首页> 外文会议>NATO Advanced Study Institute on Carbon Filaments and Nanotubes >Optimizing growth conditions for carbon filaments and vapor-grown carbon fibers
【24h】

Optimizing growth conditions for carbon filaments and vapor-grown carbon fibers

机译:优化碳丝和汽化碳纤维的生长条件

获取原文
获取外文期刊封面目录资料

摘要

The production, properties and applications of vapor-grown carbon fibers (VGCF) and carbon filaments were reviewed in the course of a previous NATO ASI [1]. It is generally accepted that the growth of carbon fibers from gaseous hydrocarbons in the presence of a catalyst (VGCF) occurs as a result of the initial formation of carbon filaments or nanofibers, by a mechanism involving the dissolution and diffusion of carbon at the exposed surface of the catalyst particles and precipitation at the metal/support interfaces. In this way, the catalyst particles are carried out on top of the growing filaments [2,3]. This lengthening stage stops when the catalyst particles become covered with a carbon layer; thereafter, thickening occurs by chemical vapour deposition of pyrolytic carbon, leading to the production of VGCF exhibiting the well known "tree-trunk" structure of concentric carbon layers [4-6]. Originally, a Vapor-Solid process (V-S) was invoked, as the catalyst particles were considered to be in the solid state [7]. However, it was later recognised that, in order to account for the observed rates of fiber growth, a Vapour-Liquid-Solid (V-L-S) mechanism must be involved in the production of VGCF. Indeed, Benissad et al. [8] proposed that the catalyst particles can be molten, according to their sizes, in the temperature range where fiber lengthening occurs (1050-1100°C). More recently, Tibbetts and Balogh [9] showed that only molten particles are effective in catalyzing fiber growth. Two different methods have been developed to produce VGCF: The substrate seeding method and the floating catalyst, or fluidization seeding method [10,11]. The latter has the advantage of being a continuous process, but it produces shorter fibers (some micrometers) with smaller diameters (hundreds of nanometers) when compared to the first method (which leads to fibers several centimeters long and some micrometers in diameter).
机译:在先前的北约ASI [1]的过程中综述了汽化碳纤维(VGCF)和碳丝的生产,性质和应用。通常接受,由于碳丝或纳米纤维的初始形成,通过涉及碳纤维丝或纳米纤维在暴露的表面溶解和扩散的机制,从催化剂(VGCF)存在中,在催化剂(VGCF)存在下,在催化剂(VGCF)存在下发生碳烃(VGCF)的结果催化剂颗粒和金属/支撑界面的沉淀。以这种方式,催化剂颗粒在生长长丝的顶部进行[2,3]。当催化剂颗粒被碳层覆盖时,该延长阶段停止;此后,通过热解碳的化学气相沉积发生增稠,导致vGCF的产生,该VGCF表现出同心碳层的众所周知的“树干”结构[4-6]。最初,调用蒸汽固体方法(V-S),因为催化剂颗粒被认为是固态[7]。然而,稍后认识到,为了考虑观察到的纤维生长速率,蒸气液固体(V-L-S)机制必须参与VGCF的产生。确实,Benissad等。 [8]提出,催化剂颗粒可以根据它们的尺寸来熔融,在纤维延长发生(1050-1100℃)的温度范围内。最近,Tibbetts和Balogh [9]表明,仅熔融颗粒在催化纤维生长方面是有效的。已经开发出两种不同的方法以产生VGCF:衬底播种方法和浮催化剂,或流化接种方法[10,11]。后者具有作为连续过程的优点,但是与第一方法相比,它产生较短的直径(数百纳米)的较短纤维(一些微米)(这导致纤维数厘米长,直径为一些微米)。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号