Chemical Engineering Design, Fourth Edition: Chemical Engineering Volume 6 (Coulson & Richardson's C

Chemical Engineering Design, Fourth Edition: Chemical Engineering Volume 6 (Coulson & Richardson's C pdf epub mobi txt 电子书 下载 2026

☆☆☆☆☆
出版者:A Butterworth-Heinemann Title (2005年7月8日)
作者:R K Sinnott
出品人:
页数:1056 页
译者:
出版时间:2005年07月
价格:483.0
装帧:平装
isbn号码:9780750665384
丛书系列:
图书标签:
  • 化学工程
  • 设计
  • 化工原理
  • 传热
  • 流体
  • 分离
  • 反应工程
  • 过程控制
  • 工程计算
  • Coulson & Richardson
想要找书就要到 本本书屋
立刻按 ctrl+D收藏本页
你会得到大惊喜!!

具体描述

"An essential support text for the traditional design product...Well written using a clear type, is easy to read and is superbly indexed." Trans IChemE

"An excellent book for professionals and university students .. you can find everything you need about mass and heat transfer." Mehmet Aras, Bayer

"Bottom line: For a holistic view of chemical engineering design, this book provides as much, if not more, than any other book available on the topic. Nearly every subject is accompanied by examples and new technologies are also addressed. In short, a complete, well-written and illustrated resource that is a pleasure to use." www.cheresources.com (Chemical Engineering Resources)

Chemical Engineering Design, Fourth Edition: Chemical Engineering Volume 6 (Coulson & Richardson's Chemical Engineering) A Comprehensive and Indispensable Guide for Modern Chemical Engineers This volume stands as a cornerstone in the comprehensive series, Coulson & Richardson's Chemical Engineering, dedicated to providing engineers with the foundational knowledge and advanced methodologies required for the successful design and execution of chemical processes. Moving beyond the fundamental principles covered in earlier volumes, this edition zeroes in on the critical aspects of process synthesis, equipment selection, economic evaluation, and the rigorous safety and environmental considerations intrinsic to contemporary chemical engineering practice. The core philosophy underpinning this text is the integration of theoretical understanding with practical, industrial-scale application. It serves not merely as a reference text but as a working manual, guiding the reader through the complex journey from a laboratory-scale reaction to a full-scale, economically viable production plant. The structure is meticulously designed to mirror the real-world design workflow, ensuring that every concept builds logically upon the preceding one. Part I: The Conceptualization and Feasibility of Process Design The initial sections establish the framework for effective design thinking. Chemical process design is inherently an iterative and multi-objective optimization problem. This volume addresses this challenge head-on by first detailing the crucial preliminary steps that dictate the success or failure of any large-scale endeavor. Process Flowsheet Development: A significant emphasis is placed on interpreting and generating Process Flow Diagrams (PFDs) and Piping and Instrumentation Diagrams (P&IDs). Readers will learn the standardized symbology and the critical information conveyed by these documents—information that forms the blueprint for all subsequent engineering disciplines. The shift from simple block flow diagrams to detailed PFDs is explored, highlighting the importance of mass and energy balances in defining the scope of unit operations. Thermodynamics and Process Simulation: While fundamental thermodynamics is assumed knowledge, this part focuses on the application of advanced thermodynamic models (such as UNIFAC, NRTL, and advanced equations of state) essential for accurate vapor-liquid equilibrium (VLE) and liquid-liquid equilibrium (LLE) calculations encountered in separation processes. Furthermore, the utilization of modern process simulators (like Aspen Plus or HYSYS, though the book maintains generality) is integrated into the discussion, showing how software tools are leveraged to rapidly test various process configurations and thermodynamic packages, thereby accelerating the initial design phase. Economic Assessment and Feasibility Studies: No design is complete without a thorough economic justification. This section provides a robust grounding in capital cost estimation (using methods like the Lang factor and detailed component costing), operating cost analysis, and the calculation of key financial metrics such as Net Present Value (NPV), Internal Rate of Return (IRR), and payback period. The concept of the "design envelope"—the range of operating conditions that remain economically attractive—is thoroughly explored. Sensitivity analysis, which assesses how fluctuations in raw material prices or utility costs impact profitability, is treated as a mandatory step in the feasibility review. Part II: Unit Operations and Equipment Specification The heart of the volume delves into the specific engineering challenges associated with sizing and selecting the major equipment pieces found in nearly every chemical plant. Unlike introductory texts that treat unit operations in isolation, this volume emphasizes their integration and the iterative feedback loops that exist between them. Reactor Engineering in the Design Context: Design choices for reactors (batch, CSTR, plug flow) are directly tied to kinetics and heat management. This section moves beyond simple conversion calculations to address issues of non-ideality in large reactors, including heat transfer limitations, mixing effects in polymerization or slurry reactors, and the implications of reaction kinetics on product selectivity and separation train requirements. Catalyst deactivation models critical for long-term operational planning are also examined. Separation Processes Optimization: Separation costs often dominate the total operating expenses of a chemical facility. A deep dive is provided into the design of distillation columns, where the complexity of trays, packing internals, and reflux ratio optimization is explored using modern shortcut methods and rigorous stage-by-stage simulation techniques. For complex systems, a detailed analysis of extractive and azeotropic distillation is included. Furthermore, the selection criteria for membrane separation technologies (e.g., reverse osmosis, gas permeation) versus conventional methods like crystallization or adsorption are presented within the context of process integration and energy penalty trade-offs. Heat Transfer and Utility Systems: Effective thermal management is crucial for both safety and energy efficiency. The design procedures for shell-and-tube heat exchangers are covered exhaustively, including the application of the Overall Heat Transfer Coefficient ($U$) adjustment based on fouling factors specific to the process streams. The design and layout of utility systems—cooling water networks, steam generation, and compressed air—are treated as interconnected subsystems, focusing on minimizing utility consumption through process-to-process heat recovery networks (Pinch Analysis). Part III: Process Control, Safety, and Environmental Compliance Modern chemical design places equal weight on operational stability, inherent safety, and adherence to environmental regulations. This part addresses the crucial aspects that transform a theoretically sound process into a reliable, sustainable industrial asset. Process Control System Design: Control is not an afterthought but an integral part of design. This section outlines the steps for defining control structures, including the selection of primary and secondary control loops. Emphasis is placed on dynamic simulation to test the robustness of control schemes against disturbances. Topics include the specification of control valves, sensors, and transmitters, ensuring that the selected equipment can adequately execute the required control strategy (e.g., managing tight temperature profiles in highly exothermic reactions). Inherent Safety and Risk Assessment: The philosophy of inherent safety—designing out hazards rather than adding protective layers—is rigorously promoted. Techniques such as HAZOP (Hazard and Operability Studies) and FMEA (Failure Mode and Effects Analysis) are detailed, providing step-by-step methodologies for systematically identifying potential deviations and their consequences. The principles of designing for containment, reaction runaway mitigation (including quench and relief systems sizing), and the proper selection of materials of construction to prevent catastrophic failure are covered in depth. Environmental Engineering Integration: Compliance with discharge regulations necessitates proactive design. This involves the specification of necessary effluent treatment units (air scrubbers, wastewater treatment stages) early in the design process, rather than tacking them on at the end. Readers are introduced to concepts of atom economy, waste minimization strategies, and the integration of solvent recovery systems to reduce volatile organic compound (VOC) emissions, directly impacting both operational expenditure and regulatory adherence. Conclusion This volume serves as the definitive bridge between undergraduate chemical engineering knowledge and professional design practice. It mandates a holistic, systems-level approach, ensuring that the student or practicing engineer can synthesize all necessary components—from kinetics and thermodynamics to economics and safety regulations—into a cohesive, optimized, and responsible chemical plant design. The rigor embedded within its pages prepares the next generation of engineers to tackle the increasing complexity and scrutiny of modern chemical process development.

作者简介

目录信息

读后感

评分☆☆☆☆☆

评分☆☆☆☆☆

评分☆☆☆☆☆

评分☆☆☆☆☆

评分☆☆☆☆☆

用户评价

评分☆☆☆☆☆

从装帧和排版的角度来看,这本书的风格非常传统,基本上延续了早期学术专著的风格,字体偏小,图表密度非常高,而且很多关键公式的推导步骤省略得比较快。这使得在没有充足光线或需要频繁在不同章节之间跳转查阅时,阅读体验并不算轻松。不过,这也可以理解,毕竟它聚焦于内容的密度而非表面的吸引力。我特别欣赏它对规范引用和历史背景的交代,很多地方你会看到对早期化工先驱工作的致敬,以及不同设计标准(比如欧标和美标)在特定情况下的差异分析。这种对“历史演进”的尊重,让你明白今天的工程实践并非空中楼阁,而是建立在无数次实验和失败之上的经验总结。虽然初读时会被密集的公式和文字淹没,但随着实践经验的积累,你会发现这些看似晦涩的推导,其实是应对那些“非标准问题”的强大工具箱。这本书更像是你在职业生涯中,每当遇到一个瓶颈或新的设计挑战时,都会忍不住翻开的工具书,而非一气呵成的读物。

评分☆☆☆☆☆

这本厚重的《化工原理设计》(Chemical Engineering Design)第四版,作为Coulson & Richardson这个经典系列的第六卷,实在是让初涉化工设计领域的学生们又爱又恨的“圣经”。我拿到这本书时,首先被它那沉甸甸的质感和几乎要将书架压塌的分量所震撼。它不是那种能轻松翻阅、快速获取速成知识的小册子,更像是一部详尽的工程手册,需要你沉下心来,一步一个脚印地去啃。 最让我印象深刻的是它对基本单元操作的深入剖析。很多参考书在介绍诸如精馏、吸收塔这类核心设备时,往往只是给出几个公式和流程图就草草带过,但这本书不同,它会花大量的篇幅去解释背后的热力学和传递现象原理,并且会结合实际工业案例,展示设计参数是如何一步步确定的。比如,在处理塔盘设计时,它不仅会给出理论上的最小塔板数计算,还会深入探讨实际操作中流体力学的影响,如何平衡压降与分离效率之间的矛盾。这种详尽的、追本溯源的讲解方式,虽然阅读起来比较费力,但一旦理解了,对于建立稳固的设计思维体系是极其宝贵的。它教会你思考的不是“怎么做”,而是“为什么这么做”。我个人感觉,这本书更像是为那些有志于成为真正化工设计师的人准备的,它要求读者具备一定的数学和物理基础,否则光是那些复杂的微分方程和迭代计算就足以让人望而却步了。 读完其中的章节,你会有一种自己真的掌握了设计某类单元的信心,而不是仅仅停留在公式套用的层面。

评分☆☆☆☆☆

这本书的价值,我认为很大一部分体现在它对“工程实践”与“理论模型”之间鸿沟的弥合上。它没有沉溺于完美的数学模型,而是非常务实地指出了实际操作中必须面对的妥协和约束。例如,在泵选型这一章中,作者不仅仅是讲解了扬程和流量的匹配,更是花了显著篇幅讨论了材料选择、腐蚀防护、密封技术以及设备维护周期对初始设计决策的影响。这些“软知识”恰恰是课堂教学中常常被忽略的,却是决定一个设计能否在真实环境中长期稳定运行的关键。当我阅读到关于设备布局和工厂公用工程系统整合的部分时,我意识到这本书的视野已经超越了单个单元操作的范畴,开始进入到整个工厂层面的系统集成。它强迫你思考,你设计的那个精馏塔,它的蒸汽是哪里来的?冷凝水如何回收?这些看似琐碎的辅助系统,在经济性和可靠性评估中占据了多大的比重?这提供了一种非常整体性的、系统性的工程思维,远超出了我之前接触的任何一本教材所能提供的广度。

评分☆☆☆☆☆

如果要用一个词来形容阅读这本书的感受,那或许是“敬畏”。它不是一本让你轻松掌握技能的指南,而是一扇通往深度理解化工设计复杂性的门。我记得我在学习换热器设计时,对于不同清洗周期和污垢因子的影响分析,书里给出了一个非常精细的经济性模型,权衡了初始投资和长期运行维护成本。这个模型展示了设计决策如何直接影响到企业的长期利润。它不再是抽象的“A+B=C”的计算,而是真实的商业决策过程。它让我开始用“成本效益”的视角来审视每一个工程选择,认识到“完美设计”在经济上往往是不成立的,最优解总是在技术可行性、安全性与经济性之间寻求一个动态的平衡点。这本书的每一个章节似乎都在提醒你,化工设计是一个高度集成、充满权衡取舍的艺术与科学的结合体,它要求的不只是精确的计算,更是对现实世界约束条件的深刻洞察。阅读它,如同接受了一次高强度的、全方位的思维训练,让人对未来面对的工程挑战多了一份踏实的信心。

评分☆☆☆☆☆

说实话,如果仅仅是想应付一次期末考试,或者快速了解一个新工艺的大致流程,这本书可能显得有些“过重”了。它的叙事风格非常严谨、学术化,几乎没有太多花哨的排版或者轻松的阅读引导。每一次知识点的跳转都显得非常逻辑化,需要读者自己去构建知识之间的联系。我记得有一次我查阅关于反应器热管理的部分,本来是想找一个现成的计算模板,结果却发现作者花了整整三章的篇幅来讨论不同类型反应器(如CSTR和PFR)的热稳定性、失控风险评估以及安全联锁系统的设计原则。这部分内容无疑是极其重要的,直接关系到工厂的生命线,但对于初学者来说,这种深度解析可能导致学习曲线过于陡峭。它更像是为资深工程师在进行复杂、高风险项目设计时提供的“终极参考”。我常常需要对照着其他更基础的教材来看这本书,用基础教材建立框架,再用这本“大部头”来填充细节和应对那些“没人告诉你答案”的复杂边界条件。它不会直接给你一个“最优解”,而是提供一套严谨的“求解方法论”。

评分☆☆☆☆☆

评分☆☆☆☆☆

评分☆☆☆☆☆

评分☆☆☆☆☆

评分☆☆☆☆☆

本站所有内容均为互联网搜索引擎提供的公开搜索信息,本站不存储任何数据与内容,任何内容与数据均与本站无关,如有需要请联系相关搜索引擎包括但不限于百度,google,bing,sogou 等

© 2026 onlinetoolsland.com All Rights Reserved. 本本书屋 版权所有