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    • 4. 发明申请
    • Process For Recovering Solvent From Ashphaltene Containing Tailings Resulting From A Separation Process
    • 从分离过程产生的含尾沥青中回收溶剂的方法
    • US20100126906A1
    • 2010-05-27
    • US12530078
    • 2008-03-27
    • Ken Sury
    • Ken Sury
    • C10G73/02
    • C10G1/045
    • A process for recovering paraffinic solvent from tailings produced in the treatment of bitumen froth comprising introducing the tailings into a tailings solvent recovery unit (TSRU), the TSRU having internals, and distributing the tailings over the internals. An inert gas or steam is then introduced below the internals and above the liquid pool for enhancing the vaporization of the contained solvent. Solvent is vaporized from asphaltene agglomerates. In one embodiment, the process is affected in the absence of mechanical means used to substantially break up asphaltene agglomerates or to prevent the agglomeration of asphaltene. In another aspect, the process comprises introducing the tailings into a first TSRU as described above and then into a second TSRU operated at a lower pressure. In another aspect, internals are optionally present and steam or inert gas is injected in the liquid pool.
    • 一种从处理沥青泡沫产生的尾矿中回收石蜡溶剂的方法,包括将尾矿引入尾矿溶剂回收装置(TSRU)中,TSRU具有内部结构,并将尾矿分配在内部件上。 然后将惰性气体或蒸汽引入到内部和液体池之上,以增强所含溶剂的蒸发。 溶剂从沥青质附聚物中蒸发。 在一个实施方案中,该方法在没有用于基本上分解沥青质附聚物的机械装置或者防止沥青质的团聚的情况下受到影响。 在另一方面,该方法包括将尾矿引入如上所述的第一TSRU中,然后进入在较低压力下操作的第二TSRU。 在另一方面,任选地存在内件,并且将蒸汽或惰性气体注入到液体池中。
    • 6. 发明授权
    • Cold dense slurrying process for extracting bitumen from oil sand
    • 用于从油砂中提取沥青的冷稠浆料加工工艺
    • US6007708A
    • 1999-12-28
    • US943283
    • 1997-10-03
    • Geoff AllcockRobert SiyJonathan SpenceKen Sury
    • Geoff AllcockRobert SiyJonathan SpenceKen Sury
    • B03D1/02C10G1/04
    • B03D1/02C10G1/047B03D1/1456
    • Average grade oil sand is mixed with water to produce a low temperature (20-35.degree. C.), dense (1.4-1.65 g/cc) slurry. The slurry is pumped through a pipeline for sufficient time to condition it. Air is injected into the slurry after the last pump. The slurry density is adjusted to about 1.5 g/cc by adding flood water near the end of the pipeline. The slurry is introduced into a primary separation vessel slurry as it is introduced into the (PSV), excess air is vented from the PSV and a hot water underwash is used to heat the froth produced. Slurry loading to the PSV is greater than about 4.78 tonnes of oil sand/hour/square meter to reduce velocity gradient in the fluid in the vessel. Bitumen froth is recovered. When fed low grade oil sand, the process is modified by adding flotation aid chemicals to the slurry in the pipeline and subjecting the PSV tailings and middlings to secondary recovery with agitation and aeration in a secondary separation vessel.
    • 将平均级油砂与水混合以产生低温(20-35℃),致密(1.4-1.65g / cc)浆料。 浆料通过管道被泵送足够的时间来调节它。 最后一次泵将空气注入浆料。 通过在管道末端附近添加洪水,将浆料密度调节至约1.5g / cc。 当浆料被引入到(PSV)中时,将浆料引入初级分离容器浆料中,从PSV排出多余的空气,并使用热水洗涤剂来加热所产生的泡沫。 装载到PSV的泥浆大于约4.78吨油砂/小时/平方米,以减少船舶流体中的速度梯度。 沥青泡沫被回收。 当加入低等级​​油砂时,通过向管道中的浆料中加入浮选助剂化学物质,并在二次分离容器中搅拌和通气使PSV尾矿和中等二次回收物进行改性。