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CL in methanol distillation wastewater

2009-03-18View Original

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Should there be no chloride ions in normal methanol distillation wastewater? If it reaches 30PPM, does it necessarily mean there is a leak in the wastewater cooler, or in one of the water coolers in that tower?
Reply #22009-03-20
On the second floor, you have facilities for methanol extraction there. Could you share some experience? I am interested in carrying out extraction using a ternary system of methyl acetate, methanol, and water.
Reply #32009-03-20
The composition of the extraction water in our factory is still DW, and the chloride content in DW is definitely below 10PPM. Only the CW with additives has a high value, right?
Reply #42009-03-20
Adding extractant water is intended to allow the formed methanol azeotrope to be separated from methanol, so that low-boiling compounds can be removed during distillation to obtain high-purity methanol
Reply #52009-03-20
Of course, there should be no chloride ions (in the ppb range) during the synthesis phase; if present, they can poison the synthesis catalyst. Therefore, it is most likely that they are introduced by the extraction water
Reply #62009-03-20
Is it because of the high chloride content in the alkaline solution? We’re using industrially pure material, so the chloride content should be high; it’s just my guess. You might as well give it a try!
Reply #72009-03-21
It shouldn’t be a water issue. Generally, deionized water is used for extraction. It’s impossible for chloride levels to be too high. Could it be a problem with the alkaline solution? It could also be a leak in the crude methanol preheater.
Reply #82009-03-21
The distillation wastewater at the bottom of the tower is generally assumed to have a H2O content of 99.5%, CH3OH content of 0.1%, and a content of other alcohols of 0.4%. The influence of perchloride ions is not taken into account. The material used for the heat exchanger is also assumed to be carbon steel.
Reply #92009-03-21
The wastewater from our plant is sent to gasification coal grinding; the flow rate of the wastewater pump remains constant. Therefore, when the amount of wastewater increases, we need to find out the reason for this. A reboiler is impossible; there’s none even in the steam ; The pressure tower and the three-tower water coolers can’t leak; otherwise, the moisture content of the finished product would already be high ; Methanol synthesis cannot exceed a certain limit, so I suspect the issue lies in the tower and the wastewater cooler. As for the chloride content in the alkaline solution, that wasn’t taken into account; thanks for pointing it out. I’ll go check it after work
Reply #102009-03-22
It has been analyzed: the chloride content before the wastewater cooler is 2.0 PPM, while it is 26 PPM after the cooler. 10PPM in alkaline solution

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