WO2008143593A3 - Bbn 100 to substitute diesel fuel - Google Patents

Bbn 100 to substitute diesel fuel Download PDF

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Publication number
WO2008143593A3
WO2008143593A3 PCT/SG2008/000181 SG2008000181W WO2008143593A3 WO 2008143593 A3 WO2008143593 A3 WO 2008143593A3 SG 2008000181 W SG2008000181 W SG 2008000181W WO 2008143593 A3 WO2008143593 A3 WO 2008143593A3
Authority
WO
WIPO (PCT)
Prior art keywords
tank
proceeded
reserved
result
reactor
Prior art date
Application number
PCT/SG2008/000181
Other languages
French (fr)
Other versions
WO2008143593A2 (en
Inventor
Hendery @ Hendery Sie
B. F. Prawoto
Original Assignee
Sie Hendery Hendery
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 Sie Hendery Hendery filed Critical Sie Hendery Hendery
Publication of WO2008143593A2 publication Critical patent/WO2008143593A2/en
Publication of WO2008143593A3 publication Critical patent/WO2008143593A3/en

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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
    • 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

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)

Abstract

BBN 100 (biofuel) production process as an alternative material to substitute diesel fuel, essentially covers the following distillation stages: - refinery of oil waste originated from palm coconut or jatropha through distillation - the end-product proceeds into R1A, R1B, R1C reactor while adding methanol and sulphuric acid - the result is put in E1 evaporator, - the result is being proceeded into D1 distillation column to be distilled - methanol distillation result is retained in TB1 bait tank and proceeded into R3 tank, at the same time NaOH/KOH is included, - then to have VWO flow in (oil waste of fruits/palm coconut) which have been evaporated in E1 and reserved in PR1 (Pre Reactor Reserved), mixed and put into the R2A and R2B (Main Reactor CSTR) through M1 together with the mixture result of R3 - the result of R2A and R2B is then proceeded into PR2 (Pre Reactor Reserved), - then is proceeded into D2 distillation column for continued process in D1 so that D1 input becomes two that is D2 and E1, and hereafter distilled as in D1 initial stage - the bottom/liquid fraction, in the form of (glycerol + soap + methyl ester) through the reboiler, in liquid condition, is recovered/withdrawn through D3 distillation column, retained in TB2 Glycerol reserved tank, - at D3 distillation column, the top/vapour fraction, in the form of methanol through the condenser, in liquid condition is proceeded to TB2, methyl ester/biodiesel is proceeded into R4 Reactor, - at R4 neutralizing reactor being neutralized by adding sulphuric acid from TB3 tank (the sulphuric acid bait tank) and water from TB4 water reserve tank, processed as the second catalyst, which then being evaporated in E2, - the evaporation result, the top fraction consisting of water + soap + salt is retained in TB5 Dirty Water Reserved Tank, and the bottom fraction in the form of biodiesel 100 (futher-on called as Biofuel BBN-100 being the substitution of diesel fuel) is reserved in the Biofuel BBN-100 Product Tank.
PCT/SG2008/000181 2007-05-24 2008-05-14 Bbn 100 to substitute diesel fuel WO2008143593A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ID20070247 2007-05-24
IDP00200700247 2007-05-24

Publications (2)

Publication Number Publication Date
WO2008143593A2 WO2008143593A2 (en) 2008-11-27
WO2008143593A3 true WO2008143593A3 (en) 2011-09-09

Family

ID=40032302

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SG2008/000181 WO2008143593A2 (en) 2007-05-24 2008-05-14 Bbn 100 to substitute diesel fuel

Country Status (1)

Country Link
WO (1) WO2008143593A2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BRPI1001608B1 (en) * 2010-05-21 2018-09-11 Petroleo Brasileiro S.A. - Petrobras aviation biokerosene production process
CN105270771B (en) * 2015-11-20 2017-05-17 重庆恒宇华顿新能源开发有限公司 Distributed control linkage oil storage tank with gas concentration detection function

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001012581A1 (en) * 1999-08-18 2001-02-22 David Gavin Brooke Boocock Single-phase process for production of fatty acid methyl esters from mixtures of triglycerides and fatty acids
WO2006105306A2 (en) * 2005-03-29 2006-10-05 Arizona Chemical Company Compostions containing fatty acids and/or derivatives thereof and a low temperature stabilizer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001012581A1 (en) * 1999-08-18 2001-02-22 David Gavin Brooke Boocock Single-phase process for production of fatty acid methyl esters from mixtures of triglycerides and fatty acids
WO2006105306A2 (en) * 2005-03-29 2006-10-05 Arizona Chemical Company Compostions containing fatty acids and/or derivatives thereof and a low temperature stabilizer

Also Published As

Publication number Publication date
WO2008143593A2 (en) 2008-11-27

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