US4110370A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of separating high-boiling or non-volatile materials
Assignee: BASF SE
•
Filing: 1975-10-07
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Granted: 1978-08-29
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Expires: 1995-10-07
Abstract
Abstract In the oxidation of propylene and/or acrolein, high-boiling or non-volatile byproducts are separated from the solvents used for absorbing the acrylic acid by treating the said solvents laden with byproducts with the hot reaction gases in such amounts that the major portion of the solvents evaporates, the residual solvent containing a high percentage of said byproducts then being discarded or worked up.
Inventors
- 👤 Heinz Engelbach
- 👤 Richard Krabetz
- 👤 Gerd Duembgen
- 👤 Carl-Heinz Willersinn
- 👤 Walter Frey
- 👤 Ulrich Lebert
- 👤 Fritz Thiessen
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 14:37
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/42; C07C51/48; Y; Y10; Y10S; Y10S203/00; Y10S203/22
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
216 words
In a process for separating acrylic acid from the hot reaction gas obtained from the manufacture of acrylic acid by catalytic oxidation of propylene and/or acrolein with molecular oxygen, said hot reaction gas containing acrylic acid and low-boiling impurities, wherein the acrylic acid and low-boiling impurities are absorbed with a solvent in a means for absorbing gases into solvents and high-boiling and non-volatile impurities are formed in said means, the solvent boiling in the range from about 200° to 360° C., and the solvent is re-used for absorption after being separated from the acrylic acid and low-boiling impurities, the improvment comprising: (a) taking a portion of the solvent containing acrylic acid and high-boiling and non-volatile impurities, (b) contacting said portion of solvent with the hot reaction gas containing acrylic acid and low-boiling impurities in a means for gas-liquid exchange at such a rate that between about 90 and 99.9% of the solvent evaporates thereby producing a gas containing vaporized solvent, acrylic acid and low-boiling impurities and a residual solvent, the residual solvent containing the high-boiling and non-volatile impurities, (c) conducting the gas containing vaporized solvent, acrylic acid and low-boiling impurities to said means for absorbing gases into solvents with a means for conducting gas, and (d) separating the residual solvent from said means for gas-liquid exchange.
Claim 2
Dependent Claim
216 words
In a process for separating acrylic acid from the hot reaction gas obtained from the manufacture of acrylic acid by catalytic oxidation of propylene and/or acrolein with molecular oxygen, said hot reaction gas containing acrylic acid and low-boiling impurities, wherein the acrylic acid and low-boiling impurities are absorbed with a solvent in a means for absorbing gases into solvents and high-boiling and non-volatile impurities are formed in said means, the solvent boiling in the range from about 200° to 360° C., and the solvent is re-used for absorption after being separated from the acrylic acid and low-boiling impurities, the improvment comprising: (a) taking a portion of the solvent containing acrylic acid and high-boiling and non-volatile impurities, (b) contacting said portion of solvent with the hot reaction gas containing acrylic acid and low-boiling impurities in a means for gas-liquid exchange at such a rate that between about 90 and 99.9% of the solvent evaporates thereby producing a gas containing vaporized solvent, acrylic acid and low-boiling impurities and a residual solvent, the residual solvent containing the high-boiling and non-volatile impurities, (c) conducting the gas containing vaporized solvent, acrylic acid and low-boiling impurities to said means for absorbing gases into solvents with a means for conducting gas, and (d) separating the residual solvent from said means for gas-liquid exchange.
Claim 3
Dependent Claim
28 words
A process as set forth in claim 1, wherein the means for gas-liquid exchange is a packed column or a column provided with baffles suitable for gas-liquid exchange.
Claim 4
Dependent Claim
20 words
A process as set forth in claim 1, wherein the separated residual solvent containing high-boiling and non-volatile materials is distilled.
Claim 5
Dependent Claim
40 words
A process as set forth in claim 1, wherein the hot reaction gas is first cooled to about 120° C. to 220° C. in the means for gas-liquid exchange and then loaded with vaporized solvent, acrylic acid and low-boiling impurities.
Claim 6
Dependent Claim
22 words
A process as set forth in claim 1, wherein the acrylic acid and low-boiling impurities are absorbed by re-used solvent flowing countercurrently.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-08-28 | 1982-02-27 | 1982-08-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-08-28 | 1986-02-27 | 1986-08-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-08-28 | 1990-02-27 | 1990-08-29 | $7700.00 | Window Closed / Lapsed |