{"product_id":"distillation-control-9780470381946","title":"Distillation Control","description":"\u003cb\u003eBook Synopsis\u003c\/b\u003e\u003cbr\u003e\u003cp\u003e\u003cb\u003eLearn to Design the Best Control Configuration for Any Distillation Column\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eToday, distillation is by far the most common separation technique used in the chemical and petroleum industries. All distillation columns need to be carefully controlled in order to meet specified production and quality levels. \u003ci\u003eDistillation Control\u003c\/i\u003e enables readers to do this by approaching the subject from a process to develop, analyze, and troubleshoot all aspects of column controls. Readers are efficiency and effectiveness and minimizing coats.\u003c\/p\u003e \u003cp\u003e\u003ci\u003eDistillation Control\u003c\/i\u003e begins with a chapter dedicated to underlying principles, including separation processes, reflux and boilup ratios, and composition dynamics. Next, the author covers such critical topics as:\u003c\/p\u003e \u003cul\u003e \u003cli\u003eComposition control\u003c\/li\u003e \u003cli\u003ePressure control and condensers\u003c\/li\u003e \u003cli\u003eReboilers and feed preheaters\u003c\/li\u003e \u003cli\u003eApplication of feedforward\u003c\/li\u003e \u003cli\u003eUnit optimization\u003c\/li\u003e \u003cli\u003eComplex towers\u003c\/li\u003e \u003c\/ul\u003e \u003cp\u003eAs reader\u003cbr\u003e\u003cbr\u003e\u003cb\u003eTable of Contents\u003c\/b\u003e\u003cbr\u003e\u003c\/p\u003e\u003cp\u003ePreface ix\u003c\/p\u003e \u003cp\u003e\u003cb\u003e1 Principles 1\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e1.1. Separation Processes 2\u003c\/p\u003e \u003cp\u003e1.2. Total Material Balance 9\u003c\/p\u003e \u003cp\u003e1.3. Reflux and Boilup Ratios 13\u003c\/p\u003e \u003cp\u003e1.4. Total Material Balance around Condenser 18\u003c\/p\u003e \u003cp\u003e1.5. Total Material Balance around Reboiler 21\u003c\/p\u003e \u003cp\u003e1.6. Component Material Balances 24\u003c\/p\u003e \u003cp\u003e1.7. Energy and the Separation Factor 28\u003c\/p\u003e \u003cp\u003e1.8. Multicomponent Distillation 35\u003c\/p\u003e \u003cp\u003e1.9. Stage-by-Stage Separation Model 38\u003c\/p\u003e \u003cp\u003e1.10. Formulation of the Control Problem 47\u003c\/p\u003e \u003cp\u003e1.11. Tower Internals 50\u003c\/p\u003e \u003cp\u003e1.12. Flooding 55\u003c\/p\u003e \u003cp\u003e1.13. Tray Hydraulics 59\u003c\/p\u003e \u003cp\u003e1.14. Inverse Response in Bottoms Level 62\u003c\/p\u003e \u003cp\u003e1.15. Composition Dynamics 65\u003c\/p\u003e \u003cp\u003eReferences 69\u003c\/p\u003e \u003cp\u003e\u003cb\u003e2 Composition Control 70\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e2.1. Product Specifications 71\u003c\/p\u003e \u003cp\u003e2.2. Columns in Series 75\u003c\/p\u003e \u003cp\u003e2.3. Composition Analyzers 78\u003c\/p\u003e \u003cp\u003e2.4. Temperature 83\u003c\/p\u003e \u003cp\u003e2.5. Distillate Composition Control: Constant Boilup 91\u003c\/p\u003e \u003cp\u003e2.6. Distillate Composition Control: Constant Bottoms Flow 96\u003c\/p\u003e \u003cp\u003e2.7. Operating Lines 100\u003c\/p\u003e \u003cp\u003e2.8. Temperature Profiles 106\u003c\/p\u003e \u003cp\u003e2.9. Feed Composition Disturbances 111\u003c\/p\u003e \u003cp\u003e2.10. Bottoms Composition Control 116\u003c\/p\u003e \u003cp\u003e2.11. Propagation of Variance in Level Control Configurations 122\u003c\/p\u003e \u003cp\u003e2.12. Level Control in Direct Material Balance Configurations 126\u003c\/p\u003e \u003cp\u003e\u003cb\u003e3 Pressure Control and Condensers 136\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e3.1. Pressure Control 137\u003c\/p\u003e \u003cp\u003e3.2. Once-Through Heat Transfer Processes 142\u003c\/p\u003e \u003cp\u003e3.3. Water-Cooled Condensers 147\u003c\/p\u003e \u003cp\u003e3.4. Flooded Condensers 151\u003c\/p\u003e \u003cp\u003e3.5. Air-Cooled Condensers 159\u003c\/p\u003e \u003cp\u003e3.6. Partial Condensers 162\u003c\/p\u003e \u003cp\u003e3.7. Atmospheric Towers 167\u003c\/p\u003e \u003cp\u003e3.8. Vacuum Towers 169\u003c\/p\u003e \u003cp\u003e3.9. Floating Pressure\/Pressure Minimization 173\u003c\/p\u003e \u003cp\u003eReference 179\u003c\/p\u003e \u003cp\u003e\u003cb\u003e4 Reboilers and Feed Preheaters 180\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e4.1. Types of Reboilers 181\u003c\/p\u003e \u003cp\u003e4.2. Steam-Heated Reboilers 185\u003c\/p\u003e \u003cp\u003e4.3. Hot Oil 195\u003c\/p\u003e \u003cp\u003e4.4. Fired Heaters 198\u003c\/p\u003e \u003cp\u003e4.5. Feed Preheater 200\u003c\/p\u003e \u003cp\u003e4.6. Economizer 204\u003c\/p\u003e \u003cp\u003eReferences 208\u003c\/p\u003e \u003cp\u003e\u003cb\u003e5 Applying Feedforward 209\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e5.1. Feed Flow and Composition 210\u003c\/p\u003e \u003cp\u003e5.2. Internal Reflux Control 220\u003c\/p\u003e \u003cp\u003e5.3. Extreme Feedforward 226\u003c\/p\u003e \u003cp\u003e5.4. Feedforward for Bottoms Level 229\u003c\/p\u003e \u003cp\u003e5.5. Feedforward for Column Pressure 234\u003c\/p\u003e \u003cp\u003e5.6. Product Compositions 238\u003c\/p\u003e \u003cp\u003eReference 242\u003c\/p\u003e \u003cp\u003e\u003cb\u003e6 Unit Optimization 243\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e6.1. Energy and Separation 244\u003c\/p\u003e \u003cp\u003e6.2. Optimization of a Column 250\u003c\/p\u003e \u003cp\u003e6.3. Constraints in Distillation Columns 255\u003c\/p\u003e \u003cp\u003e6.4. Control Configurations for Single Constraint 258\u003c\/p\u003e \u003cp\u003e6.5. Control Configurations for Multiple Constraints 266\u003c\/p\u003e \u003cp\u003eReferences 272\u003c\/p\u003e \u003cp\u003e\u003cb\u003e7 Double-End Composition Control 273\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e7.1. Defining the Problem 273\u003c\/p\u003e \u003cp\u003e7.2. Options for Composition Control 275\u003c\/p\u003e \u003cp\u003e7.3. Relative Gain 283\u003c\/p\u003e \u003cp\u003e7.4. Relative Gains from Open Loop Sensitivities 290\u003c\/p\u003e \u003cp\u003e7.5. Relative Gains for Other Configurations 294\u003c\/p\u003e \u003cp\u003e7.6. Ratios for Manipulated Variables 296\u003c\/p\u003e \u003cp\u003e7.7. Effect of Operating Objectives 300\u003c\/p\u003e \u003cp\u003e7.8. MPC 303\u003c\/p\u003e \u003cp\u003e\u003cb\u003e8 Complex Towers 306\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e8.1. Heat Integration 307\u003c\/p\u003e \u003cp\u003e8.2. Side Heater\/Side Cooler 311\u003c\/p\u003e \u003cp\u003e8.3. Sidestreams 316\u003c\/p\u003e \u003cp\u003e8.4. Withdrawing a Liquid Sidestream 319\u003c\/p\u003e \u003cp\u003e8.5. Withdrawing a Vapor Sidestream 322\u003c\/p\u003e \u003cp\u003e8.6. Composition Control in Sidestream Towers 324\u003c\/p\u003e \u003cp\u003eIndex 329\u003c\/p\u003e","brand":"Wiley","offers":[{"title":"Default Title","offer_id":52090689061207,"sku":"9780470381946","price":77.36,"currency_code":"GBP","in_stock":true}],"thumbnail_url":"\/\/cdn.shopify.com\/s\/files\/1\/0817\/1739\/5799\/files\/9780470381946.jpg?v=1762273095","url":"https:\/\/bookcurl.com\/products\/distillation-control-9780470381946","provider":"Book Curl","version":"1.0","type":"link"}