『Ammonia flowmeter』Related information(clamp on meter|electromagnetic meter|venturi meterrotameter|orifice meter|ultrasonic flow meter|mass flow meter|coriolis mass flow meter|coriolis flow meter|magnetic flow meter|magmeter flow meter|magflow flow meter|mag meter flow meter|electromagnetic flow meter|vortex flow meter|turbine flow meter|thermal mass flow meter|thermal flow meter|rotameter flow meter)

1. How to calculate the actual gas volume in the ammonia decomposition purifier and decomposition furnace flowmeter? In the ammonia decomposition hydrogen purification equipment, liquid ammonia needs to be heated to 800-850 ℃ and decomposed under the action of nickel based catalyst to produce a mixed gas containing 75% hydrogen and 25% nitrogen for sale. Liquid ammonia first enters the vaporizer through the ammonia inlet valves F
1 and F2
(1). The vaporizer is equipped with an electric heating element to maintain the water temperature at 45-60 ℃ to achieve vaporization of liquid ammonia. The pressure of vaporized ammonia is generally controlled at 0.4-0.5MPa, and after being reduced to 0.05MPa, it is measured by a corrosion-resistant flow meter. These ammonia gases enter the heat exchanger and, through heat exchange, their temperature rises. The high-temperature mixed gas is cooled by the decomposition furnace, and the heated ammonia enters the decomposition furnace to decompose into a hydrogen nitrogen mixture. The decomposed high-temperature mixture enters the heat exchanger, is further cooled by the water cooler, and finally sent to the place of use. If the purity of the hydrogen nitrogen mixture needs to be improved, an FC type purification device can be used for processing. In the process flow of the device, two adsorption dryers work in parallel, with one running while the other can be regenerated to ensure continuous operation of the equipment. The dryer operates at room temperature and is heated to 350 ℃ for air flushing regeneration. The decomposed mixed gas enters a group of dryers through valve F14, utilizing the co adsorption of NH3 and H2O by molecular sieves, while adsorbing residual ammonia


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