Monday, December 29, 2014

[EXCEL] How to Design Entrainment Separation Vessels / Gravity Deacanter

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A Knockout drum with a mist eliminator is common whenever a process requires entrained droplets to be separated from a vapor stream. A simple knockout drum (no mist eliminator) will remove droplets larger than about 380 microns by gravity settling M. generally gravity settling removes more than 90% of the liquid entering the vessel .However the remaining droplets smaller than 380 microns can be a significant problem for a downstream unit. A mist eliminator in the top of the knockout drum will remove the remaining droplets down to a diameter of 6 microns or less, depending on the type of mist eliminator. A knockout drum with mist eliminator can achieve an overall efficiency of 99.99% liquid removal.

Knockout Drum Configurations

Knockout drums may be oriented vertically or horizontally. In both types, the mist eliminator may also be oriented vertically or horizontally. For a vertical mist eliminator (horizontal vapor flow), the drainage flow is cross-current, whereas for vertical upflow the drainage flow is counter-current. Because cross-current flow results in less liquid holdup, a vertical mist eliminator can be operated at a higher vapor loading without reentrainment (depending on the liquid load and on the height).

A horizontal entrainment separation vessel can also be designed to operate as a droplet coalesce. In this case, the mist eliminator operates beyond the reentrainment load. Large, coalesced droplets blow off the down stream side of the mist eliminator and either settle by gravity or are collected by a vane type mist eliminator.

Monday, December 22, 2014

[EXCEL FILE] Heavy Oil Programs Worksheet (51 Sheets)

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Heavy Oil Programs Worksheet (51 Sheets)

Program Description

0 Conversion Factors

1 API - Determines oil API, density and molecular weight at any temperature

2 Water Properties: Density and thermal properties of water

3 Thermal Properties: Heat capacity, thermal conductivity and diffusivity of fluid saturated rocks/and liquids

4 Viscosity of Liquid Mixtures & Emulsions

Tuesday, December 16, 2014

An Introduction to Block Flow Diagram (BFD)

1 Comment
A Block Flow Diagram - BFD, is a schematic illustration of the major process.The block or rectangles used represent a unit operation. The blocks are connected by straight lines which represent the process flow streams which flow between the units. These process flow streams may be mixtures of liquids, gases and solids flowing in pipes or ducts, or solids.


Thursday, December 11, 2014

An introduction to Pipe & Tube Classification

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Pipe classification:

Iron pipe size (approximate internal dia.)

Manufacturers’ weight: NPS +

  • STD
  • XS
  • XXS


Monday, November 24, 2014

General Guidelines for Ladders and Platforms

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Types of Ladders

1)    Step Through
2)    Side Step
3)    Straight/vertical Ladder
4)    Inclined

General Guidelines
·        Platforms are provided for access to manholes, instruments, valves and equipment, and for crossovers between ladders.

Wednesday, November 12, 2014

Mott MacDonald Chennai HR Email and Company Address

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Mott MacDonald Chennai HR Email and Company Address

Company Name
Mott MacDonald Pvt Ltd
Domain Expertise
EPC - INFRASTRUCTURE
City
Chennai
Country
India
Name of HR Manager
Mrs. Malathy .T
Phone/Mobile
00914430680212
Email
malathi.tamizh@mottmac-india.com
Website
www.mottmac-india.com

Monday, November 10, 2014

General Guidelines of Pump Piping Layout

2 Comments

General Guidelines

Following sketch (sketch-1) shows a portion of a typical plot plan with few Equipment's, pipe rack etc shown. For equipment spacing pl refer, plant layout and piping specification number P-GS-PL-003, GE Gap guidelines, and/or OISD 118.

Thursday, October 30, 2014

Commonly Used Waterworks Pipes and Fittings

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The functions of some commonly used waterworks pipes and fittings are described below:-

Wednesday, October 15, 2014

Comparison of ANSI and API Pump Designs

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Comparison of ANSI and API Pump Designs


General Considerations for Steam Piping

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General Design Considerations

• Piping shall be designed for complete condensate removal. Drip legs complete with steam traps shall be provided at all low points, at the base of a vertical risers, at dead-ends, and on long runs at intervals.


Wednesday, September 24, 2014

Why There is a Need For Pipe Supporting?

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The Piping Profile in general can be considered as a complex and rigid piping network consisting of various piping components, which have different diameters and weights. At the same time the above network is also subjected to temperature change while switching from installed to operating condition (and visa versa) resulting into its thermal growth in various directions in proportion to the length of pipes. The structural integrity of the above network must therefore take into account the overall weight effect of the profile besides its thermal growth. 

A satisfactory design of the Piping System should therefore give a careful consideration to achieve the above requirement. This is generally accomplished by providing external attachments (known as pipe supports) at various locations of the piping profile. 

Tuesday, September 16, 2014

[PPT] Under Ground Piping (Trench, Culvert, Buried)

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Types of Under Ground Piping:

Ø Trench Piping

Ø Culvert Piping

Ø Buried Piping


Sunday, September 14, 2014

[PPT] Accessibility Factors - Human Factor Guide Line

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Ø If height of ladder is more than 2.1m then ladder should be provided with safety loop.

Ø Ladder step interval should not be more than 300mm.

Ø Provide at least main height clearance from over head beam.

Ø Stair way slope from horizontal should be in range 45 to 60 degree.

Thursday, September 11, 2014

[PPT] Yard and Rack Area Piping

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Yard area piping: Piping out side power block is known as yard area Piping.

Yard area piping can be divided in two parts
Ø Above Ground
Ø Under Ground

In above ground piping following topic will be covered
Ø Rack Piping
Ø Sleeper Piping
Ø Clearance
Ø Human factor guide line

Tuesday, September 9, 2014

[PPT] General Pipe Routing Criteria

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General Pipe Routing Criteria

There are some criteria that optimize piping cost and proper functioning of system.

Ø Piping from source to destination should be as short as possible with minimum change in direction.

Ø Piping should not hinder any normal passage way also should not encroach any equipment maintenance space.

Sunday, August 31, 2014

[PPT] Basics of Pump Piping

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The Pump Should Be Located As Close As Possible To The Source Of Suction.

The Main Reason For This Is To Minimize Pressure Drop. This Keeps Line Sizes And Equipment Elevations To A Minimum Due To Support Availability.

Thursday, August 21, 2014

[PDF FILE] Introduction to Piping Engineering

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Here's a presentation on piping engineering in PDF format, now available for all. This presentation covers the basics points of piping, which are meant for those persons who are first time entering our EPC industry. This presentation covers various aspects of piping engineering like:

Wednesday, August 13, 2014

[Excel File] A Guide of Refinery Process

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This excel file (A Guide of Refinery Process) is indeed a great resource for learning basics of the whole refining process from crude oil to processed product like Gasoline or Diesel. I am sharing this to all readers for educational purpose. Please do share the link of this article with you friends and colleagues, so that they may also benefit from it. Download it and then view it as it's an interlinked file and cannot be viewed properly online.

 at One drive

Alternate: A Guide of Refinery Process.xls

Sharing is Caring...

Tuesday, July 8, 2014

Pressure Relief Valve Piping Design

4 Comments
Block valves are usually provided upstream (and downstream if discharging into a closed system) of pressure relief valves where necessary to permit on stream isolation and maintenance of the PR devices without interrupting process unit operations.

Where block valves are used, the installation should conform to the requirements of Section VIII of the ASME Boiler and Pressure Vessel Code when protecting an unfired pressure vessel. These valves are typically installed so that they are car sealed open (CSO). Mechanical interlocks or key systems are usually required for spared PR valve installations to help ensure continuous safety protection of the system.

Monday, July 7, 2014

Sequence of Distillation Column Piping Study

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The designer now starts thinking about the proper orientation of nozzles and provisions for access to the points of operation and maintenance.

Considerations of the pipeline leaving the tower area and the adjacent piping shall be visualised.

The first step is to orient the manholes preferably all in same directions. Normally, manholes shall be oriented towards dropout area within a 30° segment of column as this facilitates the lowering of tower internals to the main access way. The manhole segment of platform should not be occupied by any piperack.

Tuesday, July 1, 2014

Information Required for Distillation Piping

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The basic layout and general engineering specifications describe:

  • The minimum access, walkways, platforms width and headroom requirements.
  • Handling facilities for tower internals, manhole covers, line blinds, relief valves. 
  • Maximum rise of ladders.
  • Pipe-system requirements, such as open or closed relieving systems.
  • Minimum line-size and required hose-stations. 
  • Access to valves and instruments. 


Monday, June 23, 2014

Basics of Distillation Column Piping

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The Distillation is a Process of separation of constituents of a Liquid Mixture & separate Recovery of Vapour Residue.

Basics of Distillation Column
Basics of Distillation Column
Various Kinds of devices Called Plates or Trays are used to bring the two phases in intimate contact. The trays are stacked one above other & enclosed in a Cylindrical Shell To Form An Equipment what we call as
'Distillation Column'.

Monday, June 16, 2014

Basics of Piping Calculations

4 Comments
The piping system of this tannery waste water treatment plant used stainless steel, austhenitic 18Cr, 8Ni type of tube as its material of construction. This type of material has a maximum allowable stress of 75,000 psi. The pressure inside the tube of waste water experiences 100psi. The assumed pressure is 100 psi. To get the schedule number of the said tube,


Since the calculated value of schedule number is less than forty, then schedule 40 type of tube will be used.

Tuesday, June 10, 2014

Pump and Pump Piping Presentation

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Pump and Pump Piping Presentation

Pump  

-     Introduction to Pumps
-       Classification of Pump
-       Industry Codes & Standards
-       Selection Criteria for Pumps
-       NPSH & Cavitation
-       Definitions

Monday, June 9, 2014

Flange Specification and Identification, Surface Finish & Distortion

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Flange Specification and Identification

Specification

A flange is specified by the following information:

a) Type and Facing: i.e. whether the flange is for example “Weld Neck, RTJ” or “Socket Weld, RF”.

b) Nominal Pipe Size: required for all flanges, usually in inches. 

c) Flange Pressure Class: required for all flanges, e.g. Class 150, 300, 900, 1500, 2500 etc.

d) Standard: i.e. ANSI B16.5, BS 1560, API 6A, API 605 or ASME B16.47.

Sunday, June 1, 2014

How to do Pump Piping with Layout Explained

7 Comments

1.0 PURPOSE

To provide the layout designer guidelines for developing pump piping designs that fully consider safety, operation, maintenance and economics.

2.0 EXCLUSIONS

All or part of this guide may be superseded by client mandatory standards or by the codes and regulations imposed by governmental jurisdictions covering the location where the piping is installed.

3.0 DISCUSSION

3.1 SAFETY

Proper consideration for personnel safety around pumps requires piping and valve arrangements that do not obstruct access for operation, maintenance or egress. Care must be exercised not to create tripping hazards with auxiliary piping.

3.2 OPERATION

Pumps normally require minimal attention during operation. Valves however, must be located for easy access; this is particularly true for paired or spared pumps. Where manual valves cannot be operated from grade, chain operators shall be used. If chain operators are not allowed per client specifications, platform access to valves shall be considered.

Thursday, May 22, 2014

Urgent Design Engineer Openings in Chicago, USA (Indians can Apply)

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One of my friend emailed me these job descriptions and he requires resumes for following positions on urgent basis at Chicago, USA. For this job, it's not mandatory for you to be a USA resident. He is basically working as a project engineer there and if you have got similar profile, i can get your resume through. Getting a work experience from USA can add 7 stars to your career. Here are the openings detail:

Preference would be given who can join us immediate or with a short notice. Please circulate this opportunities in your friends circle. We do have some of our USA requirements experience in Autodesk – Inventor – Sheetmetal, Weldments, assembly & detailing modules areas. If anyone is having B1 & H1B VISA, feel free to share their profiles or contact me directly to know more about it.

Job title: Design Support  Engineer

Domain: Rubber Tyred Gantry (RTG) Cranes Manufacturing

Qualification: Mechanical Engineering Degree

Years of experience: 3+

Expected profile of the candidate:

·         Good knowledge in sheetmetal designing.

·          2 years (Min.) of hands on experience in Autodesk – Inventor – Sheetmetal, Weldments, assembly & detailing modules.

·         Good Knowledge in PLM/PDM – Vault.

·         Good knowledge in heavy fabrication industry.

·         Good knowledge in welding processes.

·         Sound Knowledge in GD&T

·         Good knowledge in Tolerance stack-up  analysis

·         Good communication skill

·         Good knowledge in MS-Office

·         QMS - ISO awareness

·         Good experience in offshoring (India), project coordination, & risk mitigation.

Location: Chicago
Duration: 1-2 years

Another opening

Job DescriptionPlant Design Engineer
Exp. level4 to 8 years
Qualification: BE - Mechanical (4+ years exp)
Work Profile
aMust have
Ability to read Mechanical and Piping drawings
Ability to create interpret and create drawings using Autocad 2013
Ability to create parametric models and assemblies using Inventor or Autodesk
Plant design suite
Ability to prepare skids and piping drawings
Ability to Interpret and develop P&ID
Ability to carryout mechanical design hand calculations
Ability to apply QC tools in design
Ability to handle project communications both Internal and
external (interaction with overseas customers)
Industry exposure at least 2 years in a mechanical industry
preferably in a project management consultancy
bSoftware Exposure:- Hands on exposure with any one of these packages.
Multiple software exposure is an added advantange
Auto Cad 2013- High level of competency in 2d drawing preparations
Solidworks
Inventor
Plant design software
Office tools such as Excel, Word and Power Point
cData management :- Hands on exposure on one of the following:-
Windchill
Team center
Mapics
Vault
Meridian
Others
Additonal requirementsAdditional Exposure weightages:
Pipe support calculations
Silo Calculations
Structural member detailing
Structural support calculations
Preparation of drawings for chutes and ducts

For applying for above positions, please send your resume to ankit@pipingguide.net

If you have got some openings to share with our readers, please email me details of that too.

Tuesday, May 20, 2014

Things You Must Know When you do Piping Design

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Tubular products are termed ‘tube’ or ‘pipe’. Tube is customarily specified by its outside diameter and wall thickness, expressed either BWG (Birmingham wire guage) or in inches or in thousands. Pipe is customarily identified by ‘nominal pipe size’ with wall thickness defined by ‘schedule number’.


Piping materials

Carbon steel pipe is strong ,ductile, weldable, machineable, reasonably  durable and is nearly always cheaper than pipe made from other materials. If carbon steel pipe can meet the requirements of pressure, temperature, corrosion resistance and hygiene, it is the natural choice.

Sunday, May 18, 2014

Material Selection – Common Specifications for Carbon Steel Systems

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As can be seen from the Table, material selection can be made from available national standards such as ASTM and API.


Thursday, May 8, 2014

Important Definitions & Considerations in Piping

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Creep: Time dependent deformation of material that occurs under load at Elevated temperatures. 
  • Creep range for Low Carbonsteel Material =0.05 to 0.25 
  • Creep range for Medium Carbonsteel Material = 0.25 to 0.5
  • Creep range for High Carbonsteel Material = >0.5
Jacking oil: In order to prevent the metal to metal contact b/w the journal & bearing shell during startup & shut down, which is damaging in the long term, an oil pocket is machined in to the bottom shell of the journal bearing is supplied with oil under high pressure.

Pipe Size & Material Selection

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Velocity of material which the pipes are holding.

                   Velocity of the gases and air =15 to 20 m/s
                   Velocity of steam                   = 40 m/s

Pressure drop should be minimized to get better efficiency of machine.

Generally we allow 1% of pressure drop in 100mt.length.

Pressure drop is inversely proportional to Dia. of the pipe.

Monday, May 5, 2014

Steel Pipe And Fittings

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The decision regarding where to apply the mortar lining for steel pipe — at the manufacturing plant or in the field — is based on a number of factors including manufacturer capabilities, pipe diameter, shipping and handling considerations, and field installation conditions. As with ductile iron pipe, steel pipe can be supplied
with a range of linings, only one of which is cement mortar lining.


Thursday, May 1, 2014

Ductile Iron Pipe and Fittings

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In most cases, ductile iron pipe and fittings are mortar-lined at the factory. Field application of a mortar lining is normally done on older, in-service pipe for rehabilitation purposes. Ductile iron pipe can be supplied with protective linings other than cement mortar lining. Some of the other protective linings may be more appropriate, depending upon the fluid being transported. For instance, ductile iron pipe transmitting raw sewage under gravity flow conditions might be lined with a protective material since sulfuric acid, which may form in the space above the flow, can severely attack portland cement mortar linings and ferrous pipe materials. For most non-aggressive raw water and potable water transmission situations, cement mortar linings are very economical and the most common means of protection.

Saturday, April 26, 2014

Concrete Pressure Pipe and Fittings

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Pipe

Pipe manufactured in accordance with the ANSI/AWWA C300,3 C301,4 and C3025 standards is required to have high-strength structural concrete on the inside surfaces of the pipe which, in addition to enhancing the load-carrying capability, provides corrosion protection to the embedded reinforcing elements. All concrete is placed at the factory by vertical casting, centrifugal casting, or radial compaction methods.

Pipe manufactured in accordance with the ANSI/AWWA C3036 standard is required to have a mortar protective lining. The mortar is mixed using 1 part portland cement to 3 parts fine aggregate, with enough water added to obtain the necessary workability. The mortar lining is placed at the factory by the centrifugal
casting method.


Thursday, April 10, 2014

Upload Your Resume and Help Others in Getting Jobs

3 Comments
Hey Guys, here i am back after a long break with something special for all my readers. I have getting frequent emails lately that they wanted to contribute to Piping Guide in some form. But i was so packed behind busy schedules that i was not able to reply to those queries instantly. So, here is something i have decided to do for my loyal readers.

Recently i have signed a NDA with an upcoming big EPC company who will be starting their operations in India very soon, might be in a month or two. Currently they are finalizing the office space and i am not sure whether they're going to finalize this in Delhi/NCR or in somewhere in sound India. And most probably, they'll be requiring nearly 200+ people at least in various departments. Hint: It'll be a company like Petrofac and they have a big project in their backlog.

Saturday, March 29, 2014

Cement Mortar and Concrete Linings For Pipe

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History

It has been known for over 100 years that portland cement mortar and concrete provide considerable protection to embedded ferrous materials against the corrosive effects of soil and water. The most common embedded ferrous material receiving this type of protection has been the steel bars in reinforced concrete. There are literally thousands of reinforced concrete bridges, buildings, parking garages, and other structures in service today. During the 1920s practical methods were developed to apply portland cement mortar linings to cast-iron and steel pipe in the manufacturing plant. In the 1930s a method for applying cement mortar linings to in-situ pipe was developed.

Friday, March 28, 2014

Selection Criteria for Tracing Systems

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Assuming that methods for avoiding the need for tracing have been considered and rejected, the first step in matching the heat-tracing to the piping system requires an analysis of fundamentals. These include the type of application, suitability and relative cost of different types of heat-tracing, availability of steam and/or electricity, amount of heat loss which must be made up, requirements for temperature control, and classification of the traced area as a hazardous or ordinary environment due to the presence of flammable substances.

AREA CLASSIFICATION

Areas are classified according to their potential fire hazard as defined by Articles 500 to 505 of the National Electrical Code (NEC).48 [In industrial applications, verification that electric components meet NEC hazardous-area requirements is issued by a nationally recognized testing laboratory (NRTL).] Under this system, there are classified and unclassified (ordinary) areas. Hazardous areas have two different classification systems, the old class/division method and the new zone system. The zone system has been used in Europe for many years and is now being included in the International Electrotechnical Committee (IEC) specifications. The old Class/Division system rates locations by class, division, and group. The area class determines the category of combustible atmosphere: flammable gases, vapors, or liquids (Class I); combustible dust (Class II); and combustible fibers (Class III). The division indicates the likelihood of a hazard to be present under different conditions. Hazardous atmospheres with similar combustion properties
are listed in the same group.

Friday, March 21, 2014

Types of Heat Tracing Systems

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Heat-tracing systems can be divided into two broad classes, electric and fluid. Fluid heat-tracing systems utilize heating media at elevated temperatures to transfer heat to a pipeline. The fluid is usually contained in a tube or a small pipe attached to the pipe being traced. If steam is the tracing fluid, the condensate is either returned to the boiler or dumped. If an organic heat-transfer fluid is employed, it is returned to a heat exchanger for reheating and recirculation. In general, heating of tracing fluids can be provided by waste heat from a process stream, burning of fossil fuels, steam, or electricity.

Electric heat-tracing systems convert electric power to heat and transfer it to the pipe and its contained fluid. The majority of commercial electric heat-tracing systems in use today are of the resistive type and take the form of cables placed on the pipe. When current flows through the resistive elements, heat is produced in proportion to the square of the current and the resistance of the elements to current flow. Other specialized electric tracing systems make use of impedance, induction, and skin conduction effects to generate and transfer heat. Table A lists the operating and exposure temperatures and the principal characteristics of the different types of heat tracing.

Introduction to Heat Tracing of Piping System

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The term heat-tracing refers to the continuous or intermittent application of heat to a pipeline or vessel in order to replace heat loss to ambient. The major uses of heat-tracing include freeze protection, thawing, maintenance of fluids at process temperature (or at pumping viscosities), prevention of fluid component separation, and prevention of gas condensation.

The following examples are typical of the diversity of heat-tracing applications: freeze protection of piped water; transfer of molten process chemicals such as phosphoric acid, sulphur, and p-xylene; low-viscosity maintenance of pumped fluids including petroleum products, vegetable oils and syrups, polymeric and resinous materials, and aqueous concentrates and slurries; avoidance of condensation and subsequent improper burning of fuel gas in refineries; preventing moisture from condensing out of piped natural gas; preventing freezing of control valves and compressor damage; elimination of pipeline corrosion due to wet hydrogen sulphide resulting from condensed moisture.

Saturday, January 25, 2014

Tecnimont ICB Mumbai HR Email and Company Address

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Tecnimont ICB Mumbai HR Email and Company Address


Company Name
Tecnimont ICB Private Limited
Domain Expertise
EPC - OIL AND GAS
City
Mumbai
Country
India
Name of HR Manager
Mr. Devendra Pisat
Phone/Mobile
02266945912
Email
d.pisat@ticb.com
Website
www.ticb.com        


7 HATS Bangalore HR Email and Company Address

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7 HATS Bangalore HR Email and Company Address

Company Name
7 HATS
Domain Expertise
IT (Java) Non IT (Marketing)
City
Bangalore / Chennai
Country
India
Name of HR Manager
Smitha.K.B
Phone/Mobile
9945504445
Email
smitha@7hats.in
Website
www.7hats.in          


Valdel Engineers & Constructors Bangalore HR Email and Company Address

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Valdel Engineers & Constructors Bangalore HR Email and Company Address

Company Name
Valdel Engineers & Constructors Pvt. Ltd
Domain Expertise
EPC - OIL AND GAS
City
Bangalore
Country
India
Name of HR Manager
Mr.B.M.Gowrish
Phone/Mobile
08066282000
Email
hr@valdelec.com
Website
www.valdelec.com


L&T - Valdel Engineering Bangalore HR Email and Company Address

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L&T - Valdel Engineering Bangalore HR Email and Company Address

Company Name
L&T-Valdel Engineering Limited
Domain Expertise
EPC - OIL AND GAS
City
Bangalore
Country
India
Name of HR Manager
Mr.Pramod V.P
Phone/Mobile
08040330000
Email
career@lntvaldel.com
Website
www.lntvaldel.com

Name of HR Manager
Ms.Alka Srivastava
Phone/Mobile
09108040330117
Email
jobs@lntvaldel.com


 

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