公开(公告)号：US20240279058A1

公开(公告)日：2024-08-22

申请号：US18570999

申请日：2022-06-16

Applicant: TECHNIP ENERGIES FRANCE

Inventor： Jan-Jaap Riegman ,  Stephane Walspurger ,  Prateek Jain

IPC: C01B3/38 ,  B01J8/04 ,  C01B3/02 ,  C01B3/48 ,  C01C1/04 ,  C07C29/152

CPC classification number: C01B3/382 ,  B01J8/0492 ,  B01J8/0496 ,  C01B3/025 ,  C01B3/384 ,  C01B3/48 ,  C01C1/0417 ,  C07C29/152 ,  B01J2208/00309 ,  B01J2208/00504 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0283 ,  C01B2203/061 ,  C01B2203/068 ,  C01B2203/0816 ,  C01B2203/0833 ,  C01B2203/0883 ,  C01B2203/141 ,  C01B2203/142

Abstract: Process for producing a chemical product, comprising subjecting hydrocarbon feed and further reforming reactant to an endothermal reaction whereby a primary reformate is formed, in a primary fired heat-recuperating reformer reaction unit, comprising a catalyst zone and a primary reformate passage way arranged to transfer heat from said reformate to said catalyst zone; optionally subjecting the primary reformate to a secondary reforming reaction, thereby forming a secondary reformate; and using primary reformate or second reformate as a heat exchange medium to supply reaction heat to an endothermal reaction, which endothermal reaction is carried out in a parallel heat-exchanger reactor.

公开(公告)号：US12060533B2

公开(公告)日：2024-08-13

申请号：US17824404

申请日：2022-05-25

Applicant: Saudi Arabian Oil Company

Inventor： Lianhui Ding ,  Alberto Lozano Ballesteros ,  Ibrahim Al-Nutaifi ,  Abdennour Bourane

IPC: C10G69/06 ,  B01D3/14 ,  B01D15/10 ,  B01J8/04

CPC classification number: C10G69/06 ,  B01D3/143 ,  B01D15/10 ,  B01J8/0457 ,  B01J8/0492 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/206 ,  C10G2300/208 ,  C10G2300/308 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30

Abstract: A process for upgrading a hydrocarbon feed, such as crude oil or other heavy oils, may include hydrotreating a hydrocarbon feed in a hydrotreating unit to produce a hydrotreated effluent that includes asphaltenes, coke precursors, or both. The process further includes hydrocracking the hydrotreated effluent in a hydrocracking unit to produce a hydrocracked effluent, adsorbing at least a portion of the asphaltenes, coke precursors, or both, from the hydrotreated effluent, the hydrocracked effluent, or both, separating the hydrocracked effluent into at least an upgraded lesser-boiling effluent and a greater-boiling effluent in a hydrocracked effluent separation system, and steam cracking the upgraded lesser-boiling effluent to produce olefins, aromatic compounds, or combinations of these. The process may further include recycling the greater boiling effluent back to the hydrotreating unit and hydrocracking a middle distillate effluent from the hydrocracked effluent separation system. Systems for conducting the processes are also disclosed.

公开(公告)号：US20240181416A1

公开(公告)日：2024-06-06

申请号：US18285185

申请日：2022-03-26

Applicant: HINDUSTAN PETROLEUM CORPORATION LIMITED

Inventor： Valavarasu GNANASEKARAN ,  Pradyut Kumar DHAR ,  Samuel Jedidiah MEKALA ,  Bojja RAMACHANDRA RAO

IPC: B01J8/04

CPC classification number: B01J8/0492 ,  B01J8/0453 ,  B01J2208/00849 ,  B01J2208/00938

Abstract: A quench mixing device (100, 200, 300) is disclosed for mixing multiphase process fluids in 5 the inter-bed region of a concurrent downflow reactor (10) for obtaining homogeneity of the temperature and chemical composition of the mixed stream. The quench mixing device comprises of outer mixing zone (109), inner mixing zone (120), swirl mixing zone (151) and exit zone. Due to the position of the disperser (142), the liquid coming from above is dispersed in droplets. The fluid impact on the other side of the outer mixing zone. The gas is bubbled into 0 liquid in the inner mixing zone. The fluids enter the swirl mixing zone via two-phase duct (131) which is shaped to have low pressure loss and high velocity at the outlet to induce dispersed regime. The outlet of the two-phase duct is placed such that liquid is injected into the swirl zone below liquid surface, causing increased momentum for inducing liquid swirl in the swirl zone and increased number of rotations.

公开(公告)号：US20240067587A1

公开(公告)日：2024-02-29

申请号：US18280265

申请日：2022-03-02

Applicant: MITSUBISHI HEAVY INDUSTRIES, LTD. ,  The University of Tokyo

Inventor： Koichiro Yoshitoku ,  Yukio Tanaka ,  Atsuhiro Yukumoto ,  Noriaki Senba ,  Kazuhiro Takanabe

IPC: C07C2/84 ,  B01J8/04 ,  B01J21/08 ,  B01J23/10 ,  B01J23/30 ,  B01J27/232

CPC classification number: C07C2/84 ,  B01J8/0492 ,  B01J8/0496 ,  B01J21/08 ,  B01J23/10 ,  B01J23/30 ,  B01J27/232 ,  B01J2208/025 ,  C07C2523/04 ,  C07C2523/10 ,  C07C2523/30 ,  C07C2527/167

Abstract: An olefin production device for producing an olefin from a raw material gas containing methane and oxygen includes a reactor containing: a first catalyst; and a second catalyst disposed downstream of the first catalyst in a flow direction of the raw material gas. The first catalyst is a catalyst in which a zirconium salt or carbonate of an alkali metal, an oxide of an alkaline earth metal, an oxide of one kind of lanthanoid element, a composite oxide containing a lanthanoid element, or a combination thereof is supported on a support. The second catalyst is a catalyst containing a tungsten oxide, phosphate, or carbonate of an alkali metal.

公开(公告)号：US11845719B1

公开(公告)日：2023-12-19

申请号：US18314591

申请日：2023-05-09

Applicant: PHILLIPS 66 COMPANY

Inventor： Anthony O. Baldridge ,  Matthew J. Wulfers ,  Neal D. McDaniel ,  Robert M. Walston ,  Soumen Kundu ,  Bruce B Randolph

IPC: C07C6/10 ,  C07C7/09 ,  B01J8/04 ,  B01D3/14 ,  B01D5/00

CPC classification number: C07C6/10 ,  B01D3/14 ,  B01D5/006 ,  B01J8/0492 ,  C07C7/09 ,  B01J2208/00017 ,  B01J2208/00539 ,  C07C2529/40

Abstract: The present disclosure relates generally to processes and systems for producing liquid transportation fuels by converting a feed stream that comprises both isopentane and n-pentane, and optionally, some C6+ hydrocarbons. Isopentane and smaller hydrocarbons are separated to form a first fraction while n-pentane and larger components of the feed stock form a second fraction. Each fraction is then catalytically-activated in a separate reaction zone with a separate catalyst, where the conditions maintained in each zone maximize the conversion of each fraction to olefins and aromatics, while minimizing the production of C1-C4 light paraffins. In certain embodiments, the first fraction is activated at a lower temperature than the second fraction. Certain embodiments additionally comprise mixing at least a portion of the two effluents and contacting with either an oligomerization catalyst or alkylation catalyst to provide enhanced yields of upgraded hydrocarbon products that are suitable for use as a blend component of liquid transportation fuels or other value-added chemical products.

公开(公告)号：US20230392085A1

公开(公告)日：2023-12-07

申请号：US18250047

申请日：2021-10-22

Applicant: CHINA PETROLEUM & CHEMICAL CORPORATION ,  SINOPEC DALIAN RESEARCH INSTITUTE OF PETROLEUM AND PETROCHEMICALS CO., LTD.

Inventor： Meng DAI ,  Shicai LI ,  Yang LI ,  Dahai XU ,  He DING ,  Guang CHEN ,  Han ZHANG ,  Jiawen ZHOU

IPC: C10G49/00 ,  B01J8/04 ,  B01J8/02 ,  C10G65/16 ,  C10G65/08

CPC classification number: C10G49/002 ,  B01J8/0453 ,  B01J8/0492 ,  B01J8/025 ,  C10G65/16 ,  C10G65/08 ,  B01J2208/00823 ,  B01J2208/00893 ,  B01J2208/025 ,  B01J2208/00991 ,  C10G2400/04 ,  C10G2300/202 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/4025 ,  C10G2300/4037 ,  C10G2300/1044 ,  C10G2300/1055 ,  C10G2300/1051 ,  C10G2300/30

Abstract: A multi-phase combination reaction system has at least one fixed bed hydrogenation reactor. The fixed bed hydrogenation reactor has, arranged from top to bottom, a first hydrogenation reaction area, a gas-liquid separation area, a second hydrogenation reaction area and a third hydrogenation reaction area. The gas-liquid separation area is provided with a raw oil inlet. A hydrogen inlet is provided between the second hydrogenation reaction area and the third hydrogenation reaction area. The system is capable of simultaneously obtaining two fractions in one hydrogenation reactor.

公开(公告)号：US20230364573A1

公开(公告)日：2023-11-16

申请号：US18030329

申请日：2021-11-05

Applicant: NOVA CHEMICALS (INTERNATIONAL) S.A.

Inventor： Shahin GOODARZNIA ,  Vasily SIMANZHENKOV ,  Bolaji OLAYIWOLA ,  David GENT

IPC: B01J8/04 ,  B01J8/00 ,  B01J8/02 ,  C07C5/333

CPC classification number: B01J8/0438 ,  B01J8/003 ,  B01J8/0492 ,  B01J8/0285 ,  C07C5/3332 ,  B01J2208/00115 ,  B01J2208/00752 ,  B01J2208/00805 ,  B01J2208/024 ,  B01J2208/027

Abstract: A fixed bed reactor system for the oxidative dehydrogenation of ethane, comprising a catalyst bed wherein the catalyst capacity profile increases along the length of catalyst bed from the upstream end to the downstream end. The catalyst bed may include one or more sections, across one or more fixed bed reactors, that are identified by a change in catalyst capacity. Catalyst capacity, or the ability to convert ethane into ethylene, may be altered by changing the dilution ratio, void fraction, and or the 35% conversion temperature. A method for loading a fixed bed reactor with an increasing catalyst capacity is also described.

公开(公告)号：US20230219049A1

公开(公告)日：2023-07-13

申请号：US18001192

申请日：2021-06-22

Applicant: CASALE SA

Inventor： Enrico Rizzi ,  Matteo Masanti

IPC: B01J8/04 ,  C01C1/04

CPC classification number: B01J8/0415 ,  B01J8/0496 ,  B01J8/0492 ,  C01C1/0441 ,  B01J2208/00194

Abstract: A multi-bed catalytic reactor, particularly for the synthesis of ammonia, wherein the beds have an annular shape, the first bed has L(1)*(V/V(1)) equal to or greater than 50 wherein L(1) is the slenderness ratio of the first bed which is calculated as the axial length over the radial width; V is the total volume of the beds of the reactor and V(1) is the volume of the first bed.

公开(公告)号：US11661386B2

公开(公告)日：2023-05-30

申请号：US17335916

申请日：2021-06-01

Applicant: FINA TECHNOLOGY, INC.

Inventor： Joseph E Pelati ,  Jason Clark

IPC: B01J8/04 ,  C07C5/333 ,  C07C15/46

CPC classification number: C07C5/333 ,  B01J8/0496 ,  C07C5/3332 ,  C07C15/46 ,  B01J8/0492 ,  B01J2208/00061 ,  B01J2208/00168 ,  B01J2208/00539 ,  B01J2208/00893 ,  B01J2219/0004 ,  B01J2219/00038 ,  C07C2523/04 ,  C07C2523/745 ,  C07C2523/78 ,  C07C5/3332 ,  C07C15/46

Abstract: A multi-stage dehydrogenation process including contacting, in a first stage, a feed stream comprising a hydrocarbon and steam with a dehydrogenation catalyst under dehydrogenation conditions to yield a first stage effluent, heating the first stage effluent, and contacting, in a second stage, the heated first stage effluent with a dehydrogenation catalyst under dehydrogenation conditions to yield a second stage effluent comprising a dehydrogenation product, wherein the first stage includes a first reactor and a second reactor arranged in parallel, and wherein the second stage includes a third reactor connected in series with the first reactor and the second reactor. A multi-stage dehydrogenation system for carrying out dehydrogenation is also provided.

公开(公告)号：US20180305273A1

公开(公告)日：2018-10-25

申请号：US15809121

申请日：2017-11-10

Applicant: Siluria Technologies, Inc.

Inventor： Bipinkumar PATEL ,  Greg NYCE ,  Peter CZERPAK ,  Jarod McCORMICK ,  Guido RADAELLI ,  Erik C. SCHER ,  Joel CIZERON ,  Rahul IYER ,  Carlos FAZ ,  William MICHALAK ,  Tim A. RAPPOLD ,  Ron RUNNEBAUM ,  Aihua ZHANG ,  Peter BERGSTROM

IPC: C07C2/12 ,  C10G57/02 ,  B01J8/04 ,  B01J8/02 ,  B01J8/00 ,  B01J8/18 ,  B01J8/06 ,  C10G50/00

CPC classification number: C07C2/12 ,  B01J8/003 ,  B01J8/025 ,  B01J8/0278 ,  B01J8/0457 ,  B01J8/0492 ,  B01J8/065 ,  B01J8/067 ,  B01J8/1827 ,  B01J2208/00176 ,  B01J2208/00238 ,  B01J2208/00256 ,  B01J2208/0053 ,  B01J2208/025 ,  B01J2219/00006 ,  B01J2219/00038 ,  B01J2219/0004 ,  C07C2529/40 ,  C10G50/00 ,  C10G57/02 ,  Y02P20/582

Abstract: Integrated systems are provided for the production of higher hydrocarbon compositions, for example liquid hydrocarbon compositions, from methane using an oxidative coupling of methane system to convert methane to ethylene, followed by conversion of ethylene to selectable higher hydrocarbon products. Integrated systems and processes are provided that process methane through to these higher hydrocarbon products.