Tsinghua University

Boe Technology Group Co., Ltd.

Hefei Boe Display Lighting Co., Ltd.

Fude (beijing) Chemical & Industry Co., Ltd.

Huadian Coal Industry Group Co., Ltd.

Fude Chemical & Industry Co., Ltd

Funde Holding Group Co., Ltd.

Fei Wei

Yao M Wang

Guohua Luo

Yang Yang

Yi Liu

Hao Yu

Tong Wang

Zhi Yang

Jun Gao

Yao Wang

Weizhong Qian

Zhenxing Zhu

Dejun Li

Jinfu Wang

Zhifei Li

Zhi Zhu

Yong Jin

Dezheng Wang

Yinyan Xue

Xiulin Wang

Zhanwen Wang

Xiaobo Wei

Zhong Chen

Zuoru Yin

Yu Cui

Silei Sun

Chang Zhu

Shanzhi Hu

Yejia Qian

Xiaofan Huang

Xiaoping Tang

Changping Gao

Feng Hu

This disclosure relates to the technical field of carbon nanotubes, provides an ultra-long chiral carbon nanotube and a method for preparing the same. The ultra-long chiral carbon nanotube has a diameter of about 1.5 nm to 5.5 nm and has a length of about 100 mm to 650 mm, the ultra-long chiral carbon nanotube includes a double-walled carbon nanotube and a triple-walled carbon nanotube, and each layer of the ultra-long chiral carbon nanotube is semiconducting and has a helix angle greater than 10&#xb0;.

Ultra-long chiral carbon nanotube, method for preparing the same, application thereof, and high-performance photoelectric device

The present invention relates to a system and process for preparing aromatics from syngases, which has advantages of shortened flow process and reduced investment. The process comprises reforming the liquefied gas, separated dry gas with a water steam to produce carbon monoxide and hydrogen, which return, as raw materials, to the aromatization system, so that the problem of by-product utilization is solved, and the syngas unit consumption per ton of aromatic products is reduced. The problem of utilization of a dry gas as a by-product is also solved in the present invention from the perspective of recycling economy, which reduces the water consumption in the process, and conforms to the concept of green chemistry.

System and method for preparing aromatics by using syngas

A device, a system, a backlight module and a test method for simulating a light guide plate, the device for simulating a light guide plate includes: a light guide substrate layer; and an electroactive polymer layer, wherein the electroactive polymer layer is formed on the light guide substrate layer and is configured to produce a deformation according to a layout signal of dot-patterns to simulate the dot-patterns.

Device, system, backlight module and test method for simulating light guide plate

The present invention provides a fluidized bed reactor and its use for producing olefins from oxygenates, the fluidized bed reactor comprises: a reaction zone located in the lower portion of the fluidized bed reactor and comprising a lower dense phase zone and an upper riser, wherein the dense phase zone and the riser are connected with each other transitionally; a separation zone located in the upper portion of the fluidized bed reactor and comprising a settling chamber, a fast gas-solid separation means, a cyclone and a gas collecting chamber, wherein the riser extends upwardly into the separation zone and is connected at its outlet with the inlet of the fast gas-solid separation means, the fast gas-solid separation means is connected at its outlet with the inlet of the cyclone via a fast gas passage, the cyclone is connected at its outlet with the gas collecting chamber, and the gas collecting chamber is located below the reactor outlet and connected therewith; and a catalyst recycle line for recycling the catalyst from the settling chamber back to the dense phase zone, a catalyst withdrawl line for withdrawing the deactivated catalyst from the settling chamber and/or the dense phase zone to the catalyst regeneration means, and a catalyst return line for returning the regenerated catalyst from the catalyst regeneration means to the dense phase zone.

Fluidized bed reactor and process for producing olefins from oxygenates

The present application provides multistage and multilayer reactors useful for the efficient and continuous production of carbon nanotubes and methods of using the apparatus in the preparation of carbon nanotubes. In one aspect, the multistage reactors include an array of interconnected fluidized-bed reactors. The multilayer reactors include a plurality of reaction zones.

Multistage reactors for continuous production of carbon nanotubes

The present invention relates to a method for continuous production of carbon nanotubes in a nano-agglomerate fluidized bed, which comprises the following steps: loading transition metal compounds on a support, obtaining supported nanosized metal catalysts by reducing or dissociating, catalytically decomposing a carbon-source gas, and growing carbon nanotubes on the catalyst support by chemical vapor deposition of carbon atoms. The carbon nanotubes are 4&#x2dc;100 nm in diameter and 0.5&#x2dc;1000 &#x3bc;m in length. The carbon nanotube agglomerates, ranged between 1&#x2dc;1000 &#x3bc;m, are smoothly fluidized under 0.005 to 2 m/s superficial gas velocity and 20&#x2dc;800 kg/mbed density in the fluidized-bed reactor. The apparatus is simple and easy to operate, has a high reaction rate, and it can be used to produce carbon nanotubes with high degree of crystallization, high purity, and high yield.

Continuous mass production of carbon nanotubes in a nano-agglomerate fluidized-bed and the reactor

A method and apparatus for measuring the gas amounts adsorbed on a powder which directly measures pressure changes in a gas supply chamber with the use of differential pressure sensors between the gas supply chamber and a reference chamber which gas amount is maintained constant. Calculations of the gas amounts adsorbed are based on the pressure changes in a sample cell and the pressure changes in the gas supply chamber or a gas reference chamber. The method and apparatus of this invention measures the adsorption or desorption isotherm or gas uptake at constant pressure curve of a powder with, as compared with presently available measurement techniques, increased accuracy and resolution. The experimental data can be analyzed to obtain information on the surface area, pore size distribution, pore volume, pore structure and diffusion coefficient of the powder.

Method and apparatus to measure gas amounts adsorbed on a powder sample

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Beijing, China

Fei Wei