CA2566117A1 - Viscoelastic upgrading of heavy oil by altering its elastic modulus - Google Patents
Viscoelastic upgrading of heavy oil by altering its elastic modulus Download PDFInfo
- Publication number
- CA2566117A1 CA2566117A1 CA002566117A CA2566117A CA2566117A1 CA 2566117 A1 CA2566117 A1 CA 2566117A1 CA 002566117 A CA002566117 A CA 002566117A CA 2566117 A CA2566117 A CA 2566117A CA 2566117 A1 CA2566117 A1 CA 2566117A1
- Authority
- CA
- Canada
- Prior art keywords
- elastic modulus
- acid
- resid
- lowering agent
- acids
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/04—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
- C10B57/06—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing additives
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G17/00—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
- C10G17/02—Refining 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G17/00—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
- C10G17/02—Refining 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
- C10G17/04—Liquid-liquid treatment forming two immiscible phases
- C10G17/06—Liquid-liquid treatment forming two immiscible phases using acids derived from sulfur or acid sludge thereof
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G17/00—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
- C10G17/02—Refining 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
- C10G17/04—Liquid-liquid treatment forming two immiscible phases
- C10G17/07—Liquid-liquid treatment forming two immiscible phases using halogen acids or oxyacids of halogen
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G19/00—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
- C10G19/02—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment with aqueous alkaline solutions
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/005—Coking (in order to produce liquid products mainly)
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1033—Oil well production fluids
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1077—Vacuum residues
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
- C10G2300/805—Water
- C10G2300/807—Steam
Abstract
A method for upgrading the viscoelastic properties of a heavy oil by altering its elastic modulus. An effective amount of one or more elastic modulus lowering agents are used, wherein preferred elastic modulus lowering agents include mineral and organic acids and bases, preferably strong bases, such as hydroxides of metals selected from the alkali and alkaline-earth metals.
Claims (12)
1. A method for improving the flow properties of a heavy oil feedstock by lowering its elastic modulus, which method comprises:
treating the feedstock with an effective amount of one or more elastic modulus lowering agent selected from acids, bases, and porphyrins.
treating the feedstock with an effective amount of one or more elastic modulus lowering agent selected from acids, bases, and porphyrins.
2. A delayed coking process comprising:
a) heating a petroleum resid, which is essentially a solid at room temperature, in a first heating zone, to a temperature below coking temperatures for conversion into a pumpable liquid;
b) conducting said heated resid to a second heating zone wherein the heated resid is heated to an effective coking temperature;
c) conducting said heated resid from said second heating zone to a coking zone wherein vapor products are collected overhead and coke is formed; and d) introducing into said resid or heated resid at least one elastic modulus lowering agents that are effective for lowering the elastic modulus of the resid, wherein said at least one elastic modulus lowering agent is introduced into said vacuum resid at a point upstream of the first heating zone, upstream of the second heating zone, or both.
a) heating a petroleum resid, which is essentially a solid at room temperature, in a first heating zone, to a temperature below coking temperatures for conversion into a pumpable liquid;
b) conducting said heated resid to a second heating zone wherein the heated resid is heated to an effective coking temperature;
c) conducting said heated resid from said second heating zone to a coking zone wherein vapor products are collected overhead and coke is formed; and d) introducing into said resid or heated resid at least one elastic modulus lowering agents that are effective for lowering the elastic modulus of the resid, wherein said at least one elastic modulus lowering agent is introduced into said vacuum resid at a point upstream of the first heating zone, upstream of the second heating zone, or both.
3. The method of claim 2 wherein the elastic modulus lowering agent is selected from acids, bases, and porphyrins.
4. The method of any preceding claim wherein the elastic modulus lowering agent is at least one mineral acid selected from sulfuric acid, hydrochloric acid and perchloric acid.
5. The method of any preceding claim wherein the acid is selected from sulfuric acid and hydrochloric acid.
6. The method of any preceding claim wherein the acid is an organic acid selected from para-toluene sulfonic, alkyl toluene sulfonic acids, mono di-and trialkkyl phosphoric acids, organic mono or di carboxylic acids, formic, C3 to organic carboxylic acids, succinic acid, low molecular weight petroleum naphthenic acid, and mixtures thereof.
7. The method of any preceding claim wherein the acid is para-toluene sulfonic acid.
8. The method of any preceding claim wherein the elastic modulus lowering agent is as least one metallo-porphyrin selected from nickel and/or vanadium porphyrin.
9. The method of any preceding claim wherein the elastic modulus lowering agent is at least one hydroxide of a metal selected from the alkali metals and/or alkaline earth metals.
10. The method of any preceding claim wherein the hydroxide is of one or more metals selected from sodium, potassium, calcium and magnesium.
11. The method of any preceding claim wherein the hydroxide is of a metal selected from sodium and/or potassium.
12. The method of any preceding claim wherein the elastic modulus lowering agent is used in combination with an effective amount of steam.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US57134904P | 2004-05-14 | 2004-05-14 | |
US60/571,349 | 2004-05-14 | ||
PCT/US2005/016706 WO2005113707A1 (en) | 2004-05-14 | 2005-05-12 | Viscoelastic upgrading of heavy oil by altering its elastic modulus |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2566117A1 true CA2566117A1 (en) | 2005-12-01 |
CA2566117C CA2566117C (en) | 2012-12-04 |
Family
ID=34969519
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2566117A Expired - Fee Related CA2566117C (en) | 2004-05-14 | 2005-05-12 | Viscoelastic upgrading of heavy oil by altering its elastic modulus |
Country Status (9)
Country | Link |
---|---|
US (1) | US7794586B2 (en) |
EP (1) | EP1773967A1 (en) |
JP (1) | JP2007537342A (en) |
CN (1) | CN1954049B (en) |
AU (1) | AU2005245862A1 (en) |
BR (1) | BRPI0510984A (en) |
CA (1) | CA2566117C (en) |
MX (1) | MXPA06012602A (en) |
WO (1) | WO2005113707A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7871510B2 (en) * | 2007-08-28 | 2011-01-18 | Exxonmobil Research & Engineering Co. | Production of an enhanced resid coker feed using ultrafiltration |
US7794587B2 (en) * | 2008-01-22 | 2010-09-14 | Exxonmobil Research And Engineering Company | Method to alter coke morphology using metal salts of aromatic sulfonic acids and/or polysulfonic acids |
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-
2005
- 2005-05-12 AU AU2005245862A patent/AU2005245862A1/en not_active Abandoned
- 2005-05-12 EP EP05747557A patent/EP1773967A1/en not_active Withdrawn
- 2005-05-12 US US11/127,824 patent/US7794586B2/en not_active Expired - Fee Related
- 2005-05-12 CN CN2005800155162A patent/CN1954049B/en not_active Expired - Fee Related
- 2005-05-12 JP JP2007513377A patent/JP2007537342A/en active Pending
- 2005-05-12 MX MXPA06012602A patent/MXPA06012602A/en unknown
- 2005-05-12 WO PCT/US2005/016706 patent/WO2005113707A1/en active Application Filing
- 2005-05-12 BR BRPI0510984-1A patent/BRPI0510984A/en not_active IP Right Cessation
- 2005-05-12 CA CA2566117A patent/CA2566117C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
AU2005245862A1 (en) | 2005-12-01 |
US7794586B2 (en) | 2010-09-14 |
EP1773967A1 (en) | 2007-04-18 |
US20050258075A1 (en) | 2005-11-24 |
CN1954049A (en) | 2007-04-25 |
BRPI0510984A (en) | 2007-12-04 |
CN1954049B (en) | 2012-02-29 |
WO2005113707A1 (en) | 2005-12-01 |
CA2566117C (en) | 2012-12-04 |
MXPA06012602A (en) | 2007-01-31 |
JP2007537342A (en) | 2007-12-20 |
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