Granted Patent B2

US 8,921,618 · App. 13/621,345 · Granted Dec 30, 2014

Abstract

Claims (68)

1. A method of reclaiming trimethylolpropane from purification residue comprising hydrolyzing a purification residue with an aqueous medium in the presence of (i) an acid and (ii) an oxidizing agent to reclaim trimethylolpropane from one or more TMP-formals selected from:

monocyclic TMP-formal (MCF); Formula I:

monolinear bis-TMP-formal (MBLF); Formula II:

[C 2 H 5 C(CH 2 OH) 2 CH 2 O] 2 CH 2   (II)

Methyl-(monolinear)TMP-formal; Formula III

C 2 H 5 C(CH 2 OH) 2 CH 2 OCH 2 OCH 3   (III)

Methyl-(bislinear)TMP-formal; Formula IV

C 2 H 5 C(CH 2 OH) 2 CH 2 OCH 2 OCH 2 OCH 3   (IV)

and the cyclic formal of di-TMP; Formula V:

wherein the hydrolysis reaction is carried out at a pH of from 1 to 4 and wherein the oxidizing agent is supplied to the hydrolysis reaction in an amount of from 2 wt % to 40 wt % based on the dry weight of the purification residue.

2. The method according to claim 1 , comprising hydrolyzing monolinear bis-TMP-formal (MBLF); Formula II:

[C 2 H 5 C(CH 2 OH) 2 CH 2 O] 2 CH 2   (II).

3. The method according to claim 1 , wherein said acid is selected from sulfuric acid, phosphoric acid, hydrochloric acid, sulfonic acid, organic acids or acid-functional ion exchange resin.

4. The method according to claim 1 , wherein said acid is formic acid.

5. The method according to claim 1 , wherein said acid is an acid functional ion exchange resin.

6. The method according to claim 1 , further comprising neutralizing said aqueous medium with a neutralizing agent.

7. The method according to claim 1 , effective to reclaim at least 85% by weight of the trimethylolpropane present in the trimethylolpropane formals of the purification residue.

8. The method according to claim 1 , wherein the acid is supplied to the aqueous reaction medium in an amount of from 0.5 wt % to 20 wt % based on the total weight of the aqueous medium.

9. The method according to claim 1 , wherein water is supplied to the reaction medium in a weight ratio of water:organic mixture from 1 W/W to 3 W/W.

10. The method according to claim 1 , wherein the hydrolysis temperature is maintained within the range of from 70° C. to 95° C.

11. The method according to claim 1 , wherein the hydrolysis reaction is carried out for a reaction period of from about 1 hour to about 7.5 hours.

12. The method according to claim 1 , wherein reactants, temperature and reaction time are selected such that the yield of trimethylolpropane is from 75% to 95% based on the weight of TMP-formal derivate in the purification residue.

13. A process for reclaiming trimethylolpropane from purification residue comprising:

(a) continuously feeding a purification residue stream to a reaction vessel, said purification residue stream containing one or more trimethylolpropane formals selected from:

monocyclic TMP-formal (MCF); Formula I:

monolinear bis-TMP-formal (MBLF); Formula II:

[C 2 H 5 C(CH 2 OH) 2 CH 2 O] 2 CH 2   (II)

Methyl-(monolinear)TMP-formal; Formula III

C 2 H 5 C(CH 2 OH) 2 CH 2 OCH 2 OCH 3   (III)

Methyl-(bislinear)TMP-formal; Formula IV

C 2 H 5 C(CH 2 OH) 2 CH 2 OCH 2 OCH 2 OCH 3   (IV)

and formal of di-TMP; the cyclic Formula V:

(b) providing water, an acid and an oxidizing agent to the reaction vessel such that a reaction mixture including the purification residue, water, acid and oxidizing agent is formed;

(c) maintaining the reaction mixture in the reaction vessel at a time and temperature such that one or more of said TMP-formals are hydrolyzed to thereby enrich the reaction mixture with reclaimed trimethylolpropane, wherein the hydrolysis reaction is carried out at a pH of from 1 to 4 and wherein the oxidizing agent is supplied to the hydrolysis reaction in an amount of from 2 wt % to 40 wt % based on the dry weight of the purification residue; and

(d) continuously withdrawing a reclaimed trimethylolpropane stream from the reaction vessel.

14. The process according to claim 13 , wherein the reclaimed trimethylolpropane stream from step (d) is subjected to a distillation to obtain trimethylolpropane containing light ends and a distillation residue.

15. The method according to claim 14 , wherein the reclaimed trimethylolpropane stream is combined with another trimethylolpropane stream to provide a combined trimethylolpropane stream prior to distillation.

16. The method according to claim 15 , wherein formate is extracted from the combined trimethylolpropane stream prior to distillation.

17. A process for purifying a trimethylolpropane containing stream comprising:

(a) distilling a trimethylolpropane containing stream to provide an overhead product stream and a purification residue stream;

(b) feeding the purification residue stream to a reaction vessel, said purification residue stream containing one or more trimethylolpropane formals selected from:

monocyclic TMP-formal (MCF); Formula I:

monolinear bis-TMP-formal (MBLF); Formula II:

[C 2 H 5 C(CH 2 OH) 2 CH 2 O] 2 CH 2   (II)

Methyl-(monolinear)TMP-formal; Formula III

C 2 H 5 C(CH 2 OH) 2 CH 2 OCH 2 OCH 3   (III)

Methyl-(bislinear)TMP-formal; Formula IV

C 2 H 5 C(CH 2 OH) 2 CH 2 OCH 2 OCH 2 OCH 3   (IV)

and formal of di-TMP; the cyclic Formula V:

(c) continuously providing water, an acid and an oxidizing agent to the reaction vessel such that a reaction mixture including the purification residue, water, acid and oxidizing agent is formed;

(d) maintaining the reaction mixture in the reaction vessel at a time and temperature such that one or more of said trimethylol formals are hydrolyzed to thereby enrich the reaction mixture with reclaimed trimethylolpropane, wherein the hydrolysis reaction is carried out at a pH of from 1 to 4 and wherein the oxidizing agent is supplied to the hydrolysis reaction in an amount of from 2 wt % to 40 wt % based on the dry weight of the purification residue;

(e) withdrawing a reclaimed trimethylolpropane stream from the reaction vessel; and

(f) recycling reclaimed trimethylolpropane to step (a).

18. A purification system for recovering trimethylolpropane from a raw product stream comprising trimethylolpropane and formate comprising:

(a) an extraction system adapted to receive the raw product stream and provide aqueous output containing formate and an organic output containing trimethylolpropane;

(b) a distillation tower adapted to receive organic output of the extraction system and provide trimethylolpropane and light ends as overhead and purification residue,

wherein the purification residue contains one or more TMP-formals selected from:

monocyclic TMP-formal (MCF); Formula I:

monolinear bis-TMP-formal (MBLF); Formula II:

[C 2 H 5 C(CH 2 OH) 2 CH 2 O] 2 CH 2   (II)

Methyl-(monolinear)TMP-formal; Formula III

C 2 H 5 C(CH 2 OH) 2 CH 2 OCH 2 OCH 3   (III)

Methyl-(bislinear)TMP-formal; Formula IV

C 2 H 5 C(CH 2 OH) 2 CH 2 OCH 2 OCH 2 OCH 3   (IV)

and formal of di-TMP; the cyclic Formula V:

(c) means for providing water, an oxidizing agent, and acid to the purification residue to provide an aqueous residue mixture;

(d) a reactor adapted for receiving the aqueous residue mixture and maintaining the reaction mixture in the reaction vessel at a time and temperature such that one or more of said TMP-formals are hydrolyzed to thereby enrich the reaction mixture with reclaimed trimethylolpropane, wherein the hydrolysis reaction is carried out at a pH of from 1 to 4 and wherein the oxidizing agent is supplied to the hydrolysis reaction in an amount of from 2 wt % to 40 wt % based on the dry weight of the purification residue; and

(e) a recycle system for recycling reclaimed trimethylolpropane from the reactor vessel to the extraction system of part (a) or for recycling reclaimed trimethylolpropane from the reactor to the distillation tower of part (b).

Assignments (8)