Hydrogen Separation of Ag Tube Coated with Pd-Ag Membrane

碩士 === 國立清華大學 === 材料科學工程學系 === 90 === Abstract Hydrogen is one of the most potential clean energies in the 21st century. Although it can be produced by solar light, electricity, etc., the purification process is still very costly step. To lower the cost and get higher purity...

Full description

Bibliographic Details
Main Authors: Chun-Sheng Yeh, 葉春生
Other Authors: Tsong-Pyng Perng
Format: Others
Language:en_US
Published: 2002
Online Access:http://ndltd.ncl.edu.tw/handle/42270201960340614046
id ndltd-TW-090NTHU0159096
record_format oai_dc
spelling ndltd-TW-090NTHU01590962015-10-13T10:34:05Z http://ndltd.ncl.edu.tw/handle/42270201960340614046 Hydrogen Separation of Ag Tube Coated with Pd-Ag Membrane 銀管及鈀銀薄膜之製備及其氫分離性質研究 Chun-Sheng Yeh 葉春生 碩士 國立清華大學 材料科學工程學系 90 Abstract Hydrogen is one of the most potential clean energies in the 21st century. Although it can be produced by solar light, electricity, etc., the purification process is still very costly step. To lower the cost and get higher purity and large amount of hydrogen, palladium-silver membrane supported on the porous substrate is used in hydrogen purification. The palladium-silver alloy membrane has been extensively studied in recent years due to the absence of α/β phase transition and embrittlement associated with hydrogen permeation. In addition to the application for ultra high purity hydrogen separation, it is also widely utilized in recovery or purification of hydrogen in petroleum industry, hydrogen reactor in fuel cells, and methane-steam reforming. In this study, silver powder agglomerate was used to prepare porous substrate. The porous silver substrate was obtained by uniaxial mechanical pressing and sintering at 350℃ in air for 1 hr. Prior to sputter deposition, the surface was modified by filling with Pd70Ag30 nanoparticles to reduce the pore size and cleaning with acetone to remove the residual particles. After the surface modification, a 5μm-thick Pd-Ag membrane was deposited on the surface by dc magnetron sputtering. For the tube substrate, the membrane was deposited with a rotating design. The surface and cross-section morphologies of the substrate and membrane were examined by scanning electron microscopy. The compositions of the membrane were calibrated by X-ray diffraction. Besides, the permeation rate of hydrogen at 250℃ was measured by a gas permeation apparatus. It was observed that cleaning surface with acetone was very important for the modification process. A dense and continuous Pd-Ag membrane could be uniformly prepared on the modified tube surface. A 5μm-thick membrane was successfully deposited on the 2cm-long silver tube surface. The maximum hydrogen pressure the tube membrane could support was 2.5 kg/cm2. The thermal stability and durability at different pressures was very good even after 48 cycles of test. The Sievert’s law was not obeyed in this study. Tsong-Pyng Perng 彭宗平 2002 學位論文 ; thesis 86 en_US
collection NDLTD
language en_US
format Others
sources NDLTD
description 碩士 === 國立清華大學 === 材料科學工程學系 === 90 === Abstract Hydrogen is one of the most potential clean energies in the 21st century. Although it can be produced by solar light, electricity, etc., the purification process is still very costly step. To lower the cost and get higher purity and large amount of hydrogen, palladium-silver membrane supported on the porous substrate is used in hydrogen purification. The palladium-silver alloy membrane has been extensively studied in recent years due to the absence of α/β phase transition and embrittlement associated with hydrogen permeation. In addition to the application for ultra high purity hydrogen separation, it is also widely utilized in recovery or purification of hydrogen in petroleum industry, hydrogen reactor in fuel cells, and methane-steam reforming. In this study, silver powder agglomerate was used to prepare porous substrate. The porous silver substrate was obtained by uniaxial mechanical pressing and sintering at 350℃ in air for 1 hr. Prior to sputter deposition, the surface was modified by filling with Pd70Ag30 nanoparticles to reduce the pore size and cleaning with acetone to remove the residual particles. After the surface modification, a 5μm-thick Pd-Ag membrane was deposited on the surface by dc magnetron sputtering. For the tube substrate, the membrane was deposited with a rotating design. The surface and cross-section morphologies of the substrate and membrane were examined by scanning electron microscopy. The compositions of the membrane were calibrated by X-ray diffraction. Besides, the permeation rate of hydrogen at 250℃ was measured by a gas permeation apparatus. It was observed that cleaning surface with acetone was very important for the modification process. A dense and continuous Pd-Ag membrane could be uniformly prepared on the modified tube surface. A 5μm-thick membrane was successfully deposited on the 2cm-long silver tube surface. The maximum hydrogen pressure the tube membrane could support was 2.5 kg/cm2. The thermal stability and durability at different pressures was very good even after 48 cycles of test. The Sievert’s law was not obeyed in this study.
author2 Tsong-Pyng Perng
author_facet Tsong-Pyng Perng
Chun-Sheng Yeh
葉春生
author Chun-Sheng Yeh
葉春生
spellingShingle Chun-Sheng Yeh
葉春生
Hydrogen Separation of Ag Tube Coated with Pd-Ag Membrane
author_sort Chun-Sheng Yeh
title Hydrogen Separation of Ag Tube Coated with Pd-Ag Membrane
title_short Hydrogen Separation of Ag Tube Coated with Pd-Ag Membrane
title_full Hydrogen Separation of Ag Tube Coated with Pd-Ag Membrane
title_fullStr Hydrogen Separation of Ag Tube Coated with Pd-Ag Membrane
title_full_unstemmed Hydrogen Separation of Ag Tube Coated with Pd-Ag Membrane
title_sort hydrogen separation of ag tube coated with pd-ag membrane
publishDate 2002
url http://ndltd.ncl.edu.tw/handle/42270201960340614046
work_keys_str_mv AT chunshengyeh hydrogenseparationofagtubecoatedwithpdagmembrane
AT yèchūnshēng hydrogenseparationofagtubecoatedwithpdagmembrane
AT chunshengyeh yínguǎnjíbǎyínbáomózhīzhìbèijíqíqīngfēnlíxìngzhìyánjiū
AT yèchūnshēng yínguǎnjíbǎyínbáomózhīzhìbèijíqíqīngfēnlíxìngzhìyánjiū
_version_ 1716828982069952512