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US1733620A - Process of treating hydrocarbons - Google Patents

Process of treating hydrocarbons Download PDF

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Publication number
US1733620A
US1733620A US228500A US22850027A US1733620A US 1733620 A US1733620 A US 1733620A US 228500 A US228500 A US 228500A US 22850027 A US22850027 A US 22850027A US 1733620 A US1733620 A US 1733620A
Authority
US
United States
Prior art keywords
oil
coke
residual
particles
forming particles
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US228500A
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
Original Assignee
Universal Oil Products Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US668481A external-priority patent/US1770181A/en
Application filed by Universal Oil Products Co filed Critical Universal Oil Products Co
Priority to US228500A priority Critical patent/US1733620A/en
Application granted granted Critical
Publication of US1733620A publication Critical patent/US1733620A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M1/00Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
    • C10M1/08Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants with additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/108Residual fractions, e.g. bright stocks
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/125Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/129Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/20Rosin acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/04Groups 2 or 12

Definitions

  • This invention relates to improvements in a process of treating hydrocarbon oils, and refers more particularly to the treatment of cracked residual oils to eliminate the settling out of more or less of the coke forming particles remain in suspension for short or longer periods of time, but eventually settle out. For instance, a certain portion may settle in the run-down lines with a consequent slowing up of the flow and eventual clogging up of the pipe. When used as fuel, the larger coke forming particles of the residual oil will eventually clog the nozzle of the burner pipe.
  • coke forming or pitch-like particles are dispersed throughout an external phase consisting of relatively clear oil.
  • the particles in the internal phase vary in size but a great many of them, and especially the aggregate, can be seen with a microscope.
  • oils may be accomplished by forcing the oil under high pressure through small minute apertures in order to obtain a finely clivided dispersion, or the homogenization may be accomplished by subjecting the part1cles to mechanical impact which will tend to break the substantially solid coke forming particles, or the oil subjected to a strain to cause breaking of the larger particles into smaller particles in the usual colloid Illlll.
  • the agitation may be accomplished by the homogenization heretofore explained.
  • An example of a working formula for the addition of an alkaline earth metal soluble in the oil may be illustrated as followsfrom 0.1 to 2% of the alkaline earth soap is dissolved in the residual oil, and the latter then homogenized, or the alkaline earth soap may be dissolved first in a lighter oil such as gas oil, and this solution added to the cracked residual oil so that the final proportion of the soap in the oil is 0.1 to 2%.
  • a process for stabilizing the coke-forming particles of hydrocarbon residual oils resulting from an oil cracking process comprising introducing to the residual oil an alkaline earth metal soap and in subjecting the residual oil to which the alkaline earth metal soap has been introduced to a homgenizing v treatment.
  • a process for stabilizing the coke-forming particles of hydrocarbon residual oils" resulting from an oil cracking process comprising adding to the residual 011 containing the co e-forming particles a colloidal stabilizing agent, subjecting the residual oil subsequent to the addition of such colloidal stabilizing agent to a homogenizing treatment.

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)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • Coke Industry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

Patented Oct. 29, 1929 UNITED STATES PATENT OFFICE JACQUE C. MORRELL, OF CHICAGO, ILLINOIS, ASSIGNOR TO UNIVERSAL OIL PRODUCTS COMZPANY, OF CHICAGO, ILLINOIS, A CORPORATION OI SOUTH DAKOTA PROCESS OF TREATING HYDROCABBONS No Drawing. Original application filed October 15, 1923, Serial No. 668,481;
filed October 24, 1927. Serial No. 228,500.
This application is a division of my former application, Serial No. 668,481, filed October 15th, 1923.
This invention relates to improvements in a process of treating hydrocarbon oils, and refers more particularly to the treatment of cracked residual oils to eliminate the settling out of more or less of the coke forming particles remain in suspension for short or longer periods of time, but eventually settle out. For instance, a certain portion may settle in the run-down lines with a consequent slowing up of the flow and eventual clogging up of the pipe. When used as fuel, the larger coke forming particles of the residual oil will eventually clog the nozzle of the burner pipe.
These coke forming or pitch-like particles are dispersed throughout an external phase consisting of relatively clear oil. The particles in the internal phase vary in size but a great many of them, and especially the aggregate, can be seen with a microscope.
I have discovered that by stabilizing the coke-forming particles in the oil, a state rcsembling emulsification exists, and the coke forming particles remain suspended in the oil more or less permanently. This stabilization is produced as follows:
I subject some residual oils to homogenization which may be accomplished by forcing the oil under high pressure through small minute apertures in order to obtain a finely clivided dispersion, or the homogenization may be accomplished by subjecting the part1cles to mechanical impact which will tend to break the substantially solid coke forming particles, or the oil subjected to a strain to cause breaking of the larger particles into smaller particles in the usual colloid Illlll. With some oils, it may be desirable to apply heat before attempting to homogenize, as a semisolid will homogenize more readily than a Ilivldecl and this application and magnesium .oleate, stearate or resinate,
to the oil. The niixture is then agitated for a period of time sufiicientto make a substantially permanent suspension, the oil being in the external phase, and the coke forming particles in the internal phase.
The agitation may be accomplished by the homogenization heretofore explained.
By treating the residual oils in the manner" described, it has been found that a relatively stable suspension is produced, resulting in a dispersion of the coke forming particles through the oils, which will remain suspended for a considerable period of time.
An example of a working formula for the addition of an alkaline earth metal soluble in the oil may be illustrated as followsfrom 0.1 to 2% of the alkaline earth soap is dissolved in the residual oil, and the latter then homogenized, or the alkaline earth soap may be dissolved first in a lighter oil such as gas oil, and this solution added to the cracked residual oil so that the final proportion of the soap in the oil is 0.1 to 2%.
I claim l. A process for stabilizing the coke-forming particles of hydrocarbon residual oils resulting from an oil cracking process comprising introducing to the residual oil an alkaline earth metal soap and in subjecting the residual oil to which the alkaline earth metal soap has been introduced to a homgenizing v treatment.
2. A process for stabilizing the coke-formsequent to the introduction of such alkaline earth metal soap to a homo enizing action by agitating'the mixture pro ucing a material havin the oil in the external phase andthe 5 cokeorming particles in the internal phase. 3. A process for stabilizing the coke-forming particles of hydrocarbon residual oils" resulting from an oil cracking process comprising adding to the residual 011 containing the co e-forming particles a colloidal stabilizing agent, subjecting the residual oil subsequent to the addition of such colloidal stabilizing agent to a homogenizing treatment. v
In testimony whereof I affix my signature.
, JACQUE C. MORRELL.
US228500A 1923-10-15 1927-10-24 Process of treating hydrocarbons Expired - Lifetime US1733620A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US228500A US1733620A (en) 1923-10-15 1927-10-24 Process of treating hydrocarbons

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US668481A US1770181A (en) 1923-10-15 1923-10-15 Process of treating hydrocarbons
US228500A US1733620A (en) 1923-10-15 1927-10-24 Process of treating hydrocarbons

Publications (1)

Publication Number Publication Date
US1733620A true US1733620A (en) 1929-10-29

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Family Applications (1)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2658823A (en) * 1951-08-28 1953-11-10 Socony Vacuum Oil Co Inc Fuel oil composition
US2909488A (en) * 1954-07-13 1959-10-20 Eugene L Colichman Nuclear reactor coolant
US20110275505A1 (en) * 2008-11-28 2011-11-10 Rutgers Chemicals Gmbh Sinterable semi-coke powder with high bulk density

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2658823A (en) * 1951-08-28 1953-11-10 Socony Vacuum Oil Co Inc Fuel oil composition
US2909488A (en) * 1954-07-13 1959-10-20 Eugene L Colichman Nuclear reactor coolant
US20110275505A1 (en) * 2008-11-28 2011-11-10 Rutgers Chemicals Gmbh Sinterable semi-coke powder with high bulk density
US8613801B2 (en) * 2008-11-28 2013-12-24 Rheinkalk Gmbh Sinterable semi-coke powder with high bulk density

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