(553g) CFD Study of a Pilot-Scale Multi-Tube Palladium Membrane Module for Hydrogen Separation

CFD Analysis of
Pilot-Scale Multitube Pd Membrane Module for Hydrogen Purification from
Coal-Derived Syngas

Rui Ma¹,
Bernardo Castro-Dominguez², Ivan P. Mardilovich¹, Nikolaos
K. Kazantzis¹, Anthony G. Dixon¹, Yi Hua Ma¹

^1.Center for
Inorganic Membrane Studies, Department of Chemical Engineering, Worcester
Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, USA.

^2. University of
Limerick, Sreelane, Castletroy, Co. Limerick, Ireland

          Syngas production and hydrogen separation technologies are
very mature, and also extremely important for the energy and chemical
industries. Enhancing or intensifying these mature technologies is extremely
challenging, but on the other hand would have tremendous impact on performance
and economics of many processes. At this moment, most research on Pd membrane
technology has been conducted at lab scale, and membrane module scale up and
commercial unit design are still challenges that need to be addressed in order
to commercialize this promising technology. Compared with the one shell, one
membrane tube module, many questions need to be answered for a pilot scale,
multitube membrane module, such as the study of tube to tube variation in
hydrogen permeation due to the position in the module, the exploration of the optimal
shell side operating conditions and the evaluation of mass transfer limitations
such as concentration polarization. For this purpose, a three dimensional CFD
simulation model was developed and used to study the aforementioned aspects of
a pilot scale membrane module.

      
The geometry of a seven-tube module with a total permeable area of 1050 cm²
is shown in Figure 1a; coal-derived syngas was introduced to the shell side
(retentate side) and pure hydrogen was collected from the tube side (permeate
side). The asymmetrical fluid flow (Fig 2a) resulting from the outlet location
leads to an uneven hydrogen permeation rate in each membrane tube (Fig 3). By
adding a manifold for the membrane tubes in between the membrane tubes and the
outlet (Fig1b), fluid flow tends to be more symmetrical (Fig 2b.), hydrogen
permeance flux of each outer tube appears to be more even (Fig 3), thus the
membranes are used more efficiently. In addition, due to the competition effect
of the center tube with the six tubes around it, the center tube has the lowest
hydrogen permeance flux. This phenomenon was addressed more in detail by the
study of a further scaled-up module with 19 membrane tubes and a total
permeable area of 2850 cm² (Fig 4). Concentration polarization was also
observed from the model and indicated by the second Damkohler Number.
Furthermore, hydrogen recovery appears to be favored by high pressure and low
temperature while membrane usage benefits from moderate pressure and high
temperature, the trade-off between these two most important parameters of
membrane modules is investigated and a thorough process optimization study was carried
out using Box-Behnken method.

Figure1. Geometry of the 7 membrane tube
module: (a) without manifold (b) with manifold

Figure2. Velocity field of the 7
membrane tubes module: (a) without manifold (b) with manifold

Figure 3. Hydrogen permeance flux of the
outer tubes with different geometry

Figure 4. Cross sectional view of the 19
membrane tubes module