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US2713601A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of acetylene

Assignee: Union Oil Company of California
•
Filing: 1951-07-28
•
Granted: 1955-07-19
•
Expires: 1971-07-28
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Abstract

No abstract record available.

Inventors

  • 👤 John L Bills

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 05:20
CPC Classifications
C; C07; C07C; C07C2/00; C07C2/76; C07C2/78; Y; Y10; Y10S; Y10S585/00; Y10S585/909; Y10S585/91

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 288 words
THE PROCESS FOR PRODUCING ACETYLENE WHICH COMPRISES (1) PREHEATING A REACTANT GAS CONSISTING ESSENTIALLY OF OXYGEN AND A NON-AROMATIC HYDROCARBON HAVING A NORMAL BOILING POINT BELOW ABOUT 400* C. TO A TEMPERATURE BELOW THAT AT WHICH REACTION BETWEEN THE COMPONENTS THEREOF TAKES PLACE TO ANY SUBSTANTIAL EXTENT; (2) INITIATING AN ACETYLENE-PRODUCING REACTION BY INTRODUCING INTO THE PREHEATED REACTANT GAS A HYDROGEN-CONTAINING GAS AT A TEMPERATURE BELOW THAT AT WHICH ANY SUBSTANTIAL AMOUNT OF ATOMIC HYDROGEN IS FORCED, SAID HYDROGENCONTAINING GAS BEING PROVIDED IN A AMOUNT SUFFICIENT TO PROVIDE BETWEEN ABOUT 0.5 AND ABOUT 5 MOLES OF HYDROGEN PER MOLE OF SAID HYDROCARBON; (3) CONTROLLING THE TEMPERATURES OF SAID PREHEATED REACTANT GAS AND SAID HYDROGEN-CONTAINING GAS SO THAT THE TEMPERATURE ATTAINED IN SAID ACETYLENE-PRODUCING REACTION IS BETWEEN ABOUT 1100* C. AND ABOUT 1500* C.; (4) WITHIN FROM ABOUT 0.001 TO ABOUT 0.05 SECOND AFTER INTRODUCTION OF THE SAID HYDROGEN-CONTAINING GAS INTO THE SAID PREHEATED RECTANT GAS, COOLING THE PRODUCT GAS TO A TEMPERATURE SUBSTANTIALLY ABOVE THE BOILING POINT OF WATER BUT AT WHICH SUBSTANTIALLY NO FURTHER REACTION OCCURS; (5) PASSING THE COOLED PRODUCT GAS IN INDIRECT HEAT EXCHANGE RELATIONSHIP WITH WATER TO GENERATE STEAM AND FURTHER COOL THE PRODUCT GAS; (6) PASSING SAID STEAM IN CONTACT WITH A MATERIAL SELECTED FROM THE CLASS CONSISTING OF METALS AND METAL OXIDES CAPABLE OF REDUCING STEAM AND MAINTAINED AT A STEAM-REDUCING TEMPERATURE TO FORM A HYDROGENCONTAINING GAS AND A HIGHER METAL OXIDE; (7) RETURNING THE HYDROGEN-CONTAINING GAS SO FORMED TO THE AFORESAID STEP 2; (8) SEPARATING ACETYLENE FROM THE COOLED PRODUCT GAS; AND (9) PASSING THE ACETYLENE-FREE PRODUCT GAS IN CONTACT WITH SAID HIGHER METAL OXIDE AT A REDUCING TEMPERATURE TO REDUCE SAID METAL OXIDE TO A LOWER STEAM-REDUCING STATE OF OXIDATION.
Claim 2
Dependent Claim 288 words
THE PROCESS FOR PRODUCING ACETYLENE WHICH COMPRISES (1) PREHEATING A REACTANT GAS CONSISTING ESSENTIALLY OF OXYGEN AND A NON-AROMATIC HYDROCARBON HAVING A NORMAL BOILING POINT BELOW ABOUT 400* C. TO A TEMPERATURE BELOW THAT AT WHICH REACTION BETWEEN THE COMPONENTS THEREOF TAKES PLACE TO ANY SUBSTANTIAL EXTENT; (2) INITIATING AN ACETYLENE-PRODUCING REACTION BY INTRODUCING INTO THE PREHEATED REACTANT GAS A HYDROGEN-CONTAINING GAS AT A TEMPERATURE BELOW THAT AT WHICH ANY SUBSTANTIAL AMOUNT OF ATOMIC HYDROGEN IS FORCED, SAID HYDROGENCONTAINING GAS BEING PROVIDED IN A AMOUNT SUFFICIENT TO PROVIDE BETWEEN ABOUT 0.5 AND ABOUT 5 MOLES OF HYDROGEN PER MOLE OF SAID HYDROCARBON; (3) CONTROLLING THE TEMPERATURES OF SAID PREHEATED REACTANT GAS AND SAID HYDROGEN-CONTAINING GAS SO THAT THE TEMPERATURE ATTAINED IN SAID ACETYLENE-PRODUCING REACTION IS BETWEEN ABOUT 1100* C. AND ABOUT 1500* C.; (4) WITHIN FROM ABOUT 0.001 TO ABOUT 0.05 SECOND AFTER INTRODUCTION OF THE SAID HYDROGEN-CONTAINING GAS INTO THE SAID PREHEATED RECTANT GAS, COOLING THE PRODUCT GAS TO A TEMPERATURE SUBSTANTIALLY ABOVE THE BOILING POINT OF WATER BUT AT WHICH SUBSTANTIALLY NO FURTHER REACTION OCCURS; (5) PASSING THE COOLED PRODUCT GAS IN INDIRECT HEAT EXCHANGE RELATIONSHIP WITH WATER TO GENERATE STEAM AND FURTHER COOL THE PRODUCT GAS; (6) PASSING SAID STEAM IN CONTACT WITH A MATERIAL SELECTED FROM THE CLASS CONSISTING OF METALS AND METAL OXIDES CAPABLE OF REDUCING STEAM AND MAINTAINED AT A STEAM-REDUCING TEMPERATURE TO FORM A HYDROGENCONTAINING GAS AND A HIGHER METAL OXIDE; (7) RETURNING THE HYDROGEN-CONTAINING GAS SO FORMED TO THE AFORESAID STEP 2; (8) SEPARATING ACETYLENE FROM THE COOLED PRODUCT GAS; AND (9) PASSING THE ACETYLENE-FREE PRODUCT GAS IN CONTACT WITH SAID HIGHER METAL OXIDE AT A REDUCING TEMPERATURE TO REDUCE SAID METAL OXIDE TO A LOWER STEAM-REDUCING STATE OF OXIDATION.

References Cited (Backward Citations)

GB332731A Cited
US2167471A Cited
GB479438A Cited
US2449635A Cited
US2549240A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1958-07-18 1959-01-17 1959-07-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1962-07-18 1963-01-17 1963-07-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1966-07-18 1967-01-17 1967-07-19 $7700.00 Window Closed / Lapsed

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