公开(公告)号：US07691908B2

公开(公告)日：2010-04-06

申请号：US11198864

申请日：2005-08-04

申请人： Romuald Bokotko ,  Francis V. Hanson ,  Jan Hupka

发明人： Romuald Bokotko ,  Francis V. Hanson ,  Jan Hupka

IPC分类号： B01F3/08

CPC分类号： B09C1/00 ,  B01F17/0021 ,  B01F17/0064

摘要： A crude oil simulant is disclosed that is an emulsion of an organic continuous phase, an aqueous dispersed phase, and an emulsifier. To enhance the biodegradability rate of the simulant various strains of bacteria can be added to the aqueous phase. Nutrients can be added to the aqueous phase to increase activity of the bacteria. The components of the simulant of the invention can be mixed under high shear conditions such as 1,000-12,000 reciprocal minutes. The emulsion based oil simulants can be prepared on-site and can be readily tailored to simulant a wide variety of crude oils under various conditions.

摘要翻译： 公开了一种原油模拟物，其是有机连续相，水性分散相和乳化剂的乳液。 为了提高模拟物的生物降解率，可以将各种细菌菌株加入到水相中。 可以向水相中加入营养物以增加细菌的活性。 本发明的模拟物的组分可以在高剪切条件下混合，例如1,000-12,000相互分钟。 基于乳液的油模拟物可以现场制备，并且可以容易地定制成在各种条件下模拟各种各样的原油。

公开(公告)号：US4035430A

公开(公告)日：1977-07-12

申请号：US708955

申请日：1976-07-26

申请人： Francis G. Dwyer ,  Francis V. Hanson ,  Albert B. Schwartz

发明人： Francis G. Dwyer ,  Francis V. Hanson ,  Albert B. Schwartz

IPC分类号： C07C1/20 ,  C10G3/00

CPC分类号： C07C1/20 ,  C10G3/49 ,  C10G3/60 ,  C07C2529/40 ,  C10G2300/1037 ,  C10G2300/4006 ,  C10G2300/703 ,  C10G2400/02 ,  C10G2400/30 ,  Y02P20/584 ,  Y02P30/20 ,  Y10S585/934

摘要： The conversion of methanol to gasoline boiling products in a plurality of sequentially arranged catalyst beds comprising a dehydration catalyst followed by a special class of crystalline zeolite conversion catalyst is described wherein the dehydration catalyst life is prolonged and durene formed in the process is recycled to the zeolite catalyst conversion step.

摘要翻译： 描述了在包括脱水催化剂和特殊类型的结晶沸石转化催化剂的多个顺序排列的催化剂床中将甲醇转化为汽油沸点产物，其中脱水催化剂寿命延长，并且在该方法中形成的杜烯再循环至沸石 催化剂转化步骤。

公开(公告)号：US4337143A

公开(公告)日：1982-06-29

申请号：US155257

申请日：1980-06-02

申请人： Francis V. Hanson ,  Jan D. Miller ,  Alex G. Oblad

发明人： Francis V. Hanson ,  Jan D. Miller ,  Alex G. Oblad

IPC分类号： C10G1/00 ,  C10G1/02 ,  C10G1/04

CPC分类号： C10G1/02 ,  C10G1/006 ,  C10G1/047

摘要： A novel thermal process for recovering hydrocarbon and other products from tar sand. The process includes blending tar sand with a bitumen-rich concentrate while heating the same with a hot, burnt sand. The products are recovered by passing the combined feed through a fluidized bed and selectively controlling the temperature and residence times to obtain predetermined ratios of products. Coked sand residue from the fluidized bed is burned to produce the hot, burnt sand, a portion of which may be recycled to provide heat to the fluidized bed. Coked sand may also be recycled into a known, hot-water, caustic separation process where it synergistically improves the separation efficiency of the hot-water, caustic separation process.

摘要翻译： 一种用于从焦油砂中回收烃类和其他产品的新型热处理方法。 该方法包括将焦油砂与富含沥青的浓缩物混合，同时用热的烧焦砂加热。 通过使组合的进料通过流化床并选择性地控制温度和停留时间以获得预定比例的产物来回收产物。 来自流化床的焦化砂渣被燃烧以产生热的燃烧的砂，其一部分可以被再循环以向流化床提供热量。 焦化砂还可以循环到已知的热水苛性碱分离方法中，其中它协同地提高了热水，苛性碱分离过程的分离效率。

公开(公告)号：US07528097B2

公开(公告)日：2009-05-05

申请号：US11198006

申请日：2005-08-04

申请人： Francis V. Hanson ,  John V. Fletcher ,  Alyssa M. Redding ,  Christopher Olson ,  Jumpol Jaturapitpornsakul

发明人： Francis V. Hanson ,  John V. Fletcher ,  Alyssa M. Redding ,  Christopher Olson ,  Jumpol Jaturapitpornsakul

IPC分类号： C10M169/04

CPC分类号： C10L1/14 ,  C10L1/003 ,  C10L1/02 ,  C10L1/1832 ,  C10M169/04 ,  C10M2207/0203 ,  C10M2207/026 ,  C10M2207/401 ,  C10N2230/64 ,  Y10S210/922 ,  Y10S210/923 ,  Y10S210/924 ,  Y10S210/925

摘要： A composition and method for a non-emulsion crude oil simulant containing biodegradable oil, and a terpene is disclosed and described. Biodegradable oils such as canola oil, cottonseed oil, and soybean oil can be particularly beneficial for use in connection with these oil simulants. Terpenes such as d-limonene can be included to provide oil simulant compositions which exhibit good oil simulant properties. Additives such as photochromic dyes, food dyes, food-grade antioxidants, microorganisms, and nutrients can also be used. These non-emulsion based oil simulants can be readily tailored and adjusted to approximate relevant properties of a specific target fluid for use in assessing oil spill response, containment, clean-up of equipment, percolation, and/or spill behavior.

摘要翻译： 公开和描述了含有可生物降解油和萜烯的非乳化原油模拟物的组合物和方法。 生物可降解油如卡诺拉油，棉籽油和大豆油对于与这些油模拟物相关的使用可能是特别有利的。 可以包括萜烯如d-柠檬烯以提供具有良好的油模拟性质的油模拟组合物。 还可以使用光致变色染料，食品染料，食品级抗氧化剂，微生物和营养物等添加剂。 这些基于乳液的油模拟剂可以容易地定制和调整以接近特定目标流体的相关性质，以用于评估漏油响应，遏制，设备清理，渗透和/或溢出行为。

公开(公告)号：US4409090A

公开(公告)日：1983-10-11

申请号：US344324

申请日：1982-02-01

申请人： Francis V. Hanson ,  Jan D. Miller ,  Alex G. Oblad

发明人： Francis V. Hanson ,  Jan D. Miller ,  Alex G. Oblad

IPC分类号： C10G1/00 ,  C10G1/02 ,  C10G1/04

CPC分类号： C10G1/02 ,  C10G1/006 ,  C10G1/047

摘要： A combination physical separation process and thermal fluidized bed process for recovering products from tar sands. The process includes initially separating a portion of the sand from the tar sand through a physical separation process, yielding a bitumen-rich concentrate. The bitumen-rich concentrate is introduced into a heated fluidized bed and products are recovered and distilled into their respective fractions. A coked sand is removed from the fluidized bed and placed into a combustor where the carbonaceous residue on the sand is burned to produce a hot burnt sand, a portion of which may be recycled to provide heat to the bitumen-rich concentrate in the fluidized bed. The coked sand and a certain fraction of the distilled products may be recycled to the physical separation process to improve the separation efficiency thereof.

摘要翻译： 用于从焦油砂中回收产物的组合物理分离过程和热流化床方法。 该方法包括首先通过物理分离方法将一部分砂与焦油砂分离，产生富含沥青的浓缩物。 将富含沥青的浓缩物引入加热的流化床中，将产物回收并蒸馏成各自的馏分。 将焦化的砂从流化床中移出并放置在燃烧器中，其中在砂上的碳质残余物被燃烧以产生热的烧砂，其一部分可以再循环以向流化床中的富含沥青的浓缩物提供热量 。 焦化砂和一定馏分的蒸馏产物可以再循环到物理分离过程中以提高其分离效率。

公开(公告)号：US4207248A

公开(公告)日：1980-06-10

申请号：US970299

申请日：1978-12-18

申请人： Stephen A. Butter ,  Francis V. Hanson ,  Howard S. Sherry

发明人： Stephen A. Butter ,  Francis V. Hanson ,  Howard S. Sherry

IPC分类号： B01J29/46 ,  C07C9/14 ,  C10G2/00 ,  C07C1/04 ,  C07C1/16

CPC分类号： C10G2/334 ,  B01J29/46 ,  B01J2229/26 ,  B01J2229/42

摘要： A method is disclosed for the conversion of synthesis gas to a liquid hydrocarbon product having a boiling point range maximum of less than 400.degree. F. at a 90% overhead and being a predominantly olefinic product. The novel method involves contacting synthesis gas with a single particle catalyst containing cobalt, a crystalline acidic aluminosilicate zeolite having a silica-to-alumina ratio of at least 12, a pore size greater than about 5 Angstrom units, and a constraint index of about 1 to 12, and a siliceous matrix. The catalyst does not contain promoters and the alumina content of the matrix is severely restricted.

摘要翻译： 公开了一种在90％塔顶馏分将合成气转化为沸点范围最大小于400°F的液体烃产物并且主要是烯烃产物的方法。 该新方法包括使合成气与含有钴的单一颗粒催化剂接触，二氧化硅与氧化铝之比至少为12的结晶酸性硅铝酸盐沸石，孔径大于约5埃单位，约束指数约为1 至12，和硅质基质。 催化剂不含助催化剂，并且基体的氧化铝含量受到严格限制。