GB1500401A - Process for the formation of pumpable slurries from waxy hydrocarbon mixtures - Google Patents

Process for the formation of pumpable slurries from waxy hydrocarbon mixtures

Info

Publication number
GB1500401A
GB1500401A GB1730275A GB1730275A GB1500401A GB 1500401 A GB1500401 A GB 1500401A GB 1730275 A GB1730275 A GB 1730275A GB 1730275 A GB1730275 A GB 1730275A GB 1500401 A GB1500401 A GB 1500401A
Authority
GB
United Kingdom
Prior art keywords
liquid
pour point
point fraction
column
wax
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
Application number
GB1730275A
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.)
Marathon Oil Co
Original Assignee
Marathon Oil 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 Marathon Oil Co filed Critical Marathon Oil Co
Publication of GB1500401A publication Critical patent/GB1500401A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00Pipe-line systems
    • F17D1/08Pipe-line systems for liquids or viscous products
    • F17D1/088Pipe-line systems for liquids or viscous products for solids or suspensions of solids in liquids, e.g. slurries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/0318Processes
    • Y10T137/0391Affecting flow by the addition of material or energy

Landscapes

  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Water Supply & Treatment (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

1500401 Pumpable waxy hydrocarbon slurries MARATHON OIL CO 25 April 1975 [17 June 1974] 17302/75 Heading C5E A pumpable slurry is produced from a waxcontaining hydrocarbon mixture by separating the mixture into at least two fractions, viz: a liquid low pour point fraction and a high pour point fraction, the latter containing the major proportion of the wax, introducing at least a portion of the high pour point fraction as a stream of discrete liquid droplets into a column of liquid having a density greater than the high pour point fraction, allowing the droplets to rise through the column to solidify therein, recovering the solidified particles from the top of the column and redispersing the solidified particles in a hydrocarbon carrier liquid comprising at least some of the low pour point fraction at a temperature below the solution temperature of the particles therein to form the slurry, the column of liquid comprising a first body of liquid at the bottom of the column into which the high pour point fraction is introduced which is maintained at a temperature above the pour point of the high pour point fraction, and a second body of liquid having a density less than that of the first body of liquid and positioned in the column above the first body and maintained below the melting point of the high pour point fraction to effect the solidification of the droplets as they pass therethrough. The waxy hydrocarbon mixture may contain 1-80% by weight of wax. Wax is defined as the precipitate which forms after one part by weight of the hydrocarbon mixture is dissolved in 10 parts by weight of methyl ethyl ketone at 80‹ C. and the mixture cooled to -25‹ C. The first body of liquid preferably has a temperature below that of the high pour point fraction, suitably at least 140‹ F., and the colder less dense liquid may be at ambient temperature. The difference in density between the two liquids may be at least 0À2 g./c.c. The coolants may be halogenated hydrocarbons but are preferably water containing water soluble agents imparting increased density, e.g. potassium alum, potassium metaphosphate, aluminium acetate or strontium fluoride. A surfactant, e.g. sorbitan monolaurate or a petroleum sulphonate may be added to the molten wax. A liquid and/or gaseous diluent may be admixed with the liquid hydrocarbon carrier before, during or after the slurrying operation. The final slurry may contain 1-60% by weight of the wax particles.
GB1730275A 1974-06-17 1975-04-25 Process for the formation of pumpable slurries from waxy hydrocarbon mixtures Expired GB1500401A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US47994974 US3880177A (en) 1974-06-17 1974-06-17 Method for transporting waxy hydrocarbon mixtures

Publications (1)

Publication Number Publication Date
GB1500401A true GB1500401A (en) 1978-02-08

Family

ID=23906074

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1730275A Expired GB1500401A (en) 1974-06-17 1975-04-25 Process for the formation of pumpable slurries from waxy hydrocarbon mixtures

Country Status (12)

Country Link
US (1) US3880177A (en)
AR (1) AR210578A1 (en)
AT (1) AT341432B (en)
BR (1) BR7502541A (en)
CH (1) CH606388A5 (en)
DD (1) DD119301A1 (en)
DE (1) DE2518610C3 (en)
FR (1) FR2274550A1 (en)
GB (1) GB1500401A (en)
IT (1) IT1037635B (en)
PL (1) PL95928B1 (en)
SU (1) SU622422A3 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4050742A (en) * 1976-11-04 1977-09-27 Marathon Oil Company Transporting heavy fuel oil as a slurry
US4104171A (en) * 1976-12-30 1978-08-01 Union Oil Company Of California Method for transporting waxy oils by pipeline
US6313361B1 (en) 1996-02-13 2001-11-06 Marathon Oil Company Formation of a stable wax slurry from a Fischer-Tropsch reactor effluent
US6294076B1 (en) * 2000-04-21 2001-09-25 Exxonmobil Research And Engineering Company Fischer-Tropsch wax and hydrocarbon mixtures for transport (law938)
US6268401B1 (en) * 2000-04-21 2001-07-31 Exxonmobil Research And Engineering Company Fischer-tropsch wax and crude oil mixtures having a high wax content
GB2386607B (en) * 2000-11-08 2004-09-08 Chevron Usa Inc Method for transporting fischer-tropsch products
US6518321B1 (en) * 2000-11-08 2003-02-11 Chevron U.S.A. Inc. Method for transporting Fischer-Tropsch products
US20060065573A1 (en) * 2004-09-28 2006-03-30 Chevron U.S.A. Inc. Fischer-tropsch wax composition and method of transport
FR3019624A1 (en) * 2014-04-04 2015-10-09 Total Sa PARAFFINIC FLUID TRANSPORT

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3468986A (en) * 1966-11-15 1969-09-23 David J Watanabe Method for producing a solid particulate material
US3804752A (en) * 1972-09-18 1974-04-16 Marathon Oil Co Transporting hydrocarbon mixtures as a slurry

Also Published As

Publication number Publication date
AR210578A1 (en) 1977-08-31
SU622422A3 (en) 1978-08-30
US3880177A (en) 1975-04-29
AT341432B (en) 1978-02-10
DE2518610A1 (en) 1975-12-18
CH606388A5 (en) 1978-10-31
DE2518610B2 (en) 1979-05-17
AU8053775A (en) 1976-10-28
PL95928B1 (en) 1977-11-30
BR7502541A (en) 1976-06-29
FR2274550A1 (en) 1976-01-09
IT1037635B (en) 1979-11-20
ATA322175A (en) 1977-05-15
DE2518610C3 (en) 1980-01-17
DD119301A1 (en) 1976-04-12

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Legal Events

Date Code Title Description
CSNS Application of which complete specification have been accepted and published, but patent is not sealed