Process for the production of 1,4-butanediol and tetrahydrofuran from furan
The present invention provides a process for the production of 1,4-BDO and THF from furan, said process comprising: (i) contacting furan with hydrogen and water in a reactor in the presence of a catalytic composition, wherein the furan and water are contacted in the presence of a solvent, said solvent being selected from one or more of THF, 1,4-BDO and NBA, and converting at least a portion of said furan to 1,4-BDO and THF; (ii) producing a reactor product stream comprising gases, water, THF, 1,4-BDO and furan; (iii) separating gases from the reactor product stream; (iv) then separating at least a portion of each of the THF and 1,4-BDO from said reactor product stream; and (v) recycling the remainder of the reactor product stream, comprising water, optionally furan, and at least one of THF, 1,4-BDO and NBA, to the reactor.
1. A process for the production of 1,4-BDO and THF from furan, said process comprising:
(i) contacting furan with hydrogen and water in a reactor in the presence of a catalytic composition, wherein the furan and water are contacted in the presence of a solvent, said solvent comprising THF, 1,4-BDO and NBA, wherein each of THF, 1,4-BDO and NBA are in an amount of at least 10 wt % and no more than 70 wt % and the sum of all does not exceed 100 wt % (based on the solvent), such that a single phase is formed with the solvent, furan and water and converting at least a portion of said furan to 1,4-BDO and THF;
(ii) producing a reactor product stream comprising gases, water, THF, 1,4-BDO and furan;
(iii) separating gases from the reactor product stream;
(iv) then separating at least a portion of each of the THF and 1,4-BDO from said reactor product stream; and
(v) recycling the remainder of the reactor product stream, comprising water, optionally furan, and more than one of THF, 1,4-BDO and NBA, to the reactor.
2. The process according to claim 1 , wherein the reactor product stream also comprises NBA and at least a portion of the NBA is separated from said reactor product stream in step (iv).
3. The process according to claim 1 , wherein the portion of each of the THF, 1,4-BDO and NBA separated from the reactor product stream in step iv) corresponds to at least 90 wt % of the amount of each produced in the reaction of the furan with hydrogen and water.
4. The process according to claim 3 , wherein the portion of each of the THF, 1,4-BDO and NBA separated from the reactor product stream in step iv) corresponds to at least 100 wt % of the amount of each produced in the reaction of the furan with hydrogen and water.
5. The process according to claim 2 , wherein separating at least a portion of each of the THF, 1,4-BDO and NBA from said reactor product stream comprises, in a first step, separating by distillation a bottoms stream comprising water and 1,4-BDO from a top stream comprising THF, NBA and water and, optionally, furan.
6. The process according to claim 5 , wherein the stream comprising THF, NBA and water is subjected to liquid/liquid separation to provide an aqueous stream which is recycled to the reactor and an organics stream comprising THF and NBA.
7. The process according to claim 1 , wherein the amount of NBA, 1, 4-BDO and THF produced in the reactors is isolated with the remaining amount being recycled.