| Page summary |
|---|
| 1. Definition of a screw feeder |
| 2. Position in the process |
| 3. Important considerations for the design |
| 4. Screw flight design |
| 5. Dosing |
| 6. Common problems with screw conveyors |
| 7. Screw conveyor manufacturers |
| 8. Interactive Screw Sizing Calculator |
| 9. Rules of Thumb & Safety Limits |
This Engineering overview gives you in one page all what you need to know regarding screw conveyor design and operation. Looking for a calculation guide, have a look to our Screw Conveyor Design calculation page.
A screw conveyor is made of a housing, typically a tube or a U trough, in which is rotating a screw flight or auger (helical shaped blade) that allows to mechanically move bulk materials. The screw can be shaftless, or having a shaft on which is welded the helical blade.
Screw conveyors are a very popular equipment in solids processing industry to move and / or dose products. Their principle allows a simple and quite robust operation, although the design must be well detailed in order to avoid issues that could lead to damages to the product and to the equipment itself (generation of foreign bodies). Screw feeders are used with product causing no or medium abrasion but should be avoided with products causing high level of abrasion ; the screw rotating in the product, is indeed very sensitive to abrasion phenomena.
A screw fitted directly to a hopper upstream is often referred in the literature as screw feeder while the equipment alone is often referred as screw conveyor. The screw conveyor takes sometimes the denomination of Auger screw.
A typical screw conveyor design is shown below :

Figure 1 : Screw conveyor principle drawing and key components
Looking for other dosing equipment / feeder ? check these other pages out : AIRLOCK ROTARY VALVES, VIBRATING TUBES. By PowderProcess.net
Auger conveyors are usually placed below hoppers where they can convey horizontally the product to another process operation. When the conveying involves also a weighing, the screw feeder is actually used as a dosing equipment.
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Screw conveyors can also introduce solids in a pneumatic conveying system. In most of the case, they are used in vacuum transport since there is no pressure problem, but some designs can also used to feed the product towards a pressure conveying line. For this particular purpose, the screw flight design must allow a compression of the solid so that the plug formed avoids the pressurized air of the conveying line to come back through the screw. This cannot be used for all products, thus, for pressure conveying, airlock rotary valves are usually preferred to screw conveyors for introducing the product.
Screw feeders are found in any industries handling bulk materials, to convey and / or to dose bulk solids :
Industrial Auger conveyors can be very long reaching >5 m, however this kind of design can only be used with non sensitive product and when no cleaning is required. It is indeed not possible to remove the flight of such screws, and if some designs exist to still access the inside (trough design for example), the efficiency of cleaning is reduced and the time to clean will be long. Besides, the length of the screw makes it prone to bending and to possible metal / metal contacts with the housing, risking to pollute the product with metal chips. As a reference, a screw flight of 4 m can bend up to 7-8 mm from the shaft straight axe, if no proper provision have been taken to allow for such bending, metal / metal contact can happen.
The deflection of a screw that is supported on both ends can be calculated thanks to [1] :
\[\delta = \frac{5 \cdot W \cdot L^3}{384 \cdot E \cdot I}\]
(Shaft deflection between two rigid end bearings under uniform self-weight)
With :
\(W\) : total weight of the screw (N or lbf)
\(L\) : length in between bearings (m or in)
\(E\) : modulus of elasticity (\(\text{N/m}^2\) or psi)
\(I\) : moment of inertia of the shaft (\(\text{m}^4\) or \(\text{in}^4\)), where for a pipe shaft of outer diameter \(D_o\) and inner diameter \(D_i\):
\[I = \frac{\pi}{64} \left( D_o^4 - D_i^4 \right)\]
It appears better, for hygienic applications, to request the following characteristics :
Inclined screws are tempting because they allow to solve many process problems especially when retrofitting installations, one should however be very careful that these types of screws are usually difficult to access and extract for cleaning, may be also more sensitive to bending and metal metal contacts, and are not very efficient (efficiency is decreasing with the angle).
Table 1 : Screw conveyor capacity as a function of its inclination
| Angle of screw (degrees) | Percent of max capacity (%) |
|---|---|
| <8 | 100 |
| 20 | 55 |
| 30 | 30 |
| 45 | 0 |
There are different types of screw feeders that can be found in process industries :
Screw conveyors are rotating equipment, which make them a risk for operators who would try to reach the inlet of outlet of the screw. For this reason, a special attention must be paid to the inlet and down pipe. If they are equipped with flexibles especially, those flexibles should be dismantable only with a tool and the operator trained to stop the machine if such dismantling is necessary. In case it is not possible, a cross in the pipe preventing to reach the screw flight can be installed, provided that it does not prevent the flow of product. In any case, a risk analysis must be carried out by the plant operator to make sure the access is properly protected.
The screw flight can take different shape and pitch according to the application in which it is used.
Other designs are available with paddles or cut flights when there is a need for mixing the material.
In applications requiring high hygiene degree of execution, the shaft must be plain, not hollow, and the flight must be fully welded and polished. This in order to avoid that material get trapped in non accessible areas and pollute later good products.
The design of the shaft and the motor must be well aligned so that the motor is able to run the screw and start it from 0 speed or run it overloaded, when it requires the most torque. Conversely, the shaft must be designed to sustain such a torque and not break when it is applied.
When used in dosing applications, the screw must be equipped with a motor on VFD in order to run in coarse speed and fine speed (see dosing page). Screw conveyors are most often integrated in automatic Gain in Weight or Loss in Weight systems. When running Loss of Weight, the screw feeder can be operated either in volumetric mode or on automatic gravimetric mode.
Use this interactive tool to estimate volumetric throughput, mass delivery rate, screw flight peripheral tip speed, shaft deflection, and drive power requirements. Switch between SI Metric and US Imperial units.
| Outer Peripheral Tip Speed (\(v_{tip}\)) | - |
| Theoretical 100% Volumetric Flow (\(V_{th}\)) | - |
| Actual Volumetric Throughput (\(V_{act}\)) | - |
| Mass Flow Rate (\(\dot{m}\)) | - |
| Radial Flight-to-Trough Clearance | - |
| Calculated Center Shaft Deflection (\(\delta\)) | - |
| Estimated Shaft Deflection / Radial Clearance Ratio | - |
| Estimated Drive Motor Power (\(P_{est}\)) | - |
Screw conveyors are usually reliable equipment, however a certain number of issues may require some corrections :
Table 2 : common problems with screw conveyors
| Issue | Root cause and action |
|---|---|
| Metal - metal contact | Bearing damage - change the bearing Incorrect clearance screw flight / housing - review the design or change the flight Foreign body in the screw - review foreign body prevention prior to screw conveyor |
| Bearing damage | Powder has entered the bearing - check bearing seal and flushing |
| Screw performance below design | Screw flight mounted in the wrong direction Bad feed of powder to the screw - check the feed of product if no bridging or ratholing |
| Screw conveyor blocked | Check if outlet valve is opened Check pitch of the screw - the powder should not be compacted |
| Inaccurate dosing with screw | Size too big - check screw size or adapt screw flight profile at the end of the screw |
Many companies can offer screw conveyors however not all companies can make really safe and reliable equipment. Few references of screw conveyor manufacturers is given below (note that powderprocess.net has no relation with those companies) :
For bulk solids handling equipment operating in potentially explosive dust atmospheres (ATEX Zone 20/21/22), the circumferential flight tip speed should be kept below 1.0 m/s (approx. 197 ft/min). Exceeding this velocity increases mechanical friction and hot-spot risks, potentially creating an effective ignition source for combustible dusts.
As the angle of inclination increases, bulk solids tend to slip backward over the flights. Up to 8° the capacity remains near 100%. At 20° inclination, capacity drops to roughly 55%; at 30°, it drops to approximately 30%; and above 40° to 45°, standard pitch screw conveyors lose nearly all conveying efficiency unless designed with short pitches, tight housing clearances, or tubular casings operated at higher speeds.
To prevent metal-to-metal rubbing between the screw flight and trough (which generates metal particulate contamination and ignition risks), total beam deflection δ should not exceed 5 mm to 8 mm (0.25 to 0.31 inches) and must remain safely below 50% of the nominal radial clearance between the outer flight tip and the trough.
Source
[1] Bulk
Solids Handling, Don McGlinchey, Blackwell, page 203