimization 179

13.1 Why Tankage Size Matters 179

13.2 Example Problem Overview 180

13.3 Same Availability for both Upstream and Downstream Process Units 181

13.4 Downstream Availability Variable with Constant Upstream Availability 182

13.5 Conclusion 184

14 Improving Availability 185

14.1 Options to Improve Availability 186

14.2 How Reliability and Process Configuration Effects Availability Results 189

14.3 Which Option Is the Best? 190

14.4 Conclusion 191

15 Equipment Reliability Optimization 192

15.1 General Approach 193

15.2 Example Problem Data 195

15.3 First Impressions of Example Data – Impact on Problem Solution 196

15.4 Effect of Failure Standard Deviation 197

15.5 Single Equipment Design Optimization 198

15.6 Intra-Unit Design Optimization 201

15.7 Inter-Unit Design Optimization 210

15.8 Scenario Final Thoughts 212

15.9 Conclusion 212

16 Plant Optimization Within the Design Process 214

16.1 Combining Process Simulation with Monte Carlo Simulation 214

16.2 Balancing the


Marty Moran is a chemical engineer who has concentrated his career on using advanced computer technology in the areas of Advanced Process Control, Asset Management/Reliability, and Plant Optimization to improve the financial and technical operation of process plants Mr. Moran holds a US patent for multivariable control. He has more than 35 years of experience and has worked for companies such as Setpoint, Continental Controls, AspenTech, Meridium, and Sadara, as well as his own personal consulting business.



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