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Project Phase – I
                             Review -I



Development of green telecom networks by employing
 Solar driven Absorption Chiller (SAC) - Phase Change
   Material (PCM) Integrated Technology (SAPIT) for
     cooling telecommunication shelters in India

  Undertaken by: Anirudh B                Mentored by: Dr.R.Velavan
          11MN01                             Associate Professor
                                              School of Energy
        PG Scholar                        PSG College of Technology
   ME Energy Engineering
      School of Energy
  PSG College of Technology
Project motivation

 The Indian Telecommunications network is the third largest in the
  world and the second largest among the emerging economies of Asia
 By March 2009 there were as many as 2,58,459 telecom towers in
  the country and with a customer base of more than 600 million
  subscribers in 2011, 1,50,000 more towers were installed to meet
  the demand.
 Erecting one telecom tower involves an investment of about Rs. 30
  lakhs
 Power consumed by a telecom tower varies from 1-5kW (24X7)
 A telecom tower is installed with a DG set of 20kVA capacity running
  16-20hrs (rural/semi-urban) a day , thereby consuming 4000lts per
  year and emitting 10 tons of CO2 per year.
 Out of which nearly 60% of the power is required for ventilation
  requirements in the form of air-conditioning.
Literature Review

 Design of a solar absorption cooling system in a Greek hospital
  T. Tsoutsos , E. Aloumpi , Z. Gkouskos , M. Karagiorgas
 Energy and Buildings (2009)

 The authors have used Transient System Simulation Program (TRNSYS)
 v.15 to simulate a hospital building in Greek to calculate its cooling
 and heating demand and thereby designed a LiBr-H2O Solar absorption
 cooling system and also made feasibility study based on economic
 analysis.
 Modeling of a solar powered absorption cycle for Abu Dhabi
  A. Al-Alili, M.D. Islam , I. Kubo, Y. Hwang, R. Radermacher,
 Applied Energy (2012)

 The authors have modeled and studied the feasibility of implementing
 NH3-H2O solar absorption cooling system for Abu Dhabi’s weather
 conditions using TRNSYS
Literature Review

 Solar Thermal Driven Cooling System for a Data Center in
  Albuquerque New Mexico
 N. Fumo, V. Bortone, J. C. Zambrano,
 Journal of Solar Energy Engineering, ASME(2011)

 The authors have done a theoretical analysis based energy, exergy and
 cost of an absorption chiller driven by solar thermal energy as cooling
 plant alternative for data centers
 Design and performance of solar powered absorption cooling
  systems in office buildings
 Ursula Eicker, Dirk Pietruschka
 Energy and Buildings (2009)

 The authors have modeled and simulated the feasibility of
 implementing LiBr-H2O solar absorption cooling system in office
 buildings in Germany using TRNSYS
Literature Review

 A second law analysis and entropy generation minimization of an
  absorption chiller
 Aung Myat, Kyaw Thu, Young-Deuk Kim, A. Chakraborty, Won Gee Chun, Kim
 Choon Ng
 Applied Thermal Engineering (2011)
 The authors have done a performance analysis of an absorption refrigeration
 system using entropy generation under transient conditions. Genetic
 Algorithm was used as an optimization tool to locate the system minimum
 under all defined domain of heat sources and cooling water temperatures
 Optimization of a solar driven absorption refrigerator in the transient
   regime
 Mouna Hamed, Ali Fellah, Ammar Ben Brahim
 Applied Energy (2012)
 The authors have done a theoretical study in dynamic mode of an absorption
 refrigerator endoreversible Model . A global minimizing time optimization is
 performed in view to reach maximum performances. A mathematical model
 combining the classical thermodynamics and heat and mass transfers
 principles was developed
Identified research variables for future work

Optimization of Collector size
Collector inclination angle
Hot water flow rate
Hot water temperature
Chilled water temperature (inlet/outlet)
Chilled water flow rate
Type of Refrigerants
Types of Phase Change Materials
Concentration of LiBr-H2O
Solution flow rate
Cooling water flow rate
Proposed Activity of research
Proposed Activity of research
S.no   Equipment required     Specifications                                               Unit cost     No. of     Total cost
                                                                                                         units      (`)
1      Telecom cabinet        1 × 0.5 × 0.75m                                              -             1          10000
2      Vapour Absorption      Hot water based Vapour Absorption chiller - 0.5TR            25000 `/kW    1          50000
       chiller (including
       cooling tower)
3      Solar Evacuated tube   Size:1.5𝑚2                                                   12500 `/m2    1          25000
       collectors             Evacuated glass tube with selective coating
4      Resistance heater      500W                                                         2000 `/kW     2          4000
5      Thermal Storage tank   0.3m3                                                        7500 `/m3     1          2275


6      PCM panels             HS-29 (Inorganic salt) in HDPE panels (1000 × 160 × 16mm),   1000 `/kg     5 panels   7000
                              Phase change temp: 27 to 29oC                                              (7kg)
                              Density: 1150kg/m3, Operating range: 22 to 34oC
                              Latent heat: 190 kJ/kg



7      Thermocouples          K-Type, Range: -200oC to +1350oC, Resolution: 0.1oC from -   300 `/piece   10 Nos.    3000
                              200oC to 640oC, Accuracy: ±1oC


8      Insulation             Polyurethane foam insulation for both thermal storage tank   -             -          2000
                              andtelecom cabinet
9      Labour + contigency    -                                                            -             -          10000


10     Total                  -                                                            -             -          1,13,275
Milestone for completion

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11 mn01 review 1

  • 1. Project Phase – I Review -I Development of green telecom networks by employing Solar driven Absorption Chiller (SAC) - Phase Change Material (PCM) Integrated Technology (SAPIT) for cooling telecommunication shelters in India Undertaken by: Anirudh B Mentored by: Dr.R.Velavan 11MN01 Associate Professor School of Energy PG Scholar PSG College of Technology ME Energy Engineering School of Energy PSG College of Technology
  • 2. Project motivation The Indian Telecommunications network is the third largest in the world and the second largest among the emerging economies of Asia By March 2009 there were as many as 2,58,459 telecom towers in the country and with a customer base of more than 600 million subscribers in 2011, 1,50,000 more towers were installed to meet the demand. Erecting one telecom tower involves an investment of about Rs. 30 lakhs Power consumed by a telecom tower varies from 1-5kW (24X7) A telecom tower is installed with a DG set of 20kVA capacity running 16-20hrs (rural/semi-urban) a day , thereby consuming 4000lts per year and emitting 10 tons of CO2 per year. Out of which nearly 60% of the power is required for ventilation requirements in the form of air-conditioning.
  • 3. Literature Review Design of a solar absorption cooling system in a Greek hospital T. Tsoutsos , E. Aloumpi , Z. Gkouskos , M. Karagiorgas Energy and Buildings (2009) The authors have used Transient System Simulation Program (TRNSYS) v.15 to simulate a hospital building in Greek to calculate its cooling and heating demand and thereby designed a LiBr-H2O Solar absorption cooling system and also made feasibility study based on economic analysis. Modeling of a solar powered absorption cycle for Abu Dhabi A. Al-Alili, M.D. Islam , I. Kubo, Y. Hwang, R. Radermacher, Applied Energy (2012) The authors have modeled and studied the feasibility of implementing NH3-H2O solar absorption cooling system for Abu Dhabi’s weather conditions using TRNSYS
  • 4. Literature Review Solar Thermal Driven Cooling System for a Data Center in Albuquerque New Mexico N. Fumo, V. Bortone, J. C. Zambrano, Journal of Solar Energy Engineering, ASME(2011) The authors have done a theoretical analysis based energy, exergy and cost of an absorption chiller driven by solar thermal energy as cooling plant alternative for data centers Design and performance of solar powered absorption cooling systems in office buildings Ursula Eicker, Dirk Pietruschka Energy and Buildings (2009) The authors have modeled and simulated the feasibility of implementing LiBr-H2O solar absorption cooling system in office buildings in Germany using TRNSYS
  • 5. Literature Review A second law analysis and entropy generation minimization of an absorption chiller Aung Myat, Kyaw Thu, Young-Deuk Kim, A. Chakraborty, Won Gee Chun, Kim Choon Ng Applied Thermal Engineering (2011) The authors have done a performance analysis of an absorption refrigeration system using entropy generation under transient conditions. Genetic Algorithm was used as an optimization tool to locate the system minimum under all defined domain of heat sources and cooling water temperatures Optimization of a solar driven absorption refrigerator in the transient regime Mouna Hamed, Ali Fellah, Ammar Ben Brahim Applied Energy (2012) The authors have done a theoretical study in dynamic mode of an absorption refrigerator endoreversible Model . A global minimizing time optimization is performed in view to reach maximum performances. A mathematical model combining the classical thermodynamics and heat and mass transfers principles was developed
  • 6. Identified research variables for future work Optimization of Collector size Collector inclination angle Hot water flow rate Hot water temperature Chilled water temperature (inlet/outlet) Chilled water flow rate Type of Refrigerants Types of Phase Change Materials Concentration of LiBr-H2O Solution flow rate Cooling water flow rate
  • 9. S.no Equipment required Specifications Unit cost No. of Total cost units (`) 1 Telecom cabinet 1 × 0.5 × 0.75m - 1 10000 2 Vapour Absorption Hot water based Vapour Absorption chiller - 0.5TR 25000 `/kW 1 50000 chiller (including cooling tower) 3 Solar Evacuated tube Size:1.5𝑚2 12500 `/m2 1 25000 collectors Evacuated glass tube with selective coating 4 Resistance heater 500W 2000 `/kW 2 4000 5 Thermal Storage tank 0.3m3 7500 `/m3 1 2275 6 PCM panels HS-29 (Inorganic salt) in HDPE panels (1000 × 160 × 16mm), 1000 `/kg 5 panels 7000 Phase change temp: 27 to 29oC (7kg) Density: 1150kg/m3, Operating range: 22 to 34oC Latent heat: 190 kJ/kg 7 Thermocouples K-Type, Range: -200oC to +1350oC, Resolution: 0.1oC from - 300 `/piece 10 Nos. 3000 200oC to 640oC, Accuracy: ±1oC 8 Insulation Polyurethane foam insulation for both thermal storage tank - - 2000 andtelecom cabinet 9 Labour + contigency - - - 10000 10 Total - - - 1,13,275