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US3225516A Expired / Lapsed US ⏱️ 0.0 years remaining

Method and apparatus for purifying gaseous mixtures by cyclic adsorption

Assignee: CM Kemp Manufacturing Co
•
Filing: 1963-04-15
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Granted: 1965-12-28
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Expires: 1983-04-15
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Abstract

No abstract record available.

Inventors

  • 👤 Smith Weston Emerson
  • 👤 Lehmann Wallace Kemp

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 10:51
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D2256/00; B01D2256/10; B01D2257/00; B01D2257/30; B01D2257/302; B01D2257/304; B01D2257/50; B01D2257/504; B01D2257/80; B01D2259/00; B01D2259/40; B01D2259/402; B01D2259/41; Y; Y02; Y02C; Y02C20/00; Y02C20/40

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 244 words
A PROCESS FOR CONTINUOUS NON-SELECTIVE SEPARATION OF IMPURITIES FROM A GAS STREAM CONTAINING COMBUSTION PRODUCTS OF A HYDROCARBON FUEL WHICH COMPRISES ALTERNATELY ADSORBING THE GREATER PROPORTION OF THE INPURITIES FROM A GAS STREAM IN ONE OF TWO FIRST ADSORBENT BEDS ARRANGED FOR ALTERNATELY SHIFTING BETWEEN CYCLES OF HIGH PRESSURE ADSORPTION AND LOW PRESSURE DESORPTION AND CONTROLLED SO AS TO OPERATE FOR SHORT PERIODS OF CYCLIC ADSORPTION AND DESORPTION, CONTINUOUSLY RECOVERING A PARTIALLY PURIFIED EFFLUENT FROM ONE OF SAID ADSORBENT BEDS, ALTERNATELY ADSORBING SUBSTANTIALLY ALL OF THE REMAINING IMPURTIES FROM SAID PARTIALLY PURIFIED GAS IN ANOTHER ONE OF TWO SECOND ADSORBENT BEDS ARRANGED FOR ALTERNATELY SHIFTING BETWEEN CYCLES OF HIGH PRESSURE ADSORPTION AND LOW PRESSURE DESORPTION AND CONTROLLED SO AS TO OPERATE FOR EXTENDED PERIODS OF CYCLIC ADSORPTION AND DESORPTION, CONTINUOUSLY RECOVERING A SUBSTANTIALLY PURIFIED GAS FROM ONER OF SAID SECOND ADSORBENT BEDS; AT THE SAME TIME, DIVERTING A PORTION OF THE RECOVERED PURIFIED EFFLUENT GAS TO A DISTRIBUTION ZONE, PASSING THE MAJOR PORTION OF THE PURIFIED EFFLUENT FROM THE DISTRIBUTION ZONE THROUGH A PRESSURE REDUCING ZONE TO EXPAND THE PURIFIED EFFLUENT, PURGING THE IMPURITIES FROM THE OTHER OF SID FIRST ADSORBENT BEDS WITH SAID EXPANDED PURIFIED EFFLUENT, PASSING THE REMAINING PORTION OF GAS IN SAID DISTRIBUTION ZONE TO ANOTHER PRESSURE REDUCING ZONE, AND PURGING THE IMPURITIES FROM THE OTHER OF SAID SECOND ADSORBENT BEDS WITH SAID REMAINING PORTION OF SAID PURIFIED EFFLUENT WHILE SUPPLYING HEAT TO SAID SECOND ADSORBENT BED DURING THE DESORPTION CYCLE.
Claim 2
Dependent Claim 244 words
A PROCESS FOR CONTINUOUS NON-SELECTIVE SEPARATION OF IMPURITIES FROM A GAS STREAM CONTAINING COMBUSTION PRODUCTS OF A HYDROCARBON FUEL WHICH COMPRISES ALTERNATELY ADSORBING THE GREATER PROPORTION OF THE INPURITIES FROM A GAS STREAM IN ONE OF TWO FIRST ADSORBENT BEDS ARRANGED FOR ALTERNATELY SHIFTING BETWEEN CYCLES OF HIGH PRESSURE ADSORPTION AND LOW PRESSURE DESORPTION AND CONTROLLED SO AS TO OPERATE FOR SHORT PERIODS OF CYCLIC ADSORPTION AND DESORPTION, CONTINUOUSLY RECOVERING A PARTIALLY PURIFIED EFFLUENT FROM ONE OF SAID ADSORBENT BEDS, ALTERNATELY ADSORBING SUBSTANTIALLY ALL OF THE REMAINING IMPURTIES FROM SAID PARTIALLY PURIFIED GAS IN ANOTHER ONE OF TWO SECOND ADSORBENT BEDS ARRANGED FOR ALTERNATELY SHIFTING BETWEEN CYCLES OF HIGH PRESSURE ADSORPTION AND LOW PRESSURE DESORPTION AND CONTROLLED SO AS TO OPERATE FOR EXTENDED PERIODS OF CYCLIC ADSORPTION AND DESORPTION, CONTINUOUSLY RECOVERING A SUBSTANTIALLY PURIFIED GAS FROM ONER OF SAID SECOND ADSORBENT BEDS; AT THE SAME TIME, DIVERTING A PORTION OF THE RECOVERED PURIFIED EFFLUENT GAS TO A DISTRIBUTION ZONE, PASSING THE MAJOR PORTION OF THE PURIFIED EFFLUENT FROM THE DISTRIBUTION ZONE THROUGH A PRESSURE REDUCING ZONE TO EXPAND THE PURIFIED EFFLUENT, PURGING THE IMPURITIES FROM THE OTHER OF SID FIRST ADSORBENT BEDS WITH SAID EXPANDED PURIFIED EFFLUENT, PASSING THE REMAINING PORTION OF GAS IN SAID DISTRIBUTION ZONE TO ANOTHER PRESSURE REDUCING ZONE, AND PURGING THE IMPURITIES FROM THE OTHER OF SAID SECOND ADSORBENT BEDS WITH SAID REMAINING PORTION OF SAID PURIFIED EFFLUENT WHILE SUPPLYING HEAT TO SAID SECOND ADSORBENT BED DURING THE DESORPTION CYCLE.

References Cited (Backward Citations)

US3103425A Cited
US2712981A Cited
US2882243A Cited
US2944627A Cited
US3102013A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1968-12-27 1969-06-28 1969-12-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1972-12-27 1973-06-28 1973-12-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1976-12-27 1977-06-28 1977-12-28 $7700.00 Window Closed / Lapsed

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