[go: up one dir, main page]

WO2008143593A3 - Bbn 100 to substitute diesel fuel - Google Patents

Bbn 100 to substitute diesel fuel Download PDF

Info

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
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.)
Ceased
Application number
PCT/SG2008/000181
Other languages
French (fr)
Other versions
WO2008143593A2 (en
Inventor
Hendery @ Hendery Sie
B. F. Prawoto
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of WO2008143593A2 publication Critical patent/WO2008143593A2/en
Anticipated expiration legal-status Critical
Publication of WO2008143593A3 publication Critical patent/WO2008143593A3/en
Ceased legal-status Critical Current

Links

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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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 Ceased 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 Ceased 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

Similar Documents

Publication Publication Date Title
WO2008016330A3 (en) Bio formula to substitute diesel fuel
Bournay et al. New heterogeneous process for biodiesel production: A way to improve the quality and the value of the crude glycerin produced by biodiesel plants
Arzamendi et al. Alkaline and alkaline-earth metals compounds as catalysts for the methanolysis of sunflower oil
Peng et al. Extremely low sulfuric acid catalyst system for synthesis of methyl levulinate from glucose
Silitonga et al. Schleichera oleosa L oil as feedstock for biodiesel production
Olutoye et al. Production of biodiesel fuel by transesterification of different vegetable oils with methanol using Al2O3 modified MgZnO catalyst
AU2006293812B2 (en) Improved method for making ethyl esters from natural fats
Calixto et al. Synthesis of fatty acid methyl esters via direct transesterification with methanol/carbon dioxide mixtures from spent coffee grounds feedstock
Hájek et al. Transesterification of rapeseed oil by butanol and separation of butyl ester
Rengasamy et al. Biodiesel production from Pongamia pinnata oil using synthesized iron nanocatalyst
Malabadi et al. Biodiesel production: An updated review of evidence
EP3026096B1 (en) Method for preparing fatty acid alkyl ester using fat
MX2007003709A (en) Product for dust control and freeze control.
WO2008123925A3 (en) Biodiesel process
Hidawati et al. Treatment of glycerin pitch from biodiesel production
WO2008143593A3 (en) Bbn 100 to substitute diesel fuel
AU2013343475B2 (en) Process for manufacturing biofuels
CN107286001B (en) Method for separating polymethoxy dimethyl ether
FR3002936A1 (en) USE OF SULFONIC ACID FOR THE RECOVERY OF GLYCEROL RESULTING FROM TRIGLYCERIDE TRANS-ESTERIFICATION REACTION
Nage et al. Biodiesel production by a continuous process using a heterogeneous catalyst
JP5454996B2 (en) Method for producing fatty acid alkyl ester composition and method for treating fats and oils
CN101560141A (en) System and operating method for removing light oil impurity by methanol rectification
Li et al. Production of levulinic acid and furfural from biomass hydrolysis through a demonstration project
US9126967B2 (en) Process for the production of a dioxolane compound from crude glycerol
JP2004217864A (en) Fatty acid alkyl ester diesel fuel

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 08754019

Country of ref document: EP

Kind code of ref document: A2

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 08754019

Country of ref document: EP

Kind code of ref document: A2