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·India has the potential to monetise the huge high ash coal reserves through gasification based polygeneration; as on April 2022 estimated coal reserves including lignites in India stand at 408 billion tons of which 48% are proven [1] These vast and largely untapped coal reserves present opportunities to promote energy security in a reliable manner through co
·The co burning profiles of different blends had been compared with the profiles of high ash coal and waste tyre Fig 1 a c shows the TG and DTG profiles of the blends high ash coal and waste tyre The characteristic parameters were obtained from the burning profiles as shown in Table Download Download full size image Fig 1
·Due to the low volatiles content the maximum values of the mass loss rate for coal containing raw materials in an inert gas are almost two orders of magnitude lower than for biomass the corresponding DTG dependences are not shown in Fig 1 and are shifted to the high temperature air flow the mass losses due to oxidation for CC and ASW are
Mechanism experiments were performed to investigate NO x formation and reduction during the combustion of high ash low volatile coal Additionally industrial scale trials were conducted to study the effects of air staging degree on the combustion and NO x emission characteristics of high ash coal on a 350 MW supercritical down fired boiler The results showed that the total
·Since the Indian coals are high ash content and the nature of low ash coal is completely different from Indian coal In the present communication an effort has been made to investigate the effect of alkali concentration and followed by acid treated on the demineralization of high ash coal by varying leaching temperature and contact time and
·Gasification of high ash coal in dry and slurry entrained flow gasifiers is investigated through equilibrium modeling Effects of oxygen and steam to coal mass flow rate ratios in a dry fed gasifier and also the effect of water concentration in slurry on composition temperature heating value and cold gas efficiency are studied
·Many different kinds of coal do naturally occur and due to shrinking natural resources there has been a substantial gain of interest in poor ash rich coal Beside the quality of coal there is a number of other parameters influencing the efficiency of coal gasification such as temperature pressure and reactor type
·The presence of high ash in the coal matrix resulted in low yield and low quality of carbon nanostructures Importantly coal chars produced via microwave pyrolysis possess high specific surface area 130 m 2 g −1 as compared to coal chars from other studies which is primarily due to the microwave effect The coal tar was rich in
·Co gasification of coal and biomass emerged as an alternative clean energy source to produce syngas useful for power generation manufacturing of chemicals and fertilizers [[1] [2] [3]] Technically co gasification is a thermochemical conversion or transformation of carbonaceous constituents of coal and biomass into syngas mainly consist of H 2 CO CO 2
·Considerable literature existing on coal combustion is focused on low ash < 10% content coal Chen et al 2015 In contrast Indian utilities burn coal having very high ash content typically 30% 40% and sometimes up to 50% Zhang et al 2013a b Combustion behaviour of these high ash coals could be different from that of low ash coal
·The present paper is a part of the study done on settling of coal fines by flocculation to enhance the clarification efficiency such that the process water could be recycled in coal washing circuits In this study flocculation performance results of the tests carried out using two polymer flocculants namely Nalco 83370 and Magna 1011 varied at different pulp
·The ash fusion temperature AFT of gasification feedstock is an important parameter for all gasifiers For fluidised bed gasifiers the upper operating temperature is determined by AFT to avoid ash agglomeration [1] For entrained flow gasifiers the operating temperature should be above the flow temperature FT of coal ash to ensure slag flow from
·The coal ash fusion temperature AFT is an important parameter on coal ash fouling and slagging properties It determines the behavior of coal ash in the processes of coal combustion gasification liquefaction and ash utilization [1] [2] [3] It can cause slagging problems on combustion chamber and pipe surfaces and decline heat transfer efficiency [4] [5]
·High ash coal also known as low grade coal has becomes a viable alternative in recent years to high quality coal because available resources have become increasingly scarce due to extensive mining activity This work aims to provide a comprehensive understanding of the structural characteristics of high ash coal and construct a plausible molecular structure to
·These results once again illustrate that coal particles are positively charged relative to the inorganic matter and accordingly the low ash coal particles are collected at the negative electrode A clean coal of 18% ash was collected in bin 4 indicating that it was possible to beneficiate the 43% ash coal by tribo electrostatic method
·Ash deposition phenomena are influenced by coal type ash composition fusion temperature and the distribution of mineral matter reaction atmosphere particle temperature and so forth [10] The adjustment of AFT is generally achieved by adding flux [11] [12] and coal blending [13] In the aspect of adding flux Jing et al found that the formation of low melting
·The present research shows the combustion characteristics of different specific gravity fractions of high ash thermal coal Coal with different mean specific gravity SGM ranging from to was produced using the float sink experiment All SGM coals were characterized with proximate analysis ultimate analysis higher heating value ash analysis
·This coal sample mainly consists of high ash coal particles kg/L density fraction The weight of coal particle with the density less than kg/L is only % with ash content of % It means the coal sample contains a small part of low ash materials and is difficult to separate the low ash components from high ash gangue particles
Premium Grade Coal with high heat output and very low ash For use in Coal Size large Heat Output Ash Content Low Bag weight s 20kg / 25kg / 50kg Hi Flame Colombian Doubles Quality is the same as Hi Flame Colombian Coal but smaller For use in Coal Size medium Heat Output Ash Content
·In the coal based combustion and gasification processes the mineral matter contained in the coal predominantly oxides is left as an incombustible residue termed ash Commonly ash deposits are formed on the heat absorbing surfaces of the exposed equipment of the combustion/gasification processes These deposits lead to the occurrence of slagging or
·An advanced low NOx burner [10] [11] which is designed to have a combustion capacity of approximately 100 kg/h on bituminous coal combustion is used Combustion air supplied by a forced draft fan is injected into the furnace through the burner and the two stage combustion air ports and the air through the burner is divided into primary air secondary air
·The present research shows the combustion characteristics of different specific gravity fractions of high ash thermal coal Coal with different mean specific gravity SGM ranging from to was produced using the float sink experiment All SGM coals were characterized with proximate analysis ultimate analysis higher heating value ash analysis
·High ash coal also known as low grade coal has becomes a viable alternative in recent years to high quality coal because available resources have become increasingly scarce due to extensive
·Oil agglomeration is an alternative technique for the cleaning and upgrading of low rank coal or high ash content coal slimes Therefore this approach was used to beneficiate coal slime with high ash content of % in this work The single factor tests of oil agglomeration were performed to determine the appropriate ranges for various
·In this study a model of the supercritical coal fired power plant CFPP fed with a high ash coal was developed and validated a validated model of a PCC pilot plant using monoethanolamine MEA solvent is scaled up to meet the CFPP capacity a CO 2 compression unit model was developed to fully assess the energy penalty and the three models
·Fouling and slagging are major challenges that impede the clean and efficient use of high sodium coals HC for power generation To address these persistent issues this study examined the impact of sodium Na on ash melting behaviors and assessed the feasibility of mitigating fouling and slagging through the co combustion of HC with coal gangue CG
·For −3 2 mm fine coal the cleaned coal yield was % the ash content of clean coal was % and the deash rate could reach % The shallow bed dense phase gas−solid fluidized bed exhibited poor liquidity and high viscosity under conditions of