Understanding the Laureate™ LT Series DIN Rail Transmitter for Batch Controller Pulse Input
The Laureate™ LT Series DIN rail transmitter for batch controller pulse input is a low cost, powerful, and highly accurate batching controller for repetitive fill operations. It uses the FR dual-channel pulse input signal conditioner for turbine flow meters and most industrial pulse-output transducers. Fill operations repeat continually with a programmable delay from 10 ms to 199.99 sec, or based on an external control input.
Item #1/#2/#3 Tracking
Three items are tracked by the batch control software, each scalable to engineering units and displayed on the controller's six-digit LED display. Item #1 is the current batch total, settable to count up from zero to a preset limit, or down from a preset limit to zero. Item #2 can be assigned to grand total or number of batches. Item #3 is the flow rate.
Dual-Channel Signal Conditioning
The same signal is applied in parallel to Channels A and B, used independently: either channel accepts pulse rates from 0.005 Hz to 250 kHz, exceeding the working range of turbine flow meters. Channel A is used for totalizing, scaled mathematically for volume in engineering units. Channel B is used for rate, with frequency determined by timing an integral number of periods over a specified gate time (plus 30 ms and 0-2 periods), then taking the inverse of period — this inverse-period approach allows much greater accuracy and faster update times (up to 25/sec) than conventional rate meters that count pulses over a fixed time interval.
Relay Options and Hysteresis Modes
Relay control is provided by two or four 8A contact relays, or two or four 120 mA AC/DC solid state relays. Relay latching modes are latching or non-latching; active modes are active on or off, active high or low. Hysteresis modes include QA passband mode, split hysteresis, and span hysteresis.
Custom Curve Linearization
The Extended Laureate computer board can display rate based on successive readings and allows exceptionally accurate custom curve linearization — for example, reading out liquid volume or flow rate in a horizontal cylindrical tank based on level reported by a 4-20 mA transmitter. Up to 180 data points are entered into a spreadsheet or text file; the computer calculates spline-fit segments, which are downloaded into the transmitter.
Real-World Batching Applications
- Up/Down Totalizing — pulses are added or subtracted on Channel A based on a direction input on Channel B; counting can also be inhibited by a Channel B input.
- Combining Two Totals — A+B sums two totals; A-B subtracts outflow total from inflow total; A/B ratio applied to two totals helps assure proper mixing of components.
- Up or Down Counting with Preset — a single transmitter handles two repetitive fill operations, counting from zero up to a preset or down from a preset to zero; the dual relay option is required.
- Machine ON Time and Utilization — count AC line cycles and scale to hours for ON time; connect Channel A to switched AC and Channel B to the AC line, applying a 100 multiplier to the A/B ratio for duty cycle percent.
- Custom Curve Linearization — the Extended version transmits scaled rate or total for the same channel at the push of a button, alarms both, and extends the working range and accuracy of flow transducers.
Factory-Calibrated Accuracy
All signal conditioner board ranges are factory-calibrated, with calibration factors stored in EEPROM, enabling field replacement of signal conditioner boards without necessitating recalibration of the transmitter. Factory recalibration is recommended annually.
Where Batch Controller Pulse Input DIN Rail Transmitters Are Used
- Chemical & Liquid Batch Dosing — precise repetitive fill control via turbine flow meter pulses.
- Multi-Component Mixing — combined-total ratio checks for accurate batch composition.
- Dual-Station Fill Lines — two independent preset-based fill operations on one transmitter.
- Machine Runtime & Utilization Tracking — AC-line-cycle-based ON time and duty cycle monitoring.
- Nonlinear Tank & Sensor Linearization — custom curve correction for irregular tank geometry.
- Multi-Point RS485 Batching Networks — daisy-chained transmitters reporting to a central controller.
- OEM Batch Control Instrumentation — DIN rail integration into existing control panels.
Batch Controller Pulse Input DIN Rail Transmitter Frequently Asked Questions
Why does the same input signal get applied in parallel to both Channel A and Channel B, rather than each channel receiving a separate signal?
Documented description specifically explains this is intentional — Channel A and Channel B are used independently on the same pulse signal specifically so that one channel (A) can be dedicated to totalizing while the other (B) is independently dedicated to rate calculation via the inverse-period method; running both functions off the same physical sensor signal, but processed through two independent channels, is what allows simultaneous total and rate tracking from a single flow meter.
Why does the inverse-period method for Channel B rate calculation offer better accuracy than counting pulses over a fixed time interval?
Documented explanation specifically contrasts these two approaches — a conventional method counting pulses over a fixed time window is limited by how many whole pulses fall within that window, while the inverse-period method times an integral number of periods precisely and calculates the inverse, which is documented as allowing both greater accuracy and faster update times than the conventional counting approach, particularly at lower pulse rates where a fixed time window might capture very few pulses.
Does QA passband mode, split hysteresis, and span hysteresis all serve the same underlying purpose, or do they address different control needs?
Documented specification lists these as three distinct, separately selectable hysteresis modes rather than variations of one function — while all three relate to how a relay's on/off transition points are defined around a setpoint, they're documented as separate configuration options, implying each is suited to a different specific application need (such as the QA passband mode's specific fit for pass/fail testing around a target value) rather than being interchangeable descriptions of the same behavior.
Does Item #2 need to be configured as either grand total or number of batches, or can both be tracked simultaneously on one transmitter?
Documented description specifically frames Item #2 as assignable to either grand total or number of batches, phrased as an either/or configuration choice — this indicates Item #2 is a single configurable slot that displays one of these two related but distinct values at a time, rather than the transmitter simultaneously displaying both as separate tracked items.
Why does the batch delay range specifically span from 10 ms up to 199.99 seconds rather than allowing arbitrarily short or long delays?
The documented range (10 ms to 199.99 s) represents the specified selectable delay window between batches, without further detail on why these specific bounds were chosen — practically, the lower bound reflects a delay short enough to be effectively negligible for most fill cycles, while the upper bound of just under 200 seconds provides ample settling time for even fairly slow batch processes, without requiring a separate external timer for longer delays.
Does choosing magnetic relays over solid state relays for batch control change the transmitter's documented accuracy or timing specifications?
No — documented specifications for the relay output boards (contact rating, isolation, latching modes, hysteresis modes) are listed separately from the transmitter's core measurement accuracy specifications (input frequency range, inverse-period timing, output update rate); the relay type selected affects load-switching capability and mechanical/solid-state tradeoffs, not the underlying pulse measurement and totalizing accuracy documented for the FR signal conditioner itself.
Can custom curve linearization be applied specifically to the batch total (Item #1), or only to the flow rate (Item #3)?
Documented capability describes custom curve linearization as extending the working range and accuracy of flow transducers generally, without restricting it to only rate or only total — since Item #1 (batch total) and Item #3 (rate) are both derived from the same underlying signal conditioning and scaling process, the documented linearization capability is consistent with correcting either the totalized or the rate-based reading, depending on where the transducer's nonlinearity actually needs correction.
Does the FR signal conditioner's documented 250 kHz maximum on both channels limit which turbine flow meters can be used with this batch controller?
In practice, no — documented guidance specifically notes this 250 kHz maximum exceeds the working range of turbine flow meters, meaning the vast majority of real turbine flow meter pulse outputs fall well within this documented ceiling; the 250 kHz figure is presented as generous headroom above typical turbine meter output frequencies rather than a practical constraint most installations would need to work around.
Does an external control input for triggering batch fill operations replace the need for the programmable 10 ms-199.99 s delay, or can both be used together?
Documented description specifically presents these as two separate, alternative ways fill operations can be initiated — "repeated continually with a programmable delay... or based on an external control input" — the wording separates these with "or," indicating a given installation is documented as choosing one triggering method or the other for a given fill cycle, rather than the two being combined as simultaneous requirements.
Does relay isolation (250V rms working, 2.3 kV rms test) apply equally to both the magnetic and solid state relay board options?
Documented specification lists relay isolation as a single shared figure (250V rms working, 2.3 kV rms per 1 minute test) applying at the "Relay Output Boards" level generally, rather than listing separate isolation figures for magnetic versus solid state relay variants — this indicates the documented isolation rating is common across the relay board options, while the specific contact ratings (8A for magnetic, 120 mA for solid state) are what genuinely differ between the two relay technologies.
Relay Hysteresis & Deadband Questions From the Field
What specifically is hysteresis in a setpoint-based relay control, and why is it deliberately added rather than triggering exactly at the setpoint?
Documented explanation specifically describes hysteresis as the difference in the transition level when a signal is approached from opposite directions, creating a deadband region where no action takes place between the two transition levels — this is deliberately added specifically because if the input signal is near a single setpoint value with no hysteresis, small noise or signal fluctuation can cause rapid, repeated output transitions, which documented guidance identifies as a cause of excessive wear on relay contacts and other system components.
Does inadequate hysteresis or deadband genuinely cause measurable process settling time problems, or is this mainly a theoretical concern?
It's a documented measurable effect, not just theoretical — one documented field example specifically describes a flow control loop with 5% valve hysteresis taking close to 3 minutes to settle at a new setpoint following a step change, compared to a documented settling time of approximately 20 seconds for the same loop if the hysteresis had been eliminated, illustrating a genuinely large, measurable difference in real settling behavior.
Can too much deadband cause a control loop to oscillate rather than settle smoothly, and if so, why?
Yes — documented explanation specifically describes "limit cycling," where the controller's output changes but the final control element doesn't respond until the deadband is overcome, at which point it moves and often overcorrects the error; this documented mechanism produces sustained oscillation around the setpoint rather than smooth settling, since each correction tends to overshoot before the next deadband-crossing correction occurs.
Does hysteresis in a batch/setpoint context always refer to a single global deadband value, or can hysteresis be configured differently for each direction of transition?
Documented guidance specifically distinguishes multiple named hysteresis and deadband configuration approaches across different control systems — some interfaces define one combined "hysteresis" figure applied symmetrically, while others separately define distinct setpoint and reset-point values whose difference constitutes the effective hysteresis; the specific configuration approach documented as available depends on the particular control system, rather than there being one universal hysteresis definition across all systems.
Does deadband increase the effective variability of a controlled process, even if the deadband itself is a fixed, known value?
Yes — documented analysis specifically states that the presence of deadband directly translates to less precise control and higher process variability, since the process variable is allowed to drift within the deadband range before any corrective action occurs; even though the deadband width itself is fixed and known, its presence is documented as inherently reducing how tightly the process can be held to the exact setpoint.
Is there a documented practical method for measuring how much deadband actually exists in a given control loop's final control element?Yes — documented field practice specifically describes measuring deadband by making small, incremental changes to the controller output and observing the specific point at which the final control element (such as a valve stem) actually begins to physically move; this documented empirical method reveals the real deadband present in the mechanical system, which may differ from a theoretical or nameplate specification.
Does a setpoint switch's documented "repeatability" specification relate directly to its hysteresis figure, or are they separate specifications?
They're documented as related but distinct concepts — repeatability is documented as the switch's ability to actuate reliably at the desired setpoint within sensor tolerance across repeated cycles, while hysteresis (or the associated deadband) is documented specifically as the difference between the setpoint and the separate reset point at which the switch returns to its original state; a switch can have a well-documented, consistent hysteresis figure while its repeatability describes a related but separate measure of cycle-to-cycle consistency.
Can hardware-level component wear (such as valve linkage backlash) contribute to effective deadband, independent of any electronic hysteresis setting?
Yes — documented guidance specifically identifies mechanical factors like loose or worn actuator linkages as a genuine, physical source of deadband, separate from any electronically configured hysteresis setting; documented best practice specifically recommends using high-performance actuators and tight, backlash-free linkages precisely because mechanical deadband adds to whatever deadband is separately configured at the control or instrumentation level, compounding the overall effective deadband the process experiences.































