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    • 3. 发明申请
    • Mine site oil sands processing
    • 矿场油砂加工
    • US20050134102A1
    • 2005-06-23
    • US10738089
    • 2003-12-18
    • George CymermanJuhan CowardJim McTurk
    • George CymermanJuhan CowardJim McTurk
    • E02F1/00E02F7/00E21C41/26
    • E21C41/26E02F1/00E02F7/00E21C41/31
    • A process line comprising a combination of mobile and relocatable equipment units is provided at an oil sand mine site. The process line may comprise: a mobile shovel; a mobile bin and double roll crusher; a relocatable conveyor belt extending along the mine face; a relocatable slurry preparation assembly, such as a secondary crusher and jet pump; a pipeline; and a relocatable desanding circuit of separators. The process line conducts the following steps: mining the oil sand; crushing it to conveyable size; conveying it to a slurry preparation location; further crushing it to slurrying size and mixing it with heated water to produce a pumpable, aerated oil sand slurry; transporting and conditioning the slurry in the pipeline; desanding it to produce a product comprising bitumen and water and tailings; depositing tailings in a retention facility; and removing the product from the mine site in a pipeline.
    • 在油砂矿场提供了包括移动和可重定位设备单元的组合的生产线。 工艺线可以包括:移动铲; 移动式垃圾桶和双辊破碎机; 沿着矿面延伸的可重新定位的输送带; 可重新定位的浆料制备组件,例如二次破碎机和喷射泵; 一条管道 和分离器的可重新定位的去电路。 流程线进行以下步骤:开采油砂; 将其粉碎至可输送尺寸; 将其输送到浆料制备位置; 进一步粉碎成浆料大小并与加热水混合,生产可泵送的充气油砂浆料; 运输和调节管道中的浆料; 将其除砂以生产包含沥青和水和尾矿的产品; 将尾矿放置在保留设施中; 并从管道中的矿场移除产品。
    • 5. 发明申请
    • RELOCATABLE OIL SAND SLURRY PREPARATION SYSTEM
    • 可靠的油砂浆制备系统
    • US20070068769A1
    • 2007-03-29
    • US11162819
    • 2005-09-23
    • George CymermanKhaled ObaiaStewart Johnson
    • George CymermanKhaled ObaiaStewart Johnson
    • C10C3/08B01D11/02C10G17/00
    • C10G31/08C10G1/047C10G2300/805Y10S241/38
    • A relocatable oil sand slurry preparation system is provided for preparing an aqueous oil sand slurry amenable to pipeline conveyance while producing minimum overall rejects, comprising (a) a relocatable rotary digester for slurrying oil sand and water and digesting oil sand lumps to form a pumpable slurry, the rotary digester having a feed end for receiving oil sand and water, a slurrying chamber comprising a plurality of lifters for slurrying the oil sand and water, and a trommel screen end for screening out oversize rejects from the oil sand slurry which falls through the trommel screen; and (b) a relocatable rejects recirculation unit operably associated with the rotary digester for receiving oversize rejects and delivering the rejects back to the rotary digester for further digestion. In a preferred body, relocatable oil sand slurry preparation system further comprises a rejects crusher for crushing oversize rejects prior to delivering rejects back to the rotary digester.
    • 提供一种可重新定位的油砂浆料制备系统,用于制备适于管道输送的含水油砂浆料,同时产生最小的总排渣量,其包括(a)用于使油砂和水浆化的可重新定位的旋转蒸煮器,并消化油砂块以形成可泵送的浆料 具有用于接收油砂和水的进料端的旋转式蒸煮器,包括多个用于使油砂和水浆化的提升器的调浆室和用于筛选来自油砂浆的大型废料的转筛筛 转筛屏; 和(b)可重新定位的废弃循环单元,其可操作地与旋转蒸煮器相关联,用于接收过大的废料并将废弃物返回到旋转消化器进行进一步消化。 在优选的主体中,可重新定位的油砂浆料制备系统还包括用于在将废弃物返回到旋转蒸煮器之前破碎过大的废料的废料破碎机。
    • 6. 发明申请
    • Low energy process for extraction of bitumen from oil sand
    • 从油砂中提取沥青的低能量过程
    • US20060249431A1
    • 2006-11-09
    • US11123031
    • 2005-05-06
    • George CymermanJonathan SpenceYin NgRobert Siy
    • George CymermanJonathan SpenceYin NgRobert Siy
    • C10G1/04
    • C10G1/047
    • An improved low energy extraction process for recovering bitumen from oil sand whereby essentially all of the thermal energy input for processing the oil sand takes place at the slurry mixing step as opposed to at both the slurry mixing step and the slurry flooding step. Mined oil sand is mixed with sufficient hot slurry water to produce an oil sand slurry having a density in the preferred range of about 1.50 g/cc to about 1.60 g/cc and a temperature in the preferred range of about 40° C. to about 55° C., more preferably greater than about 43° C. The oil sand slurry is conditioned, preferably by pumping it through a pipeline for a sufficient length of time, and then flooded with cold flood water to produce a diluted slurry having a density in the range of about 1.4 g/cc to about 1.5 g/cc and a temperature generally below 40° C. and typically in the range of about 30° C. to about 35° C. The diluted slurry is introduced into a gravity separation vessel where bitumen froth is recovered.
    • 一种用于从油砂中回收沥青的改进的低能量提取方法,因此在浆料混合步骤中与浆料混合步骤和浆料淹没步骤相反,基本上所有用于加工油砂的热能输入都发生。 将精制油砂与足够的热浆水混合以产生密度在约1.50g / cc至约1.60g / cc的优选范围内且在约40℃至约优选范围内的温度的油砂浆料 55℃,更优选大于约43℃。将油砂浆料调节,优选通过将其泵送通过管道足够长的时间,然后用冷洪水充满水以产生具有密度 在约1.4g / cc至约1.5g / cc的范围内,通常温度低于40℃,通常在约30℃至约35℃的范围内。将稀释的浆液引入重力分离 收集沥青泡沫的容器。
    • 7. 发明授权
    • Staged settling process for removing water and solids from oils and extraction froth
    • 从油和提取泡沫中去除水和固体的分阶段沉降过程
    • US06746599B2
    • 2004-06-08
    • US09877260
    • 2001-06-11
    • George CymermanPat DouganTom TranJim LorenzCorey Mayr
    • George CymermanPat DouganTom TranJim LorenzCorey Mayr
    • C10G104
    • C10G1/047C10G1/045
    • Diluent-diluted bitumen froth containing bitumen and naphtha diluent, hydrocarbons, water, sand and fines (collectively “dilfroth”) is fed into a vapor-tight gravity settler (‘splitter’) and temporarily retained to produce a bottom layer of tails comprising sand and middlings, a rag layer of discrete three-dimensional structures, each comprising hydrocarbons contained in a skin of fines, and a top layer of hydrocarbons containing small droplets of water and fines (‘raw dilbit’). The flux in the splitter is less than 6 m3/h of dilfroth fed per m2 of horizontal cross-sectional rag area. The in-coming dilfroth is fed directly into the splitter middlings. Demulsifier is added to the overflow stream of raw dilbit and the mixture is subjected to prolonged settling in a vapor-tight polisher tank, to produce polished dilbit containing less than 1.0 wt. % water and 0.3 wt. % solids. The splitter underflow tails, containing less than 15 wt. % bitumen, is mixed with additional diluent to raise the diluent/bitumen ratio to 4:1 to 10:1 and is gravity settled in a vapor-tight scrubber. Scrubber overflow, mostly diluent containing residual bitumen stripped from the tails, is recycled to the splitter. In concept, the sand is first separated from the bitumen in the stripper. The substantially sand-free bitumen can then feasibly be treated with chemical demulsifier and subjected to prolonged settling in the polisher to reduce water and fines contents to low levels. Bitumen lost with the splitter tails is recovered in the scrubber using a high concentration of diluent. The scrubber overflow of bitumen and diluent is recycled to the stripper to conserve diluent.
    • 含有沥青和石脑油稀释剂,碳氢化合物,水,沙子和细粉(统称为“稀释剂”)的稀释稀释的沥青泡沫进料到气密重力沉降器(“分离器”)中并暂时保留以产生包含砂的尾部底层 和中间物,分散的三维结构的碎布层,每层包含细粉表皮中含有的碳氢化合物,以及含有小水滴和细粉(“未稀释”)的顶层烃。 分流器中的通量小于每m 2水平横截面抹布面积进给的稀释度小于6m 3 / h。 进来的dilfroth直接进入分流器中。 将破乳剂加入到原料稀释液的溢流中,并将混合物在气密的抛光槽中长时间沉降,以产生含有小于1.0wt。 %水和0.3wt。 固体%。 分流器下溢尾部含有少于15wt。 %的沥青与另外的稀释剂混合,将稀释剂/沥青比提高到4:1至10:1,并将其重力沉降在气密的洗涤器中。 洗涤剂溢出,主要是从尾部剥离的含有残留沥青的稀释剂,被再循环到分离器。 在概念上,沙子首先与汽提塔中的沥青分离。 然后可以用化学破乳剂可靠地处理基本上无砂的沥青,并在抛光机中经过长时间的沉降,以减少水分并将内容物细粉至低水平。 使用高浓度的稀释剂在洗涤器中回收分配器尾部损失的沥青。 沥青和稀释剂的洗涤器溢流被再循环到汽提塔中以保存稀释剂。
    • 9. 发明授权
    • Method for treating bitumen froth with high bitumen recovery and dual quality bitumen production
    • 用高沥青回收和双重质量沥青生产处理沥青泡沫的方法
    • US08114274B2
    • 2012-02-14
    • US12177050
    • 2008-07-21
    • Kevin MoranGeorge CymermanTom Tran
    • Kevin MoranGeorge CymermanTom Tran
    • C10G21/00
    • C10G1/045C10G2300/201C10G2300/308C10G2300/802
    • A process for removing contaminants, namely water and particulate solids, from hydrocarbon diluent-diluted bitumen froth (“dilfroth”) is provided to produce hydrocarbon diluent-diluted bitumen (“dilbit”), comprising subjecting the dilfroth to gravity settling in a primary settler to produce an overflow stream of primary raw dilbit, comprising bitumen containing water and some fine solids, and an underflow stream of primary tails, comprising solids, water and residual bitumen; removing the overflow stream of primary raw dilbit and subjecting it to gravity settling in a clarifier vessel for sufficient time to produce an overflow first stream of cleaned dilbit and an underflow stream of clarifier sludge; diluting the primary tails with hydrocarbon diluent and subjecting the diluted primary tails to gravity settling in a secondary settler to produce an overflow second stream of cleaned dilbit and an underflow stream of secondary tails; and removing the clarifier sludge and diluting the clarifier sludge with a hydrocarbon diluent, if necessary, and subjecting the clarifier sludge to gravity separation to produce a third stream of cleaned dilbit.
    • 提供从烃稀释剂稀释的沥青泡沫(“dilfroth”)除去污染物(即水和颗粒固体)的方法以产生烃稀释剂稀释的沥青(“稀释”),其包括将稀释剂重力沉降在初级沉降器 以产生主要原料稀释物的溢流,其包含含有水和一些细固体的沥青和包含固体,水和残余沥青的主要尾部的下溢流; 除去主要稀释物的溢流并使其重力沉降在澄清器容器中足够的时间以产生净化稀释物的溢流第一流和澄清池污泥的下溢流; 用碳氢化合物稀释剂稀释主要尾部,并将稀释的主要尾部重新沉淀在第二沉降器中以产生清洗的稀释物的溢出的第二流和次级尾部的下溢流; 如果需要,用烃稀释剂除去澄清池污泥并稀释澄清池污泥,并对澄清池污泥进行重力分离,产生第三清洗稀释物流。