99/02864 Specific heat consumption as a function of pusher furnace throughput

1999 ◽  
Vol 40 (4) ◽  
pp. 298
2015 ◽  
Vol 789-790 ◽  
pp. 165-169
Author(s):  
Ján Spišák ◽  
Branislav Vaňko ◽  
Ján Kerekanič ◽  
Daniela Čuchtová

Coke production is carried out by coal carbonization. The most frequently used coal is anthracite, which features a very low content of volatile substances that not exceed 7%. Current anthracite production is carried out in rotary furnaces, consists of processes as follows: drying, heating, pyrolysis and calcination. Coke cooling is performed in cooling device located at the end of the furnace. To enhance the performance and reduce the specific heat consumption, use of the preheating device for rotary charge was proposed. The charge granulometry allows using the preheating device based on thin layer principle. Proposed solution was verified by simulations.


2013 ◽  
Vol 448-453 ◽  
pp. 3350-3353
Author(s):  
Jian Wang ◽  
Yu Wei Chen ◽  
Jian Sun ◽  
Sheng Ji Liu

Experiments were separately carried out on Liquefied Petroleum Gas (LPG) and gasoline as fuel for a spark ignition (SI) engine. According to the indicator diagram and the calculation of corresponding heat release, combustion characteristics of the two fuels were analyzed. The results showed that using LPG would lead to 7.64% power reduction and a little peak pressure reduction when the structures and ignition advance angle of the engine were remained. At rated speed and full load, the power of engine fueled with gasoline reaches the maximum when the excess air ratio is 0.90 and 0.76 fueled with LPG; when comparing the maximum power and specific heat consumption at different excess air ratios, we can see that the change of excess air ratio has a greater effect on the engine fueled with gasoline than that fueled with LPG; the specific heat consumption of both fuels decrease with the increase of load. Besides, under the same Фa, LPG has a shorter combustion delay period, faster combustion speed and shorter combustion period than gasoline.


2016 ◽  
Vol 820 ◽  
pp. 171-176 ◽  
Author(s):  
Peter Buday

According to requirements of STN 73 0540-2, 2012 is defined the requirement to meet energy criteria using the specific heat consumption for heating as well as normalized value of specific heat consumption for heating with expectation of achieving of energy efficiency in buildings. These requirements are followed by springboard to legislative evaluation of buildings in terms of energy performance of building (promulgation 364/2012 Z.z.) – using of energy certificate.Although very significant aspect in this process is the way to implement complex environmental engineering, efficiency of the entire system, the heating medium, renewable energy, energy efficiency is the basis on specific heat consumption for heating. Paper is dealing with assessment of this parameter.


2011 ◽  
Vol 32 (4) ◽  
pp. 101-107 ◽  
Author(s):  
Henryk Rusinowski ◽  
Grzegorz Szapajko

Energy evaluation of steam-water cycle operation with mathematical modelling application In recent years, we can observe the development of the thermal diagnosis and operating control systems based on measuring techniques and mathematical modelling of processes improvement. Evaluation of the actual operating state is insufficient to make an optimal operating decisions. Thus, information about the influence of the operating parameters' deviations from the reference state on indicators describing energy consumption of the process (for example specific heat consumption or specific energy consumption) is also necessary. The paper presents methods for generation the information about the influence of the steam-water cycle operating parameters on specific heat consumption in a turbine's cycle. A mathematical model of steam-water cycle for a CHP (Cogeneration - also Combined Heat and Power) unit is being worked out. Methods for calculation of operating deviations with the application of correction curves and a mathematical model are described. Exemplary calculation results are presented.


2008 ◽  
Vol 62 (1) ◽  
pp. 13-24
Author(s):  
Zorana Arsenijevic ◽  
Zeljko Grbavcic ◽  
Radmila Garic-Grulovic

A fluid bed dryer with inert particles represents a very attractive alternative to other drying technologies according to the main efficiency criteria, i.e. specific water evaporation rate, specific heat consumption and speci?fic air consumption. A high drying efficiency results from the large con?tact area and from the large temperature difference between the inlet and outlet air. A rapid mixing of the particles leads to nearly isothermal conditions throughout the bed. A fluid bed dryer with inert particles was used for drying of slurries. Experiments were performed in a cylindrical column 215 mm in diameter with glass spheres as inert particles. In this paper, results of drying experi?ments with slurries of Zineb fungicide, copper hydroxide, calcium carbo?nate and pure water used as the feed material are presented. In our fluidized bed we successfully dried a number of other materials such as: fungicides and pesticides (Ziram, Propineb, Mangozeb, copper oxy-chloride, copper oxy-sulphate, Bordeaux mixture), other inorganic compounds (calcium sulphate, cobalt carbonate, electrolytic copper, sodium chloride), and a complex compound (organo-bentonite). The effects of operating conditions on dryer throughput and product quality were investigated. Main performance criteria, i.e. specific water evaporation rate, specific heat consumption and specific air consumption, were quantified. Temperature profile along the bed was mapped, and nearly isothermal conditions were found due to thorough mixing of the particles. Analysis of drying and energy efficiencies as a function of inlet and outlet air temperature difference was performed for deeper insight in dryer behavior and for optimizing dryer design and operation from an energy point of view. A simple mathematical model based on an overall heat balance predicts the dryer performance quite well. The industrial prototype with fluid bed of 0.8 m in diameter and capacity 650 kg of evaporated moisture per hour was realized on the basis of presented investigations on pilot unit. The most important results are 50% decrease in energy consumption and no-additional grinding of dried product in comparison with old tunnel drying technology.


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