Solvents used in industrial examples are not recommendations for beverage production or bottle blending.
Chapter-level engineering discussion by Mirko Skiborowski, Andreas Harwardt, and Wolfgang Marquardt; paraphrase of printed pp. 311–335.
Nonideal separation feasibility depends on composition paths, boundaries, phase behavior and operating conditions. Shortcut tests and rigorous models have different assumptions; finite-reflux feasibility can differ from total-reflux predictions.
335
311
Chapter 8: Conceptual Design of Azeotropic Distillation Processes. Printed pages; chapter begins at original PDF 321.
Paraphrase checked against the supplied PDF text. Verification establishes source fidelity, not independent validation of every author claim or numerical equation.
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Evidence
Nonideal separation feasibility depends on composition paths, boundaries, phase behavior and operating conditions. Shortcut tests and rigorous models have different assumptions; finite-reflux feasibility can differ from total-reflux predictions.
Location and context
Mirko Skiborowski, Andreas Harwardt, and Wolfgang Marquardt. Conceptual Design of Azeotropic Distillation Processes, printed pp. 311–335. Chapter original PDF pages 321–371. This is an original paraphrase, not a quotation.
Annotation
Solvents used in industrial examples are not recommendations for beverage production or bottle blending.
Verification
Source text checked; locator and source relation present. Source fidelity is verified, not every underlying claim independently established.
