Conclusions
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1.
The catalytic cracking of the 400–450°C fraction of Stavropol'skii petroleum on a zeolite-containing catalyst takes place with an increased degree of conversion of the raw material and a markedly greater yield of the naphtha fraction as compared with cracking on an alumosilicate catalyst.
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2.
For the same cracking conditions (temperature of 475°C flow rate for adding the raw material 1.2 h−1), the activity of the zeolite containing catalyst with respect to the naphtha is 16% by weight higher than the activity of the alumosilicate catalyst.
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Translated from Khimiya i Tekhnologiya Topliv i Masel, No. 8, pp. 7–10, August, 1971.
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Mamaev, O.A., Dorogochinskii, A.Z. Catalytic cracking of the 400–450°C fraction of stavropol'skii petroleum on the AShNTs-3 zeolite-containing catalyst. Chem Technol Fuels Oils 7, 566–569 (1971). https://doi.org/10.1007/BF00714026
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DOI: https://doi.org/10.1007/BF00714026