公开(公告)号：US06521003B2

公开(公告)日：2003-02-18

申请号：US09794314

申请日：2001-02-27

Applicant: Jacobus Swanepoel ,  Ruan Lombaard ,  Julian Charles Mast-Ingle

Inventor： Jacobus Swanepoel ,  Ruan Lombaard ,  Julian Charles Mast-Ingle

IPC: C10L300

CPC classification number: C10B19/00 ,  B01J8/125 ,  B01J8/1836 ,  B01J8/1881 ,  B01J19/088 ,  B01J2208/0053 ,  B01J2219/00155 ,  B01J2219/0218 ,  B01J2219/0227 ,  B01J2219/0236 ,  B01J2219/0809 ,  B01J2219/0886 ,  B01J2219/0894 ,  B01J2219/185 ,  C01B32/00 ,  C10J3/18 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/1238

Abstract: A process and an installation for treating solid carbonaceous material comprises heating the material to a temperature of about 1800° C. or higher, by means of a non-transfer arc generated plasma flame. This causes components of, or present in, the carbonaceous material to be gasified and thus to be separated or removed from any residual solid material as a hot gas phase, with residual solid material being obtained as a product. The installation comprises a vertical shaft non-transfer arc plasma reactor comprising an upper preheating zone (14) an intermediate reaction zone (16) in which at least one non-transfer arc plasma generator or reactor (40) is located and a lower cooling zone (18).

Abstract translation: 用于处理固体碳质材料的方法和装置包括通过非转移电弧产生的等离子体火焰将材料加热至约1800℃或更高的温度。 这使得碳质材料中的组分或气体物质被气化，因此被作为热气相从作为热气相的任何残余固体材料中分离或除去，得到剩余的固体物质作为产物。 该装置包括垂直轴非转移电弧等离子体反应器，其包括上部预热区（14）中间反应区（16），其中至少一个非转移电弧等离子体发生器或反应器（40）位于其中，下部冷却区 （18）。

公开(公告)号：US06495731B1

公开(公告)日：2002-12-17

申请号：US09489838

申请日：2000-01-24

Applicant: Remy Cordier ,  Thierry Ferlin ,  Guy Tackels ,  Thierry Mine

Inventor： Remy Cordier ,  Thierry Ferlin ,  Guy Tackels ,  Thierry Mine

IPC: C10L300

CPC classification number: F23N1/002 ,  F23N2021/10 ,  F23N2037/08 ,  Y10T137/2509

Abstract: A method of regulating the calorific power of a stream of gaseous fuel of the fossil-gas type, comprising a predominant fuel gas, denoted “A” and flowing in a pipe. This regulation is performed, at least partly, by controlled addition of at least one fuel gas called having a calorific power greater than that of “A” into the stream. The subject of the invention is also its apparatus for implementation and its applications.

Abstract translation: 一种调节化石气体类型的气体燃料流的发热量的方法，其包括表示为“A”并在管道中流动的主要燃料气体。 该调节至少部分地通过将被称为具有大于“A”的发热量的至少一种燃料气体的控制添加到流中来进行。 本发明的主题也是其实现装置及其应用。

公开(公告)号：US06607569B1

公开(公告)日：2003-08-19

申请号：US09623753

申请日：2000-10-13

Applicant: Yasuki Namiki ,  Masatoshi Kobayashi ,  Akira Kidoguchi ,  Hidenobu Itoh ,  Masataka Hiraide ,  Kunihiro Imada ,  Kenji Inokuchi

Inventor： Yasuki Namiki ,  Masatoshi Kobayashi ,  Akira Kidoguchi ,  Hidenobu Itoh ,  Masataka Hiraide ,  Kunihiro Imada ,  Kenji Inokuchi

IPC: C10L300

CPC classification number: C10G1/008

Abstract: Disclosed is a method of estimating the outflow amount for each component of the effluent of a coal liquefying reactor consisting of vessel type reactors (16a, 16b, 16c) operated under a high temperature and a high pressure. The outflow amount for each component of the effluent is assumed, and the gas-liquid equilibrium composition of the mixture of the composition within the reaction vessel is calculated. Further, the volume flow rates of the gaseous phase and the liquid phase within the reaction vessel are calculated, and the residence time (&tgr;1G, &tgr;2G, &tgr;3G), (&tgr;1S, &tgr;2S, &tgr;3S) of each of the gaseous phase and the liquid phase is calculated on the basis of the gas hold-up within the reaction vessel calculated on the basis of the volume flow rate and the empirical formula. The outflow amount for each component of the effluent is calculated on the basis of the residence time (&tgr;1, &tgr;, . . . &tgr;n) within the reaction vessel, the inflow amount for each component of the influent into the reactor, and the primary irreversible reaction rate formula derived from a specified coal liquefying reaction model. The effluent amount for each component assumed first is compared with the effluent amount for each component obtained by calculation, and the series of calculations are repeated until these two effluent amounts for each component coincide with each other within a predetermined range of error.

Abstract translation: 公开了一种估计由在高温高压下操作的容器型反应器（16a，16b，16c）组成的煤液化反应器的流出物的每个组分的流出量的方法。 假设流出物的每个组分的流出量，并且计算反应容器内的组合物的混合物的气液平衡组成。 此外，计算反应容器内的气相和液相的体积流量，并且每个气相和液相的停留时间（tau1G，tau2G，tau3G），（tau1S，tau2S，tau3S） 是基于基于体积流量和经验公式计算的反应容器内的气体滞留量来计算的。 基于反应容器内的停留时间（tau1，tau，...，taun）计算出流出物的每个组分的流出量，流入反应器的每个组分的流入量和初级不可逆 来自特定煤液化反应模型的反应速率公式。 将首先假设的每个组分的流出物量与通过计算获得的每个组分的流出物量进行比较，并重复该系列计算，直到每个组分的两个流出物量在预定的误差范围内彼此一致。

公开(公告)号：US06680006B2

公开(公告)日：2004-01-20

申请号：US10015783

申请日：2001-12-17

Applicant: Pierre D. Chantal

Inventor： Pierre D. Chantal

IPC: C10L300

CPC classification number: C01B3/386 ,  C01B2203/0261 ,  C01B2203/1052 ,  C01B2203/1082 ,  C01B2203/1241 ,  Y02P20/52

Abstract: A process is described for converting gaseous lower alkanes, e.g. methane, into synthesis gas. In the process, a mixture of the alkanes and oxygen is subjected to partial oxidation in a reaction zone in the presence of a catalyst comprising a mesoporous aluminosilicate solid catalyst having the structure of MCM-41 with a silica-to-alumina ratio of about 5:1 to 1000:1 pore diameters of at least 5 Å and a nickel loading of about 5-20% by weight. This provides a high level of conversion of the alkanes as well as a high selectivity to formation of carbon monoxide and hydrogen.

Abstract translation: 描述了用于转化气态低级烷烃的方法，例如 甲烷，进入合成气。 在此过程中，烷烃和氧气的混合物在催化剂的存在下在反应区域中进行部分氧化，该催化剂包含具有约5的二氧化硅与氧化铝比的MCM-41结构的介孔硅铝酸盐固体催化剂 ：1至1000:1孔径至少为5埃，镍负载量为约5-20重量％。 这提供了高水平的烷烃转化率以及对一氧化碳和氢气的形成的高选择性。

公开(公告)号：US06419477B1

公开(公告)日：2002-07-16

申请号：US09672890

申请日：2000-09-28

Applicant: Barnett Joel Robinson

Inventor： Barnett Joel Robinson

IPC: C10L300

CPC classification number: F23J7/00 ,  C10L10/02 ,  F23J2215/10

Abstract: A method of improving fuel efficiency in combustion chambers, for simultaneously enhancing combustion of hydrocarbon fuels while inhibiting nitrogen oxidation. A mixture of vaporous metallic compounds is introduced into the flame zone of a combustion chamber, such that this mixture is held by gases in the flame zone prior to and during the combustion of the fuel, and the mixture is thereby ionized prior to or during the combustion. The ionized mixture of compounds contains platinum, rhodium, rhenium, molybdenum, aluminum and ruthenium.

Abstract translation: 一种提高燃烧室燃料效率的方法，用于同时增强烃燃料的燃烧同时抑制氮氧化。 将气态金属化合物的混合物引入燃烧室的火焰区域中，使得该混合物在燃料燃烧之前和燃烧期间在火焰区域内由气体保持，并且混合物在之前或之后被电离 燃烧。 化合物的电离混合物包含铂，铑，铼，钼，铝和钌。