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1. 发明申请

US20080105622A1 COATED GAS BUBBLES FOR RECOVERY OF HYDROCARBON 审中-公开
标题翻译：用于石油烃回收的包覆气体泡沫
公开(公告)号：US20080105622A1
公开(公告)日：2008-05-08
申请号：US11850533
申请日：2007-09-05
申请人： KEVIN MORAN , JAN CZARNECKI
发明人： KEVIN MORAN , JAN CZARNECKI
IPC分类号： B32B1/00 , B05D1/18 , B01D35/00 , B03D1/02
CPC分类号： C10G1/047 , B01D17/0205 , B01D17/0208 , B03D1/006 , B03D1/008 , B03D1/02 , B03D2203/006 , Y10T428/2991
摘要： A coated gas bubble for recovering oil from oil-containing samples is provided, comprising a gas bubble and a coating mixture comprising a hydrophobic coating agent and a coating promoting additive, wherein the coating promoting additive is present in an amount sufficient to promote the substantially continuous coating of the gas bubble with the hydrophobic coating agent. A method for forming such coated gas bubbles and a method for recovering oil from oil-containing samples using coated gas bubbles is further provided.
摘要翻译：提供了一种用于从含油样品中回收油的涂覆气泡，其包括气泡和包含疏水涂层剂和涂层促进添加剂的涂料混合物，其中所述涂料促进添加剂以足以促进基本连续的量存在用疏水涂层剂涂覆气泡。还提供了一种用于形成这种涂覆气泡的方法以及使用涂覆气泡从含油样品中回收油的方法。

2. 发明申请

US20150247094A1 METHODS FOR SEPARATING A FEED MATERIAL DERIVED FROM A PROCESS FOR RECOVERING BITUMEN FROM OIL SANDS 审中-公开
标题翻译：用于分离从用于从油层中回收铋的方法获得的进料的方法
公开(公告)号：US20150247094A1
公开(公告)日：2015-09-03
申请号：US14713511
申请日：2015-05-15
申请人： KEVIN MORAN , Jacques DOIRON
发明人： KEVIN MORAN , Jacques DOIRON
IPC分类号： C10G1/04
CPC分类号： C10G1/045 , B03D1/02 , B03D2203/006 , C10G2300/4081 , C10G2300/44 , C10G2300/802
摘要： Separation methods for producing an extract and a raffinate from a solvent extraction feed material, wherein the feed material is derived from a process for recovering bitumen from oil sands. The methods may include producing an intra-stage recycle component from an overflow zone of a solvent extraction stage and recycling the intra-stage recycle component to the solvent extraction stage, and/or the methods may include providing an underflow component withdrawal rate for a solvent extraction stage other than a final solvent extraction stage which is greater than an underflow component withdrawal rate for the final solvent extraction stage.
摘要翻译：用于从溶剂萃取原料生产提取物和萃余液的分离方法，其中所述进料是从油砂中回收沥青的方法得到的。所述方法可以包括从溶剂萃取阶段的溢流区产生阶段内再循环组分，并将该阶段内再循环组分再循环到溶剂萃取阶段，和/或该方法可以包括为溶剂提供下溢成分萃取速率萃取阶段除了最终溶剂萃取阶段之外，其大于最终溶剂萃取阶段的底流成分萃取速率。

3. 发明申请

US20100012555A1 METHOD FOR TREATING BITUMEN FROTH WITH HIGH BITUMEN RECOVERY AND DUAL QUALITY BITUMEN PRODUCTION 失效
标题翻译：用高二甲苯回收和双质量生产生产白炽灯的方法
公开(公告)号：US20100012555A1
公开(公告)日：2010-01-21
申请号：US12177050
申请日：2008-07-21
申请人： KEVIN MORAN , GEORGE CYMERMAN , TOM TRAN
发明人： KEVIN MORAN , GEORGE CYMERMAN , TOM TRAN
IPC分类号： F26B5/08
CPC分类号： C10G1/045 , C10G2300/201 , C10G2300/308 , C10G2300/802
摘要： 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.
摘要翻译：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。

4. 发明申请

US20100243534A1 SILICATES ADDITION IN BITUMEN FROTH TREATMENT 审中-公开
标题翻译：硅胶加热处理
公开(公告)号：US20100243534A1
公开(公告)日：2010-09-30
申请号：US12411793
申请日：2009-03-26
申请人： YIN MING SAMSON NG , BRIAN ALLEN KNAPPER , KEVIN MORAN , GEORGE JIRO HIRASAKI , CLARENCE A. MILLER , TIANMIN JIANG
发明人： YIN MING SAMSON NG , BRIAN ALLEN KNAPPER , KEVIN MORAN , GEORGE JIRO HIRASAKI , CLARENCE A. MILLER , TIANMIN JIANG
IPC分类号： C10G1/04
CPC分类号： C10G1/047 , C10G1/04
摘要： A method for processing a bitumen froth comprising bitumen, water and solids including fine solids for reducing the solids concentration in diluted bitumen is provided comprising diluting the bitumen froth with a hydrocarbon diluent to form a dilfroth; adding a sufficient amount of a silicate to the dilfroth to cause a substantial amount of fine solids to associate with the water instead of the diluted bitumen; and allowing the diluted bitumen to separate from the water containing the substantial amount of fine solids to produce a dilbit having less than 3 percent by weight solids.
摘要翻译：提供一种处理包含沥青，水和固体的沥青泡沫的方法，包括用于降低稀释沥青中固体浓度的细固体，包括用烃稀释剂稀释沥青泡沫以形成稀释剂; 向稀释剂中加入足够量的硅酸盐以使大量的细小固体与水而不是稀释的沥青缔合; 并且使稀释的沥青与含有大量细固体的水分离以产生具有小于3重量％固体的稀释物。

5. 发明申请

US20170335200A1 PROCESS FOR RECOVERING BITUMEN FROM FROTH TREATMENT TAILINGS 有权
公开(公告)号：US20170335200A1
公开(公告)日：2017-11-23
申请号：US15184625
申请日：2016-06-16
申请人： KEVIN MORAN
发明人： KEVIN MORAN
IPC分类号： C10G1/04
CPC分类号： C10G1/047 , C10G1/045
摘要： A method for processing a froth treatment tailings separated from a bitumen froth produced in a process for recovering bitumen from oil sand ore, includes subjecting the froth treatment tailings to a first solvent extraction process to produce a first extract including bitumen, and a first raffinate, subjecting the first raffinate to a separation process to produce a fine mineral material fraction including fine solid mineral material having a particle size less than 44 microns and a coarse mineral material fraction including a coarse mineral material having a particle size equal to or greater than 44 microns, subjecting the coarse mineral material fraction to a froth flotation process to produce a heavy mineral concentrate and a coarse mineral material tailings, and subjecting the heavy mineral concentrate to a second solvent extraction process to produce a second extract including bitumen and a second raffinate including a debitumenized heavy mineral concentrate.

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