Modeling and simulation of petroleum coke calcination in rotary kilns

2002 ◽  
Vol 43 (3) ◽  
pp. 213
Fuel ◽  
2001 ◽  
Vol 80 (11) ◽  
pp. 1611-1622 ◽  
Author(s):  
Marcio A. Martins ◽  
Leandro S. Oliveira ◽  
Adriana S. Franca

Author(s):  
Ian S. Hamilton ◽  
Donald A. Halter ◽  
Donald F. Haumann ◽  
Erich H. Fruchtnicht ◽  
Matthew G. Arno

Petroleum coke, or “petcoke,” is a waste by-product of the oil refining industry. The majority of petcoke consumption is in energy applications; catalyst coke is used as refinery fuel, anode coke for electricity conduction, and marketable coke for heating cement kilns. Roskill has predicted that long-term growth in petroleum coke production will be maintained, and may continue to increase slightly through 2012. Petcoke must first be calcined to drive off any undesirable petroleum by-products that would shorten the coke product-life cycle. As an example, the calcining process can take place in large, rotary kilns heated to maximum temperatures as high as approximately 1400–1540°C. The kilns and combustion/settling chambers, as well as some cooler units, are insulated with refractory bricks and other, interstitial materials, e.g., castable refractory materials, to improve the efficiency of the calcining process. The bricks are typically made of 70–85-percent bauxite, and are slowly worn away by the calcining process; bricks used to line the combustion chambers wear away, as well, but at a slower rate. It has been recognized that the refractory materials contain slight amounts of naturally occurring radioactive materials (NORM) from the uranium- and thorium-decay series. Similarly, low levels of NORM could be present in the petcoke feed stock given the nature of its origin. Neither the petcoke nor the refractory bricks represent appreciable sources of radiation or radioactive waste. However, some of the demolished bricks that have been removed from service because of the aforementioned wearing process have caused portal alarms to activate at municipal disposal facilities. This has lead to the current investigation into whether there is a NORM concentrating mechanism facilitated by the presence of the slightly radioactive feed stock in the presence of the slightly radioactive refractory materials, at calcining-zone temperatures. Research conducted to date has been used to determine the speciation and concentration of nuclides in both the feed stock and the various refractory materials, as well as the slag that forms at the interface of the two materials, as a function of temperature. Further investigation into any potential for generation of a NORM hazard as a result of refractory demolition has been conducted. Aerosol generation (mass loading), particle size distribution, and pulmonary solubility class have been investigated as a function of demolition-task description. In addition, external radiation levels in the kilns, chambers and waste piles, as a function of temperature profile and brick/operating history have been investigated.


2020 ◽  
pp. 56-62
Author(s):  
I. I. Lapaev ◽  
◽  
V. E. Polovnikov ◽  
A. M. Konstantinov ◽  
V. E. Belyanin ◽  
...  

JOM ◽  
2015 ◽  
Vol 68 (2) ◽  
pp. 643-655 ◽  
Author(s):  
Jin Xiao ◽  
Jindi Huang ◽  
Qifan Zhong ◽  
Hongliang Zhang ◽  
Jie Li

2007 ◽  
Vol 2 (3) ◽  
Author(s):  
Elamin Mohamed Elkanzi

The objective of this study is to simulate the green petroleum coke calcining processes using the simulation program HYSYS and using actual industrial data. Because counter-current mass flow is not allowed in the HYSYS program, the kiln was described by using fictive streams and unit operations. By the simulation, it is possible to predict the operating conditions that control the contents of undesirable impurities in the calcined petroleum coke, namely, sulfur, volatile matter and moisture contents. It also gives the desirable calcined petroleum coke properties such as density. Apart from the metal contents, the simulation allows the coke calciner to utilize any type of green coke regardless of the undesirable impurities. This is done without resorting to the costly blend from different types of green cokes. Simulation is also effective in controlling and optimizing calcination processes' variables. From the simulation it was found that it is possible to process any type of green coke for varying sulfur, volatile matter and water content by adjusting the amount of tertiary air and/or fuel. Two simulation cases were studied for low and high volatile matter contents of 8.5 and 14.7 wt% in the feed. Mass flow rates of fuel and tertiary air were both increased in the first case, while no fuel was required in the second case. The benefit from this is to reduce the operating costs.


Author(s):  
I. I. Lapaev ◽  
V. V. Sorokin ◽  
S. E. Goloskin ◽  
A. V. Orlov

The brief description is given in the article for the engineering process and design of the rotary kilns for the petroleum coke KEP-1 and KEP-2 calcination, as well as the requirements to the lining of some parts of these kilns are presented. The lining bricklaying's features and principal methods used for the rotary kilns the foreign ones including are shown. The efficient possible lining option for the rotary kilns with the diameter both of 3 and 45 meters is described. The design and the modern materials are proposed to line up the calcining kiln for the KEP-2 calcined petroleum coke manufacturing. Ill. 5. Ref. 7. Tab. 1.


2019 ◽  
Vol 60 (1) ◽  
pp. 1-5
Author(s):  
I. I. Lapaev ◽  
V. V. Sorokin ◽  
S. E. Goloskin ◽  
A. V. Orlov
Keyword(s):  

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