1 (p1): SECTION ONE Equipment Design2 (p1-1): 1:Fluid Flow3 (p1-1-1): Velocity head4 (p1-1-2): Piping pressure drop4 (p1-1-3): Equivalent length5 (p1-1-4): Recommended velocities7 (p1-1-5): Two-phase flow9 (p1-1-6): Compressible flow12 (p1-1-7): Sonic velocity12 (p1-1-8): Metering13 (p1-1-9): Control valves16 (p1-1-10): Safety relief valves19 (p1-2): 2:Heat Exchangers20 (p1-2-1): TEMA24 (p1-2-2): Selection guides27 (p1-2-3): Pressure drop shell and tube29 (p1-2-4): Temperature difference30 (p1-2-5): Shell diameter30 (p1-2-6): Shellside velocity maximum31 (p1-2-7): Nozzle velocity maximum31 (p1-2-8): Heat transfer coefficients38 (p1-2-9): Fouling resistances40 (p1-2-10): Metal resistances42 (p1-2-11): Vacuum condensers42 (p1-2-12): Air-cooled heat exchangers:forced vs induced draft43 (p1-2-13): Air-cooled heat exchangers:pressure drop air side44 (p1-2-14): Air-cooled heat exchangers:rough rating46 (p1-2-15): Air-cooled heat exchangers:temperature control48 (p1-2-16): Miscellaneous rules of thumb49 (p1-3): 3:Fractionators50 (p1-3-1): Introduction50 (p1-3-2): Relative volatility51 (p1-3-3): Minimum reflux52 (p1-3-4): Minimum stages52 (p1-3-5): Actual reflux and actual theoretical stages53 (p1-3-6): Reflux to feed ratio54 (p1-3-7): Actual trays54 (p1-3-8): Graphical methods55 (p1-3-9): Tray efficiency59 (p1-3-10): Diameter of bubble cap trays60 (p1-3-11): Diameter of sieve/valve trays(F factor)61 (p1-3-12): Diameter of sieve/valve trays(Smith)63 (p1-3-13): Diameter of sieve/valve trays(Lieberman)63 (p1-3-14): Diameter of ballast trays65 (p1-3-15): Diameter of fractionators,general65 (p1-3-16): Control schemes69 (p1-3-17): Optimization techniques72 (p1-3-18): Reboilers76 (p1-3-19): Packed columns97 (p1-4): 4:Absorbers98 (p1-4-1): Introduction98 (p1-4-2): Hydrocarbon absorber design100 (p1-4-3): Hydrocarbon absorbers,optimization101 (p1-4-4): Inorganic type104 (p1-5): 5:Pumps105 (p1-5-1): Affinity laws105 (p1-5-2):...

zlibzh/no-category/Carl Branan著, ( )Carl Branan著, Anan Br/化学工程师用的经验法则 英文版_29479125.pdf

RULES OF THUMB FOR CHEMICAL ENGINEERS A MANUAL OF QUICK,ACCURATE SOLUTIONS TO EVERYDAY PROCESS ENGINEERING PROBLEMS THIRD EDITION

RULES OF THUMB FOR MECHANICAL ENGINEERS: A MANUAL OF QUICK, ACCURATE SOLUTIONS TO EVERYDAY PROCESS ENGINEERING PROBLEMS.

Rules of thumb for chemical engineers : a manual of quick, accurate solutions to everyday process engineering problems

Rules of Thumb for Chemical Engineers, Third Edition (Rules of Thumb for Chemical Engineers)

Carl Branan; Elsevier Science Publishers

Carl R. Branan, editor

GULF PROFESSIONAL PUBLISHING AN IMPRINT OF ELSEVIER SCIENCE

World Books Publishing Corporation

Butterworth-Heinemann Ltd

Architectural Press

Focal Press

3rd ed., Amsterdam, New York, Netherlands, 2002

United Kingdom and Ireland, United Kingdom

China, People's Republic, China

Reprinted ed, Beijing, 2005

Ying yin ban, Beijing, 2005

3, FR, 2002

Bookmarks: p1 (p1): SECTION ONE Equipment Design
p1-1 (p2): 1：Fluid Flow
p1-1-1 (p3): Velocity head
p1-1-2 (p4): Piping pressure drop
p1-1-3 (p4): Equivalent length
p1-1-4 (p5): Recommended velocities
p1-1-5 (p7): Two-phase flow
p1-1-6 (p9): Compressible flow
p1-1-7 (p12): Sonic velocity
p1-1-8 (p12): Metering
p1-1-9 (p13): Control valves
p1-1-10 (p16): Safety relief valves
p1-2 (p19): 2：Heat Exchangers
p1-2-1 (p20): TEMA
p1-2-2 (p24): Selection guides
p1-2-3 (p27): Pressure drop shell and tube
p1-2-4 (p29): Temperature difference
p1-2-5 (p30): Shell diameter
p1-2-6 (p30): Shellside velocity maximum
p1-2-7 (p31): Nozzle velocity maximum
p1-2-8 (p31): Heat transfer coefficients
p1-2-9 (p38): Fouling resistances
p1-2-10 (p40): Metal resistances
p1-2-11 (p42): Vacuum condensers
p1-2-12 (p42): Air-cooled heat exchangers:forced vs induced draft
p1-2-13 (p43): Air-cooled heat exchangers:pressure drop air side
p1-2-14 (p44): Air-cooled heat exchangers:rough rating
p1-2-15 (p46): Air-cooled heat exchangers:temperature control
p1-2-16 (p48): Miscellaneous rules of thumb
p1-3 (p49): 3：Fractionators
p1-3-1 (p50): Introduction
p1-3-2 (p50): Relative volatility
p1-3-3 (p51): Minimum reflux
p1-3-4 (p52): Minimum stages
p1-3-5 (p52): Actual reflux and actual theoretical stages
p1-3-6 (p53): Reflux to feed ratio
p1-3-7 (p54): Actual trays
p1-3-8 (p54): Graphical methods
p1-3-9 (p55): Tray efficiency
p1-3-10 (p59): Diameter of bubble cap trays
p1-3-11 (p60): Diameter of sieve/valve trays(F factor)
p1-3-12 (p61): Diameter of sieve/valve trays(Smith)
p1-3-13 (p63): Diameter of sieve/valve trays(Lieberman)
p1-3-14 (p63): Diameter of ballast trays
p1-3-15 (p65): Diameter of fractionators,general
p1-3-16 (p65): Control schemes
p1-3-17 (p69): Optimization techniques
p1-3-18 (p72): Reboilers
p1-3-19 (p76): Packed columns
p1-4 (p97): 4：Absorbers
p1-4-1 (p98): Introduction
p1-4-2 (p98): Hydrocarbon absorber design
p1-4-3 (p100): Hydrocarbon absorbers,optimization
p1-4-4 (p101): Inorganic type
p1-5 (p104): 5：Pumps
p1-5-1 (p105): Affinity laws
p1-5-2 (p105): Horsepower
p1-5-3 (p105): Efficiency
p1-5-4 (p105): Minimum flow
p1-5-5 (p106): General suction system
p1-5-6 (p107): Suction system NPSH available
p1-5-7 (p108): Suction system NPSH for studies
p1-5-8 (p109): Suction system NPSH with dissolved gas
p1-5-9 (p109): Larger impeller
p1-5-10 (p109): Construction materials
p1-6 (p112): 6：Compressors
p1-6-1 (p113): Ranges of application
p1-6-2 (p113): Generalized Z
p1-6-3 (p114): Generalized K
p1-6-4 (p115): Horsepower calculation
p1-6-5 (p119): Efficiency
p1-6-6 (p121): Temperature rise
p1-6-7 (p121): Surge controls
p1-7 (p122): 7：Drivers
p1-7-1 (p123): Motors:efficiency
p1-7-2 (p124): Motors:starter sizes
p1-7-3 (p124): Motors:service factor
p1-7-4 (p125): Motors:useful equations
p1-7-5 (p125): Motors:relative costs
p1-7-6 (p126): Motors:overloading
p1-7-7 (p126): Steam turbines:steam rate
p1-7-8 (p126): Steam turbines:efficiency
p1-7-9 (p127): Gas turbines:fuel rates
p1-7-10 (p129): Gas engines:fuel rates
p1-7-11 (p129): Gas expanders:available energy
p1-8 (p130): 8：Separators/Accumulators
p1-8-1 (p131): Liquid residence time
p1-8-2 (p132): Vapor residence time
p1-8-3 (p133): Vapor/liquid calculation method
p1-8-4 (p135): Liquid/liquid calculation method
p1-8-5 (p135): Pressure drop
p1-8-6 (p136): Vessel thickness
p1-8-7 (p136): Gas scrubbers
p1-8-8 (p136): Reflux drums
p1-8-9 (p137): General vessel design tips
p1-9 (p138): 9：Boilers
p1-9-1 (p139): Power plants
p1-9-2 (p139): Controls
p1-9-3 (p140): Thermal efficiency
p1-9-4 (p141): Stack gas enthalpy
p1-9-5 (p142): Stack gas quantity
p1-9-6 (p143): Steam drum stability
p1-9-7 (p144): Deaerator venting
p1-9-8 (p145): Water alkalinity
p1-9-9 (p145): Blowdown control
p1-9-10 (p145): Impurities in water
p1-9-11 (p147): Conductivity versus dissolved solids
p1-9-12 (p148): Silica in steam
p1-9-13 (p148): Caustic embrittlement
p1-9-14 (p150): Waste heat
p1-10 (p153): 10：Cooling Towers
p1-10-1 (p154): System balances
p1-10-2 (p154): Temperature data
p1-10-3 (p156): Performance
p1-10-4 (p158): Performance estimate:a cast history
p1-10-5 (p158): Transfer units
p2 (p161): SECTION TWO Process Design
p2-1 (p162): 11：Refrigeration
p2-1-1 (p163): Types of systems
p2-1-2 (p163): Estimating horsepower per ton
p2-1-3 (p164): Horsepower and condenser duty for specific refrigerants
p2-1-4 (p182): Refrigerant replacements
p2-1-5 (p183): Ethylene/propylene cascaded system
p2-1-6 (p183): Steam jet type utilities requirements
p2-1-7 (p186): Ammonia absorption type utilities requirements
p2-2 (p187): 12：Gas Treating
p2-2-1 (p188): Introduction
p2-2-2 (p188): Gas treating processes
p2-2-3 (p190): Reaction type gas treating
p2-2-4 (p191): Physical solvent gas treating
p2-2-5 (p191): Physical/chemical type
p2-2-6 (p192): Carbonate type
p2-2-7 (p192): Solution batch type
p2-2-8 (p193): Bed batch type
p2-3 (p194): 13：Vacuum Systems
p2-3-1 (p195): Vacuum jets
p2-3-2 (p196): Typical jet systems
p2-3-3 (p197): Steam supply
p2-3-4 (p198): Measuring air leakage
p2-3-5 (p198): Time to evacuate
p2-3-6 (p199): Design recommendations
p2-3-7 (p200): Eiector specification sheet
p2-4 (p202): 14：Pneumatic Conveying
p2-4-1 (p203): Tvpes of systems
p2-4-2 (p204): Differential pressures
p2-4-3 (p204): Equipment sizing
p2-5 (p206): 15：Blending
p2-5-1 (p207): Single-stage mixers
p2-5-2 (p207): Multistage mixers
p2-5-3 (p208): Gas/liquid contacting
p2-5-4 (p208): Liquid/liquid mixing
p2-5-5 (p208): Liquid/solid mixing
p2-5-6 (p209): Mixer applications
p2-5-7 (p210): Shrouded blending nozzle
p2-5-8 (p210): Vapor formation rate for tank filling
p3 (p211): SECTION THREE Plant Design
p3-1 (p212): 16：Process Evaluation
p3-1-1 (p213): Introduction
p3-1-2 (p213): Study definition
p3-1-3 (p215): Process definition
p3-1-4 (p222): Battery limits specifications
p3-1-5 (p226): Offsite specifications
p3-1-6 (p230): Capital investments
p3-1-7 (p237): Operating costs
p3-1-8 (p240): Economics
p3-1-9 (p244): Financing
p3-2 (p247): 17：Reliability
p3-3 (p249): 18：Metallurgy
p3-3-1 (p250): Embrittlement
p3-3-2 (p256): Stress-corrosion cracking
p3-3-3 (p257): Hydrogen attack
p3-3-4 (p259): Pitting corrosion
p3-3-5 (p260): Creep and creep-rupture life
p3-3-6 (p262): Metal dusting
p3-3-7 (p264): Naphthenic acid corrosion
p3-3-8 (p265): Fuel ash corrosion
p3-3-9 (p267): Thermal fatigue
p3-3-10 (p269): Abrasive wear
p3-3-11 (p270): Pipeline toughness
p3-3-12 (p271): Common corrosion mistakes
p3-4 (p272): 19：Safety
p3-4-1 (p273): Estimating LEL and flash
p3-4-2 (p273): Tank blanketing
p3-4-3 (p275): Equipment purging
p3-4-4 (p276): Static charge from fluid flow
p3-4-5 (p279): Mixture flammability
p3-4-6 (p282): Relief manifolds
p3-4-7 (p288): Natural ventilation
p3-5 (p289): 20：Controls
p3-5-1 (p290): Introduction
p3-5-2 (p290): Extra capacity for process control
p3-5-3 (p291): Controller limitations
p3-5-4 (p292): False economy
p3-5-5 (p292): Definitions of control modes
p3-5-6 (p292): Control mode comparisons
p3-5-7 (p292): Control mode vs application
p3-5-8 (p293): Pneumatic vs electronic controls
p3-5-9 (p294): Process chromatographs
p4 (p295): SECTION FOUR Operations
p4-1 (p296): 21：Troubleshooting
p4-1-1 (p297): Introduction
p4-1-2 (p297): Fractionation:initial checklists
p4-1-3 (p299): Fractionation:Troubleshooting checklist
p4-1-4 (p301): Fractionation:operating problems
p4-1-5 (p307): Fractionation:mechanical problems
p4-1-6 (p311): Fractionation:Getting ready for troubleshooting
p4-1-7 (p312): Fractionation:"Normal"parameters
p4-1-8 (p313): Fluid flow
p4-1-9 (p316): Refrigeration
p4-1-10 (p317): Firetube heaters
p4-1-11 (p318): Safety relief valves
p4-1-12 (p319): Gas treating
p4-1-13 (p323): Compressors
p4-1-14 (p325): Measurement
p4-2 (p326): 22：Startup
p4-2-1 (p327): Introduction
p4-2-2 (p327): Settings for controls
p4-2-3 (p328): Probable causes of trouble in controls
p4-2-4 (p330): Checklists
p4-3 (p334): 23：Energy Conservation
p4-3-1 (p335): Target excess oxygen
p4-3-2 (p336): Stack heat loss
p4-3-3 (p336): Stack gas dew point
p4-3-4 (p338): Equivalent fuel values
p4-3-5 (p339): Heat recovery systems
p4-3-6 (p340): Process efficiency
p4-3-7 (p341): Steam traps
p4-3-8 (p343): Gas expanders
p4-3-9 (p344): Fractionation
p4-3-10 (p344): Insulating materials
p4-4 (p345): 24：Process Modeling Using Linear Programming
p4-4-1 (p346): Process modeling using linear programming
p4-5 (p351): 25：Properties
p4-5-1 (p352): Introduction
p4-5-2 (p352): Approximate physical properties
p4-5-3 (p353): Viscosity
p4-5-4 (p357): Relative humidity
p4-5-5 (p358): Surface tension
p4-5-6 (p358): Gas diffusion coefficients
p4-5-7 (p360): Water and hydrocarbons
p4-5-8 (p364): Natural gas hydrate temperature
p4-5-9 (p366): Inorganic gases in petroleum
p4-5-10 (p368): Foam density
p4-5-11 (p369): Equivalent diameter
p4-5-12 (p371): Autoignition temperature
p4-5-13 (p376): Gibbs free energy of formation
p4-5-14 (p386): New refrigerants
p4-6 (p387): 26：Approximate Conversion Factors
p4-6-1 (p388): Approximate conversion factors
p5 (p389): Appendixes
p5-1 (p390): Appendix 1：Shortcut Equipment Design Methods—Overview
p5-2 (p392): Appendix 2：Geographic Information Systems
p5-3 (p394): Appendix 3：Internet Ideas
p5-4 (p397): Appendix 4：Process Safety Management
p5-5 (p399): Appendix 5：Do-It-Yourself Shortcut Methods
p5-6 (p406): Appendix 6：Overview for Engineering Students
p5-7 (p409): Appendix 7：Modern Management Initiatives
p5-8 (p410): Appendix 8：Process Specification Sheets
p5-8-1 (p411): Vessel data sheet
p5-8-2 (p412): Shell and tube exchanger data sheet
p5-8-3 (p413): Double pipe (G-fin)exchanger data sheet
p5-8-4 (p414): Air-cooled(fin-fan)exchanger data sheet
p5-8-5 (p415): Direct fired heater data sheet
p5-8-6 (p416): Centrifugal pump(horizontal or vertical) data sheet
p5-8-7 (p417): Pump(vertical turbine—can or propellor) data sheet
p5-8-8 (p418): Tank data sheet
p5-8-9 (p419): Cooling tower data sheet
p6 (p423): Index

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Includes bibliographical references and index.

The most complete guide of its kind, this is the standard handbook for chemical and process engineers. All new material on fluid flow, long pipe, fractionators, separators and accumulators, cooling towers, gas treating, blending, troubleshooting field cases, gas solubility, and density of irregular solids. This substantial addition of material will also include conversion tables and a new appendix, "Shortcut Equipment Design Methods."
This convenient volume helps solve field engineering problems with its hundreds of common sense techniques, shortcuts, and calculations. Here, in a compact, easy-to-use format, are practical tips, handy formulas, correlations, curves, charts, tables, and shortcut methods that will save engineers valuable time and effort. Hundreds of common sense techniques and calculations help users quickly and accurately solve day-to-day design, operations, and equipment problems.
* The standard handbook for chemical and process engineers
* All new material on fluid flow, long pipe, fractionators, separators and accumulators, cooling towers, gas treating, blending, troubleshooting field cases, gas solubility, and density of irregular solids
* Hundreds of common sense techniques, shortcuts, and calculations

With hundreds of common sense techniques, shortcuts and calculations, this text helps solve field-engineering problems. Also included are practical tips, formulas, correlations, curves, charts and tables that should save engineers valuable time and effort.

2024-06-13