煤焦油蒽馏分制焦炭

IF 0.5 Q4 ENGINEERING, CHEMICAL

Coke and Chemistry Pub Date : 2025-07-21 DOI:10.3103/S1068364X25600502

N. T. Smagulova, Zh. K. Karibekov, B. M. Iskakbai

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引用次数: 0

摘要

在ARN-LAB-03系统中蒸馏煤焦油可产生9%的轻油馏分（沸点高达170°C）， 12%的中油馏分（沸点在170 - 230°C）， 10%的重油馏分（沸点在230-270°C）， 32%的蒽馏分（沸点在270-360°C）和35%的固体沥青残渣。蒽部分经过焦化处理。在500℃条件下，在3.5 MPa压力下焦化5.5 h后，焦炭样品K-3的产率为45%。在相同条件下，在4.5 MPa下得到的焦炭样品K-4的产率为50%。在此基础上，提出了一种从煤焦油的蒽馏分制取焦炭的有效方法。

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Coke Production from the Anthracene Fraction of Coal Tar

Distillation of coal tar in an ARN-LAB-03 system yields 9% of a light oil fraction (boiling up to 170°C), 12% of a medium oil fraction (boiling at 170–230°C), 10% of a heavy oil fraction (boiling at 230–270°C), 32% of an anthracene fraction (boiling at 270–360°C), and 35% of a solid pitch residue. The anthracene fraction is subjected to coking. After coking the anthracene fraction for 5.5 h under a pressure of 3.5 MPa at 500°C, the yield of coke sample K-3 is 45%. The yield of coke sample K-4 obtained in the same conditions, but at 4.5 MPa, is 50%. On that basis, an effective method is proposed for producing coke from the anthracene fraction of coal tar.

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来源期刊

Coke and Chemistry ENGINEERING, CHEMICAL-

CiteScore

0.70

自引率

50.00%

发文量

期刊介绍： The journal publishes scientific developments and applications in the field of coal beneficiation and preparation for coking, coking processes, design of coking ovens and equipment, by-product recovery, automation of technological processes, ecology and economics. It also presents indispensable information on the scientific events devoted to thermal rectification, use of smokeless coal as an energy source, and manufacture of different liquid and solid chemical products.