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How to address liquid carryover in the MTO gas-phase methanol feed

2015-12-16View Original

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This post was last edited by lzy4225925 on 2015-12-16 at 16:31. It is said that liquid in the MTO gaseous methanol feed can cause the reactor to malfunction or stop operating. This liquid tends to accumulate in the lower part of the U-shaped section of the feed pipeline. So, what methods can be used to get rid of this liquid?
Reply #22015-12-16
Add it to the lower part? Is it actually used?
Reply #32015-12-17
Accumulation of fluid in the U-tube is usually caused by insufficient insulation, and this issue can be resolved by adding heating. Also, I’m not very familiar with the MTO process specifically – shouldn’t the methanol vapor fed into it be superheated? Is it saturated?
Reply #42015-12-17
The feed is gasified methanol; crude methanol contains a certain amount of water, which can cause liquid accumulation at the U-tube section
Reply #52015-12-17
Generally, the methanol fed into the system is vaporized, and then a superheater is used to heat it further in order to ensure a certain degree of superheat. From what I’ve seen of the DMTO process, superheating is also required; however, it seems that liquid methanol is mixed with the superheated methanol in order to control the degree of superheat. I’m not sure what your process flow is; it would be best to check whether there is any impact on the superheat of the methanol vapor fed into the system
Reply #62015-12-17
After passing through the methanol steam heat exchanger, methanol flows through the U-tube section, then goes through the large heat exchanger, and finally enters the reactor directly, without going through a superheater
Reply #72015-12-17
By ‘Dali exchange’ you are referring to the heat exchange between the reaction gas and methanol vapor, right? That’s the superheater; there must be some issues with your piping or equipment layout At least allow the condensed liquid to flow back to the methanol-vapor heat exchanger by gravity. For now, it seems necessary to use steam for heating, but the temperature and pressure of this heating steam cannot be too low; otherwise, it won’t be effective.
Reply #82015-12-17
Yes, but how can the condensed liquid flow back to the methanol vapor heat exchanger on its own?
Reply #92015-12-17
Those are the things to keep in mind when arranging the equipment and installing the piping. . You can go and check the layout of your pipes on site to see if there are any opportunities for optimization.

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