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United States Patent (19) 11 4,412,981 Kubicek 45) Nov

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United States Patent (19) 11 4,412,981 Kubicek 45) Nov United States Patent (19) 11 4,412,981 Kubicek 45) Nov. 1, 1983 54 CONVERSION OF HYDROGEN SULFIDE TO 3,103,411 9/1963 Fuchs .............................. 423/224 X SULFUR BY DIRECT OXDATION 3,516,793 6/1970 Renault.... ... 42.3/573 3,914,309 10/1975 Beazley ............ ... 42.3/573 (75) Inventor: Donald H. Kubicek, Bartlesville, 4,313,916 2/1982 Jones et al. ......................... 423/226 Okla. FOREIGN PATENT DOCUMENTS 73) Assignee: Phillips Petroleum Company, Bartlesville, Okla. 1080530 7/1957 Fed. Rep. of Germany ...... 423/573 1492797 8/1967 France ................................ 423/573 597655 5/1945 United Kingdom ... ... 42.3/571 21 Appl. No.: 302,942 84.1610 7/1960 United Kingdom.... ... 42.3/573 (22 Filed: Sep. 16, 1981 1182255 2/1970 United Kingdom................ 423/573 51) Int. Cl........................ C01B 17/04; B01D 53/34 Primary Examiner-Earl C. Thomas 52 U.S.C. ................................ 423/573 R; 423/224; 57) ABSTRACT 423/226; 210/758; 208/235 58) Field of Search ............... 423/224, 226,571, 573; In a process wherein hydrogen sulfide is converted to 208/235; 55/73; 210/758, 763 elemental sulfur in the presence of oxygen, an improve ment is made by employing an alcoholic solution of an 56 References Cited alkali metal hydroxide, free of iron-group salts or other U.S. PATENT DOCUMENTS heterogeneous catalysts. High yields of pure sulfur are 2,556,836 6/1951 Browder et al. obtained from such reactions begun at room tempera 2,600,328 6/1952 Riesenfeld et al. ............. 423/226X ture, without a requirement for heterogeneous catalysts 2,972,522 2/1961 Urban . or troublesome intermediates such as sulfur dioxide. 3,097,926 7/1963 Nickin et al. 3,099,536 7/1963 Urban et al. ........................ 423/575 9 Claims, No Drawings 4,412,981 1. CONVERSION OF HYDROGEN SULFIDE TO SUMMARY OF INVENTION An object of this invention is the removal of hydro SULFUR BY DIRECT oxIDATION gen sulfide from gases comprising hydrogen sulfide, or BACKGROUND OF THE INVENTION 5 containing hydrogen sulfide, or containing hydrogen Hydrogen sulfide is a material commonly available sulfide in any proportion in conjunction with other from many sources and potentially useful when con gases such as carbon dioxide, carbon monoxide, hydro verted to other materials such as elemental sulfur or gen, aliphatic and aromatic hydrocarbons, oxygen and sulfuric acid. However, recovery of hydrogen sulfide 10 nitrogen, and from liquid or gaseous hydrocarbon mix from various sources for conversion is frequently diffi tures. A further object of this invention is the treating, cult or expensive. For example, in the refining of petro or "sweetening' of sour petroleum distillates. Another leum, hydrogen sulfide is produced in large quantities as object is the production of sulfur from hydrogen sulfide. an undesirable dangerous contaminant mixed with OBJECTS larger quantities of other materials. Often hydrogen 15 This invention provides an improved means for the sulfide thus produced is passed into the atmosphere as removal of hydrogen sulfide from gaseous or liquid waste material, since the cost of recovery is not war process streams or other sources and its conversion to ranted by the value of the product recovered. However, elemental sulfur without the need for heterogeneous in populated areas such disposal of hydrogen sulfide catalysts or the production of undesirable intermediates represents a nuisance, and expensive recovery methods 20 such as sulfur dioxide. must be employed. Generally, the process of this invention involves con In some cases hydrogen sulfide must be removed tacting a hydrogen sulfide-containing stream, whether from various process streams to prevent the contamina gaseous or liquid, with an alcoholic solution of an alkali tion of those streams. For example, the presence of metal or alkaline earth metal hydroxide, essentially free sulfur compounds in gasoline is detrimental, since they 25 of iron group salts. The reaction of this invention is have a suppressing effect on octane number and cause carried out substantially free of iron group catalyst the gasoline to be corrosive, unstable and sour. In some materials, particularly free of cobalt salts; this requires process streams hydrogen sulfide must be removed to that not more than inconsequential amounts of such prevent its detrimental effect upon later employed cata materials are present in the reaction mixture. By simul lysts. For example, in catalytically reforming a gasoline 30 taneously or subsequently adding oxygen or air to the fraction, a net hydrogen production is realized which is resulting solution, the hydrogen sulfide is converted to at least partially recirculated to the reforming zone to elemental sulfur. The reaction is exothermic, beginning saturate olefinic material and to prevent carbonization attemperatures as low as 25 C. By carrying on the of the catalyst. It is desirable for the recycled hydrogen 35 reaction without heterogeneous catalysts, an essentially containing stream to contain as little hydrogen sulfide as pure conversion product of elemental sulfur may be possible, thus preventing its undesirable effects upon the recovered simply and economically. catalyst. Thus, it is often necessary and always desirable The materials required to be absent (except for possi to remove hydrogen sulfide from this and similar ble small, inconsequential amounts) from the system of streams. The present invention provides improved this invention are compounds of group VIII of the Peri means for recovering valuable sulfur as a by-product odic System; in particular, Fe, Co, Ni and their salts. from hydrogen sulfide, thus providing an economical The reaction of this invention may be commenced and efficient means for removing hydrogen sulfide from under mild conditions such as room temperature (25 other materials even though it is present in relatively C.) and atmospheric pressure. Since the reaction is exo 45 thermic, the system temperature will normally increase, low concentrations. with about 100° C. being the practical maximum and 15 The challenge of effective and economical recovery C. to 60° C. the preferred range. Possible feedstocks can and conversion of hydrogen sulfide from its various comprise hydrogen sulfide in essentially pure form, or sources has been approached by various means in the in liquid or gaseous mixtures of aliphatic and aromatic prior art. For instance, U.S. Pat. No. 2,972,522 describes 50 hydrocarbons, carbon dioxide, carbon monoxide, hy the production of sulfur from hydrogen sulfide by the drogen, oxygen and nitrogen. The reaction is most ef absorption of gaseous hydrogen sulfide in an ammonia fective when oxygen is used in a nearly pure state, but cal or amine solution and oxidation with oxygen in the depending upon the feedstock, the partial pressure of presence of a heterogeneous catalyst such as cobalt. oxygen can be controlled to avoid mixtures within the U.S. Pat. No. 3,097,926 describes a process for the re 55 explosive limits of hydrogen sulfide or other flammable moval of hydrogen sulfide from gas or liquid streams by feedstock components. With closed reaction systems, washing with aqueous alkali metal hydroxides contain the reaction may be considered complete when oxygen ing a cobalt salt and a chelating agent in the presence of is no longer absorbed by the system. In other systems, free oxygen. Hydrogen sulfide is thus converted to flow rates must be determined empirically, depending elemental sulfur. In U.S. Pat. No. 2,556,836 a process is 60 upon partial pressures of oxygen and hydrogen sulfide described whereby sour petroleum distillates free from and availability of base, so that the reactants are in hydrogen sulfide are sweetened by treatment with an contact for a sufficient time to produce optimum con alcoholic alkali metal hydroxide in the presence of a version. The alkali metal or alkaline earth metal hydrox mild oxidizing agent such as oxygen. At temperatures of ide is used as a catalyst, thus no particular pH range is 60 to 200 F., mercaptans are converted to disulfides. 65 specified. Hydrogen sulfide and other acidic compounds are re There are four essential ingredients used in the pro ported as causing the alkali metal hydroxide catalyst to cess of this invention, namely, hydrogen sulfide (H2S), quickly become depleted in activity. an alkali or alkaline earth metal hydroxide, a hydroxyl 4,412,981 3 4. containing liquid, and oxygen. Variations within each ranging from approximately 0.1 weight percent to 10 ingredient type are listed in the following paragraphs. weight percent based on the amount of hydroxyl con Hydroxyl-Containing Liquids taining medium. The concentration should be limited to maintain the system as a liquid solution of low to moder Hydroxyl-containing liquids are those materials rep ate viscosity. resented by the formula Solvents ROHO Solvents are not necessarily required in this invention but if used can be any inert aliphatic, cycloaliphatic or where R equals hydrogen or any alkyl or alkylene radi 10 cal having one to six carbon atoms; and n equals the aromatic hydrocarbon having from about five to about valence of R, being 1 or 2. Examples of materials that nine carbon atoms. Such materials include, for example, can be used include but are not limited to, the following: Water methyl alcohol 15 pentane hexane ethyl alcohol n-propyl alcohol heptane octahe isopropyl alcohol butanol cyclopentane methylcyclopentane pentanol hexanol cyclohexane benzene ethylene glycol propylene glycol toluene xylene 1,4-butanediol 1,6-hexanediol 20 and mixtures of two or more of these solvents. and mixtures of two or more of these compounds. The prerequisite for a solvent is that it be capable of The hydroxy-containing liquid is a contact medium dissolving or partially dissolving the ingredients of the for the alkali metal or alkaline earth metal hydroxide, invention, particularly the hydroxyl-containing liquid H2S and oxygen. Therefore, the hydroxy-containing 25 and the metal hydroxide.
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