For the insulation of hot objects-especially large-dimensional ducts such as those found in nuclear power plants, flue gas desulphurisation and denitronisation systems-reinforcing stiffeners on the duct wall must always be considered thermal bridges. Because of this, two problems result:
- The increased thermal transmission through the thermal bridge leads to reduced temperatures at the inner surface of the duct wall. This may lead to going below the dew point temperature of the flue gas on that inner surface. Such a situation isn’t considered in this article.
- With unacceptably high temperature differentials between the inner and the outer edge of the stiffeners, thermal stress may result, leading to distortion of profiles and cracking of welded seams. For this reason, it’s common to calculate and maintain maximum admissible temperature differences through an appropriate construction and dimensioning of the insulation.
The limitation to the demanded temperature differences doesn’t constitute a problem in steady-state service, such as with flue-gas temperatures not changing over time as long as the required insulation material coverage on the outside of the stiffeners – 1/3 s for stiffeners up to 100 mm, 2/3 s for stiffeners over 100 mm – is observed.
Difficulties, however, may occur in the non-steady-state service-where flue-gas temperatures change over time as the installation is started up or shut down.
Starting the installation, the temperature on the inner surface of the wall and the inner edges of the reinforcing stiffeners follows the increasing flue gas temperature, while the outer edges of the stiffeners remain cold and the temperature there increases only after a considerable delay. This may lead to temperature differentials substantially above those in steady-state service.
The magnitude of these "non-steady-state temperature differentials" is dependent upon a variety of factors:
- the speed of temperature increase in the flue gas; the faster the installation started, the higher the temperature differences
- size of the stiffeners: with big profiles and large masses, the temperature differences are higher than with small profiles
- shape of the reinforcing stiffeners
- thermal conductivity of the materials used
- thermal transmission conditions
To lower the temperature differences, measures must be taken to allow for the movement of as much heat as possible through radiation and convection from the duct wall to the outer edge of the reinforcing stiffeners. This may be achieved-if technically feasible-by leaving an ample portion of the duct wall uninsulated.
These and other measures in the insulation area are, however, of limited effect. With big reinforcing stiffeners, the steady-state temperature differences can’t be reduced to acceptable values even through "the best possible insulation." Therefore, other measures outside of the control of the insulation trade are required. These may include using several smaller stiffeners instead of one large one, or reducing the rate of temperature increase when starting up the installation.
Depending upon the individual design, the temperatures in reinforcing stiffeners are influenced by the shapes and the appropriate insulation material design values. Some observations of principle can be made for the design examples given in Figures 1 and 2.
The simple reinforcing fin (steel sheet; generally smaller than 100 millimeters) would generally have roughly equal temperatures at the inner and outer edges, providing the insulation material coverage d was sufficiently extensive. In this case, no elevated thermal stress occurs. The "dew point temperature problem" on the inner surface of the duct wall, however, must also be considered in this case.
Contrary to this example, the temperature on the outer edge of the normally bigger I-profile (double T-profile – generally with webs exceeding 100 millimeter) definitely be lower than of the inner edge, since bigger masses must be heated on the outer edge and the heat transport requires more time due to the length of the web.
Frequently, the insulation contractor is required to mathematically prove what type of temperature differentials are-normally calculated against known warming-up conditions in the initial phase of the installation. Such calculations can be computed with numerical procedures such as the finite difference or the finite element method. However, it must be remembered that with these methods the thermal transmission inside the stiffener can be calculated satisfactorily exact. However, assumptions must be made regarding the movement of heat through radiation and convection, the precision of which is frequently difficult to assess. This applies especially to radiation. Here, the surface conditions of the duct wall and the reinforcing stiffener are decisively important. They aren’t known to the insulation contractor with the required precision. Therefore, caution should be used in the declaration of warranties on the basis of such calculations.
For the insulation following the surface of the profile IPE 360 as in Figure 2a, some results of finite element calculations are listed. Figures 3 shows the temperature increase over time at an uninsulated duct wall, the inner and outer edges of the reinforcing flange when the warming-up transient is 1.6 K/min and 0.4 K/min.
The maximum occurring temperature differences for a profile IPE 400, insulated according to Figure 2a, is given for different warming-up transient and for the steady-state service in Table 1. Table 2 shows the maximum temperature differences for I-profiles, insulated with "air gaps" according to Figure 2b.
The results show that especially while warming up the installation, critical stress maxima must be expected. The warming-up gradient has decisive influence here.
A comparison of the two designs considered here makes it obvious that the result of "air-gap" insulation compared to the surface-following insulation is smaller temperature differences for both the steady-state and the non-steady-state conditions. These observations, however, only hold true when uncontrolled convection influence can be prevented.
For the insulation of large-dimensional, hot objects, special thermal conduction considerations are required. Additionally, investigation of the possible deformation in the stiffeners as a result of temperature differentials is needed. This applies specifically to non-steady-state service conditions such as start-up and shut-down phases and accidents.
A mathematical proof of the maximum occurring thermal stresses in the steel construction of an object is not within the area of responsibility of the insulation contractor. The static system selected and the static and dynamic stresses to be born by the construction are in the area of responsibility of the installation contractor.
Nevertheless, this problem should be addressed when discussing contracts and the builder should be made aware of it. It could be possible that there is a duty to caution against possible damages, if the thermal stresses to be expected as result of the layout and size of the reinforcements and the temperature differences to be expected could lead to damages.
In critical cases, the necessity may even occur to ensure an even distribution of heat at the outer edges of the reinforcement in the warming-up phase of the installation by installing an extra heating system.
The European Federation of Associations of Insulation Contractors (FESI) is based in Berlin, Germany, with member organizations in 17 European countries. Among its goals are to promote the interests of insulation contractors in its member associations, and to establish its "opinion leadership" in all technical matters related to thermal and cold insulation and acoustic protection, both in buildings and in building equipment and industrial installations. For more information on FESI, contact (30) 2 12 86-1 62/-1 63, or e-mail to: email@example.com.
Initial temperature = +40 °C
|Profile||Temperature differences in stiffeners = = DJ[K]||Initial temperature
Initial temperature = +40 °C
|Profile||Temperature difference in stiffeners = = DJ[K]||Initial temperature
|IPE 400||about 10||IPE 400||about 50-60||1.6|
|– ” –||about 40||0.8|
|– ” –||90||2.0|
|IPE 460||about 10||IPE 460||75||1.6|
|– ” –||50||0.8|
|HEA 300||about 10||HEA 300||57||1.6|
|– ” –||45||0.8|
|IPE 370||about 10||IPE 370||53||1.6|
|– ” –||34||0.8|
|IPE 300||about 10||IPE 300||45||1.6|
|IPE 270||about 10||IPE 270||42||1.6|