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Pneumatic conveying pipe

For calculating pressure drop in conveying pipe, please visit our pneumatic conveying handbook

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Section summary
1. Introduction
2. Piping connections / coupling
3. Piping bends
4. Piping length
5. Pressure and vacuum service


1. Introduction

Conveying pipes are used in pneumatic conveying to send the product from a point A to a point B. There design is resulting from the considerations of different inputs or constraints.

Among the constraints are the aspects related to the performance of the conveying system and its influence on products. This will fix the pneumatic conveying pipe diameter but also the design of the bends of the pipe layout.

Some inputs will have also to be done by the plant operator, especially regarding the type of pipe coupling (clamping) to be used or the length of pipe sections.

2. Pneumatic Transport Piping connections

How to best chose the pipe coupling ? Pros and cons of each type of coupling ?

Different types of pneumatic conveying pipe couplings are available in the market. The main ones are the following : SMS connections, Morris clamps and flanges. The decision to go for one or the other will depend on the service conditions of the pneumatic conveying line, the habits of the plant operator but also the confidence on the reliability of the conveying line - if the product to be transported is very difficult and blockages are expected, it is better to have quick dismantling connections.

Table 1 : Different types of piping connections and their advantages and drawbacks

Type of coupling Picture Pros Cons
SMS PowderProcess.net - SMS pipe connectionPowderProcess.net - SMS pipe connection Quick dismantling

Easy to dismantle and clean the pipe
More expensive - need to have threaded pipes

Sometimes difficult to have a tight connection
Morris coupling PowderProcess.net - Morris pipe connection Less sensitive to pipe alignement vs SMS

Generally tight

No need to have threaded pipe
Long to dismantle

Not always easy to adjust
Flange PowderProcess.net - Morris pipe connection Tighter connection, can be qualified for high pressures
Long lasting - usually preferred when the pipes goes over long distance outside building
Very Long to dismantle

Not always easy to adjust

Need to change the gasket at each opening

3. Pneumatic conveying pipe bends

How to design at best conveying pipe bends ?

The design of Conveying Pipe Bends is of particular importance for lean phase conveying where the product is circulated at high velocity. When hitting the bends some products will be damages - fragiles powder breaking and forming fines,

In order to avoid such phenomena, the pneumatic transport bend radius must not be too sharp. As a general rule, the ratio Bend Radius / Pipe diameter should not be below 10.

4. Piping length

Deciding on the pipe section length will mainly depends on the service which is expected for the pipe. If it is expected to be dismantled often for cleaning for example, then short pipe sections are recommended. On the contrary, if the system is not expected to be dismantled, while conveying a single and well known product for instance, then it will be economically sounder to have longer sections.

As a rule of thumbs :
- High frequency for dismantling : pipe section length < 6 m
- No dismantling expected : pipe section > 10 m

When having to dismantle pipes frequently, specific access may be foreseen in order to ensure a safe access to the piping.


5. Pressure and vacuum service

The pressure at which will be operated the pipe must be taken into consideration for the choice of the piping but also the coupling required. Although pressure in conveying line is usually moderate, it is a good engineering practice to define the maximum pressure that could happen, especially in case of problem on the line, and chose piping and coupling qualified for a higher pressure.

A proper installation of the coupling is also critical for both pressure and vacuum service. It is important to avoid leakages of product in the case of pressure conveying, which would lead to losses but also to dust explosion risks. For vacuum conveying ingress of air in the pipe must be avoided as it could bring pollutants if the air is not treated or which could reduce the performance of the conveying line by bypassing the inlet of product and reducing the conveying air available at the beginning of the line potentially leading to blockages of the pipe.