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  <channel rdf:about="http://localhost:8081/jspui/handle/123456789/121">
    <title>DSpace Collection:</title>
    <link>http://localhost:8081/jspui/handle/123456789/121</link>
    <description />
    <items>
      <rdf:Seq>
        <rdf:li rdf:resource="http://localhost:8081/jspui/handle/123456789/20782" />
        <rdf:li rdf:resource="http://localhost:8081/jspui/handle/123456789/20781" />
        <rdf:li rdf:resource="http://localhost:8081/jspui/handle/123456789/20780" />
        <rdf:li rdf:resource="http://localhost:8081/jspui/handle/123456789/20779" />
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    </items>
    <dc:date>2026-05-10T05:38:02Z</dc:date>
  </channel>
  <item rdf:about="http://localhost:8081/jspui/handle/123456789/20782">
    <title>NUMERICAL INVESTIGATION OF BURNING BEHAVIOR OF  POWER CABLES</title>
    <link>http://localhost:8081/jspui/handle/123456789/20782</link>
    <description>Title: NUMERICAL INVESTIGATION OF BURNING BEHAVIOR OF  POWER CABLES
Authors: Meena, Mukut Kumar
Abstract: Numerical simulation is used to increase the knowledge base for the failure of instrumentation or &#xD;
control cables utilized in the power industry. With the development of new technologies, the &#xD;
energy demand is continuously increasing and so for the transmission of these energies power &#xD;
cables are required. Nowadays, there are many incidents in industrial as well as residential areas &#xD;
where cables become one of the major concerns because of their combustible nature and it becomes &#xD;
a source of fire itself. The help of numerical modeling of fires in cables can help in the development &#xD;
of procedures, and norms, which we can implement, to protect the personnel to prevent material &#xD;
and economic losses. The model used for the simulation includes the electrical core of the &#xD;
conductors, the enveloping insulation, the filler material, steel armour, and the jacket. A constant &#xD;
current is supplied to the cable for study one but during the second study, a continuous current is &#xD;
supplied simultaneously with an average heat flux applied to the cable for one-fourth part of the &#xD;
cable until a short circuit in the cable i.e. failure of the cable after average heat flux applied than &#xD;
the third study started with same conditions only change is that there is an internal fire in the cable &#xD;
due to short circuit, and after complete burning of the cable cooling phase of the cable has been &#xD;
started i.e. the fourth study. The temperature distribution of the different layers of the cable, and &#xD;
incident heat flux will be measured for the ten different simulations with necessary changes &#xD;
according to experiments and to validate these numerical data compared them with &#xD;
experimentation, the correlation was found to be a conservative estimate of the time of failure.</description>
    <dc:date>2022-04-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://localhost:8081/jspui/handle/123456789/20781">
    <title>PLATE HEAT EXCHANGERS: AN INVESTIGATIVE STUDY</title>
    <link>http://localhost:8081/jspui/handle/123456789/20781</link>
    <description>Title: PLATE HEAT EXCHANGERS: AN INVESTIGATIVE STUDY
Authors: Ali, Noureldin Omer Abdellatif
Abstract: A gasket plate heat exchanger is a vital heat recovery equipment that exchanges heat from high to &#xD;
low fluid Temperature with the help of corrugation plates. The heat exchanger plates provide a &#xD;
large surface area for heat transfer per unit volume. So now days play an important part in &#xD;
industrialized society, as energy demands rise, and its performance must increment as well. They &#xD;
have been widely used in various industrial applications, including chemical, chilling water and &#xD;
dairy. &#xD;
In the present work, the thermal modeling and optimal solution design of the gasket plate heat &#xD;
exchanger have been presented. For the numerical simulation and range of operating parameters &#xD;
and geometrical have been considered. for performance of the gasket plate heat exchanger has &#xD;
been studied in terms of effectiveness, heat transfer and pressure drop for both fluids. Correlations &#xD;
have been developed to calculate the heat transfer, effectiveness and friction coefficients using the &#xD;
analysis regression process.  &#xD;
The next step has been optimized for the single objective and multi-objective functions, applying &#xD;
genetic algorithm optimisation “MATLAB TOOLS OPTIMIZATION.” This work aims to minimize &#xD;
the entropy generation units (Ns) and annual cost (TAC) for two independent objective functions. &#xD;
The results of optimized designs have been solved after generations for two objectives, single&#xD;
objective and multi-objective Optimization. The optimum solutions decision has been compared &#xD;
for constraint heat transfer and unconstrained optimisation.</description>
    <dc:date>2022-11-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://localhost:8081/jspui/handle/123456789/20780">
    <title>PERFORMANCE ANALYSIS OF EVACUATED TUBE SOLAR  COLLECTOR FOR DIFFERENT CONFIGURATIONS OF THE  ABSORBER</title>
    <link>http://localhost:8081/jspui/handle/123456789/20780</link>
    <description>Title: PERFORMANCE ANALYSIS OF EVACUATED TUBE SOLAR  COLLECTOR FOR DIFFERENT CONFIGURATIONS OF THE  ABSORBER
Authors: Singh, Shivani
Abstract: Solar water heaters (SWHs) are well-established and widely utilized worldwide in renewable &#xD;
energy technology. For low to moderate temperature applications, Flat Plate Solar Collectors are &#xD;
used. There are some advantages like ease to manufacture, no complex tracking devices, &#xD;
utilization of both the diffuse and beam solar radiation components, etc. With these advantages, &#xD;
there are certain limitations, i.e., conduction, convection, and radiation heat loss from the &#xD;
absorber plate. One can reduce the loss by providing proper insulation, incorporating a glazing &#xD;
cover, maintaining the vacuum between the absorber plate, and glazing (to avoid conduction and &#xD;
convection losses), and using a selective absorber surface (to prevent radiation losses). Though &#xD;
it is technically feasible, there are some practical limitations to achieving the above-said &#xD;
objectives (to reduce losses in an FPC). To overcome the above-mention functional limitations &#xD;
evacuated tube solar collectors came into existence. ETSC has two co-axial glass tubes with a &#xD;
selective coating over the inner tube surface and the system maintains a vacuum between tubes. &#xD;
As a part of the thesis, a series of experimental studies has been conducted and compared the &#xD;
performance of marquise shape FPC and ETSC in various modes (with &amp; without glazing in &#xD;
series &amp; parallel orientation for marquise shape FPC and with different reflectors configurations &#xD;
for series &amp; parallel orientation for ETSC) in a forced circulation mode. The study on marquise &#xD;
shape FPC (for 1 to 7lpm, for the month of Sept-Oct 2021) shows that the first law efficiency &#xD;
increases (for 1 to 4lpm) and then decreases (for 4 to 7lpm). The exergy efficiency decreases as &#xD;
the mass flow rate increases (for 1 to 7lpm). The maximum temperature difference acquired was &#xD;
14.49°C (for the series glazed system, for constant solar Irradiation value). The series glazed &#xD;
system shows better performance for lower lpm and the parallel unglazed system shows better &#xD;
performance for higher lpm. A study of ETSC and its comparison with marquise shape FPC, (for &#xD;
1 to 4lpm and constant solar irradiation value for the month of March 2022, for Ac is 1m2 and for &#xD;
an, I value of 920W/m2) shows that the marquise shaped flat plates have acquired the maximum &#xD;
temperature difference up to 9.38°C (for the series glazed system) and 7.66°C for ETSCs with &#xD;
flat reflector. The results show that marquise shape flat plate collectors have better performance &#xD;
output than ETSC in forced circulation mode. The performance comparison of six different &#xD;
ETSC systems (without reflector, flat reflector, triangular reflector; in both series and parallel) &#xD;
has been carried out.  The average Qu in a day (for the same inlet conditions) is getting higher for &#xD;
the flat reflector system with series orientation. The triangular reflector system shows better Qu &#xD;
than other systems when the sun is at its zenith.</description>
    <dc:date>2022-04-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://localhost:8081/jspui/handle/123456789/20779">
    <title>PIN FINNED COOLING: INVESTIGATION OF DESIGN AND  PERFORMANCE</title>
    <link>http://localhost:8081/jspui/handle/123456789/20779</link>
    <description>Title: PIN FINNED COOLING: INVESTIGATION OF DESIGN AND  PERFORMANCE
Authors: Bhaware, Amrutaunsh
Abstract: Gas turbines play an important part in industrialized society and as power demands is increasing, &#xD;
gas turbine power output and thermal efficiency must increase as well. The energy of burning &#xD;
gases and air, which is at high temperature and pressure, is harnessed by the gas turbine power &#xD;
plant by expanding through numerous rings of fixed and moving blades. The principal failure &#xD;
mode of gas turbine blades is 'creep', which is caused by thermal loads. Despite their thickness, &#xD;
turbine blades break before compressor blades. Blade cooling is critical because it permits gas &#xD;
turbines to operate at temperatures above the melting point of the blade material, which is &#xD;
+300°C. Pin-fin is one of the most effective ways used for cooling of gas turbine blades. &#xD;
In the present work, effect of pin fin has been presented with the help of Numerical modelling &#xD;
using Ansys Fluent. The combinations of two different shaped fins are taken into account i.e., &#xD;
one with 45 tilted elliptical shape and other with diamond shape arranged in staggered array is &#xD;
selected. Streamwise and spanwise directions are taken as Sx/D = 2.5 and Sy/D = 2.5 whereas &#xD;
H/D = 2 is taken. In current numerical study we determined the Nusselt No. and friction Factor &#xD;
through pin-fin array for the Reynolds number between 10000 to 50000. Results showed that &#xD;
with increase Reynolds no. thermal performance of pin-fin decreases.</description>
    <dc:date>2022-04-01T00:00:00Z</dc:date>
  </item>
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