| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 61 | Adsorption method for producing ultra low sulfur hydrocarbon streams | JP2001503965 | 2000-06-02 | JP4755792B2 | 2011-08-24 | バル クリスハン カウル |
| The instant invention is directed to a method for reducing the amount of sulfur in hydrocarbon streams comprising the steps of:(a) contacting a hydrocarbon stream comprising hydrocarbons and sulfur compounds with an adsorbent selective for adsorption of said sulfur compounds, under adsorption conditions capable of retaining said sulfur compounds on said adsorbent and obtaining an adsorption effluent comprising a desulfurized hydrocarbon stream,(b) collecting said desulfurized hydrocarbon stream,(c) desorbing said sulfur compounds from said adsorbent by passing a desorbent through said adsorbent under desorption conditions to obtain a desorption effluent comprising sulfur compounds and said desorbent,(d) treating said desorption effluent to remove said sulfur compounds from said desorption effluent and collecting a desulfurized desorbent effluent comprising desorbent. | ||||||
| 62 | Method for simultaneous processing and rectification of light naphtha hydrocarbon stream | JP2000569899 | 1999-08-10 | JP4642233B2 | 2011-03-02 | ギルダート，ゲイリー・アール; グロテン，ウィリブロード・エイ; パットマン，ヒュー・エム |
| A process for concurrently fractionating and hydrotreating of a full range naphtha stream. The full boiling range naphtha stream is subjected to simultaneous hydrodesulfurization and splitting into a light boiling range naphtha and a heavy boiling range naphtha. The two boiling range naphthas are treated separately according to the amount of sulfur in each cut and the end use of each fraction. | ||||||
| 63 | System and method for producing high quality gasoline hydrocarbons recombined catalytically | JP2010532411 | 2008-11-05 | JP2011503264A | 2011-01-27 | 丁冉峰 |
| This invention relates to a system for the preparation of a high quality gasoline through the recombination of catalytic hydrocarbon and its process. The characteristics are as follows: the upper part of the fractionator is connected with light petrol hydrogenation unit through the light petrol pipeline. The lower part of the fractionator is connected with the extractor through the heavy petrol pipeline. The upper part of the extractor directly extracts the product through the pipeline and the lower part of the extractor is connected to the light petrol pipeline behind the light petrol hydrogenation unit. Compared with the prior art, this invention has the following advantages: the volume of used catalyst is greatly reduced. In addition, the sulfur reduction and olefin reduction effect are remarkable by using the hydrogenation units with special catalysts and parameters regarding different petrol fractions. | ||||||
| 64 | Petroleum fuel combustion combined cycle electric power generation system and method thereof | JP32350499 | 1999-11-15 | JP4509267B2 | 2010-07-21 | 朝芳 佐々木; 芳範 増子; 剛 岡田; 誠 猪俣 |
| A light portion is extracted from feed oil by a separation system. The light portion is then subject to a hydrotreatment to obtain impurity-removed fuel oil which is stored in an intermediate tank. A residue of the feed oil after extraction of the light portion is gasified to obtain syngas (H2 gas+CO gas) which is used as basic fuel for power generation in a power generation system. The fuel oil is fed to the power generation system as auxiliary fuel for supplementing the power generation based on the syngas. The power generation system includes a plurality of gas turbines and generators. The number of the gas turbines to be driven by the fuel oil is controlled to adjust the power generation amount depending on demand. | ||||||
| 65 | Process for the conversion of heavy crude oil and heavy feedstock such as distillation residue | JP2005502551 | 2003-12-12 | JP2006511681A | 2006-04-06 | アルベルト デルビアンコ; ニコレッタ パナリティー; マリオ マルキオンナ; ロモロ モンタナリ; セルジオ ロッシ |
| Process for the conversion of heavy feedstocks selected from heavy crude oils, distillation residues, heavy oils coming from catalytic treatment, thermal tars, oil sand bitumens, various kinds of coals and other high-boiling feedstocks of a hydrocarbon origin known as black oils, by the combined use of the following three process units: hydroconversion with catalysts in slurry phase (HT), distillation or flash (D), and deasphalting (SDA). | ||||||
| 66 | Method for manufacturing ultra-low sulfur content gas oil base | JP2003393582 | 2003-11-25 | JP2005154538A | 2005-06-16 | IKI SUGURU; TANAKA YUICHI; SUGANO HIDEAKI; KAMATA TAKATSUGU; KUDO HIDENORI; KANEKO SADANORI |
| <P>PROBLEM TO BE SOLVED: To provide a method which enables production of an ultra-low sulfur content gas oil base having a sulfur content of not more than 1 mass ppm by using the existing desulfurization plant for gas oil manufacturing. <P>SOLUTION: The method for manufacturing the ultra-low sulfur content gas oil base having a sulfur content of not more than 1 mass ppm comprises a step (1) of hydrodesulfurizing a gas oil fraction having a sulfur content of ≤1.6 mass% under the conditions of an LHSV of 0.05-1.2 h<SP>-1</SP>, a hydrogen to oil ratio of 200-800 NL/L, a reaction temperature of 300-390°C, and a hydrogen partial pressure of 2-9 MPa, a step (2) of recovering the formed oil from the step (1), and a step (3) of removing a light oil fraction of 0.1-8 vol% based on the total amount of the formed oil from the formed oil recovered from the step (2) at a pressure lower than atmospheric pressure so that the end point of the light oil fraction to be removed becomes ≥200°C. <P>COPYRIGHT: (C)2005,JPO&NCIPI | ||||||
| 67 | Hydrogenation, fractionation, comprising the conversion process and desulfurization of the sulfur-containing compound, a method for producing a low sulfur content gasoline | JP2002571794 | 2002-01-29 | JP2004523628A | 2004-08-05 | ドゥニ ウジオ; カンタン デビュイシェール; ジャン リュック ノッカ; フロラン ピカール |
| The invention relates to a method for producing petrol having a low sulphur content comprising at least one selective hydrogenation of diolefins, optionally at least one transformation stage, preferably an increase stage, of light sulphur compounds present in petrol, at least one fractioning of the petrol obtained into at least two fractions, light petrol and heavy petrol, then an optional transformation stage, preferably alkylation or adsorption of sulphur compounds and a one-stage desulphurization treatment of at least one part of the heavy fraction. | ||||||
| 68 | A method of removing sulfur compounds from gasoline | JP2001558173 | 2000-11-15 | JP2003531922A | 2003-10-28 | ライト ウィットチャーリー，ランディ; クレトイウ，ルシア; シー ジェントリー，ジョセフ; シュヤムクマー，カラムブール; リー，フ−ミン |
| (57)【要約】 硫黄化合物を炭化水素ストリームから除去する。 好ましい実施形態において、オレフィンをラフィネートストリームに向けて排除するとともに、同時に硫黄化合物を抽出物ストリームに抽出するために、流動接触分解装置からのガソリンストリームを抽出蒸留塔（Ｃ−２０１）内で抽出蒸留する。 | ||||||
| 69 | Adsorption method for producing ultra low sulfur hydrocarbon streams | JP2001503965 | 2000-06-02 | JP2003502477A | 2003-01-21 | バル クリスハン カウル |
| The instant invention is directed to a method for reducing the amount of sulfur in hydrocarbon streams comprising the steps of:(a) contacting a hydrocarbon stream comprising hydrocarbons and sulfur compounds with an adsorbent selective for adsorption of said sulfur compounds, under adsorption conditions capable of retaining said sulfur compounds on said adsorbent and obtaining an adsorption effluent comprising a desulfurized hydrocarbon stream,(b) collecting said desulfurized hydrocarbon stream,(c) desorbing said sulfur compounds from said adsorbent by passing a desorbent through said adsorbent under desorption conditions to obtain a desorption effluent comprising sulfur compounds and said desorbent,(d) treating said desorption effluent to remove said sulfur compounds from said desorption effluent and collecting a desulfurized desorbent effluent comprising desorbent. | ||||||
| 70 | Gasoline quality improvement method | JP50947596 | 1995-07-25 | JPH10505381A | 1998-05-26 | サーリ，マイケル・セバスチャン; ヒルバート，ティモシー・リー; マゾン，ドミニク・ニコラス |
| (57)【要約】 ガソリン沸点範囲の分解フラクションを、許容できる硫黄レベルに接触脱硫する方法では、最初に、オクタン価の多少の減少を伴って供給原料を脱硫する水素化処理段階を用い、その後、自己結合またはバインダー無含有ゼオライトによって、失われたオクタン価を回復させるために処理する。 本発明の方法は、オクタン価を維持しながら、ＦＣＣナフサならびに熱分解ガソリンおよびコーカーナフサのような接触分解ナフサならびに熱分解ナフサを脱硫するのに利用することができ、ガソリンブレンド中での改質油およびアルキレートに対する要求を減少させる。 自己結合触媒は、活性の点で有利であり、本発明の方法をより低い温度で行うことを可能にする。 | ||||||
| 71 | JPH0547594B2 - | JP21621291 | 1991-08-02 | JPH0547594B2 | 1993-07-19 | HAYASHI MASAHIRO; KUBO TOSHIHIKO; MASUDA TOSHIHIKO |
| 72 | Removal of h2s from tail gas by using recirculating nmp extractant | JP16846479 | 1979-12-26 | JPS5588832A | 1980-07-04 | JIYON EICHI BURIYUMU; JIEIMUZU DEII BUSHIYUNERU; MIRUTON DEII REITON |
| 73 | JPS49112904A - | JP1401674 | 1974-02-02 | JPS49112904A | 1974-10-28 | |
| 74 | API 그룹 II 중질 기유의 개선된 생산 방법 | KR1020187007542 | 2016-08-04 | KR102626869B1 | 2024-01-19 | |
| 75 | 인-시튜 유기 과산화물 생산 및 산화성 이종원자 전환을 위한 통합 시스템 및 공정 | KR1020147005202 | 2012-06-28 | KR101934136B1 | 2019-04-05 | |
| 76 | 경질 유분의 흡착에 의한 탈황 및 중질 유분의수소화탈황을 포함하는 가솔린의 탈황 방법 | KR1020087005565 | 2006-08-02 | KR1020080038208A | 2008-05-02 | 니꼴라오알렉상드르; 삐까르플로랑 |
| The invention relates to a gasoline desulfurization method consisting of a step in which the gasoline is fractionated into a light fraction comprising thiophenic compounds, such as thiophene or methylthiophenes, and a heavy fraction concentrating the heaviest aromatic sulfur compounds. The heavy fraction is treated by hydrodesulfurization, while the light fraction is brought into contact with a solid adsorbent that can be used to eliminate at least part of the light thiophenic compounds, said solid adsorbent being regenerated by a flux within the method. | ||||||
| 77 | 燃料及びその配合組み合わせ | JP2020090195 | 2020-05-25 | JP2020143299A | 2020-09-10 | ウォハイビ、ムゥハァミィドゥ; プルット、トム エフ. |
| 【課題】ライトタイトオイル及び高硫黄燃料油を使用して製造した、非常に低い硫黄及び窒素を有し、実質的に金属を含まない燃料、及び、燃料として有用な配合組み合わせの提供。 【解決手段】ライトタイトオイルを、処理された可溶性脱アスファルト化油及び高硫黄燃料油由来のより軽い材料を有する水素化変換反応流出物または残留物水素化処理によって処理された他の残留物に組み合わせて得られる燃料。未変換油は溶剤分離を通過して不溶性の残存金属及びアスファルテンを除去し、可溶性脱アスファルト化油を形成し、続いて水素化処理または水素化変換により処理されて前記処理可溶性脱アスファルト化油を形成する。組み合わせで得られた燃料の硫黄含有量は0.5重量%以下である。 【選択図】図1 |
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| 78 | 原油全体を脱アスファルトおよび脱硫するための統合された方法 | JP2015516064 | 2013-05-29 | JP5991562B2 | 2016-09-14 | オメル・レファ・コセオグル; 牛尾 賢; 中野 宏二 |
| 79 | System and method for producing high quality gasoline hydrocarbons recombined catalytically | JP2010532412 | 2008-11-06 | JP5438683B2 | 2014-03-12 | 丁冉峰 |
| 80 | A method of removing sulfur compounds from gasoline | JP2001558173 | 2000-11-15 | JP4828762B2 | 2011-11-30 | ライト ウィットチャーリー，ランディ; クレトイウ，ルシア; シー ジェントリー，ジョセフ; シュヤムクマー，カラムブール; リー，フ−ミン |
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