摘要:
The invention relates to a process and an apparatus for producing hydrocarbon components in the presence of a hydrodesulphurization catalyst. The components obtained by the process are suitable for use as fuel composition as such or as an additive in fuel compositions, and in cosmetics or pharmaceutical products.
摘要:
The present invention relates to a process for producing mixture of fuel components, which process comprises providing a feed of biological origin; subjecting said feed of biological origin and a hydrogen gas feed to a single step of hydroprocessing in the presence of a catalyst system comprising dewaxing catalyst to form a mixture of fuel components. The present invention relates also to an apparatus for producing a mixture of fuel components from a feed of biological origin. The invention relates also to the use of the fuel components.
摘要:
The present invention relates to a process for catalytically converting material of biological origin into hydrocarbons useful as fuel components. The process includes hydrodeoxygenation and isomerization of the material. The present invention relates also to a reactor and an apparatus suitable for use in the process.
摘要:
The present invention relates to a process for producing mixture of fuel components, which process comprises providing a feed of biological origin; subjecting said feed of biological origin and a hydrogen gas feed to a single step of hydroprocessing in the presence of a catalyst system comprising dewaxing catalyst to form a mixture of fuel components. The present invention relates also to an apparatus for producing a mixture of fuel components from a feed of biological origin. The invention relates also to the use of the fuel components.
摘要:
The invention relates to a process for producing hydrocarbon components, comprising: providing a feedstock comprising tall oil and terpene-based compounds; subjecting the feedstock and a hydrogen gas feed to a hydroprocessing treatment in the presence of a hydroprocessing catalyst to produce hydrocarbon components including n-paraffins, and subjecting the hydrocarbon components including n-paraffins to isomerisation in the presence of a dewaxing catalyst to form a mixture of hydrocarbon components. The invention also relates to an apparatus for implementing the process. The invention further relates to a use of the hydrocarbon components produced by the process as a fuel or as an additive in fuel compositions. The invention also relates to a use of a NiW catalyst on a support selected from Al2O3, zeolite, zeolite-Al2O3, and Al2O3—SiO2 for producing fuel or an additive for fuel compositions from a feedstock comprising tall oil and terpene-based compounds.
摘要翻译:本发明涉及一种生产烃组分的方法,包括:提供包含妥尔油和萜烯类化合物的原料; 在加氢处理催化剂的存在下使原料和氢气进料进行加氢处理以产生包括正链烷烃的烃组分,并在脱蜡催化剂存在下将包含正链烷烃的烃组分进行异构化以形成混合物 的烃组分。 本发明还涉及一种用于实现该过程的装置。 本发明还涉及通过该方法制备的烃组分作为燃料或作为燃料组合物中的添加剂的用途。 本发明还涉及NiW催化剂在选自Al 2 O 3,沸石,沸石-Al 2 O 3和Al 2 O 3 -SiO 2的载体上的用途,用于从包含妥尔油和萜烯类化合物的原料生产燃料或用于燃料组合物的添加剂。
摘要:
The invention relates to a process for producing hydrocarbon components, comprising: providing a feedstock comprising tall oil and terpene-based compounds; subjecting the feedstock and a hydrogen gas feed to a hydroprocessing treatment in the presence of a hydroprocessing catalyst to produce hydrocarbon components including n-paraffins, and subjecting the hydrocarbon components including n-paraffins to isomerisation in the presence of a dewaxing catalyst to form a mixture of hydrocarbon components. The invention also relates to an apparatus for implementing the process. The invention further relates to a use of the hydrocarbon components produced by the process as a fuel or as an additive in fuel compositions. The invention also relates to a use of a NiW catalyst on a support selected from Al2O3, zeolite, zeolite-Al2O3, and Al2O3—SiO2 for producing fuel or an additive for fuel compositions from a feedstock comprising tall oil and terpene-based compounds.
摘要翻译:本发明涉及一种生产烃组分的方法,包括:提供包含妥尔油和萜烯类化合物的原料; 在加氢处理催化剂的存在下使原料和氢气进料进行加氢处理以产生包括正链烷烃的烃组分,并在脱蜡催化剂存在下将包含正链烷烃的烃组分进行异构化以形成混合物 的烃组分。 本发明还涉及一种用于实现该过程的装置。 本发明还涉及通过该方法制备的烃组分作为燃料或作为燃料组合物中的添加剂的用途。 本发明还涉及NiW催化剂在选自Al 2 O 3,沸石,沸石-Al 2 O 3和Al 2 O 3 -SiO 2的载体上的用途,用于从包含妥尔油和萜烯类化合物的原料生产燃料或用于燃料组合物的添加剂。
摘要:
The invention relates to a process and an apparatus for producing hydrocarbon components in the presence of a hydrodesulphurization catalyst. The components obtained by the process are suitable for use as fuel composition as such or as an additive in fuel compositions, and in cosmetics or pharmaceutical products.
摘要:
The invention relates to producing liquid hydro carbonaceous product (1) from solid biomass (2). In the invention solid biomass (2) is gasified in a gasifier (6) to produce raw synthesis gas (3). The raw synthesis gas (3) is conditioned to purify the raw synthesis gas (3) to obtain purified synthesis gas (4), the conditioning comprising lowering the temperature of the raw synthesis gas (3) in a cooler (19) producing saturated steam (51). Then the purified gas (4) is subjected to a Fischer-Tropsch synthesis in a Fischer-Tropsch reactor (5) to produce liquid hydro carbonaceous product (1). In the invention the saturated steam (51) produced by the cooler (19) is further superheated in a superheating boiler (50) for producing superheated steam (52).
摘要:
The invention relates to a method and apparatus for producing liquid hydro carbonaceous product (1) such as biofuel from solid biomass (2). The method comprises a gasifying step for gasifying solid biomass (2) in a gasifier (6) to produce raw synthesis gas (3), conditioning of the raw synthesis gas (3) to purify the raw synthesis gas (3) to obtain purified synthesis gas (4) having a molar ratio of hydrogen to carbon monoxide between 2.5 to 1 and 0.5 to 1, preferably to between 2.1 to 1 and 1.8 to 1, more preferably about 2 to 1, and subjecting purified synthesis gas (4) to a Fischer-Tropsch synthesis in a Fischer-Tropsch reactor (5) to produce liquid hydro carbonaceous product (1).
摘要:
A metathesis process of the conversion of olefines, in which at least one olefine is brought into contact with a solid catalyst system comprising on a solid silica carrier 0.1-40% by weight of a tungsten compound under reaction conditions such that the catalyst system converts the olefine into olefines having a different molecular weight. In the process a magnesium oxide or titanium oxide containing co-gel prepared by means of a co-gelling system is used as the silica carrier.