Patents by Inventor Christopher Roosen
Christopher Roosen has filed for patents to protect the following inventions. This listing includes patent applications that are pending as well as patents that have already been granted by the United States Patent and Trademark Office (USPTO).
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Patent number: 12264129Abstract: The present invention relates to a process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; (f) performing a separation operation to obtain different streams of chemical products comprising ethylene, propylene, isobutene, 1-butene, 2-butene, 1,2-butadiene, 1,3-butadiene, benzene, styrene, toluene, ethylbenzene and xylenes; wherein in step (d): ? the coil outlet temperature is ?800 and ?870° C., preferably ?805 and ?835° C.Type: GrantFiled: July 15, 2021Date of Patent: April 1, 2025Assignee: SABIC GLOBAL TECHNOLOGIES B.V.Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Patent number: 12215188Abstract: Process for the production of polycarbonates comprising: providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; supplying a feed C comprising a fraction of the hydrocarbon stream A to a thermal cracker furnace comprising cracking coil(s); thermally cracking in the presence of steam to obtain a cracked hydrocarbon stream D; separating a product stream E comprising propylene and a product stream F comprising benzene from the cracked hydrocarbon stream D; performing a reaction and one or more separation step to obtain a product stream G comprising phenol; supplying the product stream G and acetone to a reactor and performing a reaction and one or more separation step to obtain a product stream H comprising bisphenol-A; and supplying the product stream H with phosgene or diphenyl carbonate to a reactor and performing a polymerisation reaction to obtain a polycarbonate.Type: GrantFiled: July 15, 2021Date of Patent: February 4, 2025Assignee: SABIC GLOBAL TECHNOLOGIES B.V.Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20240424424Abstract: Systems and methods to enhance vaporization of a hydrocarbon feed may include an evaporator positioned to receive a hydrocarbon feed and partially evaporate the hydrocarbon feed to provide a gaseous hydrocarbon portion and a liquid hydrocarbon portion. A first mixing unit may be positioned to receive the gaseous hydrocarbon portion and dilution steam and provide a hydrocarbon-steam mixture. A heater may be positioned to receive the hydrocarbon-steam mixture to provide a heated hydrocarbon-steam mixture. A second mixing unit may be positioned to receive the liquid hydrocarbon portion and the heated hydrocarbon-steam mixture STEAM and to evaporate at least a portion of the liquid hydrocarbon portion via energy associated with the heated hydrocarbon-steam mixture to provide one or more of an evaporated hydrocarbon portion or a heated liquid hydrocarbon portion.Type: ApplicationFiled: June 27, 2022Publication date: December 26, 2024Inventors: Christoph ROOSEN, Sabriye FREDRIKSSON, Arno Johannes Maria OPRINS, Thomas DIJKMANS
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Patent number: 12152001Abstract: Process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; and (f) performing a separation operation to obtain different streams comprising isobutene, 1-butene, 2-butene, 1,2-butediene and 1,3-butadiene; wherein in step (d): •the coil outlet temperature is ?800 and ?850° C.; and•the weight ratio of steam to feed C is >0.3 and <0.8.Type: GrantFiled: July 15, 2021Date of Patent: November 26, 2024Assignee: SABIC GLOBAL TECHNOLOGIES B.V.Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20240317939Abstract: Methods for producing a compound of Formula I, Formula I, wherein R1 and R2 are independently a i) linear or branched or cyclic, ii) saturated or unsaturated, and iii) substituted or unsubstituted hydrocarbon group comprising 8 to 20 carbon atoms; R3 is a hydrocarbon group; n is an integer from 2 to 5, m is an integer from 30 to 70, and L is a linker. The method includes: a) contacting a fatty acid having a chemical formula of R1—COOH and a primary amine having a chemical formula of R2—NH2 to form an amide having a chemical formula of R1—C(O)—NH—R2; b) contacting the amide with a reducing agent to form a secondary amine having a chemical formula of R1—CH2—NH—R2; and c) contacting the secondary amine with a polyolefin-glycol compound to form the compound of Formula I. Intermediates produced in the method, salts of compound of Formula I and of intermediates.Type: ApplicationFiled: January 12, 2022Publication date: September 26, 2024Inventors: Adam Ross Brown, Shane Allen Eisenbeis, Aran Kathleen Hubbell, Ruizhi Li, Giselle Padilla Reyes, Philipp Christopher Roosen
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Patent number: 12024683Abstract: A process for the production of ethylene-based polymers from waste plastics feedstocks includes the steps in this order of: providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; providing a hydrocarbon stream B; supplying a feed C including a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace having cracking coil(s); performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; supplying the cracked hydrocarbon stream D to a separation unit to obtain a product stream E containing ethylene; supplying the product stream E to a polymerisation reactor; and performing a polymerisation reaction to obtain an ethylene-based polymer; wherein in step (d): the coil outlet temperature is ?800 and ?870° C.; and the weight ratio of steam to feed C is >0.3 and <0.8.Type: GrantFiled: January 24, 2020Date of Patent: July 2, 2024Assignee: SABIC GLOBAL TECHNOLOGIES B.V.Inventors: Anthoni Van Zijl, Nicolas Goyheneix, Lara Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20240076561Abstract: A system and a method for steam cracking hydrocarbons are disclosed. The system includes a steam cracking system comprising a first steam cracking furnace and a second steam cracking furnace. A hydrocarbon feed stream is fed into a convection section of a first steam cracking furnace. The preheated feed stream is mixed with steam and then separated into a light vapor stream and a heavy stream in a vapor-liquid separation unit. The light vapor stream is further steam cracked in a radiant section of the first steam cracking furnace. The heavy stream is further heated and steam cracked in the second steam cracking furnace.Type: ApplicationFiled: November 22, 2021Publication date: March 7, 2024Inventors: Thomas DIJKMANS, Safa FARAJZADEH BIBALAN, Johannes Maria MAAS, Gerardus Theodorus Cornelis KWAKKENBOS, Christoph ROOSEN, Philip Roydon EDWARDS
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Patent number: 11879102Abstract: The present invention relates to a process for the production of ethylene-based polymers from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and optionally a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising ethylene; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an ethylene-based polymer; wherein in step (d): ? · the coil outleType: GrantFiled: January 24, 2020Date of Patent: January 23, 2024Assignee: SABIC GLOBAL TECHNOLOGIES B.V.Inventors: Anthoni Van Zijl, Nicolas Goyheneix, Lara Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20230323213Abstract: Process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps: (a) providing a hydrocarbon stream A obtained by hydrotreatment of pyrolysis oil produced from a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and optionally a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; and (f) performing a separation operation to obtain different streams comprising isobutene, 1-butene, 2-butene, 1,2-butediene and 1,3-butadiene; wherein in step (d): • the coil outlet temperature is ? 800 and ? 850° C.; and • the weight ratio of steam to feed C is > 0.3 and < 0.Type: ApplicationFiled: July 15, 2021Publication date: October 12, 2023Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20230295061Abstract: The present invention relates to a process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; (f) performing a separation operation to obtain different streams of chemical products comprising ethylene, propylene, isobutene, 1-butene, 2-butene, 1,2-butadiene, 1,3-butadiene, benzene, styrene, toluene, ethylbenzene and xylenes; wherein in step (d): ? the coil outlet temperature is ?800 and ?870° C., preferably ?805 and ?835° C.Type: ApplicationFiled: July 15, 2021Publication date: September 21, 2023Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20230287175Abstract: Process for the production of polycarbonates comprising: providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of a hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); thermally cracking in the presence of steam to obtain a cracked hydrocarbon stream D; separating a product stream E comprising propylene and a product stream F comprising benzene from the cracked hydrocarbon stream D; performing a reaction and one or more separation step to obtain a product stream G comprising phenol; supplying the product stream G and acetone to a reactor and performing a reaction and one or more separation step to obtain a product stream H comprising bisphenol-A; and supplying the product stream H with phosgene or diphenyl carbonate to a reactor and performing a polymerisation reaction to obtain a polycarbonate.Type: ApplicationFiled: July 15, 2021Publication date: September 14, 2023Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20230279179Abstract: Process for the production of polycarbonates comprising providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; supplying a feed C comprising a fraction of the hydrocarbon stream A to a thermal cracker furnace comprising cracking coil(s); thermally cracking in the presence of steam to obtain a cracked hydrocarbon stream D; separating a product stream E comprising propylene and a product stream F comprising benzene from the cracked hydrocarbon stream D; performing a reaction and one or more separation step to obtain a product stream G comprising phenol; supplying the product stream G and acetone to a reactor and performing a reaction and one or more separation step to obtain a product stream H comprising bisphenol-A; and supplying the product stream H with phosgene or diphenyl carbonate to a reactor and performing a polymerisation reaction to obtain a polycarbonate.Type: ApplicationFiled: July 15, 2021Publication date: September 7, 2023Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20230272286Abstract: The present invention relates to a process for the production of aromatics from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; (f) performing a separation operation to obtain different streams comprising benzene, toluene, styrene, ethylbenzene and xylenes; wherein in step (d): ? the coil outlet temperature is ?800 and ?80° C., preferably ?830 and ?870° C.; 7 and ? the weight ratio of steam to feed C is >0.3 and <0.8, preferably >0.3 and <0.5.Type: ApplicationFiled: July 15, 2021Publication date: August 31, 2023Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20230272287Abstract: The present invention relates to a process for the production of aromatics from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by hydrotreatment of pyrolysis oil produced from a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and optionally a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; (f) performing a separation operation to obtain different streams comprising benzene, toluene, styrene, ethylbenzene and xylenes; wherein in step (d): ? the coil outlet temperature is ?800 and ?850° C., preferably ?805 and ?835° C.; and ? the weight ratio of steam to feed C is >0.3 and <0.8, preferably >0.3 and <0.5.Type: ApplicationFiled: July 15, 2021Publication date: August 31, 2023Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20230265351Abstract: A process for the production of polymers from waste plastics feedstocks includes: providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; optionally providing a hydrocarbon stream B; supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; supplying the cracked hydrocarbon stream D to a separation unit; performing a separation operation in the separation unit to obtain a product stream E comprising a monomer; supplying the product stream E to a polymerisation reactor; and performing a polymerisation reaction to obtain an polymer. The process allows for optimisation of the quantity of waste plastic material that finds its way back into a polymer that is produced as outcome of the process.Type: ApplicationFiled: May 2, 2023Publication date: August 24, 2023Inventors: Anthoni VAN ZIJL, Nicolas GOYHENEIX, Lara GALAN-SANCHEZ, Christoph ROOSEN, Johan PASTWA, Safa FARAJZADEH BIBALAN
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Publication number: 20230257323Abstract: Process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; and (f) performing a separation operation to obtain different streams comprising isobutene, 1-butene, 2-butene, 1,2-butediene and 1,3-butadiene; wherein in step (d): • the coil outlet temperature is ? 800 and ? 850° C. and • the weight ratio of steam to feed C is > 0.3 and < 0.8.Type: ApplicationFiled: July 15, 2021Publication date: August 17, 2023Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Patent number: 11685867Abstract: The present invention relates to a process for the production of polymers from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising a monomer; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an polymer.Type: GrantFiled: January 24, 2020Date of Patent: June 27, 2023Assignee: SABIC GLOBAL TECHNOLOGIES B.V.Inventors: Anthoni Van Zijl, Nicolas Goyheneix, Lara Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20230183579Abstract: The present invention relates to a process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by hydrotreatment of pyrolysis oil produced from a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and optionally a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; (f) performing a separation operation to obtain different streams of chemical products comprising ethylene, propylene, isobutene, 1-butene, 2-butene, 1,2-butadiene, 1,3-butadiene, benzene, styrene, toluene, ethylbenzene and xylenes; wherein in step (d): the coil outlet temperature is >800 and <870° C.Type: ApplicationFiled: July 15, 2021Publication date: June 15, 2023Inventors: Anthoni Wouter Zijl Van, Nicolas Goyheneix, Lara Maria Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Patent number: 11667854Abstract: The present invention relates to a process for the production of propylene-based polymers from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising propylene; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an propylene-based polymer; wherein in step (d): •? the coil outlet temperature is 2:: 800 and:::; 850° C.Type: GrantFiled: January 24, 2020Date of Patent: June 6, 2023Assignee: SABIC GLOBAL TECHNOLOGIES B.V.Inventors: Anthoni Van Zijl, Nicolas Goyheneix, Lara Galan-Sanchez, Christoph Roosen, Johan Pastwa, Safa Farajzadeh Bibalan
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Publication number: 20220135889Abstract: The present invention relates to a process for the production of ethylene-based polymers from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and optionally a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising ethylene; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an ethylene-based polymer; wherein in step (d): • ? the coil outleType: ApplicationFiled: January 24, 2020Publication date: May 5, 2022Inventors: Anthoni VAN ZIJL, Nicolas GOYHENEIX, Lara GALAN-SANCHEZ, Christoph ROOSEN, Johan PASTWA, Safa FARAJZADEH BIBALAN