It is an extremely important operation to control the blast volume in the melting operation with a cupola and this has close connexions not only to the tapping amount, the combustion condition in cupola, the save of fuel and other materials to be needed but also to the carburization percentage of carbon and the loss of silicon that seems to have great influences on the qualities of molten metal. On the actual operation of melting, both the air resistance and the air pressure in cupola are affected very much owing to the charging procedures of materials and the variation of electric source, therefore, it is almost impossible to keep the blast volume properly by the human ability. If this very delicate control of blast volume is fairly accomplished, then the percentages of carbon and silicon contained in molten metal can be controlled desirably and the molten metal which will produce the optimum chill depth when cast can be attained. The following results have been taken by employing the Askanian-type blast volume control instrument to the cupola having 1500 ton capacity which is installed in our factory. 1. The variation of blast volume was ± 0.1 N m
3/min against to the total blast volume of 20 N m
3/min. 2. The percentage of CO
2 contained in top gas was retained in 12.0∼12.5% after the condition of melting operation was stabilized, and the proper volume of blast could be supplied into the furnace corresponding to the test results of chilled pieces. And this adjustment could be made easily by remote control. 3. By giving the adequate control on both materials and blast volume, the molten metal which produces the most preferable chill depth to the desired castings was attained. 4. The adoption of the high temperature melting operation to this procedure was possible and the measured tapping temperature of the molten metal by an optical pyrometer was 1510∼1530°C. (the manipulated temperature value plus 110°C) 5. In the heretofore carried operation, the residual percentage of products was 85∼92 per cent, but it was developed to 92∼95 per cent by the installation of an automatic blast volume controller. Especially, the percentage of the rejected goods due to the lack of hydraulic pressure resistance or the defective horning finish was decreased down to 1. 2 per cent. 6. The material cost this time was reduced to 10 per cent compared with that of commonly used operation by adding 40∼50 per cent of steel scrap to pig irons. 7. The blast volume was kept almost constant and the tapping amount was increased 12 per cent. Consequently, the melting time was shortened. 8. Even if the percentage of steel scrap addition becomes greater and the amount of coke to be used is not increased, the fear of the decrease of melting temperature and the oxidation of molten metal can not be introduced. The save of the amount of coke is accomplished at the rate of approximately 12 per cent. 9. The amount of lime stone was also saved 40∼50 per cent owing to the applications of the techniques of high temperature melting and remote controlling of blast volume. 10. The number of cleaning the tuyére was reduced by controlling the blast pressure and tuyére sizes. As mentioned above, the employment of the automatic blast volume controlling instrument facilitates the melting operation with a cupola. (T. M.)
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