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Ankur's_Chemical_Engg_Blog > You Are Most Likely To Be A Chemical Engineer If.....
Posted
ankur2061
on 27 July 2012 - 01:59 AM
2. You maintain different colored hard hats and safety goggles in your wardrobe.
3. You are planning to install a scrubber on your kitchen exhaust duct
4. Somebody mentions...
Ankur's_Chemical_Engg_Blog > Fixed Water Spray Demand Calculations For Fire Protection Of Tanks / Vessels
Posted
ankur2061
on 12 July 2012 - 02:07 AM
When we talk of fire protection, some of the most comprehensive guidelines and standards developed for fire...
Ankur's_Chemical_Engg_Blog > Faq On Process Design Engineering
Posted
ankur2061
on 12 August 2010 - 08:53 AM
Some of the frequently asked questions (FAQ's) are what are the activities that a process design engineer do,...
Ankur's_Chemical_Engg_Blog > Perforated Pipe Distributor Sizing Calculations
Posted
ankur2061
on 16 May 2013 - 03:48 PM
Perry’s Handbook (8th Editio...
Ankur's_Chemical_Engg_Blog > How To Write A Plant Operating Manual
Posted
ankur2061
on 13 July 2013 - 06:48 AM
Ankur's_Chemical_Engg_Blog > Gas Boot Sizing Upstream Of Fwko Tanks
Posted
ankur2061
on 28 April 2014 - 12:34 AM
Ankur's_Chemical_Engg_Blog > Safety Rules To Be Followed For A Field Visit By A Process Design Engineer
Posted
ankur2061
on 02 August 2012 - 03:27 AM
Ankur's_Chemical_Engg_Blog > The Flip Side Of Engineering Standards And Practices
Posted
ankur2061
on 07 October 2013 - 11:40 AM
I like to keep myself abreast of the latest engineering standards and practices from international organizations (API / ISO) and from engineering / operating companies. The best thing about them is I don't have to overload my memory trying to remember established engineering and design practices which are generally well...
Ankur's_Chemical_Engg_Blog > Minimum Safe Recyle Process Flow Schemes For Centrifugal Pumps
Posted
ankur2061
on 01 January 2013 - 06:46 AM
Ankur's_Chemical_Engg_Blog > As-Built Piping & Instrument Diagrams
Posted
ankur2061
on 06 July 2012 - 02:47 AM
Most of you are aware that during the engineering phase an important task by the process engineer is to prepare "Piping and Instrument Diagrams", in short...
Ankur's_Chemical_Engg_Blog > Some Utility Consumption Estimates
Posted
ankur2061
on 14 February 2012 - 10:33 AM
Ankur's_Chemical_Engg_Blog > Project Management - A Lost Art
Posted
ankur2061
on 29 June 2011 - 11:12 PM
Ankur's_Chemical_Engg_Blog > Careers Options For Chemical Engineers With Special Emphasis On Females
Posted
ankur2061
on 04 June 2011 - 11:28 PM
Ankur's_Chemical_Engg_Blog > Solid-Liquid Mixing In Agitated Vessels (Just Suspended Speed)
Posted
ankur2061
on 08 April 2016 - 06:29 AM
Solid suspension and dispersion in a liquid is an important operation carried out in mixing systems. The primary objective of solid-liquid mixing is to create and maintain a solid-liquid slurry, and to promote and enhance the rate of mass transfer between the solid and liquid phases. Such processes are typically carried out in mechanically agit...
Ankur's_Chemical_Engg_Blog > Heat Transfer In Buried Liquid Lines (Stagnant Liquid)
Posted
ankur2061
on 13 February 2016 - 01:42 PM
My earlier blog entry on heat transfer in buried liquid pipelines related to temperature reduction of the flowing liquid at a certain distance from the pipeline inlet.
Let us think of a buried pipeline or pipeline section where the liquid flow has been stopped and the liquid is now in a stagnant condition in the pipeline or pipeline section. L...
Ankur's_Chemical_Engg_Blog > Natural Gas Pipeline Blowdown Time Calculation
Posted
ankur2061
on 02 June 2013 - 07:31 PM
The idea of posting blog entries with equations and calculation steps is to encourage young...
Ankur's_Chemical_Engg_Blog > Comparing Iso13709 / Api 610 With Ansi / Asme B73.1 Centrifugal Pumps
Posted
ankur2061
on 05 December 2012 - 02:50 AM
Ankur's_Chemical_Engg_Blog > Know Your Career Opportunities - A Primer On Seeking New Employment
Posted
ankur2061
on 01 June 2011 - 02:41 AM
Ankur's_Chemical_Engg_Blog > Steam Tracing Design
Posted
ankur2061
on 04 November 2017 - 12:54 PM
It is well known that chemical process plants located in areas where ambient temperatures can fall well below freezing may require heat tracing of lines and equipment containing process fluids that can freeze or congeal and stop flowing thereby causing costly plant outages and economic losses. In certain cases, freezing of line contents and flo...
Ankur's_Chemical_Engg_Blog > Empirical Equations For Pressure Drop In Crude Oil And White Oil Pipelines
Posted
ankur2061
on 27 August 2012 - 12:17 AM
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