Valve Archives - Just Measure it

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Should a Cut-off Valve Be Installed in the Inlet and Outlet Pipelines of a Safety Valve?

This seemingly simple question has caused confusion for many companies and designers. Some choose to install cut-off valves, while others don’t, with practices varying widely. But what do the standards say? Are there clear requirements in the regulations? In this article, we will clarify the principles for the installation of cut-off valves in safety valve […]

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Breather Valves Are Not Safety Devices

A Common Engineering Misunderstanding in Atmospheric and Low-Pressure Storage Tanks In the petroleum, chemical, energy, and pharmaceutical industries, atmospheric and low-pressure storage tanks are among the most widely used process equipment.Unlike pressure vessels, the safety of these tanks does not rely on shell strength, but instead depends heavily on the effectiveness of their venting systems.

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Why Control Valves Become Unstable: The Real Problem May Be the Positioner

In process automation, control valves are the final elements responsible for executing the control signal. However, due to friction, fluid forces, actuator limitations, and other mechanical factors, the actual valve position often fails to match the input signal. A valve positioner—commonly referred to simply as a “positioner”—is the key device designed to eliminate this deviation.

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The Key Functions and Applications of Explosion-Proof Junction Box Breather Valves

Explosion-proof junction box breather valves play a critical role in industrial environments, especially in areas where flammable or explosive gases are present. Below are the key functions of breather valves in explosion-proof junction boxes: 1. Maintaining Pressure Balance During operation, the internal pressure of an explosion-proof junction box may fluctuate due to temperature changes, heat

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How to Choose the Right Drive Voltage for Electric Valves: 220V vs. 380V – Key Considerations and Advantages

In chemical plants and automated control systems, selecting the correct drive voltage (220V single-phase vs. 380V three-phase) for electric valves directly impacts the stability of the equipment, energy consumption, and maintenance costs. This article explores how to determine the appropriate voltage based on key selection criteria and highlights the core advantages of each voltage level,

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Purpose of the Three-Valve Manifold Operation Sequence

When operating a three-valve manifold for differential pressure instruments, two principles must always be observed: Never allow the condensate or sealing liquid in the impulse lines to drain. Never expose the measuring element (diaphragm or bellows) to sudden pressure or temperature stress. To achieve this, the three-valve manifold must be operated in the correct sequence

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Should Metal Hoses Be Installed Before or After the Emergency Shut-Off Valve?

In tank farm piping design, both metal flexible hoses and emergency shut-off valves (ESVs) are critical safety components. However, when they appear on the same pipeline, engineers often ask: “Should the metal hose be installed upstream or downstream of the emergency shut-off valve?” This article explains the correct arrangement from the perspectives of functional requirements,

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Understanding the Differences Between Control Valves, Regulating Valves, and Instrument Manifolds

In process automation, the terms control valve, regulating valve, and instrument manifold (instrument valves) are mentioned daily.Although all of them are “valves,” they perform entirely different roles in a process control loop. This article provides a clear engineering-level comparison across system architecture, industry applications, sizing considerations, reliability, and safety. 1. A Simple Control Loop Perspective

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Recommended Downstream Velocity Control After Control Valves

In industrial fluid control systems, the velocity of the medium downstream of a control valve is a key factor affecting system stability, equipment service life, noise generation, and overall operating efficiency. Selecting an appropriate velocity range requires considering the fluid type, thermodynamic conditions, pipeline configuration, and valve design. There is no single universal value, but

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