Compressed air for pneumatic conveying should be selected from the conveying system's required airflow, pressure and air quality. Start with the material and transport duty. Then match the air source, treatment and controls to that duty. A compressor motor rating, a pipe diameter or a desired production rate cannot define the complete air requirement on its own.
This guide focuses on the interface between a bulk-material conveying system and its air supply. It helps plant engineers and buyers prepare an enquiry, compare proposals and plan acceptance. It does not replace the conveying designer's material tests, transport calculations or approved operating procedures. Those documents establish the conditions that the air package must actually deliver.

What belongs in a conveying-air specification?
Define the transport task before selecting equipment
Describe the material, origin and destination of each transfer. Include the operating schedule, required throughput and the ways production can change. Distinguish a continuous feed from batch transfers and identify any routes that can operate together. The resulting duty schedule should show what the conveying system must accomplish, rather than simply list the machines a buyer expects to purchase.
Give the conveying designer the actual material information available. Relevant properties may include particle condition, moisture sensitivity, bulk characteristics and the consequences of product breakage. Do not substitute a familiar material name for the required test information. Powders sold under the same commercial description may behave differently in a transport system. The designer should identify which properties need confirmation before providing an air requirement.
Identify the air-supply handover point
Mark the physical point where the air supplier's responsibility ends and the conveying equipment begins. State which side includes the final filter, isolation arrangement, connecting pipework and measurement points. A pressure quoted at the compressor outlet is different from a pressure required at a conveying vessel or injection point. A quotation for compressed air for pneumatic conveying needs an explicit delivery location.
Use a simple interface schedule shared by both suppliers. Include required operating conditions and the documents that establish them. Assign an owner to every unresolved field. This prevents the air supplier from selecting against an assumption that the conveying supplier later rejects. It also clarifies who supplies the instruments needed to demonstrate that the interface requirement has been met.
| Required information | Who should define it? | Why it matters |
|---|---|---|
| Material and transfer duty | Plant and conveying designer | Establishes the process task |
| Airflow and reference basis | Conveying designer | Allows comparable air-source selection |
| Pressure at the connection | Conveying designer, coordinated with air supplier | Defines the delivery requirement |
| Moisture and contamination limits | Process owner and equipment suppliers | Defines treatment scope |
| Concurrent routes and operating sequence | Plant controls and process teams | Defines combined demand and transitions |
Choose the air-source category from the duty
A blower and a compressor are different selection options
Pneumatic conveying can use different air-moving technologies. The CAGI blower guide includes pneumatic conveying among blower applications. That does not mean every conveying line should use a blower. The required pressure and flow, together with the selected transport arrangement, determine which equipment categories deserve evaluation.
When reviewing a dry oil-free screw blower, ask for the proposed model's performance at the actual duty. Compare the complete package and operating envelope. Do not infer suitability from the word oil-free or from the equipment's appearance. A blower proposal must still meet the process pressure, flow and inlet-condition requirements established for the project.
Do not create a low-pressure duty by assumption
A dedicated low-pressure screw compressor may be worth assessing when its documented operating range matches the duty. Selection requires confirmation of the delivered pressure, capacity basis and air-quality arrangement. A product category page starts that discussion; the selected configuration and its technical offer complete it.
Reducing pressure from a general factory header is another possible architecture, but it needs a system review. Establish whether the header can support the combined demand and whether the pressure-reduction arrangement suits the process. Compare the consequences for existing users, controls and treatment. A low process pressure does not automatically establish that an existing high-pressure source is the preferred long-term arrangement.
Keep vacuum and positive-pressure arrangements distinct
A conveying project may involve suction, positive pressure or separate stages with different functions. Identify where the air mover sits relative to the material route. Then describe the relevant inlet and discharge conditions. Do not send a positive-pressure compressor specification to a supplier when the actual requirement concerns a vacuum duty or a different process stage.
The conveying designer should define the selected arrangement and the equipment that protects it. The air supplier can then assess the appropriate machine and package. Where the project includes several air-moving duties, give each one its own identification. This keeps conveying air, instrument air and dust-extraction requirements from being merged into a single ambiguous equipment schedule.
Turn the operating sequence into an airflow schedule
List the phases of each transfer
Ask the process supplier to describe the transfer sequence in practical terms. Relevant stages may include preparation, material feeding, transport, clearing and the defined end condition. The required air delivery can differ between stages. The equipment enquiry should identify those stages and ask which requirement governs selection, rather than assume that one steady reading describes the entire transfer.
State how long the process operates in each condition using the plant's actual production information. Where timing is not yet agreed, mark the field as unresolved. Do not invent a cycle duration to produce a neat average. An average built from unsupported timing can hide a short demand event that the air source and controls still have to accommodate.
Separate concurrent demand from alternative routes
A material-handling drawing may show several destinations, but that does not establish that all transfers run simultaneously. Write an operating matrix identifying permitted combinations. Include the production constraints that prevent other combinations. This matrix can reduce uncertainty without quietly reducing the required production capability. It also gives the controls team a clear description of the intended operating cases.
For each permitted combination, obtain the corresponding feed-air requirement from the conveying designer. Add other users only when they share the same air-supply boundary. Keep each contribution visible in the calculation. If the quoted flow already includes a particular process stage or accessory, do not add that demand again under a separate allowance.
Align every airflow quantity before comparing proposals
Record the units and reference conditions behind each airflow value. Distinguish the air supplier's delivery basis from the conditions within the conveying pipe. A numerical match between two quoted flows does not prove that they describe the same mass of air or the same measurement location. Both suppliers should confirm the conversion basis used in the interface schedule.
Use the existing air-compressor CFM explanation when reviewing the terminology. The project calculation should retain its own agreed definitions. Keep the original values beside any converted figures so another engineer can follow the calculation. Conversion accuracy cannot correct an input that belongs to the wrong process condition.

Compressed air for pneumatic conveying: pressure at the process
Account for the route between machine and process
Draw the air path from the selected package to the process connection. Include treatment equipment, valves and connecting pipework within the supply scope. Ask the responsible supplier to establish the pressure requirement at each defined boundary. This makes it possible to distinguish the process inlet requirement from the source discharge condition.
Do not add unrelated pressure allowances taken from another factory. The proposed route, equipment selection and operating flow govern this project. Where layout details remain provisional, identify the assumptions and the stage when they must be confirmed. A quotation can remain conditional during early design, but its condition should be visible to the person comparing offers.
Review changes in process resistance
The conveying system's operating condition can change as material moves through it. Ask its designer to identify the pressure and airflow combinations that the air source must support. Include the expected transitions and any normal variation associated with the receiving equipment. These requirements belong in the selection envelope rather than an informal note issued after purchase.
A higher pressure indication is not, by itself, a reason to increase the compressor setting. Establish where it was measured and which part of the transport sequence was active. The process supplier should define the permitted response to an abnormal condition. Air-package controls must support that response without overriding equipment protection or the site's approved procedures.
Specify air quality around the material and equipment
Separate the product requirement from the machine description
Define what air quality the material and process require at the connection. Consider moisture, particles and oil-related contamination separately. The term oil-free describes an equipment category or a documented performance scope; it is not a complete specification for every contaminant in the delivered air. Ask how the complete proposed system will meet the stated requirements.
A dry oil-free screw compressor can be evaluated where that equipment category suits the process. Keep the selection tied to the model's documented scope. Requirements from food, pharmaceutical or other sensitive production must come from the process owner and applicable project documents. Do not assign a universal air-quality class from the industry name alone.
Define moisture control before choosing a dryer
Ask whether the material is sensitive to moisture and how that affects the required delivery condition. Identify the relevant air temperature and pressure basis. Then assess the treatment proposal against that requirement. A visible absence of water at one observation point does not establish that the specified moisture condition is maintained throughout the required operating cases.
Review a refrigerated air dryer or another treatment arrangement only where it meets the defined duty. Include selection conditions and the equipment upstream and downstream of the dryer. The treatment package should be sized and protected for the proposed air source, rather than copied from an unrelated utility installation.
Include treatment consumption and pressure requirements
If the selected treatment uses air for regeneration, identify how that consumption is supplied and represented in the quotation. Establish whether it is included in the delivered-air requirement or needs a separate contribution. Keep treatment demand distinct from process conveying demand so changes to one can be reviewed without rebuilding an unexplained total.
For example, an enquiry involving a heatless adsorption dryer should request the proposed configuration's regeneration information. It should also state the relevant inlet conditions and required output condition. No generic purge percentage is needed at the planning stage when the correct model-specific information can be requested and recorded.
Design the control interface around production
Agree how the process requests air
The conveying controls and air-package controls need a shared description of normal operation. Define how a transfer requests air, how availability is confirmed and how the process responds when supply is unavailable. Separate a request signal from proof that the required condition exists at the handover point. The two signals serve different purposes.
Specify who supplies and interprets each signal. Include the meaning of ready, running, available and fault within the actual project documents. A signal label that seems obvious to one supplier may have a narrower meaning in another controller. Clear definitions help prevent a process from starting because a compressor is electrically enabled while the required air condition has not been established.
Plan the normal end of a transfer
Define the expected sequence when material transfer finishes. The conveying designer should specify any required clearing stage and the conditions for stopping air delivery. The air supplier can then establish a suitable response for the selected package. Avoid designing the supply around a simple on-off request if the actual process requires a more detailed transition.
Keep routine stopping separate from protective stopping. The project should identify who owns each action and which instructions govern it. This is especially useful when several packages are supplied by different companies. A clear sequence reduces the need for operators to improvise between equipment manuals during commissioning or after a later controls change.

Compare a dedicated source with a shared plant supply
Review the complete shared operating case
When conveying takes air from a factory header, identify the other users that can operate during a transfer. Check the required quality, pressure and availability of each user group. The conveying demand should be assessed against the plant's actual operating combinations. A successful transfer during a quiet shift does not demonstrate every required production condition.
Review where measurements are available in the shared system. A reading near the compressor station may not explain a disturbance at the conveying connection. Put the measurement locations on the system drawing. The commissioning plan can then distinguish a source-capacity question from a distribution issue or a process event without relying on unrelated controller screenshots.
Compare project boundaries as well as machine prices
A dedicated supply can create a clearer operating boundary, but it also needs installation space, utilities and a maintenance plan. A shared supply may reuse existing equipment while introducing additional coordination. Compare those scopes explicitly. Neither architecture should be described as automatically cheaper or more reliable without the project's own operating and cost information.
The existing discussion of air supply for jet-mill applications addresses a different material-processing duty. Do not carry a milling requirement into a conveying selection simply because both processes handle powder. Keep separate schedules when a production line includes both milling and transport, even if the project later evaluates a common utility source.
Prepare the installation and maintenance scope
Reserve access for equipment that needs attention
Arrange the package so technicians can reach the components identified in its service instructions. Include the path for moving replacement parts and the access needed around filters, valves and connections. A layout that fits within the room outline may still make routine maintenance difficult. Review service activities before fixing the final position of surrounding equipment.
Coordinate cooling, electrical supply and any other required utilities using the proposed model's documents. State who supplies the connecting services and who checks them before start-up. The package supplier should identify the conditions used for selection. The plant then has a clear list of site requirements to confirm rather than a general instruction to provide a suitable installation.

Document isolation and responsibility boundaries
Identify how the air package and conveying equipment can be isolated for their intended maintenance tasks. The responsible site personnel should develop the procedure from the actual installation and applicable equipment instructions. The purchasing documents should make the required isolation hardware and access visible, so those items are not left outside every supplier's scope.
Keep the air-system maintenance plan separate from the material-handling maintenance plan while showing their interfaces. A change to a treatment element, connecting valve or process sequence can affect the shared delivery condition. Record who approves such changes. This supports future modifications without turning an early project assumption into a permanent but undocumented operating rule.
Use a common quotation comparison sheet
Ask suppliers to return the same technical schedule
A specification for compressed air for pneumatic conveying should keep the air source and process duty connected throughout quotation review. Use the interface identifier on the technical schedule and the equipment drawing so each proposed delivery condition has a clear destination.
Send the same duty matrix, interface definition and site conditions to each bidder. Ask each supplier to return the proposed model, performance basis, scope and exclusions against that schedule. Highlight differences rather than force incompatible offers into a single price column. A proposal with more included equipment may answer a different scope from an apparently lower-priced alternative.
Make unresolved conditions visible in the comparison. Examples include final route information, a material test requirement or a utility condition awaiting confirmation. Assign a decision date and owner to each item. This is more useful than labelling every incomplete proposal compliant and leaving the project team to discover the differences during installation.
Evaluate operating cost from documented inputs
Build any cost calculation from the expected operating schedule, the selected equipment's documented performance and the plant's own tariffs. Keep each operating case separate when the required delivery changes. Include relevant auxiliary and treatment consumption within the agreed scope. Do not compare one proposal's complete package input against another proposal's motor rating.
If the production schedule is uncertain, present the missing inputs rather than invent an annual saving. A transparent worksheet can be updated as production planning develops. It should identify the purpose of the calculation, its units and its limitations. Purchase decisions can then use a traceable comparison instead of an unsupported percentage attached to an equipment category.
Agree acceptance before the package is ordered
Separate air delivery from material-transfer performance
The air package should be assessed against the agreed supply conditions at the defined boundary. The conveying system should be assessed against its own process requirements and scope. Link the operating cases, but preserve the separate conclusions. A successful material transfer does not automatically document every air-quality requirement, and a compliant air reading does not prove the required material throughput.
State which instruments, methods and operating conditions support each acceptance result. Retain the original readings and relevant equipment configuration. The records should allow another person to understand what was actually demonstrated. Avoid an acceptance sheet that records only a general statement that the system operated normally during a short observation.
Include the transitions that matter to production
Choose commissioning cases from the intended operating matrix. Consider the defined start sequence, relevant route combinations and normal transfer completion. Where availability requirements include a particular equipment lineup, assess that lineup through the agreed plan. Do not create an arbitrary demonstration that bears little relation to the way the factory will use the system.
Record deviations and their agreed resolution separately from accepted results. A temporary commissioning arrangement should not silently become the final operating configuration. Confirm the final settings, drawings and responsibility schedule at handover. These records become especially useful when a later production change adds a route, changes material or increases the required transfer frequency.
Build a useful process-to-air troubleshooting record
Capture the event before deciding which package caused it
If a transfer does not reach its intended result, record the process step, route and material batch involved. Add the air pressure and flow observations at their named measurement points. Include the status of the receiver, conveying controls and air package. This creates a common event record that both suppliers can interpret without assuming that either the material equipment or the air source must be responsible.
Keep the event time consistent across the available records. A compressor trend from one period and a process alarm from another can suggest a relationship that never occurred. Where instruments use different clocks, document that limitation. Ask the project team to agree how records will be aligned before using them to support a diagnosis or a proposed equipment change.
Use a decision table to direct the next enquiry
| Observation | Information to compare | Responsible next step |
|---|---|---|
| Air condition differs between station and process | Simultaneous readings, route and connected equipment | Review distribution and the defined supply scope |
| Transfer changes with material batch | Material information and recorded process sequence | Ask the conveying designer to assess the changed material condition |
| A problem appears only with another route running | Permitted operating matrix and concurrent air demand | Review the combined duty with both suppliers |
| Pressure indication changes during a transfer | Measurement location and active process stage | Compare the event with the approved operating envelope |
| Air delivery appears satisfactory but transport remains poor | Air acceptance evidence and separate process requirements | Continue the process investigation without changing the accepted air duty by assumption |
This table organizes an investigation; it does not assign a cause from a symptom alone. The important distinction is between an observation and a conclusion. For example, a pressure change can be recorded objectively, while its relationship to a transport problem still needs assessment. Keep proposed explanations in a separate field so later evidence can support or reject them without rewriting the original observation.
Handle route extensions and material changes deliberately
A new destination creates a new operating case
When a factory adds a receiving point, send the revised route information to the conveying designer. Ask whether the existing air requirement remains valid and which operating combinations need reassessment. The air package may have unused capacity, but that alone does not establish that the modified conveying system will perform as intended. The complete process requirement still needs to be defined.
Update the operating matrix as well as the drawing. A new line that cannot run together with existing lines has a different duty from an additional simultaneous transfer. Make that distinction explicit in the production plan and control description. It allows the suppliers to review the actual expansion instead of selecting against an overly broad or incomplete interpretation of future demand.
Keep material substitution separate from equipment capacity
A change in raw-material supplier, grade or handling condition should be reviewed through the process owner's change procedure. The relevant question is whether the new material remains within the approved conveying scope. Ask the conveying designer which information is needed to answer that question. Do not assume that additional compressor pressure can compensate for every change in material behavior.
Preserve the original selection documents so the review has a clear starting point. Record the changed input, the suppliers' conclusions and any resulting equipment or operating changes. This makes future enquiries more efficient. The plant can explain what changed and why the previous duty was accepted, rather than reconstructing the project from a sequence of unrelated quotations and operator recollections.
Create a handover file that remains useful
Organize records by interface and operating case
Keep the agreed air schedule, equipment selection and acceptance results together under the relevant interface identifier. Add the current drawing and the final control description. Group commissioning records by the operating case they demonstrate. This structure helps a new engineer find the evidence for a particular route or production condition without reading every document supplied with the project.
Include the boundaries of the accepted scope. A package may be accepted for the documented material and route arrangement without being assessed for every future extension. Clear scope records protect the usefulness of the original acceptance result. They also show where a later review is needed when the plant changes production, rather than suggesting that the original supplier promised unlimited capability.
Make routine operating observations easy to record
A practical shift record can identify the active route, material, relevant air readings and unusual events. It should use the same equipment names as the project drawing. Avoid a form that asks operators to infer technical causes they cannot confirm. A brief, consistent observation is more useful than a confident diagnosis unsupported by the available measurement.
Agree who reviews recurring events and when equipment suppliers should become involved. Keep a record of actions taken and the conditions observed afterward. This links daily operation to the original design without turning normal production monitoring into a repeated commissioning exercise. It also gives the plant a factual basis for the next maintenance, capacity or process-improvement discussion.
Questions to settle before the final enquiry
Can compressor power determine conveying capacity?
No. Motor power alone does not establish the airflow, delivery condition or material-transport performance required by the project. Obtain the conveying duty from the process designer. Then select an air package against that duty and its operating envelope. Keep production throughput and air delivery as separate quantities in the enquiry.
Should every powder system use the same treatment?
No. Material sensitivity, process requirements and equipment instructions determine the treatment scope. Specify the required delivery condition and the relevant operating cases. The selected dryer, filtration and other equipment should answer that schedule. A treatment arrangement used successfully elsewhere can be a discussion reference, but it is not a substitute for this project's requirements.
What should a buyer send to SEIZE AIR?
Send the conveying designer's air schedule, material-transfer description, operating matrix, site conditions and interface drawing. Include the required quality and availability, together with existing equipment the project proposes to reuse. Mark unresolved items so the technical discussion can address them directly.
Use the SEIZE AIR enquiry page to discuss compressed air for pneumatic conveying. A clear duty and supply boundary make it easier to evaluate the appropriate blower or compressor, treatment package and controls. They also provide a practical basis for comparing proposals and confirming what the selected system must deliver.