US1770181A - Process of treating hydrocarbons - Google Patents

Process of treating hydrocarbons Download PDF

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Publication number
US1770181A
US1770181A US668481A US66848123A US1770181A US 1770181 A US1770181 A US 1770181A US 668481 A US668481 A US 668481A US 66848123 A US66848123 A US 66848123A US 1770181 A US1770181 A US 1770181A
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US
United States
Prior art keywords
oil
particles
residual
coke
oils
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
US668481A
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
Application filed by Universal Oil Products Co filed Critical Universal Oil Products Co
Priority to US668481A priority Critical patent/US1770181A/en
Priority to US228500A priority patent/US1733620A/en
Application granted granted Critical
Publication of US1770181A publication Critical patent/US1770181A/en
Anticipated expiration legal-status Critical
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
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/32Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/322Coal-oil suspensions
    • 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

  • the residualoils withdrawn from the still or expansion chamber have a certain amount of coke forming substantially solid" particles suspended therein. These particles remain in suspensionfor short or but eventually settle out. For instance, a crtain'portion may settle in the run-down lines with a consequent slowing up of. the flow and eventual clogging upto the pipe.
  • the larger coke forming particles of the residual oil will eventually clog the'nozzle of the burner pipe.
  • These coke forming or pitch-likeparticles are dispersed throughout an external phase consisting of relatively clear oil. The particlesin the internal phase vary in size but a greatmany of them, and especially the ag gregate, can be seen with a microscope.
  • a stabilizing agent usually of a colloid nature and soluble in the oil, for instance, soaps of the alkaline earth metals, such as calcium and magnesium oleate, stearate or resinate, to the oil.
  • soaps of the alkaline earth metals such as calcium and magnesium oleate, stearate or resinate
  • the mixture is then agitated for a period of time suflicient to 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.
  • A;process for stabilizing residual oils jectinga cracked residual oil containing free carbon in temporary suspension to a homogenizip'g action. 7
  • a liquid fuel obtained by passing a residual-oil containing free earbon in tempoary suspension between closely adjacent surfaces under high pressnre v v JACQUE C. MQRRELL.

Description

35 tion which may 15 longer periods of. time,
Patented July 8, 1930 UNITED STATES PATENT OFFICE- JAGQUE c. monnnnt, on cmcaeo, rumors, ASSIGNOB ro mum on. raonuc'rs COMPANY, OI CHICAGO, HILINOIS, A CORPORATION OF SOUTH DAKOTA PROCESS OF TREATING EYDROCABBONS Il'o Drawing. Application filed October 15, 1923, Serial No. 668,481. Renewed July 28, 1927- cracked residual (oils to eliminate the setv out ofmore or less of the coke formmg particles therein; Y With the advance made in the cracking of hydrocarbon Oils in the past few years,
there hasarisen an ever increasing problem in that some of: the residualoils withdrawn from the still or expansion chamber have a certain amount of coke forming substantially solid" particles suspended therein. These particles remain in suspensionfor short or but eventually settle out. For instance, a crtain'portion may settle in the run-down lines with a consequent slowing up of. the flow and eventual clogging upto 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-likeparticles are dispersed throughout an external phase consisting of relatively clear oil. The particlesin the internal phase vary in size but a greatmany of them, and especially the ag gregate, can be seen with a microscope. l have'discovered that'by sta'blizing the eiike forming particles in the oil, a state resembling emulsification exists, and the coke iori'ning particles remain suspended in the oil more or less permanently. This stabilization is produced as follows:
I subjectsome residual oils to homogenizabe accomplis'hdd by forcing the oil under high pressure through small minute apertures in order to obtain a finely divided dispersion, or the homogenization may be accomplished by subjecting the par- 40 ticles to mechanical impact which will tend' to break the substantially solid coke form- With some oils,
or the oil subjected to a strain ing particles,
to cause breaking of the larger particles into smaller particles in the usual colloid mill. it may be desirable to apply mogemzing heat before attempting to homogenize, as a semi-solid will homogenize more readily than a solid. In addition, it has been found that these particles or aggregates of the particles will assume a globular semi-solid form when subjected to heat. V
Homogenization of certain types of residual' oils will not stabilize the coke forming particles so as to secure a substantially .permanent suspension. I propose to add a stabilizing agent, usually of a colloid nature and soluble in the oil, for instance, soaps of the alkaline earth metals, such as calcium and magnesium oleate, stearate or resinate, to the oil. The mixture is then agitated for a period of time suflicient to 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 desbribed, 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 sushomogenized, 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 proportions of the soap-in the oil is 01 to 2%. Y Y
I claimas my invention:
resulting from thesubjection of hydrocarbon oil to cracking conditions which comprises subjecting said residual oil containing suspended coke or pitch-like particles to a hoaction.
2. A stabilized liquid fuel obtained by sub- 1. A;process for stabilizing residual oils jectinga cracked residual oil containing free carbon in temporary suspension to a homogenizip'g action. 7
3. "A liquid fuel obtained by passing wresidual oil containing 'free carbon in temporary suspension between a. pair of closely contiguous surfaces under relatively e'xtreme- 1y high ressure.
4. A liquid fuel obtained by passing a residual-oil containing free earbon in tempoary suspension between closely adjacent surfaces under high pressnre v v JACQUE C. MQRRELL.
US668481A 1923-10-15 1923-10-15 Process of treating hydrocarbons Expired - Lifetime US1770181A (en)

Priority Applications (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

Applications Claiming Priority (1)

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

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2754267A (en) * 1954-07-12 1956-07-10 Shell Dev Carbon black concentrates
US3272605A (en) * 1951-05-18 1966-09-13 Gulf Research Development Co Fuel oils
US4479805A (en) * 1983-09-12 1984-10-30 Columbia Chase Corporation Treating-high asphaltene fuel oils

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3272605A (en) * 1951-05-18 1966-09-13 Gulf Research Development Co Fuel oils
US2754267A (en) * 1954-07-12 1956-07-10 Shell Dev Carbon black concentrates
US4479805A (en) * 1983-09-12 1984-10-30 Columbia Chase Corporation Treating-high asphaltene fuel oils

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