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WO2018161134A1 - Système d'extraction d'huile de palmiste par procédé hydrodynamique - Google Patents

Système d'extraction d'huile de palmiste par procédé hydrodynamique Download PDF

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Publication number
WO2018161134A1
WO2018161134A1 PCT/BR2017/050058 BR2017050058W WO2018161134A1 WO 2018161134 A1 WO2018161134 A1 WO 2018161134A1 BR 2017050058 W BR2017050058 W BR 2017050058W WO 2018161134 A1 WO2018161134 A1 WO 2018161134A1
Authority
WO
WIPO (PCT)
Prior art keywords
water
ground
separation
oil
transporting
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/BR2017/050058
Other languages
English (en)
Portuguese (pt)
Inventor
Marius Juliano FARINA
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.)
Fast Industria E Comercio Ltda
Original Assignee
Fast Industria E Comercio Ltda
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 Fast Industria E Comercio Ltda filed Critical Fast Industria E Comercio Ltda
Priority to MYPI2019001575A priority Critical patent/MY198305A/en
Priority to MX2019004661A priority patent/MX2019004661A/es
Priority to CN201780067427.5A priority patent/CN109923196A/zh
Priority to PE2019000779A priority patent/PE20190861A1/es
Priority to CR20190167A priority patent/CR20190167A/es
Publication of WO2018161134A1 publication Critical patent/WO2018161134A1/fr
Priority to CONC2019/0003408A priority patent/CO2019003408A2/es
Priority to PH12019500914A priority patent/PH12019500914A1/en
Priority to ECSENADI201940560A priority patent/ECSP19040560A/es
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, 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
    • C11B1/00—Production of fats or fatty oils from raw materials
    • C11B1/10—Production of fats or fatty oils from raw materials by extracting
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, 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
    • C11B1/00—Production of fats or fatty oils from raw materials
    • C11B1/12—Production of fats or fatty oils from raw materials by melting out
    • C11B1/14—Production of fats or fatty oils from raw materials by melting out with hot water or aqueous solutions
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, 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
    • C11B3/00—Refining fats or fatty oils

Definitions

  • Palm In Brazil, the plant that supplies Palm Oil is the Palm itself, also called “Palm Palm Tree”. Scientific name: Elaeis guineensis. Already Palm Oil is called “Palm Oil”, “Palm Oil” or “Palm Oil” itself. Palm is an oilseed from which two different types of oils can be extracted very distinctly: from the pulp (mesocarp) Palm Oil is extracted and almond is extracted from Palm kernel oil.
  • Palm kernel oil is extracted from palm fruit almond by physical methods (mechanical pressing) or chemical process, using solvents. In current physical methods press extraction is done at the end of the process. Prior to pressing, the walnut is heated with indirect steam to reduce moisture.
  • Patent document CN105087148 - Technology and device for manufacturing oil from palm berry fruit through dry method yeast killing features a system that extracts oil from palm fruit, has a separator for dividing and directing almond and pulp, but only the extraction of the pulp oil by press is described; pressing process. The nuts undergo a polishing process to remove the fibers and are stored whole for another extraction process not described in the document.
  • the system comprises a hydrocyclone for separation of dust and impurities, assisting in steam generation.
  • WO2014035760 - Pressed palm fiber solvent extraction performs solvent extraction and uses the cyclone to separate a solvent / palm oil fraction and a "heavy" fraction containing predominantly solid particles.
  • the walnut is heated with indirect steam to reduce moisture.
  • the Palm kernel oil extraction system described in this report uses a mechanical milling process and comprises the use of a hydrodynamic separation process for almond oil. It is characterized by successive milling steps of the walnut (shelled almond), diluted in water, so that by simple heating of the water allows the separation of the oil from the crushed solid material. Unlike the mechanical extraction processes of the current state of the art which use press at the end of the process.
  • the extraction system disclosed here equals or reduces the loss of the resulting product, with an increase in energy efficiency and a significant reduction in equipment maintenance costs.
  • the system unifies the processes of grinding the almond with the shell and separating them later through a hydrocyclone process, in addition the extraction of the oil will take place through the use of hydrodynamic separation system by centrifugal tridecanter. , rather than mechanical separation by pressing or chemical separation using solvents.
  • the system revealed in this report compared to existing mechanical systems, has several advantages, among them: higher energy efficiency, because it reduces the electricity consumption above 50%; lower steam consumption, over 60%; less equipment and the consequent reduction of maintenance costs; longer interval between maintenance; reduction of physical space, over 50%;
  • the extraction performance is 40% to 46%, unlike the mechanical process which is a maximum of 40% and decreases over time with the wear of the mechanical components of the equipment.
  • the disclosed system is characterized by simplifying the physical methods (mechanical pressing) eliminating several productive phases and consequently eliminating several equipments used today.
  • the disclosed system is characterized by not using solvents in the oil extraction processes, and consequently eliminates media and equipment for further separation of oil and solvent.
  • the Palm kernel oil extraction system by hydrodynamic process is characterized by a sequence of 3 grinding processes, reaching a sufficiently fine grain size that allows to release the almond oil; when it is in its last grinding phase, and is poured with a certain amount of water at a temperature of 90 to 100 ° for a period of 30 to 120 minutes, this mixture is passed into a centrifugal tridecanter for the separation of the 3 phases: water, oil and solid material in flour form. This flour is reprocessed. Again intended for a hot water tank with a temperature of 90 to 100 ° C, for a period of up to 30 to 120 minutes, for extraction of the remaining oil still contained in this flour. Preferably 60 minutes.
  • FIGURE 1 shows schematically a block diagram with components, raw material flow in the palm kernel oil extraction system.
  • the system comprises a sequence of steps that begins with transporting the nut from the storage silo to the hopper hopper (2).
  • Walnuts are ground in shell through a mill (3). Because the nuts are ground with the shell, there is a significant reduction in equipment, production steps and processing time.
  • Ground nuts are mixed with water in a static mixer (4).
  • a water reservoir (9) supplies water to the static mixer (4).
  • the resulting material is conveyed by hydraulic pump (5) to a hydrocyclone (6).
  • hydrocyclone (6) granulometric separation of nut shells occurs with the aid of water. The peel portion is separated from the larger granulometry in relation to ground almonds and the peel portion is separated from the smaller granulometry.
  • the larger grain portion of peels separated in the hydrocyclone is transported to a shell deposit.
  • the ground almond with the smallest shell size, classified in hydrocyclone (6) goes through a first centrifugal decanter separation process (7), where part of the moisture is removed.
  • the water (8) returns to the water reservoir (9) and the ground almond and part of the shell (10) is transported (101) to two or more milling processes (11) to reduce the particle size as much as possible. .
  • the ground almond and part of the shell (10), material coming from the last milling process (11), is heated by steam (12) in a first tank of heating (13) at a temperature of 90 to 100 ° C, with the addition of water and a residence time of 30 to 120 minutes.
  • the oil (16) removed in the second separation process (14) goes to the storage tanks (26) for dispatch.
  • the solid material (17) goes to a second heating tank (19), where it is heated again with the addition of water at a temperature of 90 to 100 ° C and with a residence time of up to 60 minutes.
  • the solid material (17) is then pumped (20) into a third separation process (21) by centrifugal tridecanter to remove as much oil as possible from the second separation process (14).
  • the oil (23) extracted in the third separation process (21) goes to the storage tanks (26) for dispatch.
  • the solid part (24) of the third separation process (21) may undergo a drying process to be transformed into dry flour used as animal feed or as biofuel, or to be used in wet form.
  • the revealed oil extraction system is characterized by the use of the hydrodynamic separation concept, eliminating existing pressing and chemical separation system in the current state of the art. This way, it occurs a variation in the types of fundamental equipment applied in the disclosed system relative to the systems available in the current state of the art. It provides space savings because the developed system uses less equipment and is faster with shorter product residence time in the system, generating a lower need for industrial floor space. Due to the fact that the revealed system is more compact, a reduction of equipment maintenance is expected; It has less need for installed equipment in relation to the physical methods (mechanical pressing), as well as reduction of the operating manpower and maintenance manpower. Below is a comparative table of the existing system in the current state of the art compared to the system disclosed in this report:
  • the walnut is stored in the silo.
  • the walnut is transported from the drying silo in order to be stored for the hopper to eliminate moisture from the dosing almond;
  • the almond is heated with the shells separated in the indirect steam hydrocyclone in order to be transported to the boilers. reduce humidity;
  • the water with almond and part of the resulting ground shell goes through a separation system (centrifugal decanter), where much of the moisture is removed.
  • the almond and part of the ground shell go to the second grinding system and the water returns to the mixing tank.
  • the oil is homogenized in the Almond and ground shell portion of the stirring tank. from the grinding process they are heated in a water heating tank to a temperature of about 90 to 100 ° C, where it remains for a time of 30 to 120 minutes. The mixture is pumped to a centrifugal tridecanter separation process where the oil will be separated from the water and solid without the use of chemicals.
  • the oil is sent to the tanks.
  • the oil extracted in the process goes from storage to the storage tanks for dispatch.
  • the water (cooking process liquid) returns to the heating tank.
  • Silo stores almond The solid part can pass a pressed system (in the form of flour); to be processed into animal feed or to be used as biofuel, or to be used in wet form.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Fats And Perfumes (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Centrifugal Separators (AREA)
  • Cyclones (AREA)
  • Seeds, Soups, And Other Foods (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

L'invention concerne un système d'extraction d'huile de palmiste faisant intervenir un procédé de "broyage" de la noix (amande avec enveloppe) consistant à effectuer la séparation par granulométrie de la matière triturée, au moyen d'un procédé "hydrocyclone", et à utiliser un procédé "hydrodynamique" pour la séparation de l'huile contenue dans la matière triturée, par "tridécanteur centrifuge", caractérisé en ce qu'il comprend des étapes successives de trituration et de broyage.
PCT/BR2017/050058 2017-03-08 2017-03-15 Système d'extraction d'huile de palmiste par procédé hydrodynamique Ceased WO2018161134A1 (fr)

Priority Applications (8)

Application Number Priority Date Filing Date Title
MYPI2019001575A MY198305A (en) 2017-03-08 2017-03-15 System for Extracting Palm Kernel Oil Using a Hydrodynamic Method
MX2019004661A MX2019004661A (es) 2017-03-08 2017-03-15 Sistema de extraccion de aceite de palmiste por proceso hidrodinamico.
CN201780067427.5A CN109923196A (zh) 2017-03-08 2017-03-15 借由流体动力学过程的棕榈仁油提取系统
PE2019000779A PE20190861A1 (es) 2017-03-08 2017-03-15 Sistema de extraccion de aceite de palmiste por proceso hidrodinamico
CR20190167A CR20190167A (es) 2017-03-08 2017-03-15 Sistema de extracción de aceite de palmiste por proceso hidrodinámico
CONC2019/0003408A CO2019003408A2 (es) 2017-03-08 2019-04-05 Sistema de extracción de aceite de palmiste por proceso hidrodinámico
PH12019500914A PH12019500914A1 (en) 2017-03-08 2019-04-24 System for extracting palm kernel oil using a hydrodynamic method
ECSENADI201940560A ECSP19040560A (es) 2017-03-08 2019-06-06 Sistema de extracción de aceite de palmiste por proceso hidrodinámico

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
BR102017004632-0A BR102017004632B1 (pt) 2017-03-08 2017-03-08 Sistema de extração de óleo de palmiste por processo hidrodinâmico
BRBR1020170046320 2017-03-08

Publications (1)

Publication Number Publication Date
WO2018161134A1 true WO2018161134A1 (fr) 2018-09-13

Family

ID=61965545

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/BR2017/050058 Ceased WO2018161134A1 (fr) 2017-03-08 2017-03-15 Système d'extraction d'huile de palmiste par procédé hydrodynamique

Country Status (10)

Country Link
CN (1) CN109923196A (fr)
BR (1) BR102017004632B1 (fr)
CO (1) CO2019003408A2 (fr)
CR (1) CR20190167A (fr)
EC (1) ECSP19040560A (fr)
MX (1) MX2019004661A (fr)
MY (1) MY198305A (fr)
NI (1) NI201900035A (fr)
PH (1) PH12019500914A1 (fr)
WO (1) WO2018161134A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3660135A1 (fr) * 2018-11-30 2020-06-03 Alfa Laval Corporate AB Procédé et système de production d'un produit pauvre en matières grasses

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020106431A1 (en) * 2000-12-01 2002-08-08 Jean-Pierre Martel Process and apparatus for the integral utillization of oil-producing drupes, particularly olives, and specific products obtained
WO2014035760A1 (fr) * 2012-08-29 2014-03-06 Desmet Ballestra North America, Inc. Extraction par solvant de fibrse de palme pressées

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB401550A (en) * 1932-08-06 1933-11-16 Krupp Fried Grusonwerk Ag Process and apparatus for the extraction of oil from oilcontaining fruits
FR2750431B1 (fr) * 1996-06-27 1998-09-18 Cooperation Internationale En Procede d'extraction d'huile de palmier et huile ainsi extraite
CA2645333C (fr) * 2006-03-03 2017-10-10 Specialty Protein Producers, Inc. Procedes permettant de separer la graisse de matieres vegetales autres que le soja et compositions ainsi produites
CN101904367B (zh) * 2010-08-11 2012-07-04 江西省粮油科学技术研究所 低温干燥油磨水代提取植物油脂的方法
MY165646A (en) * 2013-05-13 2018-04-18 Sime Darby Malaysia Berhad Method, apparatus and system for digestion and pressing of oil palm fruit
CN103484242B (zh) * 2013-09-30 2015-08-05 广西科学院 一种超声波辅助低温水浸提取桐油的方法
MY163847A (en) * 2015-02-10 2017-10-27 Teng Ye Ngan A method for treating effluent produced from palm oil milling process
CN106244313A (zh) * 2016-08-18 2016-12-21 贵州石阡佛顶山野生油茶油业有限公司 一种水代法茶油加工生产方法

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020106431A1 (en) * 2000-12-01 2002-08-08 Jean-Pierre Martel Process and apparatus for the integral utillization of oil-producing drupes, particularly olives, and specific products obtained
WO2014035760A1 (fr) * 2012-08-29 2014-03-06 Desmet Ballestra North America, Inc. Extraction par solvant de fibrse de palme pressées

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3660135A1 (fr) * 2018-11-30 2020-06-03 Alfa Laval Corporate AB Procédé et système de production d'un produit pauvre en matières grasses
WO2020109135A1 (fr) * 2018-11-30 2020-06-04 Alfa Laval Corporate Ab Procédé de production d'un produit à faible teneur en matière grasse et système de production d'un produit à faible teneur en matière grasse
CN113195693A (zh) * 2018-11-30 2021-07-30 阿法拉伐股份有限公司 生产低脂肪产品的方法和用于生产低脂肪产品的系统
AU2019389601B2 (en) * 2018-11-30 2022-08-04 Alfa Laval Corporate Ab Method of producing a low-fat product and a system for producing a low-fat product
US12173253B2 (en) 2018-11-30 2024-12-24 Alfa Laval Corporate Ab Method of producing a low-fat product and a system for producing a low-fat product

Also Published As

Publication number Publication date
BR102017004632A2 (pt) 2017-09-19
ECSP19040560A (es) 2019-06-30
CR20190167A (es) 2019-08-16
CN109923196A (zh) 2019-06-21
MX2019004661A (es) 2019-08-21
BR102017004632B1 (pt) 2022-12-27
MY198305A (en) 2023-08-22
PH12019500914A1 (en) 2019-08-05
NI201900035A (es) 2019-09-12
CO2019003408A2 (es) 2019-04-12

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