WO2018161134A1 - System for extracting palm kernel oil using a hydrodynamic method - Google Patents
System for extracting palm kernel oil using a hydrodynamic method Download PDFInfo
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- 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
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- 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
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- 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
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- 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.
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- 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)
- Disintegrating Or Milling (AREA)
- Seeds, Soups, And Other Foods (AREA)
- Centrifugal Separators (AREA)
- Cyclones (AREA)
Abstract
Description
SISTEMA DE EXTRAÇÃO DE ÓLEO DE PALMISTE POR PROCESSO HIDRODINÂMICO PALMISM OIL EXTRACTION SYSTEM BY HYDRODYNAMIC PROCESS
[001 ] Trata-se de sistema de extração de óleo de palmiste que utiliza processo de "moagem" da noz (amêndoa com casca), faz a separação por granulometria do material triturado, por processo "hidrociclone" e utiliza processo "hidrodinâmico" na separação do óleo contido no material triturado, por "tridecanter centrífugo". It is a palm kernel oil extraction system that uses walnut "grinding" process (almond in shell), makes separation by granulometry of the crushed material, by "hydrocyclone" process and uses "hydrodynamic" process in the separation of the oil contained in the crushed material by "centrifugal tridecanter".
ESTADO DA TÉCNICA TECHNICAL STATE
[002] No Brasil, a planta que fornece o Óleo de Palma é a própria Palma, também chamada de "Palmeira do Dendê". Nome científico: Elaeis guineensis. Já o Óleo de Palma é chamado de "Azeite de Dendê", "Azeite de Dendém" ou "Óleo de Palma" mesmo. A Palma é uma oleaginosa da qual se pode extrair dois tipos diferentes de óleos bem distintos: da polpa (mesocárpio) se extrai o Óleo de Palma e da amêndoa se extrai o Óleo de Palmiste. [002] 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.
[003] O óleo de Palmiste é extraído da amêndoa do fruto da palmeira por métodos físicos (prensagem mecânica) ou processo químico, com o uso de solventes. Nos métodos físicos atuais faz-se a extração com uso de prensa ao final do processo. Antes da prensagem, a noz é aquecida com vapor indireto com o intuito de reduzir a umidade. 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.
[004] No documento de patente EP121 1303 - Method and apparatus for the integrated upgrading of oil-bearing drupes, especially olives and the products resulting therefrom é apresentado um sistema para extração de óleo a partir de diferentes partes da fruta. A fruta inteira é esquentada e em seguida transferida para um compartimento, onde ocorre a separação da polpa a partir de filtros de tela e um mecanismo agitador. O restante da fruta, pele e amêndoa (inteira e com casca), são enviados para um hidrociclone, onde são separados. A pele é utilizada para produção de ração ou ceras, enquanto a amêndoa é enviada para um novo mecanismo separador, onde é retirada a casca, que é então enviada para a caldeira. Finalmente a amêndoa, inteira, é prensada para extração do óleo de palmiste. A extração do óleo é por processo mecânico de prensagem. [004] In patent document EP121 1303 - Method and apparatus for the integrated upgrading of oil-bearing drupes, especially olives and products resulting therefrom, a system for extracting oil from different parts of the fruit is presented. The whole fruit is heated and then transferred to a compartment where the pulp is separated from water filters. screen and a shaker mechanism. The remaining fruit, skin and almond (whole and in shell) are sent to a hydrocyclone, where they are separated. The skin is used for the production of feed or wax, while the almond is sent to a new separating mechanism, where the shell is removed, which is then sent to the boiler. Finally the whole almond is pressed to extract palm kernel oil. Oil extraction is by mechanical pressing process.
[005] O documento de patente CN105087148 - Technology and device for manufacturing oil from palm berry fruit through dry method yeast killing apresenta um sistema que extrai óleo da fruta da palmeira, possui um separador para dividir e direcionar a amêndoa e a polpa, porém apenas é descrita a extração do óleo da polpa, feita com prensa; processo de prensagem. As nozes passam por um processo de polimento para remoção das fibras e são armazenadas inteiras para outro processo de extração, não descrito no documento. O sistema compreende um hidrociclone para separação da poeira e impurezas, auxiliar na geração de vapor. [005] 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.
[006] O documento de patente WO2014035760 - Pressed palm fibre solvent extraction faz a extração por solvente e utiliza o ciclone para separação de uma fracção de solvente / óleo de palma e uma fracção "pesada" contendo predominantemente partículas sólidas. 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.
[007] Objetos de interesse, que consolidam o estado da técnica, estão publicados nos endereços abaixo: [007] Objects of interest, which consolidate the state of the art, are published at the following addresses:
• http://www.palmoilfactory.com/products/palm-oil-mill-plant/palm-kernel- recoverv-station.html • http://www.iimer.com/papers/Vol3 lssue4/BA3420232026.pdf• http://www.palmoilfactory.com/products/palm-oil-mill-plant/palm-kernel- recoverv-station.html • http://www.iimer.com/papers/Vol3 lssue4 / BA3420232026.pdf
• http://www.palmoilmachine.com/Palm Kernel Recoverv Station 62.ht ml • http://www.palmoilmachine.com/Palm Kernel Recoverv Station 62.ht ml
• http://www.palmoilmills.org/products/palm-oil-mill-plant/palm-kernel- recovery-station.html • http://www.palmoilmills.org/products/palm-oil-mill-plant/palm-kernel- recovery-station.html
[008] A noz é aquecida com vapor indireto com o intuito de reduzir a umidade. The walnut is heated with indirect steam to reduce moisture.
DESCRIÇÃO DA INVENÇÃO DESCRIPTION OF THE INVENTION
[009] O sistema para extração de óleo de Palmiste, descrito neste relatório, utiliza processo mecânico de moagem e compreende o uso de processo de separação hidrodinâmico do óleo da amêndoa. Se caracteriza por sucessivas etapas moagem da noz (amêndoa com casca), diluída em água, de modo que por simples aquecimento da água permite a separação do óleo do material sólido triturado. Diferente dos processos mecânicos de extração, do atual estado da técnica, que usam prensa ao final do processo. O sistema de extração, aqui revelado, iguala ou reduz a perda do produto resultante, com aumento no rendimento energético e expressiva redução com gastos com manutenção dos equipamentos. 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.
[0010] O sistema unifica os processos de moagem da amêndoa com a casca e separá-las posteriormente através de um processo de hidrociclone, além disso a extração do óleo dar-se-á através do uso de sistema de separação hidrodinâmico, por tridecanter centrífugo, ao invés da separação mecânica por processo de prensagem ou separação química que usa solventes. O sistema revelado neste relatório, em relação aos sistemas mecânico existentes, possui várias vantagens, entre elas: maior rendimento energético, pois reduz o consumo de energia elétrica acima de 50%; menor consumo de vapor, acima de 60%; menor quantidade de equipamentos e a consequente redução dos custos de manutenção; maior intervalo entre manutenções; redução de espaço físico, acima de 50%; o rendimento na extração é de 40% a 46%, diferente do processo mecânico que é de no máximo 40% e decaí com o passar do tempo, com o desgaste dos componentes mecânicos dos equipamentos. O sistema revelado se caracteriza por simplificar os métodos físicos (prensagem mecânica) eliminando diversas fases produtivas e por consequência dispensando vários equipamentos hoje utilizados. O sistema revelado se caracteriza por não utilizar solventes nos processos de extração do óleo, e consequentemente elimina meios e equipamentos para posterior separação do óleo e do solvente.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.
] O Sistema de Extração de Óleo de Palmiste por Processo Hidrodinâmico, se caracteriza por uma sequência de 3 processos de moagem, atingindo uma granulometria suficientemente fina que permita desprender o óleo da amêndoa; quando está na sua última fase de moagem, e for posta com uma determinada quantidade de água a uma temperatura de 90 a 100°, por um período de 30 até 120 minutos, essa mistura passa em um equipamento tridecanter centrífugo para separação das 3 fases: água, óleo e material sólido, em forma de farinha. Esta farinha é reprocessada. Novamente destinada a um tanque de água quente com temperatura de 90 a 100°C, por um período de até 30 até 120 minutos, para extração do óleo remanescente ainda contido nesta farinha. Preferencialmente 60 minutos. ] A FIGURA 1 mostra de forma esquemática diagrama de bloco com componentes, fluxo da matéria prima no sistema de extração do óleo de palmiste.] 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.
] DESCRIÇÃO DETALHADA DA INVENÇÃO ] DETAILED DESCRIPTION OF THE INVENTION
] O sistema compreende uma sequência de etapas que se inicia com o transporte da noz do silo de armazenamento até a moega dosadora(2). As nozes são moídas com casca através de um moinho(3). Pelo fato das nozes serem moídas com a casca, há uma expressiva redução de equipamentos, de etapas produtivas e tempo de processamento. As nozes moídas são misturadas com água num misturador estático(4). Um reservatório(9) de água fornece água ao misturador estático(4). O material resultante é transportado por bomba(5) hidráulica para um hidrociclone(6). No hidrociclone(6) ocorre a separação granulométrica das cascas das nozes, com auxílio de água. Faz-se a separação da porção de cascas, de maior granulometria em relação as amêndoas moídas e a separação da porção das cascas, de menor granulometria. A porção de cascas, de maior granulometria, separadas no hidrociclone é transportada até um depósito de cascas. A amêndoa moída com a porção de cascas de menor granulometria, classificada no hidrociclone(6), passa por um primeiro processo de separação por decanter centrífugo(7), onde é retirada parte da umidade. A água(8), retorna para reservatório(9) de água e a amêndoa e parte da casca moídas(10) é transportada(101 ) para dois ou mais processos de moagem(1 1 ), para reduzir, ao máximo, a granulometria. A amêndoa e parte da casca moídas (10), material vindo do último processo de moagem(1 1 ), é aquecida, por vapor(12), num primeiro tanque de aquecimento(13) com temperatura de 90 a 100°C, com adição de água e com tempo de permanência de 30 a 120 minutos. Em seguida é bombeado(131 ) até um segundo processo de separação(14), por tridecanter, onde será separado o óleo(16) da água(15) e do material sólido(17) das nozes moídas(10). A separação ocorre sem o uso de produtos químicos. A água(15), em forma de líquido do processo de cozimento, é transportada por gravidade de volta para o primeiro tanque de aquecimento(13);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). In 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. It is then pumped (131) to a second separation process (14) by tridecanter, where oil (16) will be separated from water (15) and solid material (17) from ground nuts (10). Separation occurs without the use of chemicals. The liquid-shaped water (15) of the cooking process is gravity conveyed back to the first heating tank (13);
] O óleo(16) retirado no segundo processo de separação(14) vai para os tanques(26) de armazenamento para expedição. O material sólido(17) vai para um segundo tanque de aquecimento(19), onde é novamente aquecido, com adição de água e com temperatura de 90 a 100°C e com tempo de permanência de até 60 minutos. Em seguida, o material sólido(17) é bombeado(20) para um terceiro processo de separação(21 ), por tridecanter centrífugo, com o objetivo de retirar o máximo de óleo possível remanescente do segundo processo de separação(14). O óleo(23) extraído no terceiro processo de separação(21 ) vai para os tanques(26) de armazenamento para expedição. A água(22), por gravidade, volta para o segundo tanque de aquecimento(19). A parte sólida(24) do terceiro processo de separação(21 ) pode passar por um processo de secagem para ser transformada em farinha seca utilizada como ração animal ou como biocombustível, ou ser usada na forma úmida. ] 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 water (22), by gravity, returns to the second heating tank (19). 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.
] O sistema de extração de óleo revelado se caracteriza pela utilização do conceito de separação hidrodinâmica, eliminando sistema de prensagem e separação química existente no atual estado da técnica. Dessa forma, ocorre uma variação nos tipos de equipamentos fundamentais aplicados no sistema revelado em relação aos sistemas disponíveis no atual estado da técnica. Proporciona economia de espaço, pois o sistema revelado utiliza menos equipamentos e é mais rápido com menor tempo de permanência do produto no sistema, gerando uma menor necessidade de área útil industrial. Devido ao fato do sistema revelado ser mais compacto, é esperado uma redução de manutenção dos equipamentos; possui menor necessidade de equipamentos instalados em relação aos métodos físicos (prensagem mecânica), assim como redução da mão de obra de operação e da mão de obra de manutenção. ] Abaixo um quadro comparativo de sistema existente no atual estado da técnica em comparação com o sistema revelado neste relatório: ] 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:
Sistema de Extração de Oleo Sistema de Extração de Oleo de de Palmiste do estado da Palmiste revelado neste relatório técnica Oil Extraction System Palm State Oil Palm Extraction System disclosed in this white paper
1 A noz é armazenada no silo de A noz é transportada do silo de secagem com o intuito de se armazenamento para a moega eliminar a umidade da amêndoa dosadora; 1 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;
e desprender a amêndoa da and shed the almond from
casca; bark;
2 No tambor classificador as As nozes são moídas; 2 In the sorting drum the walnuts are ground;
nozes são classificadas em 3 walnuts are classified in 3
tamanhos (pequeno, média e sizes (small, medium and
grande) para serem large) to be
direcionadas para os directed towards
quebradores (para tamanhos breakers (for sizes
específicos). specific).
3 Este conteúdo será A amêndoa moída com casca é transportado para a mesa de misturada com água em misturador gravidade para separar a casca estático. 3 This content will be The ground almond in shell is transported to the mixing table with water in gravity mixer to separate the static shell.
da amêndoa; ou separado em almond; or separated into
hidroci clone; Observação: O que muda? hydrocyclone; Note: What changes?
Pelo fato das amêndoa serem moídas com a casca, há uma expressiva redução de equipamentos, etapas produtivas e tempo de processamento. Because almonds are ground with the shell, there is a significant reduction in equipment, production steps and processing time.
6 O conteúdo segue para o silo O material resultante é transportado secador de amêndoa para para um hidrociclone. 6 Content goes to the silo The resulting material is transported almond dryer to a hydrocyclone.
reduzir a umidade em até 5%; reduce humidity by up to 5%;
7 O conteúdo é transportado para No hidrociclone ocorre a separação de um dosador na entrada do parte da casca de maior granulometria moinho (onde entra por e da amêndoa com parte de casca de gravidade); menor granulometria. In the hydrocyclone there is the separation of a feeder at the inlet of the part of the highest mill shell (where it enters by and of the almond with gravity shell part); lower particle size.
8 A amêndoa é aquecida com As cascas separadas no hidrociclone vapor indireto com o intuito de são transportadas até as caldeiras. reduzir a umidade; A água com amêndoa e parte da casca moídas resultante passa por um sistema de separação (decanter centrífugo), onde é retirada boa parte da umidade. A amêndoa e parte da casca moída vão para o segundo sistema de moagem e a água retorna para o tanque de mistura. 8 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.
9 Prensagem: prensa a amêndoa Depois de retirada parte da umidade, o para separar o óleo; material passa por dois processos de moagem, para reduzir a granulometria. 9 Pressing: almond pressing After removing some of the moisture, or to separate the oil; material goes through two grinding processes to reduce the particle size.
10 O óleo é homogeneizado no A amêndoa e parte da casca moídas tanque de agitação. vindo do processo de moagem são aquecidas num tanque de aquecimento com água até atingir temperatura em torno de 90 a 100°C, onde permanece por um tempo de 30 a 120 minutos. A mistura é bombeada até um processo de separação por tridecanter centrífugo, onde será separado o óleo da água e sólido sem o uso de químicos. 10 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.
1 1 No outro caminho segue o óleo O óleo retirado no processo, vai para para uma peneira vibratória os tanques de armazenamento para expedição. 1 1 In the other way follows the oil The oil removed in the process goes to a vibrating sieve the storage tanks for dispatch.
12 Por fim, o óleo passa por um O sólido vai para um segundo tanque, sistema de filtragem. onde é novamente aquecido com água, e em seguida passa por um processo de separação por tridecanter centrífugo, com o objetivo de retirar o máximo de óleo possível remanescente. 12 Finally, the oil goes through a solid. The solid goes into a second tank, filtration system. where it is heated again with water, and then goes through a tridecanter separation process centrifuge to remove as much oil as possible.
O óleo é enviado aos tanques O óleo extraído no processo vai para de armazenamento para a os tanques de armazenamento para expedição expedição. A água (líquido do processo de cozimento) volta para o tanque de aquecimento. 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: armazena a amêndoa A parte sólida pode passar um sistema prensada (em forma de farinha); de secagem para ser transformada em ração animal ou ser utilizada como biocombustível, ou ser usada na forma úmida. 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.
Claims
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 |
| CR20190167A CR20190167A (en) | 2017-03-08 | 2017-03-15 | PALMISTE OIL EXTRACTION SYSTEM BY HYDRODYNAMIC PROCESS |
| CN201780067427.5A CN109923196A (en) | 2017-03-08 | 2017-03-15 | By the palm-kernel oil extraction system of hydrodynamic processes |
| PE2019000779A PE20190861A1 (en) | 2017-03-08 | 2017-03-15 | PALMISTE OIL EXTRACTION SYSTEM BY HYDRODYNAMIC PROCESS |
| MX2019004661A MX2019004661A (en) | 2017-03-08 | 2017-03-15 | System for extracting palm kernel oil using a hydrodynamic method. |
| CONC2019/0003408A CO2019003408A2 (en) | 2017-03-08 | 2019-04-05 | Palm kernel oil extraction system by hydrodynamic process |
| PH12019500914A PH12019500914A1 (en) | 2017-03-08 | 2019-04-24 | System for extracting palm kernel oil using a hydrodynamic method |
| ECSENADI201940560A ECSP19040560A (en) | 2017-03-08 | 2019-06-06 | PALMISTE OIL EXTRACTION SYSTEM BY HYDRODYNAMIC PROCESS |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BR102017004632-0A BR102017004632B1 (en) | 2017-03-08 | 2017-03-08 | PALM KERNEL OIL EXTRACTION SYSTEM BY HYDRODYNAMIC PROCESS |
| BRBR1020170046320 | 2017-03-08 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2018161134A1 true WO2018161134A1 (en) | 2018-09-13 |
Family
ID=61965545
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|---|---|---|---|
| PCT/BR2017/050058 Ceased WO2018161134A1 (en) | 2017-03-08 | 2017-03-15 | System for extracting palm kernel oil using a hydrodynamic method |
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| Country | Link |
|---|---|
| CN (1) | CN109923196A (en) |
| BR (1) | BR102017004632B1 (en) |
| CO (1) | CO2019003408A2 (en) |
| CR (1) | CR20190167A (en) |
| EC (1) | ECSP19040560A (en) |
| MX (1) | MX2019004661A (en) |
| MY (1) | MY198305A (en) |
| NI (1) | NI201900035A (en) |
| PH (1) | PH12019500914A1 (en) |
| WO (1) | WO2018161134A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3660135A1 (en) * | 2018-11-30 | 2020-06-03 | Alfa Laval Corporate AB | Method of producing a low-fat product and a system for producing a low-fat product |
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| WO2014035760A1 (en) * | 2012-08-29 | 2014-03-06 | Desmet Ballestra North America, Inc. | Pressed palm fibre solvent extraction |
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| GB401550A (en) * | 1932-08-06 | 1933-11-16 | Krupp Fried Grusonwerk Ag | Process and apparatus for the extraction of oil from oilcontaining fruits |
| FR2750431B1 (en) * | 1996-06-27 | 1998-09-18 | Cooperation Internationale En | PROCESS FOR EXTRACTING PALM OIL AND EXTRACTED OIL |
| EP1991064A1 (en) * | 2006-03-03 | 2008-11-19 | Specialty Protein Producers, Inc. | Methods of separating fat from non-soy plant materials and compositions produced therefrom |
| CN101904367B (en) * | 2010-08-11 | 2012-07-04 | 江西省粮油科学技术研究所 | Method for aqueous extraction of vegetable fat by using low-temperature drying oil mill |
| 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 (en) * | 2013-09-30 | 2015-08-05 | 广西科学院 | The method of tung oil is got in the lixiviate of a kind of ultrasonic assistant water at low temperature |
| MY163847A (en) * | 2015-02-10 | 2017-10-27 | Teng Ye Ngan | A method for treating effluent produced from palm oil milling process |
| CN106244313A (en) * | 2016-08-18 | 2016-12-21 | 贵州石阡佛顶山野生油茶油业有限公司 | A kind of water substitution Oleum Camelliae method for producing |
-
2017
- 2017-03-08 BR BR102017004632-0A patent/BR102017004632B1/en not_active IP Right Cessation
- 2017-03-15 MX MX2019004661A patent/MX2019004661A/en unknown
- 2017-03-15 CN CN201780067427.5A patent/CN109923196A/en active Pending
- 2017-03-15 WO PCT/BR2017/050058 patent/WO2018161134A1/en not_active Ceased
- 2017-03-15 MY MYPI2019001575A patent/MY198305A/en unknown
- 2017-03-15 CR CR20190167A patent/CR20190167A/en unknown
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2019
- 2019-04-05 CO CONC2019/0003408A patent/CO2019003408A2/en unknown
- 2019-04-12 NI NI201900035A patent/NI201900035A/en unknown
- 2019-04-24 PH PH12019500914A patent/PH12019500914A1/en unknown
- 2019-06-06 EC ECSENADI201940560A patent/ECSP19040560A/en unknown
Patent Citations (2)
| 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 (en) * | 2012-08-29 | 2014-03-06 | Desmet Ballestra North America, Inc. | Pressed palm fibre solvent extraction |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3660135A1 (en) * | 2018-11-30 | 2020-06-03 | Alfa Laval Corporate AB | Method of producing a low-fat product and a system for producing a low-fat product |
| WO2020109135A1 (en) * | 2018-11-30 | 2020-06-04 | Alfa Laval Corporate Ab | Method of producing a low-fat product and a system for producing a low-fat product |
| CN113195693A (en) * | 2018-11-30 | 2021-07-30 | 阿法拉伐股份有限公司 | Method for producing a low-fat product and system for producing a low-fat product |
| 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 |
|---|---|
| PH12019500914A1 (en) | 2019-08-05 |
| MX2019004661A (en) | 2019-08-21 |
| NI201900035A (en) | 2019-09-12 |
| MY198305A (en) | 2023-08-22 |
| BR102017004632B1 (en) | 2022-12-27 |
| CR20190167A (en) | 2019-08-16 |
| CN109923196A (en) | 2019-06-21 |
| BR102017004632A2 (en) | 2017-09-19 |
| ECSP19040560A (en) | 2019-06-30 |
| CO2019003408A2 (en) | 2019-04-12 |
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