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    • 2. 发明授权
    • Steam plasma torch
    • 蒸汽等离子火炬
    • US08742284B2
    • 2014-06-03
    • US11979631
    • 2007-11-06
    • Heng-Yi LiChin-Ching TzengLieh-Chih Chang
    • Heng-Yi LiChin-Ching TzengLieh-Chih Chang
    • B23K9/00
    • H05H1/34H05H2001/3468H05H2001/3484
    • A steam plasma torch includes a anode in the form of a nozzle, a first body for receiving the anode, a flow swirler mounted between the anode and the rod type cathode for inducing vorticity into working gas flow, an insulator connected to the first body, a second body connected to the insulator and formed with a thread, an adjusting element formed with a thread engaged with the thread of the second body, a collet fit in the adjusting element and a cathode in the form of a rod fit in the collet. A gap between the anode and cathode is adjusted when the adjusting element is rotated relative to the second body.
    • 蒸汽等离子体焰炬包括呈喷嘴形式的阳极,用于接收阳极的第一主体,安装在阳极和棒状阴极之间的用于将涡流引入工作气体流中的流量旋流器,连接到第一主体的绝缘体, 连接到绝缘体并形成有螺纹的第二主体,形成有与第二主体的螺纹接合的螺纹的调节元件,配合在调节元件中的夹头和装配在夹头中的杆形式的阴极。 当调节元件相对于第二主体旋转时,调节阳极和阴极之间的间隙。
    • 9. 发明授权
    • Direct current steam plasma torch and method for reducing the erosion of electrodes thereof
    • 直流蒸汽等离子体焰炬及减少其电极侵蚀的方法
    • US08530780B2
    • 2013-09-10
    • US13548812
    • 2012-07-13
    • Deng-Lian LinChin-Ching Tzeng
    • Deng-Lian LinChin-Ching Tzeng
    • B23K10/00
    • H05H1/3405
    • A DC steam plasma torch includes front, middle and rear sections. The front section includes a first amount and a first electrode attached to the first amount, thus defining co-axial first internal and external coolant channels. The middle section includes a second mount and a second electrode co-axially connected to the second mount, thus defining co-axial second internal and external coolant channels. The rear section includes an insulating transient element connected to the second electrode, a window frame connected to the insulating transient element and a window provided in the window frame. A first swirl generator is provided between the first and second sections to receive primary working gas and generating a swirl in the same. A second swirl generator is provided between the middle and rear sections to receive auxiliary working gas and generating a swirl in the same.
    • 直流蒸汽等离子炬包括前部,中部和后部。 前部包括第一量和连接到第一量的第一电极,从而限定同轴的第一内部和外部冷却剂通道。 中间部分包括同轴地连接到第二安装件的第二安装件和第二电极,从而限定同轴的第二内部和外部冷却剂通道。 后部包括连接到第二电极的绝缘瞬态元件,连接到绝缘瞬态元件的窗框和设置在窗框中的窗口。 第一涡旋发生器设置在第一和第二部分之间以接收初级工作气体并在其中产生涡流。 第二涡旋发生器设置在中间部分和后部之间以接收辅助工作气体并在其中产生涡流。
    • 10. 发明申请
    • Method for Making Dimethyl Ether by Reactive-Distillation
    • 通过反应蒸馏制备二甲醚的方法
    • US20120232311A1
    • 2012-09-13
    • US13044271
    • 2011-03-09
    • Cheng-Ting HsiehHow-Ming LeeKuo-Chao LiangChin-Ching Tzeng
    • Cheng-Ting HsiehHow-Ming LeeKuo-Chao LiangChin-Ching Tzeng
    • C07C41/09
    • B01D3/009C07C41/09Y02P20/127C07C43/043
    • Disclosed is a method for making dimethyl ether by reactive distillation. The method provides a reactive distillation tower with a top, a bottom, and rectification, reaction and stripping zones defined therein. The top of the reactive distillation tower is retained at 25° C. to 40° C. while the bottom of the reactive distillation tower is retained at 84.6° C. to 170° C. Each of the rectification, reaction and stripping zones includes several sieving trays. The reaction zone of the reactive distillation tower is filled with catalyst. The pressure in the reactive distillation tower is lower than 8.0 bars. Methanol is introduced into the reactive distillation tower so that the methanol travels from the reaction zone toward the bottom for contact with the catalyst to provide a top stream and a bottom stream. The top stream includes dimethyl ether. The bottom stream includes water and a remaining portion of the methanol. Finally, the dimethyl ether is collected in the top of the reactive distillation tower. The purity of the collected dimethyl ether is higher than 99%.
    • 公开了通过反应蒸馏制备二甲醚的方法。 该方法提供了反应蒸馏塔,其中限定了顶部,底部和精馏,反应和汽提区。 反应蒸馏塔的顶部保持在25℃至40℃,而反应蒸馏塔的底部保持在84.6℃至170℃。每个精馏,反应和汽提区包括几个 筛分托盘 反应蒸馏塔的反应区用催化剂填充。 反应蒸馏塔中的压力低于8.0巴。 将甲醇引入反应蒸馏塔中,使得甲醇从反应区向底部移动以与催化剂接触以提供顶部流和底部流。 顶级流包括二甲醚。 底部流包括水和甲醇的剩余部分。 最后,将二甲醚收集在反应蒸馏塔的顶部。 收集的二甲醚的纯度高于99%。