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- Organic peroxide (6) (entfernen)
Single and multiple fireballs of di-tert-butyl peroxide are numerically investigated using ANSYS CFX. Calculations contain varying inlet conditions, scale-adaptive shear stress turbulence modeling and one-step combustion reaction on a three-dimensional hexahedral mesh. Time-resolved flame temperatures, sizes and thermal radiation are compared to experimental results. There, fireballs were generated by fire engulfment of steel drums containing 200 l substance. After a vigorous burning, the remaining peroxide forms single and multiple fireballs involving 10 % to 20 % of the initial amount. The comparison of all simulations and two selected experiments show the special numerical treatment required for organic peroxides. Finally, the numerical predictions of irradiance in 30 m distance to the fire show a good agreement for both experiments. This proves the use of CFD as an appropriate method for thermal hazard assessment and the prediction of safety distances for organic peroxide fireballs.
To simulate a full fire engulfment during transportation or storage a closed removable head steel drum filled with 200 l Di-tert-butyl peroxide (DTBP) is subjected to a wood fire. Due to the enormous heat flux and the exothermic self-decomposition large flames arise and finally multiple fireballs occur. The fireballs consume up to 20 % of the total mass (20 % equals to 31 kg). They are characterized by high surface emissive power and large flames associated with high thermal radiation causing spontaneous ignition of objects in the surrounding. The measured sizes of the DTBP fireballs are smaller compared to the results of the general equations for hydrocarbon fireballs. Because these equations are recommended by the Health and Safety Executive (UK) to be applicable for organic peroxides explicit comparisons of DTBP with LPG, diesel and gasoline concerning the characteristics of fireballs are carried out. Also the burning time is compared and confirms a faster combustion of the peroxide. Moreover, the development of size and emissive power for DTBP and diesel fireballs are compared in a normalized graph. The results provide the assumption that new empirical models are required to be developed for hazard assessment of organic peroxide fireballs.
For the industrial production of chemicals a safe process design is required to avoid harm to people and
environment. It becomes tremendous important if one or more of the following points are characteristic for
the synthesis: high heat release, explosive atmosphere, presence of toxic and/or of thermal unstable substances.
One substance group, known for being unstable, is the group of organic peroxides. They are potential
high energetic substances. Many syntheses of organic peroxides are carried out in semi-batch
mode to control the heat release in a good manner. With the aim to increase process control, the advantages
of continuous reaction mode, combined with micro reaction technology, are used for the synthesis
of one specific organic peroxide in this work.
This approach is not only characterised by shorter residence time, good heat transfer, but also by smaller
quantities of managed chemicals, and, therefore, by a lower hazard potential. Often yield and selectivity
can be improved additionally.
For the study a peroxyester, namely tert-Butyl peroxy-2-ethylhexanoate (TBPEH), with known thermal
hazard potential was chosen. The two phase liquid/liquid reaction was carried out in three types of reactors.
A small scale tubular reactor, stressed by ultrasound, and two different micro structured reactors were
used. One of them had a meandering and the other a split-and-recombine channel structure. Synthesis
temperature was also varied.
From preliminary studies it was known that the side reaction of the involved carboxylic acid chloride to the
corresponding acid can become more important in continuous mode compared to semi-batch mode. The
effect of reactor type and temperature on selectivity and therefore yield of TBPEH was analysed and compared.
In result the reaction could be carried out in a safe manner. The high heat-exchanging efficiency of the
used reactors and the short residence time allowed synthesis temperature near the onset temperature of
decomposition of TBPEH. In relation to the results of the capillary tube and of the reactor with meandering
channel structure (MR), the results for the split-and-recombine reactor (SAR) showed the best trend line.
Further studies have to underline the result. Compared to the traditional reaction path (the semi-batch
mode), a higher space time yield could be achieved. This promising information is accompanied by the fact
of low reaction volumes. In consequence the productivity is low without a numbering up of reaction channels
or a scaling up of it. The nowadays existing philosophy of producing a specific quantity of product by a
company, followed by the transport to the costumer may change. Just organic peroxides, used in small
quantities, e.g. as initiators for polymerisation processes or as resin hardeners, provide the opportunity for
an on-demand-production.
Combustion of peroxy-fuels
(2011)
The diffusion flames of organic peroxides exhibit quite different characteristics than hydrocarbons. What makes them interesting to study is their fast burning behaviour. As a result the flame temperature enhances and so does the thermal radiation. Due to all these they demand safe handling during processing. However, they can be utilised at several places in different industries where a fuel with fast burning, high temperature and intense radiation are desired. Some of the possibilities to use them as a main or supporting fuel in a wide range of industrial utilities are the major content of this paper.
The use of energetic materials as a main fuel in high temperature process
industries are not known to the scientific community as such. This paper
highlights some of the features and advantages of using organic peroxides
especially di-tert-butyl peroxide (DTBP) in high temperature process industries.
The feasibility of using DTBP as a main or supporting fuel in process industries
have also been justified with the help of Computational Fluid Dynamics (CFD)
simulations. For peroxides requirement of less fuel and air for the same amount
of heat flux has been shown. The resulted emission from the combustion of
DTBP is also discussed.
A new burner concept (PEROXY-BAM®) for the combustion of liquid organic peroxides (Peroxy-fuels) is presented. As peroxy-fuels are thermally unstable the design of burners for them should be accordingly modified ensuring a safe operation. It is found that 10 to 100 time less amounts of peroxy fuels are required for the same heat flux or output in comparison to hydrocarbons. Correspondingly, the fuel pump power and the volume of combustion chamber (furnace) are also reduced. As a result of less amount of fuel the emissions will also be stepped down and oxygen in the molecule helps to establish conditons like in an oxy-fuel combustion process. The advantages of using peroxy-fuels over hydrocarbons inside a model combustion chamber are also investigated with the help of CFD (Computational Fluid Dynamics) simulations.