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General Remarks on Producer Gas
Reactions on Gasification in the Producer Stoichiometric
Thermal Conditions in Gasification of Carbon
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1*86 cubic metre able addition admits air-gas amount of heat ascertained available heat basic open-hearth furnace bath Bessemer process blast furnace calculation calories cals carbon content carbon monoxide carbonic acid cent charge combustible value combustion chamber composition contained cubic metre gas decarburisation distillation gas elimination employed final slag flame formation formula fuel furnace structure further gas and air gasification grammes hearth heat content hydrogen increased ingot iron oxide iron peroxide iron protoxide kilo kilogramme steel ladle lime limestone manganese materials means melting metal metre H millimetres molten pig iron o-oi obtained open-hearth process oxidising action oxygen phosphate phosphoric acid phosphorus pig and scrap portion possible preheating producer gas products of combustion pure quantity of slag reducing agents removal silicate slag silicic acid silicon steam steam-air gas substances sulphur taken takes place thereby utilisation vide volume waste gases water-vapour whilst yields