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Piping Design and Analysis Seminar (Feb 17-20, 2009)
 
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November 13, 2007

Temperature Conditions for Piping Stress Analysis Consideration

Before you start piping stress calculation, you have to refer to line index ( or called the line classification lists or process line lists) to check design temperature and an operating temperature for line to be checked.Stress analysis shall be carried out on the basis of the design temperature.

Secondly, you have to know requirements base on your project specification such as

Minimum Ambient Temperature. ( TAMIN )

Maximum Ambient Temperature. ( TAMAX )

Maximum Solar Radiation Temperature. ( TS )

Site Installation Temperature. (TAs )

 

We will use value below in our piping stress analysis tutorials:

 

TAMIN = 16°C ( For Stress Range Purpose, in case hot lines)

TAMAX = 36°C ( For Stress Range Purpose , incase cold lines )

TS = 70°C

TAs = 21°C

Line design temperature shall be taken from process line lists ( or line index).

 

In case plus design temperatures <70°C , 70°C will be taken as design temperature

 

Example 1:

 

Line design temperature as per line index is 65°C so we will take 70°C as design temperature for stress calculation

TAMIN = 16°C ( For Stress Range Purpose )

TAs = 21°C

 

Example 2:

Line design temperature as per line index is -250°C so we will take -250°C as design temperature for stress calculation

TAMAX = 36°C ( For Stress Range Purpose with )

TAs = 21°C

 

Noted:

TAMIN= 16°C in example 1 ( for hot line) and TAMAX = 36°C in example 2 ( for cold line)
You have to find Minimum Ambient Temperature, Maximum Ambient Temperature, Maximum Solar Radiation Temperature, Site Installation Temperature in your project specifications

 

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November 15, 2007

Dual Plate Check Valves

Dual Plate Check valve is a type of non-slam check valves used to protect the equipment near it in an event of a backflow

or a change in flow rate (water hammer).  This has two semicircular plate-shaped discs attached to a central hinge pin located

in the valve body.  The disc plates are acted upon by one or more torsion springs mounted on the hinge springs.  Dual Plate

Check valves have minimum weight and compact design for lighter pipe work system suitable for installation for vertical

pipelines.

HERE ARE TYPICAL INFORMATION TO VENDOR
1. Item Number
2. Quantity
3. Size
4. Weep Hole diameter
5. Connection (Flange Rating)
6. Valve Materials
* Body
* Trim
* spring
* Gasket
7. Fluid
8. Design Condition
* Pressure
* Temperature
7. Operating Condition
* Pressure
* Temperature
* Flow Rate
* Density
* Viscosity
* Mounting Position
* Maximum Allowable Pressure Drop
* Hydrostatic Test Pressure
8. Location
* Line No.
* Equipment No.
* Line Class
SOME DUAL PLATE CHECK VALVES VENDORS
1. Crane Valve Group        http://www.cranevalve.com
2. Goodwin International Ltd. http://www.energyweb.net
3. Mueller Steam Specialty        http://www.fluidcontrolinstitute.org
   http//www.ustpvf.com
4. Tyco Valves & Control       http://hydeburnett.co.uk   

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Flame Arresters

A flame arrester serves as a safety device installed to pipelines transporting flammable or explosive gases or vapor.  In an event of an ignition of these materials, damage to lives and property can be minimized by installing flame arrester in-line or at the end of a piping system.  The flame arrester puts off the flame as it enters thru it by reducing the temperature of the flame below the auto-ignition point of the gas.

HERE ARE TYPICAL INFORMATION TO VENDOR

1. Type
2. Size & Connection (Flange Rating)
3. Fluid
4. Design Condition
* Pressure
* Temperature
5. Operating Condition
* Pressure
* Temperature
* Flow Rate
* Density
* Max. Allowable Pressure Drop
6. Materials
* Body
* Internal
7. Additional Requirements
* Test Pressure
* Corrosion Allowance
* Heat Treatment
* Installation Orientation
8. Location
* Line No.
* Line Class
9. Service Category

SOME FLAME ARRESTERS VENDORS

1. IMI Amal
2. Kaneko
3. Knitmesh
4. Niikura

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Steam Trap and Drain Trap

A steam trap serves as an automatic valve, which removes the hot condensate, a byproduct of the heat transfer between the steam and the fluid to be heated in a steam system.  The hot condensate is returned to the boiler to conserve its available heat.  Likewise, it is also important to remove the condensate from the heat system because if left at the bottom of a system, it reduces the efficiency of the heat transfer and it can cause several types of water hammer and thus, damage the pipe system.  Steam traps also remove air and other non-condensable gases as they reduce the efficiency of the heat transfer.  Other gases like CO2 and O2 have to be kept out of the system as well because they react to form the corrosive carbonic acid.  Steam traps open to release condensate, air and CO2 but close to keep the steam in.

    A drain trap serves as an automatic loss prevention valve.  Water or moisture may be carried with the air being used in machinery or some tools.  Presence of these elements is unwanted because it washes away the lubricating oil within these machines, accelerating wear and tear.  In instrument air systems, water can collect dirt causing sensitive instruments to fail.  In compressed air systems, excess moisture and oil tend to decrease the efficiency of the gaskets and hoses.  Removing water, moisture or oil may be done manually or using a drain trap.  A drain trap opens to discharge fluids and closes to prevent air and gas loss.

HERE ARE TYPICAL INFORMATION TO VENDOR
 (SAME FOR BOTH)

1. Item No.
2. Quantity
3. Type
4. Size & Connection (Flange Rating)
5. Fluid
6. Design Conditions
* Upstream Work Pressure
* Temperature
7. Operating Conditions
* Upstream Work Pressure
* Downstream Work Pressure
* Temperature
* Flow Rate
5. Materials
* Body
* Trim
6. Heat Treatment
7. Accessories
* Strainer
8. Installation
9. Location
* Equipment No.
* Line No.
* Line Class

SOME STEAM TRAP AND DRAIN TRAP VENDORS

1. TLV Co.            http://www.tlv.com
2. Nippon Keystone  - 
3. Spirax Sarco Ltd.        http://www.spirax-sarco.com.au
4. Armstrong         http://www.armintl.com
5. Miyawaki Inc.        http://www.miyawaki.net
6. Velan Engineering

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Strainers

A strainer is a device used to provide a mechanical means of removing solids from a flowing liquid or gas by using a barrier.

Strainers are classified into three categories:

(1) Simplex
A strainer consisting of a single element chamber that normally requires the flow through the unit to be shutdown before cleaning.

Conical Strainer  -    serves as temporary strainer for temporary installation during the commissioning, or start up service for the efficient removal of solids/debris for the protection of Fluid and Gas handling equipment from damage.  This can be installed either vertically or horizontally.  Also, it can be manufacture using any kind of wire mesh or perforated plate, in carbon steel and stainless steel or in alloys.
        

Y”-Type Strainer  -     economical method of protecting the pipeline equipment by removing solids/debris from flowing liquid or gas.     
        
        
T-Type Strainer  -    fabricated to satisfy any filtration requirements and provide a very high filtering area, therefore ensuring a very low pressure drops.
               

Bucket Type Strainer  -    Simple and efficient method of protecting the vital pipeline equipment by removing of solids/debris and reducing expensive plant maintenance.          
     
    
(2) Duplex or Multiplex
A strainer usually consisting of at least two elements chambers separated by a valve that permits continuous flow of fluid through one chamber while the other is accessible for cleaning.

(3) Automatic (Self Cleaning)
A strainer providing some means of back flushing or cleaning of the straining element while the unit is in service.
   
HERE ARE TYPICAL INFORMATION TO VENDOR

1. Item Number
2. Type
3. Size
4. Quantity
5. Connection
* Screwed
* Socket weld
* Flange
6. Fluid
7. Design Condition
* Pressure
* Temperature
8. Operating Condition
* Pressure
* Temperature
* Specific Gravity
* Viscosity
9. Materials
* Body
* Perforated PLATE
* Screen
* Screen Mesh
* Diameter of Wire
10. Location
* Line No.
* Line Class
11. Remarks

SOME STRAINERS VENDORS

1. Douglas Italia S.p.a         http://www.douglas-chero.com
2. Vee Bee Limited            http://www.veebee.co.uk/
3. Koyo Seisakusho Co. Ltd.
4. Plenty Filters            http://www.plenty.co.uk
5. Spirax Sarco Inc.            http://www.spirax-sarco.com.au
6. YAC Filter Systems Corp.
7. Mueller Steam Specialty
8. BP Flow Equipment

 

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November 16, 2007

Piping Technical Questionnaire Part 1

Piping Technical Questionnaire Part 1

1. Write your  answers for definition or describe of following piping related design deliverables or documents listed
  

1.1   Key Plan

1.2   Plot Plan

1.3   Piping Arrangement or Layout

1.4   Piping Plan Drawing
 
1.5   Piping Isometric Drawing

1.6   Piping Information

1.7   Pipe Rack

1.8   Pipe Sleeper

1.9   Tie-in List

1.10 BM (Bill of Material)

1.11 BQ (Bill of Quantities)

1.12 Material Take-Off

1.13 Requisition

1.14 Piping Material Specification

1.15 Piping Bulk Materials

1.16 Piping General Specification

1.17 PFD (Process Flow Diagram)

1.18 P&ID (Piping and Instrument Diagram)

1.19 UFD (Utility Flow Diagram)

1.20 Model Review

1.21 Equipment Engineering (Equipment Skeleton)
    
1.22 Vendor Drawing

1.23 Data Sheet

1.24 Instrument Data Sheet

1.25 Engineering Schedule

1.26 General Project Schedule

1.27 Scope of Project

1.28 Job Code
      

1.29 Standard Drawing

1.30 Standard Support Drawing

1.31 Special Support Drawing

1.32 Steam Trace Drawing

1.33 Client Specificatione.

1.34 Client Standard Drawing

1.35 Client Existing Drawing

1.36 Demolition Drawing

1.37 Conceptual Layout

1.38 Clarification List

1.39 Deviation List

1.40 Document Master List

1.41 Information List

1.42 Line Index

1.43 Line Numbers

1.44 Line Class

1.45 Installation Level

1.46 NPIC (Notification of P&ID Change)

1.47 NPPC (Notification of Plot Plan Change)

1.48 NPMC (Notification of Piping Material Change)

1.49 Basic Design Data

1.50 Basic Engineering Design Data

1.51 Design Basis

1.52 Detail Engineering Design Data
   
1.53 Design Pressure

1.54 Design Temperature

1.55 Dimension Table

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OVERVIEW OF PIPING LAYOUT


1 What is Piping Layout? (Purpose of Piping Layout)

To determine the following:

a. Equipment Layout
b. Construction & Structure (configuration & elevation)
c. Equipment (vessel) nozzle orientation, platform, lug & ladder (location & configuration)
d. Piping Arrangement (line routing, location of piping component & instrument)
e. Electrical/ Instrument cable layout, location local panel, junction boxer lighting, etc.
f. Location of buried piping & drip funnels.

2 Related Work for Piping Layout

a. Plot Plan Preparation
b. Design Info Preparation
c. Piping Strength Analysis
d. Piping Material Take-off
e. Piping Drawing Preparation

3 Data Gathering & Verification

a. Collect necessary Documents
b. Verify Accuracy

4 Preparation of Basic Piping Layout Plan

a. Piping Conceptual Routing
b. Equipment Layout
c. Civil/Structure Formation
d. Valve & Instrument Assembly
e. Electrical/Instrument Cable Routing
f. Fire Escape Routes/ Maintenance Area

5 Preparation of Breakdown of Piping Layout

a. By Facilities
b. By Section of Facilities
c. By Structure
d. By Unit

6 Determination of Area of Priority

a. Tight Schedule for Design Info. Issuance
b. Some connection with other company (Hook-Up)
c. Plot Plan to Fix Early
d. Complete Set of Documents
e. Having Lines w/ High Temperature: High Pressure (material to be use is high Grade (special) material & Large Size)
f. Piping Material to be Ordered Early

7 Preparation of Piping Layout

7.1 Piping Design Input Data   (Before layout preparation)

a. Plot Plan
b. Process Flow Diagram, Piping & Instrument Diagram & Utility Flow Diagram
c. Line Index
d. Client Standard
e. Piping Material Specification (line classes)
f. Equipment Skeleton Drawing (Pressure vessel except H/E)   
g. Piping General Specifications
h. Standard Drawing (standard pipe support, max. supporting span, & typical detail
i. Existing Job Ref. Vendor Catalog (pump/comp.)
j. Instrument Data Sheet Dwg & Catalog
k. Data Sheet (H/E)
l. Vendor Catalog/ Existing Job Ref.
m. Layout Procedure

7.2 Piping Design Input Data   (During layout preparation)

7.2.1 Supplied from instrument department

a. Cable Routing (main/ pipe rack/sub pipe rack & sleeper)
b. Vendor Drawings
c. Tie-in Dimension List
d. Air Supply Tapping Point
e. Piping/Instrument Split of Work

7.2.2 Supplied from Electrical Department

> Cable Routing (main/ pipe rack/sub pipe rack & sleeper)

7.2.3 Supplied from Fire Fighting Section

a. P & ID
b. General Arrangement
c. Typical Detail (Hydrant; monitor)
d. Vendor Drawings

7.2.4 Supplied from Package Department

a. Package Equipment Vendor Drawing
b. Package P & ID

7.2.5 Supplied from Piping Department

a. Piping Special Component Vendor Drawing
b. LC/LG Arrangement

7.2.6 Supplied from Civil Department

> Site Grading Plan

7.3 Piping Design Output Data   (During layout preparation)

7.3.1 Supply to Equipment Department

a. Equipment Installation Height
b. Nozzle Orientation
c. Platform & Ladder
d. Support Lug
e. LG/LC Arrangement
f. Nozzle Force & Moment

7.3.2 Supply to Civil/ Structural Department

a. Equipment Installation Height
b. Pipe Rack
c. Structure
d. Table Top
e. Sleeper
f. Pump Foundation
g. Pipe Support
h. Drip Funnel Location
i. Operating Platform (Misc.)
j. Pipe Trench
k. Embedded Plate
l. U/G Pressure Piping Layout
m. Spill Wall
n. Pit Information
o. Pit Support Foundation Location

7.3.3 Supply to Instrument Department

a. LG/Visual Direction
b. LC Visual Direction
c. CV Direction

7.3.4 Supply to Furnace (Optional)

a. Platform & Stair or Ladder
b. Pipe Support
c. Burner Orientation

7.3.5 Supply to Package Equipment (Optional)

> Package Unit Orientation

7.3.6 Supply to Rotary

> Rotary Machine Orientation

7.4 Piping Design Output Data   (After layout preparation)

> Final Piping Layout

8 Checking of Piping Layout

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OVERVIEW OF PLOT PLANNING


1 What is Plot Plan?

> Is a drawing which express complete configuration of unit or plant by showing equipment layout & structure planning.
> Is one of the most important basic design documents for detail design engineering.

2 What is the “Function of Plot Plan?

2.1 Piping Design
2.2 Civil Engineering
2.3 Electrical Engineering
2.4 Instrument Engineering
2.5 Process/ System Engineering
2.6 Scheduling
2.7 Construction
2.8 Client

3 Functions of Plot Plan:

3.1 Piping Design:

> To produce equipment arrangement studies that facilitate the interconnection of above & underground process/ utility piping.
> To estimate piping material quantity

3.2 Civil Engineering:
 
> To develop grading & drainage plan, holding ponds, diked areas, foundation & structural design & material estimate.   

3.3 Electrical Engineering:
 
> To produce area classification drawings, locate switchgear; substation & motor control center; cable route & material estimate.

3.4 Instrument Engineering:

> To locate analyzer houses & cable trays, assist     in the location of main control house & material estimate.

3.5 Process/ System Engineering:

> To facilitate hydraulic design, line sizing &     utility block flow diagram.

3.6 Estimations:

> To estimate the overall cost of the plant.

3.7 Construction:
                 
> To schedule the erection sequence of all plant equipment, rigging studies for large lift, constructability review, marshaling, & lay down areas throughout the entire construction phase.

3.8 Client:
   
> To safety, operator & maintenance reviews & develop as-built record of plant arrangement.

4  “Required Document/ Data” for Plot Planning:

4.1 Space of Unit Area
4.2 Process Flow Diagram (PFD)
4.3 Utility Flow Diagram (UFD)
4.4 Proposal Plot Plan (from ITB Document)
4.5 Skeleton drawing of equipment showing dimension & configuration
4.6 Data Sheet of H/E, Tank, etc.
4.7 Applicable Code & Standard (Local & Int’l)
4.8 Applicable Laws & Regulations
4.9 Basic Engineering Design Data (BEDD)

5 Steps of Preparation of plot Plan:

5.1 Preparation of Preliminary Plot Plan

> Preliminary equipment layout or arrangement
> Preliminary arrangement of structures, building & other facilities

5.2 Study on Preliminary Plot Plan

> Study on safety instances
> Study on pipe rack width
> Study on routing for main piping & cables
> Study on construction & maintainability
> Study on operation accessibility & operability
> Study on underground obstruction

5.3 Completion of Plot Plan

> Determination of dimension between equipment, structures and etc.
> Modification as a result of piping layout

6 Basic Consideration of Plot Planning:

6.1 General

a. Construction & Maintenance
b. Access & Ease Operation
c. Safety & Prevention of the Spread of Fire
d. Economical Design & Future Expansion

6.2 Blocking

The plant site shall be formed by block in consideration of hazard attendant to plant operation.

a. Process Area
b. Storage Area
c. Utilities Area
d. Administrative & Service Area
e. Other Areas such as:

> Loading & unloading area
> Flare & burnt pit area
> Waste water treatment area or effluent treatment area

6.3 Terrain & Weather

a. Terrain

> Contour
> Land Profile
> Area Physical Character   

b. Weather: Climatic condition such as:

> Stormy weather
> Seasons
> Seismic condition

6.4 Prevailing Wind

Some equipment/ Facilities shall be laid/ mounted on the following wind direction:

a. Windward direction
b. Upwind direction

6.5 Classification of Hazard

The plant layout shall be determined in consideration of classified hazardous area:

a. Classification of location for Electrical Installation in Petroleum Refineries API-RP-500A
b. Area Classification

6.6 Maintenance Space

> Sufficient space shall be provided of maintenance of the facilities.

6.7 Future Expansion

> Shall take into consideration for future expansion.

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DESIGN INTERFACE AMONG DISCIPLINES

HERE ARE DESIGN INTERFACE AMONG DISCIPLINES

1 CIVIL DEPARTMENT

1.1 Information to Civil

a.  Equipment Installation Height
b.  Pipe rack/Structure/Tabletop
c.  Sleeper
d.  Foundation Installation Height
e.  Pipe Support
f.  Drip Funnel Location
g.  Platforms
h.  Pipe Trench
i.  U/G Pressure Piping
j.  Embedded Plate
k.  Plot Plan
l.  Layout/Arrangement in 3D Model

1.2 Information from Civil

a.  Design Drawings

2 MECHANICAL DEP’T

2.1 Information to Mechanical
 
a. Equipment Installation Height
b. Nozzle Orientation
c. Platform & Ladder
d. Lug Support
e. LC/LG Arrangement
f. Nozzle Force & Moment

2.2 Information from Mechanical
 
a. Vendor Catalog
b. Mechanical Data Sheet
c. Engineering Drawing
d. Vendor Drawings
3 INSTRUMENT DEP’T

3.1 Information to Instrument

a. Plot Plan
b. Layout/Arrangement in 3D Model

3.2 Information from Instrument
 
a. Cable Routing
b. Data Sheet, Drawing and Catalog
c. In-line Instrument Dimension
d. Air Supply Connection
e. Design Drawings
f. LC/LG Requirement
4 PROCESS DEPARTMENT

4.1 Information to Process
 
a. UFD Draft for Hose Station
b. Marked-up UFD
c. Hydraulic Sketch

4.2 Information from Process

a. Datasheets for Special Components
b. Line Index
c. P&ID

5 PACKAGE SECTION

5.1 Information to Package

a. Plot Plan

5.2 Information from Package
 
a. Special Equipment Vendor Dwg
b. Package Equipment Vendor Dwg
6 ELECTRICAL DEP’T

6.1 Information to Electrical

a. Plot Plan
b. Layout/Arrangement in 3D Model

6.2 Information from Electrical
 
a. Cable Routing
b. Lighting System Typical Drawing
c. Design Drawings
7 FIRE PROTECTION 

7.1 Information to Fire Protection
 
a. Plot Plan
b. Piping Layout

7.2 Information from Fire Protection
 
a. Fire Fighting P&ID
b. General Arrangement
c. Typical Detail Arrangement
d. Fire Equipment Vendor Drawing

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November 17, 2007

Unit Conversions 2000

Unit Conversions 2000 is a small utility that will allow you to quickly convert units of measure from one system to another.

Facilities are included to convert various Lengths, Weights, Volumes, Areas, Density, Power and Scale measurements.

Unit Conversions 2000

  Requires MS Windows 95/98, ME, XP, Vista, 2000 or Windows NT
  Download Download  UCONVERT.ZIP (169K Bytes)
  Updated May 22nd, 2005
  Installation Unzip to a temporary directory and run SETUP.EXE
  Price Free
  Source http://www.gregorybraun.com/uConvert.html
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