Selected heat pump is a classic heat pump, consists ofevaporator, compressor, condenser and thermalexpansion valve. Cold water circuit carried out of theheat source well or vertical ground heat exchanger,pump, piping, and drains well to absorb the thermalused water. In the center of the optimization procedureare the mass flow rates of the water obtained by thepumps.Hot water circuit is also the focus of observation.Pipeline and heaters are very important but onlyprovide indirect influence on the COP of the system.The element of the hot water circuit affects thecondensation temperature but does not have directinfluence on the COP of the system. With increase thesurface of the heating panels the degree of COP risingcontinually without extremesIn this regard pumps provide energy optimum of thesystem through mass flow rate. For each water-waterheating system with heat pump should determine theoptimal power of the circulating pumps to reach themaximum COP of the system.Heat expressed by the latent heat of refrigerantvaporization(3.)The power of real compressorThe power of real cintrifugal pumpThe power of real circulation pump(4.)(5.)(6.)IV. AUXILIARY STATIONARY EQUATIONSOF THE MATHEMATICAL MODELHeat transfer coefficient between water andrefrigerant in the evaporator, approksimatry(7.)mT cci, ,q0+PcmcTPcp, cu,ΣΔPIn studied case evaporator is coaxial, consisting ofparallel copper pipe bundle.The coefficient of convective heat transfer whenwater or antifreeze flows outside of the copper pipes.(8.)(9.)A,Fmf, ifc,TcThe coefficient of heat transfer when evaporation ofrefrigerant inside the copper tubesPcA,Fmf, ifo,TfLogarithmic temperature difference between the waterand the refrigerant temperature. ApproximatelymwTwi, ,mwT, wu,ΣΔPq0PwpFigure 1. Energy flows and the signs of physical systemsIII. GUVERNING STATIONARY EQUATIONSTHE MATHEMATICAL MODELHeat transfer in the evaporator between the water andthe refrigerant, Freon:Quantity of heat expressed by the convectivecoefficient of heat and the logarithmictemperature-difference .(1.)Heat expressed by caloric equation for the well water.(2.)The flow direction of refrigerant and water notimportant because of the constant evaporationtemperature.For the same direction flow the maximum and theminimum temperature difference isTtemperature difference between input and output ofwater in the evaporator.The evaporation latent heat of refrigerant R134adepends on evaporation temperature.Increment of Freon vapor enthalpy due adiabaticcompression18
V. OBJECTIVE FUNCTIONThe objective function in analyzed case is the COP ofthe heating systemIn the above function each term depends on the massflow rate.Maximum value of COP is obtained optimalcombination of mass flow rate of well water, heatingwater and mass flow rate of Freon.For optimization is applied numerical procedure, themethod of genetic algorithm.The application of classical optimization procedureusing the first derivative at mass flow rates is verycomplicated and difficult to implement.VI. MATHEMATICAL OPTIMIZATIONPROCEDUREA. Genetic algorithmsMethods of evolutionary computation are widely usedfor optimisation of problems [5-7] which can be multimodel,non-differentiable, non-continuous, also in thedomain of heating, ventilation and air conditioning [8].Genetic algorithms proved to be very useful foroptimization of multicriteria and multiparameterproblems as presented problem of optimization ofheating cooling system with heat pump. Evolutionarycomputation employs the vocabulary taken from theworld of genetics itself, and as a result solutions referto organisms of a population. Each organism representsthe code of a potential solution to a problem. A furtherimportant characteristic of GAs is that they work bymaintaining a set (population) of potential solutions,where as the other search methods process a singlepoint of the search space.Traditional analytical or numerical based approachesgenetic algorithms are based on building of solution.Because this is in the case of optimization of heatingsystem with water-water heat pump impossible we cantake different approach. The combination of allindependent variables used in the mathematical modelfor calculation of COP we can designate as solution.And previously stated mathematical formulation forcalculation of COP can be designated as targetfunction. The solution is feasible combination ofindependent variables not only the optimal solution.Representation of organism is:Our desire is to advance during evolution of solutionsto the optimal solution. In the world of evolutionarycomputation, solution is called organism. And set ofsolutions created in one step is called generation. Thisbasically means we are searching for such combinationof , and that the COP will, be at hismaximum. We could check all possible combinationsof , and . Unfortunately this is impossiblebecause of infinite size of search space. An exhaustivesearch method or an exhaustive search methodcombined with conventional gradient based methodscan be applied to find the optimal solutions, eventhough it is impractical in real time applications forsuch a complicated problem due to its time consumingnature.With genetic algorithms we can manage this problem.Genetic algorithms are effective at search in such largespace. It works on set (generation) of possible solutionand afterwards it checks the quality of solution (valueof COP). The creation of new set of solution (offspringgeneration) is based on principles of evolution andgenetics which takes into account the value of COP.Basic steps of genetic algorithm which repeat for everygeneration are (Figure 2):1. Creation of an initial set of solutions (initialgeneration of organisms).In our case organismrepresent combination of mass flows of cooling/heatingmedia. Organism it’s a set of numerical values. Firstgeneration of solution is created at random from theinterval of possible values.2. Evaluation of organisms by means of a fitnessfunction. This basically means calculation of COPvalue for all solutions (organism).3. Execution of evolutionary (reproduction andcrossover) and genetic (mutation) operations onsolutions (organisms) which solve the problem aboveaverage in current generation.In our model of optimization the tournament selectionis used. Tournament selection randomly chooses fromthe population at least two organisms and the onewhich represents better solution (COP in our case) isused for creation of new solution by crossover andmutation. It was used simple one point crossover, forexample:The mutation is based on the randomly insertion ofnew random value:The biggest advantage of search for solution bygenetic algorithms is possibility to use mathematicalcorrect definition of COP, without need forsimplification. Traditional methods of solving complexreal-world problems are based on simplification. Atsimplification process we have to deal with possibilitytoo simplify too much. With genetic algorithms we cantry evolutionary created solutions in the real world, inour case mathematical formulation of COP.19
- Page 1 and 2: 4 4 th IEEE International Symposium
- Page 3 and 4: EXPRES 20124 th International Sympo
- Page 5 and 6: Application of Thermopile Technolog
- Page 7 and 8: Design of a Solar Hybrid System....
- Page 9 and 10: ___________________________________
- Page 11 and 12: environmental protection and global
- Page 13 and 14: But can we use the human body sweat
- Page 15 and 16: IX. REFERENCES[1] Todorovic B. Cvje
- Page 17 and 18: QQ⎛ Λt⎞=⎜⎟⎝ Λ ⎠Nt Nwh
- Page 19: Analysis of the Energy-Optimum of H
- Page 23 and 24: The Set-Up Geometry of Sun Collecto
- Page 25 and 26: continuous east-west sun collector
- Page 27 and 28: continuously measure the thermal ch
- Page 29 and 30: CEvaluation of measurement resultsA
- Page 31 and 32: Application of Thermopile Technolog
- Page 33 and 34: Temperature of the components [C]90
- Page 35 and 36: nighttime, to weather or to the cha
- Page 37 and 38: η uη u0.50.40.30.20.1T 1 - 400K0.
- Page 39 and 40: Figure 10. . SPS Concept illustrati
- Page 41 and 42: [16] Zoya B. Popović: Wireless Pow
- Page 43 and 44: 25.0020.0015.0010.005.000.00Figure
- Page 45 and 46: · ℃ 0.0738 · 1.209 0.0892
- Page 47 and 48: use may be advantageous not only in
- Page 49 and 50: To find the reasons for this disagr
- Page 51 and 52: Toward Future: Positive Net-Energy
- Page 53 and 54: EnergyPlus environment, we used mod
- Page 55 and 56: To keep future energy consumption d
- Page 57 and 58: A New Calculation Method to Analyse
- Page 59 and 60: On Fig. 3. can be seen the areas th
- Page 61 and 62: Present and Future of Geothermal En
- Page 63 and 64: TABLE II.THE TEMPERATURE DATA AND C
- Page 65 and 66: Error in Water Meter Measuring at W
- Page 67 and 68: III.RESULTS OF MEASURMENTSEach meas
- Page 69 and 70: TABLE I.THE AVERAGE VALUE OF THERMA
- Page 71 and 72:
If the walls of the DHEs are made o
- Page 73 and 74:
Environmental External Costs Associ
- Page 75 and 76:
iodiesel production facility with a
- Page 77 and 78:
Contribution of unit processesto ex
- Page 79 and 80:
Heat Pump News in HungaryBéla Ád
- Page 81 and 82:
Thermal Comfort Measurements In Lar
- Page 83 and 84:
IV.DISCUSSIONThe sample frequencies
- Page 85 and 86:
For a Clear View of Traditional and
- Page 87 and 88:
esults in geographically distribute
- Page 89 and 90:
Design of a Solar Hybrid SystemMari
- Page 91 and 92:
Maintaining the set point temperatu
- Page 93 and 94:
Decision system theory model of ope
- Page 95 and 96:
parameter of pump in the function o
- Page 97 and 98:
Importance and Value of Predictive
- Page 99 and 100:
D. Overview of existing boiler oper
- Page 101 and 102:
HEAVY FUEL OIL FIRED, STEAMNATURAL
- Page 103 and 104:
MATHEMATICAL MODEL AND NUMERICAL SI
- Page 105 and 106:
C. Energy balance equationMathemati
- Page 107 and 108:
Discretization energy balance equat
- Page 109 and 110:
T ulf=32 º C, A - m =0.00162 kg/s,
- Page 111 and 112:
Comparison of Heat Pump and MicroCH
- Page 113 and 114:
the microCHP development. The energ
- Page 115 and 116:
control and stabilizer must be deve
- Page 117 and 118:
In Figure 1, in relation to the ord
- Page 119 and 120:
NPCC BHXOBYNI x1I x2I x3I x4LO YKYO
- Page 121 and 122:
exchange, as in reality, economies
- Page 123 and 124:
esponsibilities for consequences, o
- Page 125 and 126:
Coca-Cola Enterprise Inc had approx
- Page 127 and 128:
Flow Pattern Map for In Tube Evapor
- Page 129 and 130:
circumference with a liquid film. T
- Page 131 and 132:
Tube diameter: d 6 mm W Heat flux
- Page 133 and 134:
Realization of Concurrent Programmi
- Page 135 and 136:
applications the development, optim
- Page 137 and 138:
Renewable energy sources in automob
- Page 139 and 140:
commercial arrays can be built at b
- Page 141 and 142:
of multiple thin films produced usi
- Page 143:
EXPRES 20124 th International Sympo