WO2008016330A3 - Bio formula to substitute diesel fuel - Google Patents
Bio formula to substitute diesel fuel Download PDFInfo
- Publication number
- WO2008016330A3 WO2008016330A3 PCT/SG2007/000224 SG2007000224W WO2008016330A3 WO 2008016330 A3 WO2008016330 A3 WO 2008016330A3 SG 2007000224 W SG2007000224 W SG 2007000224W WO 2008016330 A3 WO2008016330 A3 WO 2008016330A3
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- tank
- fraction
- proceeded
- distillation
- retained
- Prior art date
Links
- 239000002283 diesel fuel Substances 0.000 title abstract 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract 6
- 238000004821 distillation Methods 0.000 abstract 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract 3
- 230000000717 retained effect Effects 0.000 abstract 3
- 235000013162 Cocos nucifera Nutrition 0.000 abstract 2
- 244000060011 Cocos nucifera Species 0.000 abstract 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract 2
- 239000003225 biodiesel Substances 0.000 abstract 2
- 239000007788 liquid Substances 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 2
- 239000001117 sulphuric acid Substances 0.000 abstract 2
- 235000011149 sulphuric acid Nutrition 0.000 abstract 2
- 239000002699 waste material Substances 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 abstract 1
- 239000007795 chemical reaction product Substances 0.000 abstract 1
- 235000013399 edible fruits Nutrition 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 abstract 1
- 230000008020 evaporation Effects 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 150000004702 methyl esters Chemical class 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 230000003472 neutralizing effect Effects 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS 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
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
-
- 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
- C10G2300/1011—Biomass
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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)
- Liquid Carbonaceous Fuels (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fats And Perfumes (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Bio formula 100 production process as an alternative material to substitute diesel fuel is disclosed. The process covers the following stages: refinery of oil waste originated from palm coconut, the end-product proceeds into R1 reactor while adding methanol and sulphuric acid, evaporation in E1, distillation in column D1, the result is retained in TB1 bait tank and proceeded into R3 tank, NaOH/KOH is included, having WVO flow in (oil waste of fruits/palm coconut) which have been evaporated in E1 and reserved in PR1, mixed and put into the R2A and R2B through M1 together with the mixture result of R3 proceeded into PR2, then distillation into D2 column for continued process in D1 so that D1 input becomes two that is D2 and E1, the bottom/liquid fraction through the reboiler, in liquid condition, is recovered/withdrawn through D3 distillation column, retained in TB2, at D3 distillation column, the top/vapour fraction, in the form of methanol through the condenser, proceeding to TB2, methyl ester/biodiesel is proceeded into R4 Reactor, neutralising by adding sulphuric acid from TB3 tank and water from TB4 water reserve tank, processed as the second catalyst, which then being evaporated in E2, the top fraction is retained in TB5, and the bottom fraction in the form of biodiesel 100 is reserved.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ID20060449 | 2006-08-01 | ||
INP00200600449 | 2006-08-01 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2008016330A2 WO2008016330A2 (en) | 2008-02-07 |
WO2008016330A3 true WO2008016330A3 (en) | 2009-06-11 |
Family
ID=38997593
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/SG2007/000224 WO2008016330A2 (en) | 2006-08-01 | 2007-07-30 | Bio formula to substitute diesel fuel |
Country Status (2)
Country | Link |
---|---|
US (1) | US20080047194A1 (en) |
WO (1) | WO2008016330A2 (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010062958A1 (en) * | 2008-11-26 | 2010-06-03 | Elevance Renewable Sciences, Inc. | Methods of producing jet fuel from natural oil feedstocks through metathesis reactions |
WO2010062932A1 (en) * | 2008-11-26 | 2010-06-03 | Elevance Renewable Sciences, Inc. | Methods of producing jet fuel from natural oil feedstocks through oxygen-cleaved reactions |
US8735640B2 (en) | 2009-10-12 | 2014-05-27 | Elevance Renewable Sciences, Inc. | Methods of refining and producing fuel and specialty chemicals from natural oil feedstocks |
US9000246B2 (en) | 2009-10-12 | 2015-04-07 | Elevance Renewable Sciences, Inc. | Methods of refining and producing dibasic esters and acids from natural oil feedstocks |
US9169447B2 (en) | 2009-10-12 | 2015-10-27 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils, and methods of producing fuel compositions |
US9175231B2 (en) | 2009-10-12 | 2015-11-03 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils and methods of producing fuel compositions |
CA3035015C (en) | 2009-10-12 | 2021-03-16 | Elevance Renewable Sciences, Inc. | Methods of refining and producing fuel from natural oil feedstocks |
US9365487B2 (en) | 2009-10-12 | 2016-06-14 | Elevance Renewable Sciences, Inc. | Methods of refining and producing dibasic esters and acids from natural oil feedstocks |
US9382502B2 (en) | 2009-10-12 | 2016-07-05 | Elevance Renewable Sciences, Inc. | Methods of refining and producing isomerized fatty acid esters and fatty acids from natural oil feedstocks |
US9051519B2 (en) | 2009-10-12 | 2015-06-09 | Elevance Renewable Sciences, Inc. | Diene-selective hydrogenation of metathesis derived olefins and unsaturated esters |
US9222056B2 (en) | 2009-10-12 | 2015-12-29 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils, and methods of producing fuel compositions |
US9133416B2 (en) | 2011-12-22 | 2015-09-15 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
US9139493B2 (en) | 2011-12-22 | 2015-09-22 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
US9169174B2 (en) | 2011-12-22 | 2015-10-27 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
US9388098B2 (en) | 2012-10-09 | 2016-07-12 | Elevance Renewable Sciences, Inc. | Methods of making high-weight esters, acids, and derivatives thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5525136A (en) * | 1994-09-06 | 1996-06-11 | Rosen; Richard M. | Gasketed multi-media air cleaner |
US20040074760A1 (en) * | 2002-10-17 | 2004-04-22 | Carnegie Mellon University | Production of biofuels |
US6965044B1 (en) * | 2001-07-06 | 2005-11-15 | Iowa State University Research Foundation | Method of converting free fatty acids to fatty acid methyl esters with small excess of methanol |
JP2005350632A (en) * | 2004-06-14 | 2005-12-22 | Electric Power Dev Co Ltd | Method for producing biodiesel fuel |
WO2008008042A1 (en) * | 2006-07-11 | 2008-01-17 | W.J.E. Investments Limited | Biofuel(s) |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3444893A1 (en) * | 1984-12-08 | 1986-06-12 | Henkel KGaA, 4000 Düsseldorf | METHOD FOR PRODUCING FATTY ACID METHYL ESTERS |
FR2696185B1 (en) * | 1992-09-25 | 1994-12-02 | Inst Francais Du Petrole | Improved process for the production of esters from fatty substances of natural origin. |
MY150129A (en) * | 2004-04-09 | 2013-11-29 | Archer Daniels Midland Co | Method of preparing fatty acid alkyl esters from waste or recycled fatty acid stock |
-
2007
- 2007-07-30 WO PCT/SG2007/000224 patent/WO2008016330A2/en active Application Filing
- 2007-07-31 US US11/831,535 patent/US20080047194A1/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5525136A (en) * | 1994-09-06 | 1996-06-11 | Rosen; Richard M. | Gasketed multi-media air cleaner |
US6965044B1 (en) * | 2001-07-06 | 2005-11-15 | Iowa State University Research Foundation | Method of converting free fatty acids to fatty acid methyl esters with small excess of methanol |
US20040074760A1 (en) * | 2002-10-17 | 2004-04-22 | Carnegie Mellon University | Production of biofuels |
JP2005350632A (en) * | 2004-06-14 | 2005-12-22 | Electric Power Dev Co Ltd | Method for producing biodiesel fuel |
WO2008008042A1 (en) * | 2006-07-11 | 2008-01-17 | W.J.E. Investments Limited | Biofuel(s) |
Non-Patent Citations (1)
Title |
---|
C.A.W.ALLEN ET AL.: "Comparative Analysis of the Atomization Characteristics of Fifteen Biodiesel Fuel Types", AMERICAN SOCIETY OF AGRICULTURAL ENGINEERS, vol. 43, no. 2, 1996, pages 207 - 211 * |
Also Published As
Publication number | Publication date |
---|---|
US20080047194A1 (en) | 2008-02-28 |
WO2008016330A2 (en) | 2008-02-07 |
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