共查询到20条相似文献,搜索用时 31 毫秒
1.
I. I. Mel’nikov V. M. Kryachuk D. A. Mezin A. A. Gorbunov T. G. Voloshchuk 《Coke and Chemistry》2011,54(12):447-449
Given the shortage of coal with good coking properties, a petroleum coking additive is introduced in coal batch so as to expand
the range of plasticity. This additive improves coke quality in every respect, except the total sulfur content. Measures to
reduce the additive’s negative impact on the coal pitch are considered. 相似文献
2.
M. V. Zorin V. I. Matyukhin A. V. Matyukhina N. V. Yashmanova 《Coke and Chemistry》2016,59(5):186-191
The properties of coking batch may be stabilized by means of DK coking additive based on the products of petroleum pyrolysis, characterized by low ash content (Ad = 0.4%), high sulfur content (Std= 4.1%), and high yield of volatiles (Vdaf = 17.2%) relative to coal concentrates. Individual coking of DK coking additive yields a product (particle size >40 mm) with postreactive strength CSR = 77–79%, reactivity CRI = 18–22%, and density 1200–1400 kg/m3. Differential scanning calorimetry of experimental coke samples reveals six stages in their heat treatment in air: preliminary heating, intense oxidation, gasification of carbon, surface combustion of the gaseous products, their flare combustion, and oxidation of the residue. The use of DK coking additive in the coking batch shifts the oxidation process to higher temperatures and ensures the largest interval of heat liberation at elevated heating rate, with up to 50% DK additive. With increase in the content of DK additive from 30 to 50%, the activation energy is increased by 4.56 kJ/mol for each additional 10%. In that case, the supply of atmospheric oxygen to the combustion zone must be improved 相似文献
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V. N. Rubchevskiy Yu. A. Chernyshov A. V. Podlubnyy Yu. S. Vasilyev I. V. Shulga A. L. Fidchunov 《Coke and Chemistry》2014,57(4):154-157
At PAO Zaporozhkoks, the coke yield is determined experimentally as a function of the batch properties and the final coking temperature, in box coking. An empirical formula for the coke yield is obtained. With increase in the yield of volatiles from dry batch by 1%, the coke yield falls by 0.71%. With increase in the final coking temperature by 50°C, the coke yield falls by 0.35%. 相似文献
5.
Experimental coking with spent ion-exchange resins as an additive in the coal batch is considered; rammed batch is employed.
Both box coking and large-scale coking are considered; the resin content in the batch is 1–5 wt %. The influence of the resins
on coke quality is assessed. The coal blend used in industrial coke production is employed. Adding small quantities of resin
(<5 wt %) to the batch improves the coke’s cold strength M
80 and M
40, without impairment of CRI and CSR. The quality of the coal tar and the organized gas emission remains unchanged. Hence, spent ion-exchange resins may be recycled
by adding small quantities (3%) to the coal batch in coke production. 相似文献
6.
At OAO Zapadno-Sibirskii Metallurgicheskii Kombinat (ZSMK), research is undertaken to improve the optimization of coking batch.
The basic approach, proposed by specialists from OAO Nizhne-tagil’skii Metallurgicheskii Kombinat, employs the coefficient
K
opt, which characterizes the deviation of the batch from its optimal composition. The coking properties of the OAO ZSMK coal
batch over the last few years are analyzed. After laboratory and industrial coking of batch with different K
opt, the strength and reactivity of the resulting coke is investigated. Evaluation of coke-grade coal in terms of its rank according
to State Standard GOST 25543-88 proves inadequate, since coal of the same rank may differ markedly in coking properties. A
method is established for assessing the optimality of the coal batch at OAO ZSMK. 相似文献
7.
Determinations of weathered coal by petrographic methods, and coking tests in an 18-inch () test oven were used to quantify the effects of weathered coal on coking properties and coke quality. The results show that the presence of weathered coal causes a decrease in coke stability and coking rate and an increase in coke reactivity and coke-breeze generation. Because these effects contribute to increased costs in both the coke plant and the blast furnace, every effort should be made to reduce the amount of weathered coal in coking coal mixes. 相似文献
8.
《Fuel Processing Technology》1998,55(2):129-141
The addition of petroleum coke to a typical industrial coal blend used in the production of metallurgical coke was studied. Cokes were produced at semi-industrial scale at the INCAR coking plant, using petroleum coke of different particle size distribution as an additive. Special attention was paid to changes caused in the textural properties (porosity, pore size distribution, fissures at the interface between metallurgical coke and petroleum coke) which have been found to be responsible for variations in the metallurgical coke quality parameters (e.g., mechanical strength and reactivity towards CO2). Variation in porosity was found to depend on particle size and the proportion of the additive. The decrease in the microporosity (i.e., pore radius<3.7 nm) of the metallurgical cokes observed when petroleum coke is added to the coal blend, is postulated to be one of the main factors responsible for the decrease in the reactivity of these cokes. The variation of the mechanical strength indices can be explained by the changes in porosity and the quality of the interfaces between petroleum coke and metallurgical coke. 相似文献
9.
G. R. Gainieva V. I. Byzova N. N. Nazarov L. D. Nikitin R. L. Boryachikova 《Coke and Chemistry》2008,51(10):383-389
The evaluation of coal batch is considered, along with its influence on coke quality and the coking properties. The quality of the coal available for coking at OAO Zapadno-Sibirskii Metallurgicheskii Kombinat is declining. Given the shortage of coking coal, coal ranks that are not of equivalent coking and enrichment characteristics are being added to the batch. In some cases, mixtures with energy coals are prepared. The ash content of the batch sent for enrichment is rising, and the concentrate yield is falling. With decrease in the content of bituminous coal in the coking batch, the strength of the coke is declining. Improving the performance of the coke-production and blast-furnace shops depends on access to coal of satisfactory structure and quality. 相似文献
10.
炼焦生产工艺管理如加热制度、装平煤操作会影响焦炭的机械强度,只有通过不断加强炼焦的生产管理才能提高焦炭质量。 相似文献
11.
Blast-furnace performance is dependent on the coke quality and, above all, its stability. The stability of coke properties is ensured by effective homogenization of the coal components on storage and on blending crushed coal to form the coking batch. 相似文献
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Two plastic wastes (polyolefin-enriched and multicomponent), two lube oils (paraffinic and synthetic) and one coal-tar were assessed as individual and combined additives to coal blends for the production of blast furnace coke. The effects of adding 2 wt.% of these additives or their mixtures (50:50 w/w) on the coking capacity of coal, coking pressure and coke quality parameters were investigated. It was found that the two plastic wastes reduce fluidity, whereas the addition of oils and tar helps to partially restore the fluidity of the coal-plastic blend. From the co-carbonization of the coking blend with the different wastes in a movable wall oven of over 15 kg capacity, it was deduced that polyolefins have a detrimental effect on coking pressure. The addition of oils and tar to the coal-plastic blend has different modifying effects. Whereas paraffinic oil eliminated the high coking pressure caused by the polyolefins, polyol-ester oil had a weak reducing effect unlike coal-tar which had a strong enhancing effect. The compatibility of the oils/tar with plastics and coal and the beneficial influence of these combinations on coking pressure is discussed in relation to the miscibility of the plastic and the oily and bituminous additives, and the amount and composition of the volatile matter evolved from each additive during pyrolysis as evaluated by thermal analysis. Furthermore, it was found that coke reactivity towards CO2 (CRI) and coke strength after reaction with CO2 (CSR) are heavily dependent on the composition of the plastic waste, with polystyrene (PS) and polyethylene terephthalate (PET) having a clear negative effect. The porosity of the cokes obtained from blends containing plastic wastes is always higher, but the pores are smaller in size. 相似文献
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V. N. Rubchevskiy S. A. Ovchinnikova Yu. A. Chernyshov Yu. S. Kaftan E. I. Toryanik A. V. Gryzlov 《Coke and Chemistry》2014,57(4):147-153
Existing methods of assessing coke in production conditions are analyzed. Significant deficiencies are noted in the gravimetric method of determining the yield of volatiles and in methods of determining the temperature of the coke leaving the coking chamber. Assessment of coke on the basis of a modified method of determining the yield of volatiles (by volume) at 1150°C is proposed. In the coke shops at PAO Zaporozhkoks, samples of industrial coke are assessed by the proposed method. A close correlation is found between the yield of volatiles (by volume) and two important coking characteristics: the final temperature and the coking rate. Determination of the yield of volatiles by volume is currently used in the central laboratory at PAO Zaporozhkoks in continually assessing the coke produced and correcting the coking temperature. 相似文献
16.
焦化炉是延迟焦化装置的核心设备 ,认为引起焦化炉管结焦的主要原因有进料性质、辐射管表面热强度、辐射炉管排列方式、炉出口温度控制、炉管介质流速及流动状态等。根据延迟焦化原理 ,合理设计 ,精心操作 ,可减缓焦炭生成速度 ,使焦化炉的连续开工周期得以延长。针对焦化装置普遍存在的炉管结焦、大油气线结焦、分馏塔底结焦等问题 ,在生产中摸索了一些经验 ,取得了良好的效果 相似文献
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K. Singh M.V.P. Menon B.C. Mitra S.K. Chatterjee S.R. Sarkar S. Biswas R.B. Paul S.T. Raghavan 《Fuel Processing Technology》1984,9(1):79-89
Assessment of the coking behaviour of coals and blends by conducting coking tests in experimental coke ovens still continues to be the most reliable method and is extensively used all over the world. The oil-cum-gas fired experimental coke oven developed at CFRI has a coal charging capacity of 1100 kg and simulates industrial carbonising conditions. The oven is capable of intermittent operation and can be brought up to working temperature within 36 hours.Correlation studies of coke quality were carried out by conducting a series of coking tests on the same blend, carbonised under similar conditions in the CFRI experimental coke oven and the commercial coke ovens of Bokaro Steel Plant. The study has revealed that the physical strength of the CFRI oven coke compares favourably with the Bokaro oven coke. M40 and M10 indices of the commercial oven coke can be predicted fairly accurately from the results of CFRI oven coke.T-tests performed on the shatter results showed that at 5% probability level there was no significant variation between the shatter indices of both cokes. The quality of the gas produced from the CFRI test oven was very similar to that of the gas produced from the Bokaro ovens. 相似文献
19.
The granulometric composition of coke dust from the dry-slaking machine is determined. The influence of additions of 3−7%
coke dust on the quality of industrial coking batch and the coke obtained by box coking is estimated. Adding 1% coke dust
to coking batch does not markedly change the coke quality. Industrial equipment for the supply of dry-slaking dust to the
batch is described. 相似文献
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