| 摘要 |
There are provided a dividing wall distillation column for producing high-purity acrylic acid, and a fractional distillation method using the same. The dividing wall distillation column includes a condenser, a reboiler and a main column having a dividing wall. Here, the main column is divided into a column-top zone, an upper feed zone, an upper outflow zone, a lower feed zone, a lower outflow zone and a column-bottom zone. Accordingly, since one distillation column can be used to realize the same effect as that obtained from the use of two distillation columns, the dividing wall distillation column can have an effect of reducing the costs of equipment to produce high-purity acrylic acid, as well as an energy-reducing effect, compared to a conventional process system. |
| 主权项 |
1. A dividing wall distillation column comprising a condenser, a reboiler and a main column having a dividing wall,
wherein the main column is divided into a column-top zone, an upper feed zone, an upper outflow zone, a lower feed zone, a lower outflow zone and a column-bottom zone, a raw material having an acrylic acid content of 90% by weight or more flows in a middle inflow plate in which the upper feed zone and the lower feed zone come in contact with each other, a low boiling point component flows out from the column-top zone, a high boiling point component flows out from the column-bottom zone, and a middle boiling point component flows out through a middle outflow plate in which the upper outflow zone and the lower outflow zone come in contact with each other, wherein the middle boiling point component is acrylic acid, wherein the number of plates provided respectively in the column-top zone, the upper feed zone, the upper outflow zone, the lower feed zone, the lower outflow zone and the column-bottom zone is in a range of 80 to 150% of a theoretical plate number, as calculated from a distillation curve, wherein a length of the dividing wall is in a range of 30 to 85% of the total theoretical plate number in the column-top zone, the upper feed zone, the lower outflow zone and the column-bottom zone, as calculated from the distillation curve, wherein a temperature of the column-top zone is in a range of 55 to 65° C. at a pressure of 4.666 kPa, in a range of 50 to 60° C. at a pressure of 3.333 kPa, and in a range of 60 to 70° C. at a pressure of 6.666 kPa, wherein a temperature of the column-bottom zone is in a range of 90 to 100° C. at a pressure of 4.666 kPa, in a range of 85 to 95° C. at a pressure of 3.333 kPa, and in a range of 93 to 103° C. at a pressure of 6.666 kPa, and wherein a temperature of the middle outflow plate is in a range of 73 to 83° C. at a pressure of 4.666 kPa, in a range of 70 to 80° C. at a pressure of 3.333 kPa, and in a range of 77 to 87° C. at a pressure of 6.666 kPa. |
