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Swift Sensors cloud wireless sensor system

Thu, 08 Dec 2016 15:18:07 -0500

The unified sensor system delivers real-time actionable data and monitors temperature, humidity, vibration, motion, activity, location, electric voltage and current.

Testing a First-Order Plus Deadtime model

Thu, 08 Dec 2016 12:34:00 -0500

FOPDT model has demonstrated utility for controller tuning rules, for structuring decouplers and feedforward control algorithms.

Memosens CLS82D four-electrode sensor

Wed, 07 Dec 2016 13:41:47 -0500

Measures conductivity from 1 µS/cm to 500 mS/cm and temperature from 23 to 248 °F (-5 to 120 °C) with 4% accuracy 0.2% repeatability.

GE ‘all in’ on digital transformation

Wed, 07 Dec 2016 13:20:00 -0500

Strategic acquisitions, organic investments and customer wins showcased at 2016 Minds + Machines event.

Product roundup: Terminal blocks and I/O

Wed, 07 Dec 2016 12:02:00 -0500

Because they're the crossroads, nexus and Grand Central Station for sensor signals and data arriving and requests and actuation instructions departing, it's a big help that I/O and terminal blocks are more flexible and capable than ever.

Neptune Series MP7000 mechanical diaphragm metering pumps

Tue, 06 Dec 2016 16:05:17 -0500

Oversized check valves, straight-through flow design and elimination of the contour plate improve flow characteristics for viscous, shear-sensitive and fluids with suspended solids.

Emerson Automation Solutions offers new tools for reliable, safe level measurement

Tue, 06 Dec 2016 14:59:00 -0500

Includes SIL 3-capable Rosemount 5408 Series non-contracting, radar level transmitters for continuous measurement and Rosemount 2140 vibrating-fork, liquid-level detector with wired HART for point-level measurement

PID Loop Tuning Pocket Guide version 5 now available

Tue, 06 Dec 2016 11:04:00 -0500

ControlSoft Inc.’s PID Loop Tuning Pocket Guide has been expanded. This 12-page publication includes a short, easy-to-use guide for tuning PID loops, along with updated controller references for many of the more common controllers on the market today.

Seven new members join Rockwell Automation’s Machinery Safety System Integrator program

Mon, 05 Dec 2016 17:19:00 -0500

Additions bring total number of participants to 33

Resource Guide: the latest in level measurement

Mon, 05 Dec 2016 14:14:00 -0500

Control's monthly guide brings you invaluable industry information to stay up to date on the latest trends and developments.

Pentair’s Hoffman PROLINE G2 modular enclosure

Mon, 05 Dec 2016 13:34:40 -0500

Able to bear the heavy loads of industrial applications, faster to assemble, and easier to populate electrical and electronic components.

Aurora is real and has caused damage

Sun, 04 Dec 2016 20:49:00 -0500

In preparation for a new book, I was able to find information about an actual Aurora event. The event affected a non-utility facility (no generator involved) where it experienced multiple Aurora events over a multi-day span resulting in damage to motors.

Deadtime Dominance - Sources, Consequences and Solutions

Thu, 01 Dec 2016 20:30:00 -0500

If the total loop deadtime becomes larger than the open loop time constant, you have a deadtime dominant loop. There is a lot of misunderstanding posed by this difficult challenge including a lot of prevalent myths.  Here we look at how we get into this situation, what to expect and what to do. Deadtime is the ultimate limit to loop performance. A controller cannot correct for a disturbance until it starts to see a change in the process variable and can start to change the manipulated variable (e.g., flow). If the deadtime was zero, the controller gain could be set as large as you want and the peak and integrated errors made as small as you want provided there is no noise. The PID gain could theoretically approach infinity and lambda approach zero. Without deadtime, I would be out of job. Sources Fortunately, deadtime dominant loops where the deadtime is much larger than the open loop time constant, is usually relegated to a few loops for processes involving liquids and gases.  Deadtime dominance typically occurs due to transportation delays (deadtime = volume/flow), cycle times of at-line analyzers (deadtime = 1.5 x cycle time, or improper setting of PID execution rates or wireless update rates (dead time = 0.5 execution or update rate time interval). Deadtime dominance due to transportation delay is more common in the mining industry and other processes that are primarily dealing with solids. Large transportation delays result from conveyors or feeders or extruders where the feed of solids are manipulated at the inlet and the quality or quantity is measured at the outlet (discharge) assuming the sensor lag is much less than the transportation delay (i.e., total loop deadtime). The use of a gravimetric feeder can eliminate the delay for feed flow control making a much more precise and responsive loop.  A kiln has a temperature sensor lag that creates an open loop time constant that is usually larger than the transportation delay. However, the use of an optical sensor (e.g., pyrometer) for temperature control eliminates this lag possibly making the loop deadtime dominant. In vessels and pipes where there is no axial mixing, also known as back mixing due to an agitation or recirculation or sparging, there is no mixing up and down in the vessels and mixing forward and backwards in the pipe. We call this plug flow. There may be radial mixing, to make the concentration or temperature in a cross section of the vessel or pipe more uniform or to keep solids dispersed. Radial mixing does not reduce transportation delays whereas axial mixing eliminates plug flow decreasing transportation delays. Any remaining delay from axial mixing depends upon the degree of mixing. For vessels with good geometry and axial agitators, the delay is approximately the turnover time that is the volume divided by the summation of the agitator pumping rate, recirculation rate and feed rate.       Deadtime dominance usually doesn’t occur in temperature loops except for inline systems, such as plug flow liquid or polymer reactors where there is negligible heat transfer lag in the equipment or sensor.   Consequences For a deadtime dominant system, the peak error for a step load disturbance approaches the open loop error (error if loop is in manual). Better tuning and feedback control algorithms cannot do much to improve the peak error. There can be a significant improvement in the integrated error by better tuning and feedback algorithms for a load disturbance but the ultimate limit to the integrated error is the peak error multiplied by the deadtime. Solutions The best solution is to eliminate the deadtime that is the source of deadtime dominance by better process, equipment or automation system design. The next be[...]

List of major big data tools

Thu, 01 Dec 2016 13:52:00 -0500

Software packages, data management and storage methods, new communication protocols, programming tools, and cloud-computing services from the IT side.

Plan for big data success

Wed, 30 Nov 2016 14:48:00 -0500

Big data can only help users if they understand what it is, how it can affect their controls and processes, and how they can use it to optimize operations.

Rockwell Automation’s FactoryTalk TeamONE app

Wed, 30 Nov 2016 14:07:27 -0500

Aims to boost team productivity by enabling users to collaborate and share knowledge, view live production diagnostics, interact with machine alarms, and troubleshoot devices.

ICC 2016: Clarksville utilities automate securely

Wed, 30 Nov 2016 11:44:00 -0500

Electricity, water, wastewater services in Arkansas city establish secure network and SCADA to optimize operations and assist economics

Improve business results at the operator interface

Tue, 29 Nov 2016 18:20:00 -0500

Powerful connectivity, integration and visualization lead to better decisions in real time.

Reduce the cost of tank blanketing

Tue, 29 Nov 2016 18:06:00 -0500

Tank blanketing with nitrogen prevents contamination, leaks, and explosions. Download FCI's Tank Blanketing White Paper to learn how FCI’s ST100 Air/Gas Flow Meter provides precise flow measurement to reduce the cost of inert gases.

ICC 2016: Predictive analytics at Sierra Nevada Brewing

Tue, 29 Nov 2016 16:14:00 -0500

Sierra Nevada's David Lewis explores how the company set out to achieve proactive identification of failing RTDs and improve its data visualization tools.