PROCESS FOR MAKING ETHYLENE GLYCOL AND/OR PROPYLENE GLYCOL FROM ALDOSE- AND/OR KETOSE-YIELDING CARBOHYDRATES WITH EX SITU HYDROGENOLYSIS OR HYDROGENATION CATALYST TREATMENT

1 . A catalytic process for producing a lower glycol comprising at least one of ethylene glycol and propylene glycol from a carbohydrate-containing feed that comprises at least one of aldose- and ketose-yielding carbohydrate, said process comprising continuously or intermittently supplying the feed to a reaction zone containing a liquid medium having therein one or more catalysts for converting said carbohydrate to said glycol, wherein at least one of the catalysts is a hydrogenolysis or hydrogenation catalyst that is suspended in the liquid medium, said liquid medium being at catalytic conversion conditions including the presence of dissolved hydrogen, to produce a reaction product containing said lower glycol, and continuously or intermittently withdrawing liquid medium that contains reaction product from the reaction zone, wherein

(i) continuously or intermittently at least a portion of said suspended catalyst is withdrawn from the reaction zone;

(ii) at least a portion of the withdrawn suspended catalyst is subjected to treatment to provide a treated catalyst having enhanced performance; and

(iii) at least a portion of the treated catalyst is passed to the reaction zone.

2 . The process of claim 1 wherein the withdrawn catalyst has deposits and the treatment of the catalyst comprises washing or chemical removal of deposits.

3 . The process of claim 2 wherein an aqueous liquid is used for the treatment.

4 . The process of claim 3 wherein the aqueous liquid has a pH greater than 5.

5 . The process of claim 4 wherein the aqueous liquid contains a base.

6 . The process of claim 4 wherein the aqueous liquid comprises exogenous carbonate anion.

7 . The process of claim 3 wherein the aqueous liquid contains lower glycol.

8 . The process of claim 1 wherein the treatment of the catalyst comprises contact with hydrogen at a temperature in a range of about 150° C. to 400° C. and a hydrogen partial pressure in a range of about 2000 to 20,000 kPa for a time sufficient to effect reduction of the catalyst.

9 . The process of claim 1 wherein the catalyst is treated with hydrazine or borohydride or subjected to oxidation.

10 . The process of claim 1 wherein the treatment of the catalyst comprises a conditioning.

11 . The process of claim 10 wherein the conditioning is placing on the catalyst an adjuvant that affects its performance.

12 . The process of claim 11 wherein the adjuvant comprises at least one of promotors, modifiers, co-catalysts, or catalytic inhibitors.

13 . The process of claim 10 wherein the conditioning comprises selective poisoning of the catalyst.

14 . The process of claim 10 wherein the conditioning comprises depositing organic or inorganic substance on the catalyst.

15 . The process of claim 14 wherein the catalyst is contacted with an aqueous solution of solubilized tungsten compound and causing insoluble tungsten complexes or compounds to form and deposit on the catalyst.

16 . The process of claim 15 wherein the pH of the solution is reduced to cause insoluble tungsten complexes or compounds to form.

17 . A continuous catalytic process for producing a lower glycol of at least one of ethylene glycol and propylene glycol from a carbohydrate-containing feed comprising at least one of aldose- and ketose-yielding carbohydrate, said processes being conducted in a reaction system containing a liquid medium wherein the reaction system contains homogeneous, tungsten-containing retro aldol catalyst and at least a portion of the reaction system contains heterogeneous hydrogenation catalyst, said liquid medium being at catalytic conversion conditions including the presence of dissolved hydrogen, to produce a reaction product containing said glycol wherein tungsten-containing precipitate forms on the hydrogenation catalyst, wherein said process comprises:

i. continuously or intermittently supplying the feed to the liquid medium in the reaction system;

ii. maintaining the liquid medium in at least the portion of the reaction system containing under catalytic conversion conditions including the presence hydrogenation catalyst and retro-aldol catalyst and the presence of dissolved hydrogen, to effect retro aldol and hydrogenation to produce a reaction product containing said glycol;

iii. continuously or intermittently withdrawing a portion of the liquid medium containing reaction product from the reaction system; and

iv. continuously or intermittently withdrawing a portion of the hydrogenation catalyst from the reaction system,

v. treating the withdrawn hydrogenation catalyst to remove at least a portion of the tungsten-containing deposit and provide a treated catalyst having enhanced performance; and

vi. passing at least a portion of the treated catalyst to the reaction system.

18 . The process of claim 17 wherein the hydrogenation catalyst is a nickel-containing hydrogenation catalyst.

19 . The process of claim 17 wherein the treatment of the catalyst comprises washing or chemical removal of deposits.

20 . A process for attenuating the activity of a hydrogenation catalyst for use in the conversion of carbohydrate feed to at least one of ethylene glycol and propylene glycol by a retro-aldol and hydrogenation process comprising contacting the hydrogenation catalyst with an aqueous solution of solubilized tungsten compound and causing insoluble tungsten complexes or compounds to form and deposit on the hydrogenation catalyst to provide a hydrogenation catalyst having attenuated activity.

21 . The process of claim 20 wherein the hydrogenation catalyst is a nickel-containing hydrogenation catalyst.

22 . The process of claim 21 wherein the pH of the solution is reduced to cause insoluble tungsten complexes or compounds to form.