What to Prepare Before a First Consultation
When you contact a plant engineering partner for the first time, the conversation usually starts with a general description of your process. That is useful, but it rarely gives the other side enough to propose something concrete. After a few rounds of emails and calls, both parties realize they need specific numbers to move forward. The question is which numbers matter and how to gather them without wasting time.
In the context of continuous-flow chemical plants, the variables that define a valve or actuator specification are not always obvious to a procurement team. Pressure range, fluid composition, temperature profile, and acceptable leakage rate are the obvious ones. But there are others that engineers often forget until the middle of a project: the viscosity at operating temperature, the presence of solid particles, the required response time for a control loop, and the type of electrical or pneumatic signal available in the field.
Below is a checklist of items that help a technical sales engineer or an applications specialist give you a meaningful answer during a first consultation. Having these ready cuts the back-and-forth by at least two days.
Process Parameters
- Operating pressure range (min and max, including transient spikes)
- Fluid temperature at the point of measurement or actuation
- Fluid composition: chemical name, concentration, and any known impurities
- Viscosity at operating temperature (if available, otherwise the fluid type is enough for an estimate)
- Required flow rate range (normal, minimum, and maximum)
Control and Integration
- Type of control signal available (4–20 mA, 0–10 V, digital IO-Link, or discrete)
- Required response time for the actuator or valve (e.g., full stroke in under 2 seconds)
- Existing PLC or DCS brand and communication protocol
- Space constraints: pipe diameter, flange standard, and available mounting orientation
Environmental and Safety
- Ambient temperature range at the installation site
- ATEX or IECEx classification if the area is hazardous
- Acceptable leakage rate (class per ISO 5208 or similar)
- Material compatibility requirements (e.g., no copper, specific elastomers)
Having these points written down before the first call does not mean you need to answer every one. Some are unknown until a site survey. But the act of listing them forces a structured conversation. The person on the other side can immediately see where the gaps are and what needs to be measured or estimated next.
In our experience, the consultations that move fastest are the ones where the client brings a process flow diagram, a datasheet of the fluid, and a clear idea of the control architecture. Even a rough sketch of the piping and instrument diagram helps more than a long email describing the problem in words. Visual information removes ambiguity.
If you are unsure about a parameter, do not guess. Note it as unknown and let the engineer propose a conservative assumption or a measurement method. Guessing a pressure rating too low can lead to a valve that fails in service. Guessing too high adds cost and weight without benefit.