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Transformed water vapor ratio

2016-05-23View Original

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Dear sea friends, how is the changing water vapor ratio calculated? Which manufacturer produces the online instruments for measuring water vapor ratio, and what is their performance?
Reply #22016-05-23
This post was last edited by 654262293 on 2016-5-25 05:59. As an example: the pressure of water gas is 3.40 MPa (gauge pressure), its temperature is 214.8°C, and the flow rate of wet water gas is 180,000 Nm3/h. The water vapor ratio can be calculated as follows: By referring to the table showing the relationship between saturation temperature and pressure of water vapor, it can be determined that at 214.8°C, the saturated vapor pressure of water vapor is 2.0 MPa (gauge pressure). Vapor ratio = partial pressure of saturated water vapor / partial pressure of water-gas mixture = (2.0 + 0.1) / (3.4 – 2.0 + 0.1) = 1.4. Online sensors for measuring the vapor ratio are rarely installed in conversion units. In processes such as medium-low temperature conversion, full low-temperature conversion, sulfur-tolerant conversion for water-gas slurry production, and sulfur-tolerant conversion for pulverized coal gasification, such sensors have been seen many times; however, there are no instances of online sensors for measuring the vapor ratio being used, as there is no need for them.
Reply #32016-05-24
Is there a formula that allows the calculation of the water vapor ratio without the need to refer to a table of steam temperature values?
Reply #42016-05-24
On the DCS screen, the water vapor ratio is calculated using software. Does anyone know how to do this and what the results are like?
Reply #52016-05-24
This post was last edited by 654262293 on 2022-3-11 19:16
Reply #62016-05-25
Yunnan Dada has DCS screens available; you can ask about them
Reply #72016-06-20
At this temperature, the saturated vapor pressure of water divided by the total pressure minus the saturated vapor pressure of water
Reply #82016-09-13
The actual water-vapor ratio is higher than the calculated value; since it is not an ideal gas, the calculated value must be divided by a compression factor. The specific value can be found in textbooks on chemical engineering principles, and it is generally around 0.8

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