The <str<strong>on</strong>g>12th</str<strong>on</strong>g> <str<strong>on</strong>g>Internati<strong>on</strong>al</str<strong>on</strong>g> <str<strong>on</strong>g>Symposium</str<strong>on</strong>g> <strong>on</strong> <strong>District</strong> <strong>Heating</strong> <strong>and</strong> <strong>Cooling</strong>,September 5 th to September 7 th , 2010, Tallinn, Est<strong>on</strong>iaRESULTS AND CORRELATIONSIt is again the company´s philosophy that paves theway for innovati<strong>on</strong>s. One of these innovati<strong>on</strong>s is thedevelopment of an in-house device for testing pipesystems, directly from producti<strong>on</strong>, cured <strong>and</strong> degassed.This proved to be a suitable device for producti<strong>on</strong>c<strong>on</strong>trol, but also for gaining more insights into productparameters.The objective of testing is to improve the knowledge ofthe produced pipe systems in order to optimize:Producti<strong>on</strong> methods:Machine data can be adjusted based <strong>on</strong> test results.Test results may lead to new producti<strong>on</strong> methods withnew equipment.Chemical <strong>and</strong> physical compositi<strong>on</strong> of layer material:Knowledge of various compositi<strong>on</strong> materials may leadto an improvement of insulating values.Cell structure <strong>and</strong> gap between insulating foam <strong>and</strong>medium pipe:Cell size influences values, test result basedimprovements are possible. The gap is a bad insulator.The quest for a minimal gap started with testing.Improvement <strong>and</strong> minimizati<strong>on</strong> of this gap was anachieved challenge in the testing period.Thermaflex is a lean <strong>and</strong> mean organisati<strong>on</strong> thatresp<strong>on</strong>ds quickly to new insights. Therefore newinsights were applied even before the complete rangeof producti<strong>on</strong> testing was performed.For the company, improvements of product <strong>and</strong>producti<strong>on</strong> have the highest priority. Although theproducti<strong>on</strong> range is wide, the insight into specific <strong>and</strong>general parameters increased c<strong>on</strong>siderably.The research provides the prominent variables toimprove insulati<strong>on</strong> performance. Practical heat lossdeterminati<strong>on</strong>, in combinati<strong>on</strong> with analytical studies,results in a clear underst<strong>and</strong>ing of heat loss behaviourin single <strong>and</strong> twin flexible pipe systems during theirentire lifetime.As a result of the tests the manufacturing process isimproved in two steps.The emphasis of the first step was to diminish the cellsize of the foam. This succeeded in a decrease of cellsize by some 20%.DISCUSSION OF PARAMETERSTable 1 summarises the results of measurements <strong>and</strong>calculati<strong>on</strong>s of tests <strong>on</strong> Flexalen 600 pipes directly fromproducti<strong>on</strong>. Various diameters are tested <strong>and</strong>calculated according to EN 15632 for a surfacetemperature of 10 °C <strong>and</strong> a comm<strong>on</strong> mediumtemperature of 70 °C (Instead of the maximum mediumtemperature of 95 °C).The table indicates the relati<strong>on</strong>ships between product,cross secti<strong>on</strong>al area of the foam, foam density, cell sizeof the foam, remaining foaming agent, calculatedthermal c<strong>on</strong>ductivity <strong>and</strong> the calculated heat loss of aburied piping system.The products 50A25, 63A32, 75A40 <strong>and</strong> 90A50 arenewly developed. These products are not necessarily<strong>District</strong> <strong>Heating</strong> products. However, they are producedusing the same process <strong>and</strong> have their applicati<strong>on</strong> inthe c<strong>on</strong>necti<strong>on</strong> between the district heating network<strong>and</strong> the building or house. It is also applicable in caseof low temperature differences, cooling or in-househeating or cooling.Table 1: Test results of fresh, uncured piping systemsProductFoamsecti<strong>on</strong> density cell size agent 50,calc Heat Loss*mm² kg/m³ (mm) % mW/m.K W/m50 A 25 1.473 50,0 0,47 52 39 15,363 A 32 2.313 34,0 0,50 52 38 15,275 A 40 3.044 38,0 0,40 46 44 17,890 A 40 5.105 42,0 0,80 64 51 17,190 A 50 4.398 39,0 0,80 62 55 23,0125 A 63 9.155 39,0 0,88 70 56 22,0160 A 75 15.688 40,3 1,20 81 54 21,0160 A 90 13.745 35,0 1,30 85 61 25,2200 A 110 21.913 45,0 1,60 81 68 27,4*) calculated heat loss of buried system at temperature difference of 60 KIn Graph 1 foam density <strong>and</strong> cell size are related to thecross secti<strong>on</strong>al surface.In Table 1 the foam density varies from about 35 kg/m³to about 50 kg/m³. Graph 1 shows hardly anyrelati<strong>on</strong>ship with the surface of the cross secti<strong>on</strong>.Table 1 shows that cell size varies from 0.47 to 1.60mm. Graph 1 shows that cell size is directly related tothe cross secti<strong>on</strong>al surface, however less than 1 to 1.This relati<strong>on</strong>ship is influenced by physical producti<strong>on</strong>parameters.The latest step is altering producti<strong>on</strong> such that thec<strong>on</strong>tent of anti-radiati<strong>on</strong> agent increases. The initialresults are promising but are not yet c<strong>on</strong>clusive as theanti-radiati<strong>on</strong> agent is also a good heat c<strong>on</strong>ductor.115
The <str<strong>on</strong>g>12th</str<strong>on</strong>g> <str<strong>on</strong>g>Internati<strong>on</strong>al</str<strong>on</strong>g> <str<strong>on</strong>g>Symposium</str<strong>on</strong>g> <strong>on</strong> <strong>District</strong> <strong>Heating</strong> <strong>and</strong> <strong>Cooling</strong>,September 5 th to September 7 th , 2010, Tallinn, Est<strong>on</strong>iaAverage cell size [mm]60504030201001,81,51,20,90,60,30,0- 5.000 10.000 15.000 20.000 25.000Cross secti<strong>on</strong> of foam [mm²]Graph 1: Density <strong>and</strong> cell size in relati<strong>on</strong> to foam crosssecti<strong>on</strong>Heat loss of buried piping [W/m]40,035,030,025,020,015,03050 100 150 200Outer diameter pipesystem [mm]Graph 2: 50,calculated <strong>and</strong> calculated heat loss of buriedpipe in relati<strong>on</strong> to outer pipe size8070605040C<strong>on</strong>ductivity [mW/m.K]Density [kg/m³]Graph 3 shows the relati<strong>on</strong>ship between outer pipesystem diameter size <strong>and</strong> the percentage of foamingagent directly from producti<strong>on</strong>. With increasingdiameter the foaming agent increases, possibly to anasymptotic value.An additi<strong>on</strong>al interesting factor is the <strong>on</strong>going processin the foam during <strong>and</strong> after producti<strong>on</strong>. As describedbefore the final step in the producti<strong>on</strong> is a 5-day curingstage.During the curing stage the foam exp<strong>and</strong>s <strong>and</strong> part ofthe foaming agent releases from the foam. As the foamis locked by a hard outer shell, expansi<strong>on</strong> is directedinwards. By this the gap between the foam <strong>and</strong> the PBmedium pipe, typical for our producti<strong>on</strong> method, isdecreased.Table 2 shows the effect of curing <strong>and</strong> degassing <strong>on</strong>both the c<strong>on</strong>tents of foaming agent <strong>and</strong> the calculatedheat loss.Even when forced, degassing takes time. The numberof degassed samples manufactured in the same wayas the fresh samples is therefore limited. Table 2 isshort due to a lack of adequate <strong>and</strong> comparablesamples.Table 2: The effect of time <strong>on</strong> curing <strong>and</strong> degassingFresh6 days curing DegassedProduct AgentHeatHeatHeatAgent AgentLossLossLoss% W/m % W/m % % W/m %63 A 32 52 15 23 17,5 15 0 17,1 1275 A 40 46 18 40 16,9 -5 0 20,1 1390 A 40 64 17 53 18 5 0 18,5 8Graph 2 shows the influence of outer pipe size tocalculated c<strong>on</strong>ductivity 50 <strong>and</strong> heat loss of buried pipesystems.It also shows that part of the increase of the heat losswith the diameter is caused by increase of c<strong>on</strong>ductivity.Percentage foaming agent90807060504050 100 150 200Outer diameter pipesystem [mm]Graph 3: Foaming agent c<strong>on</strong>tent in relati<strong>on</strong> to outerdiameter sizeHeat loss of buried piping [W/m]2019181716150 10 20 30 40 50 60Percentage of foaming agentGraph 4: Relati<strong>on</strong>ship between heat loss <strong>and</strong> foamingagentGraph 4 shows that there is a tendency of decreasingheat loss with increasing foaming agent. This tendencyhas seems weak. The spread is large over the entiregraph.116
- Page 1:
12th Inter
- Page 5 and 6:
The 12th I
- Page 7 and 8:
The 12th I
- Page 10 and 11:
The 12th I
- Page 12 and 13:
The 12th I
- Page 14 and 15:
For the case of parallel buried pip
- Page 16 and 17:
The 12th I
- Page 18 and 19:
The 12th I
- Page 20 and 21:
The 12th I
- Page 22 and 23:
The 12th I
- Page 24 and 25:
The 12th I
- Page 26 and 27:
The 12th I
- Page 28 and 29:
The 12th I
- Page 30 and 31:
The 12th I
- Page 32 and 33:
The 12th I
- Page 34 and 35:
The 12th I
- Page 36 and 37:
The 12th I
- Page 38 and 39:
The 12th I
- Page 40 and 41:
The 12th I
- Page 42 and 43:
The 12th I
- Page 44 and 45:
The 12th I
- Page 46 and 47:
The 12th I
- Page 48 and 49:
The 12th I
- Page 50 and 51:
The 12th I
- Page 52 and 53:
The 12th I
- Page 54 and 55:
The 12th I
- Page 56 and 57:
The 12th I
- Page 58 and 59:
The 12th I
- Page 60 and 61:
The 12th I
- Page 62 and 63:
The 12th I
- Page 64 and 65:
The 12th I
- Page 66 and 67: The 12th I
- Page 68 and 69: The 12th I
- Page 70 and 71: The 12th I
- Page 72 and 73: The 12th I
- Page 74 and 75: The 12th I
- Page 76 and 77: The 12th I
- Page 78 and 79: The 12th I
- Page 80 and 81: The 12th I
- Page 82 and 83: The 12th I
- Page 84 and 85: The 12th I
- Page 86 and 87: The 12th I
- Page 88 and 89: The 12th I
- Page 90 and 91: The 12th I
- Page 92 and 93: The 12th I
- Page 94 and 95: The 12th I
- Page 96 and 97: The 12th I
- Page 98 and 99: the street the more shallow the sha
- Page 100 and 101: The 12th I
- Page 102 and 103: The 12th I
- Page 104 and 105: The 12th I
- Page 106 and 107: The 12th I
- Page 108 and 109: The 12th I
- Page 110 and 111: P-1P-4P-9P-7E-5P-14P-8The 1
- Page 112 and 113: The 12th I
- Page 114 and 115: The 12th I
- Page 118 and 119: The 12th I
- Page 120 and 121: The 12th I
- Page 122 and 123: The 12th I
- Page 124 and 125: The 12th I
- Page 126 and 127: The 12th I
- Page 128 and 129: The 12th I
- Page 130 and 131: The 12th I
- Page 132 and 133: The 12th I
- Page 134 and 135: The 12th I
- Page 136 and 137: The 12th I
- Page 138 and 139: to heating costs of 14,5 ct/kWh. Th
- Page 140 and 141: The 12th I
- Page 142 and 143: The 12th I
- Page 144 and 145: The 12th I
- Page 146 and 147: The 12th I
- Page 148 and 149: academic access is facilitated as t
- Page 150 and 151: The 12th I
- Page 152 and 153: The 12th I
- Page 154 and 155: The 12th I
- Page 156 and 157: The 12th I
- Page 158 and 159: The 12th I
- Page 160 and 161: The 12th I
- Page 162 and 163: 1. CHP system operation in A2. Ther
- Page 164 and 165: The 12th I
- Page 166 and 167:
is covered by operating HOB. In oth
- Page 168 and 169:
The 12th I
- Page 170 and 171:
The 12th I
- Page 172 and 173:
The 12th I
- Page 174 and 175:
The 12th I
- Page 176 and 177:
The 12th I
- Page 178 and 179:
The 12th I
- Page 180 and 181:
The 12th I
- Page 182 and 183:
The 12th I
- Page 184 and 185:
The 12th I
- Page 186 and 187:
The 12th I
- Page 188 and 189:
The 12th I
- Page 190 and 191:
The 12th I
- Page 192 and 193:
The 12th I
- Page 194 and 195:
The 12th I
- Page 196 and 197:
produce heat and electricity. Fluct
- Page 198 and 199:
The 12th I
- Page 200 and 201:
The 12th I
- Page 202 and 203:
The 12th I
- Page 204 and 205:
The 12th I
- Page 206 and 207:
The 12th I
- Page 208 and 209:
The 12th I
- Page 210 and 211:
To assure that the temperatures mea
- Page 212 and 213:
The 12th I
- Page 214 and 215:
The 12th I
- Page 216 and 217:
The 12th I
- Page 218 and 219:
The 12th I
- Page 220 and 221:
production and provide for marginal
- Page 222 and 223:
The 12th I
- Page 224 and 225:
The 12th I
- Page 226 and 227:
The 12th I
- Page 228 and 229:
The 12th I
- Page 230 and 231:
The 12th I
- Page 232 and 233:
The 12th I
- Page 234 and 235:
The 12th I
- Page 236 and 237:
The 12th I
- Page 238 and 239:
The 12th I
- Page 240 and 241:
The 12th I
- Page 242 and 243:
In addition, it can also be observe
- Page 244 and 245:
The 12th I
- Page 246 and 247:
owner is normally only interested i
- Page 248 and 249:
The 12th I
- Page 250 and 251:
The 12th I
- Page 252 and 253:
The 12th I
- Page 254 and 255:
The 12th I
- Page 256 and 257:
The 12th I
- Page 258 and 259:
The 12th I
- Page 260 and 261:
The 12th I
- Page 262 and 263:
The 12th I
- Page 264 and 265:
The 12th I
- Page 266 and 267:
The 12th I
- Page 268 and 269:
The 12th I
- Page 270 and 271:
The 12th I
- Page 272 and 273:
The 12th I
- Page 274 and 275:
The 12th I
- Page 276 and 277:
The 12th I
- Page 278 and 279:
The 12th I
- Page 280 and 281:
The 12th I
- Page 282 and 283:
The 12th I
- Page 284 and 285:
The 12th I
- Page 286 and 287:
The 12th I
- Page 288 and 289:
The 12th I
- Page 290 and 291:
Stockholm district heating system a
- Page 292 and 293:
The 12th I
- Page 294 and 295:
The 12th I
- Page 296 and 297:
The 12th I
- Page 298 and 299:
The 12th I
- Page 300 and 301:
The 12th I
- Page 302 and 303:
The 12th I
- Page 304 and 305:
The 12th I
- Page 306 and 307:
The 12th I
- Page 308 and 309:
The 12th I
- Page 310 and 311:
The 12th I
- Page 312 and 313:
The 12th I
- Page 314 and 315:
The values presented do of course l
- Page 316 and 317:
The 12th I
- Page 318 and 319:
The 12th I
- Page 320 and 321:
The 12th I
- Page 322 and 323:
The 12th I
- Page 324 and 325:
The 12th I
- Page 326:
The 12th I