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Bernoulli’s Theorem

It states that in a steady state, ideal flow of an incompressible fluid, the total energy at any point of the fluid is constant.  The total energy consists of pressure energy, Kinematic energy and potential energy or datum energy.

Assumptions:
a.       The fluid is ideal, i.e. viscosity is zero
b.       The flow is steady
c.        The flow is incompressible
d.       The flow is irrotational

Bernoulli’s Equation for Real Fluid:
The Bernoulli’s equation was derived on the assumption that fluid is inviscid (non-viscous) and therefore frictionless.  But all the real fluids are viscous and hence offer resistance to flow.  Thus there are always some loses in fluid flows and hence in the application of Bernoulli’s equation, these loses have to be taken into consideration.  Thus the Bernoulli’s equation for real fluids between point 1 and 2 is given by
                p1  +  v1  +  z1  =  p2  +  v2  + z2  +  hL
                     rg        2g                    rg         2g
where hL is loss of energy between point 1 and 2.

Practical Applications of Bernoulli’s Equation:
Bernoulli’s equation is applied in all problems of incompressible fluid flow where energy considerations are involved.
  1. Venturimeter.
  2. Orifice meter
  3. Pitot-tube
Venturimeter and Orifice Meter:
Both the devices are used for measuring the rate of a flow of a fluid flowing through a pipe. 

Pitot Tube:
It is a device used for measuring the velocity of flow at any point in a pipe or a channel.

Types of Fluid Flow:


  •       Steady and unsteady flow.
  •       Uniform and non-uniform flow.
  •       Laminar and turbulent flow.
  •       Compressible and incompressible flow.
  •       Rotational and irrotational flow.
  •       One, two and three-dimensional flows.


Steady and Unsteady flow:
Steady flow is defined as that type of flow in which the fluid characteristics like velocity, pressure, density, etc. at a point do not change with time.
Unsteady flow is that type of flow, in which the velocity, pressure or density at a point changes with respect to time.

Uniform and Non-uniform flow:
Uniform flow is defined as that type of flow in which the velocity at any given time does not change with respect to space (i.e., length of direction of the flow).
Non-uniform flow is that type of flow in which the velocity at any given time changes with respect to space.

Laminar and Turbulent flow:
Laminar flow is defined as that type of flow in which the fluid particles move along well-defined paths or streamline and all the streamlines are straight and parallel.  Thus the particles move in laminas or layers gliding smoothly over the adjacent layers.  This type of flow is also called as streamline flow or viscous flow.
Turbulent flow is that type of flow in which the fluid particles move in zigzag way.  Due to the movement of fluid particles in a zigzag way, the eddies formation takes place which are responsible for high-energy loss.  For a pipe flow, the type of flow is determined by a non-dimensional number called the Reynold number.
If the Reynold number is less than 2000, the flow is laminar.  If the Reynold number is more than 4000, it is called turbulent flow.  It the Reynold number lies between 2000 and 4000, the flow may be laminar or turbulent.

Compressible and Incompressible flows:
Compressible flow is that type of flow in which the density of the fluid changes from point to point or in other words the density is not constant for the fluid.
Incompressible flow is that type of flow in which the density is constant for the fluid flow.  Liquids are generally incompressible while gases are compressible.

Rotational and Irrotational flows:
Rotational flow is that type of flow in which the fluid particles while flowing along streamlines also rotate about their own axis.
And if the fluid particles while flowing along the streamlines, do not rotate about their own axis that type of flow is called irrotational flow.

One, Two and Three-Dimensional flows:
One-dimensional flow is that type of flow in which the flow parameter such as velocity is a function of time and one space co-ordinate only.  For a steady one-dimensional flow, the velocity is a function of one-space-co-ordinate only.  The variation of velocities in other two mutually perpendicular directions is assumed negligible.
Two-dimensional flow is that type of flow in which the velocity is a function of time and two rectangle space co-ordinates.  For a steady two-dimensional flow the velocity is a function of to space co-ordinates only.  The variation of velocity in the third direction is negligible.
Three-dimensional is that type of flow in which the velocity is a function of time and three mutually perpendicular directions.  But for a steady three-dimensional flow the fluid parameters are functions of three space co-ordinates.

Types of Forces Acting in Moving Fluid

For the fluid flow problems, the forces acting on the fluid mass may be any one, or a combination of the several of the following forces:

  • Inertia force, Fi
  • Viscous force, Fv
  • Gravity force, Fg
  • Pressure force, Fp
  • Surface tension force, Fs
  • Elastic force, Fe

Inertia Force (Fi):
It is equal to the product of mass and acceleration of the flowing fluid and acts in the direction opposite to the direction of acceleration. It always exists in the fluid flow problems.

Viscous Force (Fv):
It is equal to the product of shear stress due to viscosity and surface area of the flow. It is present in fluid flow problems where viscosity is having an important role to play.

Gravity Force (Fg):
It is equal to the product of mass and acceleration due to gravity of the flowing fluid. It is present in case of open surface flow.

Pressure Force (Fp):
It is equal to the product of pressure intensity and cross sectional area of the flowing fluid. It is present in case of pipe flow.

Surface Tension Force (Fs):
It is equal to the product of surface tension and length of surface or flowing fluid.

Elastic Force (Fe):
It is equal to the product of elastic stress and area of the flowing fluid.

- For a flowing fluid, all the above forces may not always be present. And also the forces, which are present in a fluid flow problem, are not of equal magnitude. There are always one or two forces, which dominate the other forces. These dominating forces govern the flow of fluid.

Abbrevation : Piping

ADCP

Acoustic Doppler Current Profiler

AGA

American Gas Association

AISI

American Iron and Steel Institute

ALARP

As Low As Reasonably Practicable

ALS

Accidental Limit State or Accidental Load Situation

API

American Petroleum Institute

ASD

Allowable Stress Design

ASM

American Society of Metals

ASME

American Society of Mechanical Engineers

ASTM

American Society for Testing and Materials

BOP

Blow Out Preventer

BS

British Standard

CAPEX

Capital Cost

CBV

Cost Benefit Value

CEN

Centre Européen de Normalisation

CEV

Carbon Equivalent

CIV

Corrected Inherent Viscosity

COE

C-bending, O-pressing, Expansion

CP

Centre Point, Cathodic Protection

CPT

Cone Penetrometer Testing

CRA

Corrosion Resistant Alloy

CTOD

Crack Tip Opening Displacement

CSA

Canadian Standards Association

DEH

Direct Electrical Heating

DFI

Design, Fabrication and Installation

DFO

Documents For Operation

DFT

Dry Film Thickness

DIN

Deutscher Institut für Normung

DNV

Det Norske Veritas

DONG

Dansk Olie og Naturgas

DP

Dynamic Positioning

DS

Dansk Standard

DWT

Dead Weight Tonnage

DWTT

Drop Weight Tear Test

ECA

Engineering Criticality Assessment

EEZ

Exclusive Economic Zone

EFC

European Federation of Corrosion

EIA

Environmental Impact Assessment

EN

Euro Norm

ENV

European Pre-Standard (draft EN)

ESD

Emergency Shut Down (valve)

EU

European Union

FAR

Fatal Accident Rate

FBE

Fusion Bonded Epoxy

FEM

Finite Element Method

FLS

Fatigue Limit State

FMEA

Failure Mode Effect Analysis

FPS

Floating Production System

FPSO

Floating Production, Storage and Offloading

FRP

Fibre Reinforced Polymer

GA

General Arrangement (drawing)

GIS

Geographical Information System

GL

Germanischer Lloyd

GMAW

Gas Metal Arc Welding

GPS

Global Positioning System

GPTC

Gas Piping Technology Committee

HAZ

Heat Affected Zone

HAZID

Hazard Identification

HAZOP

Hazard and Operability (study)

HD-

High Density (e.g. HDPE, HDPU)

HDD

Horizontal Directional Drilling

HFW

High Frequency Welding

HIC

Hydrogen Induced Cracking

HIP

Hot Isostatic Pressing

HIPPS

High Integrity Pressure Protection System

HP/HT

High Pressure/High Temperature

HSE

Health, Safety and Environmental Protection

ID

Internal Diameter (pipe bore)

IEC

International Electrotechnical Commission

IP

Intersection Point

ISO

International Standardisation Organisation

ISO/DIS

Draft International (ISO) Standard

KP

Kilometre Post

LAT

Lowest Astronomical Tide

LCI

Life Cycle Information

LI

Liquidity Index

LL

Liquid Limit

LRFD

Load and Resistance Factor Design

MAIP

Maximum Allowable Incidental Pressure

MAOP

Maximum Allowable Operating Pressure

MBR

Minimum Bending Radius

MD

Medium Density (e.g. MDPE)

MEG

Methyl Ethyl Glycol/Mono Ethylene Glycol

MPI

Magnetic Particle Inspection

MSL

Mean Sea Level

MTO

Material Take-Off

NACE

National Association of Corrosion Engineers (USA)

NDE/NDT

Non-Destructive Examination/Non-Destructive Testing

NGL

Natural Gas Liquids

NKT

Nordisk Kabel og Tråd

NORSOK

Norsk Sokkels konkuranseposisjon (competitive standing of the

Norwegian offshore sector)

NPV

Net Present Value

OD

Outer Diameter

OPEX

Operational Cost

OREDA

Offshore Reliability Data

OS

Offshore Standard

P&ID

Process and Instrumentation Diagram

PA

Polyamide

PD

Published Document

PE

Polyethylene

PI

Plasticity Index

PL

Plastic Limit

PP

Polypropylene

PRCI

Pipeline Research Council International, Inc.

prEN

European Pre-Standard

PSD

Process Shut Down (valve)

PSV

Pressure Safety (relief) Valve

PU

Polyurethane

PVC

Poly Vinyl Chloride

PVDF

Polyvinylidene Fluoride

QA/QC

Quality Assurance/Quality Control

QRA

Quantified Risk Analysis

REM

Rare Earth Materials

RFO

Ready For Operation

ROV

Remotely Operated Vehicle

RP

Recommended Practice

RTS

ROV-operated Tie-in System

S

Seamless (pipe)

SAR

Synthetic Aperture Radar

SAW

Submerged-Arc Welding

SAWH

Submerged-Arc Welding Helical

SAWL

Submerged-Arc Welding Longitudinal

SCADA

Supervision, Control and Data Acquisition

SCF

Stress Concentration Factor

SI

Système Internationale/International System for Units

SLOR

Single Line Offset Riser

SLS

Serviceability Limit State

SMAW

Shielded Metal Arc Welding

SMSS

Super Martensitic Stainless Steel

SML

Seamless (pipe)

SMTS

Specified Minimum Tensile Strength

SMYS

Specified Minimum Yield Stress

SOHIC

Stress Oriented Hydrogen Induced Cracking

SRB

Sulphate Reducing Bacteria

SSC

Sulphide Stress Cracking

SSIV

Subsea Safety Isolation Valve

SWC

Stepwise Cracking

SZC

Soft Zone Cracking

TEG

Tri-Ethylene Glycol

TLP

Tension Leg Platform

TFL

Through Flowline

TMCP

Thermo-Mechanical Controlled Processing

TP

Tangent Point

TÜV

Technische Überwachungs Verein

ULS

Ultimate Limit State

UNECE

United Nations Economic Commission for Europe

UNS

Unified Numbering System

UOE

U-shaping, O-pressing, Expansion

UTC

Unit Transportation Cost

UV

Ultraviolet (radiation)

VIV

Vortex Induced Vibrations

WBC

Wet Buckle Contingency

WBS

Work Breakdown Structure

WC

Water Content

WT

Wall Thickness (steel)

XLPE

Cross-linked Polyethylene

3-RF

3-Roller Forming (7.2.4)

Valves Abbrevation

Abbreviations List:

AISI = American Iron and Steel Institute

AL = Aluminium

ANSI = American National Standard Institute

API = American Petroleum Institute

ASME = American Society of Mechanical Engineers

ASTM = American Society for Testing Materials

AWS = American Welding Society

AWWA = American Water Works Association

BB = Bolted Bonnet

BC = Bolted Cap or Bolted Cover

BR = Bronze

BS = British Standard

BSPP = British Standard Pipe Thread,Parallel

BSPT = British Standard Pipe Thread,Taper

BUNA = Nitrile Rubber

BW = Butt Welding Ends

CFM = Cubic Feet per Minute

CI = Cast Iron

CR = Chloroprene or Neoprene

CS = Carbon Steel

CWP = Cold Working Pressure

DIN = Deutschen Industrie Norm

DN = Diameter Nominal

EPDM = Ethylene Popylene Diene Monomer

EPT = Ethylene-Propylene Ter Polymer

FE = Flanged Ends

FEP = Fluorinated Ethylene Propylene

FF = Flat Face

Fig.No. = Figure Number

FLG = Flanged

FNPT = Female National Pipe Taper

FPM = Fluorinated Ethylene Propylene

FS = Forged Steel

GPM = Gallons per Minute

GR = Grade

HF = (Hard Face)Stellite Face

IBBM = Iron Body Bronze Mounted

IN = Inch

IPM = Inches per Minute

ISRS = Inside Screw Rising Stem

Max. = Maximum

MI = Malleable Iron

Min = Minimum

MSS = Manufacturers Standardization Society

NACE = National Association of Corrosion Engineers

NBR = Nitrile or Buna N Rubber

NC = Normally Closed

NDT = Non Destructive Testing

Nod.CI = Nodular Cast Iron

NPS = Nominal Pipe Size

NPT = National Pipe Thread

NRS = Non Rising Stem

NYL = Nylon

OD = Outside Diameter

OS&Y = Outside Screw and Yoke

PCD = Pitch Circle Diameter

PE = Polyethylene

PMI = Positive Material Identification

PP = Polypropylene

PSI = Pounds Per Square Inch

PSIA = Pounds Per Square Inch Absolute

PSIG = Pounds per Square Inch Gauge

PTFE = Poly Tetra Fluoro ethylene

PVC = Polyvinyl Chloride

RF = Raised Face

Rilsan = Super Polyamide

RPM = Revolution per Minute

RS = Rising Stem

RTJ = Ring Type Joint

SAE = Society of Automotive Engineers

SB = Screw Bonnet

Scr = Screwed

SE = Screwed ends

SJ = Scolder Ends

SS = Stainless Steel

STL = Stellite

SW = Socket Welding Ends

TFE = Tetra Fluoro Ethylene

VITON = Fluorinated Elastomer

WB = Welded Bonnet

WOG = Water, OIL, Gas

WP = Working Pressure