US2663698A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing synthetic tannins by dehydrating and sulfonating a novolak resin in a vacuum
Assignee: Monsanto Chemicals Ltd
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Filing: 1950-04-11
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Granted: 1953-12-22
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Expires: 1970-04-11
Abstract
No abstract record available.
Inventors
- 👤 Compton Ell Dee
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 23:31
CPC Classifications
C; C14; C14C; C14C3/00; C14C3/02; C14C3/08; C14C3/18; C14C3/20
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
214 words
A PROCESS FOR PRODUCING SYNTHETIC TANNINS WHICH COMPRISES DEHYDRATING A PHOSPHORIC ACIDCATALYST NOVOLAK RESIN OF 1 MOLECULAR PROPORTION OF PHENOL AND 0.65 TO 0.75 MOLECULAR PROPORTION OF FORALDEHYDE BY HEATING THE RESIN AT A PRESSURE BETWEEN ABOUT 38 AND 42 MILLIMETERS OF MERCURY (ABSOLUTE PRESSURE) UNTIL THE TEMPERATURE OF THE RESIN IS BETWEEN 90 AND 100* C., ADDING COMMERCIAL SULFURIC ACID OF 93% STRENGTH TO THE RESIN GRANUALLY AND CONCURRENTLY MAINTAINING THE REACTION MASS AT A PRESSURE BETWEEN ABOUT 38 AND 42 MILLIMETERS OF MERCURY (ABSOLUTE PRESSURE) AND ALSO MAINTAINING THE TEMPERATURE OF THE REACTION MASS BETWEEN 90 AND 100* C. UNTIL THE RESIN CONTAINS FROM 0.3 TO 0.35 MOL OF COMBINDED SO3 PER MOL OF PHENOL, THE AMOUNT OF ACID ADDED BEING 0.4 TO 0.5 MOLS OF SULFURIC ACID (CALCULATED AS 100% ACID) FOR EACH MOL OF PHENOL, ALLOWING THE PRESSURE SURROUNDING THE RESIN TO RISE TO THE PREVAILING ATMOSPHERIC PRESSURE AND SUBSTANTIALLY CONCURRENTLY ADDING BETWEEN 40 AND 150% BY WEIGHT OF WATER, BASED ON THE WEIGHT OF THE NOVALAK RESIN, SAID WATER BEING AT A TEMPERATE BETWEEN 75 AND 95* C., AND THEN NEUTRALIZING THE RESULTING MIXTURE WITH AN AQUEOUS SOLUTION OF AN ALKALINE SUBSTANCE AND AN ORGANIC ACID BUFFER TO FORM A SOLUTION HAVING A PH BETWEEN ABOUT 3 TO 4.7.
Claim 2
Dependent Claim
214 words
A PROCESS FOR PRODUCING SYNTHETIC TANNINS WHICH COMPRISES DEHYDRATING A PHOSPHORIC ACIDCATALYST NOVOLAK RESIN OF 1 MOLECULAR PROPORTION OF PHENOL AND 0.65 TO 0.75 MOLECULAR PROPORTION OF FORALDEHYDE BY HEATING THE RESIN AT A PRESSURE BETWEEN ABOUT 38 AND 42 MILLIMETERS OF MERCURY (ABSOLUTE PRESSURE) UNTIL THE TEMPERATURE OF THE RESIN IS BETWEEN 90 AND 100* C., ADDING COMMERCIAL SULFURIC ACID OF 93% STRENGTH TO THE RESIN GRANUALLY AND CONCURRENTLY MAINTAINING THE REACTION MASS AT A PRESSURE BETWEEN ABOUT 38 AND 42 MILLIMETERS OF MERCURY (ABSOLUTE PRESSURE) AND ALSO MAINTAINING THE TEMPERATURE OF THE REACTION MASS BETWEEN 90 AND 100* C. UNTIL THE RESIN CONTAINS FROM 0.3 TO 0.35 MOL OF COMBINDED SO3 PER MOL OF PHENOL, THE AMOUNT OF ACID ADDED BEING 0.4 TO 0.5 MOLS OF SULFURIC ACID (CALCULATED AS 100% ACID) FOR EACH MOL OF PHENOL, ALLOWING THE PRESSURE SURROUNDING THE RESIN TO RISE TO THE PREVAILING ATMOSPHERIC PRESSURE AND SUBSTANTIALLY CONCURRENTLY ADDING BETWEEN 40 AND 150% BY WEIGHT OF WATER, BASED ON THE WEIGHT OF THE NOVALAK RESIN, SAID WATER BEING AT A TEMPERATE BETWEEN 75 AND 95* C., AND THEN NEUTRALIZING THE RESULTING MIXTURE WITH AN AQUEOUS SOLUTION OF AN ALKALINE SUBSTANCE AND AN ORGANIC ACID BUFFER TO FORM A SOLUTION HAVING A PH BETWEEN ABOUT 3 TO 4.7.
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) | 1956-12-21 | 1957-06-22 | 1957-12-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1960-12-21 | 1961-06-22 | 1961-12-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1964-12-21 | 1965-06-22 | 1965-12-22 | $7700.00 | Window Closed / Lapsed |