Accurate measurement and control of moisture in gases are essential in industrial processes such as semiconductor manufacturing and technical gas production, where low water vapour content directly affects product quality and reliability. Existing systems for calibrating hygrometers are highly accurate but are often too slow under ultra-dry gas conditions, as drying the system is very slow due to the desorption of water from internal surfaces. The aim of this thesis is to design and construct a system that could shorten the time required for hygrometer calibration.
The thesis first introduces the fundamentals of hygrometry and the key quantities used to describe water vapour content in gases, namely relative and absolute humidity, volumetric concentration, specific humidity, and dew point. This is followed by an overview of hygrometers used for measuring low water vapour concentrations, including spectroscopic, capacitive, and chilled-mirror types, together with their measurement principles, advantages, and limitations.
Based on the reviewed technologies, a hygrometer calibration system was designed and constructed. The system uses high-purity nitrogen (5.0N) as a carrier gas, which passes through a molecular-sieve filter before entering a calibration cell made of 316L stainless steel. An exchangeable permeation tube made of polyamide (PA) is installed inside the cell, while the dew point of the gas at the system outlet is measured using an MBW 373LX dew-point hygrometer.
The performance of the system was evaluated by a continuous four-day measurement of the dew point at the system outlet. The measurement consisted of two consecutive parts. The permeation tube was empty at the start, so the system was first only drying, and the dew point fell from −2.7 °C to −62.1 °C over 52 h. Once this minimum was reached, water was introduced into the tube, which caused the dew point to rise to −53.7 °C by the end of the measurement.
The measurement showed that drying the system is slow and requires more than two days of continuous operation, whereas after the water was introduced the system approached its new operating point within about ten hours. Establishing an operating point is therefore faster than drying the system, which enables rapid switching between operating points using several permeation tubes installed in parallel, drying would be required only when the system is first brought into operation.
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