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Showing posts with label Piping. Show all posts
Showing posts with label Piping. Show all posts

PIPING & PIPELINE CALCULATIONS MANUAL

Wednesday, December 5, 2012


Contents
PART I
INTRODUCTION
Chapter 1:  Major Codes and Standards  3
Chapter 2:  Metric versus U.S. Customary Measurement  13
Chapter 3:   Selection and Use of Pipeline Materials  21

PART II
CONSTRUCTION AND DESIGN FABRICATION
Chapter 4:  Piping and Pipeline Sizing, Friction Losses, 
and Flow Calculations  35
Chapter 5:  Piping and Pipeline Pressure Thickness 
Integrity Calculations  57
Chapter 6:  Straight Pipe, Curved Pipe, and Intersection 
Calculations  85
Chapter 7:  Piping Flexibility, Reactions, and Sustained 
Thermal Calculations  119
Chapter 8:  Pipe-Supporting Elements and Methods 
Calculations  145
Chapter 9:  Specialty Components  161
Chapter 10:  High-Frequency versus Low-Frequency 
Vibration Calculations  181
Chapter 11:  Occasional Loads Calculations  199
Chapter 12:  Slug Flow and Fluid Transients Calculations  225
Chapter 13:  Fabrication and Examination Elements Calculations  241
Chapter 14:  Valves and Flow Control Calculations  263
Appendix:  Charts, Graphs, and Other Helpful Guides  281
Bibliography  355
Index  357

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Pipeline Rules of Thumb Handbook 5th

Monday, August 13, 2012

1: General Information, 1

Basic formulas 2

Mathematics—areas 3

Mathematics—surfaces and volumes 4

Cables and Ropes 5

Estimating strength of cable 5

Find the working strength of Manila rope 5

How large should drums and sheaves be for various types of wire rope? 5

Find advantages of block and tackle, taking into account pull out friction 6

Safe loads for wire rope 6

Stress in guy wires 7

Strength and weight of popular wire rope 9

Measuring the diameter of wire rope 9

Wire rope: ?eld troubles and their causes 9

Capacity of drums 11

Belts and Shafts  11

Determine length of a V-belt 11

Calculate stress in shaft key 12

Calculate V-belt length using simple equation 12

Estimate the horsepower that can be transmitted by a shaft 13

How to estimate length of material contained in roll 13

Convenient anti-freeze chart for winterizing cooling systems 13

How to determine glycol requirements to bring a system to a desired temperature protection level 14

Weight in pounds of round steel shafting 14

Properties of shafting 15

Tap drills and clearance drills for machine screws 16

Common nails 17

Drill sizes for pipe taps 17

Carbon steel—color and approximate temperature 17

Bolting dimensions for raised face weld neck ?anges 18

Steel ?tting dimensions 19

ANSI forged steel ?anges  20

Color codes for locating underground utilities 21

Approximate angle of repose for sloping sides of excavations 21

Trench shoring—minimum requirements  22

Reuniting separated mercury in thermometers 23

Typical wire resistance 23

How to cut odd-angle long radius elbows  24

How to read land descriptions 25

Size an air receiver for engine starting 27

Wind chill chart 28

Pipeline Pigging   29

Sizing plates  29

Caliper pigging 29

Cleaning after construction 29

Flooding for hydrotest 30

Dewatering and drying 30

Estimate volume of onshore oil spill 30

Estimating spill volume on water  32

2: Construction, 34

Project Scoping Data  35

Project scoping data worksheet for major facilities 35

Right-of-Way 36

How to determine the crop acreage included in a right-of-way strip 36

Clearing and grading right-of-way: labor/equipment considerations  36

Estimating manhours for removing trees  37

Estimating manhours for removing tree stumps 37

Clearing and grading right-of-way 38

Ditching  39

How many cubic yards of excavation in a mile of ditch?  39

Shrinkage and expansion of excavated and compacted soil 39

Ditching and trenching: labor/equipment considerations  39

Concrete Work  40

How to approximate sacks of cement needed to ?ll a form 40

What you should know about mixing and ?nishing concrete 40

Pipe Laying  40

How to determine the degrees of bend in a pipe that must ?t a ditch calling for a bend in both horizontal and vertical planes 40

How to bend pipe to ?t ditch—sags, overbends and combination bends 41

Pipe bending computations made with hand-held calculator  41

Calculate maximum bend on cold pipe 46

Determine length of a pipe bend  47

Length of pipe in arc subtended by any angle 47

Average pipelay table—Underground  48

Average pipelay table—On supports 49

Allowable pipe span between supports 49

How engineers make pipe ?t the ditch 50

Pipe Lowering  53

How to lower an existing pipeline that is still in service  53

Welding  56

When should steel be preheated before welding?  56

Welding and brazing temperatures 57

Mechanical properties of pipe welding rods 57

Lens shade selector 58

Pipeline Welding  58

How many welds will the average welder make per hour?  67

How much welding rod is required for a mile of schedule 40 pipeline?  67

How many pounds of electrodes are required per weld on line pipe?  67

Welding criteria permit safe and effective pipeline repair  68

Cross country pipeline—vertical down electrode consumption, pounds of electrode per joint 74

Guidelines for a successful directional crossing bid package 74

3: Pipe Design, 83

Steel pipe design  84

Properties of pipe 89

Length of pipe in bends 91

Calculation of pipe bends  92

Spacing of pipe supports  94

American standard taper pipe threads 96

British standard taper pipe threads 97

Normal engagement between male and female threads to make tight joints 98

Hand-held computer calculates pipe weight, contents,velocity 98

Formulas and constants of value in solving problems relating to tubular goods 101

How to calculate the contraction or expansion of a pipeline 102

Estimate weight of pipe in metric tons per kilometer 102

How to ?nd pipe weight from outside diameter and wall thickness  103

What is the maximum allowable length of unsupported line pipe? 103

Identify the schedule number of pipe by directmeasurement 103

Determine buoyancy of bare steel pipe 104

Determine buoyancy of bare and concrete coated steel pipe in water and mud 104

Weights of piping materials 105

Allowable working pressure for carbon steel pipe  105

Find the stress in pipe wall due to internal pressure 106

How to calculate stress in above/below ground transition 107

How to identify the series number of ?anged ?ttings  110

Dimensions of three-diameter ells with tangents  110

Polypipe design data  111

4: Electrical Design, 114

Electrical design  115

Hazardous locations 116

NEMA Enclosure Types  117

Size portable electric generators 118

Typical wattages for tools and applicances 119

Knockout dimensions  119

National Electrical Code Tables 120

Electrical formulas 124

Full load currents—single phase transformers 124

Full load currents—three phase transformers  125

Motor controller sizes 125

Voltage drop on circuits using 600V copper conductors in steel conduit 126

Determine the most economical size for electric power conductors  126

How to ?nd the resistance and weight of copper wires 127

What you should remember about electrical formulas 127

How to calculate microwave hops on level ground 127

For quick determination of the horsepower per ampere for induction motors (3 phase) at different voltages 128

Chart gives electric motor horsepower for pumping units 128

Pumping stations  129

Floodlighting Concepts  130

Terms 130

Floodlighting calculations  130

Point-by-point method 130

Beam-lumen method  131

Design procedure 131

Conductor size coversion chart—Metric to AWG  132

5: Hydrostatic Testing, 133

Hydrostatic testing for pipelines 134

Appendix A  140

Volume of water required to ?ll test section 140

Volume required at test pressure  141

Appendix B  142

How to use charts for estimating the amount of pressure change for a change in test water temperature 142

Compressibility factor for water 145

6: Pipeline Drying, 146

Pipeline Dewatering, Cleaning, and Drying   147

Dewatering 147

Cleaning pipelines 148

Brush pig run with gas 148

Brush pig run with liquid  148

Internal sand blasting  148

Chemical cleaning 149

Pipeline drying 149

Moisture content of air 151

Commissioning petrochemical pipelines 153

Vacuum drying 156


7: Control Valves, 159

Control valve sizing formulas  160

Sizing control valves for thruput 164

Control valve selection 169

Relief Valve Sizing, Selection, Installation and Testing   171

Rupture disc sizing 175

Rupture disc sizing using the resistance to ?ow method (KR) 176

Variable ori?ce rotary control valves 178

Sizing Valves for Gas and Vapor 180

Basic valve ?ow-capacity coef?cient (Cv)  180

8: Corrosion/Coatings, 185

Hand-held computer determines concrete coating thickness 186

NAPCA speci?cations 188

How much primer for a mile of pipe? 191

How much coal-tar enamel for a mile of pipe? 192

How much wrapping for a mile of pipe?  192

Estimating coating and wrapping materials required per mile of pipe 192

Coef?cient of friction for pipe coating materials 193

Troubleshooting cathodic protection systems: Magnesium anode system  195

Cathodic protection for pipelines  196

Estimate the pounds of sacri?cial anode material required for offshore pipelines  204

Comparison of other reference electrode potentials with that of copper-copper sulfate reference electrode at 25°C  206

Chart aids in calculating ground bed resistance and recti?er power cost 207

How can output of magnesium anodes be predicted?  208

How to determine the ef?ciency of a cathodic protection recti?er  208

How to calculate the voltage drop in ground bed cable quickly 209

What is the most economical size for a recti?er cable?  209

How to estimate the number of magnesium anodes required and their spacing for a bare line or for a corrosion “hot spot” 210

How can resistivity of fresh water be determined from chemical analysis? 210

What will be the resistance to earth of a single graphite anode? 211

How to estimate the monthly power bill for a cathodic protection recti?er  211

What will be the resistance to earth of a group of graphite anodes, in terms of the resistance of a single anode? 211

How can the current output of magnesium rod used for the cathodic protection of heat exchanger shells be predicted?  211

What spacing for test leads to measure current on a pipeline? 211

How many magnesium anodes are needed for supplementary protection to a short-circuited bare casing? 212

Group installation of sacri?cial anodes 212

How can the life of magnesium anodes be predicted?  213

How to ?nd the voltage rating of a recti?er if it is to deliver a given amount of current through a given ground bed (graphite or carbon) 213

Determining current requirements for coated lines 213

Determining current requirements for coated lines  when pipe-to-soil potential values are estimated 213

HVDC effects on pipelines 214

Troubleshooting cathodic protection systems: Recti?er ground bed 218

How to control corrosion at compressor stations 219

Project leak growth 220

Advances in Pipeline Protection  221

Methods of locating coating defects 222

Case histories 225

Estimate the number of squares of tape for pipe coating (machine applied)  226

Estimate the amount of primer required for tape  227

Tape requirements for ?ttings 227

Induced AC Voltages on Pipelines May Present a Serious Hazard 228

Measuring Unwanted Alternating Current in Pipe  230

Minimizing shock hazards on pipelines near HVAC lines 235

9: Gas—General, 237

Know the gas laws 238

Calculate gas properties from a gas analysis 240

Physical properties of selected hydrocarbons and other chemicals and gases  244

Nomograph for calculating density and speci?c volume of gases and vapors 252

Considerations for Selecting Energy Measurement Equipment 253

Facts about methane and its behavior 259

Conversion table for pure methane 263

Categories of natural gas and reserves terminology 264

Glossary of common gas industry terms 265

10: Gas—Compression, 268

Compressors  269

Performance calculations for reciprocating compressors 270

Estimating suction and discharge volume bottle sizes for pulsation control for reciprocating compressors 272

Compression horsepower determination 274

Generalized compressibility factor 276

Nomograph aids in diagnosing compressor cylinder ills  277

Centrifugal Compressor Data   278

Centrifugal compressor performance calculations  278

Nomographs for estimating compressor performance 282

Estimate hp required to compress natural gas 287

Estimate compressor hp where discharge pressure is1,000psi 287

Calculate brake horsepower required to compress gas 288

How to ?nd the size fuel gas line for a compressor station  288

Estimate engine cooling water requirements  289

Estimate fuel requirements for internal combustion engines 289

Estimating fuel requirements for compressor installation  290

11: Gas—Hydraulics, 291

Gas pipeline hydraulics calculations 292

Equivalent lengths for multiple lines based on Panhandle A 293

Determine pressure loss for a low-pressure gas system  294

Nomograph for determining pipe-equivalent factors  295

How much gas is contained in a given line section? 296

How to estimate equivalent length factors for gas lines 296

Estimating comparative capacities of gas pipelines 297

Determination of leakage from gas line using pressure drop method 297

A quick way to determine size of gas gathering lines 298

Energy conversion data for estimating 298

How to estimate time required to get a shut-in test on gas transmission lines and approximate a maximum acceptable pressure loss for new lines  299

How to determine the relationship of capacity increase to investment increase 299

Estimate pipe size requirements for increasing throughput volumes of natural gas  300

Calculate line loss using cross-sectional areas table when testing mains with air or gas  301

Flow of fuel gases in pipelines 302

Calculate the velocity of gas in a pipeline  303

Determining throat pressure in a blow-down system  303

Estimate the amount of gas blown off through a line puncture 304

A practical way to calculate gas ?ow for pipelines  304

How to calculate the weight of gas in a pipeline 305

Estimate average pressure in gas pipeline using up and downstream pressures  305

Chart for determining viscosity of natural gas  306

Flow of gas 306

Multi-phase ?ow  310

Nomograph for calculating Reynolds number for compressible ?ow friction factor for clean steel and wrought iron pipe  315

12: Liquids—General, 318

Determining the viscosity of crude 319

Chart gives API gravity of blends quickly  320

Liquid gravity and density conversion chart 321

Nomograph for calculating viscosities of liquid hydrocarbons at high pressure  321

Calculate viscosity of a blend  323

Calculate gravity of a blend 323

Convert viscosity units 323

Convert speci?c gravity to API gravity 323

Calculate bulk modulus 323

Viscosities of hydrocarbon liquids  324

Nomograph for calculating viscosity of slurries 325

Nomograph for calculating velocity of liquids in pipes 327

Nomograph for calculating velocity of compressible fluids in pipes  327

Nomograph for calculating velocity of liquids in  pipes 328

Derivation of basic ultrasonic ?ow equations  330

How fast does oil move in a pipeline? 332

Estimate the volume of a pipeline per linear foot using the inside diameter 332

What is the line?ll of a given pipe in barrels per mile? 332

Estimate leakage amount through small holes in a pipeline 333

Table gives velocity heads for various pipe diameters and different rates of discharge 334

13: Liquids—Hydraulics, 335

Marine Hose Data  336

CALM system 336

SALM system 336

Tandem system 337

Multi-point mooring system 337

Pressure loss in hose string 339

Pressure drop calculations for rubber hose 341

Examples of pressure drop calculations for rubber hose 341

Typical formulas used for calculating pressure drop and ?ow rates for pipelines 341

Hydraulic gradients 343

Equivalent lengths 346

Series systems 347

Looped systems 348

Calculate pressure loss in annular sections 349

Calculate pressure and temperature loss for viscous crudes =1,000 cP 349

Determine batch injection rate as per enclosure 352

Pressure Loss through Valves and Fittings   353

Representative resistance coef?cients (K) for valves and ?ttings 353

Nomograph for calculating Reynolds number for ?ow of liquids and friction factor for clean steel and wrought iron pipe  359

Nomograph for calculating pressure drop of liquids in lines for turbulent ?ow 361

Drag-Reducing Agents   365

The basics of drag reduction  365

How drag-reducing agents can outweigh looping or boosting 370

How active, passive drag affect DRA injections 376

How to estimate the rate of liquid discharge from a pipe 382

Predict subsurface temperature ranges 382

Sizing pipelines for water ?ow 383

How approximate throughput of a line can be estimated from pipe size 384

Gauge liquid ?ow where no weir or meter is available 384

Estimate crude gathering line throughput for a given pipe diameter  384

How to determine head loss due to friction in ordinary iron pipeline carrying clear water  384

How to size lines, estimate pressure drop and optimum station spacing for crude systems 385

Estimate the optimum working pressures in crude oiltransmission lines  385

How to size crude and products lines for capacity increases 386

How to determine the maximum surge pressure in liquid-?lled pipeline when a main valve is closed suddenly 386

What is the hydrostatic pressure due to a column of oil H feet in height? 386

Transient pressure analysis 387

Tank farm line sizing  396

14: Pumps, 399

Centrifugal pumps 400

Speed torque calculation  412

Pulsation Control for Reciprocating Pumps  413

Key Centrifugal Pump Parameters and How They Impact Your Applications Part 1  421

Key Centrifugal Pump Parameters and How They Impact Your Applications Part 2  426

Estimate the discharge of a centrifugal pump at various speeds  431

How to estimate the head for an average centrifugal pump  431

Find the capacity of reciprocating pump  432

How to estimate the horsepower required to pump at a given rate at a desired discharge pressure  432

Nomograph for determining reciprocating pump capacity 432

Nomograph for determining speci?c speed of pumps  434

Nomograph for determining horsepower requirement of pumps 435

How to select motors for ?eld gathering pumps 435

Reciprocating pumps  436

Understanding the basics of rotary screw pumps  445

15: Measurement, 451

Pipeline ?ow measurement—the new in?uences  452

Liquid measurement ori?ce plate ?ange taps  455

Mass measurement light hydrocarbons 459

Pipeline measurement of supercritical carbon dioxide 460

Gas Measurement  466

Master meter proving ori?ce meters in dense phase ethylene 466

Gas or vapor ?ow measurement—ori?ce plate ?ange taps 473

Properties of gas and vapors 477

Determine required ori?ce diameter for any required differential when the present ori?ce and differential are known in gas measurement 482

Estimate the temperature drop across a regulator 483

Estimate natural gas ?ow rates 483

How to estimate the average pressure differential on the remaining meter runs of a parallel system when one or more runs are shut off 484

Sizing a gas metering run  484

List of typical speci?cations for domestic and commercial natural gas 484

Determine the number of purges for sample cylinders 485

Find the British thermal units (Btu) when the speci?cgravity of a pipeline gas is known 485

Estimate for variations in measurement factors 485

Rules of measurement of gas by ori?ce meter 486

How to measure high pressure gas 486

Four ways to calculate ori?ce ?ow in ?eld 490

Practical maintenance tips for positive displacement meters  493

Sizing headers for meter stations  497

16: Instrumentation, 500

Types of control systems  501

Developments in Pipeline Instrumentation  503

Flow measurements 504

Proving devices 506

Valves 507

Acoustic line break detectors  508

“Smart” pressure sensors  509

Densitometers 510

Pipeline samplers  511

Pipeline monitoring systems 512

Computer systems 513

SCADA systems 515

Cathodic protection 515

System design guidelines  515

Future trends 516

Choosing the Right Technology for Integrated SCADA Communications  517

17: Leak Detection, 522

Pipeline Leak Detection Techniques   523

Causes and economic aspects of leaks 523

Simple leak detection systems 524

Pig-based monitoring systems 525

Computer-based monitoring systems  525

Pipeline leak phenomena  526

Background philosophy of pipeline modeling  526

Basic pipeline modeling equations 527

Impact of instrument accuracy 528

System design aspects and guidelines  529

Development of pipeline monitoring systems  530

18: Tanks, 532

Charts give vapor loss from internal ?oating-roof tanks 533

Estimating the contents of horizontal cylindrical tanks 535

How to gauge a horizontal cylindrical tank 536

Use nomograph to and tank capacity  536

Correct the volume of light fuels from actual temperature to a base of 60°F  538

Volume of liquid in vertical cylindrical tanks 538

Chart gives tank’s vapor formation rate 538

Hand-held calculator program simpli?es like computations 539

19: Maintenance, 544

How to Plan for Oil Pipeline Spills  545

Regulatory requirements  545

Contingency plan objectives 545

Related studies 545

Planning concepts 546

Contingency response 547

Immediate response 548

Immediate response actions 549

Flexible response actions  549

Training 550

20: Economics, 552

Rule of thumb speeds payroll estimates 553

Rule of thumb estimates optimum time to keep construction equipment 554

How to estimate construction costs 556

Cost estimating strategies for pipelines, stations, terminals 559

Economics 566

Time Value of Money: Concepts and Formulas  570

Simple interest vs compound interest 570

Nominal interest rate vs effective annual interest rate 571

Present value of a single cash ?ow to be received in the future  571

Future value of a single investment 572

The importance of cash ?ow diagrams 572

Analyzing and valuing investments/projects with multiple or irregular cash ?ows 572

Perpetuities 573

Future value of a periodic series of investments 574

Annuities, loans, and leases 574

Gradients (payouts/payments with constant growth rates) 575

Analyzing complex investments and cash ?ow problems 576

Decision and Evaluation Criteria for Investments and Financial Projects  577

Payback method  577

Accounting rate of return (ROR) method  578

Internal rate of return (IRR) method  579

Net present value (NPV) method  580

Sensitivity Analysis  581

Decision Tree Analysis of Investments and Financial Projects 582

Accounting Fundamentals   586

Estimate the cost of a pipeline in the US (based on 1994 data)  590

How to compare the cost of operating an engine on diesel and natural gas  591

How to estimate energy costs for different pipelinethroughputs 591

Comparing fuel costs for diesel and electric prime movers 592

Nomograph for calculating scale-up of equipment or plant costs  592

Nomograph for calculating scale-up of tank costs  594

Nomograph for determining sum-of-years depreciation 595

Nomograph for estimating interest rate of return oninvestment (“pro?tability index”) 595

Nomograph for determining break-even point 597

Chart gives unit cost per brake horsepower of reciprocating compressors with various types of prime movers  598

Chart shows in?uence on unit cost of numbers of reciprocating compressor units installed in one station  598

Chart gives unit cost per brake horsepower of  centrifugal compressors with various types of prime movers 599

21: Rehabilitation—Risk

Evaluation, 600

When does a pipeline need revalidation? The in?uence of defect growth rates and inspection criteria on an operator’s maintenance program 601

Pipeline risk management 610

22: Conversion Factors, 614

Units of measurement from one system to another 615

Viscosity—equivalents of absolute viscosity 623

General liquid density nomograph 624

Chart gives speci?c gravity/temperature relationship for petroleum oils  626

Weight density and speci?c gravity of various liquids  626

Metric conversions—metric to English, English to metric  627

Temperature conversion—centigrade to Fahrenheit,Fahrenheit to centigrade 628

Viscosity—equivalents of kinematic viscosity 629

Viscosity—equivalents of kinematic and Saybolt Universal Viscosity  629

Viscosity—equivalents of kinematic and SayboltFurol Viscosity at 122°F 630

Viscosity—general conversions 631

Pressure conversion chart 633

A simple method to determine square root 633

SI data 634

Energy conversion chart  635

Flow conversion chart 635

Conversions involving different types of fuel  636

Weight of water per cubic ft at various temperatures 641

Engineering constants 641

Mensuration units 642

Minutes to decimal hours conversion table 642

How to compare costs of gas and alternate fuels 643

Typical characteristics of fuel oils  643

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Piping Systems Manual

Tuesday, April 5, 2011

Introduction
I have for many years wanted to compile some thoughts about piping design. As a young engineer, I was often confronted with a problem that was new to me. Older engineers and superiors would often advise me to “check the Corinth job,” or “see what we did five years ago on the XYZ project.” I would dig through stacks of files and dozens of drawings, only to find that the problems were not the same, or what they had imagined as an existing solution existed only in their failing memories. Nothing was on paper that could be applied to the problem at hand. I suppose this sort of thing applies not just to piping design, but to every other aspect of engineering as well.

In any case, I would waste a lot of time looking for answers in the existing reference materials, only to discover that many texts were silent on the topic under investigation. I would then be forced to do a lot of research and draw my own conclusions.

An example of this was when I was responsible for the start-up of a hot oil calender system, circa 1984. The mill engineers and project managers were concerned over the cleanliness of the piping. My initial reaction was that someone should be watching what the contractors were doing as they fabricated and hung the pipe to ensure that the pipe remained clean. And although this seems to be a reasonable approach, it would
not have assisted in this particular case. Nor is it common to bird-dog the fitters to ensure that hard hats, wrenches, 2 x 4’s, etc. don’t get left inside pipes.


Cleanliness of piping is not often addressed in the reference books. While there are
standards for the cleanliness of hydraulic piping and piping found in the pharmaceutical
and food and beverage industries, there was not a lot to choose from in the general
arena of industrial service piping.

Many phone calls later, I was finally able to lay my hands on a copy of PFI Standard ES-5, Cleaning of Fabricated Piping. This was a three-page document published by the Pipe Fabrication Institute. At least now I had a starting point and was able to apply this standard to the system that was causing so much heartburn among my managers. Back in 1984, one had to rely on picking up a scent, persistence, and lots of phone calls and trips to the library. Now that we have the Internet, the playing field has been leveled, although a quick Internet search of “pipe cleanliness standards” proves that today the process is still no picnic.

There are many excellent reference materials available. Some of these are referenced in this manual, and no serious student of piping should be without the Piping Handbook by Nayyar, or earlier editions by Crocker and King.

This is not a scholarly manual. I have tried to organize it in a logical manner and make the information readable and easy to access. The reader will forgive me for stating certain opinions (which should be obvious in the text, and not to be confused with facts).

Further, this text is intended to be practical rather than comprehensive. I have tried to highlight the items a piping engineer will most likely encounter, rather than to attempt an encyclopedic volume. For example, while there is much wonderful information in ASME B31.1, I have touched only on the portions one might encounter in a “typical”piping job.

Throughout the preparation of this manuscript, I was faced with trying to strike a balance between solving the tough problems we face every day, and overstating the obvious. A review of online discussion sites indicated to me that there really was no shortage of elementary questions out there, but in fairness to those who appear to be new to the profession, the more you delve into an issue, the less you seem to know1. And though I tried to remain practical, some subjects are irresistible, and so I couldn’t resist footnoting that PTFE is the only known substance to which a gecko cannot stick.

The piping engineer for a project will encounter many issues outside of any strict definition of “piping.” There will be process equipment such as tanks, heat exchangers, pumps, structures, and so on. Early in a project, the piping engineer is asked to determine the horsepower of the pumps, so that electrical equipment may be sized. This often occurs before complete process information is available. As the project continues, it is most often the piping engineer who becomes the focal point, the lightning rod, the bottle-neck.

Operating and maintenance issues must always be considered, and are often left to the piping engineer to resolve. Broad knowledge of the other disciplines’ needs, as well as the industry served, is often required. My task in writing this book was to concentrate on the piping side, though I have made some minor excursions into some of the areas described above. Perhaps if the publishers and the engineering community enjoy this book, they may permit me an opportunity to examine a broader scope at some later date.

Some Miscellaneous Thoughts on Piping
1. The trades should always be made aware that piping cleanliness is of the utmost importance. This certainly applies to the inside of the piping, valves, and fittings but also to sumps as well. Stressing this point will save a lot of time on startups.
2. Take advantage of “non-traditional” piping materials such as HDPE for underground applications. While these materials have been around for some time, “old-timers” may be reluctant to use them.
 3. Determining the size of piping is usually a function of its velocity. Keep in mind that the installed cost of piping is primarily a function of labor costs and it really doesn’t cost much more to increase one pipe size to reduce friction and also to allow for future capacity. On the other hand, one has to be aware of the application. Bigger is not always better, especially if you are dealing with slurries.
4. Be aware of the possibility of back flowing through Y-type strainers since these screens may be very flimsy and will collapse when the flow reverses through them.
5. Don’t neglect startup considerations in the design of the piping system. Be sure that you have high point vents and low point drains, and have the spares and clearances to remove, clean, or replace strainer screens.
6. In some cases, you may have to consider the minimum and maximum flows through a line over its life. This is particularly important for slurries and gravity flow lines.
7. Nobody likes to pay for welders. This means that if you can minimize the number of welds, everyone (except the welders) will be happier.
8. Viton gaskets smell like cinnamon.

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Technology Piping

Wednesday, March 2, 2011



Preface xv
New Developments
Acknowledgments  xxiii
1 New Pipeline Installations  
1.1 Buried Pipe History  
1.1.1 The Pipe-Soil Interaction
1.2 Open-Cut Method of Pipe Installation
1.3 Comparison of Construction Operations
1.4 Trenchless Technology Methods
1.5 Three Main Divisions of Trenchless Technology Methods
1.6 Trenchless Installation Methods  
1.6.1 Conventional Pipe Jacking
1.6.2 Utility Tunneling
1.6.3 Horizontal Earth Boring
1.7 Characteristics and Applications of Trenchless Construction Methods  
1.8 Capabilities and Limitations of New Installation Methods  
1.8.1 Conventional Pipe Jacking and Utility Tunneling  
1.8.2 Horizontal Auger Boring  
1.8.3 Horizontal Directional Drilling
1.8.4 Microtunneling
1.8.5 Pilot-Tube Microtunneling   
1.8.6 Pipe Ramming
1.9 Planning and Safety Considerations
1.10 Cost Estimating and Bidding
1.11 Summary
2 Existing Pipeline Renewal and Replacement Methods
2.1 Introduction
2.1.1 Existing Pipe Underperformance
2.2 Planning Trenchless Renewal/Replacement Project
2.2.1 Planning Activities
2.2.2 Design Process
2.3 Applicability of Trenchless Renewal and Replacement Methods
2.3.1 Cured-in-Place Pipe  
2.3.2 Sliplining
2.3.3 Modifi ed Sliplining
2.3.4 Coatings and Linings
2.3.5 Close-Fit Pipe
2.3.6 Thermoformed Pipe
2.3.7 Lateral Renewal
2.3.8 Point Source Repair or Localized Repairs
2.3.9 Trenchless Replacement Methods
2.4 Sample Decision Support Systems for Gravity and Pressure Pipes
2.5 Emerging Design Concepts for Pipeline Renewal Systems
2.5.1 Long-Term Testing  
2.6 Summary
2.7 Sample Design Calculations for CIPP
2.8 Sample Specifi cations for CIPP
3 Spray-on Coatings and Linings for Renewal of Potable Water Pipe Distributions
3.1 Introduction 
3.2 Water Distribution Pipe Applications
3.3 Selecting a Water Pipe Renewal Method
3.4 Installation Phases of Coatings and Linings
3.5 Planning and Site Investigations
3.6 Pipe Inspection  
3.6.1 Objectives of Prelining Inspections .
3.7 Pipe Cleaning Methods .
3.8 Installation Considerations .
3.9 Disinfection Methods .
3.9.1 Tablet Method .
3.9.2 Continuous Feed Method .
3.9.3 Slug Method .
3.9.4 Ozonation .
3.9.5 U.K. Method  
3.10 Pipe Sample Testing .
3.11 Quality Control .
3.12 Safety .
3.13 Reconnecting Appurtenances .
3.14 Surface Restoration and Site Clearing  .
3.15 Waste Disposal .
3.16 Descriptions of Coatings and Linings Methods .
3.16.1 Cement-Mortar Linings .
3.16.2 Epoxy Linings.
3.16.3 Polyurea .
3.16.4 Polyurethane.
3.17 Installation Procedures.
3.18 Comparison of Coating and Lining Methods.
3.19 Ongoing Research on Liner and Pipe Interactions.
3.20 Summary.
4 Pipe and Pipe Installation Considerations.
4.1 Introduction
4.2 Pipeline Construction Using Open-Cut Method.
4.3 The Pipe-Soil System.
4.3.1 Rigid Pipes and Flexible Pipes  .
4.3.2 Soils.
4.3.3 Pipe-Soil Interaction.
4.3.4 Behavior of Rigid Pipes.
4.3.5 Behavior of Flexible Pipes.
4.4 Common Modes of Pipeline Failures.
4.4.1 Failure Modes in Rigid Pipes.
4.4.2 Failure Modes in Flexible Pipe.
4.5 Pipe Selection Considerations.
4.6 Rigid Pipes.
4.6.1 Cement-Based Pipes  .
4.6.2 Vitrifi ed Clay Pipe.
4.7 Plastics Pipes.
4.7.1 Properties of Viscoelastic Pipe Materials  .
4.7.2 Polyvinyl Chloride Pipe.
4.7.3 Polyethylene Pipe.
4.7.4 Glass-Reinforced Pipe (Fiberglass Pipe)  .
4.7.5 Metallic Pipes .
4.8 Summary
5 Project Considerations for Horizontal Directional Drilling
5.1 Introduction
5.2 Method Description
5.3 Maxi-HDD Considerations
5.3.1 Site Investigation Requirements
5.3.2 Drilling Operations
5.3.3 Drilled Path Design
5.3.4 Drilling Fluids
5.3.5 Product Pipe Specifi cations
5.3.6 Specifi cations and Drawings
5.3.7 Contractual Considerations
5.3.8 Inspection and Construction Monitoring
5.4 Mini-HDD Considerations
5.4.1 Mini-HDD Planning
5.4.2 Bore Path Layout and Design—Vertical Trajectory
5.4.3 Overall Bore Path Layout and Design
5.5 Pipe Load Calculations
5.5.1 Pipe Load Calculations
5.5.2 Simplifi cations for Mini-HDD Applications
5.5.3 Applications
5.5.4 Design Example
5.6 Summary
6 Project Considerations for Pipe Replacement Methods
6.1 Introduction
6.2 Pipe Bursting
6.2.1 Pneumatic Bursting Systems
6.2.2 Hydraulic Bursting Systems
6.2.3 Static Bursting Systems
6.3 Pipe Removal Systems
6.3.1 Pipe Reaming
6.3.2 Impactor Method
6.3.3 Pipe Ejection, Extraction,
or Insertion
6.3.4 Pipe Eating
6.4 Existing Pipe Materials
6.5 Replacement (New) Pipe Material
6.6 When Is Pipe Bursting a Preferred Solution?
6.7 Pipe Bursting Project Classifi cation
6.7.1 Pipe Bursting Applicability and Limitations .
6.8 Design Considerations
6.8.1 Utility Survey
6.8.2 Investigation of Existing Pipe and Site Conditions .
6.8.3 Insertion and Pulling Shaft Requirements
6.8.4 Geotechnical Investigation Requirements
6.8.5 Maximum Allowable Operating Pressure
6.8.6 Risk Assessment Plan
6.8.7 Ground Movements
6.8.8 Drawings and Specifi cations
6.8.9 Submittals
6.8.10 Quality Assurance/Quality Control Issues
6.8.11 Dispute Resolution Mechanisms
6.8.12 Permitting Issues
6.8.13 Cost Estimating
6.9 Construction Considerations
6.9.1 Typical Pipe-Bursting Operation Layout
6.9.2 Shoring the Entry and Pulling Shafts
6.9.3 Matching System Components to Reduce Risk of Failure
6.9.4 Nearby Utilities
6.9.5 Bypass Pumping
6.9.6 Dewatering
6.9.7 Ground Movement Monitoring
6.9.8 Manhole Connections
6.9.9 Pipe Connection to Other Pipes
6.9.10 Pipe Bursting Water Mains
6.9.11 Service Connections
6.9.12 Grooves on the Outside Surface of the Pipe
6.9.13 As-Built Drawings
6.9.14 Contingency Plan
6.9.15 Safety Considerations
6.9.16 Potential Problems
6.10 Sample Pipe Load Calculations
6.10.1 Introduction
6.10.2 Pulling Loads—Theoretical Considerations
6.10.3 Pulling Loads—Planning Guide
6.10.4 Pipe Collapse Conditions
6.11 Summary
7 Construction and Inspection for Cured-in-Place Pipe
7.1 Overview of the CIPP Technology
7.1.1 Background
7.1.2 Method Description
7.2 Site Compatibility and Applications
7.2.1 Effects of Pipe Defects
7.3 Main CIPP Characteristics
7.3.1 Tube Wet-Out
7.4 CIPP Installation Methods
7.4.1 Pulled-in-Place Process
7.4.2 Inversion Process
7.4.3 Preliner Options
7.4.4 CIPP Liner Curing
7.5 Inspecting CIPP Installation
7.6 Pipe Plugging or Bypass Pumping
7.7 Quality Assurance and Testing
7.7.1 CIPP Inspection and Acceptance
7.7.2 Workmanship
7.7.3 Quality Control Issues
7.8 Summary
8 Inspection and Quality Assurance/Quality Control for Trenchless Installation and Replacement Methods
8.1 Conventional Pipe Jacking
8.1.1 Introduction
8.1.2 Materials
8.1.3 Construction
8.2 Microtunneling .
8.2.1 Introduction
8.2.2 Pipe Materials
8.2.3 Construction
8.3 Pilot-Tube Microtunneling
8.3.1 Introduction .
8.3.2 Design of the Pipe
8.3.3 Construction Considerations
8.4 Horizontal Auger Boring
8.4.1 Introduction
8.4.2 Materials
8.4.3 Construction
8.5 Pipe Ramming
8.5.1 Introduction
8.5.2 Materials
8.5.3 Construction
8.6 Horizontal Directional Drilling
8.6.1 Introduction
8.6.2 Pipe Material Standards
8.6.3 Construction
8.7 Pipe Replacement
8.7.1 Introduction
8.7.2 Materials
8.7.3 Construction
8.8 Access Pits/Driving and Receiving Shafts
8.9 Settlement/Heaving Monitoring
8.10 Groundwater Control
8.11 Boring/Ramming/Bursting Failure
8.12 Contamination
8.13 Bulkhead
8.14 Work-Site Restoration
8.15 Summary
9 Planning and Safety Considerations for Trenchless Installation Methods
9.1 Introduction
9.2 Planning for a Trenchless Project
9.2.1 Surface Survey and Site Visit
9.2.2 Subsurface Investigations
9.2.3 Geotechnical Investigations
9.2.4 Permits
9.2.5 Job Site Logistics Requirements
9.2.6 Length of Installation
9.2.7 Alignment Considerations
9.2.8 Accuracy and Tolerances Including Settlement and Heave
9.3 Trenchless Safety Considerations
9.3.1 Project Safety Planning
9.3.2 Hazard Assessment
9.3.3 Risk Assessment
9.3.4 Utility Mapping
9.3.5 Contingency Plans
9.3.6 Communication
9.3.7 Equipment Operator Training
9.4 Summary
A References
B Related Documents
C Acronyms and Abbreviations .
D Glossary of Terms
E Conversion Table
Index 

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Process Piping Drafting

Friday, November 13, 2009




CONTENTS
PREFACE
INTRODUCTION ix
I EQUIPMENT TERMS I
Definition of Terms
Linework Exercise
Lettering Exercise

2- BASIC PIPING DATA 9
Pipe, Fittings, Flanges, Valves
Symbols for Flanges & Fittings
Symbols for Valves & Flanges
Dimensions for Valves & Fittings
Projection Exercise-welded piping
Projection Exercise-screwed piping

3- FLOW DIAGRAMS INSTRUMENTATION 27
Process Flow Sheet
Mechanical Flow Sheet
Utility Flow Sheet
Instrumentation

4- ABBREVIATIONS SPECIFICATIONS 50
Abbreviations for Piping Draftsmen
Piping Specifications
Insulation
Pipe Line List
Piping Specialty List


5- NOMENCLATURE, PLANS DETAILS 72
Nomenclature: Vessels, Structural, Concrete & Electrical
Plot Plan
Foundation Location Plan
Piping Drawing Index Plan
Standard Piping Details
Bridles
Traced Lines

6- PIPING DESIGN NOTES PLANS 89
Piping Design Instructions
Meter Runs
Piping on Vertical Vessels
Standard Pipe Spacing
Flange Bolting

7- PIPING PLANS e PROCESS EQUIPMENT 99
Piping Plan and Elevation
Piping Isometric Drawing
Vessel Drawings
Exchanger Drawing
Pump Drawing
Concrete Drawings
Steel Drawings

8- ISOMETRIC DEFINITIONS, DIMENSIONING
CALL-OUTS 139
Isometric Definition
Configuration Problems
Detail Dimensioning
Isometric Call-Outs
Isometric Problems

9- PROBLEMS 166
Trigonometric Problems
Orthographic Projections
Natural Functions

10- FINAL TEST 180
Student Exercise-40 Hours
Make Piping Drawings
Make Piping Isometrics

Total 268 pages 11 mb

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Piping and Pipeline Engineering

Wednesday, November 11, 2009



Contents
PREFACE xv
CHAPTER 1 CODES, STANDARDS AND PRACTICE 1
CHAPTER 2 FUNDAMENTALS 38
CHAPTER 3 MATERIALS 46
CHAPTER 4 INTERNAL PRESSURE 84
CHAPTER 5 EXTERNAL PRESSURE 122
CHAPTER 6 LAYOUT AND SUPPORTS 126
CHAPTER 7 FLEXIBILITY AND FATIGUE 152
CHAPTER 8 VIBRATION 182
CHAPTER 9 FLUID TRANSIENTS 208
CHAPTER 10 WIND DESIGN 232
CHAPTER 11 SEISMIC DESIGN AND RETROFIT 236
CHAPTER 12 EXPLOSIONS 257
CHAPTER 13 SUBSEA PIPELINES 270
CHAPTER 14 BURIED PIPE 283
CHAPTER 15 WELDING 291
CHAPTER 16 EXAMINATION308
CHAPTER 17 PIPE FLANGE 325
CHAPTER 18 MECHANICAL JOINTS 349
CHAPTER 19 LEAK AND PRESSURE TEST 354
CHAPTER 20 DEGRADATION IN SERVICE 366
CHAPTER 21 FITNESS-FOR-SERVICE 386
CHAPTER 22 MAINTENANCE, RELIABILITY AND FAILURE ANALYSIS 411
CHAPTER 23 REPAIR TECHNIQUES 435
CHAPTER 24 PLASTIC PIPE 453
CHAPTER 25 VALVES 464
APPENDIX STANDARD PIPE SIZES 483
INDEX 489

Total 519 pages 4.2 mb
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Piping Materials Selection and Application

Tuesday, November 10, 2009



PREFACE
The Piping Material Selection Guide for Process Systems, as the title
states, is a guide for the piping engineer who is faced with the challenge
of choosing the correct piping materials of construction.
The list of codes and standards in ASME B31.3 that apply to process
plant design is huge, and it is impossible to cover them all in one book.
Instead I use ASME B31.3 as the basic construction code, and I briefly
touch on the most significant codes and standards applicable to the
design of the plant.
The EPC contractor is responsible for having all the necessary codes
and standards available at all times during the design, construction, and
commissioning of the plant. These standards must be the final reference
point, and the objective of this book is to guide the piping engineer to
that point.
Although the function of a piping material engineer is driven by code
and specifications, there is no substitute for all-around experience. This
can be gained from several areas: the design office, a manufacturer’s
facility, the fabrication yard, as well as the job site. Exposure to as many of
these facets of the process industry as possible is beneficial to the growth
of an engineer’s professional development. Each sector has its own
characteristics, and knowledge of one aids the comprehension the others.
The design office is where the project evolves and is engineered and
developed on paper. A manufacturer’s facility is were the numerous
individual components essential for construction of the project are built.
For piping this includes pipe, fittings, flanges, valves, bolts, gaskets, and
the like. In the fabrication yard, the welded piping components are
‘‘spooled’’ up for transportation to the job site. At the job site, paper and
hardware come together and final fabrication and erection take place.
The various piping systems are commissioned, and the project is brought
to its conclusion and finally handed over to the client’s operators. All
these phases of a project are equally important, and it is very important
vii
that the engineer understand the challenges that arise in these very
different environments.
The Piping Material Selection Guide for the Process Systems is written
to be useful to all piping engineers and designers involved in the design,
construction, and commissioning of oil, gas, and petrochemical facilities.
However, it is primarily aimed at the piping material engineer, the
individual responsible for the selection and the specifying of piping
material for process facilities.
Piping engineering and the materials used in the construction of piping
systems is a huge subject. It is virtually impossible to cover all aspects of
it in depth in one volume. In this book, I try to cover the most important
areas and introduce the reader to the fundamentals of the specific
subjects. I suggest readers skim through the pages to gain a familiarity
with the topics covered. I have introduced each subject and then linked it
with text and technical data. I limit my use of opinions and concentrate
on mandatory statements that are set out in the design codes. These
standards must be met or improved on.
Most of the individuals I have worked with have developed their skills
by working with fellow engineers who imparted their knowledge to the
uninitiated. The ingredients that go into making a good engineer are not
fully taught in schools, colleges, or universities, but by experience gained
listening to more-knowledgeable colleagues, absorbing information, and
through personal research.
To be a complete engineer, it is essential not only to have knowledge
but to share this knowledge with fellow piping engineers and other
colleagues. A piping material engineer’s role is driven by codes,
standards, technical data, and catalogued information. When asked a
question I believe that, if possible, the answer should be supported with a
copy from the relevant source of information. This allows recipients to
file the information, makes them more confident, and protects the piping
material engineer. It is a small action that pays big dividends.
Despite several excellent textbooks on piping design and piping stress,
I know of none that specializes in piping materials. It is not the intention
of this book to explain the geometry of the numerous piping components
and how their final shape is computed. All the piping components
discussed in this book are covered by strict design codes or recognized
manufacturers’ standards. Their dimensions are carefully calculated and
unlikely to change dramatically in the near or distant future. Indeed,
most have remained the same dimensionally for several decades and
longer.
viii Preface
Piping engineering is not rocket science. As a fellow engineer, not a
piping specialist, once said, ‘‘I thought that the Romans sorted piping
out.’’ Not true, but I see where my colleague was coming from. The
piping content of a project is generally the largest of all the disciplines in
material value, engineering, and construction personnel. Piping engineering
also creates large volumes of paper in the form of drawings,
specifications, and support documents. What it lacks in technical
complexity it more than makes up for by the volumes of paperwork,
which seem to increase each year.
So, to conclude, although piping may not advance as quickly as other
disciplines, such as instrumentation and electrical, which are driven
greatly by vendors and technology, piping does not stand still. New
materials are always being developed, as well as fresh methods of
manufacturing and new designs, that constantly fine-tune what we
inherited from our friends the Romans.
If this book does not completely answer your questions, I feel sure that
it will guide you in the right direction.
Peter Smith
Fano, Italy
June 2004


Preface vii
1 The Piping Material Engineer 1
2 Process Industry Codes and Standards 11
3 Materials 37
4 Piping Components 131
5 Joints for Process Piping Systems 171
6 Bolts and Gaskets 201
7 Valves 213
8 Glossaries and Abbreviations 243

Total 356 pages 5.5 mb
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Process Plant Piping Maintenance & Repair

Monday, November 9, 2009




I. Introduction
The structural integrity of piping systems must be maintained after they have been placed into service so that they will provide safe, reliable, long-term operation. Therefore, existing piping systems require periodic inspection to determine their current condition and permit evaluation of their structural integrity to permit future operation. Should unacceptable deterioration or flaws be identified, pipe repairs may be required. Existing piping systems might also require alterations or rerating to accommodate new operational needs (or to
accommodate deterioration that cannot or will not be repaired).

Process plants must adopt and follow established procedures for the inspection, repair, alteration, and rerating of piping systems after they have been placed into service. API 570, “Piping Inspection Code – Inspection, Repair, Alteration, and Rerating of In-Service Piping Systems,” provides the basic procedures to be followed by process plants. This course is based on API 570.

Scope of API 570
API 570 was developed for the petroleum refining and chemical process industries. But since most of its requirements have broad applicability, it may be used for any piping system. It must be used by organizations that maintain or have access to an authorized inspection agency, a repair organization, and technically qualified piping engineers, inspectors, and examiners (as defined in API 570).

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Mechanical Estimating Manual Sheet Metal Piping & Plumbing

Saturday, November 7, 2009




Contents
Preface xi
Section I—HOW TO PREPARE SHEET METAL AND PIPING ESTIMATES
Chapter

1 Successful Estimating Principles 3
Crux of Successful Contracting 3
Primary Goals of Contracting and Bidding 3
Problems and Causes of Poor Estimating 3
Estimating Competence Required 4
The Eight Facets of the Estimating Diamond 4
Performance Standards for Complete and Accurate Estimates 5
Fundamental Bidding Rules 5
How to Estimate Labor Accurately and Realistically 8
Do Your Homework 9
Use Time Saving Estimating Techniques 9
Apply Valid Overhead and Profi t Markups 10

2 Systematic, Effi cient, Accurate Estimating Procedures 11
Steps in the Estimating Procedure 11
Checking Estimates 12
Scope of Complete Sheet Metal Estimate, Check-off List 16
Heating Equipment Check-off List 17
Cooling Equipment Check-off List 18
End of Bid Factors Check-off List 18
Remodeling Work Check-off List 19
15 Bastards with No Regular Homes 20

3 Sample HVAC Estimate and Forms 23
Overview of Sample Job 23
Purpose of Forms 23
Specifi cations on Sample Job 24
IBM Offi ce Drawing 25
Sample Filled Out Estimating Forms 26
Calculating Labor Costs Per Hour 31

Section II —BUDGET ESTIMATING
Chapter
4 Budget Estimating 37
Budget Estimates 37
Semi-Detailed Scope Budget Estimates 37
Detailed Estimates 38
Budget Estimating HVAC Costs and Engineering Loads 38
Budget Estimating Galvanized Ductwork 39

Section III —EQUIPMENT ESTIMATING
Chapter
5 Heating and Cooling Equipment 59
Chilled and Hot Water Pumps 60
Hot Water Reheat Coils 61
Electric Duct Heaters 62
Duct Heaters 63
Unit Heaters 63
Gas Fired Cast Iron Boilers 64
Baseboard Heating 65
Infra Red Units 66
Electric Baseboard Heating 66
Wall Heaters 67
DX Evaporator Coils 68
Chilled Water Coils 69
Centrifugal Water Cooled Chillers 70
Reciprocating Chillers 71
Cooling Towers 73
Heat Pumps 74
Condensing Units 75

6 HVAC Units and Air Distribution Equipment 77
Rooftop Units 78
Air Handling Units 80
Self Contained Air Conditioning Units 83
Dampers 87
Louvers 89
Estimating Registers 90
Ceiling Diffusers 91
VAV Terminal Units, Components etc 92
Filter Labor 96

7 Plumbing Fixtures and Specialties 97

8 Air Pollution and Heat Recovery Equipment 101
Air pollution equipment 101

Section IV— SHEET METAL ESTIMATING
9 Sheet Metal Estimating Basics 109
Requirements of a Profi cient Sheet Metal Estimator 109
Types of Ductwork 111
Procedure for Taking Off Ductwork 112
Types of Ductwork Connections 113
Methods of Figuring Ductwork Weight 114
Methods of Calculating Ductwork Labor 115
Material Data 124
Correction Factors 125

10 Galvanized Ductwork 129
Estimating Galvanized Ductwork by the Piece 129
Estimating Galvanized Ductwork by the Pound 136
Medium and High Pressure Ductwork 142
Automatic Duct Coil Line Fabrication 143

11 Spiral and Light Gauge Round Ductwork 145
Round Duct Gauge Data 146
Furnace Pipe Flexible Tubing and Flues 146
Spiral Pipe and Fittings 147

12 Estimating Fiberglass Ductwork 155
Introduction 155
Fiberglass Ductwork Construction 156
Pricing Sheet Metal Components 158
Estimate Summary and Extension Sheet 158

13 Heavy Gauge Ductwork 159
Types of Industrial Exhaust Ductwork 159
Rectangular Black Iron 159
Round Black Iron Ductwork 166
Rolled Steel Angle Rings 171
Example of Round Black Iron 172
Aluminum 173
Stainless Steel 175
FRP Ductwork 177
FRP Coated Galvanized Ductwork 179
Labor Multipliers for Heavy Gauge Ductwork 180
Air Pollution Estimating 180

14 Sheet Metal Specialties and Acoustical Lining 187
Access Doors, Belt Guards, Drain Pans 187
Flexible Connections, Hoods, Stands and Platforms 188
Roof Hoods 189
Turning Vanes 190
Splitter Dampers 191
Sheet Metal Housings 192
Acoustic Lining 192

15 Miscellaneous Labor Operations 195
Drafting and Sketching Labor 195
Field Measuring and Sketching Labor 196
Estimating Air Testing and Balancing 196
Estimating Ductwork Leak Testing 199

Section V —PIPING ESTIMATING
Chapter
16 Piping Estimating Basics 203
Requirements of a Profi cient Piping Estimator 203
Sample Estimate 207
17 Pressure Pipe, Fittings and Insulation 217
Pressure Piping and Fittings Tables for
Threaded, Welded, Flanged, Grooved and Associated Labor 218
Copper Tubing, L, K, K Labor and Pricing etc. 236

18 Valves and Specialties 253
Bronze #125, #150 Valves 254
Iron #125, #150 Valves 256
Specialty Valves 260
19 DWV Pipe and Fittings 271
Copper Tubing, DWV 272
PVC DWV Schedule 40 274
ABS DWV 278
Cast Iron Hub and Spigot DWV 280

Section VI—CONTRACTING FOR PROFIT
Chapter
20 Markups for Overhead and Profi t 287
Understanding and Applying Correct Overhead and Profi t Factors 287

21 Contracting for Profi t 295
What Determines Your Profi tability 295
How to Legitimately Reduce Costs on a Bid 296
Star Method of Reducing Ductwork and Piping Costs 297

22 Computerized Estimating 305


Total 318 pages 5.3 mb
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Fluid-Piping-Systems

Thursday, November 5, 2009



Content
1 1. INTRODUCTION 3
1.1 BACKGROUND 3

2 FUNDAMENTALS 4
2.1 PHYSICAL PROPERTIES OF FLUIDS 4
2.2 TYPES OF FLUID FLOW 4
2.3 PRESSURE LOSS IN PIPES 5
2.4 STANDARD PIPE DIMENSIONS 7
2.5 PRESSURE DROP IN COMPONENTS IN PIPE SYSTEMS 7
2.6 VALVES 8

3 COMPRESSED AIR PIPING 12
3.1 INTRODUCTION 12
3.2 PIPING MATERIALS 12
3.3 COMPRESSOR DISCHARGE PIPING 12
3.4 PRESSURE DROP 13
3.5 PIPING SYSTEM DESIGN 14
3.6 COMPRESSED AIR LEAKAGE 16
3.7 LEAKAGE REDUCTION 17

4 STEAM DISTRIBUTION 19
4.1 INTRODUCTION 19
4.2 ENERGY CONSIDERATIONS 19
4.3 SELECTION OF PIPE SIZE 20
4.4 PIPING INSTALLATION 23

5 WATER DISTRIBUTION SYSTEM 24
5.1 RECOMMENDED VELOCITIES 24
5.2 RECOMMENDED WATER FLOW VELOCITY ON SUCTION SIDE OF PUMP 25

6 THERMAL INSULATION 26
6.1 INTRODUCTION 26
6.2 HEAT LOSSES FROM PIPE SURFACES 27
6.3 CALCULATION OF INSULATION THICKNESS 28
6.4 INSULATION MATERIAL 29
6.5 RECOMMENDED VALUES OF COLD AND HOT INSULATION 31
6.6 ECONOMIC THICKNESS OF INSULATION 32

7 CASE STUDIES 34
7.1 PRESSURE DROP REDUCTION IN WATER PUMPING 34
7.2 PRESSURE DROP REDUCTION IN COMPRESSED AIR SYSTEM 35
7.3 REPLACEMENT OF GLOBE VALVES WITH BUTTERFLY VALVES 35
7.4 REDUCTION IN PRESSURE DROP IN THE COMPRESSED AIR NETWORK 36
7.5 THERMAL INSULATION IN STEAM DISTRIBUTION SYSTEM 37
7.6 COMPRESSED AIR LEAKAGE REDUCTION AT HEAVY ENGINEERING PLANT 37
7.7 REDUCING STEAM HEADER PRESSURE 38
ANNEXURE-1: REFERENCES 40


Total 40 pages 1.5 mb
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Pipe Hanger Design

Wednesday, October 28, 2009



CONTENTS
Design of Pipe Hangers 4
Determination of Hanger Locations 4
Hanger Load Calculations 6
Thermal Movement Calculations 11
Selection of the Proper Hangers 13
Typical Pipe Support Specification 21
Nuclear pipe Hangers 24
Seismic Supports 24
Supports for Grooved Piping 27
Application Examples 30
Weights of Piping Materials 37
Charts and Tables 63

Total 84 pages 1.4 mb

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