MSc Project Proposal: Analysis and Optimization of Boiler Efficiency
VerifiedAdded on 2023/06/11
|6
|2753
|255
Project
AI Summary
This project proposal focuses on analyzing and optimizing boiler efficiency through experimental setup and theoretical calculations. It introduces the concept of boilers, fouling, and the factors affecting boiler efficiency. The literature review discusses relevant research on welding defects, radiographic inspections, and lignite-fired power plant simulations. The proposal outlines research questions related to efficiency, error analysis, and calculations. It details the methodology, including equations for heat balance, fuel combustion, and heat loss. The experimental setup involves maintaining steady-state conditions and measuring various parameters. The expected outcomes include evaluating isentropic efficiency, plotting air/mass ratio vs. efficiency, and conducting error analysis. The project aims to provide insights into improving boiler efficiency and reducing fuel consumption, with potential applications in power plants and industrial settings. Desklib provides access to similar project proposals and study tools for students.
Contribute Materials
Your contribution can guide someone’s learning journey. Share your
documents today.

Prof. Curran/Dr. Saunders, 2013, project template v2
Template Project Proposal and Plan
By ‘Author Name’
Affiliation (MSc Profile or Track) & Study no.
Executive Summary
1. Introduction
A boiler is nothing but a vessel which is closed and in this the fluid mainly the water is heated. It
is not necessary that the fluid would be boiling. Once the fluids are heated up then the fluids
which has been vaporized would be exiting the boilers which is generally used for various
processes of by the heated applications and this includes the heating of the water, generation of
power, cooking, central heating and many more. Fouling is generally considered to be the
deposition that is taking place over the convention heat surfaces. Fouling can be defined as the
deposition of the materials which are unwanted upon the solid surfaces so as to reduce the
functioning of a boiler (Dai et al. 2015). This type of fouling materials might be living as well as
non-living that is inorganic or organic substance. This type of phenomenon is generally
differentiated from the other surface deposition phenomenon. Vaporization of the volatile
inorganic elements while the coal is brunt and this act as the main reason for the fouling.
2. State-of-the-art/Literature Review
According to Hocker et al. the dye penetration has been associated with indicating the effects on
the zones which were affected by the heat of the 2014- T6 aluminum weldments. This has been
associated with causing a lot of rejections related to the production assemblies. Along with this
an investigated has also been associated with revealing the fact that the major portion of the
defects which were indicated were superficially in such a way that the amount is always less than
0.007 deep (Hocker and Wilson 2014). Along with this several tests were also conducted so as to
determine the cause and the nature of the defects occurring on the surface. The procedures were
also developed so as to eliminate or to minimize the occurrence of the indications related to dry
penetration and also for the purpose of discriminating between the effects related to real weld and
the defects related to superficial surface. For the purpose of repairing the weldments which
contains the dye penetration indications various type of procedures were also developed.
Yahia et al. has been associated with discussing the fact that the radiography is generally
considered to be a fact which is associated with evaluating and control that is non-destructive.
Besides this they have also been associated with providing relevance of the various kind of
radiographic inspections adopted by various kind of industries and along with this there also
exists various research projects which are generally aimed at automating the process of analysis
and the discontinuities that occurs in the interpretation of the welding (Muhaisen and Hokoma,
2012). In their work they have been associated with making of the automatic control and the
inspection of the defects in the welding. This has been done by using the edge detection method
Template Project Proposal and Plan
By ‘Author Name’
Affiliation (MSc Profile or Track) & Study no.
Executive Summary
1. Introduction
A boiler is nothing but a vessel which is closed and in this the fluid mainly the water is heated. It
is not necessary that the fluid would be boiling. Once the fluids are heated up then the fluids
which has been vaporized would be exiting the boilers which is generally used for various
processes of by the heated applications and this includes the heating of the water, generation of
power, cooking, central heating and many more. Fouling is generally considered to be the
deposition that is taking place over the convention heat surfaces. Fouling can be defined as the
deposition of the materials which are unwanted upon the solid surfaces so as to reduce the
functioning of a boiler (Dai et al. 2015). This type of fouling materials might be living as well as
non-living that is inorganic or organic substance. This type of phenomenon is generally
differentiated from the other surface deposition phenomenon. Vaporization of the volatile
inorganic elements while the coal is brunt and this act as the main reason for the fouling.
2. State-of-the-art/Literature Review
According to Hocker et al. the dye penetration has been associated with indicating the effects on
the zones which were affected by the heat of the 2014- T6 aluminum weldments. This has been
associated with causing a lot of rejections related to the production assemblies. Along with this
an investigated has also been associated with revealing the fact that the major portion of the
defects which were indicated were superficially in such a way that the amount is always less than
0.007 deep (Hocker and Wilson 2014). Along with this several tests were also conducted so as to
determine the cause and the nature of the defects occurring on the surface. The procedures were
also developed so as to eliminate or to minimize the occurrence of the indications related to dry
penetration and also for the purpose of discriminating between the effects related to real weld and
the defects related to superficial surface. For the purpose of repairing the weldments which
contains the dye penetration indications various type of procedures were also developed.
Yahia et al. has been associated with discussing the fact that the radiography is generally
considered to be a fact which is associated with evaluating and control that is non-destructive.
Besides this they have also been associated with providing relevance of the various kind of
radiographic inspections adopted by various kind of industries and along with this there also
exists various research projects which are generally aimed at automating the process of analysis
and the discontinuities that occurs in the interpretation of the welding (Muhaisen and Hokoma,
2012). In their work they have been associated with making of the automatic control and the
inspection of the defects in the welding. This has been done by using the edge detection method
Secure Best Marks with AI Grader
Need help grading? Try our AI Grader for instant feedback on your assignments.

Prof. Curran/Dr. Saunders, 2013, project template v2
of the radiographic images and is generally dependent upon the usage of the Multilayer
Perceptron or the MPC. This paper has also been associated with providing the definition of the
original method which is related to the detection of the defects present in the radiography and is
generally dependent upon the usage of the neural networks which are artificial in nature along
with aiming in the classification and also the recognition of the default percentage is increased in
a successful way. The work done by them has been divided into four steps and this mainly
includes the following: The first step mainly includes the preparation of the database which is to
be utilized later in order to provide training to the MPC in the second step. Followed by this step
comes the third step which has been classified into two sections the first part is totally devoted for
the purpose of detecting the contours, and after this the second section mainly includes the
elimination of contours which are additional (Wacławiak and Kalisz 2012).
The paper by Samaras et al has been associated with presenting the simulation and optimization
of the results which were obtained from the 300 MW lignite-fired power plant. For the purpose of
reducing the time needed for computation there is need of creating a module in the gPROMS FO
in order to calculate the properties related to thermodynamics and the heat transfer that the fluids
are having is also very much important. Reduction of the variables from the 375,630 to 10,906
has been done by making use of the FOs, besides this they have also been associated with
reducing the number of the parameters present in the model as well (Tzolakis et al. 2012). After
the completion of the simulation in a successful way they have been associated with optimizing
the operations in the plant so as to have improvements in the efficiency along with maintaining
the reduction in the electric power. The results have been associated with showing an absolute
rate of improvement of around 0.55% in the overall thermal efficiency, and along with this it has
been seen that they are having an important effect upon the plants as the resulting benefits
included the lower consumption of the fuel and the lower emission of the fuel gas. Besides this
the results due to reduction also has a lower penalty fee related to pollutions in the environment.
It is considered that this would be leading to the formation of decision tool which might be used
by the control room of the unit (Chen et al. 2012). The model would be working by making use
of the real time data which would be associated with allowing the engineers to make instant
decision.
3. Research Question, Aim/Objectives and Sub-goals
The experiential setup would be designed in order to determine the efficiency that a boiler is
having and also for the purpose of determining the various effects due to different kind of factors.
Heating of the water is generally done by the energy that is released by the process of
combustion.
The research questions associated with the conducting of this experiment has been listed below:
Q1. What the major reasons responsible for affecting the efficiency?
Q2. How the efficiency of the system can be increased?
Q3. What the possible errors that might occurs?
Q4. What are the ways of eliminating the error?
Q5. How are the calculations to be made?
4. Theoretical Content/Methodology
The efficiency that the boiler is having is generally considered to be the ration of the useful heat
that is taken by the water (QW) in order to avail the heat present in the fuel (QR).
of the radiographic images and is generally dependent upon the usage of the Multilayer
Perceptron or the MPC. This paper has also been associated with providing the definition of the
original method which is related to the detection of the defects present in the radiography and is
generally dependent upon the usage of the neural networks which are artificial in nature along
with aiming in the classification and also the recognition of the default percentage is increased in
a successful way. The work done by them has been divided into four steps and this mainly
includes the following: The first step mainly includes the preparation of the database which is to
be utilized later in order to provide training to the MPC in the second step. Followed by this step
comes the third step which has been classified into two sections the first part is totally devoted for
the purpose of detecting the contours, and after this the second section mainly includes the
elimination of contours which are additional (Wacławiak and Kalisz 2012).
The paper by Samaras et al has been associated with presenting the simulation and optimization
of the results which were obtained from the 300 MW lignite-fired power plant. For the purpose of
reducing the time needed for computation there is need of creating a module in the gPROMS FO
in order to calculate the properties related to thermodynamics and the heat transfer that the fluids
are having is also very much important. Reduction of the variables from the 375,630 to 10,906
has been done by making use of the FOs, besides this they have also been associated with
reducing the number of the parameters present in the model as well (Tzolakis et al. 2012). After
the completion of the simulation in a successful way they have been associated with optimizing
the operations in the plant so as to have improvements in the efficiency along with maintaining
the reduction in the electric power. The results have been associated with showing an absolute
rate of improvement of around 0.55% in the overall thermal efficiency, and along with this it has
been seen that they are having an important effect upon the plants as the resulting benefits
included the lower consumption of the fuel and the lower emission of the fuel gas. Besides this
the results due to reduction also has a lower penalty fee related to pollutions in the environment.
It is considered that this would be leading to the formation of decision tool which might be used
by the control room of the unit (Chen et al. 2012). The model would be working by making use
of the real time data which would be associated with allowing the engineers to make instant
decision.
3. Research Question, Aim/Objectives and Sub-goals
The experiential setup would be designed in order to determine the efficiency that a boiler is
having and also for the purpose of determining the various effects due to different kind of factors.
Heating of the water is generally done by the energy that is released by the process of
combustion.
The research questions associated with the conducting of this experiment has been listed below:
Q1. What the major reasons responsible for affecting the efficiency?
Q2. How the efficiency of the system can be increased?
Q3. What the possible errors that might occurs?
Q4. What are the ways of eliminating the error?
Q5. How are the calculations to be made?
4. Theoretical Content/Methodology
The efficiency that the boiler is having is generally considered to be the ration of the useful heat
that is taken by the water (QW) in order to avail the heat present in the fuel (QR).

Prof. Curran/Dr. Saunders, 2013, project template v2
Equtaion 1
The units efficiency would be affceted during the experiment and this is mainly due to the
combution which is incomplet(Qi), loss of heat from the exhaust (Qe) and lastly the loss of heat
from the environemnt (Q). In order to check the quantities which is measured
there is a need of balancing the heat (Baxter and DeSollar 2013).
Equation 2
The heat that is available in the fuel (Qf) can be identified from the complete combustion process
and this is done by writing the balance equation of the fuel.
Equation 3
hf is generally considered to be enthalpy for the formation of the substances
(kj/kg) which is generally done at a temperature of T0, 298K.
The fuel consumption is generally determined by making use of the results
obtained from analyzing the gas.
The heat that is obtained by the water is generally obtained from the measurements done on water
and also on the ambient conditions.
In order to calculate the loss of heat occurring in the chamber associated with combustion which
preset in the boiler towards the surrounding is QThis is associated with usage of the heat
transfer method.
Equation 4
In this the h is generally considered to the conventional heat transfer coefficient where h=25
W/m2K, the surrounding temperature is the T. The area A is generally obtained from the S and
the L, where S is considered to be the parameter of the combustion chamber which is around
163cm whereas the L is considered to be the length that the combustion chamber is having which
is around 97 cm. T(x) is generally considered to be the temperature at the x location of the boiler.
It is also possible to find the heat loss from the exhaust and this can be done by the equation
provided below:
Equation 5
It is also possible to calculate the effects that the incomplete combustion is having from the
equation provided below:
Equation 6
Lastly the efficiency of the boiler can be estimated by making use of the eqation provided below:
Equtaion 1
The units efficiency would be affceted during the experiment and this is mainly due to the
combution which is incomplet(Qi), loss of heat from the exhaust (Qe) and lastly the loss of heat
from the environemnt (Q). In order to check the quantities which is measured
there is a need of balancing the heat (Baxter and DeSollar 2013).
Equation 2
The heat that is available in the fuel (Qf) can be identified from the complete combustion process
and this is done by writing the balance equation of the fuel.
Equation 3
hf is generally considered to be enthalpy for the formation of the substances
(kj/kg) which is generally done at a temperature of T0, 298K.
The fuel consumption is generally determined by making use of the results
obtained from analyzing the gas.
The heat that is obtained by the water is generally obtained from the measurements done on water
and also on the ambient conditions.
In order to calculate the loss of heat occurring in the chamber associated with combustion which
preset in the boiler towards the surrounding is QThis is associated with usage of the heat
transfer method.
Equation 4
In this the h is generally considered to the conventional heat transfer coefficient where h=25
W/m2K, the surrounding temperature is the T. The area A is generally obtained from the S and
the L, where S is considered to be the parameter of the combustion chamber which is around
163cm whereas the L is considered to be the length that the combustion chamber is having which
is around 97 cm. T(x) is generally considered to be the temperature at the x location of the boiler.
It is also possible to find the heat loss from the exhaust and this can be done by the equation
provided below:
Equation 5
It is also possible to calculate the effects that the incomplete combustion is having from the
equation provided below:
Equation 6
Lastly the efficiency of the boiler can be estimated by making use of the eqation provided below:

Prof. Curran/Dr. Saunders, 2013, project template v2
Equation 7
5. Experimental Set-up
This unit would be associated with igniting and allowing the achievement of the steady state
condition by having the correct ratio of air and fuel. Besides this the flow of the water is to be
adjusted in order to provide a high outlet temperature by having a temperature of around 800C.
Along with this an extra care is to be taken by having a constant observation over the entire
experiment. During the measurements of the steady condition are generally taken of everything
which is generally associated with the process of contributing towards the gain or loss of the heat
taking place in the system and these mainly includes the rate of flow and the temperature, heating
of the cold water, temperature of the fuel gas and the composition they are having and lastly the
loss of heat taking place towards the environment from the surface of the unit. Besides this it is
also compulsory to measure the temperature of the fuel gas by making use of devices like the
suction pyrometer. Besides this it is possible to estimate the losses taking place from the Unit
surface as well. The gas flow analyzer would be used for the purpose of determining the
composition of the gas that is coming from the exhaust.
6. Results, Outcome and Relevance
After the completion of the experiment it is possible to evaluate the isentropic efficiency from the
values that are measured from the experiment. After the measurement of the experiment is
completed then there is a need of plotting a graph of the air/mass ratio vs the efficiency. All the
calculations ate conducted in order to have a clear result and also to show the estimations that has
been made. The results are then shown in a tabulated format. After the completion of the
experiment it is possible to identify the causes responsible for the various kind of errors that are
made in the experiment. After this a detailed error analysis is to be made.
Equation 7
5. Experimental Set-up
This unit would be associated with igniting and allowing the achievement of the steady state
condition by having the correct ratio of air and fuel. Besides this the flow of the water is to be
adjusted in order to provide a high outlet temperature by having a temperature of around 800C.
Along with this an extra care is to be taken by having a constant observation over the entire
experiment. During the measurements of the steady condition are generally taken of everything
which is generally associated with the process of contributing towards the gain or loss of the heat
taking place in the system and these mainly includes the rate of flow and the temperature, heating
of the cold water, temperature of the fuel gas and the composition they are having and lastly the
loss of heat taking place towards the environment from the surface of the unit. Besides this it is
also compulsory to measure the temperature of the fuel gas by making use of devices like the
suction pyrometer. Besides this it is possible to estimate the losses taking place from the Unit
surface as well. The gas flow analyzer would be used for the purpose of determining the
composition of the gas that is coming from the exhaust.
6. Results, Outcome and Relevance
After the completion of the experiment it is possible to evaluate the isentropic efficiency from the
values that are measured from the experiment. After the measurement of the experiment is
completed then there is a need of plotting a graph of the air/mass ratio vs the efficiency. All the
calculations ate conducted in order to have a clear result and also to show the estimations that has
been made. The results are then shown in a tabulated format. After the completion of the
experiment it is possible to identify the causes responsible for the various kind of errors that are
made in the experiment. After this a detailed error analysis is to be made.
Secure Best Marks with AI Grader
Need help grading? Try our AI Grader for instant feedback on your assignments.

Prof. Curran/Dr. Saunders, 2013, project template v2
7. Project Planning and Gantt chart
Fig 1: Gantt Chart
(Source: Created by Author)
8. Conclusions
The experiment helps in concluding to the fact that it is associated with providing a lot of gain as
well as loss in the amount of heat along with providing the ways of heating up of the cold water,
the temperature that the gas is having which is used for fueling the system and many more.
Measurement of the temperature can also be done by identification of the various kind of
equipment’s and besides this it is also possible to estimate the heat loss as well. The composition
that the fueling gas and the emitted gas is having can also be easily determined by use of this
experiment.
9. References
Baxter, L. and DeSollar, R. eds., 2013. Applications of advanced technology to ash-related
problems in boilers. Springer Science & Business Media.
7. Project Planning and Gantt chart
Fig 1: Gantt Chart
(Source: Created by Author)
8. Conclusions
The experiment helps in concluding to the fact that it is associated with providing a lot of gain as
well as loss in the amount of heat along with providing the ways of heating up of the cold water,
the temperature that the gas is having which is used for fueling the system and many more.
Measurement of the temperature can also be done by identification of the various kind of
equipment’s and besides this it is also possible to estimate the heat loss as well. The composition
that the fueling gas and the emitted gas is having can also be easily determined by use of this
experiment.
9. References
Baxter, L. and DeSollar, R. eds., 2013. Applications of advanced technology to ash-related
problems in boilers. Springer Science & Business Media.

Prof. Curran/Dr. Saunders, 2013, project template v2
Chen, Q., Finney, K., Li, H., Zhang, X., Zhou, J., Sharifi, V. and Swithenbank, J., 2012.
Condensing boiler applications in the process industry. Applied Energy, 89(1), pp.30-36.
Dai, B.Q., Wu, X., De Girolamo, A. and Zhang, L., 2015. Inhibition of lignite ash slagging and
fouling upon the use of a silica-based additive in an industrial pulverised coal-fired boiler. Part 1.
Changes on the properties of ash deposits along the furnace. Fuel, 139, pp.720-732.
Li, J., Brzdekiewicz, A., Yang, W. and Blasiak, W., 2012. Co-firing based on biomass
torrefaction in a pulverized coal boiler with aim of 100% fuel switching. Applied Energy, 99,
pp.344-354.
Low, F., De Girolamo, A., Wu, X., Dai, B. and Zhang, L., 2015. Inhibition of lignite ash slagging
and fouling upon the use of a silica-based additive in an industrial pulverised coal-fired boiler:
Part 3–Partitioning of trace elements. Fuel, 139, pp.746-756.
Luan, C., You, C. and Zhang, D., 2014. An experimental investigation into the characteristics and
deposition mechanism of high-viscosity coal ash. Fuel, 119, pp.14-20.
Muhaisen, N.A.R. and Hokoma, R.A., 2012. Calculating the Efficiency of Steam Boilers Based
on Its Most Effecting Factors: A Case Study. WorldAcademy of Science, Engeneering and
Technology, 6.
Pan, Y., Si, F., Xu, Z., Romero, C.E., Qiao, Z. and Ye, Y., 2012. DEM simulation and fractal
analysis of particulate fouling on coal-fired utility boilers' heating surfaces. Powder
technology, 231, pp.70-76.
Panagiotidis, I., Vafiadis, K., Tourlidakis, A. and Tomboulides, A., 2015. Study of slagging and
fouling mechanisms in a lignite-fired power plant. Applied Thermal Engineering, 74, pp.156-164.
Patiño, D., Crespo, B., Porteiro, J. and Míguez, J.L., 2016. Experimental analysis of fouling rates
in two small-scale domestic boilers. Applied Thermal Engineering, 100, pp.849-860.
Pérez, M.G., Vakkilainen, E. and Hyppänen, T., 2016. Fouling growth modeling of kraft
recovery boiler fume ash deposits with dynamic meshes and a mechanistic sticking
approach. Fuel, 185, pp.872-885.
Stam, A.F., Haasnoot, K. and Brem, G., 2014. Superheater fouling in a BFB boiler firing wood-
based fuel blends. Fuel, 135, pp.322-331.
Tzolakis, G., Papanikolaou, P., Kolokotronis, D., Samaras, N., Tourlidakis, A. and Tomboulides,
A., 2012. Simulation of a coal-fired power plant using mathematical programming algorithms in
order to optimize its efficiency. Applied Thermal Engineering, 48, pp.256-267.Hocker, R.G. and
Wilson, K.R., 2014. Dye Penetrant Indications Caused by Superficial Surface Defects in 2014
Aluminum Alloy Welds. Weld. J, pp.50-11.
Wacławiak, K. and Kalisz, S., 2012. A practical numerical approach for prediction of particulate
fouling in PC boilers. Fuel, 97, pp.38-48.
Yang, Z.C., LIU, J.L. and Yao, W., 2013. Fouling index of Zhundong coal ash. Clean Coal
Technology, 2, pp.81-84.
Chen, Q., Finney, K., Li, H., Zhang, X., Zhou, J., Sharifi, V. and Swithenbank, J., 2012.
Condensing boiler applications in the process industry. Applied Energy, 89(1), pp.30-36.
Dai, B.Q., Wu, X., De Girolamo, A. and Zhang, L., 2015. Inhibition of lignite ash slagging and
fouling upon the use of a silica-based additive in an industrial pulverised coal-fired boiler. Part 1.
Changes on the properties of ash deposits along the furnace. Fuel, 139, pp.720-732.
Li, J., Brzdekiewicz, A., Yang, W. and Blasiak, W., 2012. Co-firing based on biomass
torrefaction in a pulverized coal boiler with aim of 100% fuel switching. Applied Energy, 99,
pp.344-354.
Low, F., De Girolamo, A., Wu, X., Dai, B. and Zhang, L., 2015. Inhibition of lignite ash slagging
and fouling upon the use of a silica-based additive in an industrial pulverised coal-fired boiler:
Part 3–Partitioning of trace elements. Fuel, 139, pp.746-756.
Luan, C., You, C. and Zhang, D., 2014. An experimental investigation into the characteristics and
deposition mechanism of high-viscosity coal ash. Fuel, 119, pp.14-20.
Muhaisen, N.A.R. and Hokoma, R.A., 2012. Calculating the Efficiency of Steam Boilers Based
on Its Most Effecting Factors: A Case Study. WorldAcademy of Science, Engeneering and
Technology, 6.
Pan, Y., Si, F., Xu, Z., Romero, C.E., Qiao, Z. and Ye, Y., 2012. DEM simulation and fractal
analysis of particulate fouling on coal-fired utility boilers' heating surfaces. Powder
technology, 231, pp.70-76.
Panagiotidis, I., Vafiadis, K., Tourlidakis, A. and Tomboulides, A., 2015. Study of slagging and
fouling mechanisms in a lignite-fired power plant. Applied Thermal Engineering, 74, pp.156-164.
Patiño, D., Crespo, B., Porteiro, J. and Míguez, J.L., 2016. Experimental analysis of fouling rates
in two small-scale domestic boilers. Applied Thermal Engineering, 100, pp.849-860.
Pérez, M.G., Vakkilainen, E. and Hyppänen, T., 2016. Fouling growth modeling of kraft
recovery boiler fume ash deposits with dynamic meshes and a mechanistic sticking
approach. Fuel, 185, pp.872-885.
Stam, A.F., Haasnoot, K. and Brem, G., 2014. Superheater fouling in a BFB boiler firing wood-
based fuel blends. Fuel, 135, pp.322-331.
Tzolakis, G., Papanikolaou, P., Kolokotronis, D., Samaras, N., Tourlidakis, A. and Tomboulides,
A., 2012. Simulation of a coal-fired power plant using mathematical programming algorithms in
order to optimize its efficiency. Applied Thermal Engineering, 48, pp.256-267.Hocker, R.G. and
Wilson, K.R., 2014. Dye Penetrant Indications Caused by Superficial Surface Defects in 2014
Aluminum Alloy Welds. Weld. J, pp.50-11.
Wacławiak, K. and Kalisz, S., 2012. A practical numerical approach for prediction of particulate
fouling in PC boilers. Fuel, 97, pp.38-48.
Yang, Z.C., LIU, J.L. and Yao, W., 2013. Fouling index of Zhundong coal ash. Clean Coal
Technology, 2, pp.81-84.
1 out of 6

Your All-in-One AI-Powered Toolkit for Academic Success.
+13062052269
info@desklib.com
Available 24*7 on WhatsApp / Email
Unlock your academic potential
© 2024 | Zucol Services PVT LTD | All rights reserved.