公开(公告)号：US20250002796A1

公开(公告)日：2025-01-02

申请号：US18704642

申请日：2022-10-26

Applicant: BASF SE

Inventor： Armin LANGE DE OLIVEIRA ,  Gisela HIEBER ,  Oliver PILARSKI ,  Lisa LOEBNITZ ,  Daniel KOEPKE ,  Julian MEYER-KIRSCHNER ,  Christian MUELLER ,  Monica HAAG ,  Michael SCHREIBER ,  Mathias FEYEN ,  Artem D. VITYUK ,  Lukasz KARWACKI ,  Bernard REESINK

IPC: C10G65/08 ,  C10G65/06

Abstract: The present invention relates to a process for purifying a pyrolysis oil comprising providing a stream S0 comprising a pyrolysis oil, the pyrolysis oil comprising one or more halogenated organic compounds and one or more organic compounds comprising conjugated double bonds; subjecting the stream S0 to hydrogenation in at least one reaction zone Z1 containing a heterogeneous hydrogenation catalyst, obtaining a stream S1 being depleted, compared to S0, in the one or more organic compounds comprising conjugated double bonds; subjecting the stream S1 to dehalogenation in at least one dehalogenation zone Z2 down-stream of Z1, obtaining a stream S2 being depleted, compared to S1, in the one or more halogenated organic compounds.

公开(公告)号：US20190198206A1

公开(公告)日：2019-06-27

申请号：US16328912

申请日：2017-08-31

Applicant: BASF SE

Inventor： Johan TER MAAT ,  Sumohan MISRA ,  David VAN ASTEN ,  Bernard REESINK ,  Wilfried HERMES ,  Michael ZEILINGER ,  Fabian SEELER ,  Kerstin SCHIERLE-ARNDT ,  Ekkehard BRUECK ,  Van Thang NGUYEN

IPC: H01F1/01 ,  C22C30/00 ,  F25B21/00

CPC classification number: H01F1/015 ,  C22C30/00 ,  C22C2202/02 ,  F25B21/00 ,  F25B2321/002 ,  H01F41/00 ,  Y02B30/66

Abstract: Described are a kit comprising at least two magnetocaloric materials having identical stoichiometry but different Curie temperature, a magnetocaloric regenerator comprising at least two magnetocaloric materials having identical stoichiometry but different Curie temperature and a process for producing at least two magnetocaloric materials having identical stoichiometry but different Curie temperature.

公开(公告)号：US20200016584A1

公开(公告)日：2020-01-16

申请号：US16464998

申请日：2017-11-29

Applicant: BASF SE

Inventor： Esther GROENEVELD ,  Peter BERBEN ,  Bernard REESINK

IPC: B01J35/06 ,  B01J23/755 ,  B01J35/04 ,  B01J35/10 ,  B01J37/03 ,  B29C64/106 ,  B29C64/165

Abstract: A three-dimensionally structured porous catalyst monolith of stacked catalyst fibers with a fiber diameter of less than 1 mm made from one or more continuous fibers or stacked individual fibers, wherein the stacked catalyst fibers are arranged in a regular, recurring stacking pattern of fiber layers to form the three-dimensionally structured monolith, and wherein in each of the stacked fiber layers at least 50 wt % of the fibers are arranged parallel to each other and spatially separated from each other, or in a cobweb pattern, and wherein the side crushing strength of the monolith is at least 60 N.

公开(公告)号：US20190381491A1

公开(公告)日：2019-12-19

申请号：US16465019

申请日：2017-11-29

Applicant: BASF SE

Inventor： Esther GROENEVELD ,  Peter BERBEN ,  Bernard REESINK

IPC: B01J37/03 ,  B01J35/04 ,  B01J35/06 ,  B01J37/00 ,  B01J23/755 ,  B01J21/08 ,  B01J35/00 ,  B01J35/02 ,  B01J37/02 ,  B01J37/18 ,  B29C64/165 ,  B33Y10/00 ,  B33Y70/00 ,  B33Y80/00

Abstract: A method for producing a three-dimensional porous catalyst monolith of stacked catalyst fibers, comprising the following steps: a) Preparing a suspension paste in a liquid diluent of metal, metal alloy and/or metal oxide particles of catalytically active metal or metal alloy in which the metals, metal alloy and metal oxide particles can be supported on or mixed with inorganic oxide catalyst support particles, and which suspension can furthermore comprise a binder material, all particles in the suspension having an average particle size in the range of from 0.5 to 500 μm, b) extruding the paste of step a) through one or more nozzles preferably having a maximum diameter of less than 5 mm, more preferably less than 1 mm to form fibers, and depositing the extruded fibers to form a three-dimensional porous catalyst monolith precursor, c) drying the porous catalyst monolith precursor to remove the liquid diluent, d) if necessary, reducing the metal oxide(s) in the porous catalyst monolith precursor to form the catalytically active metal or metal alloy, wherein no temperature treatment of the porous catalyst monolith precursor or porous catalyst monolith at temperatures above 1000° C. is performed.