Abstract:
A method of deoxygenation of tall oil as well as methods for the production of aliphatic hydrocarbons and polymerizable monomers from tall oil. Sulphurous crude tall oil together with hydrogen gas is fed into a reactor comprising a catalyst bed. The oil is catalytically deoxygenated by hydrogen in the bed by use of a sulfided metal catalyst, e.g. a NiMoS catalyst. The flow exiting the reactor is cooled down and a hydrocarbon-bearing liquid phase is separated from a gas phase, followed by subjecting the liquid phase to distillation for removal of useless aromatic hydrocarbons and then to steam cracking to form a product containing olefins such as ethylene or propylene. By regulation of the deoxygenation temperature to be at least 270° C. but less than 360° C. the yield is rich in linear and cyclic aliphates that usefully turn to olefins in the steam cracking, while formation of napthalenes is reduced.
Abstract:
The present invention relates to a method of deoxygenating tall oil pitch, yielding aliphatic and aromatic hydrocarbons. The invention even comprises turning the aliphates into polymerizable olefins by steam cracking, and turning the aromates into polymerizable terephthalic acid by oxygenation and, as necessary, rearrangement. The monomers can be used for the production of polymers of partially or completely biologic origin. According to the invention, tall oil pitch is first heated to turn it into liquid, which is then fed into a catalyst bed and catalytically deoxygenated with hydrogen. The deoxygenation catalyst is preferably a Ni—Mo catalyst and, in addition, a cracking catalyst can be used, such as an acidic zeolite catalyst. The deoxygenated product stream is cooled down so as to obtain a liquid, which is distilled for separation of the aliphatic and aromatic hydrocarbons for use in the production of the respective monomers and finally polymers.
Abstract:
The present invention relates to a method of deoxygenating tall oil pitch, yielding aliphatic and aromatic hydrocarbons. The invention even comprises turning the aliphates into polymerizable olefins by steam cracking, and turning the aromates into polymerizable terephthalic acid by oxygenation and, as necessary, rearrangement. The monomers can be used for the production of polymers of partially or completely biologic origin. According to the invention, tall oil pitch is first heated to turn it into liquid, which is then fed into a catalyst bed and catalytically deoxygenated with hydrogen. The deoxygenation catalyst is preferably a Ni-Mo catalyst and, in addition, a cracking catalyst can be used, such as an acidic zeolite catalyst. The deoxygenated product stream is cooled down so as to obtain a liquid, which is distilled for separation of the aliphatic and aromatic hydrocarbons for use in the production of the respective monomers and finally polymers.
Abstract:
The present invention relates to a method of deoxygenating tall oil pitch, yielding aliphatic and aromatic hydrocarbons. The invention even comprises turning the aliphates into polymerizable olefins by steam cracking, and turning the aromates into polymerizable terephthalic acid by oxygenation and, as necessary, rearrangement. The monomers can be used for the production of polymers of partially or completely biologic origin. According to the invention, tall oil pitch is first heated to turn it into liquid, which is then fed into a catalyst bed and catalytically deoxygenated with hydrogen. The deoxygenation catalyst is preferably a NiMo catalyst and, in addition, a cracking catalyst can be used, such as an acidic zeolite catalyst. The deoxygenated product stream is cooled down so as to obtain a liquid, which is distilled for separation of the aliphatic and aromatic hydrocarbons for use in the production of the respective monomers and finally polymers.
Abstract:
The invention relates to a method of deoxygenation of tall oil as well as methods for the production of aliphatic hydrocarbons and polymerizable monomers from tall oil. Sulphurous crude tall oil (5) together with hydrogen gas (6) is fed into a reactor (1) comprising a catalyst bed (2, 3). The oil is catalytically deoxygenated by hydrogen in the bed by use of a sulfided metal catalyst, e.g. a Ni-MoS catalyst. The flow exiting the reactor is cooled down and a hydrocarbon-bearing liquid phase (10) is separated from a gas phase (18), followed by subjecting the liquid phase to distillation (14) for removal of useless aromatic hydrocarbons and then to steam cracking (4) to form a product containing olefins such as ethylene or propylene. By regulation of the deoxygenation temperature to be at least 270°C but less than 360°C the yield is rich in linear and cyclic aliphates that usefully turn to olefins in the steam cracking, while formation of napthalenes is reduced.
Abstract:
SE DESCRIBE UN MÉTODO PARA PRODUCIR MONÓMEROS OLEFÍRTICOS PARA LA PRODUCCIÓN DE UN POLÍMERO, QUE COMPRENDE LAS SIGUIENTES ETAPAS: - SE INTRODUCE BIOACEITE, CON UN CONTENIDO DE 95% A 98% EN PESO DE ÁCIDOS GRASOS DE ACEITE DE RESIRIA Y 2% A 5% EN PESO DE ÁCIDOS RESINOSOS DE ACEITE DE RESMA, E HIDRÓGENO GASEOSO EN EL LECHO DE CATALIZADOR (7); - EL ACEITE SE DESOXIGENA EN FORMA CATALÍTICA EN EL LECHO MEDIANTE LA APLICACIÓN DE HIDRÓGENO (7); - EL FLUJO DE SALIDA DEL LECHO (7) SE ENFRÍA Y DIVIDE EN UNA FASE LÍQUIDA QUE CONTIENE HIDROCARBUROS (10) Y UNA FASE GASEOSA; Y - EL LÍQUIDO QUE CONTIENE HIDROCARBUROS (13) SE SOMETE A UNA DESINTEGRACIÓN EN VAPOR (4) A FIN DE OBTENER UN PRODUCTO QUE CONTENGA OLEFINAS POLIMERIZANTES.
Abstract:
The invention relates to a method of producing olefinic monomers for the production of a polymer. The invention particularly relates to the production of tall oil-based biopolymers, such as polyolefins. In the stages of the method bio oil, with a content of over 50% of fatty acids of tall oil and no more than 25% of resin acids of tall oil, and hydrogen gas are fed into a catalyst bed (7); the oil is catalytically deoxygenated in the bed by hydrogen; the flow exiting the bed is cooled down and divided into a hydrocarbon-bearing liquid phase (10) and a gas phase; and the hydrocarbon-bearing liquid (13) is subjected to steam cracking (4) to provide a product containing polymerizing olefins. The deoxygenation in the bed can be followed by a catalytic cracking or, with a suitable catalyst, the deoxygenation and cracking can be simultaneous. The separated hydrogen-bearing gas phase can be circulated in the process.
Abstract:
The invention relates to a method of deoxygenation of tall oil as well as methods for the production of aliphatic hydrocarbons and polymerizable monomers from tall oil. Sulphurous crude tall oil (5) together with hydrogen gas (6) is fed into a reactor (1) comprising a catalyst bed (2, 3). The oil is catalytically deoxygenated by hydrogen in the bed by use of a sulfided metal catalyst, e.g. a Ni-MoS catalyst. The flow exiting the reactor is cooled down and a hydrocarbon-bearing liquid phase (10) is separated from a gas phase (18), followed by subjecting the liquid phase to distillation (14) for removal of useless aromatic hydrocarbons and then to steam cracking (4) to form a product containing olefins such as ethylene or propylene. By regulation of the deoxygenation temperature to be at least 270°C but less than 360°C the yield is rich in linear and cyclic aliphates that usefully turn to olefins in the steam cracking, while formation of napthalenes is reduced.
Abstract:
métodos de desoxigenação de óleo de tall e produção de monómeros polimerizáveis a partir deste a invenção refere-se a um método de desoxigenação de óleo de tal, bem como a métodos para a produção de hidrocarbonetos alifáticos e monómeros polimerizáveis a partir de óleo de tall. óleo de tall bruto sulfuroso (5) juntamente com gás hidrogênio (6) é alimentado a um reator (1) compreendendo um leito catalisador (2, 3). 0 óleo é desoxigenado cataliticamente por hidrogênio no leito pelo uso de um catalisador metálico sulfetado, por exemplo, um catalisador de nimos. 0 fluxo que sai do reator é resfriado e uma fase líquida contendo hidrocarboneto (10) é separada de uma fase gasosa (18), a seguir a fase líquida é submetida a destilação (14) para a remoção de hidrocarbonetos aromáticos inúteis e então a craqueamento por vapor (4) para formar um produto contendo olefinas tais 15 como etileno ou propileno. pela regulação da temperatura de desoxigenação para pelo menos 270°c, mas abaixo de 360°c, o produto é rico em hidrocarbonetos alifáticos lineares ou cíclicos que de maneira útil se convertem em olefinas no craqueamento por vapor, enquanto que a formação de naftalenos é reduzida.