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Reaction unit and process of continuous preparation of carbon nano-tube

A carbon nanotube and reaction device technology, which is applied in the field of reaction devices for preparing carbon nanotubes, can solve the problems of high energy consumption, difficult operation of the device, low conversion rate of raw material gas, etc., and achieves low energy consumption and conversion rate of raw material gas. high effect

Inactive Publication Date: 2006-11-15
CHENGDU ORGANIC CHEM CO LTD CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] There are four kinds of processes in the catalytic cracking method, namely fixed bed process, ebullated bed process, floating bed process and moving bed process. Each process has its own advantages and disadvantages. For example, the fixed bed process has simple equipment and flexible and convenient operation. The ability to process catalysts is small, and it is only suitable for the screening of catalysts or the preparation of a small amount of carbon nanotubes; the ebullated bed process can process a large amount of catalysts, and can also obtain a good yield of carbon nanotubes, but the conversion rate of raw gas is low, and the energy consumption is high. The operation is difficult; the floating bed process has great limitations, and is only suitable for ferrocene, carbonyl iron and other catalyst systems that are easy to gasify and decompose; the moving bed process has obvious advantages in the preparation of multi-walled carbon nanotubes with design specifications. Advantages, but due to the problems of temperature gradient and moving speed, it is not suitable for continuous preparation of single-walled carbon nanotubes

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  • Reaction unit and process of continuous preparation of carbon nano-tube
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  • Reaction unit and process of continuous preparation of carbon nano-tube

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Embodiment 1

[0030] Example 1: In the schematic figure 1 Among them, 1 is the catalyst container, which is used to store fresh catalyst, 2 is the catalyst quantitative tank, which controls the amount of catalyst put into the tray each time, 3 is the reaction tower, 4 is the crude product outlet, 5 is the reaction tail gas outlet, and 6 is the raw material Gas inlet, 7 is a valve, 8 is a tray, 9 is a connecting mechanism, through which the tray is connected with mechanical equipment to control the movement of the tray, 10 is a scraper, responsible for transferring the material on the tray to the next tray, 11 is the upper gate of the catalyst quantitative tank, 12 is the lower gate of the catalyst quantitative tank, 13 represents the first tray, 14 represents the second tray, 15 represents the third tray, 16 represents the fourth tray, 20 is the first group of trays, and 21 is the second group of trays.

[0031] Combine below figure 1 Explain the process of continuously preparing carbon n...

Embodiment 2

[0035] Embodiment 2: The continuous preparation of multi-walled carbon nanotubes of different specifications can also be realized by using a tower reactor. Such as figure 2 As shown, the upper tower reactor 30 is placed on the lower reaction tower 31 to form a combined reaction tower, so that the activation of the catalyst and the growth of carbon nanotubes can be carried out at different positions simultaneously, and multi-walled carbon nanotubes of different specifications can be realized. Continuous production of tubes. Among the combined tower reactors, the upper tower reactor 30 is used to activate the catalyst, and the lower tower reactor 31 is used to prepare carbon nanotubes. The two tower reactors are connected through a catalyst container 1 and a catalyst quantitative tank 2 . After the catalyst is activated by the upper tower reactor 3 (), it falls into the catalyst container 1 of the lower tower reactor 31, is quantified by the catalyst quantitative tank 2, and ...

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Abstract

The invention discloses a reaction device and process for preparing carbon nanotubes, which are particularly suitable for continuous preparation of single-wall carbon nanotubes or multi-wall carbon nanotubes. The technical solution of the invention is to adopt a reaction device for continuously preparing carbon nanotubes, the reaction device is a tower reactor, and simultaneously provide a process for continuously preparing carbon nanotubes by using the device. The technical scheme of the present invention adopts a reaction device for continuously preparing carbon nanotubes, the reaction device is a tower reactor, and the tower reactor is composed of a catalyst container, a catalyst quantitative tank, a reaction tower, a crude product outlet, a tail gas outlet, and a feed gas inlet. It consists of six parts, and there are horizontally arranged trays in the reaction tower. In the tower reactor provided by the present invention, the catalyst can reach the reaction zone at the fastest speed and leave the reaction zone at the fastest speed, the movement of the catalyst is completed under the action of mechanical force, and the raw material gas flow rate can be very low, so the energy consumption is low , Raw material gas conversion rate is high.

Description

technical field [0001] The invention relates to a reaction device and process for preparing carbon nanotubes, which are particularly suitable for continuous preparation of single-wall carbon nanotubes or multi-wall carbon nanotubes. Background technique [0002] So far, there have been many methods for preparing carbon nanotubes, but there are only three main methods, namely arc method, laser ablation method and catalytic cracking method. The arc method is the earliest method for preparing carbon nanotubes, and it is still the current method for preparing carbon nanotubes with high crystallinity. Laser ablation is currently the main method for preparing single-walled carbon nanotubes, but the yield is at the milligram level, which is difficult to scale up industrially. The catalytic cracking method uses nano-scale iron, cobalt or nickel as a catalyst, and low-carbon hydrocarbons, carbon oxides or carbon monoxide as a raw material gas, and a catalytic cracking reaction occur...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B31/02
Inventor 瞿美臻周固民赵社涛范众杰孙静于作龙
Owner CHENGDU ORGANIC CHEM CO LTD CHINESE ACAD OF SCI
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