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Methanol distillation water solubility problem

2009-12-08View Original

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This post was last edited by Qingfeng Liushui on 2009-12-9 09:35 In the later stages of use of synthetic catalysts, refined methanol has poor water solubility. The situation is as follows: 1. The device is a natural gas methanol production device. The synthesis tower is a Lurgi uniform temperature type. It is equipped with TOPSOE's MK series catalyst. It is currently in the late stage of catalyst use. The synthesis bed temperature is about 255 degrees Celsius. ; 2. The methanol content at the entrance of the synthesis tower is high, and the synthesis wax formation is serious. ; 3. The distillation system adopts the classic two towers, which are floating valve towers. ; 4. Methanol products have poor water solubility and will appear white and turbid after adding water (1+3). Measures taken and their effects: 1. Increase the reflux ratio of the main tower: The reflow ratio has been increased to about 3.8, and the quality has improved slightly. ; 2. Appropriately lower the temperature of the sensitive board: The sensitive board has dropped to about 80 degrees Celsius, and the quality has improved slightly. ; 3. Increase the heat of the pre-tower, increase the venting volume of the pre-tower, and increase the reflux temperature of the pre-tower and main tower.: Basically no change in quality ; 4. Increase the amount of alkali added: Water solubility has basically no effect ; 5. When the extraction water is added (because it can only be added to the entrance of the pre-tower and cannot be added to the reflux tank), the water solubility of the product will basically remain unchanged. ; 6. Increase the extraction of alcohol from the main tower: Basically no impact. discuss: 1. Is it necessary to add water to dilute methanol? The concentration of synthesized methanol is only 84%. In the past, products without adding water were also good. ; 2. The phenomenon of poor water solubility will occur after the synthesis system is continuously heated several times. ; 3. The sample taken from the reflux tank in the pre-tower becomes very turbid (white like milk) after adding water. ; 4. The filter entering the tower is frequently blocked by paraffin and needs to be cleaned basically every 2 days. I suspect that paraffin (C5-C10 alkanes) cannot be eliminated in the pre-column and forms an azeotrope in the main distillation column and is brought into the product. Most of the measures that can be taken have been tried, but the results are not good. I would like to ask colleagues for their methods and experience in solving this problem.
Reply #22009-12-08
Change the position where the extraction water is added. Maybe it is due to insufficient mixing. The azeotrope in methanol has been evaporated into the reflux tank without mixing. Maybe you can lower the feed temperature and see if it works. If not, change the position where the extraction water is added. However, we do not add it at the inlet now, but add it to the reflux tank.
Reply #32009-12-09
Please ask again: 50t/h crude methanol has a concentration of 84%. How much extraction water should be added? is 50 * 20%=10t/h? Then the feed will be 60t/h, and the steam consumption will increase a lot?
Reply #42009-12-09
It is recommended that a complete analysis of the crude methanol must be done. The paraffin described to the poster is already quite large, and as the temperature decreases, the filter is clogged more and more times. Solving the problem of paraffin mainly involves synthesis. I have seen that some crude alcohols have basically no paraffin, which has a lot to do with the quality of the catalyst. Distillation focuses on controlling alkane azeotropes. If adding extraction water to the reflux tank has a great impact on the balance of the pre-column, be cautious in modifying it. Appropriately increase the extraction of fusel alcohols. Regarding the amount of extraction water added, although the methanol concentration is not high, you have too many alkanes. It is recommended to increase the amount of extraction water. For comparison, what is your current prognosis proportion? I hope you can provide more data.
Reply #52009-12-09
This post was last edited by wwj728 on 2009-12-10 09:22 Prognosis Methanol PH 10.05 Specific Gravity: 0.88

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