Patent US4714003A successfully refreshed from Google Patents.
Patent US2741648A successfully refreshed from Google Patents.
US2741648A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of acetylene
Assignee: Union Oil Company of California
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Filing: 1953-05-25
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Granted: 1956-04-10
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Expires: 1973-05-25
Abstract
No abstract record available.
Inventors
- 👤 John L Bills
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 13:52
CPC Classifications
C; C07; C07C; C07C11/00; C07C11/22; C07C11/24; C10; C10G; C10G9/00; C10G9/28; C10G9/30
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
168 words
A PROCESS FOR THE MANUFACTURE OF ACETYLENE BY THE PYROLITIC CONVERSION OF HYDROCARBONS WHICH COMPRISES FLOWING A FEED GAS STREAM OF SAID HYDROCARBONS CONCURRENTLY WITH BETWEEN ABOUT 0.2 AND 10 POUNDS OF DISPERSED GRANULAR HEATING SOLIDS, PER S. C. F. OF SAID FEED GAS THROUGH A REACTION ZONE WHEREIN SAID FEED GAS IS HEATED BY SAID HEATING SOLIDS TO BETWEEN ABOUT 1800* AND 3000* F. FOR BETWEEN ABOUT 0.001 AND 0.5 SECOND, THEN IMMEDIATELY FLOWING THE RESULTING GAS-SOLIDS DISPERSION DOWNWARDLY INTO A RELATIVELY LOW-PRESSURE SEPARATION ZONE, MAINTAINING IN SAID SEPARATION ZONE A SUBSTANTIALLY COMPACT, SHARPLY DEFINED STREAM OF QUENCH SOLIDS FLOWING CONCURRENTLY AND SUBSTANTIALLY CONTIGUOUSLY TO AND SURROUNGING, BUT DISCRETE FROM, SAID EMERGING GASSOLIDS DISPERSION WHEREBY THE HOT GASES IN SAID DISPERSION ARE CAUSED TO FLOW CONCURRENTLY AND TRANSVERSELY THROUGH SAID STREAM OF QUENCH SOLIDS BEFORE ANY SUBSTANTIAL INTERMINGLING OF SAID HEATING SOLIDS AND SAID QUENCH SOLIDS HAS OCCURRED, SAID HOT GASES BEING RAPIDLY COOLED THEREBY TO BELOW ABOUT 1400* F., AND RECOVERING ACETYLENE FROM THE COOLED GASES.
Claim 2
Dependent Claim
168 words
A PROCESS FOR THE MANUFACTURE OF ACETYLENE BY THE PYROLITIC CONVERSION OF HYDROCARBONS WHICH COMPRISES FLOWING A FEED GAS STREAM OF SAID HYDROCARBONS CONCURRENTLY WITH BETWEEN ABOUT 0.2 AND 10 POUNDS OF DISPERSED GRANULAR HEATING SOLIDS, PER S. C. F. OF SAID FEED GAS THROUGH A REACTION ZONE WHEREIN SAID FEED GAS IS HEATED BY SAID HEATING SOLIDS TO BETWEEN ABOUT 1800* AND 3000* F. FOR BETWEEN ABOUT 0.001 AND 0.5 SECOND, THEN IMMEDIATELY FLOWING THE RESULTING GAS-SOLIDS DISPERSION DOWNWARDLY INTO A RELATIVELY LOW-PRESSURE SEPARATION ZONE, MAINTAINING IN SAID SEPARATION ZONE A SUBSTANTIALLY COMPACT, SHARPLY DEFINED STREAM OF QUENCH SOLIDS FLOWING CONCURRENTLY AND SUBSTANTIALLY CONTIGUOUSLY TO AND SURROUNGING, BUT DISCRETE FROM, SAID EMERGING GASSOLIDS DISPERSION WHEREBY THE HOT GASES IN SAID DISPERSION ARE CAUSED TO FLOW CONCURRENTLY AND TRANSVERSELY THROUGH SAID STREAM OF QUENCH SOLIDS BEFORE ANY SUBSTANTIAL INTERMINGLING OF SAID HEATING SOLIDS AND SAID QUENCH SOLIDS HAS OCCURRED, SAID HOT GASES BEING RAPIDLY COOLED THEREBY TO BELOW ABOUT 1400* F., AND RECOVERING ACETYLENE FROM THE COOLED GASES.
Claim 3
Independent Claim
157 words
AN APPARATUS ADAPTED FOR THE PYROLYSIS OF HYDROCARBONS TO ACETYLENE BY CONTACT WITH GRANULAR HEAT-TRANSFER MEDIA COMPRISING IN COMBINATION AN UPPER SOLIDS HEATING CHAMBER, TUBULAR REACTOR COMMUNICATING WITH THE LOWER PORTION OF SAID HEATING CHAMBER THROUGH A CONSTRICTED THROAT, FEED GAS INLET PORT COMMUNICATING WITH THE LOWER PORTION OF SAID THROAT AND POSITIONED IN SOLIDS-ASPIRATING RELATIONSHIP THEREWITH, A SURGE-VESSEL POSITIONED AROUND SAID REACTOR, THE LOWER PORTION OF SAID SURGE-VESSEL BEING HORIZONTALLY SPACED OUTWARDLY FROM SAID REACTOR, BEING THEREBY ADAPTED TO FLOW A STREAM OF SOLIDS DOWNWARDLY PAST THE LOWER END OF SAID REACTOR, A SOLIDS-RECEIVING VESSEL POSITONED BELOW THE LOWER END OF SAID REACTOR AND COMMUNICATING DIRECTLY THEREWITH, SAID SOLIDS-RECEIVING VESSEL HAVING A GAS OUTLET PORT, A SOLDIS ELEVATOR ADAPTED TO TRANSFER SOLIDS DIRECTLY FROM SAID SOLIDS-RECEIVING VESSEL TO A HOPPER POSITIONED ABOVE SAID HEATING CHAMBER CONDUITS CONNECTING SAID HOPPER WITH SAID SURGE-VESSEL AND WITH SAID HEATING CHAMBER, AND MEANS FOR COOLING SOLIDS FLOWING TO SAID SURGE-VESSEL.
Claim 4
Independent Claim
157 words
AN APPARATUS ADAPTED FOR THE PYROLYSIS OF HYDROCARBONS TO ACETYLENE BY CONTACT WITH GRANULAR HEAT-TRANSFER MEDIA COMPRISING IN COMBINATION AN UPPER SOLIDS HEATING CHAMBER, TUBULAR REACTOR COMMUNICATING WITH THE LOWER PORTION OF SAID HEATING CHAMBER THROUGH A CONSTRICTED THROAT, FEED GAS INLET PORT COMMUNICATING WITH THE LOWER PORTION OF SAID THROAT AND POSITIONED IN SOLIDS-ASPIRATING RELATIONSHIP THEREWITH, A SURGE-VESSEL POSITIONED AROUND SAID REACTOR, THE LOWER PORTION OF SAID SURGE-VESSEL BEING HORIZONTALLY SPACED OUTWARDLY FROM SAID REACTOR, BEING THEREBY ADAPTED TO FLOW A STREAM OF SOLIDS DOWNWARDLY PAST THE LOWER END OF SAID REACTOR, A SOLIDS-RECEIVING VESSEL POSITONED BELOW THE LOWER END OF SAID REACTOR AND COMMUNICATING DIRECTLY THEREWITH, SAID SOLIDS-RECEIVING VESSEL HAVING A GAS OUTLET PORT, A SOLDIS ELEVATOR ADAPTED TO TRANSFER SOLIDS DIRECTLY FROM SAID SOLIDS-RECEIVING VESSEL TO A HOPPER POSITIONED ABOVE SAID HEATING CHAMBER CONDUITS CONNECTING SAID HOPPER WITH SAID SURGE-VESSEL AND WITH SAID HEATING CHAMBER, AND MEANS FOR COOLING SOLIDS FLOWING TO SAID SURGE-VESSEL.
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) | 1959-04-10 | 1959-10-10 | 1960-04-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1963-04-10 | 1963-10-10 | 1964-04-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1967-04-10 | 1967-10-10 | 1968-04-10 | $7700.00 | Window Closed / Lapsed |