Basics of Process Engineering Design
This blog is meant for Entry level Engineers in Industries and Undergraduate Students.
Monday, February 17, 2014
Sunday, October 27, 2013
List of Companies for Freshers to Apply
Being a fresher, it is very difficult to know where to apply, and how to get a job. Here I am mentioning few of the companies dealing in Process Design suitable for Freshers & Mid level Engineers to apply for job in India...
My best suggestion is to search websites of companies on google.com and apply in their career section. Most of the companies requires Chemical / Process Engineers; However, Mechanical Engineers, Electrical Engineers, Instrumentation Engineers, Project Engineers & Peoples of different branches of Engineering should also search & apply as these companies needs engineers from almost all branches...
My best suggestion is to search websites of companies on google.com and apply in their career section. Most of the companies requires Chemical / Process Engineers; However, Mechanical Engineers, Electrical Engineers, Instrumentation Engineers, Project Engineers & Peoples of different branches of Engineering should also search & apply as these companies needs engineers from almost all branches...
- Samsung Engineering
- Valdel Engineers & Constructors Pvt. Ltd
- Cinda Engineers & Constructors Pvt. Ltd.
- Indian Oil Tanking Design & Engineering
- Lurgi India Ltd.
- Larsen & Toubro Ltd
- Doosan Babcock Engineering & Services
- ISJEC John Thompson
- Saipem Triune Engineering
- Polyplex Corporation (Hydro Power)
- UDHI India Pvt Ltd
- PL Engineering
- Tractebel Engineers & Constructors
- Worley Parsons Oman Engineering L.L.C
- Satnam Engineering
- Lahmeyer International
- WVG Engineers Consultants
- Asmetech Engineering
- Kazhtroy Engineering India Pvt. Ltd.
- Naftogaz India Pvt. Ltd.
- Triveni Engineering & Industries Ltd.
- Nuberg Engineering
- Unitech Machines
- Technofab Engineering Ltd
- Enereff Engineers Pvt. Ltd.
- JCE Engineering & Management Services Pvt. Ltd.
- Driplex Water Engineering Ltd.
- Degremont
- Multitex Filteration
- SST India India
- MultiMax Engineers
- Advance Group of Companies
- Toyo Engineering
- Aarvi Encon Pvt. Ltd
- Coperion
- Energo Group
- CH2M Hill India Pvt. Ltd.
- Desein Indure
- Quanta Process Solution Pvt. Ltd.
- A2Z Maintainence
- Global Economic Advantage
- Luminous Engineering & Technology Services Pvt. Ltd
- Jasubhai Engineering Pvt. Ltd.
- Green Leaf Engineering Ltd.
- BGR Energy Systems Ltd.
- Dimension Engineering Consultants Pvt. Ltd.
- Linde Engineering India Pvt. Ltd.
- Flovel Mecamidi Energy Pvt. Ltd.
- SK E&C
- GS E&C
- Flour Daniel
- CB & I
- UOP
- BOC
Tuesday, October 8, 2013
What is Line Sizing and How it is done?
It's a very common problem for students
and all fresher’s who start their careers as either GET or Management Trainees
in Process Industry to get familiar with terminologies used in process
industries. Here i have tried to simplify and provide most basic level
information when one is at the beginning level of his/her career.
Usually a Line refers to a Pipe and Line
size refers to its ID (Internal Diameter) which can be calculated by using the
continuity equation. Usually we have Fluid normal/standard flow rates & we
are asked to calculate the line size. Now the question is how to do it.
We have a relation
Actual Flow Rate(m3/s) = (Maximum
Allowable Velocity)x(Cross Sectional area of pipe)
i.e. Q = a.v
Where Q = Actual Volumetric Flow Rate
(m3/s)
V = Maximum Allowable
Velocity ≤ Erosion Velocity (m/s)
A = Cross Sectional Area of Pipe (Pi/4 *ID2)
(m2)
ID= Internal Diameter of Pipe (m)
In most of the practical industrial
problems you will have Volumetric Flow rate but you will not have the Maximum
Allowable Velocity or Erosion Velocity (of course no question of Pipe ID, as
you have to calculate this).
Rule
of thumb says that maximum allowable velocity for Gases is 29 m/s while optimum
is considered as 20 m/s. while for liquids minimum velocity should be kept as
0.9 m/s and maximum is 4.5 m/s. Optimum velocity is considered between 1.5 –
2.0 m/s.
Kindly note I have not considered pressure
drop in this line sizing. However; one can control the pressure drop within the
range by increasing or decreasing pipe Diameter on excel file.
Now the important part is that why to do
Line Sizing?
Of Course to control the pressure drop to
keep our pumping cost low & to make sure that a Line has such a diameter
that velocity of fluid flowing inside the line do not crosses maximum allowable
limit (normally Erosion Velocity) to prevent damage of line due to Erosion.
Now in industries, one of the major
problems is that you will never get actual flow rate. Your flow rate will be
given as either standard flow or normal flow for gases. Some of the common
Units are as follows:
1. MMSCFD :
Million Standard Cubic feet per day
2. MMSFH :
Million Standard Cubic Feet Per Hour
3. SCFM :
Standard Cubic feet per minute
4. Sm3/hr : Standard Cubic meter per hour
6. Kg/hr :
Mass Flow Rate
Now important point is to note that these
all flow rates are not actual Volumetric Flow rates.
For 1 to 4 units, convert it to
Sm3/hr and then convert it to actual
flow rates by the help of following Relation
V Actual = (V1 Standard x Standard Pressure x Actual Temperature (Max.)) divided by (Actual
Pressure (Min.) x Standard Temperature)
Here V stands for Volumetric Flow Rate,
Pstd. 1 atm, Tstd. 25 Degc / 298 K
Similarly for Flow rate in Nm3/hr
be converted to Actual Flow Rate using above formulae. Only T Normal will
reduce to 0 Deg C or 273 K.
It is interesting to note that in actual
life problem we will be given a pressure range. For line Sizing one shall
consider minimum pressure and maximum temperature in that range which will
enable us to know largest Pipe ID.
Kindly note that all units should must be
in same convention to cancel each other to give the unit of calculated
parameter.
Let me share an example for simple Line sizing, as next examples very complex.
You have been given Mass Flow Rate of Gas 69084 Kg/hr.
Molecular Weight of Gas is Given as 16.48 kg/kgmol
Temperature is Given as 60 Deg C
Pressure 11.2 bar
Solution: Now remember the formulae for Sizing a Line, You require Volumetric Flow Rate which can be obtained by Dividing Mass flow by Density.
Now the point is how to Calculate Density, Firstly convert your temperature in Rankine which is 599.67 for given case & Pressure in PSI which is 162.4 in this case.
Now if you remember basic chemical equations,
Density= (Mol. Wt x Pressure) / (R x T) which is =(16.48*162.4)*(10.73*599.67)
= 0.416 lb/ft3 which is 6.66 kg/m3.
Hence your Volumetric Flow Rate is = (69084)/(6.66*3600)= 2.88 m3/s
Now take Allowable velocity for gas = 20 m/s
Now your Line Size = Sqrt((Actual Vol. Flow Rate) / (velocity*pie/4)) in m
= SQRT((2.88)/(20*.785)) in m
= 0.428 m
= 428 mm
Hence Appropriate line Size is 450 NB
Let me share an example for simple Line sizing, as next examples very complex.
You have been given Mass Flow Rate of Gas 69084 Kg/hr.
Molecular Weight of Gas is Given as 16.48 kg/kgmol
Temperature is Given as 60 Deg C
Pressure 11.2 bar
Solution: Now remember the formulae for Sizing a Line, You require Volumetric Flow Rate which can be obtained by Dividing Mass flow by Density.
Now the point is how to Calculate Density, Firstly convert your temperature in Rankine which is 599.67 for given case & Pressure in PSI which is 162.4 in this case.
Now if you remember basic chemical equations,
Density= (Mol. Wt x Pressure) / (R x T) which is =(16.48*162.4)*(10.73*599.67)
= 0.416 lb/ft3 which is 6.66 kg/m3.
Hence your Volumetric Flow Rate is = (69084)/(6.66*3600)= 2.88 m3/s
Now take Allowable velocity for gas = 20 m/s
Now your Line Size = Sqrt((Actual Vol. Flow Rate) / (velocity*pie/4)) in m
= SQRT((2.88)/(20*.785)) in m
= 0.428 m
= 428 mm
Hence Appropriate line Size is 450 NB
Given Below are some complex problems, usually encountered in Natural Gas Industry. Kindly refer Rule of Thumb for Pipelines before arriving any conclusion.
If Pressure drop is also to be considered
for Gases case then
When Flow rate is given as mass flow rate
then it can be multiplied by density to get the flow rates. Even if Molecular weight is given, Density
can be calculated at given pressure and Temp.
For liquid fluids, there is not standard
or normal flow. Any Volumetric flow is actual flow. So it can be used directly
in above formulae.
Now it is very obvious that by knowing
actual flow rates of fluid, we can calculate the approximate line size if
pressure drop is not considered.
Tuesday, January 31, 2012
PSA Nitrogen Gas Generation and it's Benefits
HOW NITROGEN GENERATOR WORKS?
Nitrogen
generators uses compressed air to pressurize a
vessel filled with Carbon Molecular Sieves, especially made for this purpose, which actually sifts molecules
by physical composition or structure. By forcing air into this pressure vessel
or sieve bed, we cause gas molecules to be trapped in the
sieve, while the N2 gas floats free. After a period of time, we release a bit
of the pressure in the sieve bed
to draw off the N2 molecules,
and collect them in a surge/storage tank for use by the application. We then
open a valve in the sieve bed and
release all of the pressure, forcing out the captured molecules of the unwanted
gases, and cleansing the sieve for the next cycle. Molecules of gas released
into the air immediately combine back to air's ambient percentages. With our
systems, we use two sieve beds
that work at opposing ends of the cycle to provide a more consistent flow of
our captured gas into the surge tank.
Applications and Purity:
Nitrogen gas being cheapest
inert gas available is widely used as inert gas material in Chemical
industries, Food & Pharmaceutical industries, Electronic, Synthetic fiber,
Heat treatment furnaces, for fire controls in coal and mine industries etc. for
which we produces onsite nitrogen generators from 99% to 99.9999%.
If your organization falls under any of following categories, you need
a Nitrogen Generator
Agri-food &
Beverages Automotive, Aeronautical & Transportation Chemicals
& Petrochemicals
Craftsmen
& Worksites Electronic Components and Products Environment
Glass, Cement
& Lime Research Centers & Laboratories
Metal Fabrication Industries
Metallurgy Oil & Gas Optoelectronics
Pharmaceuticals
& Biotechnologies Plastics
Processing Pulp & Paper
Semiconductors Space & Aeronautics
By using Nitrogen Gas Generator you
can save 80% of your money!!!
- Nitrogen Gas Generator
reduces your Nitrogen gas cost by
80-90%.
- No attendant is required as it’s a
fit and forget unit.
- Automatic start-up time is only 5
minutes.
- Nitrogen supply as and when
needed.
- Produces the Purity and Flow rate
you need at the point of use.
- Self-Contained Skid mounted units
for easy site installation.
- Very low maintenance costs.
- Carbon Molecular Sieves never
require replacement; it lasts the whole life time of Gas Generator
.
S.N.
|
Nitrogen Cylinders
|
Nitrogen Gas Generator
|
1.
|
Cylinder Nitrogen cost is very high i.e. Rs.15 per cubic meter.
|
Nitrogen gas cost is only Rs. 2 per cubic meter.
|
2.
|
Apart
from gas cost, delivery fees, monthly tank rental fees, fuel charges,
electric charges, plus local and/or state taxes. These additional charges can
nearly double the actual cost.
|
Once plant is installed, Only
electricity cost is the cost of Nitrogen gas.
|
3.
|
All time dependency on availability
of Nitrogen cylinders.
|
Nitrogen can be produced as and when
required.
|
4.
|
Nitrogen Purity in Cylinders is not
reliable as it varies from cylinders to cylinders.
|
Nitrogen purity is very steady and
reliable.
|
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