Re: Article: Theory And Design Of Dilute Phase Pneumatic Convey…
Originally posted by Amrit Agarwal
My article "Theory and Design of Dilute Phase Pneumatic Conveying Systems" was published this month in Powder Handling and Processing magazine. This article gives an easy to use Excel-based calculation method for designing new dilute phase pneumatic conveying systems or for improving the performance of existing conveying systems.
Regards,
Amrit T. Agarwal
Consulting Engineer
Pneumatic Conveying Consulting Services
Email: polypcc@aol.com
Ph and Fax: 304 346 5125
■
Re: Article: Theory And Design Of Dilute Phase Pneumatic Convey…
Originally posted by Amrit Agarwal
My article "Theory and Design of Dilute Phase Pneumatic Conveying Systems" was published this month in Powder Handling and Processing magazine. This article gives an easy to use Excel-based calculation method for designing new dilute phase pneumatic conveying systems or for improving the performance of existing conveying systems.
Regards,
Amrit T. Agarwal
Consulting Engineer
Pneumatic Conveying Consulting Services
Email: polypcc@aol.com
Ph and Fax: 304 346 5125
■
System Design Calculations For Pneumatic Conveying
Dear Amrit
Could you send me a copy of this article?
My e-mail is wilson.meneses@jaraguaequipamentos.com
"... If you know basic Excel, you can use my calculation method published in Powder Handling and Processing magazine in its April 2005 issue. This article gives the theory and all of the equations that are internally used in computer programs. It takes the mystery out of the computer programs. I can send a free PDF copy if you need one...."
Best regards ■
System Design Calculations For Pneumatic Conveying
Dear Amrit
Could you send me a copy of this article?
My e-mail is wilson.meneses@jaraguaequipamentos.com
"... If you know basic Excel, you can use my calculation method published in Powder Handling and Processing magazine in its April 2005 issue. This article gives the theory and all of the equations that are internally used in computer programs. It takes the mystery out of the computer programs. I can send a free PDF copy if you need one...."
Best regards ■
Article On Pneumatic Conveying
Dear Wilson,
This has been done already.
Regards,
Amrit Agarwal
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125 ■
Article On Pneumatic Conveying
Dear Wilson,
This has been done already.
Regards,
Amrit Agarwal
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125 ■
Re: Design Calculations For Pneumatic Conveying
Dear Amrit,
I'm trying to find information on dust extraction system design, an area which I have very little knowledge of. Can you please help me by sending me a copy of your three articles cited throughout Bulk-Online forum, being:
1) "Theory and Design of Pneumatic Conveying Systems"
2) "Debottlenecking Pneumatic Conveying Systems" and
3) "Product Quality in Pneumatic Conveying"
My email is burroughsp@onesteel.com
Thank you.
Pakorn ■
Re: Design Calculations For Pneumatic Conveying
Dear Amrit,
I'm trying to find information on dust extraction system design, an area which I have very little knowledge of. Can you please help me by sending me a copy of your three articles cited throughout Bulk-Online forum, being:
1) "Theory and Design of Pneumatic Conveying Systems"
2) "Debottlenecking Pneumatic Conveying Systems" and
3) "Product Quality in Pneumatic Conveying"
My email is burroughsp@onesteel.com
Thank you.
Pakorn ■
System Design Calculations For Pneumatic Conveying
Dear Amrit
May I also request a copy of your article?
"... If you know basic Excel, you can use my calculation method publised in Powder Handling and Processing magazine in its April 2005 issue. This article gives the theory and all of the equations that are internally used in computer programs. It takes the mystery out of the computer programs. I can send a free PDF copy if you need one...."
My e-mail is simon@carrier.com.br
Thanks in advance
Osmar ■
System Design Calculations For Pneumatic Conveying
Dear Amrit
May I also request a copy of your article?
"... If you know basic Excel, you can use my calculation method publised in Powder Handling and Processing magazine in its April 2005 issue. This article gives the theory and all of the equations that are internally used in computer programs. It takes the mystery out of the computer programs. I can send a free PDF copy if you need one...."
My e-mail is simon@carrier.com.br
Thanks in advance
Osmar ■
Thank You
Thank you Mr. Agarwal for sending me the article on "theory and design of dilute phase pneumatic conveying systems". I found it a practical, hands on approach and I am now trying to compose my own calculation sheet. Since I am European, I have one problem: the use of non-SI units, but I'll get by that ! 
I can definitely recommend the article! ■
Thank You
Thank you Mr. Agarwal for sending me the article on "theory and design of dilute phase pneumatic conveying systems". I found it a practical, hands on approach and I am now trying to compose my own calculation sheet. Since I am European, I have one problem: the use of non-SI units, but I'll get by that !
I can definitely recommend the article! ■
Pneumatic Conveying Calculations
Osmar,
Please send your request to my email address given below:
Amrit Agarwal
Consulting Engineer
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125 ■
Pneumatic Conveying Calculations
Osmar,
Please send your request to my email address given below:
Amrit Agarwal
Consulting Engineer
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125 ■
Pneumatic Conveying System Calculation
Hi,
Pl. send me Pnuematic Conveying System Calculations.
With Best regards,
Dipak ■
Pneumatic Conveying System Calculation
Hi,
Pl. send me Pnuematic Conveying System Calculations.
With Best regards,
Dipak ■
Pnumatic Conveying Design
Dear Sir,
Could you please tell me, what will be the minimum conveying velocity and phase density to be considered to design M type F.K.PUMP pneumatic system for conveying 225 tph PPC cement(Blaine:3700cm2/gm) at a conveying distance of 260 meter & six 90 degree bends?
Regards,
R.M.SAHU,
Grasim Industries ltd.
India ■
Pnumatic Conveying Design
Dear Sir,
Could you please tell me, what will be the minimum conveying velocity and phase density to be considered to design M type F.K.PUMP pneumatic system for conveying 225 tph PPC cement(Blaine:3700cm2/gm) at a conveying distance of 260 meter & six 90 degree bends?
Regards,
R.M.SAHU,
Grasim Industries ltd.
India ■
Re: Design Calculations For Pneumatic Conveying
Dear Mr Sahu,
A FK-pump operates at approx 1.8 bar maximum.
At 225 tons/hr, I expect the pump to consume approx. 200 kW
(Check this with Fuller)
The design of your installation could be as follows.
CEMENT
SAHU sahu d 06-25-2007
Pressure discharge Cement
Preliminary design
Convey length = 260 m
Nu of bends= 6
Pump vol = 1 + 1 m^3/s
q-convey = 1.01 m^3/s
Dia begin = 293 mm Dia end = 343 mm
Pipevolume = 19.69 m^3
-------------Pipeline
Press-------Cap----------mu-----------------------v-begin ---- v-end ------kWh/ton ----- res.time
2.500------- 279 --------62--------Silo calc--------5.4 --------12.8-------- 0.78 -------- 40.12
2.250------- 264 --------58--------Silo calc.--------5.7--------12.8 --------0.75-------- 38.27
2.000-------247 ---------55-------Silo calc.-------- 6.1 --------12.8--------0.72 --------36.32
1.750-------230-----------51------Silo calc.-------- 6.7 --------12.8-------- 0.69 -------- 34.36
1.500 -------211----------47------ Silo calc. --------7.3 --------12.7-------- 0.66--------32.27
1.250-------190----------42--------Silo calc.--------8.0--------12.7-------- 0.64-------- 30.16
1.000-------167 ----------37------ Silo calc. -------9.0 --------12.6-------- 0.61 --------27.94
0.750-------140----------31--------Silo calc. -------10.2--------12.6--------0.60 --------25.63
0.500-------106-----------23-------Silo calc.--------11.9--------12.5--------0.63-------- 23.16
0.250-------54-------------12------Silo calc. --------14.1--------12.4-------- 0.93-------- 20.45
Empty pipeline pressure ...= 671.3 mmWC
To answer your question.
The minimum conveying velocity is:
approx 6.7 m/sec at 1.75 bar(o)
approx 14 m/sec at atmospheric conditions
As this design is for a 2 stepped pipeline , the velocities for a single pipeline diameter become different.
best regards
teus ■
Teus
Re: Design Calculations For Pneumatic Conveying
Dear Mr Sahu,
A FK-pump operates at approx 1.8 bar maximum.
At 225 tons/hr, I expect the pump to consume approx. 200 kW
(Check this with Fuller)
The design of your installation could be as follows.
CEMENT
SAHU sahu d 06-25-2007
Pressure discharge Cement
Preliminary design
Convey length = 260 m
Nu of bends= 6
Pump vol = 1 + 1 m^3/s
q-convey = 1.01 m^3/s
Dia begin = 293 mm Dia end = 343 mm
Pipevolume = 19.69 m^3
-------------Pipeline
Press-------Cap----------mu-----------------------v-begin ---- v-end ------kWh/ton ----- res.time
2.500------- 279 --------62--------Silo calc--------5.4 --------12.8-------- 0.78 -------- 40.12
2.250------- 264 --------58--------Silo calc.--------5.7--------12.8 --------0.75-------- 38.27
2.000-------247 ---------55-------Silo calc.-------- 6.1 --------12.8--------0.72 --------36.32
1.750-------230-----------51------Silo calc.-------- 6.7 --------12.8-------- 0.69 -------- 34.36
1.500 -------211----------47------ Silo calc. --------7.3 --------12.7-------- 0.66--------32.27
1.250-------190----------42--------Silo calc.--------8.0--------12.7-------- 0.64-------- 30.16
1.000-------167 ----------37------ Silo calc. -------9.0 --------12.6-------- 0.61 --------27.94
0.750-------140----------31--------Silo calc. -------10.2--------12.6--------0.60 --------25.63
0.500-------106-----------23-------Silo calc.--------11.9--------12.5--------0.63-------- 23.16
0.250-------54-------------12------Silo calc. --------14.1--------12.4-------- 0.93-------- 20.45
Empty pipeline pressure ...= 671.3 mmWC
To answer your question.
The minimum conveying velocity is:
approx 6.7 m/sec at 1.75 bar(o)
approx 14 m/sec at atmospheric conditions
As this design is for a 2 stepped pipeline , the velocities for a single pipeline diameter become different.
best regards
teus ■
Teus
Re: Design Calculations For Pneumatic Conveying
Sir,
Thanks for answering my query.Could you please also tell me what phase density yoy have considered for designing?What will be FAD(Free air delivery) and design pressure of the compressor for the said F.K.Pump.
Regards,
R.M.Sahu,
INDIA ■
Re: Design Calculations For Pneumatic Conveying
Sir,
Thanks for answering my query.Could you please also tell me what phase density yoy have considered for designing?What will be FAD(Free air delivery) and design pressure of the compressor for the said F.K.Pump.
Regards,
R.M.Sahu,
INDIA ■
Re: Design Calculations For Pneumatic Conveying
Dear Mr Sahu,
I designed the installation for the chosen velocities (as usual in pneumatic cement conveying).
Whether the design is dense or dilute phase is not so important.
It will be close to the minimum pressure drop per meter of length.
Less air would make the conveying dense phase.
mu in the table means the Soloid Loading Ratio (SLR)
The free air delivery is already given in the calculation as:
q-convey = 1.01 m3/sec # 60.6 m3/min
The conveying pressure at the beginning of the pipe (= FK pump pressure) shouls be approx. 1.8 bar(o) as for the FK pump, this is the maximim pressure it can handle. (Please check this with Fuller, USA).
The compressor should be an oil free screw compressor with internal compression with a displacement of approx 60 m3/min at approx 2.5 bar maximum ■
Teus
Re: Design Calculations For Pneumatic Conveying
Dear Mr Sahu,
I designed the installation for the chosen velocities (as usual in pneumatic cement conveying).
Whether the design is dense or dilute phase is not so important.
It will be close to the minimum pressure drop per meter of length.
Less air would make the conveying dense phase.
mu in the table means the Soloid Loading Ratio (SLR)
The free air delivery is already given in the calculation as:
q-convey = 1.01 m3/sec # 60.6 m3/min
The conveying pressure at the beginning of the pipe (= FK pump pressure) shouls be approx. 1.8 bar(o) as for the FK pump, this is the maximim pressure it can handle. (Please check this with Fuller, USA).
The compressor should be an oil free screw compressor with internal compression with a displacement of approx 60 m3/min at approx 2.5 bar maximum ■
Teus
Pneumatic Conveying Calculation Program
Dear Armit
could you send pneumatic conveying calculation program
best regards
my addrress is
hwiman.cho@umicore.com ■
Pneumatic Conveying Calculation Program
Dear Armit
could you send pneumatic conveying calculation program
best regards
my addrress is
hwiman.cho@umicore.com ■
Re: Design Calculations For Pneumatic Conveying
Sir,
Again thanks for your prompt reply.Sir we are running the f.k.pump for last 20 years @ 155-160 tph with two compressor having designed FAD of 56m3/min each but measured value of FAD of 45 m3/min each at @ 2kg/cm2 pressure.We are upgrading the cement mill for 225 tph by installing V-Separator in the circuit so we are redesigning it for 225 tph.I am doubtful whether it will work smoothly at FAD of 60.6m3/min.Normal back pressure is coming around 1.0 bar but some time we are facing tripping of the F.K.Pump due to high back pressurre even at 155-160 tph.Please clarify our doubt for smooth functioning the pump at FAD of 60.6m3/min @ 225 tph.
Regards,
R.M.Sahu,
INDIA ■
Re: Design Calculations For Pneumatic Conveying
Sir,
Again thanks for your prompt reply.Sir we are running the f.k.pump for last 20 years @ 155-160 tph with two compressor having designed FAD of 56m3/min each but measured value of FAD of 45 m3/min each at @ 2kg/cm2 pressure.We are upgrading the cement mill for 225 tph by installing V-Separator in the circuit so we are redesigning it for 225 tph.I am doubtful whether it will work smoothly at FAD of 60.6m3/min.Normal back pressure is coming around 1.0 bar but some time we are facing tripping of the F.K.Pump due to high back pressurre even at 155-160 tph.Please clarify our doubt for smooth functioning the pump at FAD of 60.6m3/min @ 225 tph.
Regards,
R.M.Sahu,
INDIA ■
Re: Design Calculations For Pneumatic Conveying
Dear Mr Sahu,
The FK pump is the feeder of a pneumatic conveying system.
The feeder function of the FK pump is 150 – 165 tons/hr against the pneumatic conveying pressure.
For a FK pump, this pressure is limited at approx. 1.8 bar(o)
(For 150 tons/hr, the drive motor of the FK pump should be approx. 110 kW at 980 rpm)
Increasing the FK pump capacity from 150 tons/hr to 225 tons/hr will at least require a drive change to 165 kW at 1500 rpm (if possible – ASK Fuller bulkhandling USA) or a new FK pump or an additional FK pump.
As you already experience overload tripping of your present FK pump drive motor, due to high conveying pressure, this is an indication that the pneumatic conveying system needs to be redesigned, to keep the conveying pressure at a maximum of 1.8 bar at 225 tons/hr.
The redesign is given in my earlier reply.
Using the existing pneumatic conveying system requires a recalculation to find out if that is possible anyway. (diameters and air volumes)
success
teus ■
Teus
Re: Design Calculations For Pneumatic Conveying
Dear Mr Sahu,
The FK pump is the feeder of a pneumatic conveying system.
The feeder function of the FK pump is 150 – 165 tons/hr against the pneumatic conveying pressure.
For a FK pump, this pressure is limited at approx. 1.8 bar(o)
(For 150 tons/hr, the drive motor of the FK pump should be approx. 110 kW at 980 rpm)
Increasing the FK pump capacity from 150 tons/hr to 225 tons/hr will at least require a drive change to 165 kW at 1500 rpm (if possible – ASK Fuller bulkhandling USA) or a new FK pump or an additional FK pump.
As you already experience overload tripping of your present FK pump drive motor, due to high conveying pressure, this is an indication that the pneumatic conveying system needs to be redesigned, to keep the conveying pressure at a maximum of 1.8 bar at 225 tons/hr.
The redesign is given in my earlier reply.
Using the existing pneumatic conveying system requires a recalculation to find out if that is possible anyway. (diameters and air volumes)
success
teus ■
Teus
System Design Calculations For Pneumatic Conveying
Dear Amrit,
May I have a copy of your System Design Calculations for Pneumatic Conveying.
Thanks.
Marshall ■
System Design Calculations For Pneumatic Conveying
Dear Amrit,
May I have a copy of your System Design Calculations for Pneumatic Conveying.
Thanks.
Marshall ■
Pneumatic Conveying Calculations Method
Dear Marshall,
Please send your request to my email address given below.
Amrit Agarwal
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125
Regards,
Amrit ■
Pneumatic Conveying Calculations Method
Dear Marshall,
Please send your request to my email address given below.
Amrit Agarwal
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125
Regards,
Amrit ■
Theory And Design Of Dilute Phase
Dear Mr. Amrit Agarwal,
Thank you very much for promptly sending the article. Your lucid presentation was of great help to understand basics of design for my purpose.
I request you to kindly mail me your other articles.
Thank you for your time and co-operation.
Sincerely,
Vinod Mistry ■
Theory And Design Of Dilute Phase
Dear Mr. Amrit Agarwal,
Thank you very much for promptly sending the article. Your lucid presentation was of great help to understand basics of design for my purpose.
I request you to kindly mail me your other articles.
Thank you for your time and co-operation.
Sincerely,
Vinod Mistry ■
To All Memebers
Dear friends ,
here i am introducing an article which i saw about tranfer of dense/dilute phase. This artical i got it from Mr.Amrit T. Agarwal
Consulting Engineer. This is very useful article for pnematic conveying engineers and designers.
regards
prakash ■
To All Memebers
Dear friends ,
here i am introducing an article which i saw about tranfer of dense/dilute phase. This artical i got it from Mr.Amrit T. Agarwal
Consulting Engineer. This is very useful article for pnematic conveying engineers and designers.
regards
prakash ■
Theory And Design Dilute Phase Pneumatic Conveyor System
Mr Amrit
Thanks you by sent the article of Dilute Phase Pneumatic Conveyor.
Is very clear and usefull to understand and apply to the industry.
I'm designing a pneumatic vacuum system to transport PET (polyethylene teraftalate) and there are not many information about this subject
Regards ■
Theory And Design Dilute Phase Pneumatic Conveyor System
Mr Amrit
Thanks you by sent the article of Dilute Phase Pneumatic Conveyor.
Is very clear and usefull to understand and apply to the industry.
I'm designing a pneumatic vacuum system to transport PET (polyethylene teraftalate) and there are not many information about this subject
Regards ■
Re: Design Calculations For Pneumatic Conveying
Dear Amrit,
May I have another copy of your System Design Calculations for Pneumatic Conveying?
I am very interested in your articles and in the way that you can design a pneumatic conveying installation.
Thank you very much in advance
Alfonso
alfonso@boreasconsulting.net ■
Re: Design Calculations For Pneumatic Conveying
Dear Amrit,
May I have another copy of your System Design Calculations for Pneumatic Conveying?
I am very interested in your articles and in the way that you can design a pneumatic conveying installation.
Thank you very much in advance
Alfonso
alfonso@boreasconsulting.net ■
Excel Based Sheet For Conveying
Hello,
Does anyone have a copy of the excel based spreadsheet for the example calculation in Armit's"Theory and design of dilute phase pneumatic conveying systems" article. I am trying to copy the example to match the article results and I can not get the same numbers.
I would like to check my spreadsheet with a correct one to see what I am doing wrong in excel.
Thanks. ■
Excel Based Sheet For Conveying
Hello,
Does anyone have a copy of the excel based spreadsheet for the example calculation in Armit's"Theory and design of dilute phase pneumatic conveying systems" article. I am trying to copy the example to match the article results and I can not get the same numbers.
I would like to check my spreadsheet with a correct one to see what I am doing wrong in excel.
Thanks. ■
Re: Design Calculations For Pneumatic Conveying
Mr. Agarwal,
Thank you for sending the article entitled "Theory and Design of Dilute Phase Pneumatic Conveying Sytems". This is a relatively new field of study for me, and your article has been an excellent jump start.
I have taken your information and created an Excel program, very similar to yours. I have been experimenting with different values to obtain a grasp of pressure losses in these systems.
I do have the following questions:
1. This particular article is for dilute phase.
a. I have found there is a specific distinction between dilute and bulk phase pneumatic conveying, ie material to air ratio and maximum air/solid flow. What specific criteria do you use for defining a phase as dilute or dense/bulk?
b. If you have an article/literature/calculations on dense/bulk phase pneumatic conveyor design, I would be very interested in receiving it from you.
2. Pressure, Vacuum and Pressure-Vacuum systems ~ do you have information regarding of the application of these methods?
3. In your Worksheet #3, it appears that the "Section Number" from Worksheet #2 and #3 do not entirely agree; ie Section #10, the first vertical portion, does not show vertical losses in Worksheet #3. Have these rows been skewed? Please advise.
4. At the elbow, you mention that the particle velocity at the exit is 80% of the inlet particule velocity (p 20, Sect 2.4.1). For dP.acc, would this mean there is actually a negative pressure loss at the elbow, as deceleration is at work here? Please advise.
Thanking you in advance,
Ryan Telford. ■
Re: Design Calculations For Pneumatic Conveying
Mr. Agarwal,
Thank you for sending the article entitled "Theory and Design of Dilute Phase Pneumatic Conveying Sytems". This is a relatively new field of study for me, and your article has been an excellent jump start.
I have taken your information and created an Excel program, very similar to yours. I have been experimenting with different values to obtain a grasp of pressure losses in these systems.
I do have the following questions:
1. This particular article is for dilute phase.
a. I have found there is a specific distinction between dilute and bulk phase pneumatic conveying, ie material to air ratio and maximum air/solid flow. What specific criteria do you use for defining a phase as dilute or dense/bulk?
b. If you have an article/literature/calculations on dense/bulk phase pneumatic conveyor design, I would be very interested in receiving it from you.
2. Pressure, Vacuum and Pressure-Vacuum systems ~ do you have information regarding of the application of these methods?
3. In your Worksheet #3, it appears that the "Section Number" from Worksheet #2 and #3 do not entirely agree; ie Section #10, the first vertical portion, does not show vertical losses in Worksheet #3. Have these rows been skewed? Please advise.
4. At the elbow, you mention that the particle velocity at the exit is 80% of the inlet particule velocity (p 20, Sect 2.4.1). For dP.acc, would this mean there is actually a negative pressure loss at the elbow, as deceleration is at work here? Please advise.
Thanking you in advance,
Ryan Telford. ■
Theory And Design Of Pneumatic Conveying Systems
Thank you Amrit T. Agarwal
Consulting Engineer
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125
I recieved your article named "Design of Pneumatic Conveying Systems". It is a good and concise article that gives the basic principles of simulation of dilute phase systems. It has helped me a lot to validate my methods, although I would have liked to see estimation equations for the solid solid interaction friction.
Regards
James Swift ■
Theory And Design Of Pneumatic Conveying Systems
Thank you Amrit T. Agarwal
Consulting Engineer
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125
I recieved your article named "Design of Pneumatic Conveying Systems". It is a good and concise article that gives the basic principles of simulation of dilute phase systems. It has helped me a lot to validate my methods, although I would have liked to see estimation equations for the solid solid interaction friction.
Regards
James Swift ■
Re: Pneumatic Conveying Calculations Method
[
Amrit T. Agarwal
Consulting Engineer
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125
dear mr amrit
i have gone thru all your messg in bulk poder handeling website and is very much impressed .
could yo please send me a copy of the article of following . "your article named "Design of Pneumatic Conveying Systems "
"... If you know basic Excel, you can use my calculation method published in Powder Handling and Processing magazine in its April 2005 issue. This article gives the theory and all of the equations that are internally used in computer programs. It takes the mystery out of the computer programs. I can send a free PDF copy if you need one...."
==================================================================================================== =======
FURTHER ABOUT US , IS A COMPNAY CALLED PARTH ENGINEERING PVT LTD. DOING PNEUMATIC ASH HANDELING SYSTEM FOR BOILER ASH IN SUGAR INDUSTRY.
WE HAVE JUST STARTED OUR JOURNEY WITH TWO MAJOR ORDERS FOR 170 TON EACH IN TWO SUGAR MILL AND EXPECTED 10 MORE ORDERS IN NEXT SIX MONTH.
WE HAVE TIED UP WITH ONE LOCAL EXPERT IN PNEMATIC ASH CONVEYING SYSTEM HOWEVER WE WOULD LIKE TO GO TO DEEP INTO BETTER QUALITY OF DESIGNING , CONSULTANCY , MANUFACTURING AND ERECTION AND COMMISSIONING STAGE .
WOULD YOU PLEASE LIKE TO BE A PART OF US OR SUGGEST SOME INDIAN ORGANISATION WHO CAN BE A GOOD PARTNER FOR US.
ALSO I WISH TO MENTION THAT THIS TIME IS A HIGH TIME IN INDIA WITH LOT OF POWER PLANT COMING UP IN THE MARKET WHICH HAS GOOD OPORTUNITY FOR ASH HANDELING SYSTEM AS BEING A SOLUTION TO POLUTION PROBLEM .
LOOKING FORWARD FOR A POSITIVE AND SUPPORTIVE REPLY FROM YOU.
WITH BEST REGARDS
Sanjay Agarwal,
DIRECTOR
PARTH ENGINEERING Pvt. Ltd.,FF - 06 , First Floor,National Arcade, Plot No. 4,Local Shoping Centre,Ghazipur Main Road,Ghazipur, Delhi - 110 096
Tele/Fax : 011 - 22232137 , Telephone : 011 - 22240091 Mobile : 093130 55226 OUR E MAIL ADDRESS - sanjayagarwal.delhi@gmail.com ■
Re: Pneumatic Conveying Calculations Method
[
Amrit T. Agarwal
Consulting Engineer
Pneumatic Conveying Consulting
Email: polypcc@aol.com
Ph and Fax: 304 346 5125
dear mr amrit
i have gone thru all your messg in bulk poder handeling website and is very much impressed .
could yo please send me a copy of the article of following . "your article named "Design of Pneumatic Conveying Systems "
"... If you know basic Excel, you can use my calculation method published in Powder Handling and Processing magazine in its April 2005 issue. This article gives the theory and all of the equations that are internally used in computer programs. It takes the mystery out of the computer programs. I can send a free PDF copy if you need one...."
==================================================================================================== =======
FURTHER ABOUT US , IS A COMPNAY CALLED PARTH ENGINEERING PVT LTD. DOING PNEUMATIC ASH HANDELING SYSTEM FOR BOILER ASH IN SUGAR INDUSTRY.
WE HAVE JUST STARTED OUR JOURNEY WITH TWO MAJOR ORDERS FOR 170 TON EACH IN TWO SUGAR MILL AND EXPECTED 10 MORE ORDERS IN NEXT SIX MONTH.
WE HAVE TIED UP WITH ONE LOCAL EXPERT IN PNEMATIC ASH CONVEYING SYSTEM HOWEVER WE WOULD LIKE TO GO TO DEEP INTO BETTER QUALITY OF DESIGNING , CONSULTANCY , MANUFACTURING AND ERECTION AND COMMISSIONING STAGE .
WOULD YOU PLEASE LIKE TO BE A PART OF US OR SUGGEST SOME INDIAN ORGANISATION WHO CAN BE A GOOD PARTNER FOR US.
ALSO I WISH TO MENTION THAT THIS TIME IS A HIGH TIME IN INDIA WITH LOT OF POWER PLANT COMING UP IN THE MARKET WHICH HAS GOOD OPORTUNITY FOR ASH HANDELING SYSTEM AS BEING A SOLUTION TO POLUTION PROBLEM .
LOOKING FORWARD FOR A POSITIVE AND SUPPORTIVE REPLY FROM YOU.
WITH BEST REGARDS
Sanjay Agarwal,
DIRECTOR
PARTH ENGINEERING Pvt. Ltd.,FF - 06 , First Floor,National Arcade, Plot No. 4,Local Shoping Centre,Ghazipur Main Road,Ghazipur, Delhi - 110 096
Tele/Fax : 011 - 22232137 , Telephone : 011 - 22240091 Mobile : 093130 55226 OUR E MAIL ADDRESS - sanjayagarwal.delhi@gmail.com ■
Design Calculations for Pneumatic Conveying
My article "Theory and Design of Dilute Phase Pneumatic Conveying Systems" was published this month in
href="https://who.bulk-online.com/profile/2-reinhard-h-wohlbier.html" target="blank">Powder Handling and Processing magazine. This article gives an easy to use Excel-based calculation method for designing new dilute phase pneumatic conveying systems or for improving the performance of existing conveying systems.
Regards,
Amrit T. Agarwal
Consulting Engineer
Pneumatic Conveying Consulting Services
Email:
href="mailto:polypcc@aol.com">polypcc@aol.com
Ph and Fax: 304 346 5125
Picture added by Adinistrator as an example:
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