PRECISION DATA ACQUISITION NI LABVIEW & HW INTEGRATION

DAQ & LabVIEW Engineering Services

Turnkey data acquisition, custom LabVIEW control architectures, sensor signal conditioning, and automated laboratory/factory floor telemetry built on National Instruments hardware.

The Full Data Cycle: Step 1

Capturing Physical Reality

Data Acquisition (DAQ) is the vital first step in your automation journey—the automated collection of data from physical sensors and instruments on the factory floor or laboratory workbench.

By interpreting Thermocouple, Current, or Voltage signals from any transducer, we bridge the gap between physical hardware and your digital database. We design turnkey solutions that don't just "read" data—they allow you to store, display, and analyze it in real-time.

Hardware Control

  • NI, MCCDAQ, & Omega HW
  • Sensor Signal Conditioning
  • PID & Gain Scheduling

Software Logic

  • Custom Front Panel HMI
  • SQL & Azure Logging
  • Auto-Tuning Algorithms
DAQ Signal Interpretation Diagram
SIGNAL MAPPING: THERMOCOUPLE / CURRENT / VOLTAGE

Industrial Case Study

Ethernet-Enabled Manufacturing DAQ System

SAINT-GOBAIN ABRASIVES World-Class Manufacturing | Worcester, MA

Project Scope: Implementation of a high-traceability system for dozens of manufacturing furnaces and hydraulic presses. The objective was to provide data acquisition with component-level serial number tracking across a multi-user shop floor environment.

The Solution: We developed a LabVIEW data acquisition system running on a protected networked terminal server. This central hub controls multiple ethernet-enabled DAQ devices, allowing qualified engineers to interface with a central panel from any location while operators manage production via shop-floor terminals.

The system is configured via Microsoft Excel and includes real-time alarms for over-temp and uniformity. Upon run completion, a VBA script analyzes raw data, calculates cycle metrics, and pushes them to a SQL database for JMP JSL statistical analysis.

System Architecture
Process Flow Diagram

Data Flow Integrity: Real-time writing to *.flat files ensures 100% data preservation during network interruptions, followed by post-run SQL migration for JMP SPC analysis.

Academic Research Case Study

Tank Level PID Controller Simulation

WASHINGTON UNIVERSITY IN ST. LOUIS Dept. Energy, Environmental & Chemical Engineering

Developed for the EECE Department at Washington University, this project required a proof-of-concept simulation for controlling liquid level height in a pressurized research quench vessel. The solution utilized the LabVIEW Control Design and Simulation Module to model fluid entry at a constant rate ($Q_1$) against a PID-controlled outlet valve ($Q_2$) via a PID algorithm with Relay auto-tuning and gain scheduling based on tank pressure ranges.

Key Objective

Establish starting PID Gain values for implementation in a pressurized vessel environment.

Optimization

Utilized LabVIEW Control Design & Simulation Module with PID Relay auto-tuning (Ziegler-Nichols method).

Technical Assumptions
  1. Uniform liquid density throughout.
  2. Straight, vertical tank walls.
  3. Constant Control Volume (CV).
  1. Pump pressure constant throughout run.
  2. No pump time delay (Steady Flow).
WashU Research Simulation Results

Figure 1: Constant volumetric flow in ($Q_1$), PID controlled flow out ($Q_2$).

Physics & Fluid Dynamics

Foundational Mathematical Model

Derivation of the governing non-linear differential equations for liquid height $h(t)$ in a pressurized vessel.

01. Valve Flow Dynamics

Flow through a valve is proportional to the square root of the pressure drop ($\Delta P$):

Equation A
02. Linear Momentum

Conservation of linear momentum for the control volume:

Equation B
03. Derived Model

Assuming constant momentum and density ($\rho \approx c, \gamma \approx 1$):

Equation F

Integrating Bernoulli's principle for incompressible flows:

Bernoulli Equation

Open Loop Simulation Logic

Block Diagram

This nonlinear differential equation for $h(t)$ is integrated numerically by the simulator. Figure 2 (left) shows the LabVIEW block diagram where the control valve is 100% open, establishing the baseline dynamic response of the vessel.

Control Engineering

Closed Loop PID Controller

The controller receives liquid level height in real-time and manages the variable output valve. A lookup table determines the nonlinear $C_v$ value from OEM specifications.

PID Diagram

Ziegler-Nichols Autotuning Results

Initial Gains: $K_c = 10, T_i = 0.1$. After Setpoint Relay experiment:

Gain ($K_c$) 18.39
Reset ($T_i$) 0.14
Rate ($T_d$) 0.00
Gain Scheduling Logic
Gain Scheduling VI

Figure 9: Closed loop simulation with autotuning and gain scheduling as a function of pump pressure.

LabVIEW Front Panel

Final Implementation

Front Panel HMI Design

The final front panel provides real-time visualization of liquid level, PID status, and alarm states. As observed in Figure 13 (left), the output valve fully opens to meet setpoints, then closes just enough to maintain constant setpoint height with zero-overshoot stability.