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
•
Expires: 1999-07-06
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.
References Cited (Backward Citations)
US2121981A
Cited
DE725842C
Cited
DE705274C
Cited
GB513708A
Cited
US2224910A
Cited
US2276192A
Cited
US2272378A
Cited
US2271083A
Cited
US2269935A
Cited
DE888096C
Cited
DE884791C
Cited
DE830951C
Cited
DE822385C
Cited
US2760983A
Cited
GB745557A
Cited
US2775621A
Cited
DE1044157B
Cited
DE2639084A1
Cited
GB1542980A
Cited
DE2714084A1
Cited
DE2714104A1
Cited
DE2721093A1
Cited
DE2732077A1
Cited
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 |