(676i) Direct Synthesis of Propene from Ethene Feedstock: Investigation of Catalytic Concepts

The production capacities of
polypropylene and propylene oxide, cumene and acrylic acid have grown over the
past decades leading to an increased demand in propene. The most common source
of propene is currently the cracking of naphtha, which is not sufficient to
meet the present demand [1]. A promising alternative is the direct conversion
of ethene to propene (ETP-reaction). The suggested reaction mechanism for this
overall reaction consists of three steps [2]. The first step is the dimerization
of ethene to 1-butene. Secondly 1-butene is isomerized. In the final third step
the produced 2-butene reacts with unconverted ethene via a metathesis reaction and
gives propene [2].

Ni loaded aluminized MCM-41 is a promising catalyst for the described reaction
scheme, because it is capable of supporting all three steps. However, this
catalyst represents a complex integrated system.

In previous works different preparation methods of the catalyst have been
developed [2, 3]. In this presentation a decoupled approach is followed. For
this, a two-catalyst/two-reactor concept is studied, in which the metathesis
step is separated from the dimerization and isomerization (Fig. 1). As a
consequence the system gains degrees of freedom with respect to residence time,
temperature and specific feed composition.

Fig. 1: Scheme of (a) an integrated catalytic system performing simultaneously all
reactions using a dedicated single catalyst and (b) a decoupled two-catalyst/two-reactor
concept using two sequentially applied catalysts.

The support MCM-41 and its aluminated
counterpart with different Si/Al ratios were synthesized using two different
procedures, reported in references [3, 4]. The incorporation of Ni and the most
common metathesis metals Re, Mo and W onto the supports was realized using the
template ion exchange (TIE) method and incipient wetness impregnation (IWI)
method [3]. The catalysts were characterized by XRD and N₂-physisorption.


The testing of the catalyst activity was carried out in a fixed bed reactor. For the experimental investigation
of the ETP-reaction a fraction of ethene in N₂ was fed into the
reactor_. Then, investigations of metathesis catalysts were conducted
with an equimolar mixture of ethene and 2-butene (trans-butene) at
atmospheric pressure. The temperature for the catalytic testing was modified in
the interval from 50 to 475 °C by increments of 25 °C. The feed and reaction
products were analyzed by online gas chromatography and mass spectrometry.

Objective of a carried out kinetic investigation is the identification of conditions
for optimal conversion of the reactants and yield of propene. Additionally it
is of interest to suppress the production of byproducts, such as pentene and
hexene. While working with hydrocarbons, furthermore, the formation of coke and
thereby the blocking of active sites should be minimized in order to prevent
deactivation processes.

The Ni catalysts (“Cat. 1”) for the ETP-reaction revealed high activities with
high specific conversions of the reactants and a selectivity of approximately
25 % for propene only at temperatures higher than 400 °C. Severe deactivation
of the Ni/(Al)MCM-41 was observed, with time on stream. Though it has been shown
that this catalyst can be regenerated [3] in a separate oxidative step.

In the approach of decoupled reactions Re has shown interesting activities in
the metathesis step at lower temperatures (“Cat. 2”). Especially the aluminized
MCM-41 with incorporated Re gave an equivalent selectivity as the Ni-catalyst at
200 °C (Fig. 2).

Fig. 2: Selectivity with respect to propene for different metals with supports
as a function of temperature, x_C2H4=2.5% and x_C4H8=2.5%;
W/F=2580 kg∙s/m³.

Main
goal of the current work is the derivation of a kinetic model in order to
optimize the reactor systems.

Acknowledgement


We would like to thank the DAAD with its PROALMEX program and Proyecto apoyado
por el Fondo Institucional de CONACYT (FOINS) for their financial support.

[1] D. Liu, W.
C. Choi, N. Y. Kang, Y. J. Lee, H. S. Park, C.-H. Shin, Y.-K. Park, Catal.
Today, 226 (2014) 52-66.

[2] M. Iwamoto, Molecules, 16 (2011) 7844-7863.

[3] L. Alvarado Perea, T. Wolff, P. Veit, L. Hilfert, F.T. Edelmann, C. Hamel,
A. Seidel-Morgenstern, J. Catal. 305
(2013) 154-168.

[4] T. Lehmann, T. Wolff, C. Hamel, P. Veit, B. Garke, A. Seidel-Morgenstern,
Microporous Mesoporous Mater. 151 (2012) 113-125.