Process for removing methacrolein from liquid phase comprising acrylic acid as a main constituent and target product, and methacrolein as a secondary component
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A process for removing methacrolein from liquid phase P comprising acrylic acid as a main constituent and target product, and methacrolein as a secondary component in which the removal is effected by crystallization, the acrylic acid accumulating in the crystals formed and the methacrolein in the re
A process for removing methacrolein from liquid phase P comprising acrylic acid as a main constituent and target product, and methacrolein as a secondary component in which the removal is effected by crystallization, the acrylic acid accumulating in the crystals formed and the methacrolein in the remaining mother liquor.
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What is claimed is: 1. A process for removing methacrolein from liquid phase P comprising acrylic acid as a main constituent and target product, and, based on the amount of acrylic acid comprised therein, 0.01 to 15% by weight of methacrolein, which comprises effecting the removal by crystallizatio
What is claimed is: 1. A process for removing methacrolein from liquid phase P comprising acrylic acid as a main constituent and target product, and, based on the amount of acrylic acid comprised therein, 0.01 to 15% by weight of methacrolein, which comprises effecting the removal by crystallization, the acrylic acid accumulating in the crystals formed and the methacrolein in the remaining mother liquor. 2. The process according to claim 1, wherein the liquid phase P comprises at least 10% by weight of acrylic acid. 3. The process according to claim 1, wherein the liquid phase P comprises at least 65% by weight of acrylic acid. 4. The process according to claim 1, wherein the liquid phase P comprises from 65 to 99.5% by weight of acrylic acid. 5. The process according to claim 1, wherein the liquid phase P, based on acrylic acid comprised therein, comprises from 0.2 to 30% by weight of water. 6. The process according to claim 1, wherein the liquid phase P stems from the product gas mixture of a heterogeneously catalyzed gas phase partial oxidation of at least one C3 precursor compound of acrylic acid. 7. The process according to claim 6, wherein the at least one C3 precursor compound is propane. 8. The process according to claim 6, wherein the at least one C3 precursor compound is propylene. 9. The process according to claim 6, wherein the at least one C3 precursor compound is propylene accompanied by propane as an inert gas constituent. 10. The process according to claim 9, wherein the propylene and the accompanying propane were a constituent of the product gas mixture of a partial dehydrogenation and/or oxydehydrogenation of propane which preceded the gas phase partial oxidation. 11. The process according to any claim 1, wherein the liquid phase P stems from a product gas mixture of a heterogeneously catalyzed gas phase partial oxidation of at least one C3 precursor compound of acrylic acid and has been obtained therefrom using at least one indistinct separation process. 12. The process according to claim 11, wherein the at least one indistinct separation process comprises at least one separation process from the group comprising absorption, partial condensation, fractional condensation, rectification, stripping and desorption. 13. The process according to claim 11, or 12, wherein mother liquor comprising accumulated methacrolein is recycled into at least one of the at least one indistinct separation process. 14. The process according to claim 13, wherein mother liquor comprising accumulated methacrolein is recycled into a fractional condensation of the product gas mixture of the heterogeneously catalyzed gas phase partial oxidation of the at least one C3 precursor compound of acrylic acid. 15. The process according to claim 1, wherein the crystallizative removal is undertaken by means of a suspension crystallization. 16. The process according to claim 15, wherein the separation of suspension crystals and remaining mother liquor is undertaken by means of a wash column. 17. The process according to claim 16, wherein the wash liquid used is the melt of acrylic acid crystals removed beforehand in the wash column. 18. The process according to claim 1, which comprises the following process steps: a) crystallization of acrylic acid out of the liquid phase P; b) separation of the acrylic acid crystals from the remaining mother liquor; c) at least partial melting of the removed acrylic acid crystals and d) at least partial recycling of the molten acrylic acid crystals to step b) and/or to step a). 19. The process according to claim 1, which is followed by a process in which acrylic acid crystals are melted and free-radically polymerized to polymers.
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이 특허에 인용된 특허 (41)
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