注冊(cè) | 登錄讀書(shū)好,好讀書(shū),讀好書(shū)!
讀書(shū)網(wǎng)-DuShu.com
當(dāng)前位置: 首頁(yè)出版圖書(shū)科學(xué)技術(shù)工業(yè)技術(shù)化學(xué)工業(yè)液相連續(xù)多相反應(yīng)器的數(shù)值模擬

液相連續(xù)多相反應(yīng)器的數(shù)值模擬

液相連續(xù)多相反應(yīng)器的數(shù)值模擬

定 價(jià):¥280.00

作 者: 楊超(Chao Yang),毛在砂(Zai-Sha Mao) 著
出版社: 化學(xué)工業(yè)出版社
叢編項(xiàng):
標(biāo) 簽: 工業(yè)技術(shù) 機(jī)械/儀表工業(yè) 專(zhuān)用機(jī)械與設(shè)備

ISBN: 9787122198525 出版時(shí)間: 2015-03-01 包裝: 精裝
開(kāi)本: 16開(kāi) 頁(yè)數(shù): 309 字?jǐn)?shù):  

內(nèi)容簡(jiǎn)介

《液相連續(xù)多相反應(yīng)器的數(shù)值模擬》系統(tǒng)介紹了液相反應(yīng)器和反應(yīng)結(jié)晶器內(nèi)多相混合、流動(dòng)、傳質(zhì)和反應(yīng)過(guò)程的數(shù)學(xué)模型、數(shù)值方法及實(shí)驗(yàn)技術(shù)等基礎(chǔ)研究和工程應(yīng)用的內(nèi)容,涵蓋了反應(yīng)器和顆粒尺度(固體顆粒、氣泡和液滴)上的氣—液、液—固、液—液、氣—液—固、液—液—固和氣—液—液等多相特性?!兑合噙B續(xù)多相反應(yīng)器的數(shù)值模擬》除了介紹作者及合作者在這些領(lǐng)域的研究新成果外,也廣泛搜集國(guó)內(nèi)外的前沿研究成果,向讀者做全景式的介紹。
  《液相連續(xù)多相反應(yīng)器的數(shù)值模擬》將為多相流反應(yīng)器和結(jié)晶29(例如攪拌槽、環(huán)流反應(yīng)器和微反應(yīng)9S)的設(shè)計(jì)、優(yōu)化和放大提供基礎(chǔ)理論和數(shù)值方法,作為在化學(xué)反應(yīng)工程、傳質(zhì)與傳熱、流體力學(xué)、結(jié)晶學(xué)等領(lǐng)域內(nèi)的科學(xué)家和工程師的一本參考書(shū),特別適合于需要掌握先進(jìn)的計(jì)算流體力學(xué)和計(jì)箅反應(yīng)工程學(xué)工具、用數(shù)學(xué)模型和數(shù)值模擬方法來(lái)研究攪拌槽、環(huán)流反應(yīng)器和微反應(yīng)器的讀者,也可供廣大化工和冶金工程師以及高等學(xué)校相關(guān)專(zhuān)業(yè)師生參考。

作者簡(jiǎn)介

楊超,男,1971年生,研究員、博士生導(dǎo)師,中國(guó)科學(xué)院綠色過(guò)程與工程重點(diǎn)實(shí)驗(yàn)室常務(wù)副主任。1998年南京工業(yè)大學(xué)獲博士學(xué)位,1998-2000年中科院化工冶金研究所博士后,2005-2006年美國(guó)康奈爾大學(xué)高訪。2010年獲國(guó)家杰出青年科學(xué)基金。
  2012年獲日本化學(xué)工學(xué)會(huì)亞洲研究獎(jiǎng)(SCEJ Asia Research Award)、第四屆“侯德榜化工科學(xué)技術(shù)獎(jiǎng)─創(chuàng)新獎(jiǎng)”,2011年獲第十二屆“中國(guó)青年科技獎(jiǎng)”、中國(guó)科學(xué)院青年科學(xué)家獎(jiǎng),2010年獲第十三屆“茅以升科學(xué)技術(shù)獎(jiǎng)─北京青年科技獎(jiǎng)”、中國(guó)石油和化學(xué)工業(yè)聯(lián)合會(huì)青年科技突出貢獻(xiàn)獎(jiǎng),2009年獲國(guó)家自然科學(xué)二等獎(jiǎng)、中國(guó)石油和化學(xué)工業(yè)協(xié)會(huì)技術(shù)發(fā)明一等獎(jiǎng),還獲得省部級(jí)科技進(jìn)步一等獎(jiǎng)、二等獎(jiǎng)和三等獎(jiǎng)各1項(xiàng)。發(fā)表期刊論文110多篇、會(huì)議報(bào)告120多篇,申請(qǐng)發(fā)明專(zhuān)利25件,獲軟件著作權(quán)3項(xiàng),撰寫(xiě)中英文專(zhuān)著7章。
  主要從事化學(xué)反應(yīng)工程和多相傳遞研究,利用數(shù)學(xué)模型和數(shù)值模擬方法,進(jìn)行多相反應(yīng)器和結(jié)晶器的優(yōu)化設(shè)計(jì)和工程放大。主持完成國(guó)家重點(diǎn)基金項(xiàng)目、973課題各1項(xiàng),現(xiàn)負(fù)責(zé)1項(xiàng)國(guó)家重大基金課題、1項(xiàng)973課題。

圖書(shū)目錄

Preface ix
CHAPTER 1 Introduction
CHAPTER 2 Fluid fow and mass transfer on particle scale
2.1 Introduction
2.2 Theoretical basis
2.2.1 Fluid mechanics
2.2.2 Mass transfer
2.2.3 Interfacial force balance
2.2.4 Interfacial mass transport
2.3 Numerical methods
2.3.1 Orthogonal boundary-ftted coordinate system
2.3.2 Level set method
2.3.3 Mirror fuid method
2.4 Buoyancy-driven motion and mass transfer of a single particle
2.4.1 Drop, bubble and solid particle motion
2.4.2 Mass transfer to/from a drop
2.5 Mass transfer-induced Marangoni effect
2.5.1 Solute-induced Marangoni effect
2.5.2 Effect of surfactant on drop motion and mass transfer
2.5.3 Surfactant-induced Marangoni effect
2.6 Behavior of particle swarms
2.6.1 Introduction
2.6.2 Forces on single particles
2.6.3 Cell model
2.7 Single particles in shear fow and extensional fow
2.7.1 Mass/heat transfer from a spherical particle in extensional fow
2.7.2 Flow and transport from a sphere in simple shear fow
2.8 Summary and perspective
2.8.1 Summary
2.8.2 Perspective
Nomenclature
References

CHAPTER 3 Multiphase stirred reactors
3.1 Introduction
3.2 Mathematical models and numerical methods
3.2.1 Governing equations
3.2.2 Interphase momentum exchange
3.2.3 RANS method
3.2.4 LES model
3.2.5 Impeller treatment
3.2.6 Numerical details
3.3 Two-phase fow in stirred tanks
3.3.1 Solid?Cliquid systems
3.3.2 Gas?Cliquid systems
3.3.3 Liquid?Cliquid systems
3.4 Three-phase fow in stirred tanks
3.4.1 Liquid?Cliquid?Csolid systems
3.4.2 Gas?Cliquid?Cliquid systems
3.4.3 Liquid?Cliquid?Cliquid systems
3.4.4 Gas?Cliquid?Csolid systems
3.5 Summary and perspective
3.5.1 Summary
3.5.2 Perspective
Nomenclature
References

CHAPTER 4 Airlift loop reactors
4.1 Introduction
4.2 Flow regime identifcation
4.3 Mathematical models and numerical methods
4.3.1 Eulerian?CEulerian two-fuid model
4.3.2 Closure of interfacial forces
4.3.3 Closure of turbulence models
4.3.4 Numerical methods
4.4 Hydrodynamics and transport in airlift loop reactors
4.4.1 Hydrodynamic behavior
4.4.2 Interphase transport phenomena
4.5 Macromixing and micromixing
4.5.1 Macromixing in airlift loop reactors
4.5.2 Micromixing in airlift loop reactors
4.6 Guidelines for design and scale-up of airlift loop reactors
4.7 Summary and perspective
Nomenclature
References

CHAPTER 5 Preliminary investigation of two-phase microreactors
5.1 Introduction
5.2 Mathematical models and numerical methods
5.3 Simulation using lattice Boltzmann method
5.3.1 Numerical simulation of two-phase fow in microchannels
5.3.2 Numerical study of heat transfer in microchannels
5.3.3 Numerical simulation of mass transfer in microchannels
5.4 Experimental
5.4.1 Flow pattern
5.4.2 Pressure drop
5.4.3 Mass transfer performance
5.4.4 Micromixing
5.5 Summary and perspective
Nomenclature
References

CHAPTER 6 Crystallizers: CFD?CPBE modeling
6.1 Introduction
6.2 Mathematical models and numerical methods
6.2.1 General population balance equation
6.2.2 Standard method of moments
6.2.3 Quadrature method of moments
6.2.4 Multi-class method or discretized method
6.3 Crystallizer modeling procedures
6.3.1 Species transport equations
6.3.2 Nucleation and growth kinetics
6.3.3 Aggregation and breakage kernels
6.3.4 Computational details
6.3.5 Simulated results of precipitation processes
6.4 Macromixing and micromixing
6.5 Summary and perspective
Nomenclature
References
Index

本目錄推薦

掃描二維碼
Copyright ? 讀書(shū)網(wǎng) leeflamesbasketballcamps.com 2005-2020, All Rights Reserved.
鄂ICP備15019699號(hào) 鄂公網(wǎng)安備 42010302001612號(hào)