MY178140A - Optimising the utilisation of renewable energy from biomass resources in the palm oil industry - Google Patents

Optimising the utilisation of renewable energy from biomass resources in the palm oil industry

Info

Publication number
MY178140A
MY178140A MYPI2013002838A MYPI2013002838A MY178140A MY 178140 A MY178140 A MY 178140A MY PI2013002838 A MYPI2013002838 A MY PI2013002838A MY PI2013002838 A MYPI2013002838 A MY PI2013002838A MY 178140 A MY178140 A MY 178140A
Authority
MY
Malaysia
Prior art keywords
steam
temperature
palm oil
energy
source
Prior art date
Application number
MYPI2013002838A
Inventor
Moorthy A/L Palanisamy Krishna
Original Assignee
Moorthy A/L Palanisamy Krishna
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 Moorthy A/L Palanisamy Krishna filed Critical Moorthy A/L Palanisamy Krishna
Publication of MY178140A publication Critical patent/MY178140A/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/12Production of fats or fatty oils from raw materials by melting out
    • C11B1/16Production of fats or fatty oils from raw materials by melting out with steam
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/12Refining fats or fatty oils by distillation
    • C11B3/14Refining fats or fatty oils by distillation with the use of indifferent gases or vapours, e.g. steam
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01DNON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D1/00Non-positive-displacement machines or engines, e.g. steam turbines
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K17/00Using steam or condensate extracted or exhausted from steam engine plant
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/14Combined heat and power generation [CHP]

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Combustion & Propulsion (AREA)
  • Fats And Perfumes (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Coke Industry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

It is imperative that the most efficient use be found for the biomass energy potential in the palm oil milling industry to reduce carbon emissions and displace the maximum amount of fossil fuel based energy. Environmental considerations have therefore invoked economic interest in technologies to improve efficient energy production and usage in the palm oil mills. The invention provides an arrangement for operating energy system of a crude palm oil extraction plant and method thereof. The arrangement for operating energy system of a crude palm oil extraction plant achieves the target of higher efficiency of energy utilisation by using steam source at a low temperature featuring in the design operation point of the energy system providing thermal energy to the palm oil extraction process. Accordingly, the present invention provides an arrangement for operating energy system of a crude palm oil extraction plant which includes a primary heat source configured to provide heat energy in the form of high pressure and temperature steam; a steam prime mover configured to receive high pressure and temperature steam from the primary heat source; a back pressure vessel configured to receive heat energy in the form of steam exiting from the steam prime mover; at least one unit process of the crude palm oil extraction plant requiring heat energy; and at least one means configured to convey heat energy from the back pressure vessel as source steam to the unit process; wherein the energy system is designed and configured to operate at a design operation point for the temperature of the source steam of the back pressure vessel wherein the temperature of the source steam of the back pressure vessel is between 100 ?C and 141 ?C at saturation pressure. Preferably, the temperature of the source steam of the back pressure vessel is between 115 ?C and 141 ?C at saturation pressure; the temperature of the source steam of the back pressure vessel between 115 ?C and 138 ?C at saturation pressure is more preferred and the temperature of the source steam of the back pressure vessel between 115 ?C and 130 ?C at saturation pressure is even more preferred. Where one of the unit processes is sterilization of fresh fruit bunches (FFB) by a continuous sterilizer the most preferred temperature of the exiting steam is between greater than 100 ?C and less than 115 ?C at saturation pressure.
MYPI2013002838A 2011-02-07 2012-02-03 Optimising the utilisation of renewable energy from biomass resources in the palm oil industry MY178140A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
MYPI2011000551 2011-02-07

Publications (1)

Publication Number Publication Date
MY178140A true MY178140A (en) 2020-10-05

Family

ID=46638811

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2013002838A MY178140A (en) 2011-02-07 2012-02-03 Optimising the utilisation of renewable energy from biomass resources in the palm oil industry

Country Status (11)

Country Link
AP (1) AP3481A (en)
BR (1) BR112013019721B1 (en)
CR (2) CR20130382A (en)
DO (1) DOP2013000173A (en)
EC (1) ECSP13013000A (en)
GB (1) GB2507173B (en)
GT (1) GT201300195A (en)
MX (1) MX362776B (en)
MY (1) MY178140A (en)
PE (1) PE20140822A1 (en)
WO (1) WO2012108756A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11955782B1 (en) 2022-11-01 2024-04-09 Typhon Technology Solutions (U.S.), Llc System and method for fracturing of underground formations using electric grid power

Also Published As

Publication number Publication date
WO2012108756A1 (en) 2012-08-16
GB2507173B (en) 2019-08-14
CR20130383A (en) 2014-02-21
MX362776B (en) 2019-02-08
BR112013019721B1 (en) 2020-11-03
MX2013009108A (en) 2014-02-28
GB2507173A (en) 2014-04-23
AP3481A (en) 2015-12-31
PE20140822A1 (en) 2014-07-12
ECSP13013000A (en) 2014-01-31
CR20130382A (en) 2014-02-06
GB201315817D0 (en) 2013-10-23
DOP2013000173A (en) 2014-04-15
GT201300195A (en) 2017-05-23
BR112013019721A2 (en) 2016-12-20

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