公开(公告)号：US20150065764A1

公开(公告)日：2015-03-05

申请号：US14383914

申请日：2013-02-26

Applicant: IFP ENERGIES NOUVELLES

Inventor： Antoine Daudin ,  Alain Quignard ,  Olivier Thinon

IPC: C10G65/04 ,  C10G1/00 ,  C10G65/12

CPC classification number: C10G65/043 ,  B01J21/04 ,  B01J21/18 ,  B01J23/866 ,  B01J23/883 ,  B01J37/0009 ,  B01J37/20 ,  C08H8/00 ,  C10G1/002 ,  C10G3/46 ,  C10G3/48 ,  C10G3/50 ,  C10G45/00 ,  C10G47/00 ,  C10G65/12 ,  C10G2300/4081 ,  Y02P30/20

Abstract: A process for the production of hydrocarbon products from a feed comprising at least one non-pre-treated bio-oil, comprising a first step for hydroreforming in the presence of hydrogen and a hydroreforming catalyst, used alone or as a mixture, to obtain at least one liquid effluent comprising at least one aqueous phase and at least one organic phase, a second step in which at least a portion of the organic phase of the effluent obtained from the first hydroreforming step is recycled to the first hydroreforming step with a recycle ratio equal to the ratio of the mass flow rate of said organic phase to the mass flow rate of the non-pre-treated bio-oil in the range 0.05 to 2 and in which the hydrocarbon effluent obtained from the hydrotreatment and/or hydrocracking step is not recycled to said first hydroreforming step.

Abstract translation: 一种从含有至少一种未经预处理的生物油的原料生产烃产物的方法，其包括在氢气和氢化反应形成催化剂存在下进行氢化反应的第一步骤，单独或混合使用，以获得 至少一种液体流出液，其包含至少一个水相和至少一个有机相，第二步是将从第一加氢步骤获得的流出物的有机相的至少一部分的至少一部分循环至第一加氢步骤，再循环比 等于所述有机相的质量流量与非预处理生物油的质量流量的比例在0.05至2的范围内，并且其中从加氢处理和/或加氢裂化步骤获得的烃流出物为 不回收到所述第一加氢步骤。

公开(公告)号：US09163180B2

公开(公告)日：2015-10-20

申请号：US13706905

申请日：2012-12-06

Applicant: IFP Energies nouvelles

Inventor： Pierre Marion ,  Alain Quignard ,  Wilfried Weiss

IPC: C10G1/06 ,  C10G2/00 ,  C10G1/00 ,  C10G45/64 ,  C10G47/16 ,  C10G47/20 ,  C10K3/02 ,  C10G65/14 ,  C10G1/08 ,  C01B3/36 ,  C25B1/04 ,  C10J3/00 ,  C10K1/00 ,  C10K3/06

CPC classification number: C10G2/332 ,  C01B3/36 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0415 ,  C01B2203/0475 ,  C01B2203/062 ,  C10G1/002 ,  C10G1/065 ,  C10G1/08 ,  C10G2/32 ,  C10G45/64 ,  C10G47/16 ,  C10G47/20 ,  C10G65/14 ,  C10G2300/1011 ,  C10G2300/1022 ,  C10G2300/4043 ,  C10G2400/02 ,  C10G2400/04 ,  C10J3/00 ,  C10J2300/093 ,  C10J2300/0989 ,  C10J2300/1618 ,  C10J2300/1659 ,  C10J2300/1671 ,  C10J2300/1684 ,  C10J2300/1846 ,  C10K1/005 ,  C10K3/026 ,  C10K3/06 ,  C25B1/04 ,  Y02E50/32 ,  Y02E60/366 ,  Y02P20/133 ,  Y02P20/134 ,  Y02P20/145 ,  Y02P20/146 ,  Y02P30/10 ,  Y02P30/20

Abstract: A process for the conversion of carbon-based material to fuel bases by a hybrid route combining direct ebullent bed liquefaction and indirect liquefaction by gasification followed by a Fischer-Tropsch synthesis, including a stage of production of hydrogen resulting from non-fossil resources and a reverse water gas reaction stage. This process makes it possible to limit emissions of greenhouse gases.

Abstract translation: 通过将直接沸腾床液化和间接液化的混合途径转化为碳基材料到燃料基的方法，其通过气化接着进行费 - 托合成，包括由非化石资源产生的氢的生成阶段 反向水煤气反应阶段。 这个过程使得有可能限制温室气体的排放。

公开(公告)号：US12049591B2

公开(公告)日：2024-07-30

申请号：US17409856

申请日：2021-08-24

Applicant: IFP Energies Nouvelles

Inventor： Alain Quignard ,  Wilfried Weiss ,  Isabelle Merdrignac ,  Jeremie Barbier

IPC: C08L95/00 ,  C10C3/02 ,  C10C3/06

CPC classification number: C10C3/06 ,  C08L95/00 ,  C10C3/02

Abstract: Between 40% and 75% by weight of a first bitumen base B1 an asphalt obtained by a solvent deasphalting of a first vacuum residue R1 resulting from the distillation of an effluent hydroconverted by a process for the ebullated bed hydroconversion of a heavy hydrocarbon feedstock, and



Between 25% and 60% by weight of a second bitumen base B2 and/or of a flux F, F at least one heavy aromatic cut with a hydrogen content of greater than 8.5% by weight, B2, R1 or a second vacuum residue R2 resulting from a distillation of a crude oil or a mixture of R1 and R2.

公开(公告)号：US09074139B2

公开(公告)日：2015-07-07

申请号：US13706713

申请日：2012-12-06

Applicant: IFP ENERGIES NOUVELLES

Inventor： Alain Quignard ,  Eric Sanchez ,  Jean Francois Le Coz

IPC: C10G1/08 ,  C10G65/12 ,  C10G35/04 ,  C10G47/02 ,  C10G1/00 ,  C10G49/00 ,  C10G63/00 ,  C10G63/04 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10G1/06

CPC classification number: C10G1/006 ,  C10G1/002 ,  C10G1/06 ,  C10G1/08 ,  C10G35/04 ,  C10G47/02 ,  C10G49/002 ,  C10G63/00 ,  C10G63/04 ,  C10G2400/20 ,  C10G2400/30 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08

Abstract: The invention relates to a process for coal conversion, optionally in co-processing with other feedstocks, notably of the biomass type, comprising at least one liquefaction step, followed by a fixed-bed hydrocracking step and a catalytic reforming step. With this process, aromatic compounds can be obtained from a feedstock containing coal.

Abstract translation: 本发明涉及一种煤转化方法，任选地与其他原料（特别是生物质类型）共处理，包括至少一个液化步骤，随后是固定床加氢裂化步骤和催化重整步骤。 通过该方法，可以从包含煤的原料获得芳族化合物。

公开(公告)号：US09644154B2

公开(公告)日：2017-05-09

申请号：US14383914

申请日：2013-02-26

Applicant: IFP ENERGIES NOUVELLES

Inventor： Antoine Daudin ,  Alain Quignard ,  Olivier Thinon

IPC: C10G65/02 ,  C10G65/12 ,  C10G65/04 ,  C08H8/00 ,  C10G3/00 ,  C10G45/00 ,  C10G47/00 ,  B01J37/20 ,  B01J21/04 ,  B01J21/18 ,  B01J23/86 ,  B01J23/883 ,  B01J37/00 ,  C10G1/00

CPC classification number: C10G65/043 ,  B01J21/04 ,  B01J21/18 ,  B01J23/866 ,  B01J23/883 ,  B01J37/0009 ,  B01J37/20 ,  C08H8/00 ,  C10G1/002 ,  C10G3/46 ,  C10G3/48 ,  C10G3/50 ,  C10G45/00 ,  C10G47/00 ,  C10G65/12 ,  C10G2300/4081 ,  Y02P30/20

Abstract: A process for the production of hydrocarbon products from a feed comprising at least one non-pre-treated bio-oil, comprising a first step for hydroreforming in the presence of hydrogen and a hydroreforming catalyst, used alone or as a mixture, to obtain at least one liquid effluent comprising at least one aqueous phase and at least one organic phase, a second step in which at least a portion of the organic phase of the effluent obtained from the first hydroreforming step is recycled to the first hydroreforming step with a recycle ratio equal to the ratio of the mass flow rate of said organic phase to the mass flow rate of the non-pre-treated bio-oil in the range 0.05 to 2 and in which the hydrocarbon effluent obtained from the hydrotreatment and/or hydrocracking step is not recycled to said first hydroreforming step.