Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
214 words
IN A PROCESS FOR THE PURIFICATION OF GAS CONTAINING A MAJOR PORTION OF HYDROCARBON A THERMALLY POLYMERIZABLE DIOLEFIN AND AT LEAST ONE ACIDIC COMPONENT SELECTED FROM THE GROUP CONSISTING OF CARBON DIOXIDE AND HYDROGEN SULFIDE, WHICH PROCESS COMPRISES: A. SCRUBBING SAID GAS WITH NORMALLY LIQUID, ALKALINE, HEATREGENERATED SCRUBBING MEANS CAPABLE OF REMOVING THE ACIDIC COMPONENT AND DISSOLVING AT LEAST A PORTION OF SAID POLYMERIZEABLE DIOLEFIN TO FORM LOADED SCRUBBING MEANS CONTAINING SAID ACIDIC COMPONENT AND SIAD POLYMERIZEABLE DIOLEFIN; B. CONTACTING SAID LOADED SCRUBBING MEANS WITH LIQUID HYDROCARBON SOLVENT TO EXTRACT OUT THAN 100% OF SAID THERMALLY POLYMERIZABLE DIOLEFINE, AND SEPARATING RESULTANT LOADED HYDROCARBON SOLVENT FROM RESULTANT HYDROCARBON TREATED SCRUBBING MEANS AND C. THERMALLY REGENERATING SAID RESULTANT HYDROCARBON TREATED LOADED SCRUBBING MEANS IN A REGENERATING COLUMN TO FORM A GASEOUS OVERHEAD CONTAINING SAID AT LEAST ONE ACIDIC COMPONENT AND RESIDUAL THERMALLY POLYMERIZABLE DIOLEFIN, AND A BOTTOMS OF REGENERATED SCRUBBING MEANS, THE IMPROVEMENT WHEREIN SAID GASEOUS OVERHEAD IS COOLED TO FORM A CONDENSATE CONTAINING SAID RESIDUAL THERMALLY POLYMERIZABLE DIOLEFIN, AND PREVENTING RESULTANT CONDENSATE FROM BEING REFLUXED INTO SAID REGENERATING COLUMN THEREBY MIGITATING THE EXTEND OF POLYMERIZATION OF SAID THERMALLY POLYMERIZABLE DIOLEFIN WITHIN SAID REGENERATION COLUMN AND WHEREIN SAID CONDENSATE IS RECYCLED TO THE LOADED SCRUBBING MEANS IMMEDIATELY PRIOR TO THE CONTACTING THEREOF WITH SAID HYDROCARBON SOLVENT.
Claim 2
Dependent Claim
214 words
IN A PROCESS FOR THE PURIFICATION OF GAS CONTAINING A MAJOR PORTION OF HYDROCARBON A THERMALLY POLYMERIZABLE DIOLEFIN AND AT LEAST ONE ACIDIC COMPONENT SELECTED FROM THE GROUP CONSISTING OF CARBON DIOXIDE AND HYDROGEN SULFIDE, WHICH PROCESS COMPRISES: A. SCRUBBING SAID GAS WITH NORMALLY LIQUID, ALKALINE, HEATREGENERATED SCRUBBING MEANS CAPABLE OF REMOVING THE ACIDIC COMPONENT AND DISSOLVING AT LEAST A PORTION OF SAID POLYMERIZEABLE DIOLEFIN TO FORM LOADED SCRUBBING MEANS CONTAINING SAID ACIDIC COMPONENT AND SIAD POLYMERIZEABLE DIOLEFIN; B. CONTACTING SAID LOADED SCRUBBING MEANS WITH LIQUID HYDROCARBON SOLVENT TO EXTRACT OUT THAN 100% OF SAID THERMALLY POLYMERIZABLE DIOLEFINE, AND SEPARATING RESULTANT LOADED HYDROCARBON SOLVENT FROM RESULTANT HYDROCARBON TREATED SCRUBBING MEANS AND C. THERMALLY REGENERATING SAID RESULTANT HYDROCARBON TREATED LOADED SCRUBBING MEANS IN A REGENERATING COLUMN TO FORM A GASEOUS OVERHEAD CONTAINING SAID AT LEAST ONE ACIDIC COMPONENT AND RESIDUAL THERMALLY POLYMERIZABLE DIOLEFIN, AND A BOTTOMS OF REGENERATED SCRUBBING MEANS, THE IMPROVEMENT WHEREIN SAID GASEOUS OVERHEAD IS COOLED TO FORM A CONDENSATE CONTAINING SAID RESIDUAL THERMALLY POLYMERIZABLE DIOLEFIN, AND PREVENTING RESULTANT CONDENSATE FROM BEING REFLUXED INTO SAID REGENERATING COLUMN THEREBY MIGITATING THE EXTEND OF POLYMERIZATION OF SAID THERMALLY POLYMERIZABLE DIOLEFIN WITHIN SAID REGENERATION COLUMN AND WHEREIN SAID CONDENSATE IS RECYCLED TO THE LOADED SCRUBBING MEANS IMMEDIATELY PRIOR TO THE CONTACTING THEREOF WITH SAID HYDROCARBON SOLVENT.
Claim 3
Dependent Claim
19 words
A process as defined by claim 1 wherein said thermally polymerizable diolefin is propadiene, butadiene, cyclopentadiene or mixtures thereof.
Claim 4
Dependent Claim
19 words
A process as defined by claim 2 wherein the thermal regeneration is conducted at 95* C to 120* C.
Claim 5
Dependent Claim
18 words
A process as defined by claim 3 wherein said condensate is cooled down to at least 50* C.
Claim 6
Dependent Claim
36 words
A process as defined by claim 4 wherein said scrubbing means is an aqueous solution of potash, sodium hydroxide, potassium hydroxide, mono-, di-, or triethanolamine, or an aqueous solution of the potassium salt of N-methylaminopropionic acid.
Claim 7
Dependent Claim
19 words
A process as defined by claim 1 wherein the thermal regeneration is conducted at 95* C to 120* C.
Claim 8
Dependent Claim
18 words
A process as defined by claim 6 wherein said condensate is cooled down to at least 50* C.