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    • 1. 发明申请
    • Bituminous froth inclined plate separator and hydrocarbon cyclone treatment process
    • 沥青泡沫斜板分离器和烃旋风处理工艺
    • US20040055972A1
    • 2004-03-25
    • US10306003
    • 2002-11-29
    • William Nicholas GarnerDonald Norman MadgeWilliam Lester Strand
    • C10G001/04
    • B03B9/02B03B5/34B04C5/08C10G1/045C10G1/047
    • Discloses apparatus to perform a process to remove water and minerals from a bitumen froth output of a oil sands hot water extraction process. A bitumen froth feed stream is diluted with a solvent and supplied to a primary inclined plate separator stage, which separates the bitumen into an overflow stream providing a bitumen product output from the circuit and a bitumen depleted underflow stream. A primary cyclone stage, a secondary inclined plate separator stage and a secondary cyclone stage further process the underflow stream to produce a secondary bitumen recovery product stream and a recycle stream. The secondary bitumen recovery product steam is incorporated into and becomes part of the circuit bitumen product output stream. The recycle stream is incorporated into the bitumen froth feed stream for reprocessing by the circuit.
    • 公开了从油砂热水提取过程的沥青泡沫输出中去除水和矿物质的方法的装置。 将沥青泡沫进料流用溶剂稀释并供给到主倾斜板分离器级,其将沥青分离成溢流,提供来自回路的沥青产物输出和沥青耗尽的下溢流。 主旋风分级,次倾斜板分离器阶段和次级旋风分级进一步处理底流,以产生次级沥青回收产物流和循环流。 次级沥青回收产物蒸汽并入并成为电路沥青产物输出流的一部分。 再循环流被并入沥青泡沫进料流中,以便通过回路再处理。
    • 3. 发明申请
    • Method of and apparatus for upgrading and gasifying heavy hydrocarbon feeds
    • 升级和气化重质烃进料的方法和装置
    • US20030116470A1
    • 2003-06-26
    • US10025996
    • 2001-12-26
    • Philip RettgerRandall GoldsteinJim Arnold
    • C10G001/04C10G069/14
    • C10G49/007Y10S585/921
    • A novel apparatus for producing sweet synthetic crude from a heavy hydrocarbon feed comprising: an upgrader for receiving said heavy hydrocarbon feed and producing a distillate fraction including sour products, and high-carbon content by-products; a gasifier for receiving the high-carbon content by-products and producing synthetic fuel gas and sour by-products; a hydroprocessing unit for receiving the sour by-products and hydrogen gas, thereby producing gas and sweet crude; and a hydrogen recovery unit for receiving said synthetic fuel gas and producing further hydrogen gas and hydrogen-depleted synthetic fuel gas, said further hydrogen gas being supplied to said hydroprocessing unit.
    • 一种用于从重烃进料生产甜的合成粗品的新型装置,包括:用于接收所述重质烃进料并产生包含酸性产物和高碳含量副产物的馏出物馏分的升级装置; 用于接收高碳含量副产物并生产合成燃料气体和酸副产物的气化器; 一种用于接收酸性副产物和氢气的加氢处理装置,从而产生气体和甜味粗品; 以及用于接收所述合成燃料气体并产生另外的氢气和贫氢合成燃料气体的氢气回收单元,所述另外的氢气被供应到所述加氢处理单元。
    • 6. 发明申请
    • Recovery of heavy minerals from a tar sand
    • 从焦油砂中回收重质矿物质
    • US20040035755A1
    • 2004-02-26
    • US10417271
    • 2003-04-17
    • Titanium Corporation Inc.
    • Robert G. Reeves
    • C10G001/04
    • B03B9/02C10G1/047Y10S75/958
    • A process for recovering heavy minerals (e.g., titanium minerals such as TiO2) from a feedstock comprising tar sands or a tar sands-derived solids fraction. The feedstock comprises bitumen and heavy minerals. The process comprises the steps of: (i) contacting the solids fraction with water at a temperature of at least about 100null F. to cause production a bituminous phase and a heavy minerals phase; and (ii) separating the heavy minerals phase from the bituminous phase. Optionally, these steps may be preceded by one or more steps used to produce a tar-sands derived solids fraction from a tar sands feedstock.
    • 从包含焦油砂或焦油砂衍生的固体部分的原料中回收重矿物(例如钛矿物如TiO 2)的方法。 原料包括沥青和重矿物。 该方法包括以下步骤:(i)在至少约100°F的温度下使固体部分与水接触,以产生沥青相和重质矿物相; 和(ii)将重质矿物相与沥青相分离。 任选地,这些步骤之前可以是用于从焦油砂原料产生焦油砂衍生的固体部分的一个或多个步骤。
    • 8. 发明申请
    • Process for the conversion of heavy charges such as heavy crude oils and distillation residues
    • 用于重质原油和蒸馏残渣转化的方法
    • US20030089636A1
    • 2003-05-15
    • US10188785
    • 2002-07-05
    • ENI S.p.A
    • Mario MarchionnaAlberto DelbiancoNicoletta PanaritiRomolo MontanariSergio RosiSebastiano Correra
    • C10B055/00C10G001/04C10G021/00
    • C10G67/0454C10G67/00C10G2300/1033C10G2300/107C10G2300/1077C10G2300/205C10G2300/206C10G2300/207C10G2300/4081C10G2300/44Y02P30/20
    • Process for the conversion of heavy charges such as heavy crude oils, tars from oil sands and distillation residues, by the combined use of the following three process units: hydroconversion with catalysts in slurry phase (HT), distillation or flash (D), deasphalting (SDA), characterized in that the three units operate on mixed streams consisting of fresh charge and recycled streams, by the use of the following steps: sending at least one fraction of the heavy charge to a deasphalting section (SDA) in the presence of hydrocarbon solvents obtaining two streams, one consisting of deasphalted oil (DAO), the other of asphalts; mixing the asphalt with a suitable hydrogenation catalyst and optionally with the remaining fraction of heavy charge not sent to the deasphalting section and sending the mixture obtained to a hydro-treatment reactor (HT) into which hydrogen or a mixture of hydrogen and H2S is charged; sending the stream containing the hydro-treatment reaction product and the catalyst in dispersed phase to one or more distillation or flash steps (D) whereby the most volatile fractions are separated, among which the gases produced in the hydro-treatment reaction; recycling at least 60% by weight, preferably at least 80%, more preferably at least 95%, of the distillation residue (tar) or liquid leaving the flash unit, containing the catalyst in dispersed phase, rich in metallic sulfides produced by demetallation of the charge and possibly coke, to the deasphalting zone.
    • 通过组合使用以下三个工艺单元,将重质原油,来自油砂和蒸馏残余物的焦油转化为重质装料的方法:用浆液相(HT),蒸馏或闪蒸(D)中的催化剂进行加氢转化,脱沥青 (SDA),其特征在于,三个单元通过使用以下步骤在由新鲜电荷和再循环流组成的混合流中操作:将至少一部分重电荷发送到脱沥青部分(SDA),存在 烃溶剂获得两股,一种由脱沥青油(DAO),另一种沥青组成; 将沥青与合适的氢化催化剂混合,并且任选地将剩余部分的重质进料混合物送入脱沥青部分,并将得到的混合物送入氢气或氢气与H 2 S的混合物的氢化反应器(HT)中; 将含有分散相中的加氢处理反应产物和催化剂的物流送至一个或多个蒸馏或快速步骤(D),由此分离出最挥发性馏分,其中在加氢处理反应中产生的气体; 回收至少60重量%,优选至少80%,更优选至少95%的蒸馏残余物(焦油)或离开闪蒸单元的液体,其含有分散相中的催化剂,富含金属硫化物,其通过脱金属 该充电并可能焦化到脱沥青区。