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公开(公告)号：WO2016004503A1
公开(公告)日：2016-01-14
申请号：PCT/CA2014/050653
申请日：2014-07-09
发明人： GARNER, William Nicholas , MOETAMED-SHARIATI, Saba , MILANI, Ali , VIGUIE, Guillaume , GINGRAS, Elizaveta , PUN, Sam
CPC分类号： C08J11/02 , C08J2395/00 , C10G1/042 , C10G1/045 , C10G2300/1033 , C10G2300/4081 , C10G2300/44
摘要： A system and method is described for separating solvent from a solvent-diluted bitumen feedstream from oil sands froth treatment processing. A distillation tower receives a first feedstream portion intermediate the tower at or above the solvent bubble point and a second feedstream portion at an upper end of the tower at temperature at about or lower than the dew point of bitumen. A bitumen liquid product is recovered from a tower bottom and a solvent product is recovered from an upper end as recycle solvent to the upstream froth treatment process. Prior to splitting into first and second portions, the feedstream may be flashed, the underflow forming the tower feedstream while the overhead vapor is available directly as recycle solvent. The two feedstream portions and temperatures thereof enable solvent recovery without the use of a reflux or a bottom reboiler.
摘要翻译： 描述了一种用于从溶剂稀释的沥青进料流中分离溶剂的系统和方法，其来自油砂沫处理处理。 蒸馏塔在溶解气泡点处或上方接收塔的中间的第一进料流部分，在塔的上端处的第二进料流部分处于大约或低于沥青露点的温度。 从塔底回收沥青液体产物，将溶剂产物作为再循环溶剂从上端回收至上游泡沫处理工艺。 在分解成第一和第二部分之前，可以将进料流闪蒸，形成塔进料流的下溢，而塔顶蒸气可直接作为循环溶剂使用。 两个进料流部分和温度使得能够在不使用回流或底部再沸器的情况下进行溶剂回收。
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公开(公告)号：WO2015149181A1
公开(公告)日：2015-10-08
申请号：PCT/CA2015/050265
申请日：2015-04-02
IPC分类号： C10G1/04 , B01D17/025 , B03B9/02
CPC分类号： B03B9/02 , B01D21/0036 , B01D21/267 , B01D2221/04 , B03D2203/006 , C10G1/04
摘要： Froth settling vessels (FSU) taught herein utilize a classifier feedwell to pre-classify a solvent diluted feedstream into a less dense bitumen and solvent overflow and a more dense water, solids and asphaltene agglomerate underflow. The overflow and underflow are discharged into the FSU at axially spaced apart locations, forming a substantially non-turbulent interface therebetween. The majority of the bitumen and solvent in the overflow rises to the top, following discharge above the interface, and the majority of the dense components fall to the bottom, following discharge below the interface. Minor amounts of less dense components in the underflow and more dense components in the overflow rise and fall substantially unimpeded through the interface. The FSU can be operated at flux rates exceeding conventional FSU as the risk of breakthrough is minimized as a result of the pre-classification and discharge to discrete locations within the FSU.
摘要翻译： 本文教导的泡沫沉降容器（FSU）利用分级器供料口将溶剂稀释的进料流预分类成不太致密的沥青和溶剂溢流以及更致密的水，固体和沥青质附聚物下溢。 溢流和下溢在轴向间隔开的位置被排放到FSU中，在它们之间形成基本上非湍流的界面。 沥青中的大部分沥青和溶剂在接口上方排放后上升到顶部，并且大多数致密组分在接口下面放电后下降到底部。 下溢中较少密度较低的组分和溢流中更致密的组分通过界面基本上无阻碍地上升和下降。 FSU可以以超过常规FSU的通量速率运行，因为预分类和排放到FSU内的离散位置的结果，突破的风险最小化。
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公开(公告)号：WO2015143561A1
公开(公告)日：2015-10-01
申请号：PCT/CA2015/050233
申请日：2015-03-26
摘要： A process for polishing a dilbit product produced from a conventional paraffinic froth treatment process results in a polished dilbit product stream having minimal impurities, including water, mineral and non-mineral solids and water, therein. The dilbit product from a froth separation unit (FSU) is fed into a High G- force separator for removal of impurities therefrom. Typically, the impurities in the initial dilbit product are less than about 0.5wt% and can be reduced as taught herein to at least an order of magnitude lower. Multiple stages of polishing can be performed.
摘要翻译： 用于抛光由常规石蜡泡沫处理工艺生产的稀释产物的方法产生在其中具有最小杂质（包括水，矿物和非矿物固体和水）的抛光稀释产物流。 来自泡沫分离单元（FSU）的稀释产物进料到高G力分离器中以从中除去杂质。 通常，初始稀释产物中的杂质小于约0.5wt％，并且如本文所教导的那样可降低至少一个数量级。 可以进行多个抛光阶段。
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公开(公告)号：WO2013124744A2
公开(公告)日：2013-08-29
申请号：PCT/IB2013/001143
申请日：2013-02-22
发明人： STALDER, John, L.
IPC分类号： E21B43/24
CPC分类号： E21B43/2406
摘要： This present disclosure describes methods and systems related to SAGD injection and/or production wells that utilize flow distribution control devices. Additionally, methods and systems using limited vertical spacing separating the wells are described. These methods and systems improve steam assisted gravity drainage (SAGD) oil production, reduce SAGD start-up time and costs, and improve overall SAGD performance.
摘要翻译： 本公开描述了使用流量分配控制装置的与SAGD注入和/或生产井有关的方法和系统。 另外，描述了使用有限垂直间隔分离井的方法和系统。 这些方法和系统改善了蒸汽辅助重力排水（SAGD）的生产，降低了SAGD的启动时间和成本，并提高了SAGD的整体性能。
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公开(公告)号：WO2013124742A1
公开(公告)日：2013-08-29
申请号：PCT/IB2013/000783
申请日：2013-02-22
发明人： STALDER, John, L.
CPC分类号： E21B43/2406
摘要： Methods and systems relate to steam assisted gravity drainage (SAGD) utilizing well pairs that are at least initially in fluid communication through drilled bores toward their toe ends. At least one of a horizontal injection well and horizontal production well of such a well pair includes a hooked length toward toe ends of each other connecting said injection well and said production well. The methods and systems improve SAGD oil production, reduce SAGD start-up time and costs, and improve overall SAGD performance.
摘要翻译： 方法和系统涉及使用井对的蒸汽辅助重力排水（SAGD），这些井至少首先通过钻孔朝向其趾端流体连通。 这种井对的水平喷射井和水平生产井中的至少一个包括连接所述喷射井和所述生产井的彼此相对于趾端的钩形长度。 方法和系统改善了SAGD的石油生产，降低了SAGD的启动时间和成本，并提高了SAGD的整体性能。
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6.发明申请APPARATUS AND METHOD FOR ENHANCING EXTRACTION OF BITUMEN FROM BITUMEN FROTH 审中-公开装置和方法，用于增强从白炽灯提取铋的方法
公开(公告)号：WO2016095009A1
公开(公告)日：2016-06-23
申请号：PCT/CA2014/051223
申请日：2014-12-17
摘要： The present system increases the settling rate of asphaltenes and 2 mineral solids in bitumen froth by contacting the bitumen froth feedstream fed to a 3 froth separation unit with an aggregate-enhancing stream comprising aggregate-4 enhancing particles capable of forming larger agglomerates in the feedstream.
摘要翻译： 本系统通过将进料到3泡沫分离单元的沥青泡沫进料流与包含能够在进料流中形成较大附聚物的聚集体-4增强颗粒的聚集体增强流接触来增加沥青泡沫中沥青质和2种矿物固体的沉降速率。
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公开(公告)号：WO2016077908A1
公开(公告)日：2016-05-26
申请号：PCT/CA2014/051099
申请日：2014-11-18
CPC分类号： C10G1/04
摘要： A bitumen-containing froth is treated with a paraffinic solvent by adding the froth to the solvent in two or more additions prior to separation in a froth settling unit. The first addition of froth results in an S:B ratio which causes precipitation of asphaltenes in the bitumen. Maltenes are dissolved in the solvent. The dissolved maltenes shift the solubility parameter of the solvent. The second or more additions of the balance of the froth to the shifted solvent result in an overall S:B ratio resulting in precipitation of the asphaltenes and dissolving of the maltenes. The volumes of the two or more additions of froth can be adjusted to meet different objectives. Solvent requirements can be reduced, a target asphaltene content in the final product can be altered or both. Further, the target asphaltene content in the product can be designed so as not to foul downstream heating processes.
摘要翻译： 将含有沥青的泡沫用石蜡溶剂处理，在泡沫沉降装置中分离之前，通过在两次或多次添加剂中将泡沫添加到溶剂中。 第一次添加泡沫会导致S：B比例，导致沥青中沥青质的沉淀。 马尔顿人溶解在溶剂中。 溶解的麦芽糖转移溶剂的溶解度参数。 将泡沫的平衡的第二次或更多次添加到转移的溶剂中导致总体S：B比，导致沥青质的沉淀和麦芽糖的溶解。 可以调节两次或更多次添加泡沫的体积以满足不同的目的。 可以降低溶剂要求，最终产品中的目标沥青质含量可以改变，或两者都可以改变。 此外，产品中的目标沥青质含量可以设计成不会污染下游加热过程。
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8.发明申请SINGLE-STAGE BACKUP TRANSITIONAL ARRANGEMENT FOR PARTIALLY OFFLINE MULTI-STAGE FROTH SEPARATION UNITS 审中-公开部分离线多级分离单元的单级备份过渡安排
公开(公告)号：WO2016008024A1
公开(公告)日：2016-01-21
申请号：PCT/CA2014/050666
申请日：2014-07-14
IPC分类号： B03D1/02
CPC分类号： B03D1/02 , B03D1/1406 , B03D2203/006
摘要： A method for temporarily bypassing an offline oilsand froth settling unit (FSU) of a multi-stage FSU system in the event of failure of the offline FSU while maintaining operability, maximizing separation performance and minimizing propagation of the disturbance to other systems. The offline FSU is isolated and the underflow stream of the remaining operational stage is split between a reject stream directing solids and water to a tailing solvent recovery unit and a solvent- enriched recycle stream for comingling with bitumen froth as a feedstream to the inlet to the operational FSU. Solvent addition stream is re-routed from interstage addition to bypass the reject tailings stream and join the recycle stream, aiding in continued FSU operation for separation of maltenes and solvent from rejected solids and water. Dilbit product is recovered from the online FSU.
摘要翻译： 在保持可操作性的同时，在离线FSU发生故障的情况下临时绕过多级FSU系统的离线油和泡沫沉降单元（FSU）的方法，最大限度地提高分离性能并最小化扰动到其他系统的传播。 离线FSU被隔离，并且剩余操作阶段的下溢流在将固体和水引导到拖尾溶剂回收单元的废料流和用于将作为进料流的沥青泡沫与作为进料流的溶剂富集的再循环流分离到至 操作FSU。 溶剂添加物流从阶段添加物重新排列到旁路废弃尾矿物流并加入循环物流，有助于持续的FSU操作，以将麦芽酮和溶剂与被污染的固体和水分离。 Dilbit产品从在线FSU恢复。
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公开(公告)号：WO2015143556A1
公开(公告)日：2015-10-01
申请号：PCT/CA2015/050226
申请日：2015-03-23
CPC分类号： B65D88/54
摘要： An apparatus and methodology for storing bitumen froth comprising a fluidized bottom, froth first feed holding tank for maintaining effective tank capacity while reducing overall solid bed build up at side walls and minimizing sloughing of solids to the froth discharge outlet. Froth is fed to the tank through one or more feed inlets located between the froth outlet and side walls for fluidizing settling solids. The feed inlets urge solids to settle in sub-beds about the feed inlets, the height of which that manifests adjacent the side walls being less that some design threshold height; if not, then successive feed inlets are located between the side walls and the precious feed inlets to build further sub-beds that have a height at the wall that is less than the threshold height.
摘要翻译： 一种用于储存沥青泡沫的装置和方法，包括流化底部的泡沫第一进料容纳罐，用于保持有效的罐容量，同时减少在侧壁处积累的总固体床，并最大限度地减少固体到泡沫排出口的脱落。 泡沫通过位于泡沫出口和侧壁之间的一个或多个进料入口进料到罐中，用于使沉降固体流体化。 进料入口迫使固体物质围绕进料入口沉入子床，其高度靠近侧壁表现出较小的设计阈值高度; 如果没有，则连续的进料入口位于侧壁和珍贵的进料入口之间，以构建在壁处具有小于阈值高度的高度的另外的床。
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公开(公告)号：WO2014189614A1
公开(公告)日：2014-11-27
申请号：PCT/US2014/032044
申请日：2014-03-27
申请人： TOTAL E&P CANADA, LTD. , CONOCOPHILLIPS CANADA RESOURCES CORP. , CONOCOPHILLIPS SURMONT PARTNERSHIP , STALDER, John, L.
IPC分类号： E21B43/24
CPC分类号： E21B43/305 , E21B43/2406
摘要： The present disclosure relates to a particularly effective well configuration that can be used for SAGD and other steam based oil recovery methods. A central wellpad originates injector and/or producer wells, arranged in a radial pattern, and either or both provided with multilateral wells, thus effectively expanding the coverage.
摘要翻译： 本公开涉及可用于SAGD和其它基于蒸汽的油回收方法的特别有效的井构造。 中心井垫起源于放射状图案的注射器和/或生产井，以及提供多边井的两者或两者，从而有效地扩大覆盖范围。
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