GB/T 38432-2019 English PDF

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GB/T 38432-2019: Particle - Gas-solid reaction measurement - Micro fluidized bed method
Status: Valid

Standard ID	USD	BUY PDF	Lead-Days	Standard Title (Description)	Status
GB/T 38432-2019	359	Add to Cart	4 days	Particle - Gas-solid reaction measurement - Micro fluidized bed method	Valid

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GB/T 39990   GB/T 39193   GB/T 21649.2   GB/T 45322.1   GB/T 38431   

Basic data

Standard ID: GB/T 38432-2019 (GB/T38432-2019)
Description (Translated English): Particle - Gas-solid reaction measurement - Micro fluidized bed method
Sector / Industry: National Standard (Recommended)
Classification of Chinese Standard: A28
Classification of International Standard: 19.120
Word Count Estimation: 18,117
Date of Issue: 2019-12-31
Date of Implementation: 2020-03-01
Issuing agency(ies): State Administration for Market Regulation, China National Standardization Administration

GB/T 38432-2019: Particle - Gas-solid reaction measurement - Micro fluidized bed method

---This is a DRAFT version for illustration, not a final translation. Full copy of true-PDF in English version (including equations, symbols, images, flow-chart, tables, and figures etc.) will be manually/carefully translated upon your order.
Particle--Gas-solid reaction measurement--Micro fluidized bed method ICS 19.120 A28 National Standards of People's Republic of China Determination of particulate gas-solid reaction by micro fluidized bed method Published on December 31,.2019 2020-03-01 Implementation State Administration of Market Supervision and Administration Issued by the National Standardization Management Committee

Contents

Foreword Ⅲ Introduction IV 1 Scope 1 2 Terms and definitions 1 3 Principle 1 4 Test device composition 4 5 Reagents or materials 5 6 Test Method 6 7 Test report 6 Appendix A (informative appendix) Gas flow characteristics in a micro-fluidized bed 7 Appendix B (informative appendix) Test Case of Micro Fluidized Bed Method Graphite Combustion 9 Reference 13

Foreword

This standard was drafted in accordance with the rules given in GB/T 1.1-2009. This standard is proposed and managed by the National Technical Committee for Particle Characterization and Sorting and Screen Standardization (SAC/TC168). This standard was drafted by. Institute of Process Engineering, Chinese Academy of Sciences, Shenyang University of Chemical Technology, Shenzhen Defang Nanotechnology Co., Ltd., China Institute of Test Technology, Southwest Chemical Research and Design Institute Co., Ltd., Institute of Chemistry, China Institute of Test Technology, Huazhong University of Science and Technology, Harbin Institute of Technology, Shanxi Institute of Coal Chemistry, Chinese Academy of Sciences, Zhangjiagang Jiushun Energy Technology Co., Ltd., Shanghai Tilun Vacuum Technology Co., Ltd., Beijing University of Science and Technology, China Aviation Manufacturing Technology Research Institute, Shandong University, China University of Petroleum (Beijing), Chongqing University, Beijing Zhong Kejiechuang Energy Technology Co., Ltd. The main drafters of this standard. Xu Guangwen, Yue Junrong, Wang Fang, Shang Weili, Li Zhaojun, Zhou Lan, Yang Jiebin, Wang Shaonan, Han Zhennan, Zeng Xi, Founder, Yu Jian, Liu Xuejing, Yao Hong, Sun Shaozeng, Han Yizhuo, Zhu Qingkai, Shen Lu, Guo Zhancheng, Cui Xiangzhong, Dong Yuping, Sun Guogang, Zheng Zhong, Yin Xiang.

Introduction

Gas-solid reaction is a kind of reaction widely used in process industry, and its process is affected by chemical reaction and transmission. Research Response The nature, reaction mechanism, and calculation of reaction kinetic parameters are the foundation of process industry science and technology, and also an important content of testing science and technology. Therefore, the micro-fluidized bed method is used in this standard to test gas-solid reactions involving particulate reactants or catalysts. The concentration curve of the gas component released or generated by the chemical reaction that occurs under the constant temperature reaction condition with time can be obtained. The time required to complete the reaction, the conversion rate and reaction rate at any reaction time, and the reaction activation energy for the formation of gas components can also be studied accordingly Reaction characteristics, analysis of product laws, speculation of reaction mechanism. Determination of particulate gas-solid reaction by micro fluidized bed method

1 Scope

This standard specifies the characteristics of gas-phase products in gas-solid reactions involving particulate reactants or catalysts using a micro-fluidized bed reactor. Test methods, including principles, test device composition, reagents or materials, test methods and test reports. This standard applies to gas-solid reactions involving or involving gaseous materials. Note. This standard method provides raw data for the study of gas-solid reaction, analysis of reaction mechanism, calculation of reaction kinetic parameters, etc. using a micro-fluidized bed reactor Test method.

2 Terms and definitions

The following terms and definitions apply to this document. 2.1 Fluidized bed reactor Use gas or liquid to pass through the granular solid layer to put the solid particles in a suspended motion state, and perform the gas-solid phase reaction process or liquid Reactor for solid phase reaction process. 2.2 Microfluidizedbedreactor A fluidized bed reactor with an inner diameter not greater than 20 mm and loaded with an appropriate amount of fluidizing medium. Note. Refer to Appendix A for gas flow characteristics in the micro-fluidized bed. 2.3 Pulse-injection feed of particles A small amount of fine particles are injected into the micro fluidized bed reactor under preset conditions with gas at a high speed Note 1. The amount of injected particles is about 10 mg, and the particle size is between 5 μm and 500 μm. Note 2. The sampling process takes about 10ms. 2.4 Isothermal reaction in microfluidized bed The gas-solid reaction induced by a pulsed micro sample in a constant temperature micro-fluidized bed. Note. It takes about 0.1s for the temperature rise of the particles below 100μm in the micro fluidized bed, which is far less than the reaction time required to complete most reactions.

3 Principle

3.1 Overview With a micro-fluidized bed as the reactor, inert (silica sand) or catalyst particles as the fluidized medium, the furnace is heated to the preset temperature. anti- After the reactor reaches the preset conditions, it uses particle pulse sampling to supply micro-fine particle samples to the micro-fluidized bed, and the rapid transmission through the fluidized bed Heat and mass transfer, the sample is instantly heated to the set temperature, and the isothermal reaction of the micro-fluidized bed is induced; the target component of the gas phase product is monitored online The concentration of the product changes with the reaction time, in order to calculate the time required to complete the reaction, the conversion rate and reaction rate at any reaction time, The activation energy of the reaction generated by the gas component provides raw data. Figure 1 is a schematic diagram of the principle of the micro fluidized bed method. ......

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