Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
243 words
In a cyclic process for substantially reducing the carbon dioxide and/or hydrogen sulfide content present as acidic gases in a gas obtained from the cracking of a hydrocarbon selected from the group consisting of gas oil, naphtha and ethane, and said gas further containing undesirable organic impurities therein, with simultaneous regeneration of reagent materials which comprises: a. passing the cracked gas containing the acidic gases through an aqueous sodium hydroxide solution and obtaining an effluent containing the undesirable organic impurities and said acidic gases in converted form; b. reacting said effluent liquid with aqueous sulfuric acid or an aqueous mixture containing sulfuric acid and sodium sulfate in an amount sufficient to substantially liberate the converted acidic gases consisting essentially of hydrogen sulfide and/or carbon dioxide that may be present therein; c. subjecting said treated effluent liquid to a stripping operation to remove any liberated gases therefrom and thereby leaving an aqueous sodium sulfate containing solution; and d. subjecting said resulting aqueous sodium sulfate containing solution to an electrolytic process treatment whereby aqueous sulfuric acid or an aqueous mixture of sulfuric acid and sodium sulfate is collected at the anode and is recycled for utilization in the aforesaid reaction step and aqueous sodium hydroxide which forms at the cathode is collected and recycled for use in the sodium hydroxide treatment step, the improvement which comprises treating the effluent from the alkali metal hydroxide treatment of step (a) to remove substantially all organic impurities therefrom.
Claim 2
Dependent Claim
243 words
In a cyclic process for substantially reducing the carbon dioxide and/or hydrogen sulfide content present as acidic gases in a gas obtained from the cracking of a hydrocarbon selected from the group consisting of gas oil, naphtha and ethane, and said gas further containing undesirable organic impurities therein, with simultaneous regeneration of reagent materials which comprises: a. passing the cracked gas containing the acidic gases through an aqueous sodium hydroxide solution and obtaining an effluent containing the undesirable organic impurities and said acidic gases in converted form; b. reacting said effluent liquid with aqueous sulfuric acid or an aqueous mixture containing sulfuric acid and sodium sulfate in an amount sufficient to substantially liberate the converted acidic gases consisting essentially of hydrogen sulfide and/or carbon dioxide that may be present therein; c. subjecting said treated effluent liquid to a stripping operation to remove any liberated gases therefrom and thereby leaving an aqueous sodium sulfate containing solution; and d. subjecting said resulting aqueous sodium sulfate containing solution to an electrolytic process treatment whereby aqueous sulfuric acid or an aqueous mixture of sulfuric acid and sodium sulfate is collected at the anode and is recycled for utilization in the aforesaid reaction step and aqueous sodium hydroxide which forms at the cathode is collected and recycled for use in the sodium hydroxide treatment step, the improvement which comprises treating the effluent from the alkali metal hydroxide treatment of step (a) to remove substantially all organic impurities therefrom.
Claim 3
Dependent Claim
15 words
The process according to claim 1 wherein said aqueous sodium hydroxide solution contains sodium sulfate.
Claim 4
Dependent Claim
18 words
The process according to claim 1 wherein said sodium hydroxide which forms at the cathode contains sodium sulfate.
Claim 5
Dependent Claim
33 words
The process according to claim 1 wherein to the cathode compartment involved in the electrolytic process is added aqueous sodium sulfate in an amount sufficient to maintain the electrolytic membrane free from solids.
Claim 6
Dependent Claim
17 words
The process according to claim 1 wherein said effluent liquid contains a small amount of sodium hydroxide.
Claim 7
Dependent Claim
16 words
The process according to claim 1 wherein said effluent liquid contains sodium bisulfide and/or sodium bicarbonate.
Claim 8
Dependent Claim
22 words
The process according to claim 1 wherein the effluent liquid from sodium hydroxide contacting is extracted with a substantially water-immiscible organic solvent.
Claim 9
Dependent Claim
25 words
The process according to claim 7 wherein said organic solvent is a hydrocarbon having a boiling point no higher than that of a gas oil.
Claim 10
Dependent Claim
13 words
The process according to claim 8 wherein said hydrocarbon solvent is a naphtha.
Claim 11
Dependent Claim
14 words
The process according to claim 8 wherein said hydrocarbon solvent is a gas oil.
Claim 12
Dependent Claim
19 words
The process according to claim 1 wherein said effluent liquid from sodium hydroxide contacting is contacted with an adsorbent.
Claim 13
Dependent Claim
24 words
The process according to claim 1 wherein said sodium hydroxide treatment step consists of contacting said gas substantially countercurrently with said sodium hydroxide solution.
Claim 14
Dependent Claim
22 words
The process according to claim 1 wherein the liberated gases from the stripping operation include hydrogen sulfide which is converted to sulfur.
Claim 15
Dependent Claim
25 words
The process according to claim 1 wherein the aqueous sodium sulfate from the stripping operation is filtered before it is subjected to the electrolytic process.
Claim 16
Dependent Claim
32 words
The process according to claim 1 wherein said electrolytic process is carried out in an electrolytic cell capable of converting soluble alkali metal salts into their corresponding alkali metal hydroxides and acids.
Claim 17
Dependent Claim
24 words
The process according to claim 15 wherein said soluble alkali metal salt is sodium sulfate which is converted to sodium hydroxide and sulfuric acid.
Claim 18
Dependent Claim
56 words
The process according to claim 15 wherein said electrolytic cell is a three compartment cell comprising a cathode compartment, a center compartment and an anode compartment, the cathode compartment being separated from the center compartment by a cation selective ion exchange membrane and the center compartment being separated from the anode compartment by a fluid-permeable diaphram.