Methanol Purification Version – One Question per Day 20200312
Thread Content
Why is the liquid level in the methanol separator an important process parameter? What is the value of the indicator? Answer: If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can cause liquid slugging, damaging the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions ； If the liquid level is too low, gas intrusion accidents can occur; high-pressure gas can enter low-pressure equipment systems, leading to explosions. Therefore, the liquid level should be maintained between 30% and 50%.
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can lead to liquid slugging, which damages the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions； If the liquid level is too low, air ingress accidents are likely to occur; high-pressure air entering low-pressure equipment systems can lead to explosions. Therefore, the liquid level should be maintained between 30% and 50%. It is generally easy to adjust at around 40%
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can lead to liquid slugging, which damages the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions； If the liquid level is too low, air ingress accidents are likely to occur; high-pressure air entering low-pressure equipment systems can lead to explosions. Therefore, the liquid level should be maintained between 30% and 50%. It is generally easy to adjust at around 40%
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can lead to liquid slugging, which damages the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions； If the liquid level is too low, gas intrusion accidents can occur; high-pressure gas can enter low-pressure equipment systems, leading to explosions. Therefore, the liquid level should be maintained between 30% and 50%.
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can lead to liquid slugging, which damages the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions； If the liquid level is too low, gas intrusion accidents can occur; high-pressure gas can enter low-pressure equipment systems, leading to explosions. Therefore, the liquid level should be maintained between 30% and 50%.
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can lead to liquid slugging, which damages the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions； If the liquid level is too low, air ingress accidents are likely to occur; high-pressure air entering low-pressure equipment systems can lead to explosions. Therefore, the liquid level should be maintained between 30% and 50%. It is generally easy to adjust at around 40%.
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can lead to liquid slugging, which damages the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions； If the liquid level is too low, air ingress accidents are likely to occur; high-pressure air entering low-pressure equipment systems can lead to explosions. Therefore, the liquid level should be maintained between 30% and 50%. It is generally easy to adjust at around 40%.
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can cause liquid slugging, damaging the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions. If the liquid level is too low, air ingress accidents are likely to occur; high-pressure air entering low-pressure equipment systems can lead to explosions. Therefore, the liquid level should be maintained between 30% and 50%
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can lead to liquid slugging, which damages the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions； If the liquid level is too low, gas intrusion accidents can occur; high-pressure gas can enter low-pressure equipment systems, leading to explosions. Therefore, the liquid level should be maintained between 30% and 50%.
If the liquid level in the separator is too high, the liquid will be carried into the circulation section along with the gas; in severe cases, this can cause liquid slugging, damaging the compressor. Moreover, an increased methanol content in the gas entering the tower deteriorates the reactions taking place within the synthesis tower and exacerbates the formation of side reactions. If the liquid level is too low, air ingress accidents are likely to occur; high-pressure air entering low-pressure equipment systems can lead to explosions. Therefore, the liquid level should be maintained between 30% and 50%