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US3358460A Expired / Lapsed US ⏱️ 0.0 years remaining

Nitrogen liquefaction with plural work expansion of feed as refrigerant

Assignee: Airco Inc
•
Filing: 1965-10-08
•
Granted: 1967-12-19
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Expires: 1985-10-08
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Abstract

Abstract 1,099,669. Gas liquefaction process. AIR REDUCTION CO. Oct. 7, 1966 [Oct. 8, 1965], No. 44923/66. Heading F4P. Liquefaction of a gas, e.g. effluent nitrogen from the low pressure column (103), Fig. 6 (not shown), of a two stage air rectification plant is effected by compression to not more than 2À5 times the critical pressure of the gas at 151, 153, 155, 157, 159, 163, 166 cooling in means including paths a, a<SP>1</SP> of a first heat exchanger 169, dividing the cooled gas at 186 into a minor portion which is cooled without liquefaction in path a of a second exchanger 192 and into a major portion which is work-expanded in turbines 188, 194, with intervening warming in a path a of exchanger 192 from which latter the cooled minor portion is passed through a line 203 and is throttle-expanded at 204, 209, 213 into a product liquid storage vessel 213; uncondensed vapour from the latter being forced by a pump 217 through paths c of exchangers 192, 169 and a line 221 to the compressor inlets where it is joined by the work expanded major portion. The compressed feed gas is withdrawn from path a of exchanger 169 cooled by external refrigeration means 175 and is then returned to path a of exchanger 169. Throttle valve 204 discharges into a separater 206 which also condenses oxygen. Vapour above liquid oxygen storage vessel 112 and a portion of condensed nitrogen is passed along a line 122 to provide additional reflux for the column (103).

Inventors

  • 👤 Donald L Smith
  • 👤 John L Ferrell

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 09:14
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04187; F25J3/0423; F25J1/00; F25J1/0002; F25J1/0012; F25J1/0015; F25J1/0017; F25J1/003; F25J1/0032; F25J1/0035; F25J1/0037; F25J1/004; F25J1/02; F25J1/0203; F25J1/0208; F25J1/0228; F25J1/0234; F25J1/0243; F25J1/0279; F25J1/0285; F25J1/0288; F25J3/04157; F25J3/04218; F25J3/04224; F25J3/04242; F25J3/04248; F25J3/04278; F25J3/04284; F25J3/0429; F25J3/04303; F25J3/04333; F25J3/04351; F25J3/04357; F25J3/04375; F25J3/04393; F25J3/04406; F25J3/04412; F25J3/04763; F25J3/04769; F25J3/04854; F25J2205/00; F25J2205/02; F25J2205/04; F25J2205/60; F25J2230/00; F25J2230/08; F25J2230/42; F25J2235/00; F25J2235/50; F25J2245/00; F25J2245/90; F25J2270/00; F25J2270/04; F25J2270/06; F25J2270/90; F25J2290/00; F25J2290/10; F25J2290/34; F25J2290/62; Y; Y10; Y10S; Y10S62/00; Y10S62/912; Y10S62/913

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 282 words
IN A CYCLE FOR THE LIQUEFACTION OF LOW BOILING GAS WHICH COMPRISES THE STEPS OF: COMPRESSING A PRIMARY STREAM INCLUDING THE FEED STREAM OF SAID GAS TO A HEAD PRESSURE NOT EXCEEDING ABOUT TWO AND ONE-HALF TIMES THE CRITICAL PRESSURE OF SAID GAS, COOLING SAID COMPRESSED PRIMARY STREAM THROUGH A FIRST COOLING STEP IN A FIRST HEAT EXCHANGER, FURTHER COOLING AT LEAST A PORTION OF SAID COMPRESSED PRIMARY STREAM THROUGH A SECOND COOLING STEP IN A SECOND HEAT EACHANGER, WITHOUT SUBSTANTIAL LIQUEFACTION THEREOF, ISENTHALPICALLY EXPANDING SAID COMPRESSED PORTION AFTER SAID SECOND COOLING STEP TO A LOW PRESSURE TO FORM A LIQUID FRACTION AND A REMAINING VAPOR FRACTION, AND RETURNING THE REMAINING LOW PRESSURE VAPOR FRACTION OF SAID PORTION AT SAID LOW PRESSURE FOR RECOMPRESSION AND RECYCLING THROUGH A PATH INCLUDING SAID HEAT EXCHANGERS IN COUNTERCURRENT WITH STREAMS BEING COOLED INCLUDING SAID COMPRESSED PORTION; THE IMPROVEMENT WHICH COMPRISES: SEPARATING SAID COMPRESSED PRIMARY STREAM BEFORE SAID SEOND COOLING STEP INTO A MAJOR PORTION AND A MINOR PORTION, WHEREBY THE COMPRESSED PORTION FURTHER COOLED IN SAID SECOND HEAT EXCHANGER IS SAID MINOR PORTION, WITHDRAWING AND EXPANDING SAID MAJOR PORTION THROUGH A PLURALITY OF WORK EXPANSION STEPS WHEREIN SAID MAJOR PORTION IS COOLED AND EXPANDED TO A MEDIUM-LOW PRESSURE WITHOUT LIQUEFACTION, EACH OF SAID WORK EXPANSION STEPS BEING SEPARATED BY AN INTERVENING REHEAT STEP WHEREIN THE STREAM COMPRISING SAID MAJOR PORTION IS WARMED UP IN SAID SECOND HEAT EXCHANGER IN COUNTERCURRENT WITH STREAMS BEING COOLED INCLUDING SAID COMPRESSED MINOR PORTION, AND AFTER SAID FINAL WORK EXPANSION STEP, RETURNING SAID MAJOR PORTION AT A MEDIUM-LOW PRESSURE WITHOUT LIQUEFACTION THROUGH SAID HEAT EXCHANGERS IN COUNTERCURRENT WITH STREAMS BEING COOLED INCLUDING SAID COMPRESSED MINOR PORTION, FOR RECOMPRESSION AND RECYCLING.
Claim 2
Dependent Claim 282 words
IN A CYCLE FOR THE LIQUEFACTION OF LOW BOILING GAS WHICH COMPRISES THE STEPS OF: COMPRESSING A PRIMARY STREAM INCLUDING THE FEED STREAM OF SAID GAS TO A HEAD PRESSURE NOT EXCEEDING ABOUT TWO AND ONE-HALF TIMES THE CRITICAL PRESSURE OF SAID GAS, COOLING SAID COMPRESSED PRIMARY STREAM THROUGH A FIRST COOLING STEP IN A FIRST HEAT EXCHANGER, FURTHER COOLING AT LEAST A PORTION OF SAID COMPRESSED PRIMARY STREAM THROUGH A SECOND COOLING STEP IN A SECOND HEAT EACHANGER, WITHOUT SUBSTANTIAL LIQUEFACTION THEREOF, ISENTHALPICALLY EXPANDING SAID COMPRESSED PORTION AFTER SAID SECOND COOLING STEP TO A LOW PRESSURE TO FORM A LIQUID FRACTION AND A REMAINING VAPOR FRACTION, AND RETURNING THE REMAINING LOW PRESSURE VAPOR FRACTION OF SAID PORTION AT SAID LOW PRESSURE FOR RECOMPRESSION AND RECYCLING THROUGH A PATH INCLUDING SAID HEAT EXCHANGERS IN COUNTERCURRENT WITH STREAMS BEING COOLED INCLUDING SAID COMPRESSED PORTION; THE IMPROVEMENT WHICH COMPRISES: SEPARATING SAID COMPRESSED PRIMARY STREAM BEFORE SAID SEOND COOLING STEP INTO A MAJOR PORTION AND A MINOR PORTION, WHEREBY THE COMPRESSED PORTION FURTHER COOLED IN SAID SECOND HEAT EXCHANGER IS SAID MINOR PORTION, WITHDRAWING AND EXPANDING SAID MAJOR PORTION THROUGH A PLURALITY OF WORK EXPANSION STEPS WHEREIN SAID MAJOR PORTION IS COOLED AND EXPANDED TO A MEDIUM-LOW PRESSURE WITHOUT LIQUEFACTION, EACH OF SAID WORK EXPANSION STEPS BEING SEPARATED BY AN INTERVENING REHEAT STEP WHEREIN THE STREAM COMPRISING SAID MAJOR PORTION IS WARMED UP IN SAID SECOND HEAT EXCHANGER IN COUNTERCURRENT WITH STREAMS BEING COOLED INCLUDING SAID COMPRESSED MINOR PORTION, AND AFTER SAID FINAL WORK EXPANSION STEP, RETURNING SAID MAJOR PORTION AT A MEDIUM-LOW PRESSURE WITHOUT LIQUEFACTION THROUGH SAID HEAT EXCHANGERS IN COUNTERCURRENT WITH STREAMS BEING COOLED INCLUDING SAID COMPRESSED MINOR PORTION, FOR RECOMPRESSION AND RECYCLING.

References Cited (Backward Citations)

US3098732A Cited
US3144316A Cited
US3277655A Cited
US3214926A Cited
US3264830A Cited
US3316725A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1970-12-18 1971-06-19 1971-12-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1974-12-18 1975-06-19 1975-12-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1978-12-18 1979-06-19 1979-12-19 $7700.00 Window Closed / Lapsed

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