The effects of a kappa-distribution in the heliosheath on the global heliosphere and ENA flux at 1 AU

We investigate heliosheath energetic neutral atom (ENA) fluxes at keV energies, by assuming that the heliosheath proton distribution can be approximated by a kappa-distribution. The choice of the kappa parameter derives from observational data of the solar wind (SW). This has direct applications to the upcoming IBEX mission. We will look at all-sky ENA maps within the IBEX energy range (10 eV to 6 keV), as well as ENA energy spectra in several directions. We find that the use of kappa, as opposed to a Maxwellian, gives rise to greatly increased ENA fluxes above 1 keV, while medium energy fluxes are somewhat reduced. We show how IBEX data can be used to estimate the spectral slope in the heliosheath, and that the use of kappa reduces the differences between ENA maps at different energies. We also investigate the effect introducing a kappa-distribution has on the global interaction between the SW and the local interstellar medium (LISM), and find that there is generally an increase in energy transport from the heliosphere into the LISM, due to the modified profile of ENA's energies. This results in a termination shock that moves out by 4 AU, a heliopause that moves in by 9 AU and a bow shock 25 AU farther out, in the nose direction

Development of high-tech production of high-octane components of motor fuel from renewable vegetable raw materials

In work are studied development of new oxygen-containing high-octane fuel compositions. The short review of comparisons of the main indicators is presented. In this article is shown need of development of production of octane additives. Receiving high-octane gasolines with use of components of the fuels alternative oil, the solution of these questions can become use of alcohols as additives to traditional gasoline, and first of all the ethyl alcohol produced from renewable sources of raw materialsThe goal can be carried out by means of modeling of technological processes. Using a software package of "UnisimDesign" we will make modeling of process of receiving isoamyl alcohol. In a basis of universal system of modeling of "UnisimDesign" the general principles of calculations of material and thermal balances of technological schemes are underlain.On the calculated scheme 1 isoamyl alcohol which is used in the form of additive to motor fuels is emitted one target product. However contained in fusel oils butanol also has broad application. Butanol is applied as solvent to paints, he is a part of brake fluids, industrial detergents. But at allocation of a butanol we face a problem, fusel oils contain water and form azeotrope mixes. For the solution of this problem we suggest to enter into initial raw materials hexane, in the ratio 1:1. It will allow us to allocate besides isoamyl alcohol and butanol. Modeling of process of division of fusel oils I have shown a possibility of allocation of two demanded target products. The technological scheme of installation of division of fusel oils is provided in work. Constructive characteristics of the columned equipment are calculated, material and thermal balances of installation are

Obtaining formaldehyde on a new catalytic system

Formaldehyde is widely used in many fields of industry. The increase in the need for formaldehyde led to an increase in scientific research, the purpose of which is to obtain the greatest yield of the product (formaldehyde) with minimal costs for raw materials, catalyst and its regeneration, energy carriers, etc. At industrial plants for the production of formaldehyde by oxidative dehydrogenation of methanol on the silver on pumice catalyst, the process temperature is maintained at 600 ° C. The process of obtaining formaldehyde by oxidation of methanol with air oxygen at the combination of catalysts "silver" and "silver on pumice" in the temperature range of 250–450 °C is investigated. The results showed the possibility of practical application of the combined catalyst. Chemical and technological parameters of the process with the use of a new catalyst are slightly lower than production indicators, however, the temperature of the pilot process is 2 times lower - this will reduce not only the energy costs, but also increase the life of the catalyst and the cost of its regeneration