admin_zero, Author at Just Measure it

admin_zero

Small Signal Cutoff in Process Instrumentation: A Practical Guide

What Is Small Signal Cutoff? Have you ever encountered these situations? The pipeline is completely stopped, but the flowmeter still displays 0.2 m³/h. The process has been shut down, yet the totalized flow continues to increase. The DCS constantly shows a tiny flow value even though there is no actual flow. In many cases, the […]

Small Signal Cutoff in Process Instrumentation: A Practical Guide Read More »

Electromagnetic Flowmeter Shows Zero Flow? Check the Pipeline Before Blaming the Instrument

The Flowmeter Was Powered On, But the Flow Reading Stayed at Zero In industrial applications, one of the most common complaints about electromagnetic flowmeters is: “The flowmeter is installed, powered on, but the display shows 0.00 m³/h even though the system is running.” When this happens, many users immediately suspect the flowmeter itself: The sensor

Electromagnetic Flowmeter Shows Zero Flow? Check the Pipeline Before Blaming the Instrument Read More »

Industrial Communication Interference Troubleshooting Guide: Causes, Symptoms and Solutions

Why Do Industrial Instruments Suddenly Lose Communication? In industrial automation systems, engineers often encounter frustrating communication problems: Instrument data jumps randomly Measured values fluctuate abnormally Communication becomes unstable or frequently disconnects PLC, HMI, or SCADA systems lose connection unexpectedly Sensor signals become noisy and unreliable Many engineers try to modify communication parameters repeatedly, such as

Industrial Communication Interference Troubleshooting Guide: Causes, Symptoms and Solutions Read More »

Why PID Tuning Is Not Always the Answer: A Systematic Approach to Solving Process Control Problems

Introduction When a process control system becomes unstable, many engineers immediately focus on PID tuning. Adjusting proportional gain, integral time, or derivative settings is often considered the first solution. However, in real industrial applications, not every control problem is caused by incorrect PID parameters. A control loop is a complete system consisting of: Controller (PID)

Why PID Tuning Is Not Always the Answer: A Systematic Approach to Solving Process Control Problems Read More »

Why Are High-Strength Bolts Often Black?

In steel structures, bridges, equipment installation, and other engineering projects, high-strength bolts are often black or dark gray. Because this appearance is so common, many people naturally associate a black bolt with a high-strength bolt. That impression is understandable. High-strength bolts used in steel structures, particularly large hexagon-head high-strength bolt assemblies, are frequently supplied with

Why Are High-Strength Bolts Often Black? Read More »

Why External Tank Level Measurement Is Becoming a New Solution for VOC Emission Control

Introduction Volatile Organic Compound (VOC) emissions from storage tanks have become an increasing concern in the oil, chemical, and petrochemical industries. For many storage tanks, especially floating roof tanks and large atmospheric tanks, level measurement traditionally relies on internal components such as guide pipes, stilling wells, gauge wells, or other tank penetration structures. These openings

Why External Tank Level Measurement Is Becoming a New Solution for VOC Emission Control Read More »

FAT vs SAT vs SIT in DCS Projects: Understanding Automation System Testing and Acceptance Process

In a DCS (Distributed Control System) project, successful commissioning does not depend only on drawings, configuration documents, or manufacturer specifications. A system must be tested and verified step by step before it can be safely put into operation. In a complete DCS project lifecycle, FAT, SAT, and SIT are three critical testing stages. Many people

FAT vs SAT vs SIT in DCS Projects: Understanding Automation System Testing and Acceptance Process Read More »

Pressure Transmitter Failure Causes: Why Diaphragm Selection Matters More Than You Think

In industrial applications, pressure transmitter failures are not always caused by poor instrument quality. In many cases, the real problem starts from the beginning — incorrect diaphragm selection. The diaphragm is the first barrier between the process medium and the pressure transmitter. If the diaphragm material, filling fluid, or structural design does not match the

Pressure Transmitter Failure Causes: Why Diaphragm Selection Matters More Than You Think Read More »

Laminar Flow vs Transitional Flow vs Turbulent Flow: Why Instrument Engineers Must Understand Flow Conditions

Many instrument engineers and technicians have a common question: “I work with instruments, calibration, and maintenance. Why do I need to understand laminar flow, transitional flow, and turbulent flow?” After all, fluid dynamics seems like a topic for process engineers rather than instrumentation specialists. However, in real industrial applications, many flow measurement problems are not

Laminar Flow vs Transitional Flow vs Turbulent Flow: Why Instrument Engineers Must Understand Flow Conditions Read More »

Temperature and Pressure Compensation for Orifice Flow Meters: Calculation and PLC/DCS Implementation Guide

Introduction Orifice flow meters are widely used for measuring the flow rate of gases, steam, and liquids in industrial processes. However, when measuring compressible fluids such as gas and steam, the flow measurement accuracy can be significantly affected by changes in operating temperature and pressure. The reason is that the density of a compressible fluid

Temperature and Pressure Compensation for Orifice Flow Meters: Calculation and PLC/DCS Implementation Guide Read More »

Translate »