Neste Oyj

Neste Oil Oyj

Fortum Oyj

Marja Tiitta

Ulla Kiiski

Isto Eilos

Jaana Makkonen

Elina Harlin

Jukka Myllyoja

Marina Lindblad

Jukka Koskinen

Väinö Sippola

Antti Pyhälahti

Eveliina Mäkelä

Johan-Fredrik Selin

Markku Kuronen

Sami Toppinen

Jukka Hietala

Virpi Rämö

Vesa Niemi

Kaija Isokoski

Heli Vuori

Ville Paasikallio

Juhani Aittamaa

Mika Kettunen

Kaisa Lamminpää

Maaria Seläntaus

Jouko Nikkonen

Jyrki Hiltunen

Jan Wahlström

Matti Nurminen

Jaana Kanervo

Fredrik Nissfolk

Kari Kulmala

Pirjo Siira

Varpu Markkanen

Vesa-Matti Lehtinen

Kari I Keskinen

Merja Kouva

Anja Leminen

Kalle Lehto

José Luis González Escobedo

Maija Rouhiainen

Emma Sairanen

Marina Linblad

Tapio Salmi

Dmitry Yu Murzin

Marja-Liisa Kärkkäinen

Pasi Hagelberg

Sylvia Albersberger

Helka Turunen

Mohamed Lashdaf

Anna-Mari Illikainen

Narendra Kumar

Heidi Österholm

Jan Wahlstrom

Maaria Selantaus

Heidi Oesterholm

The present invention relates to a method for producing renewable gas D, renewable naphtha E, and renewable jet fuel F or components thereto from a renewable feedstock A, in particular to methods comprising separate hydrodeoxygenation () and hydroisomerization steps () wherein the hydroisomerization is performed in the presence of a metal impregnated ZSM-23 catalyst.

Method for producing renewable gas, renewable naphtha, and renewable jet fuel

The present invention relates to a method for producing renewable aviation fuel D or components thereto from a feed-stock A of biological origin, in particular to methods comprising separate hydrodeoxygenation 20 and hydroisomerization 40 steps wherein the hydroisomerization is performed in the presence of a catalyst comprising a noble metal, a 12-membered ring zeolite with a pore size below 0.7 nm.

Method for producing renewable aviation fuel

A process for hydrotreating recycled or renewable feedstocks with a catalytic microparticle slurry, and a process for manufacturing the catalytic microparticle slurry, are disclosed.

Catalytic hydrotreating of feedstocks

The present invention relates to a method for producing renewable C3 hydrocarbons D and renewable aromatic hydrocarbons E from a renewable feedstock A, in particular to methods comprising hydrodeoxygenation () and catalytic cracking () steps wherein the catalytic cracking is catalysed by a catalyst comprising a zeolite and a support, wherein the zeolite is a 12-membered ring zeolite with a pore size below 0.7 nm.

Method for producing renewable C3 hydrocarbons and renewable aromatic hydrocarbons

The present disclosure provides a versatile process for producing valuable renewable hydrocarbons from triglyceride containing feedstock. The triglyceride containing feedstock is first split to provide a mixture containing fatty acids, glycerol and water, from which a phase separation provides an oily phase, and an aqueous phase. The oily phase containing fatty acids is subjected to fractionation, whereby specific fractions may be refined to products with controlled hydroprocessing. Products may contain paraffinic renewable aviation fuel components, paraffinic renewable base oil, renewable paraffinic diesel fuel components, renewable paraffinic technical fluid, or any combination thereof.

Process for integrated production of renewable fuels and chemicals

An integrated production plant system includes, at one production site at least two plants of different kinds selected from a renewable paraffinic fuel plant to produce renewable paraffinic fuel in a renewable paraffinic fuel process, a renewable fatty acid alkyl ester (FAAE) fuel plant to produce renewable FAAE fuel in a renewable FAAE process, a renewable base oil plant to produce renewable base oil in a renewable base oil process, and a renewable chemical plant to produce renewable chemical in a renewable chemical process. Each of the processes is provided with a respective renewable feed, where the feed of each of the processes originates from a common renewable system feed, and the feed to at least one of the processes is altered for example by directing at least part of the feed of at least one of the processes to another of the processes.

Flexible integrated production plant system and method

The present disclosure relates to methods for producing renewable base oil and other valuable renewable fuel components from a feedstock of biological origin comprising free fatty acids and glycerides. The feedstock is first separated to two or more effluent streams containing a fatty acid fraction and glyceride fraction. The glycerides are hydrolyzed to free fatty acids and glycerol, and the fatty acids thus obtained are recycled to the separating. The fatty acids are then converted to the base oil by ketonisation, hydrodeoxygenation and hydroisomerisation. The glycerol is converted to propanols by selective hydrogenolysis.

Method for producing renewable base oil and renewable fuel components

A diesel fuel composition containing a renewable diesel component and oxymethylene ethers having molecular structure CH3O&#x2014;(CH2O)n-CH3 with n=3-5 (OME3-5). A method for producing a diesel fuel composition and use thereof. Use of OME3-5 to decrease particle emission of renewable diesel fuels is further disclosed.

Diesel fuel composition

The present invention relates to middle distillate fuel blends, in particular renewable diesel fuel blends comprising a mixture of aryl ethers.

Fuel blend comprising a mixture of aryl ethers

The present invention relates to a method using a specific catalyst for upgrading ketoacid to intermediates for fuel and chemical industry, intermediates obtained by the method and to their use.

Upgrading ketoacid

The present invention relates to a method for production of a fuel composition, more specifically a middle distillate fuel composition, and a composition&#x2014;in particular a co feed composition comprising a furanyl containing oligomerisation composition admixed with one or more material component comprising fatty acids or fatty acid derivatives and the use of such composition.

Production of a fuel composition

Disclosed is a method relating to hydrocarbon production by gasification of carbonaceous material, for example, a two-stage gas washing method as a part of gas refining. Disclosed is a method for hydrogen sulfide and carbon dioxide removal from synthesis gas produced by gasification. Disclosed is a use of a combination of two chemical wash approaches. The process can be utilized as a part of biomass to liquid (BTL) process.

Two-stage gas washing method applying sulfide precipitation and alkaline absorption

The invention relates to a method for the manufacture of branched saturated hydrocarbons, said method comprising the steps where a feed comprising olefins having at least 10 carbons is simultaneously hydrogenated and isomerized in the presence of hydrogen at a temperature of 100-400&#xb0; C., under hydrogen partial pressure of 0.01-10 MPa, in the presence of a catalyst comprising a metal selected from the metals of Group VIIIb of the Periodic Table of Elements, a molecular sieve selected from ten member ring molecular sieves, twelve member ring molecular sieves and mesoporous molecular sieves embedded with zeolite, and a carrier, to yield branched saturated hydrocarbons.

Method for the manufacture of branched saturated hydrocarbons

A method for adjusting hydrogen to carbon monoxide ratio of syngas contaminated by sulfur impurities involving a water gas shift (WGS) reaction. In light of the presence of the sulfur impurities, the WGS can be implemented as a sour gas shift. WGS can provide good results by using a non-sulfided catalyst. Conditions can be employed which contribute to further enhanced CO-conversion in the reaction. The hydrocarbons or derivatives thereof obtainable from the method can further be refined and used for production of fuels or lubricants for combustion engines.

Method for adjusting hydrogen to carbon monoxide ratio in synthesis gas

The present invention relates to a method for the deoxygenation of materials of biological origin and particularly to the removal of oxygen from biomass derived organic compounds with carbon monoxide, to yield linear and branched hydrocarbons suitable as biofuels or as blending stocks or components for biofuels, such as gas, gasoline, diesel fuel and aviation fuel, as well as solvents. The method comprises contacting a feedstock with carbon monoxide in the presence of a catalyst comprising a metal selected from a group consisting of ruthenium, manganese, rhodium, rhenium, osmium, iridium, molybdenum, copper, zinc, palladium, platinum and cobalt, in the presence of water, under alkaline conditions at a temperature from 150 to 350&#xb0; C. and under a pressure from 0.1 to 150 bar, to produce hydrocarbons.

Deoxygenation of materials of biological origin

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Porvoo, Finland

Marja Tiitta