Wiederertüchtigung schwerbeschädigter Kriegsteilnehmer in by Paul H. Perls (auth.)

By Paul H. Perls (auth.)

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Process parameters as volume ratio steam/methane temperatures pressures heat fluxes (tubes, rear wall, aperture) etc. should be taken over from the outlined plant as far as possible and necessary to assess technical risks of an upscaled plant. The items to be investigated may be function of receiver and steam reformer check of design values of components gathering operational experiences under a variety of solar conditions - 43 - It would be advisable to build the chemical experimental plant in such a way that the experimental results can be utilized for future applications.

Until now the proposer does not see problems in upgrading. d (air or (salt or metal) 2 . nS Data thermal power MW 2 • 25 inlet pressure bar 5 •c 20 inlet temperature 22 s'2s 442 430 •c 680 BOO 700 30 26 60 outlet temperature heat flux dens~ty appr. kW/m av. tv Geometr:! tube temp. 000,-- Prtce Spec. Dyn. heat cap. 1 Hydrox Jde (, 30 \) Alkali Chloride Alkali Carbonate (few) Alkali Chlonde (~30 CuCI-KCI GS 250 Alkali Hydroxide Mass-\ 40 - 60 Na-K 98 Na Mass-\ ;oc'; Melting- Boilingtemp. Malena! ~, H2 o, co, co 2 , Hz must be expecte to be very violent.

NS Data thermal power MW 2 • 25 inlet pressure bar 5 •c 20 inlet temperature 22 s'2s 442 430 •c 680 BOO 700 30 26 60 outlet temperature heat flux dens~ty appr. kW/m av. tv Geometr:! tube temp. 000,-- Prtce Spec. Dyn. heat cap. 1 Hydrox Jde (, 30 \) Alkali Chloride Alkali Carbonate (few) Alkali Chlonde (~30 CuCI-KCI GS 250 Alkali Hydroxide Mass-\ 40 - 60 Na-K 98 Na Mass-\ ;oc'; Melting- Boilingtemp. Malena! ~, H2 o, co, co 2 , Hz must be expecte to be very violent. Precautions to limit the hazard must be developed A new heat transfer system is reqUlred.

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