Classifications

• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
  • C10G27/00—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
  • C10G27/04—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen
  • C10G27/10—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen in the presence of metal-containing organic complexes, e.g. chelates, or cationic ion-exchange resins

Definitions

• This invention relates to the treatment of hydrocarbon distillates and more particularly to a novel method of gaseous fractions.
• the novel .features of the present invention may be utilized for purifying other organic fractions containing certain acidic impurities. These organic compounds include alcohols, ketones, aldehydes, etc.
• the present invention relates to a process for sweetening a sour hydrocarbon distillate which comprises reacting said distillate with an oxidizing agent in the presence of a phthalocyanine catalyst.
• the present invention relates to the process for sweetening sour gasoline which com. prises oxidizing mercaptans contained in said gasoline in the presence of caustic solution and cobalt phthalocyanine disulfonate.
• the present invention may be utilized to effect sweetening of a sour distillate having a comparatively high mercaptan content, in general it is preferred to remove a major proportion of the mercaptans from the distillate.
• removal of mercaptans from gasoline is preferred rather than conversionof the mercaptans to disulfides and subsequent retention of the disulfides in the gasoline.
• Sulfur compounds have an unfavorable elfect on tetraethyl lead-susceptibility.
• conventional treating methods remove fromabout 50 to about 95% of the mercaptans but leave a product still containing a minor concentration of mercaptans and accordingly a product which is still sour.
• the final sweetening is effected by oxidizing the mercaptans in the presence of an alkaline reagent and a phthalocyanine catalyst.
• any suitable phthalocyanine catalyst meeting the requirements of high activity and stability during use may be employed in the present invention.
• Particularly preferred metal phthalocyanines comprise cobalt phthalocyanine and vanadium phthalocyanine.
• the metal phthalocyanine in general is not readily soluble in aqueous solutions and, therefore, for improved operation is preferably utilized as a derivative thereof.
• a particularly preferred derivative is the sulfonated derivative.
• a preferred phthalocyanine catalyst comprises cobalt phthalocyanine disulfonate.
• Another preferred catalyst comprises vanadium phthalocyanine disulfonate.
• These compounds may be obtained from any suitable source or may be prepared in any suitable manner as, for example, by reacting cobalt or vanadium phthalocyanine with fuming sulfuric acid. While the sulfonic acid derivatives are preferred, it is understood that other suitable derivatives may be employed. Other derivatives 7 2,882,224! Patented Apr. 14, 1959;
• carboxylated derivative which may be prepared, for example, by the action of trichloroacetic acid on the metal phthalocyanine or by the action of phosgene and aluminum chloride. In the latter re action the acid chloride is formed and may be converted to the desired carboxylated derivative by conventional hydrolysis.
• sweetening is eifected in the presence of an alkaline reagent.
• Any suitable alkaline reagent may be employed.
• a preferred reagent comprises an aqueous solution of an alkaline metal hydroxide, such as sodium hydroxide solution, potassium hydroxide solution, etc., or these reagents containing a solubilizer or solutizer including, for example, alcohol such as methanol, ethanol, etc., phenols, cresols, etc., tannin, ism butyrate, etc.
• a particularly preferred alkaline solution is an aqueous solution of from about 5 to about 50% by weight concentration of sodium hydroxide, and, when employed, a preferred solutizer is methanol which may be used in a concentration of from about 5 to about 200 volume percent of the caustic or other alkaline solution.
• the phthalocyanine catalyst is both very active and highly stable. Because of its high activity, the catalyst is used in exceedingly small concentrations. These may range from 5 to 500 and preferably from 10 to parts per million by weight of the alkaline solution, although lower or higher concentrations may housed in some cases. The use of higher concentrations are unnecessary in most cases but may be used if desired, and thus may range up to 25% or more by weight of the alkaline solution. Be cause of its high stability, the catalyst is used for exceed ⁇ , ingly long periods of time. After a long period of use, the alkaline solution may become saturated with acidic compounds which may adversely eflect its further use, and the caustic solution either may be discarded or in some cases may be regenerated by conventional means.
• sweetening of the sour hydrocarbon distillate is effected by oxidation of mercaptans.
• an oxidizing agent is present in the reaction, Air is preferred, although. oxygen or other oxygencontaining gases may be utilized.
• the sour petroleum distillate may contain entrained oxygen orair in suflicient concentration to accomplish the desired sweetening, but generally it is preferred tointroduce air into the reaction. The amount of air must'be sufficient to effect oxidation of mercaptans, although an excess thereof generally is not objectionable.
• Sweetening of the petroleum distillate may be effected in any suitable manner and may be in batch or continuous process.
• a batch process the sour hydrocarbon distillate is introduced into a reaction zone containing the phthalocyanine catalyst and alkaline reagent, and air is introduced therein or passed therethrough.
• the reaction zone is equipped with suitable stirrers or other mixing devices to obtain intimate mixing.
• the caustic solution containing phthalocyanine catalyst is passed countercurrently to an ascending stream of sour petroleum distillate in the presence of a continuous stream of air.
• the reaction zone contains the alkaline solution and phthalocyanine catalyst, and gasoline and air are continuously passed therethrough and removed, generally from the upper portion of the reaction zone.
• the sweetening reaction is effected at ambient temperature.
• elevated temperature may be employed and generally will be within the range of from about 100 to about 400 F. or more, depending upon the pressure utilized therein, but usually below that at which substantial vaporization occurs.
• final sweetening of the gasoline may be preceded by extraction of acidic components and particularly mercaptans from the gasoline in any suitable manner.
• This pretreatment preferably comprises contacting of the gasoline with an alkaline solution, usually at ambient temperature and either in a batch or continuous process. In some cases elevated temperatures which may range up to about 200 F. may be employed.
• the alkaline reagents and, when employed, solubilizer or solutize'r heretofore set forth generally are utilized in the pretreatment. Following this treatment, the petroleum distillate will not be sweet and is subjected to final sweetening in the presence of air and the phthalocyanine catalyst.
• Example I The gasoline used in this example is a cracked gasoline having a mercaptan sulfur content of 0.003% by weight. It is subjected to sweetening by being passed in contact with 20 Baum caustic solution containing 50 parts per million of cobalt phthalocyanine disulfonate based on the active NaOI-I content of the caustic solution. On the basis of treating 1,000 barrels per day of cracked gasoline in a continuous process, barrels of caustic solution are used, and air is introduced at a rate of 10 cubic feet per hour into the sweetening zone. In order to efiect intimate contact in the sweetening zone, the caustic solution containing the phthalocyanine catalyst is preferably introduced into the upper portion of the sweetening zone through a suitable spray arrangement.
• the air is introduced into the lower portion of the sweetening zone through a suitable spray arrangement, and the sour gasoline is introduced at an intermediate point in the sweetening zone.
• the sweetening zone contains suitable contacting means such as side to side pans, bubble decks, bubble trays, etc. in order to effect intimate mixing therein.
• the sweetening is effected at ambient temperature and the treated gasoline withdrawn from the sweetening zone will be doctor sweet.
• Example 11 In this example sour kerosene containing 0.005% by weight of mercaptan sulfur is treated in a batch type process with a 28% potassium hydroxide aqueous solution containing 100 parts per million, based on the KOH content of the potassium hydroxide solution, of cobalt phthalocyanine disulfonate.
• the potassium hydroxide solution containing cobalt phthalocyanine disulfonate, "sour kerosene and air are charged into the reaction zone and are intimately mixed by means of stirring blades. The sweetening is efiected at ambient temperature.
• the kerosene is separated from the potassium hydroxide solution and cobalt phthalocyanine disulfonate.
• the kerosene so recovered is doctor sweet.
• Example III This example describes sweetening effected in the manner described in Example I except that 20% by volume, based on the caustic solution, of methanol is included in the reaction mixture.
• the gasoline treated in this manner will be doctor sweet in less than 3 hours of contacting in the manner described in Example I and utilizing the same constituents except for the addition of the methanol.
• the process for sweetening sour gasoline which comprises reacting mercaptans contained in said gasoline with air in the presence of caustic solution and cobalt phthalocyanine disulfonate.
• the process for sweetening sour gasoline which comprises reacting mercaptans contained in said gasoline with air in the presence of caustic solution and vanadium phthalocyanine disulfonate.

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• Chemical & Material Sciences (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
• Catalysts (AREA)

Priority Applications (10)

Applications Claiming Priority (1)

Publications (1)

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Cited By (32)

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Citations (4)

• 0
  • BE BE575509D patent/BE575509A/xx unknown
  • NL NL120003D patent/NL120003C/xx active
  • NL NL235884D patent/NL235884A/xx unknown
• 1958
  • 1958-02-13 US US714937A patent/US2882224A/en not_active Expired - Lifetime
• 1959
  • 1959-02-06 DE DEU5960A patent/DE1084861B/de active Pending
  • 1959-02-09 GB GB4396/59A patent/GB849998A/en not_active Expired
  • 1959-02-09 ES ES0247118A patent/ES247118A1/es not_active Expired
  • 1959-02-10 FR FR786323A patent/FR1216168A/fr not_active Expired
• 1962
  • 1962-12-31 MY MY196286A patent/MY6200086A/xx unknown
• 1964
  • 1964-11-18 OA OA50640A patent/OA00553A/fr unknown

Patent Citations (4)

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