Global Change Abstracts The Swiss Contribution - SCNAT
Global Change Abstracts The Swiss Contribution - SCNAT
Global Change Abstracts The Swiss Contribution - SCNAT
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<strong>Global</strong> <strong>Change</strong> <strong>Abstracts</strong> – <strong>The</strong> <strong>Swiss</strong> <strong>Contribution</strong> | Mitigation and Adaptation Technologies<br />
engine was used as test platform, applying the<br />
eightstage ISO 8178/4 C1 cycle. DPF applications<br />
neither affected the engine performance, nor did<br />
they increase NO, NO 2, CO, and CO 2 emissions.<br />
<strong>The</strong> latter is a metric for fuel consumption. THC<br />
emissions decreased by about 40% when deploying<br />
DPFs. PCDD/F emissions, with a focus on tetra-<br />
to octachlorinated congeners, were compared under<br />
standard and worst case conditions (enhanced<br />
chlorine uptake). <strong>The</strong> iron-catalyzed DPF neither<br />
increased PCDD/F emissions, nor did it change the<br />
congener pattern, even when traces of chlorine<br />
became available. In case of copper, PCDD/F emissions<br />
increased by up to 3 orders of magnitude<br />
from 22 to 200 to 12 700 pg I-TEO./L with fuels of<br />
< 2, 14, and 110 µg/g chlorine, respectively. Mainly<br />
lower chlorinated DD/Fs were formed. Based on<br />
these substantial effects on PCDD/F emissions, the<br />
copper-catalyzed DPF system was not approved for<br />
workplace applications, whereas the iron system<br />
fulfilled all the specifications of the <strong>Swiss</strong> procedures<br />
for DPF approval (VERT).<br />
Environmental Science Technology, 2007, V41,<br />
N16, AUG 15, pp 5789-5794.<br />
08.1-421<br />
Towards multi-source multi-product energy<br />
systems<br />
Hemmes K, Zachariah Wolff J L, Geidl M, Andersson<br />
G<br />
Netherlands, Switzerland<br />
Energy & Fuels , Engineering , Modelling<br />
Historically, energy conversion was seen as a onedimensional<br />
system, in the sense that one form<br />
of energy was converted into another form. Byproducts<br />
of the conversions such as heat were<br />
disregarded and/or treated as waste. Cogeneration<br />
is a first step towards system improvement since<br />
the ‘waste heat’ is recovered and used as a valuable<br />
product. Trigeneration systems, which take<br />
the concept even further, are proposed for the simultaneous<br />
production of chemicals, power, and<br />
heat, and are integrated into larger systems, such<br />
as chemical plants, to achieve increased overall<br />
performance. In these systems electricity may just<br />
be a by-product. However, co- and trigeneration<br />
systems are still characterized by a single input.<br />
In this paper we further extend this concept and<br />
explore the potential role of multi-source multiproduct<br />
(MSMP) systems.<br />
International Journal of Hydrogen Energy, 2007,<br />
V32, N10-11, JUL-AUG, pp 1332-1338.<br />
197<br />
08.1-422<br />
An energy management method for the food<br />
industry<br />
Müller D C A, Marechal F M A, Wolewinski T,<br />
Roux P J<br />
Switzerland<br />
Economics , Energy & Fuels , Engineering<br />
This article presents a method aimed at tracking<br />
energy saving opportunities in the food-processing<br />
industry through a combination of top-down<br />
and bottom-up approaches. On the one hand, the<br />
top-down modelling method aims at correlating<br />
the measured energy consumptions with the final<br />
products and auxiliaries as well as at allocating<br />
the energy bills among major consumers. This<br />
approach will, therefore, set priorities for energy<br />
saving actions. On the other hand, the bottom-up<br />
approach, which is based on the thermodynamic<br />
requirements of the process operations, is used to<br />
define the energy requirements of these consumers.<br />
A comparison of the measured consumptions<br />
and the energy requirements enables the identification<br />
of energy saving opportunities. In the case<br />
study presented in this article, these opportunities<br />
have been evaluated using thermo-economic<br />
modelling tools and range from good housekeeping<br />
measures and optimised process operations to<br />
energy saving investments.<br />
Applied <strong>The</strong>rmal Engineering, 2007, V27, N16,<br />
NOV, pp 2677-2686.<br />
08.1-423<br />
H 2O-splitting thermochemical cycle based on<br />
ZnO/Zn-redox: Quenching the effluents from<br />
the ZnO dissociation<br />
Müller R, Steinfeld A<br />
Switzerland<br />
Geochemistry & Geophysics , Engineering<br />
<strong>The</strong> production of zinc by thermal dissociation of<br />
zinc oxide has been experimentally investigated<br />
in the range of 1700-1950 K using a 10 kW solar<br />
chemical reactor directly exposed to concentrated<br />
solar radiation. <strong>The</strong> gaseous products Zn(g) and<br />
O-2 exiting the reactor underwent rapid cooling<br />
by flowing through an annular water-cooled<br />
quench unit and by injection of Ar. XRD analysis<br />
along with SEM and TEM images of the solid products<br />
deposited at the quenching zone revealed<br />
the formation of spherical particles of sizes in the<br />
0.1-30 µm range, with their surface covered with<br />
smaller edged structures, which are characteristic<br />
of Zn(g) undergoing condensation followed by<br />
Zn(l)/Zn(s) oxidation and coalescence.<br />
Chemical Engineering Science, 2008, V63, N1, JAN,<br />
pp 217-227.