Pneumatic Conveying Systems
Hello Sir,
Mr.Teus Tuinenburg
Dear Sir,
We are designing Pneumatic Ash Handling System for Fly Ash, please help us for calculating of air Volume requirement in m3/min for fly ash conveying.
Available data
Density of Fly Ash - 800 kg/m3
Material flow rate required - 85 T/hr.
Conveying Pipe Bore Size - 10" (inch)
Conveying distance(H) - 500 meter
Conveying Distance(V) - 39 meter
Nos of Bends used (90 deg.) - 9 Nos.
available air Pressure for conveying - 4.5 kg./ cm2
Thanking you
Sanjay
Attachments
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Re: Pneumatic Conveying Theory And Computer Calculations.
Dear Sanjay,
From the diagram, it is noticed that you are designing a pressure pot system.
In the diagram, during filling the pressure pot, the pressurized conveying air escapes through the pressure pot into the ESP hopper.
At that moment, the conveying air flow through the 500 m pipe stops and a blockage is born.
The content of the pressure pot is small compared to the volume of the 500 m line, resulting in several diluted plugs underway.
This influences the definition of the desired material flow rate.
To make this long conveying system smoothly operating requires special attention.
From the available data, everything is given, except the air flow.
F.i., how did you derive a 10 inch pipe, suitable for 85 tph? ■
Teus
Design Software For Pneumatic Conveying Systems
Good day,
Just to let you know, the newer version of PneuCalc software has modern engineering standards with a simple process interface to design/troubleshoot pneumatic conveying systems. Say goodbye to complicated simulation tools and textbook methods! See www.pneucalc.com
Cheers,
Colin ■
Ejector For Ash Cleaning
Dear Sir,
Ash evacuation is not my area of work. I have a very basic doubt and while searching the internet, I got here and I feel I am at the right place.
My Question is this:
We have 6kg/cm2 of service air present for usage (upto 250 l/s Flow- Atlas Copco compressor GA 160)
I want to suck heaps of ash which ever has accumulated through leakages (manually done right now)
This is to be transported to a cyclone separator in a mobile unit 50-60m away.
I want to make an ejector which, with the service air, is able to suck the ash from the heap and transport it to the mobile container mounted with a cyclone seperator (the ability of seperator to fil;ter fine as can be a separate issue)
We have made a small ejector (~890mm full length) design searching from the internet. It is having a great vacuum, but is too small for our requirement. Should I just keep experimenting with size increase, or is there any calculation for the same?
Also is the whole idea being used and successful or should I scrap off this thought? Whatever I have seen in the net, (either I am not using the correct names) I am not able to come across how this will work. Should I read more and contact you again? Do help ■
Re: Pneumatic Conveying Theory And Computer Calculations.
Dear ajayksajay,
Have a look at https://www.nilfisk.com/ and your problems are over. ■
Teus
Pneumatic conveying theory and computer calculations.
Over many years, pneumatic conveying threads are discussed in this forum, whereby it is noticed that in the recent years, the number of threads drastically dropped in numbers.
Most of the questions were about theory, quick answers, problem solving and many questions were asking for free engineering.
Also a number of forum members have contributed to the promotion of better understanding of the technology of pneumatic conveying.
However, a clear overview of the present state of knowledge is not easy to make.
Searching the internet, a lot of studies and theses are found, but they never result in a usable design procedure.
-The early pneumatic conveying designs were based on trial and error.
-After that scaling techniques were used, knowing that this technique was far from reliable for extrapolations.
-Companies used their own, some statistically based, methods and some used a method based on the relation between velocity head, solid loading radio and pressure drop.
All methods require material factors.
-When computers became available, the above methods were “computerized”
-With CFD computer programs, pneumatic conveying phenomena could be visualized and were very explanatory, but so far did not result in user friendly and reliable design software.
In addition, not only the pneumatic conveying parameters have to be considered, but also all the other influencing parameters and physics.
Over the years of my career in pneumatic conveying 1980 – present, I had the opportunity and the drive to study, describe, test end experiment with many pneumatic conveying installations in the field. (A 1 to 1 scaling lab)
This resulted in a pneumatic conveying computer calculation program as described hereafter.
INPUT
-Description of conveying route.
oLength horizontal
oLength vertical/slope
oPipe diameter(s)
oBends
-Description of material properties
oMaterial name
oMaterial density
oBulk density
oParticle size (distribution)
oSuspension velocity
oMaterial loss constant / material loss factor
oWall friction factor
oIntake pressure drop discharge (calculated in program)
oIntake pressure drop suction
ov-wall / v-suspension ratio
oFilter resistance factor
oMaterial specific heat constant
oGeldart class
oHausner ratio
oCarr Index
-Compressor types and properties
oOil free screw compressor with internal compression
oPD blower
oPD hybrid blower
oConstant mass pump. (sonic choke, turbo compressor, oil filled compressor)
oCompressor data curve operation points data base
oPredefined compressors and PD blowers
oCentrifugal fan
-Booster compressors
-compressor drive rpm droop
-Time increment calculation algorithm
-Ambient conditions
oTemperature
oCompressor intake Relative Humidity
oCompressor intake temperature
oAltitude
-Conveying gas
oAir
oNitrogen
oOxygen
-Predefined compressors and vacuum pumps
Calculated pneumatic conveying parameters (OUTPUT)
oCompressor gas flow
oGas volume retention in a tank system (replacement of discharged material)
oGas by pass volume in a tank system
oGas volume through conveying pipeline
oDryer/cooler water separation in gas supply
oGas leakage
Vacuum discharge rotary lock
Pressure feeding rotary lock
oBooster compressor gas flow
ogas velocities
oproduct velocities
opressure drops (per pipe section and total)
Product intake (calculated according pressure or fixed)
Nozzle pressure drop
Acceleration excluding product resistance
Product resistance
Bend extra resistance due to filled bend cross section.
Elevation
Suspension
Gas
Filter/cyclone
Gas supply piping
Vent piping
Compressor pressure
oSedimentation. (Local v-wall / v-suspension ratio)
oResidence time of a particle
oPresent mass in pipeline
oTemperature of product/gas mixture
oTemperature of pipe surface
oEnergy losses
oHeat losses
oBend gas- and material velocities.
oBend cross section material filling degree
oRH and condensation.
oCompressor pressure
oBooster pressure
oCapacity
oSolid Loading Ratio (SLR)
oConveying power
oCompressor power
oBooster compressor power
oEnergy consumption ( /ton )
oRe-Number
oMaterial loss factor (constant or formula)
oFeeders
Tank system
Screw feeder
Rotary lock
Eductor feeder
oFilter / Cyclone receivers
oSystem capacity
Filling time
Pressurizing time
Discharge time
Purge time
Cycle time
Tank system ( 1-vessel, 2-vessel, 3-vessel)
Screw feeder
Rotary lock
Eductor feeder
Bulk truck
oSystem energy consumption ( /ton )
oCapacity / pressure table
Additional Calculations
-Oil free screw compressors with internal compression
-Oil filled screw compressors with internal compression
-PD blowers
-PD hybrid blowers
-Eductor – venturi
-Self-operated pressure reducer.
-Cyclone
-Material particle size distribution
omean particle size for acceleration
omean particle size for suspension
-Air slides
-Bottom aeration
-Screw conveyor
-Filter fan power
-RH condensation
-Mesh – micron
-Quick modeling
-New installation modeling
-Cement unloader preliminary design
-Estimated capacity of cement, barite and bentonite installations.
-Bulk carrier dimensions
-Tank/silo pressure equalization.
-Compressor properties from performance curves.
-Storing data base text files
oCalculated installations
ocapacity/pressure curves
opressure/time curves for tank/silo pressure equalization
Calculation results applications
-Generating operational data for feasibility studies and economic evaluation.
-Generating operational data for locating malfunctions and fault finding.
-Calculation of special installations (Running 2 calculations parallel with manually entering shared parameters.)
oCoal injection systems with distributors
Application of ceramic control valve for capacity regulation and conveying stability.
1 feeder pipe into multiple injection lines
Shared distributor parameters are:
•distributor pressure
•Incoming capacity equals outgoing capacity
oVacuum/discharge conveyors cyclone, rotary lock
1 compressor serving as vacuum pump and discharge compressor.
Shared parameter is:
•Compressor gas flow vacuum system is equal to compressor gas flow discharge system.
oMultiple feeder systems, feeding into one common pipeline
Shared parameters are:
•Compressor gas flows
•Capacity feeder lines and capacity common line
•Pressure at combination point of feeder pipelines into common pipeline
Yarca pneumatic conveying software (www.yarca.nl) has these capabilities and possibilities. ■
Teus