US3929438A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Refrigeration process
Assignee: Phillips Petroleum Co
•
Filing: 1974-03-04
•
Granted: 1975-12-30
•
Expires: 1994-03-04
Abstract
Abstract A refrigeration process employing a single- or plural-stage flashing of a refrigerant liquid to obtain high and/or intermediate temperature cooling, and condensation of refrigerant vapor and subsequent flashing thereof to obtain low temperature cooling, of a heat exchange zone so as to remove heat from said zone. In one embodiment, a gas is passed through said heat exchange zone in heat exchange relationship with said refrigerants and at least partially liquefied.
Inventors
- 👤 Ernest A Harper
- 👤 Dunn M Bailey
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 22:59
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/0228; F25J3/0242; C; C07; C07C; C07C7/00; C07C7/04; F25J1/00; F25J1/0002; F25J1/0022; F25J1/003; F25J1/0032; F25J1/004; F25J1/0045; F25J1/0047; F25J1/0052; F25J1/0055; F25J1/02; F25J1/0211; F25J1/0212; F25J1/0228; F25J1/0229; F25J1/0243; F25J1/0244; F25J1/0245; F25J1/0249; F25J1/025; F25J1/0257; F25J1/0258; F25J1/0262; F25J1/0279; F25J1/0292; F25J3/0204; F25J3/0209; F25J3/0233; F25J2200/00; F25J2200/02; F25J2200/30; F25J2200/74; F25J2205/00; F25J2205/02; F25J2205/04; F25J2210/00; F25J2210/06; F25J2245/00; F25J2245/02; F25J2270/00; F25J2270/90; F25J2270/902; F25J2280/00; F25J2280/02; F25J2290/00; F25J2290/32; F25J2290/40
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
294 words
A PROCESS FOR RECOVERING A MIXTURE COMPRISING ETHANE AND PROPANE FROM NATURAL GAS, WHICH PROCESS COMPRISES, IN COMBINATION, THE STEPS OF: A. COOLING SAID NATURAL GAS PARTIALLY TO LIQUEFY SAID NATURAL GAS; B. DISTILLING SAID PARTIALLY LIQUEFIED GAS FROM STEP (A) IN A FIRST DISTILLATION ZONE TO RECOVER AN OVERHEAD STREAM COMPRISING METHANE, ETHANE, AND PROPANE, AND TO RECOVER FROM A FIRST REBOILER ZONE OF SAID FIRST DISTILLATION ZONE A BOTTOMS STREAM COMPRISING SOME PROPANE AND HIGHER BOILING HYDROCARBONS; C. PARTIALLY CONDENSING SAID OVERHEAD STREAM FROM STEP (B); D. IN A SECOND DISTILLATION ZONE, DISTILLING A FEED, AS OBTAINED BELOW, TO RECOVER FROM SAID SECOND DISTILLATION ZONE AN OVERHEAD STREAM COMPRISING METHANE WHICH OVERHEAD STREAM IS THEN COMBINED WITH SAID OVERHEAD STREAM FROM STEP (B) AND PASSED TO A COMMON ACCUMULATOR TO FORM A MIXTURE; E. REMOVING A STEAM COMPRISING METHANE FROM SAID COMMON ACCUMULATOR ZONE; F. RETURNING A FIRST PORTION OF SAID ACCUMULATOR MIXTURE TO SAID FIRST DISTILLATION ZONE AS REFLUX TO THE FIRST DISTALLATION ZONE; G. PASSING A SECOND PORTION OF SID ACCUMULATOR MIXTURE CONTROLLED IN ACCORDANCE WITH THE LIQUID LEVEL IN SAID REBOILER REGION OF THE SECOND DISTILLATION ZONE TO THE SECOND DISTILLATION ZONE AS FEED TO SAID SECOND DISTILLATION ZONE; H. RECOVERING A BOTTOMS STEAM COMPRISING ETHANE AND PROPANE, AS A PRODUCT OF THE PROCESS, FROM A SECOND REBOILER ZONE IN SAID SECOND DISTILLATION ZONE, SAID SECOND REBOILER ZONE HEATED BY INDIRECT HEAT EXCHANGE WITH LIQUID FROM SAID FIRST REBOILER ZONE SAID LIQUID FLOW CONTROLLED IN ACCORDANCE WITH THE TEMPERATURE IN SAID SECOND REBOILER ZONE; AND I. CONTROLLING THE AMOUNT OF HEAT SUPPLIED TO SAID FIRST REBOILER ZONE IN ACCORDANCE WITH THE LEVEL IN THE COMMON ACCUMULATOR ZONE SO AS TO MAINTAIN A DESIRED LEVEL IN SAID COMMON ACCUMULATOR ZONE.
Claim 2
Dependent Claim
294 words
A PROCESS FOR RECOVERING A MIXTURE COMPRISING ETHANE AND PROPANE FROM NATURAL GAS, WHICH PROCESS COMPRISES, IN COMBINATION, THE STEPS OF: A. COOLING SAID NATURAL GAS PARTIALLY TO LIQUEFY SAID NATURAL GAS; B. DISTILLING SAID PARTIALLY LIQUEFIED GAS FROM STEP (A) IN A FIRST DISTILLATION ZONE TO RECOVER AN OVERHEAD STREAM COMPRISING METHANE, ETHANE, AND PROPANE, AND TO RECOVER FROM A FIRST REBOILER ZONE OF SAID FIRST DISTILLATION ZONE A BOTTOMS STREAM COMPRISING SOME PROPANE AND HIGHER BOILING HYDROCARBONS; C. PARTIALLY CONDENSING SAID OVERHEAD STREAM FROM STEP (B); D. IN A SECOND DISTILLATION ZONE, DISTILLING A FEED, AS OBTAINED BELOW, TO RECOVER FROM SAID SECOND DISTILLATION ZONE AN OVERHEAD STREAM COMPRISING METHANE WHICH OVERHEAD STREAM IS THEN COMBINED WITH SAID OVERHEAD STREAM FROM STEP (B) AND PASSED TO A COMMON ACCUMULATOR TO FORM A MIXTURE; E. REMOVING A STEAM COMPRISING METHANE FROM SAID COMMON ACCUMULATOR ZONE; F. RETURNING A FIRST PORTION OF SAID ACCUMULATOR MIXTURE TO SAID FIRST DISTILLATION ZONE AS REFLUX TO THE FIRST DISTALLATION ZONE; G. PASSING A SECOND PORTION OF SID ACCUMULATOR MIXTURE CONTROLLED IN ACCORDANCE WITH THE LIQUID LEVEL IN SAID REBOILER REGION OF THE SECOND DISTILLATION ZONE TO THE SECOND DISTILLATION ZONE AS FEED TO SAID SECOND DISTILLATION ZONE; H. RECOVERING A BOTTOMS STEAM COMPRISING ETHANE AND PROPANE, AS A PRODUCT OF THE PROCESS, FROM A SECOND REBOILER ZONE IN SAID SECOND DISTILLATION ZONE, SAID SECOND REBOILER ZONE HEATED BY INDIRECT HEAT EXCHANGE WITH LIQUID FROM SAID FIRST REBOILER ZONE SAID LIQUID FLOW CONTROLLED IN ACCORDANCE WITH THE TEMPERATURE IN SAID SECOND REBOILER ZONE; AND I. CONTROLLING THE AMOUNT OF HEAT SUPPLIED TO SAID FIRST REBOILER ZONE IN ACCORDANCE WITH THE LEVEL IN THE COMMON ACCUMULATOR ZONE SO AS TO MAINTAIN A DESIRED LEVEL IN SAID COMMON ACCUMULATOR ZONE.
References Cited (Backward Citations)
US2610704A
Cited
US2666019A
Cited
US2777305A
Cited
US2823523A
Cited
US2988894A
Cited
US3212276A
Cited
US3318102A
Cited
US3304727A
Cited
US3309882A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1978-12-29 | 1979-06-30 | 1979-12-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-12-29 | 1983-06-30 | 1983-12-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-12-29 | 1987-06-30 | 1987-12-30 | $7700.00 | Window Closed / Lapsed |