Gas Blending Control; Pipe Schedule and Control Valve Size

Any Thoughts on Where to Go for Reference Material and/or Subject Matter Experts for Help with Controls Engineering Project? Is It Mandatory That Pipe Line Schedule Be Mentioned for Control Valve Sizing?

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"Ask the Experts" is moderated by Béla Lipták, process control consultant and editor of the Instrument Engineer's Handbook (IEH).  Preparation of the 4th edition of Volume 3 "Process Software and Networks" is in progress. If you are qualified to update an existing or to prepare a new chapter, please let me know. Similarly, if you feel qualified to answer questions in this column or want to ask a question, write to me at: liptakbela@aol.com.

Q: I'm looking for some information relative to a controls engineering project I'm working on. I thought you might be able to point me in the right direction. We manufacture large gas-fueled internal combustion engines. Many are designed to run on various types of gases, such as natural gas, propane, digester, landfill gas, etc. In our engineering lab we have a need to mix natural gas with propane or CO2 gases to simulate engine operation in the field across the spectrum of field gases encountered. The project involves coming up with a system to mix two separate streams of these gases continuously across a wide range of mix ratios, with automated ratio control and with automated capability to handle mix demand changes due to decreased/increased demand from the engine fed from the mixer. Precise control of the mix ratio during the transient of a demand change may not be necessary, but there likely needs to be some provision to increase the flow of each stream so the ratio doesn't stray too far. A simple controller could then be used to fine-tune the mix ratio to the desired setpoint once the new demand has been satisfied. I'm envisioning a skid with ordinary gas regulator(s) to handle the demand change, and perhaps a control valve(s) for fine-tuning of the mix ratio. Pressures are low, 60 psig max. We generally look to hold the mix output to a relatively constant outlet pressure. That constant outlet pressure then feeds an engine-mounted gas regulator. We would install one of these systems in every engine test cell. I'm looking more for some guidance as to the appropriate configuration of such a system to provide the functionality required, preferably using standard gas regulator(s), control valve(s), a simple PID controller, etc. These would be lab-only systems. Any thoughts on where to go for reference material and/or subject matter experts for help with this project?

John Swanson
john.swanson@dresser.com

A: Below you will find the configuration of a blending system (Figure 1). The power output of the engine can be modulated by varying the total flow setpoint of FIC-1.

The fuel blend ratio of the gases can by adjusted by varying the setpoint of the ratio setting of FY. The setpoints can also be adjusted manually or automatically. If automatic blend composition control is needed, you need to measure the blend composition and arrange the composition controller to act as the cascade master which is modulating the set point to FY.  

If the plant is controlled by microprocessor-based digital control or DCS systems, the configuration of such control loops requires much less effort. If the flow measurement signals are transmitted utilizing bus-based technologies, the associated dead time should be considered in the tuning of the flow ratio control loops because their time constants are short.

Béla Lipták
liptakbela@aol.com

A: This looks like a fine application for control in the field, as provided by Fieldbus Foundation devices and simple laptop applications to configure and control the devices. There's no need for a DCS. But you didn't specify the maximum flow rate and the number of cells to be controlled. The time constant of the valve determines the loop sample rate, which depends on the size of the actuator. Ten times a second is about the maximum sample rate for fieldbus devices. That matches a really small and fast valve. You did say large engines, so maybe not so small. Do you have instrument air for the valves?

You didn't specify the accuracy required, so perhaps something cheaper than fieldbus devices could be used. Digital devices will simplify logging of parameters, though they can cost more. Alarms for out-of-tolerance conditions do not cost extra with fieldbus devices. Do you need mass or volume flow measurement?

The number of loops required has a cost cross-over point between single-loop controllers and a small fieldbus system. Fieldbus Foundation control information can be found Fieldbus Foundation control information can be found beginning at www.fieldbus.org. Ian Verhappen at www.industrialautomationnetworks.com and John Rezabek are founts of non-marketing information. (Editor's Note: John's On the Bus column "Surprise! Field-Based Control Beats DCS".)

My website has a manual for control in the field at http://www.hlq-ltd.com/

Bill Hawkins
bill@iaxs.net

Q: I have a question about sizing for the body of a control valve. Is it mandatory that pipe line schedule be mentioned for control valve sizing? If ye,s then what is the role of pipe schedule in control valve sizing?

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