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公开(公告)号:WO2022008508A1
公开(公告)日:2022-01-13
申请号:PCT/EP2021/068656
申请日:2021-07-06
申请人: HALDOR TOPSØE A/S
IPC分类号: C10G25/00 , B01J20/02 , B01J20/08 , B01J20/28 , B01J20/284 , B01J21/04 , B01J23/28 , B01J23/30 , B01J23/75 , B01J23/755 , B01J35/10
摘要: The invention relates to a porous material comprising alumina, said alumina comprising alpha-alumina, said porous material comprising one or more metals selected from Co, Mo, Ni, W and combinations thereof, and said porous material having a BET-surface area of 1-110 m2/g, a total pore volume of 0.50-0.80 ml/g, as measured by mercury intrusion porosimetry, and a pore size distribution (PSD) with at least 30 vol% of the total pore volume being in pores with a radius ≥ 400 Å, suitably pores with a radius ≥ 500 Å, such as pores with a radius up to 5000 Å. The invention relates also to a process for removing impurities such as phosphorous (P) from a feedstock such as a renewable feed, by contacting said feedstock with a guard bed comprising the above porous material. The invention further relates to a guard bed for a hydrotreatment system comprising the porous material, a hydrotreatment system comprising a guard bed which comprises the porous material and a downstream hydrotreatment section comprising at least one hydrotreatment catalyst, as well as to the use of the porous material as a phosphorus guard in a hydrotreatment process.
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公开(公告)号:WO2021122999A1
公开(公告)日:2021-06-24
申请号:PCT/EP2020/086782
申请日:2020-12-17
申请人: HALDOR TOPSØE A/S
IPC分类号: B01J38/08 , B01J38/62 , B01J38/66 , B01J23/755 , B01J23/75 , B01J23/28 , B01J23/30 , B01J21/04 , B01J23/8993 , B01J23/94 , B01J27/285 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1061 , B01J37/0203 , B01J37/0205 , B01J37/0236 , B01J38/02 , C10G45/60 , C10G47/12
摘要: A method for activating an oxidic fresh hydroprocessing catalyst or the catalytically active material of a spent hydroprocessing catalyst comprising a refractory oxide support and one or more base metals selected from Ni, Co, Mo and W comprises optionally regenerating the catalyst, adjusting an aqueous activating solution, which contains an organic acid, to pH > 3 with an alkaline additive, impregnating the catalytically active material with the pH-adjusted aqueous activating solution, and heat-treating the catalyst at a temperature of 120-450°C.
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