公开(公告)号：JP2008127575A

公开(公告)日：2008-06-05

申请号：JP2007301098

申请日：2007-11-21

Applicant: Haldor Topsoe As ,  ハルドール・トプサー・アクチエゼルスカベット

Inventor： BREIVIK RASMUS ,  KNUDSEN KIM GROEN

IPC: C10G65/04 ,  C10G45/02

CPC classification number: C10G65/04 ,  C10G2300/201 ,  C10G2300/202 ,  C10G2300/4006

Abstract: PROBLEM TO BE SOLVED: To provide a method for catalytic hydrogenation of a silicon-containing hydrocarbon supplying raw material.
SOLUTION: The method for catalytic hydrogenation of a silicon compound-containing hydrocarbon supplying raw material comprises a process for bringing the supplying raw material into contact with a first hydrogenation catalyst in the presence of hydrogen at an outlet temperature of up to 410°C to reduce the content of the silicon compound in the supplying raw material, a process for cooling the thus treated supplying raw material to a temperature of 280-350°C, and a process for bringing the cooled supplying raw material into contact with a second hydrogenation catalyst under an effective condition to decrease the concentrations of sulfur compounds and nitrogen compounds, wherein the first hydrogenation catalyst is positioned in at least two serially connected reaction vessels.
COPYRIGHT: (C)2008,JPO&INPIT

Abstract translation: 待解决的问题：提供含硅烃供应原料的催化氢化方法。 解决方案：含硅化合物的烃供应原料的催化氢化方法包括在氢气存在下使供应原料与第一氢化催化剂接触的方法，出口温度高达410℃ 以降低供给原料中的硅化合物的含量，将这样处理的供给原料冷却至280-350℃的温度的方法，以及使冷却后的供给原料与第二次 氢化催化剂在有效条件下降低硫化合物和氮化合物的浓度，其中第一氢化催化剂位于至少两个串联连接的反应容器中。 版权所有（C）2008，JPO＆INPIT

公开(公告)号：JP2006291182A

公开(公告)日：2006-10-26

申请号：JP2006063517

申请日：2006-03-09

Applicant: Inst Fr Petrole ,  アンスティテュ フランセ デュ ペトロールInstitut Francais Du Petrol

Inventor： BARTHELET KARIN ,  EUZEN PATRICK ,  DULOT HUGHES ,  BOURGES PATRICK

IPC: C10G67/06 ,  B01D15/00 ,  B01J20/10 ,  B01J20/34 ,  B01J21/12 ,  B01J35/10 ,  C10G25/00 ,  C10G47/04 ,  C10G67/02

CPC classification number: C10G67/06 ,  C10G25/003 ,  C10G2300/201 ,  C10G2300/4081 ,  C10G2300/4093

Abstract: PROBLEM TO BE SOLVED: To provide a method for removing polynuclear aromatic compounds (PNA) in a hydrocracking process.
SOLUTION: The raw material oil is hydrocracked in a hydrocarbon reactor 4 and an unconverted fraction 11 separated from the liquid products in a fractionation zone 9 is recycled to the hydrocarbon reactor after the polynuclear aromatic compounds (PNA) contained therein are removed by adsorption by an adsorbent based on alumina-silica having a controlled macropore content as a pore volume measured by the mercury porosimetry in adsorption zones 17 and 18.
COPYRIGHT: (C)2007,JPO&INPIT

Abstract translation: 待解决的问题：提供一种在加氢裂化过程中除去多核芳族化合物（PNA）的方法。 解决方案：原料油在烃反应器4中加氢裂化，并且在分离区9中与液体产物分离的未转化馏分11在其中包含的多核芳族化合物（PNA）被除去之后再循环到烃反应器中 通过基于氧化铝 - 二氧化硅的吸附剂进行吸附，其具有受控大孔含量作为通过吸收区17和18中的水银孔率法测量的孔体积。（C）2007，JPO＆INPIT

公开(公告)号：JP2006291181A

公开(公告)日：2006-10-26

申请号：JP2006063494

申请日：2006-03-09

Applicant: Inst Fr Petrole ,  アンスティテュ フランセ デュ ペトロールInstitut Francais Du Petrol

Inventor： BARTHELET KARIN ,  EUZEN PATRICK ,  DULOT HUGHES ,  BOURGES PATRICK

IPC: C10G67/06 ,  B01J20/10 ,  B01J20/28 ,  B01J20/34 ,  B01J21/12 ,  B01J35/10 ,  C10G25/00 ,  C10G47/12

CPC classification number: C10G67/06 ,  C10G25/003 ,  C10G2300/201 ,  C10G2300/4081 ,  C10G2300/4093

Abstract: PROBLEM TO BE SOLVED: To provide a technique for selectively, wholly or partially removing polynuclear aromatic compounds (PNA) which accumulate on a catalyst thereby causing a loss of catalytic capacity or the total deactivation of the catalyst in a hydrocracking process with a recycle loop.
SOLUTION: The improved hydrocracking process with recycle comprises a step for removing the polynuclear aromatic compounds from at least a portion of a fraction to be recycled by adsorption on a specific adsorbent based on alumina-silica having a controlled macropore content.
COPYRIGHT: (C)2007,JPO&INPIT

Abstract translation: 要解决的问题：提供一种用于选择性地，全部或部分地除去积聚在催化剂上的多核芳族化合物（PNA）的技术，从而在加氢裂化过程中引起催化能力的损失或催化剂的总失活， 循环回路。 解决方案：具有循环的改进的加氢裂化方法包括从基于具有受控大孔含量的氧化铝 - 二氧化硅在特定吸附剂上吸附而从至少一部分待再循环的馏分中除去多核芳族化合物的步骤。 版权所有（C）2007，JPO＆INPIT

公开(公告)号：JP2017066213A

公开(公告)日：2017-04-06

申请号：JP2015190629

申请日：2015-09-29

Applicant: 株式会社日立製作所

Inventor： 佐野 理志 ,  遠藤 和広 ,  林 洋二郎 ,  磯上 尚志 ,  林田 恵星 ,  黒川 秀昭 ,  渡部 雅智

IPC: C02F11/00 ,  C10G1/00

CPC classification number: C10G1/045 ,  C10G1/002 ,  C10G31/10 ,  C10G2300/201 ,  C10G2300/44

Abstract: 【課題】安定的に、かつ、低ランニングコストで含油混合物から原油を回収する原油回収装置を提供する。 【解決手段】水と固体の両方もしくは一方と原油で構成される含油スラッジから原油を抽出する装置において、抽剤と含油スラッジを混合する抽出槽と、抽出後の抽出液を蒸留する気化・液化器とを備え、含油混合物中の原油成分であるナフサを抽剤とし、蒸留による留出液を再利用することを特徴とする原油回収装置。 【選択図】図1

公开(公告)号：JP5384825B2

公开(公告)日：2014-01-08

申请号：JP2007515101

申请日：2005-04-27

Applicant: ナルコ カンパニー

Inventor： ハウデスヘル，マイケル，ジェイムズ

IPC: C10G29/20 ,  C10G9/16 ,  C10G29/22 ,  C10G75/04

CPC classification number: C10G75/04 ,  C10G2300/201 ,  C10G2300/206 ,  C10G2300/302 ,  C10G2300/4075 ,  C10G2300/44 ,  Y10S585/95

公开(公告)号：JP2013535320A

公开(公告)日：2013-09-12

申请号：JP2013520743

申请日：2011-07-13

Applicant: サウジ アラビアン オイル カンパニー

Inventor： − サハン、ファワズ、エイ． アル ,  − ザイエド、オマー、ゼット． アル

IPC: B01D17/12 ,  B01D17/025

CPC classification number: G01N29/024 ,  B01D17/0214 ,  C10G33/06 ,  C10G33/08 ,  C10G2300/201 ,  E21B43/34 ,  G01N29/4427 ,  G01N2291/02836 ,  G01N2291/048 ,  G01N2291/102 ,  Y10T137/0318 ,  Y10T137/86389

Abstract: A method and apparatus for an improved dewatering tank system that allows for safely controlling a water stream exiting the dewatering tank system. The apparatus can include a sound velocity detector, a control system, and a control element. The sound velocity detector can include a transducer, a detector, and a transmitter. The control system can include a computer and a program product. The apparatus can optionally include a dewatering tank, a drain line, and a controllable valve. The apparatus allows for transmitting sound energy through the water stream flowing in the drain lined that is connected to the dewatering tank, calculating the velocity of the sound energy as the sound energy travels through the water stream, monitoring the velocity of the sound energy for a period of time, and controlling the position of the controllable valve depending on the calculated velocity of the sound energy.

公开(公告)号：JP5232139B2

公开(公告)日：2013-07-10

申请号：JP2009507569

申请日：2006-04-28

Applicant: エスケー ケミカルズ カンパニー リミテッド

Inventor： チュン、シン‐ホ ,  チョー、ヒュン‐ジュン ,  ロー、ハン‐ドゥク ,  リム、ジェ‐ボン ,  リー、ジョン‐イン ,  ムーン、チャン‐ウー ,  キム、ビュン‐フイ

IPC: C10L1/08 ,  C11B3/12 ,  C11C3/08

CPC classification number: C10L1/026 ,  B01J14/00 ,  B01J19/006 ,  B01J19/1818 ,  B01J19/1875 ,  B01J2219/00006 ,  B01J2219/0004 ,  B01J2219/00768 ,  B01J2219/0077 ,  C07C67/08 ,  C10G2300/1014 ,  C10G2300/201 ,  C10G2300/4006 ,  C10G2300/4012 ,  C11B3/12 ,  C11C3/003 ,  Y02E50/13 ,  Y02P30/20 ,  C07C69/24 ,  C07C69/52

Abstract: A method and an apparatus for preparing fatty acid alkyl ester for bio-diesels are disclosed, wherein fatty acid, specifically fatty acid distillate reacts with alcohol, without a catalyst. The method does not require the purification process of the catalyst and glycerin, and has the superior conversion ratio of fatty acid. The method for preparing fatty acid alkyl ester for bio-diesel fuels comprises the step of esterifying fatty acid raw material with alcohol, under a temperature of 200 to 350° C. and a pressure of atmospheric pressure to 10 bar. The apparatus for preparing fatty acid alkyl ester for bio-diesel fuels, comprises: the first reactor for esterifying fatty acid raw material with alcohol under a temperature of 200° C. to 350° C. and a pressure of atmospheric pressure to 10 bar and for converting 80 to 90% of total fatty acid into fatty acid alkyl ester; and the second reactor for converting remaining fatty acid unconverted at the first reactor into fatty acid alkyl ester.

公开(公告)号：JP2012510894A

公开(公告)日：2012-05-17

申请号：JP2011539683

申请日：2009-12-03

Applicant: ハンツマン ペトロケミカル エルエルシー

Inventor： グリグズビイ，ロバー・エイ，ジユニア ,  クリツチフイールド，ジエイムズ・イー ,  ホラブ，パトリク・イー ,  ホワイト，ラリー・アール

IPC: B01D53/14 ,  B01D11/04 ,  B01D53/52 ,  B01D53/62 ,  B01D53/77

CPC classification number: B01D53/1456 ,  B01D53/1493 ,  B01D2252/604 ,  B01D2252/606 ,  C02F1/26 ,  C02F1/68 ,  C02F2101/38 ,  C02F2103/18 ,  C02F2103/343 ,  C08G2650/50 ,  C10G21/20 ,  C10G2300/201 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/4075 ,  C10G2300/44 ,  C10G2300/80

Abstract: An amine solvent solution that is useful in absorbing acid gases from a liquid or gas feed stream may have an amine additive added thereto. Additionally or alternatively, the amine additive may be added to a liquid or gas feed stream. The addition of the amine additive decreases the presence of amine-derived contaminants and/or degradation of amine in the amine solvent solution. As such, the amine solvent solution is available for effective reuse in treating the liquid or gas feed stream and there may be a decrease in the corrosion within an amine treating system.

公开(公告)号：JP2011513512A

公开(公告)日：2011-04-28

申请号：JP2010547704

申请日：2009-02-17

Applicant: ゼネラル・エレクトリック・カンパニイGeneral Electric Company

Inventor： ゴリアスゼウスキ，アラン・イー ,  マクダニエル，カトー・アール

IPC: C10G17/04

CPC classification number: C10G21/16 ,  C10G21/06 ,  C10G21/08 ,  C10G21/22 ,  C10G21/27 ,  C10G2300/1033 ,  C10G2300/201 ,  C10G2300/205

Abstract: An extraction aid has been found which provides for enhanced contaminate removal, such as metals and amines, from crude oils that uses components that are desirable in desalting processes as the components are water soluble, have low toxicity, are highly biodegradeable and exhibit high thermal stability. According to one embodiment of the invention, an extraction aid that provides enhanced extraction properties is comprised of a blend of acids, particularly water soluble acids. More specifically, a combination of two acids chosen from the group consisting of acetic acid, sulfuric acid, glycolic acid, citric acid and methanesulfonic acid.

公开(公告)号：JP2009299060A

公开(公告)日：2009-12-24

申请号：JP2009131690

申请日：2009-06-01

Applicant: General Electric Co ,  ゼネラル・エレクトリック・カンパニイGeneral Electric Company

Inventor： OSAHENI JOHN AIBANGBEE ,  FYVIE THOMAS JOSEPH ,  O'NEILL GREGORY ALLEN ,  MATIS HOPE

IPC: C10G25/00

CPC classification number: C10G25/003 ,  B01D15/00 ,  B01J20/103 ,  B01J20/28004 ,  B01J20/28052 ,  B01J20/28064 ,  B01J20/28066 ,  B01J20/28073 ,  B01J2220/58 ,  C10G53/08 ,  C10G2300/201 ,  C10G2300/44

Abstract: PROBLEM TO BE SOLVED: To provide a method for removing impurities from a heavy fuel, particularly, a technique of lowering a level of metal or non-metal impurities in the heavy oil.
SOLUTION: An adsorption column 100 for removing impurities from the heavy fuel is provided. The adsorption column is a stationary column equipped with two or more baffles 114 and 116 arranged in the column, and is configured to have a plurality of adsorption material particles 106 therein. The adsorption material particles each have an average specific surface area of about 500 m
2 /g to about 1,200 m
2 /g, and an average fine pore volume of about 0.8 cc/g or more, an average diameter of about 5 μm to about 100 μm, and a particle size distribution wherein at least about 50% of the particles have a diameter greater than about 18 μm.
COPYRIGHT: (C)2010,JPO&INPIT

Abstract translation: 要解决的问题：提供一种从重质燃料中除去杂质的方法，特别是降低重油中的金属或非金属杂质的水平的技术。 提供了用于从重质燃料中除去杂质的吸附塔100。 该吸附塔是配备有配置在该列中的两个以上的挡板114,116的固定柱，并且构成为具有多个吸附材料粒子106。 吸附材料颗粒各自的平均比表面积为约500m 2 / SP / g至约1,200m 2 / SP / g，平均细孔容积为约0.8cc / g以上，平均直径约5μm至约100μm，以及其中至少约50％的颗粒具有大于约18μm的直径的粒度分布。 版权所有（C）2010，JPO＆INPIT