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公开(公告)号:US11473018B2
公开(公告)日:2022-10-18
申请号:US17015639
申请日:2020-09-09
Applicant: NESTE OYJ
Inventor: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Gronqvist
IPC: C10G3/00 , C10G45/02 , C07C5/22 , C10G45/58 , C10L1/08 , C10G45/62 , C10G45/64 , C10G65/04 , C07C5/27 , C07C1/24 , C07C5/03 , C07C7/10 , C07C7/12 , C07C7/13
Abstract: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
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公开(公告)号:US10550332B2
公开(公告)日:2020-02-04
申请号:US16039210
申请日:2018-07-18
Applicant: NESTE OYJ
Inventor: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Gronqvist
IPC: C10G3/00 , C07C5/03 , C10L1/08 , C10G45/62 , C10G45/64 , C10G45/58 , C10G65/04 , C10G45/02 , C07C1/24 , C07C5/27 , C07C7/10 , C07C7/12 , C07C7/13
Abstract: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
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公开(公告)号:US10059887B2
公开(公告)日:2018-08-28
申请号:US15428080
申请日:2017-02-08
Applicant: Neste Oyj
Inventor: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Gronqvist
CPC classification number: C10G3/50 , C07C1/24 , C07C5/03 , C07C5/2775 , C07C7/10 , C07C7/12 , C07C7/13 , C07C2529/076 , C10G3/46 , C10G3/47 , C10G45/02 , C10G45/58 , C10G45/62 , C10G45/64 , C10G65/043 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/205 , C10G2300/207 , C10G2300/4006 , C10G2300/4081 , C10G2300/802 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
Abstract: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
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公开(公告)号:US12203035B2
公开(公告)日:2025-01-21
申请号:US17930148
申请日:2022-09-07
Applicant: NESTE OYJ
Inventor: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Gronqvist
IPC: C10G3/00 , C07C1/24 , C07C5/03 , C07C5/22 , C07C5/27 , C07C7/10 , C07C7/12 , C07C7/13 , C10G45/02 , C10G45/58 , C10G45/62 , C10G45/64 , C10G65/04 , C10L1/08
Abstract: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
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公开(公告)号:US10800976B2
公开(公告)日:2020-10-13
申请号:US16715871
申请日:2019-12-16
Applicant: NESTE OYJ
Inventor: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Gronqvist
IPC: C10G3/00 , C10G45/58 , C07C5/22 , C10L1/08 , C10G45/62 , C10G45/64 , C10G65/04 , C07C5/27 , C10G45/02 , C07C1/24 , C07C5/03 , C07C7/10 , C07C7/12 , C07C7/13
Abstract: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
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