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US4300003A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of low molecular polyhydroxyl compounds

Assignee: Bayer AG
•
Filing: 1979-07-06
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Granted: 1981-11-10
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Expires: 1999-07-06
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Abstract

Abstract Formose solutions are hydrogenated in a batchwise alkaline two-stage catalytic process to produce low molecular weight polyhydric alcohols.

Inventors

  • 👤 Edgar Mohring
  • 👤 Hanns P. Muller
  • 👤 Kuno Wagner

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 20:29
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/132; C07C29/136; C07C29/14; C07C29/141; C07C29/143; C07C29/145; C07C31/00; C07C31/02; C07C31/10; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/30; C08G18/32; C08G18/3203; C08G18/3206; C08G18/3209; C08G18/40; C08G18/42; C08G18/4297; C08G18/48; C08G18/4829; C08G65/00; C08G65/02; C08G65/26; C08G65/2603; C08G65/2606

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 265 words
A process for the preparation of low molecular weight polyhydric alcohols by the hydrogenation of formose solutions in the presence of metal catalysts, comprising: (A) introducing a formose solution at a concentration of at least 20%, the pH of which solution has been adjusted to a value of from 7.5 to 12.5, batchwise into a first reactor at a rate such that the concentration of reducible groups (determined as carbonyl groups) inside the reactor does not exceed 2% by weight; (B) hydrogenating said solution batchwise in the presence of a catalyst, said catalyst content remaining constant in said reactor; (C) withdrawing the reaction product batchwise from the first reactor when the concentration of reducible groups (determined as carbonyl groups) has fallen below 1.5% by weight; (D) adjusting the pH of the prehydrogenated product thus obtained to a value of from 1 to 6 and maintaining a temperature of 10° to 100° C. for from 10 minutes to 2 hours; (E) introducing the reaction product thus obtained batchwise into a second reactor, the pH of said product being readjusted to a value of from 7.5 to 12.5, immediately before introduction of the product into the second reactor; (F) hydrogenating the product batchwise in the presence of a catalyst, said catalyst content remaining constant in said reactor; and (G) withdrawing the reaction product batchwise from the second reactor after a dwell time of from 5 minutes to 4 hours, further characterized in that the amount of said formose solution introduced into each reactor is from 3 to 30 times the amount of catalyst present in each reactor.
Claim 2
Dependent Claim 265 words
A process for the preparation of low molecular weight polyhydric alcohols by the hydrogenation of formose solutions in the presence of metal catalysts, comprising: (A) introducing a formose solution at a concentration of at least 20%, the pH of which solution has been adjusted to a value of from 7.5 to 12.5, batchwise into a first reactor at a rate such that the concentration of reducible groups (determined as carbonyl groups) inside the reactor does not exceed 2% by weight; (B) hydrogenating said solution batchwise in the presence of a catalyst, said catalyst content remaining constant in said reactor; (C) withdrawing the reaction product batchwise from the first reactor when the concentration of reducible groups (determined as carbonyl groups) has fallen below 1.5% by weight; (D) adjusting the pH of the prehydrogenated product thus obtained to a value of from 1 to 6 and maintaining a temperature of 10° to 100° C. for from 10 minutes to 2 hours; (E) introducing the reaction product thus obtained batchwise into a second reactor, the pH of said product being readjusted to a value of from 7.5 to 12.5, immediately before introduction of the product into the second reactor; (F) hydrogenating the product batchwise in the presence of a catalyst, said catalyst content remaining constant in said reactor; and (G) withdrawing the reaction product batchwise from the second reactor after a dwell time of from 5 minutes to 4 hours, further characterized in that the amount of said formose solution introduced into each reactor is from 3 to 30 times the amount of catalyst present in each reactor.
Claim 3
Dependent Claim 35 words
The process of claim 1, characterized in that the individual batches are pumped in at a rate corresponding to the filling of 1/6 of the volume of each reactor in from 3 to 120 minutes.
Claim 4
Dependent Claim 27 words
The process of claim 2, characterized in that the rate of filling amounts to 1/6 of the volume of each reactor in from 5 to 30 minutes.
Claim 5
Dependent Claim 41 words
The process of claim 1, characterized in that after each batch of the first reactor has been pumped in, hydrogenation is carried out for a period amounting to from 1/2 to 4 times the time taken to pump in the batch.
Claim 6
Dependent Claim 41 words
The process of claim 4, characterized in that after each batch for the second reactor has been pumped in, hydrogenation is carried out for a period corresponding to from 1/2 to 5 times the time required for pumping in the batch.
Claim 7
Dependent Claim 40 words
The process of claim 1, characterized in that in addition to formose, the starting material to be hydrogenated contains up to 80% by weight (based on the total quantity of material to be hydrogenated) of other natural and/or synthetic sugars.
Claim 8
Dependent Claim 19 words
The process of claim 1, characterized in that catalysts containing nickel are used in both reactors of the hydrogenation.
Claim 9
Dependent Claim 20 words
The process of claim 7, characterized in that the catalyst used is Raney nickel optionally modified with iron and/or zinc.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-11-09 1985-05-11 1985-11-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-11-09 1989-05-11 1989-11-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-11-09 1993-05-11 1993-11-10 $7700.00 Window Closed / Lapsed

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