Palladium-based membranes for potential application in bio-jet fuel production unit

被引:0
|
作者
Parashar, Ritu [1 ,2 ]
Nailwal, Bipin Chandra [2 ]
Goswami, Nitesh [2 ]
Lenka, Raja Kishora [3 ]
Singha, Amit Kumar [2 ]
Kar, Soumitra [1 ,2 ,6 ,7 ]
Adak, Asis Kumar [2 ]
Parida, Suresh Chandra [1 ,4 ]
Mukhopadhyay, Sulekha [1 ,5 ]
机构
[1] Bhabha Atom Res Ctr, Homi Bhabha Natl Inst, Mumbai, India
[2] Bhabha Atom Res Ctr, Desalinat & Membrane Technol Div, Mumbai, India
[3] Bhabha Atom Res Ctr, Powder Met Div, Mat Grp, Navi Mumbai, India
[4] Bhabha Atom Res Ctr, Prod Dev Div, Mumbai, India
[5] Bhabha Atom Res Ctr, Chem Engn Div, Mumbai, India
[6] Homi Bhabha Natl Inst, Bhabha Atom Res Ctr, Mumbai 400094, India
[7] Bhabha Atom Res Ctr, Desalinat & Membrane Technol Div, Mumbai 400085, India
关键词
Bio-jet fuel; palladium membrane; hydrocracker; modelling and simulation; HYDROGEN SEPARATION; PD; PERMEATION; STABILITY; SULFIDE; EVOLUTION; SUBSTRATE; REACTOR; FILMS;
D O I
10.1080/00194506.2023.2232386
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The hydrogen in the vent gas stream of the hydrocracker (used to produce bio-jet fuel) cannot be reused since it has many impurities. The metal membrane can be a potential candidate for recovering hydrogen from this vent gas. In this work, the authors report the development of a composite palladium membrane and its application, for the first time, in the recovery of hydrogen from a simulated vent gas environment. A dense thin film (thickness & SIM;3 & mu;m) of Pd metal was coated on a ceramic support tube by the sputter deposition technique. The hydrogen permeance of the Pd membrane was found to be 18.75 x 10(-6) mol & BULL;m(-2)& BULL;h(-1)& BULL;Pa-1, which was reduced to 3.25 x 10(-6) mol & BULL;m(-2)& BULL;h(-1)& BULL;Pa-1, with an exposure of 100 h in the simulated bio-jet fuel environment. To avoid the loss of permeability, a thin layer of Pt can be coated over the Pd membrane. The present study used MATLAB software to simulate the Pt-coated Pd composite membrane performance in the bio-jet fuel production environment. Simulation studies confirmed that a membrane area of & SIM;95 cm(2) (250 mm length and 12 mm OD) is sufficient for the complete recovery of hydrogen from the vent gas stream of hydrocracker at a feed velocity of 0.075 m/s.
引用
收藏
页码:556 / 573
页数:18
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