CA2976863A1 - Method for processing weathered oil sand ore - Google Patents

Method for processing weathered oil sand ore Download PDF

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Publication number
CA2976863A1
CA2976863A1 CA2976863A CA2976863A CA2976863A1 CA 2976863 A1 CA2976863 A1 CA 2976863A1 CA 2976863 A CA2976863 A CA 2976863A CA 2976863 A CA2976863 A CA 2976863A CA 2976863 A1 CA2976863 A1 CA 2976863A1
Authority
CA
Canada
Prior art keywords
oil sand
weathered
bitumen
weathered oil
sand ore
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.)
Granted
Application number
CA2976863A
Other languages
French (fr)
Other versions
CA2976863C (en
Inventor
Jun Long
Shane Hoskins
Yong Gu (Joe)
Yin Ming Samson Ng
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.)
Syncrude Canada Ltd
Original Assignee
Syncrude Canada Ltd
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 Syncrude Canada Ltd filed Critical Syncrude Canada Ltd
Priority to CA2976863A priority Critical patent/CA2976863C/en
Publication of CA2976863A1 publication Critical patent/CA2976863A1/en
Application granted granted Critical
Publication of CA2976863C publication Critical patent/CA2976863C/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00General arrangement of separating plant, e.g. flow sheets
    • B03B9/02General arrangement of separating plant, e.g. flow sheets specially adapted for oil-sand, oil-chalk, oil-shales, ozokerite, bitumen, or the like
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B1/00Conditioning for facilitating separation by altering physical properties of the matter to be treated
    • B03B1/02Preparatory heating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B1/00Conditioning for facilitating separation by altering physical properties of the matter to be treated
    • B03B1/04Conditioning for facilitating separation by altering physical properties of the matter to be treated by additives
    • 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/04Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
    • C10G1/045Separation of insoluble materials
    • 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/04Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
    • C10G1/047Hot water or cold water extraction processes

Landscapes

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

Abstract

A process for extracting bitumen from weathered oil sand ore is provided, comprising mixing the weathered oil sand ore with heated water and sodium triphosphate to form a weathered oil sand slurry; adding sodium triphosphate to either the weathered oil sand ore, the heated water, or to the weathered oil sand slurry; conditioning the weathered oil sand slurry at a temperature of at least 50°C to form a conditioned weathered oil sand slurry; and subjecting the conditioned weathered oil sand slurry to gravity separation at a temperature of at least 50°C to form a bitumen froth product.

Description

K) 22 Cydofeeder Deaerator to ,1 Materials Handling Surge/ Cyclofeed . Vessel 36 0, 12 Ifj74 co Faddy r 24 Conveyor . .0 01 14 ¨ 40 LA) .0_4,. f_n r injection -K) 341p ' 41 38 ________________________ LEAN FFROTH __ ¨:- õ (-76 RECYCLE
Steam 1--, ,1 Apron ________________ r.:__ 26 'gi=i= 0 . 0 ..

0 Feeder == Surge Feed Apron 41 Pump 12,-) 54 ,-- 60 (80 co DRC 1 i i i Box Froth 1 16 Conveyor Feeder 30 . M--1 1 _____ , ?
PSV FROTH
0, 18 44 II 42 51 V _________________________________________________________________________ 1- __ ¨7 ______________ jiv-741 Recycle Pump c 45 PS11\
________ 58' 46 ___________________________________________________________________ 2 76' ,-- r \ __ ¨

JSteam ,--- . ---..
__.
_______________________________________________________________________________ _______________________________ N
56¨ 60' ( ___ PSV 2 FROTH PSV MIDDLINGS ,_ _, ___________________________________________________________________ ) ...-.
70 64 ¨69 i ____ Water [11.11M3-j- 12,11 TOR Lean Froth 52' __________________________________________________________________ TOR

50---- ___________________________________________________ , (54' =
- - 58' TOR MIDDS ULEAN ,... _.
Wm' FROTH
________________________________________________________________ 2 -72 68 Storage 'liar PSVs TANK
2 I MIDD
TOR Midds Recycle Tanks PSV
_______________________________________________________________________________ _____________________ , i r 56, 1 TOR UIF
to Aeration Down Pipe UNDERFLOW _________________________________________________________________ (to TAILS) TAILINGS __________________________________________________________ DISTRIBUTOR s\ __________________________________________________ 1 7 = + to Tailings Pump Boxes .
Slurry Preparation Bitumen Separation =
and Conditioning FIG. 1

Claims (14)

WHAT IS CLAIMED:
1. A process for extracting bitumen from weathered oil sand ore, comprising:
mixing the weathered oil sand ore with heated water and sodium triphosphate to form a weathered oil sand slurry;
adding sodium triphosphate to either the weathered oil sand ore, the heated water, or to the weathered oil sand slurry;
conditioning the weathered oil sand slurry at a temperature of at least 50°C to form a conditioned weathered oil sand slurry; and subjecting the conditioned weathered oil sand slurry to gravity separation at a temperature of at least 50°C to form a bitumen froth product.
2. The process as claimed in claim 1, wherein conditioning and gravity separation take plarp at himtwppn tn 80°C.
3. The process as claimed in claim 1, wherein the temperature of the gravity separation step is maintained at at least 50°C by adding heated water to the conditioned weathered oil sand slurry prior to subjecting it to gravity separation.
4. The process as claimed in claim 1, wherein the dosage of sodium triphosphate is at least 0.05 wt% per tonne dry oil sand ore.
5. The process as claimed in claim 1, wherein the dosage of sodium triphosphate is at least 0.1 wt% per tonne dry oil sand ore.
6. The process as claimed in claim 1, wherein the dosage of sodium triphosphate is 0.16 wt% per tonne dry oil sand ore.
7. The process as claimed in claim 1, wherein the weathered oil sand ore comprises 2% water content or less.
8. The process as claimed in claim 1, wherein the weathered oil sand ore comprises connate water having greater than or equal to 0.5% S042-, greater than or equal to 0.1% Ca2+ and/or about 0.06% Mg2+
9. The process as claimed in claim 1, wherein the weathered oil sand ore comprises bitumen having a reduced sulfur content by up to 0.5% (absolute) and an increased bitumen asphaltene content.
10. The process as claimed in claim 1, wherein the weathered oil sand ore has very low bitumen recovery under normal extraction process conditions.
11.The process as claimed in claim 1, wherein the weathered oil sand ore:
comprises 2% water content or less; comprises connate water having greater than or equal to 0.5% S042-, greater than or equal to 0.1% Ca2+ and/or about 0.06%
Mg2+; comprises bitumen having a reduced sulfur content by up to 0.5%
(absolute) and an increased bitumen asphaltene content; and has very low bitumen recovery under normal extraction process conditions.
12. The process as claimed in claim 1, wherein conditioning and gravity separation take place at 65°C.
13. The process as claimed in claim 1, wherein the dosage of sodium triphosphate is between 0.05 and 0.2 wt% per tonne dry oil sand ore.
14. The process as claimed in claim 1, wherein when the dosage of sodium triphosphate is 0.16 wt%, the recovery of bitumen in the bitumen froth product is greater than 80%.
CA2976863A 2017-08-16 2017-08-16 Method for processing weathered oil sand ore Active CA2976863C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CA2976863A CA2976863C (en) 2017-08-16 2017-08-16 Method for processing weathered oil sand ore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CA2976863A CA2976863C (en) 2017-08-16 2017-08-16 Method for processing weathered oil sand ore

Publications (2)

Publication Number Publication Date
CA2976863A1 true CA2976863A1 (en) 2019-02-16
CA2976863C CA2976863C (en) 2019-06-11

Family

ID=65352359

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2976863A Active CA2976863C (en) 2017-08-16 2017-08-16 Method for processing weathered oil sand ore

Country Status (1)

Country Link
CA (1) CA2976863C (en)

Also Published As

Publication number Publication date
CA2976863C (en) 2019-06-11

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