公开(公告)号：US20060196174A1

公开(公告)日：2006-09-07

申请号：US11071854

申请日：2005-03-03

Applicant: Foster Lamm ,  Thomas Vanderspurt

Inventor： Foster Lamm ,  Thomas Vanderspurt

IPC: F01N3/00

CPC classification number: F23K5/08 ,  F23K2900/05081 ,  Y02E20/344

Abstract: A fuel system for an energy conversion device includes a deoxygenator system with a reducing system and an active metal catalyst system downstream thereof. The reducing system injects a reducing agent such as hydrogen into the liquid hydrocarbon fuel which contains the dissolved oxygen. The liquid hydrocarbon fuel with the dissolved oxygen is thereby enriched with the reducing agent prior to communication to the active catalyst system which reactively consumes the free oxygen dissolved within the liquid hydrocarbon fuel.

Abstract translation: 用于能量转换装置的燃料系统包括具有还原系统的脱氧器系统和其下游的活性金属催化剂体系。 还原系统将诸如氢的还原剂注入含有溶解氧的液态烃燃料中。 具有溶解氧的液态烃燃料在与活性催化剂体系连通之前被还原剂富集，反应性地消耗溶解在液态烃燃料中的游离氧。

公开(公告)号：US20050129591A1

公开(公告)日：2005-06-16

申请号：US10736922

申请日：2003-12-16

Applicant: Di Wei ,  Thomas Vanderspurt ,  Stephen Hay ,  Wayde Schmidt ,  Timothy Obee

Inventor： Di Wei ,  Thomas Vanderspurt ,  Stephen Hay ,  Wayde Schmidt ,  Timothy Obee

IPC: A61L9/20 ,  B01D53/86 ,  B01D53/88 ,  B01J20060101 ,  B01J19/08 ,  B01J19/12 ,  B01J19/24 ,  B01J21/06 ,  B01J23/34 ,  B01J23/38 ,  B01J35/00 ,  B60H3/06

CPC classification number: A61L9/205 ,  B01D53/86 ,  B01D53/885 ,  B01D2255/802 ,  B01J19/123 ,  B01J19/2485 ,  B01J21/063 ,  B01J23/34 ,  B01J23/38 ,  B01J35/0006 ,  B01J35/004 ,  B60H3/0608 ,  B60H2003/0675 ,  B60H2003/0691 ,  F24F2003/1628

Abstract: A photocatalytic/thermocatalytic coating includes an inner layer of metal/titanium dioxide or metal oxide/titanium dioxide that is applied on a honeycomb and an outer layer of titanium dioxide or metal oxide doped titanium dioxide applied on the inner layer. The inner layer of can be gold/titanium dioxide, platinum/titanium dioxide, or manganese oxide/titanium dioxide. The outer layer of titanium dioxide or metal oxide doped titanium dioxide oxides volatile organic compounds to carbon dioxide, water, and other substances. As the outer layer is thin and porous, the contaminants in the air can diffuse through the outer layer and adsorb onto the inner layer. When photons of the ultraviolet light are absorbed by the coating, reactive hydroxyl radicals are formed that oxidize the contaminant to produce water, carbon dioxide, and other substances.

Abstract translation: 光催化/热催化涂层包括施加在蜂窝上的金属/二氧化钛或金属氧化物/二氧化钛的内层，二氧化钛或金属氧化物掺杂的二氧化钛的外层施加在内层上。 内层可以是金/二氧化钛，铂/二氧化钛或氧化锰/二氧化钛。 外层二氧化钛或金属氧化物掺杂的二氧化钛将挥发性有机化合物氧化成二氧化碳，水等物质。 由于外层薄而多孔，空气中的污染物可以扩散通过外层并吸附在内层上。 当紫外线的光子被涂层吸收时，形成反应性羟基自由基，其氧化污染物以产生水，二氧化碳和其它物质。

公开(公告)号：US20070264174A1

公开(公告)日：2007-11-15

申请号：US11803481

申请日：2007-05-15

Applicant: Rhonda Willigan ,  Thomas Vanderspurt ,  Sonia Tulyani ,  Rakesh Radhakrishnan ,  Susanne Opalka ,  Sean Emerson

Inventor： Rhonda Willigan ,  Thomas Vanderspurt ,  Sonia Tulyani ,  Rakesh Radhakrishnan ,  Susanne Opalka ,  Sean Emerson

IPC: B01J23/10 ,  B01J16/00 ,  C01F17/00

CPC classification number: B01J23/63 ,  B01J23/002 ,  B01J23/10 ,  B01J23/6567 ,  B01J35/1019 ,  B01J35/1038 ,  B01J35/1061 ,  B01J37/0009 ,  B01J37/0203 ,  B01J37/0205 ,  B01J37/03 ,  B01J37/08 ,  B01J37/18 ,  B01J2523/00 ,  B82Y30/00 ,  C01B3/16 ,  C01B2203/0283 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01G25/006 ,  C01P2004/64 ,  C01P2006/12 ,  C01P2006/14 ,  C01P2006/16 ,  Y02P20/52 ,  B01J2523/47 ,  B01J2523/69 ,  B01J2523/828 ,  B01J2523/3712 ,  B01J2523/48

Abstract: A durable catalyst support/catalyst is capable of extended water gas shift operation under-conditions of high temperature, pressure, and sulfur levels. The support is a homogeneous, nanocrystalline, mixed metal oxide of at least three metals, the first being cerium, the second being Zr, and/or Hf, and the third importantly being Ti, the three metals comprising at least 80% of the metal constituents of the mixed metal oxide and the Ti being present in a range of 5% to 45% by metals-only atomic percent of the mixed metal oxide. The mixed metal oxide has an average crystallite size less than 6 nm and forms a skeletal structure with pores whose diameters are in the range of 4-9 nm and normally greater than the average crystallite size. The surface area of the skeletal structure per volume of the material of the structure is greater than about 240 m2/cm3. The method of making and use are also described.

Abstract translation: 耐用的催化剂载体/催化剂能够在高温，高压和硫含量的条件下进行扩展的水煤气变换操作。 载体是至少三种金属的均匀的，纳米晶体的混合金属氧化物，第一种是铈，第二种是Zr，和/或Hf，第三种是重要的Ti，三种金属包含至少80％的金属 混合金属氧化物的成分和Ti的含量以混合金属氧化物的原子百分比计为5％〜45％的范围。 混合金属氧化物的平均微晶尺寸小于6nm，并且形成具有直径在4-9nm范围内且通常大于平均微晶尺寸的孔的骨架结构。 骨架结构的每体积结构的材料的表面积大于约240μm2 / cm 3。 还描述了制造和使用的方法。

公开(公告)号：US20070148084A1

公开(公告)日：2007-06-28

申请号：US11315651

申请日：2005-12-22

Applicant: Rakesh Radhakrishnan ,  Thomas Vanderspurt ,  Joseph Sangiovanni

Inventor： Rakesh Radhakrishnan ,  Thomas Vanderspurt ,  Joseph Sangiovanni

IPC: C01B3/02

CPC classification number: C01B3/042 ,  B01J19/127 ,  B01J2219/0877 ,  B01J2219/0892 ,  C01B3/501 ,  C01B13/0207 ,  C01B2203/0405 ,  C01B2203/0495 ,  Y02E60/364 ,  Y02P20/134 ,  Y02P20/135

Abstract: A solar-powered hydrogen production system directly produces hydrogen. The solar-powered hydrogen production system includes at least one concentrator, a hydrogen-rich source, a catalytic layer, and a hydrogen separation membrane. The hydrogen-rich source is positioned to receive focused sunlight collected by the concentrator and is in direct contact with the catalytic layer. The catalytic layer produces hydrogen from the hydrogen-rich source. The hydrogen separation membrane subsequently separates the hydrogen produced at the catalytic layer.

Abstract translation: 太阳能氢气生产系统直接生产氢气。 太阳能氢气生产系统包括至少一个浓缩器，富氢源，催化层和氢分离膜。 富氢源定位成接收由浓缩器收集的聚焦太阳光并与催化层直接接触。 催化层从富氢源产生氢。 氢分离膜随后分离在催化层产生的氢。

公开(公告)号：US20050180901A1

公开(公告)日：2005-08-18

申请号：US10778828

申请日：2004-02-13

Applicant: Thomas Vanderspurt ,  Harry Cordatos

Inventor： Thomas Vanderspurt ,  Harry Cordatos

IPC: F02C7/22 ,  C10G27/10 ,  C10G29/06 ,  C10G53/14 ,  C10L1/00 ,  F02C7/14 ,  F02C7/16 ,  F02C7/224 ,  F02C7/30 ,  F02M27/02 ,  F23K5/08 ,  B01J8/00

CPC classification number: C10G53/14 ,  C10G27/10 ,  C10G29/06 ,  F02C7/14 ,  F02C7/16 ,  F02C7/224 ,  F02C7/30 ,  F02M27/02 ,  F23K5/08 ,  F23K2900/05081 ,  Y02T50/675

Abstract: A fuel delivery system for a gas turbine engine includes a catalytic device for treating fuel to increase the usable cooling capability of an endothermic fuel. The catalytic device operates to treat and decompose components within in the fuel to render the fuel non-coking beyond 250° F. The catalytic device includes material that initiates reactions, and decomposition of coke forming components within the fuel to non-coke forming components within the fuel.

Abstract translation: 用于燃气涡轮发动机的燃料输送系统包括用于处理燃料以提高吸热燃料的可用冷却能力的催化装置。 催化装置用于处理和分解燃料中的组分以使燃料非焦化超过250°F。催化装置包括引发反应的物质，以及燃料内焦炭形成组分分解成非焦炭形成组分 燃料。