Choosing a flow meter can be a very overwhelming prospect. Sometimes it can be hard to know where to start. You have to wade through finding out which flow meter technology out there might best serve your application and your budget. Then there are countless manufacturers out there with multiple models all offering something a little different. You also have to ensure that the specific variable of your process fall in line with the specifications of each individual model. Knowing what information you even need to start with can be difficult.
Nobody likes to spend time or waste money that they could have saved with a little preparation. When it comes to finding the best fit for your process application, being organized and thorough can have big payoffs in making sure that all factors are appropriately compensated for in your choice. Accidentally overlooking some variable that ends up in equipment malfunction, damage, or failure can be avoided by asking the right questions at the beginning. Below is a farily comprehensive list of questions to help you build a complete application profile for an optimum selection process.
Price/Customer Service
What do you have in your budget to spend? While it is tempting to think that price needs to always be the first consideration and to think that the lowest priced option is always the way to go, that can lead to headaches down the road. Cheaper models, options, or technologies may not provide the same length of service life, require more maintenance, or may require more downtime for things like calibration. These things all cost money in the long run and should also be added to the total lifetime cost of the instrument. Ask what the average life span of the model you are looking at is.
Also ask about warranties. How long is the instrument covered and does the company you are purchasing from have a known customer service record for supporting their instrumentation in an accessible and personal manner. This can make all the difference in ensuring that an instrument has been correctly installed and to easily troubleshoot any questions that come up as part of that process.
Another aspect is how long will it take to install? Will it require a shut down of a critical existing process that will cost money if it is shut down or can it be installed without this issue?
It is important to think in terms of total value and not just the initial cost. What may be cheaper at first may cost much, much more in the long run.
If you are looking to replace a part that has shut down a process, lead-time for the replacement is also an important consideration. Can you get it fast to get the process back up and running?
Wouldn’t it be nice if you could try one out first to make sure it works? Some companies are open to the idea of suppying short term demo units to ensure that it is the correct solution for the application.
The Basic Process
Who will be using it? What do they need to use it for? Where will it be placed?
Does the process require totalizing or batching capabilities?
Is visual rate indication needed only? Is a switch or transmitter needed? Is local or remote indication needed?
Getting the basic layout of the process and the people involved will help you in selecting certain features.
The Immediate Characteristics/Surroundings to the Place of Installation
What is the size of the pipe and what is it made out of?
Is the environment around the area stable or variable? Is there danger of explosion? Is the area a harsh environment?
What length of straight run of pipe is possible before and after where they instrument will be placed?
Will there be other types of instrumentation placed close to the flow meter on either the upstream or downstream?
Are there space limitations where the installation will need to be that restrict the size that the instrument can be?
Will the installation are require a certain angle that the instrument will be installed at?
Usually limited to a 10:1 turndown
Cannot tolerate coating or crystalizing
Most do not handle large solids or debris
Has defined operating conditions
Changes in SG, pressure, and viscosity cause significant reading errors
Must be calibrated for density, viscosity, and compressed gases
Orientation must be vertical installation, with flow from bottom to top in most cases
Non-transparent liquids obscure reading the float
Not good for pulsating flow
Without protection, glass/plastic tube models can break
Laboritories
Chemical Injection
Boiler Control
Purge Applications
Flitration Loading
Process Analyzers
Early warning for clogged systems
Lube Oil
Coolant Flow
Liquids or gases
Suitable for a wide variety of media
Low to medium viscosity
Minimal large particulate matter
No significant coating or crystalizing