Process for the production of furfural
A process for the production of furfural from a biphasic composition including furfural, an organic solvent and soluble organic debris. The said process includes subjecting the biphasic composition to a liquid-liquid separation step to provide an organic phase and an aqueous phase. The organic phase includes the organic solvent, a first portion of the furfural and a first portion of soluble organic debris. The aqueous phase includes a remainder portion of the furfural and a remainder portion of soluble organic debris. The organic phase is subjected to a distillation step to provide a furfural stream and an organic solvent stream including the organic solvent and the first portion of the soluble organic debris. The organic solvent stream is conveyed to an adsorption unit to adsorb a second portion of the soluble organic debris, forming an organic debris-depleted recycle stream.
1. A process for the production of furfural from a biphasic composition ( 2 ) comprising furfural, an organic solvent and soluble organic debris, said process comprising:
(a) subjecting the biphasic composition to a liquid-liquid separation step ( 3 ) to provide:
an organic phase ( 5 ) comprising the organic solvent, a first portion of the furfural and a first portion of soluble organic debris; and
an aqueous phase ( 4 ) comprising a remainder portion of the furfural and a remainder portion of soluble organic debris;
(b) subjecting the organic phase ( 5 ) to a distillation step ( 7 ) to provide:
a furfural stream ( 8 ), and
an organic solvent stream ( 9 ) comprising the organic solvent and the first portion of the soluble organic debris;
(c) conveying the organic solvent stream ( 9 ) comprising the organic solvent to an adsorption unit ( 10 ) to adsorb a second portion of the soluble organic debris, and to form an organic debris-depleted recycle stream ( 11 ).
2. The process according to claim 1 , wherein step (c) is carried out using more than one adsorption unit.
3. The process according to claim 1 , wherein the organic solvent has a boiling point higher than furfural.
4. The process according to claim 1 , wherein following step (c), the adsorption unit ( 10 ) undergoes a soluble organic debris removal step to remove any residual soluble organic debris in the adsorption unit.
5. The process of claim 1 , wherein the stream ( 11 ) comprising the organic debris-depleted recycle stream is recycled to a biphasic dehydration reactor.
6. A process for the extraction of furfural from a biphasic composition ( 2 ) comprising furfural, an organic solvent and soluble organic debris, said process comprising:
(a) subjecting the biphasic composition to a liquid-liquid separation step ( 3 ) to provide:
an organic phase ( 5 ) comprising the organic solvent, a first portion of the furfural and a first portion of soluble organic debris; and
an aqueous phase ( 4 ) comprising a remainder portion of the furfural and a remainder portion of soluble organic debris;
(b) conveying the organic phase ( 5 ) comprising the organic solvent, a first portion of the furfural and a first portion of soluble organic debris to an adsorption unit ( 10 ) to adsorb a second portion of the soluble organic debris, and to form an organic debris-depleted stream ( 5 ′) comprising the organic solvent and the first portion of the furfural;
(c) subjecting the organic debris-depleted stream ( 5 ′) comprising the organic solvent and the first portion of the furfural to a distillation step ( 7 ) to provide:
a furfural stream ( 8 ), and
an organic solvent stream ( 9 ) comprising the organic solvent.
7. The process according to claim 6 , wherein step (b) is carried out using more than one adsorption unit.
8. The process according to claim 6 , wherein the organic solvent has a boiling point higher than furfural.
9. The process according to claim 6 , wherein following step (b), the adsorption unit ( 10 ) undergoes a soluble organic debris removal step to remove any residual soluble organic debris in the adsorption unit.
10. The process of claim 6 , wherein the organic solvent stream ( 9 ) is recycled to a biphasic dehydration reactor.