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>ialoss from insulated pipes; Lund Institute of Technology,Sweden [2].The described heat loss calculati<strong>on</strong> is valid for the preinsulatedpipes. Branches <strong>and</strong> c<strong>on</strong>necti<strong>on</strong>s areexcluded.systems. Test spools can be extracted directly fromproducti<strong>on</strong>. In this way tests can be executed with freshproduct.Also testing of cured piping <strong>and</strong> piping that is aged <strong>and</strong>has been degassed during storage or in hightemperature aging is possible.Knowing the relati<strong>on</strong>ship between heat loss <strong>and</strong>various parameters, the most prominent parameters forheat loss can be evaluated.The most prominent parameters may lead to theimprovement of the flexible pipe system to ensureoptimal performance with minimal heat loss. Theinfluence of several prominent parameters isdetermined <strong>and</strong> recommendati<strong>on</strong>s are given in order tooptimize the insulati<strong>on</strong> performance.Figure 1, Thermaflex heat loss equipmentIn the new developed test rig (figure 1) a test spool(figure 2) is put in a slim fitting sleeve.The test spool is heated internally in three secti<strong>on</strong>s.The middle secti<strong>on</strong> of the spool is the test secti<strong>on</strong>.<strong>Heating</strong> in this secti<strong>on</strong> is c<strong>on</strong>trolled to obtain therequired test parameters. The two ends are heated tocompensate for the heat loss from the ends of themiddle test secti<strong>on</strong>. In this way an endless pipe isimitated.The outer side of the sleeve is water-cooled to obtainheat transport from the test spool.During the start of the test, heat is lost into the heatingof the pipe system <strong>and</strong> into the surrounding coolingwater. When heat losses have reached equilibrium, thesteady state heat transfer can be measured.Figure 2, L<strong>on</strong>gitudinal secti<strong>on</strong> guarded end heating probeThe time span required for testing in the test rig israther short. The time to reach equilibrium lies in theorder of hours, depending <strong>on</strong> the diameter <strong>and</strong>insulati<strong>on</strong> thickness. Comparable tests often requiretime spans in the order of days.C<strong>on</strong>taining various diameters, which are based <strong>on</strong> thest<strong>and</strong>ard producti<strong>on</strong> outer diameters, the test rigenables heat loss tests for various diameters of pipingReliability <strong>and</strong> reproducibility of the test rig is discussedin [3] Verificati<strong>on</strong> of heat loss measurements c<strong>on</strong>ducted<strong>on</strong> (semi) flexible pipe systems (van der Ven et al).MANUFACTURING PROCESSThe Flexalen 600 product has been developed byThermaflex, located in The Netherl<strong>and</strong>s. Thedevelopment started in 2002 <strong>and</strong> resulted in a firstsmall-scale commercial producti<strong>on</strong> in 2005. During theproducti<strong>on</strong> of Flexalen 600 four different producti<strong>on</strong>techniques are combined, partly simultaneous <strong>and</strong>partly sequential:1 Producti<strong>on</strong> of PB service pipes opti<strong>on</strong>ally coveredwith an EVOH oxygen barrier layer.2 Producti<strong>on</strong> of LDPE insulati<strong>on</strong> foam to fill the areabetween medium pipe <strong>and</strong> outer casing.3 Producti<strong>on</strong> of outer casing of HDPE.4 Assembly of the different elements (1, 2 <strong>and</strong> 3) witha full b<strong>on</strong>ding of the foam <strong>and</strong> the outer casing,while corrugating the casing.These techniques are based <strong>on</strong> extrusi<strong>on</strong> technology.The producti<strong>on</strong> line c<strong>on</strong>sists of purchased equipmentcombined with technology developed in-house. Thecomplete producti<strong>on</strong> is a (semi)-in-line producti<strong>on</strong>. Allpipe systems are produced at Waalwijk in theNetherl<strong>and</strong>s. Unique for the process is the ability toproduce c<strong>on</strong>tinuous lengths. For practical reas<strong>on</strong>s thelengths produced depend <strong>on</strong> the outer casing of theproduct <strong>and</strong> the size of the reel. The maximum lengthproduced can reach up to 2000 meters.The complete Flexalen 600 pipe system includes preinsulatedpipes, couplings, sleeves, pre-insulated T-c<strong>on</strong>necti<strong>on</strong>s, etc. The producti<strong>on</strong> range is described byEngel <strong>and</strong> Baars. [5]113
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>iaProducti<strong>on</strong> of PB service pipesAll service pipes are made of Poly-butene. This is aplastic with a special combinati<strong>on</strong> of properties. Polybutenehas excellent heat <strong>and</strong> creep resistance,flexibility <strong>and</strong> strength at a l<strong>on</strong>g lifespan <strong>and</strong> is fullyrecyclable. In accordance with the temperaturedurati<strong>on</strong> profile menti<strong>on</strong>ed in the BRL5609/EN15632,PB is suitable up to a maximum temperature of 95 °C.All PB-pipes are weldable by socket fusi<strong>on</strong>, electrofusi<strong>on</strong> <strong>and</strong> butt welding, which allows for an all plasticdistributi<strong>on</strong> system without metal parts that are pr<strong>on</strong>e tocorrosi<strong>on</strong>. The service pipes are produced via state-oftheart extruders.The producti<strong>on</strong> line c<strong>on</strong>sists roughly of an extruder,calibrati<strong>on</strong> tools for adjusting pipe size, cooling baths,<strong>and</strong> marking <strong>and</strong> cutting equipment.Pipe dimensi<strong>on</strong>s are checked inline every sec<strong>on</strong>dduring <strong>and</strong> after producti<strong>on</strong> with ultras<strong>on</strong>icmeasurements. PB-pipes can be produced up to anouter diameter of 225 mm.If desired an outer oxygen barrier layer may be appliedvia co-extrusi<strong>on</strong> up to an outer PB pipe diameter of 90mm.After producti<strong>on</strong> the PB-pipes are stored for a minimumperiod of 5 days <strong>and</strong> cured to create the correctcrystalline polymer structure. After curing the pipe isused for the Flexalen 600 producti<strong>on</strong>.Every batch produced is verified by the in-house QCdepartment according to Dutch directives- BRL-K5609, for PB pipes with oxygen barrier or- BRL-K17401 for PB pipes without oxygen barrier.Product <strong>and</strong> manufacturing processes are checked 6-8times a year <strong>and</strong> certified by independent agenciessuch as Bureau Veritas, KIWA <strong>and</strong> CSTB <strong>and</strong> leCentre Scientifique et Technique du Bâtiment. Thequality of the QC department is validated by thesechecks <strong>and</strong> by internal <strong>and</strong> external audits.Producti<strong>on</strong> of LDPE insulati<strong>on</strong> foamThermaflex has now approximately 35 years ofexperience in the producti<strong>on</strong> of LDPE foam viaextrusi<strong>on</strong> techniques.Most of the raw materials that are used are tailor-mademixtures according to Thermaflex specificati<strong>on</strong>s.Through these specificati<strong>on</strong>s <strong>and</strong> proper producti<strong>on</strong>quality c<strong>on</strong>trol the company‘s philosophy related tocore business is also realized for raw materials.During the heating, melting <strong>and</strong> mixing of the rawmaterials the foaming agent is injected into theextruder. This foaming agent is a hydrocarb<strong>on</strong> thatcauses the expansi<strong>on</strong> of the LDPE.The quality of the foam, moreover the insulati<strong>on</strong>properties of the foam, depends <strong>on</strong> parameters such asdensity, cell size <strong>and</strong> chemical compositi<strong>on</strong>. Allparameters are measured <strong>and</strong> adjusted within limitedtolerances to meet the specificati<strong>on</strong>s. The bestefficiency is further improved when the space betweenthe service pipe <strong>and</strong> the foam is filled better.As there is no b<strong>on</strong>ding between the service pipe <strong>and</strong>foam, there is no risk of damaging the foam <strong>and</strong>properties by expansi<strong>on</strong> of the pipes due to thermalfluctuati<strong>on</strong>s in the applicati<strong>on</strong>s.Producti<strong>on</strong> of corrugated outer casing (HDPE) <strong>and</strong>assembly of complete productThe outer casing is applied by an extrusi<strong>on</strong> process<strong>and</strong> thermally welded to the foam after the pipe hasbeen inserted. The outer casing is also corrugated tooptimize the flexibility of the finished product. Now theproduct is ready for coiling.After producti<strong>on</strong> the final product must cure for 5 days.During this curing period the degassing of the foamingagent starts, while the insulati<strong>on</strong> foam is still stabilizingProducti<strong>on</strong> testing <strong>and</strong> c<strong>on</strong>trollingDuring the producti<strong>on</strong>, parameters are checked <strong>and</strong>c<strong>on</strong>trolled, such as:1 Chemical compositi<strong>on</strong> of the foam.2 Settings of all extruders involved (foam extruder <strong>and</strong>extruder for corrugated outer casing).3 Density <strong>and</strong> cell size of the foam.4 Dimensi<strong>on</strong>s of the foam (outer diameter <strong>and</strong> innerdiameter).5 Line-speed of all involved products (Foam / PB-pipe/ End-product).6 Thickness of the corrugated outer casing <strong>and</strong> thec<strong>on</strong>necti<strong>on</strong> of the corrugated outer casing to thefoam.7 Since a few m<strong>on</strong>ths: in-line producti<strong>on</strong> c<strong>on</strong>trol ofHeat Loss of the pre-insulated pipe system.The most prominent factors to influence heat loss areparameters <strong>on</strong>e to four. The foam lambda is directlyaffected by these factors as represented in equati<strong>on</strong> 1. total c<strong>on</strong>vecti<strong>on</strong> c<strong>on</strong>ducti<strong>on</strong> radiati<strong>on</strong> blowingagent(1)114
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