Process for producing (meth)acrylic acid or (meth)acrylic ester
A technology of acrylate and acrylic acid, which is applied in the field of distillation and refining, and can solve problems such as the deterioration of the gas-liquid contact state, the reduction of the recovery rate of the target product, and the hindrance to the continuous operation of the distillation tower.
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Embodiment 1
[0089] Acrylic acid was distilled using a vacuum distillation column with a diameter of 1,000 mm. The vacuum distillation column has a column tank for supplying a raw material liquid for distillation, a column body for passing the vapor of the heated liquid in the column tank, and a condenser for condensing the vapor discharged from the top of the column.
[0090]A reboiler for heating the supplied raw material liquid is installed in the column pot. The above-mentioned tower body is a plate tower. The tower body has a structure in which 30 arbitrary perforated plates can be arranged as trays.
[0091] In this example, a total of 30 corrugated plate-type perforated plates without weirs and flat plate-type perforated plates without weirs were installed as the above-mentioned trays. In this embodiment, the perforated plate group arranged from bottom to top according to the order of four corrugated plate-type non-weir perforated plates and one flat-type non-weir perforated plate...
Embodiment 2
[0106] In this embodiment, as shown in Table 1, the group of porous plates arranged from bottom to top in the order of 3 corrugated plate-type non-weir perforated plates and 2 flat-type non-weir perforated plates is regarded as a group. Six groups of plate groups are arranged in order from bottom to top, and are configured as perforated plates as trays. In addition, as a flat plate type non-weir perforated plate, a flat type non-weir perforated plate having a hole diameter of 30 mm and an opening ratio of 27% was used. Except for this, in this example, the experiment of dehydration distillation was performed similarly to Example 1. In operation, the composition of the raffinate extracted from the bottom of the tower is the same as in Example 1.
[0107] Similar to Example 1, the pressure difference between the top and the bottom of the distillation column was 5.5 kPa, and there was no rise, and the operation could be continued stably. After 3 months, the operation was stoppe...
Embodiment 3
[0112] As shown in Table 1, as the above-mentioned corrugated plate type non-weir porous plate, a corrugated plate type non-weir porous plate having a through hole with a diameter of 25 mm and an opening ratio of 24% is used. The height of the corrugated plate type non-weir perforated plate is 30 mm. As the above-mentioned flat type non-weir perforated plate, a flat type non-weir perforated plate with a hole diameter of 30 mm and a porosity of 24% is used. In addition, The experiment of dehydration distillation was performed similarly to Example 1. In operation, the composition of the raffinate extracted from the bottom of the tower is the same as in Example 1.
[0113] Similar to Example 1, the pressure difference between the top and the bottom of the distillation column was 5.5 kPa, and there was no rise, and the operation could be continued stably. After 3 months, the operation was stopped, and when the distillation column was checked from an open point, no polymer of acry...
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