公开(公告)号：US5133877A

公开(公告)日：1992-07-28

申请号：US677738

申请日：1991-03-29

申请人： Cheryl K. Rofer ,  Steven J. Buelow ,  Richard B. Dyer ,  Joseph D. Wander

发明人： Cheryl K. Rofer ,  Steven J. Buelow ,  Richard B. Dyer ,  Joseph D. Wander

IPC分类号： A62D3/00 ,  A62D3/20 ,  A62D3/34 ,  A62D3/35 ,  A62D101/06 ,  A62D101/20 ,  A62D101/22 ,  A62D101/26 ,  A62D101/28 ,  A62D101/40 ,  B01J3/00 ,  B01J19/24 ,  B09C1/02 ,  B09C1/08 ,  C02F1/02 ,  C02F11/08

CPC分类号： A62D3/20 ,  A62D3/35 ,  B01J19/243 ,  B01J3/008 ,  B09C1/02 ,  B09C1/08 ,  C02F1/025 ,  C02F11/086 ,  A62D2101/06 ,  A62D2101/26 ,  A62D2101/28 ,  B01J2219/00063 ,  B01J2219/00065 ,  B01J2219/00103 ,  B01J2219/00126 ,  B01J2219/00135 ,  B01J2219/00166 ,  Y02P20/544 ,  Y10S149/124 ,  Y10S210/908 ,  Y10S210/909

摘要： A process for destruction of hazardous materials in a medium of supercritical water without the addition of an oxidant material. The harzardous material is converted to simple compounds which are relatively benign or easily treatable to yield materials which can be discharged into the environment. Treatment agents may be added to the reactants in order to bind certain materials, such as chlorine, in the form of salts or to otherwise facilitate the destruction reactions.

摘要翻译： 在没有添加氧化剂材料的情况下，在超临界水介质中破坏有害物质的过程。 将这种杂质转化为相对良性或易于处理的简单化合物，以产生可排放到环境中的材料。 可以将处理剂加入到反应物中以便以盐的形式结合某些物质，如氯，或以其他方式促进破坏反应。

公开(公告)号：US6111064A

公开(公告)日：2000-08-29

申请号：US325442

申请日：1999-06-03

申请人： Charles J. Maurer ,  Gordon Shaw ,  Vicky S. Smith ,  Steven J. Buelow ,  William Tumas ,  Veronica Contreras ,  Ronald J. Martinez

发明人： Charles J. Maurer ,  Gordon Shaw ,  Vicky S. Smith ,  Steven J. Buelow ,  William Tumas ,  Veronica Contreras ,  Ronald J. Martinez

IPC分类号： C08G63/78 ,  C08F6/00 ,  C08F2/00

CPC分类号： C08G63/78

摘要： A process is disclosed for the preparation of a polyester polymer or polyester copolymer under superatmospheric pressure conditions in a pipe or tubular reaction under turbannular flow conditions. Reaction material having a glycol equivalents to carboxylic acid equivalents mole ratio of from 1.0:1 to 1.2:1, together with a superatmospheric dense gaseous medium are fed co-currently to the reactor. Dicarboxylic acid and/or diol raw materials may be injected into any of the reaction zones in the process during operation to achieve the overall desired mole ratio balance. The process operates at temperatures of from about 220.degree. C. to about 320.degree. C., with turbannular flow achieved before the polymer product and gas exit the reactor process. The pressure in the reaction zones can be in the range from 15 psia to 2500 psia. A polymer product having a DP of a greater than 40, more preferably at least about 70, is achieved by the transfer of water from the reacting material polymer melt to the gaseous medium in the reactor.