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US2027648A - Refining of petroleum oil - Google Patents

Refining of petroleum oil Download PDF

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Publication number
US2027648A
US2027648A US403911A US40391129A US2027648A US 2027648 A US2027648 A US 2027648A US 403911 A US403911 A US 403911A US 40391129 A US40391129 A US 40391129A US 2027648 A US2027648 A US 2027648A
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US
United States
Prior art keywords
refining
acid
acids
oil
petroleum oil
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Expired - Lifetime
Application number
US403911A
Inventor
Jacque C Morrell
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Universal Oil Products Co
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Universal Oil Products Co
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Publication date
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Priority to US403911A priority Critical patent/US2027648A/en
Application granted granted Critical
Publication of US2027648A publication Critical patent/US2027648A/en
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Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G17/00Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
    • C10G17/02Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
    • C10G17/04Liquid-liquid treatment forming two immiscible phases
    • C10G17/07Liquid-liquid treatment forming two immiscible phases using halogen acids or oxyacids of halogen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G17/00Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
    • C10G17/02Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
    • C10G17/04Liquid-liquid treatment forming two immiscible phases
    • C10G17/06Liquid-liquid treatment forming two immiscible phases using acids derived from sulfur or acid sludge thereof

Definitions

  • This invention relates to improvements in the refining of petroleum oils, and refers more particularly to the subjection of the lighter gravity liquid products produced in petroleum cracking to the action of various refining agents for the purpose of removing or converting objectionable color-forming, odor-forming, sulphur and analogous objectionable compounds.
  • the essence of the present invention resides in the utilization, as a refining agent, of substantially sulphur-free inorganic or organic acids, or a combination of organic and inorganic acids as the sole refining agent, or in combination with any other suitable refining agent or any combination of refining agents to accomplish the purpose above set forth.
  • the substantially sulphur-free organic or inorganic acids herein set out in combination with concentrated sulphuric acid, which, of course, includes the step of subjecting the oil first to the action of the substantially sulphurfree acids before described and then to the sulphuric acid. treatment.
  • the invention contemplates the use of these refining agents, either of themselves or as separate steps, in a method of refining the oil, in combination with other treating agents including plumbite (litharge dissolved in an alkaline solution such as sodium hydroxide, potassium hydroxide, and others), caustic soda, and other alkalies, earthy adsorbent agents, copper salts and the like.
  • plumbite lithium dissolved in an alkaline solution such as sodium hydroxide, potassium hydroxide, and others
  • caustic soda caustic soda
  • earthy adsorbent agents calcium salts and the like.
  • substantially sulphur-free acids as used in the specification and claims, I mean an acid which contains no sulphur in its molecular composition. This term does not refer to the presence of small or accidental amounts of sulphur present in the materials from which the acid was made or introduced during the course of commercial manufacture, in other words, it does not refer to impurities which contain sulphur.
  • inorganic acids contemplated for use in the present invention may be listed nitric acid, hydrochloric acid, orthophosphoric acid and metaphosphoric acid. These inorganic acids pointed out may be used alone or may be mixed with each other. For instance, one mixture of inorganic acids which has been found suitable for the purpose comprises a small proportion of nitric acid in one of the phosphoric acids.
  • organic acids contemplated by the present invention may be listed the following: acetic (preferably glacial), chloracetic, and the like. These organic acids may be used alone or in combination with each other in suitable proportions, and the invention also contemplates that the organic acids may be mixed with the inorganic acids. As an illustrative example of the proportions in which these acids are mixed, phosphoric acid and acetic acid may be taken, as an example. Preferably, the acetic acid in the mixture is always less than 50% by volume of the mixture, especially where the glacial acetic acid is used, for the reason that this acid is soluble in the oil and requires a larger proportion of phosphoric acid to reduce this solubility. This points out that the properties of these acids must be considered in their use.
  • Another suitable mixture is the introduction of a small percentage of nitric acid, for example, 5 to 10%, with phosphoric acid or with acetic acid.
  • the percentage of nitric acid while not limited to the amount shown, must be kept as a smaller percentage relatively to the other acid in order to cut down its oxidizing properties, and thus obtain the benefits of the mixed acids.
  • the addition of nitric acid to acetic acid or phosphoric acid strengthens them by adding some oxidizing value to these relatively weak acids.
  • the present invention contemplates more particularly the refining of what are known as cracked distillates, and more particularly those cracked overhead products of end boiling point commercially satisfactory to the trade which are produced directly from the cracking process.
  • Steps in the process of refining a lighter gravity liquid product produced from the cracking of petroleum oil comprising subjecting the oil first to the action of a mixture of nitric and acetic acids, and then to the action of concentrated sulphuric acid, to remove or convert objectionable compounds present in said lighter gravity liquid product.
  • Steps in the process of refining a lighter gravity liquid product produced from the cracking of petroleum oil comprising subjecting the oil first to the action of acetic acid, and then to the action of concentrated sulphuric acid, to remove or convert objectionable compounds present in said lighter gravity liquid product.

Landscapes

  • 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)

Description

Patented Jan. 14, 1936 UNHTED STATES PATENT OFFICE REFINING OF PETROLEUM OIL No Drawing. Continuation of application No.
164,131, January 27, 19 tion December 9, 1925,
27. Division of applica- Serial No. 74,395. This application October 31, 1929, Serial No. 403,911
2 Claims.
This application is a continuation of my copending application, Serial No. 164,131, filed January 27, 1927, which in turn is a division of an application filed by me, Serial No. 74,395, filed on December 9, 1925 and which has matured into Patent 1,839,114, Sept. 29, 1931.
This invention relates to improvements in the refining of petroleum oils, and refers more particularly to the subjection of the lighter gravity liquid products produced in petroleum cracking to the action of various refining agents for the purpose of removing or converting objectionable color-forming, odor-forming, sulphur and analogous objectionable compounds.
The essence of the present invention resides in the utilization, as a refining agent, of substantially sulphur-free inorganic or organic acids, or a combination of organic and inorganic acids as the sole refining agent, or in combination with any other suitable refining agent or any combination of refining agents to accomplish the purpose above set forth.
I have discovered that when the lighter gravity liquid products produced in petroleum distillation and cracking are subjected to the action of concentrated sulphuric acid, for the purpose of refining and removing objectionable compounds, the strength of the concentrated acid produces an objectionable reaction, namely, the oxidation of compounds present, particularly in cracked distillates, reacting in such manner as to leave in the refined oil substances which bring about an unstable condition in the oil with respect to color and odor, where the oils are not redistilled.
To overcome this objection, various experiments were carried out, and I have discovered that it is possible to substitute for the concentrated sulphuric acid substantially sulphur-free inorganic'or organic acids, either alone or in combination. Further, it is possible to overcome the objections pointed out by preceding the treatment with concentrated sulphuric acid with the step of subjecting the oil to the action of the substantially sulphur-free acids above set forth.
It may be pointed out that it is the essence of the present invention to use, essentially as a refining agent, the substantially sulphur-free organic or inorganic acids herein set out, in combination with concentrated sulphuric acid, which, of course, includes the step of subjecting the oil first to the action of the substantially sulphurfree acids before described and then to the sulphuric acid. treatment.
The invention contemplates the use of these refining agents, either of themselves or as separate steps, in a method of refining the oil, in combination with other treating agents including plumbite (litharge dissolved in an alkaline solution such as sodium hydroxide, potassium hydroxide, and others), caustic soda, and other alkalies, earthy adsorbent agents, copper salts and the like.
By the term "substantially sulphur-free acids as used in the specification and claims, I mean an acid which contains no sulphur in its molecular composition. This term does not refer to the presence of small or accidental amounts of sulphur present in the materials from which the acid was made or introduced during the course of commercial manufacture, in other words, it does not refer to impurities which contain sulphur.
Among some of the inorganic acids contemplated for use in the present invention may be listed nitric acid, hydrochloric acid, orthophosphoric acid and metaphosphoric acid. These inorganic acids pointed out may be used alone or may be mixed with each other. For instance, one mixture of inorganic acids which has been found suitable for the purpose comprises a small proportion of nitric acid in one of the phosphoric acids.
Among the organic acids contemplated by the present invention may be listed the following: acetic (preferably glacial), chloracetic, and the like. These organic acids may be used alone or in combination with each other in suitable proportions, and the invention also contemplates that the organic acids may be mixed with the inorganic acids. As an illustrative example of the proportions in which these acids are mixed, phosphoric acid and acetic acid may be taken, as an example. Preferably, the acetic acid in the mixture is always less than 50% by volume of the mixture, especially where the glacial acetic acid is used, for the reason that this acid is soluble in the oil and requires a larger proportion of phosphoric acid to reduce this solubility. This points out that the properties of these acids must be considered in their use. Another suitable mixture is the introduction of a small percentage of nitric acid, for example, 5 to 10%, with phosphoric acid or with acetic acid. The percentage of nitric acid, while not limited to the amount shown, must be kept as a smaller percentage relatively to the other acid in order to cut down its oxidizing properties, and thus obtain the benefits of the mixed acids. On the other hand, the addition of nitric acid to acetic acid or phosphoric acid strengthens them by adding some oxidizing value to these relatively weak acids.
The present invention contemplates more particularly the refining of what are known as cracked distillates, and more particularly those cracked overhead products of end boiling point commercially satisfactory to the trade which are produced directly from the cracking process.
The claims are as follows:
1. Steps in the process of refining a lighter gravity liquid product produced from the cracking of petroleum oil, comprising subjecting the oil first to the action of a mixture of nitric and acetic acids, and then to the action of concentrated sulphuric acid, to remove or convert objectionable compounds present in said lighter gravity liquid product.
2. Steps in the process of refining a lighter gravity liquid product produced from the cracking of petroleum oil, comprising subjecting the oil first to the action of acetic acid, and then to the action of concentrated sulphuric acid, to remove or convert objectionable compounds present in said lighter gravity liquid product.
J ACQUE C. MORRELL.
US403911A 1929-10-31 1929-10-31 Refining of petroleum oil Expired - Lifetime US2027648A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2754252A (en) * 1953-01-29 1956-07-10 Standard Oil Co Refining hydrocarbon oils with bf3 and perfluoroalkanoic acid
US3120486A (en) * 1961-02-17 1964-02-04 Pure Oil Co Process for refining and deodorizing petroleum fractions

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2754252A (en) * 1953-01-29 1956-07-10 Standard Oil Co Refining hydrocarbon oils with bf3 and perfluoroalkanoic acid
US3120486A (en) * 1961-02-17 1964-02-04 Pure Oil Co Process for refining and deodorizing petroleum fractions

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