Requested by no1uno
"Few here, one is purely for my own edification, the other three (I know at least one has been put up before elsewhere, but I couldn't find it) are specifically for the drying of alcohol/water mixtures in the preparation of Na/Li Alkoxides (I think it probably works for KOH if these are true). Imagine, potassium isopropoxide at hand? KOtBu is stronger, but that is still a branched chain alkoxide and it would be plenty strong enough for home use."
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Design, manufacturing and operation of a small turbojet-engine for research purposes
Benini,Ernesto;Giacometti,Stefano
Applied Energy
2007, Vol.84(11), pp.1102-1116
DOI: 10.1016/j.apenergy.2007.05.006
Abstract
A research project is on going, at the University of Padova, to develop a 200 N static-thrust engine to be used for both didactic and research activities. This paper describes in detail all the phases required to set-up such an engine, including design, manufacturing and operation. The jet engine features a single-stage centrifugal compressor developing 2.66:1 compression ratio at 60,000 rpm, a direct-flow annular combustion chamber and a single-stage axial turbine with 950 K turbine-inlet temperature (TIT). All the design and manufacturing details are provided, as well as the operation procedure together with experimental results.
Keywords:Small turbojet; Turbojet engine; Design; Operation; Combustion
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Thermal Dehydration of Calcium Hydroxide. 1. Kinetic Model and Parameters
Irabien,Angel;Viguri,Javier;Ortiz,Inmaculada
Ind. Eng. Chem. Res.
1990, Vol.29(8 ), pp.1599–1606
DOI: 10.1021/ie00104a004
Abstract
In this work, the kinetic model describing the behavior of the dehydration reaction of calcium hydroxide in the range of temperatures 330-450'C is reported. Two different types of solids have been used in dehydration tests: commercial calcium hydroxide, S=8.3 ± 1m2-g-1 and calcium hydroxide reagent obtained in the laboratory under controlled conditions, S=18.7 ± 1m2-g-1. A discrimination of the reaction model using the structural parameter ?=0, which corresponds to a pseudohomogeneous kinetic model of the form
dx/dt=k80 exp(-E2/RT) x P0*(-?H/RT)/RT x S0(1-x)
with kinetic parameters k2 = 1.81 x 1020cm-s-1, E2 = 280.4kJ-mol-1, p0* = 1.834 x 108 atm and -?H = 138.5kJ-mol-1. The suitability of the kinetic model to describe the behavior of calcium hydroxide during the dehydration process was confirmed by the results obtained in the correlation of the experimental data of calcium hydroxide reagent, a different solid with a higher surface area.
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Thermal dehydration of calcium hydroxide. 2. Surface area evolution
Irabien,Angel;Viguri,Javier;Cortabitarte,Fernando;Ortiz,Inmaculada
Ind. Eng. Chem. Res.
1990, Vol.29(8 ), pp.1606–1611
DOI: 10.1021/ie00104a005
Abstract
The evolution of the specific surface area associated with the thermal decomposition of calcium hydroxide has been studied experimentally and described by kinetic models utilizing two different solids: commercial calcium hydroxide (S0 ~ 8.3 m2-g-1) and calcium hydroxide reagent (i]S[/i]0 ~ 18.7 m2-g-1). The surface area was observed to vary linearly with the fraction decomposed during the dehydration period. Sintering phenomena have been experimentally measured by treating calcium oxide samples (S0 ~ 46 m2-g-1) obtained after dehydration of calcium hydroxide under constant conditions, at temperatures in the range 500-900ºC for periods of time up to 24 h. A previously developed model, German and Munir (1976), fits the experimental results well if the surface area decreases to less than 55% of the initial value. An empirical kinetic model, where the surface area is linearly related to the heating time, correlates the experimental data, when ?S/S0 = > 55%. Simulated curves using the obtained kinetic models and parameters, for the specific surface during dehydration and sintering, agree well within the experimental results.
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Dehydration of Sodium Hydroxide and Lithium Hydroxide Dispersed over Calcium Oxide catalysts for the Oxidative Coupling of Methane
Maiti,G;Baerns,M
Applied Catalysis A: General
1995, Vol.127(1-2), pp.219-232
DOI: 10.1016/0926-860X(95)00071-2
Abstract
Promotion of CaO by Na+ or Li+ leads to an active and selective catalyst for the oxidative coupling of methane into higher hydrocarbons. The structural changes of NaOH- and LiOH-impregnated Ca(OH)2 during calcination were studied by applying differential thermal analysis, IR and X-ray diffraction techniques. The results indicate that both NaOH and LiOH interact with Ca(OH)2 during drying and calcination. The alkali hydroxides tend to dehydrate along with Ca(OH)2 into oxides. In situ infrared spectroscopic studies suggest that dehydration of the mixed hydroxides occurs around 450ºC. The measured lattice parameter values indicate that the inclusion of Na+ or Li+ ions into the CaO matrix remains very limited. It may be assumed that most of the alkali oxide remains in well dispersed state over the CaO matrix when calcining the samples at 600ºC. On increasing the alkali content above 10% no further increase in hydrocarbon selectivity is achieved.
Keywords: Differential thermal analysis; Infrared spectroscopy; Methane oxidative coupling; Sodium/lithiumcalcium oxide; Structural change