[0001] The present invention relates to an insulating product of mineral fibres intended
in particular for the heat insulation of pipes. The product shall have a good temperature
resistance, moisture resistance and a strength that resists a high temporary load,
e.g. the steps of the pipe fitter on the pipe during installation operations. The
insulating product shall be shapeable at once or later to the desired shape and subsequently
curable at the prevailing outer temperature or at a raised temperature.
[0002] In view of an economically optimal production of the product, the production shall
be feasible in a conventional installation for the production of mineral wool webs.
The curing temperature shall be adaptabe to the circumstances and the curing time
shall be short.
[0003] The Finnish patent specification 67751 discloses the production of insulating bodies
based on mineral wool. In order to achieve the desired compression resistance and
temperature resistance, clay sludge, preferably bentonite, is absorbed by means of
under-pressure into a preshaped and cured tubular bowl or insulating plate. The process
requires a curing of several hours in a furnace. The insulating body has a good temperature
resistance, of at least 800
° C, but is expensive owing to a slow and costly production process and expensive raw
material. An additional drawback of the bentonite body is its coarse surface, requiring
an additional surface treatment, i.e. milling, thus increasing the price of the material.
[0004] Phenol cured insulating bodies are also known. Phenol is a fairly cheap and rapidly
curing binder. A phenol cured product resists temperatures of up to 250
° C, but if the temperature is above 250
° C for a long period of time, the bonds are destroyed. At higher temperatures, of 400
° C and more, the binder residues flare up, the temperature rises rapidly and the product
collapses. Another drawback of phenol insulating bodies consists in their emitting
poisonous gases during burning.
[0005] The SE lay-out print 420 488, for instance, discloses the use of a mass based on
water glass and clay mineral substances as a binding agent. The binder provides a
good water and heat resistance in the product. On the other hand, the product has
a poor compression resistance, meaning that e.g. a tubular bowl made of mineral fibres
and treated according to the layout print does not resist temporary load. Moreover,
the product is brittle and thus causes dusting.
[0006] From DE-C2-28 04 069 a method of producing an insulating product is known where mineral
fibers are bound together by water glass, but no slag or other hydraulic bond forming
material is used.
[0007] SU 614061 discloses an insulating product comprising at least 35 wt-% of perlite
sand and optionally up to 20 wt-% of kaolin fibers (not mineral fibers) where the
binder consists of synthetic AI-Ca-slag and water glass.
[0008] DK-C-69522 relates to a stiff insulating material of mineral wool, e.g. slag wool,
which is impregnated with water glass and subsequently heated so that the water glass
is transformed to a foam whereafter the material is cooled.
[0009] GB-A-457 842 relates to an insulating product consisting e.g. of slag wool which
is impregnated e.g. with an alkaline or potassium salt in such proportions that a
silica gel is formed and a portion of the silicate remains free to combine separately
with the slag wool. Here water glass does not act as an activator of slag.
[0010] SU 622781 discloses a fire-resistant coating containing mainly mineral fiber (30-60
wt-%) and water glass (30-50 wt-%).
[0011] US 2 904 444 is related to an insulating material of calcium hydroxide and diatomaceous
earth. The material does not contain mineral wool nor is it treated with water glass.
[0012] CH-A5-238299 relates to a coating agent containing water glass and slag wool (preferably
in the proportion 3:1).
[0013] According to the present invention, it has been noted that an insulating product
can be achieved, which is especially suitable as a tubular bowl, out of a mineral
fibre web prepared in a conventional manner by using as a binding agent a water glass
based binder with an addition of slag.
[0014] The main characteristics of the invention appear from the characterizing parts of
claims 1 and 7.
[0015] The slag imparts many valuable properties to the insulating material. The alkalis
of the water glass act as activators of the slag (cf. slag alkali cement). Together
with water glass, slag forms a hydraulic bond giving the cured product an improved
compression resistance, a reduced brittleness and thus reduced dusting and greater
dust particles, compared to products treated with binders containing water glass without
a slag addition.
[0016] Moreover, a good temperature resistance is achieved in a product containing a binder
based on water glass and having a slag addition. Due to the hydraulic bond of the
slag to the water glass, the water is firmly bound, chemically bound to the structure.
The chemically bound water increases the fire-resistance capacity of the material
in that the water evaporating at a fire temperature keeps down the temperature for
a longer period. A water glass based binder resists a long-lasting temperature charge
of up to 800 °C.
[0017] Combined with the water glass, the slag increases the crystallinity of the material,
thus reducing the moisture absorption tendency and the moisture sensitivity.
[0018] Moreover, a more rapid curing and the possibility of optional curing conditions are
provided. The curing time for a product containing water glass and slag in the binder
and by using conventional curing in a curing chamber is approx. 20-60 s for thin products
and approx. 20 min. at the most for thick tubular bowls. Equally good curing times
are achieved with phenol containing binders, but these binders are unsuitable in other
respects. Other known binders require curing times of up to several hours.
[0019] Another advantage of the system water glass/slag is that the binder enables the forming
of no-swelling compounds, although the temperature exceeds the swelling temperature
of pure water glass, 160°C.
[0020] Further advantages of the slag is its reactivity at a normal temperature. This means
among others that the slag totally prevents carbonation, which is a noticeable advantage.
Other mineral curing agents, like fly ash and clay, do not possess this property.
Clay and corresponding substances mainly act as fillers.
[0021] It has been noted according to the invention, that the advantageous effects of slag
are achieved with relatively small amounts of slag, both with regard to the amount
of water glass and to the amount of fibres. In the binder, the weight ratio of the
dry substance of the water glass to the slag can be approx. 100:1 - 100:50, prefrably
10:1 - 10:2. In the product, the weight ratio of the mineral fibre amount to the dry
substance of the water glass can be approx. 100:1 - 100:20, preferably 100:5 - 100:15.
[0022] The slag of the binder is preferably blast furnace slag.
[0023] The slag/water glass system is well controllable and thus provides a geat flexiblity
for the method of preparing an insulating product of mineral wool. Controllable components
are among others:

[0024] Knowledge of the behaviour of various slags in an alkaline environment enables the
control of the properties of the final product.
[0025] The slag reacts with the alkalis of the water glass, i.e. it is activated. Thus,
water resistant hydrate phases of a zeolite type are obtained. Owing to this mechanism,
the molar ratio R
s (the ratio of the silicon moles to the alkali moles in the water glass) for the residual
unreacted water glass rises so much that also this residue becomes water resistant.
A higher alkali content, i.e. a lower molar ratio R
s, requires a higher slag portion in order to tie up the alkalis in a water resistant
form.
[0026] The molar ratio R
s of commercial water glass is approx. 3.3. According to the invention, it has been
observed that very low molar ratios are also usable, requiring in that case high slag
contents in order to provide water resistance of the final composite. Even NaOH or
Na
2C0
3 are usabe. However, it is preferable to use the molar ratio Rs 2.3. The optimal moisture
resistance with regard to the reactivity with slag is obtained for R
s = 2.7-3.0.
[0027] The main components of the slag-glass are CaO, MgO, Si0
2, Al
2O
3. It is generally true about slag/water glass systems that the lower the CaO content,
i.e. the ratio CaO/Si0
2, the lower a molar ratio R
s should be used in order to obtain a hydraulic bond within a reasonable period of
time. When using low molar ratios, R
s < 2.7, the slag content has to be increased. With a higher ratio CaO/SiO
2 1.3, water glass can be used with R
s 3.3 , still obtaining a sufficient reactivity.
[0028] The reaction degree is controlled by means of the temperature and the curing time.
A higher curing temperature shortens the curing time and vice versa.
[0029] A lower R
s shortens the curing time at a constant temperature. A higher R
s requires a longer curing time or a higher temperature.
[0030] By prereacting slag with water glass at a normal or a raised temperature under agitation,
the reaction degree and the curing rate can be further increased. A finished hydrate
phase is consequently created, speeding up the curing when the binder has been applied
onto the mineral wool.
[0031] In case the curing temperature exceeds approx. 160°C, the slag content has to be
increased in order to prevent the water glass from swelling (cf. slag alkali cement).
[0032] Trituration of the slag increases the reaction rate and the reactivity. This enables
to use a water glass with a higher R
s, or optionally a very rapid curing can be ahieved at a lower R
s. A finely ground slag also improves the stability of the slurry of water glass and
slag.
[0033] The water glass can be a sodium, potassium, lithium or ammonium silicate solution.
In case the slag content is high, hydroxides and/or carbonates can be added.
[0034] The preparation of a mineral wool product and the addition of the binder based on
water glass and containing slag takes place conventionally in a conventional set of
apparatus. The binder is added as a solution through a nozzle to the fibres in the
wool chamber of a conventional machine line. The water glass and the slag are premixed
in water and are kept in agitation before the distribution on the wool. The curing
of the binder mixed wool material takes place at once or later, at room temperature
or at a raised temperature.
[0035] Besides water glass and slag, the binder solution can contain possible additional
curing, modifying, dust binding and/or hydrophobing agents.
[0036] The spraying of the binder solution and the additives takes place directly after
the fibre formation, preferably in the wool chamber. This is an essential advantage,
since the wool is in a virginal state here and thus has a good adhesiveness.
[0037] The binder composition is sprayed on the wool through the binder nozzles of the centrifuge,
both peripheral and central sprayers being then usable. Optionally two different solutions
can be fed into the wool, so that possible modifying and/or additional curing agents
are fed through the one sprayer and a slurry of water glass/slag + possible modifying
agents through the other sprayer.
[0038] An additional binder solution can appropriately be added to the wool in a subsequent
step of the production of the insulating material. By applying more binder solution
on the primary web, a composite having a better resistance is achieved. By adding
additional additives on the primary web special properties can be given to the material.
[0039] Before the feeding of the binder only compatible substances need to be premixed,
whereas the other necessary additional components are mixed only at the moment of
application. The mixing can be carried out for istance by rapid mixing, e.g. in tubular
mixers. Thus the dwell time will be short enough not to allow any gelling or precipitating
reactions to take place. The required additional water is also adjusted by feeding
into the rapid mixer. The water amount is adjusted so as to provide the correct moisture
for the primary web and prevent dusting. The water evaporation taking place in the
wool chamber increases the viscosity of the fibre composition applied onto the fibre.
The high viscosity means a very low ion migration, thus decreasing the reaction rate.
In this manner, the primary web retains its elasticity and curability for several
days/weeks, provided that further water discharge is prevented.
[0040] When producing insulating sheets, these are appropriately cut out from a mineral
web, which has been conventionally laid out by oscillating to the desired thickness
and then cured.
[0041] According to a preferred method, the mineral fibre web is cured at room temperature,
for instance between metal sheets. Thus the sheet will acquire a better flexibility.
A slowly cured fibre body is, as is known, more flexible, elastic, than a fibre body
that has to be cured at a high temperature.
[0042] According to another preferred embodiment a secondary web having the desired thickness
is taken up in an uncured state and stored in a non curing environment, e.g. enclosed
in plastic at a suitable temperature and during a determined time at the most. This
insulating material is used in situ for the insulation in places that are not easily
accessable and have an awkward shape, such as for instance renovation objects. Afterwards,
the insulation cures at the prevailing temperature. It is relatively easy to apply
an insulating mat having a suitable thickness onto or around various bodies difficult
to access. The curing does not require any special measures or equipment since it
takes place spontaneously at the prevailing temperature.
[0043] The method is also suitable for blow wool applications, in which uncured fibre material
torn into small tufts is applied onto pipes, where the wool can be cured at the prevailing
temperature.
[0044] When producing tubular bowls, a secondary web is shaped to the desired shape of a
tubular bowl, and is subsequently cured in a known manner. The curing can take place
rapdily at a high temperature or slower at a lower temperature.
[0045] Additional additives, like additional curing, modifying, dust binding and hydrophobizing
agents cooperate with the water glass/slag system.
[0046] According to the invention, the additional curing agents consist of mineral salts
and compounds, suitable acids, esters or alcohols or of combinations of these. The
mineral salts can be e.g. magnesium, aluminium or calcium salts or compounds. Phosphoric
acid, for instance, is a usable acid. Buffer curing agents can also be used for adjusting
the storage time. The additional curing agent may be a combination of the above mentioned
curing agents.
[0047] For the water glass, various modifying agents like organic and unorganic polymers,
cellulose and silicones like silicon organic polymers are appropriately used. Also
monomers polymerized by e.g. a pH change or a temperature rise during the curing can
be used. The modifying agents of water glass have in common the fact of not being
film forming. By means of the modifying agents one aims at softening the water glass,
thus increasing its adhesiveness to the fibre surface.
[0048] The water glass modifier improves the elastic properties, the water resistance, carbonation
resistance etc. of the water glass.
[0049] As dust binding agents, alcohols, polyols, film forming polymers, gelling polymers,
waxes, oils, fats, paraffines etc. are appropriately used. The task of the dust binding
agent is to bind together the dust or to bind it to the main matrice either physically
(film forming) or chemically (surface active properties). In case high temperature
curing is used, melting dust binding agents, e.g. stearates, can be used, or curing
dust binders, forming a film over the matrice. A great number of the dust binding
agents simultaneously have a water repellent effect.
[0050] The task of the hydrophobizing agent is to prevent water and moisture from penetrating
into the product. As hydrophobizing agents, silanes, silicones, oils, various hydrophobic
compounds and hydrophobic starch are used. It is essential that possible hydrophilic
emulgators are destroyable, which happens by raising the pH value or by a temperature
raise.
[0051] The polybutene silane compound has proved especially advantageous as a dust binding
agent and a hydrophobing agent. The polybutene acts as a dust binder and the silane
as a hydrophobing agent.
[0052] Within the various groups, compatible compounds can be mixed in advance, whereas
non compatible compounds have to be mixed immediately before the application or applied
through separate nozzles.
[0053] The invention is explained below by means of various examples and indicating the
values of various essential properties of the produced insulating products.
Example 1
[0054] A suspension of 83% of water glass (R
s = 2.7, dry content 39%) and 13% of blast furnace slag were mixed with a modifying
solution (dry content 8%), containing silane as a hydrophobing agent and polybutene
as a film forming dust binder, in a tubular mixer. Calculated as dry substance, the
water glass forms 11.2% of the wool, the slag 13% of the water glass and the modifiers
1.8% of the water glass. The wool production was 2.8 tons/h and the dosing of the
various solutions was 10.2 I/min of water glass-slag- suspension, 3.2 I/min of modyfier
solution as well as water 10 I/min. The primary web was rolled into a tubular bowl
having a diametre of 350 mm and a wall thickness of 60 mm and the tubular bowl was
cured at 145°C for 3 min. A piece 63.5 x 63.5 mm was cut out from the tubular bowl
and was tested with regard to linear shrinking at 600
° C according to ASTM 356-60. The shrinking was only 1.4% when the density of the product
was 101 kg/m
3.
Example 2
[0055] A suspension of 95% of water glass (R
s =3.3, dry content 37%) and 5% of blast furnace slag were mixed with an additional
curing agent (5% H
3P0
4) and a modifier solution (dry content 5%), containing a hydrophobizing agent and
a film forming polymer as a dust binder, in a tubular mixer. Calculated as dry substance,
the water glass forms 11.4% of the wool, the slag 5%, the phosphoric acid 2.5% and
the modifiers 0.8% of the water glass. The wool production was 3.2 tons/h and the
dosing of the various solutions was 12.5 I/min of the water glass/slag-suspension,
5.3 I/min of the additional curer, 4.2 I/min of the modifier solution as well as water
11 I/min. Out of the primary web, a sheet web was prepared in a curing chamber at
140°C. Fire tests according to SFS 4193 were carried out on sheets having a thickness
of only 26 mm and a density of 217 and 225 kg/m
3 respectively, yielding a fire resistance of 52 and 58 min. respectively. The temperature
rise on the fire side according to SFS 4193 appears from fig. 1 and table 1. The test
was continued for one hour and the temperature was 925
° C at the end of the test. The sheet was totally undeformed and unbent and the burnt
area still had a high residual strength.
[0056] It should be observed that the results given in the figures do not by any means indicate
the upper limits, but only typical values that can be obtained. The results are collected
from 11 different full-scale runs testing more than 70 different formulas.
[0057] Fig. 2 shows a typical relation between the splitting resistance and the density
of a sheet product according to the invention.
[0058] Fig. 3 shows the relation between the tensile bending strength and the density of
a number of sheet products according to the invention.
[0059] The force required for compressing a cured sheet product according to the invention
5 and 10% respectively is indicated in fig.4. The force is given as kN/m
2 as a function of the density.
[0060] Water absorption was tested according to BS2972:1975. The water absorption of sheet
products aiming at a good hydrophobicity was:
After an immersion of 0.5 hours, only 0.3-1.6% by volume
After an immersion of 1 hour, only 0.6-2.4% by volume
After an immersion of 2 hours, only 1.1-3.0% by volume
After an immersion of 1 day only 3.8-7.0% by volume
After an immersion of 7 days only 9.1 by volume
The moisture resistance was tested in a climatic chamber by measuring the swelling
during storage at 40 °C and 95% relative moisture. The temperature was selected as
40 °C in order to obtain accelerated results, since swelling at 20-30 ° C is practically none or very slow. The optimal results with a sheet product having
a density of 140 kg/m3 showed no swelling after 1 day and only a swelling of 0.3% after 7 days.

Example 3
[0061] A suspension of 82% water glass (R
s = 2.4, dry matter content 44%) and 18% blast furnace slag were mixed with a modifier
solution (dry content 10%), containing a hydrophobizing agent and a film forming polymer
as a dust binding agent, in a tubular mixer. Calculated as a dry substance, the water
glass represents 15.8% of the wool, the slag 50% of the water glass and the modifiers
3.6% of the water glass. The wool production was 2.8 tons/h and the dosing of the
various solutions was 13.2 I/min of water glass/slag-suspension, 6.0 I/min of modifier
solution and water 8 I/min. Out of the primary web, tubular bowls were prepared, having
an outer diametre of 520 mm, a thickness of 120 mm and a density of 96.0 kg/m
3. The bowls were mounted on a steam pipe, whose temperature was raised up to 520 °C.
After 60 hours at this temperature the insulation was inspected and its value was
determined.
[0062] The value was: 0.1010 W/m
° C at 520 °C. The bowls resisted the temperature (520 °C) well. The only remarkable
difference was that the inner surface of the bowl had become harder than the outer
surface, probably due to the continued curing of the binder.
1. Insulating product intended in particular for the heat insulation of pipes, comprising
mineral fibers and a binder, characterized in that said binder consists mainly of
water glass and of slag or other material which forms a hydraulic bond with water
glass.
2. Insulating product according to claim 1, characterized in that the binder is present
in the product in such an amount, that the weight ratio of the mineral fibre amount
to the dry substance of the water glass is 100:1 - 100:20, preferably 100:5 - 100:15.
3. Insulating product according to claim 1 or 2, characterized in that the slag is
present in the binder in such an amount that the weight ratio of the dry substance
of the water glass to the slag is 100:1 - 100:50, preferably 10:1 - 10:2.
4. Heat insulating product according to any of the preceding claims, characterized
in that the slag is pulverized blast furnace slag.
5. Insulating product according to any of the preceding claims, characterized in that
the binder contains modifying, dust binding, hydrophobizing and/or additional curing
agents for the mineral fibres.
6. Insulating product according to claim 5, characterized in that the binder contains
polybutene as a dust binding agent and silane as a hydrophobizing agent.
7. Insulating product according to any of the preceding claims, characterized in that
it is uncured and packed in a moisture- and gasproof package.
8. Method for making an insulating product, intended in particular for the heat insulation
of pipes, comprising the steps of preparing a binder by mixing the binder components
in water into a suspension, stirring the suspension, treating mineral fibers with
the binder and curing the binder immediately or at a desired time, at the prevailing
outer temperature or at a raised temperature, characterized in that the binder consists
mainly of water glass and of slag or other material which together with water glass
forms a hydraulic bond.
9. Method according to claim 8, characterized in that additives for further curing,
modifying, dust binding and/or hydrophobing of the product are applied on the mineral
fibre wool as a separate solution or mixed into the binder solution immediately before
this is applied on the mineral fibre wool.
10. Method according to claim 8 or 9, characterized in that the binder and possible
additives are applied on the mineral fibre wool immediately after the fibre formation
and/or later during the preparation.
11. Method according to any of claims 8-10, characterized in that the mineral fibre
web equipped with a binder is cured at room temperature, e.g. between metal sheets,
or at a raised temperature, e.g. in a curing chamber, after which the web is cut into
the desired products, like insulating sheets.
12. Method according to any of claims 8-10, characterized in that the mineral fibre
web equipped with a binder is shaped into products, like tubular bowls, which are
cured in their moulds.
13. Method according to any of claims 8-10, characterized in that the mineral fibre
web equipped with a binder is stored in an uncuring environment and that the curing
is carried out at the desired time in situ, the product having been applied onto an
insulation object.
1. Dämmprodukt, insbesondere zur Wärmedämmung von Rohren vorgesehen, umfassend Mineralfasern
und ein Bindemittel,
dadurch gekennzeichnet,
daß das Bindemittel vorwiegend aus Wasserglas und aus Schlacke, oder einem anderen
Material das mit Wasserglas eine hydraulische Bindung bildet, besteht.
2. Dämmprodukt nach Anspruch 1,
dadurch gekennzeichnet,
daß das Bindemittel im Produkt in einer solchen Menge vorhanden ist, daß das Gewichtsverhältnis
der Mineralfasermenge zur Trockensubstanz des Wasserglases 100:1 - 100:20, bevorzugt
100:5 - 100:15 beträgt.
3. Dämmprodukt nach Anspruch 1 oder 2,
dadurch gekennzeichnet,
daß die Schlacke im Bindemittel in einer solchen Menge vorhanden ist, daß das Gewichtsverhältnis
der Trockensubstanz des Wasserglases zur Schlacke 100:1 - 100:50, bevorzugt 10:1 -
10:2 beträgt.
4. Wärmedämmprodukt nach einem der vorhergehenden Ansprüche,
dadurch gekennzeichnet,
daß die Schlacke pulverisierte Hochofenschlacke ist.
5. Dämmprodukt nach einem der vorhergehenden Ansprüche,
dadurch gekennzeichnet,
daß das Bindemittel modifizierende, staubbindende, hydrophobierende und/oder zusätzliche
härtende Mittel für die Mineralfasern enthält.
6. Dämmprodukt nach Anspruch 5,
dadurch gekennzeichnet,
daß das Bindemittel Polybuten als staubbindendes Mittel und Silan als hydrophobierendes
Mittel enthält.
7. Dämmprodukt nach einem der vorhergehenden Ansprüche,
dadurch gekennzeichnet,
daß es ungehärtet ist und in eine feuchtigkeits- und gasundurchlässige Verpackung
verpackt ist.
8. Verfahren zum Herstellen eines Dämmprodukts, das insbesondere zur Wärmedämmung
von Rohren vorgesehen ist, umfassend die Schritte Herstellen eines Bindemittels durch
Mischen der Bindemittelkomponenten in Wasser in eine Suspension, Rühren der Suspension,
Behandeln von Mineralfasern mit dem Bindemittel und Härten des Bindemittels unmittelbar
oder zu einem gewünschten Zeitpunkt, bei der vorherrschenden Außentemperatur oder
bei einer erhöhten Temperatur,
dadurch gekennzeichnet,
daß das Bindemittel vorwiegend aus Wasserglas und aus Schlacke, oder einem anderen
Material, das mit Wasserglas eine hydraulische Bindung bildet, besteht.
9. Verfahren nach Anspruch 8,
dadurch gekennzeichnet,
daß die Additive für weiteres Härten, Modifizieren, Staubbinden und/oder Hydrophobieren
des Produkts als eine separate Lösung auf die Mineralfaserwolle aufgebracht werden
oder der Bindemittellösung beigemischt werden, unmittelbar bevor diese auf die Mineralfaserwolle
aufgebracht wird.
10. Verfahren nach Anspruch 8 oder 9,
dadurch gekennzeichnet,
daß das Bindemittel und mögliche Additive unmittelbar nach der Faserbildung und/oder
später während der Herstellung auf die Mineralfaserwolle aufgebracht werden.
11. Verfahren nach einem der Ansprüche 8 bis 10,
dadurch gekennzeichnet,
daß das mit einem Bindemittel versetzte Mineralfaservlies bei Raumtemperatur gehärtet
wird, z.B. zwischen Metallplatten, oder bei einer erhöhten Temperatur, z.B. in einer
Härtkammer, wonach das Vlies zu den gewünschten Produkten, wie Dämmplatten, geschnitten
wird.
12. Verfahren nach einem der Ansprüche 8 bis 10,
dadurch gekennzeichnet,
daß das mit einem Bindemittel versetzte Mineralfaservlies in Produkte wie röhrenförmige
Teile geformt wird, die in ihren Formen gehärtet werden.
13. Verfahren nach einem der Ansprüche 8 bis 10,
dadurch gekennzeichnet,
daß das mit einem Bindemittel versetzte Mineralfaservlies in einer nicht-härtenden
Umgebung gelagert wird und daß das Härten zu einem gewünschten Zeitpunkt in situ durchgeführt
wird, wobei das Produkt auf ein zu dämmendes Objekt aufgebracht worden ist.
1. Produit isolant, destiné en particulier à l'isolation thermique de conduites, comprenant
des fibres minérales et un liant, caractérisé en ce que ledit liant consiste principalement
en un verte soluble et en un laitier ou autre matériau, qui forme un lien hydraulique
avec le verre soluble.
2. Produit isolant selon la revendication 1, caractérisé en ce que le liant est présent
dans le produit dans une quantité telle que le rapport pondéral de la quantité de
fibres minérales à la substance sèche du verre soluble est de 100:1 à 100:20, de préférence
de 100:5 à 100:15.
3. Produit isolant selon la revendication 1 ou 2, caractérisé en ce que le laitier
est présent dans le liant dans une quantité telle que le rapport pondéral de la substance
sèche du verre soluble au laitier est de 100:1 à 100:50, de préférence de 10:1 à 10:2.
4. Produit isolant thermique selon l'une quelconque des revendications précédentes,
caractérisé en ce que le laitier est du laitier de haut fourneau pulvérisé.
5. Produit isolant selon l'une quelconque des revendications précédentes, caractérisé
en ce que le liant contient des agents modifiants, antipoussière, hydrophobisants
et/ou des agents de durcissement supplémentaires pour les fibres minérales.
6. Produit isolant selon la revendication 5, caractérisé en ce que le liant contient
du polybutène comme agent antipoussière et du silane comme agent hydrophobisant.
7. Produit isolant selon l'une quelconque des revendications précédentes, caractérisé
en ce qu'il est non durci et conditionné dans un emballage étanche et à l'épreuve
du gaz.
8. Procédé de préparation d'un produit isolant, destiné en particulier à l'isolation
thermique de conduites, comprenant les étapes de préparation d'un liant obtenu en
mélangeant les composants de ce liant dans l'eau pour former une suspension, en agitant
la suspension, en traitant des fibres minérales avec le liant et en durcissant le
liant immédiatement ou au moment désiré, à la température régnant à l'extérieur ou
à une température élevée, caractérisé en ce que le liant consiste principalement en
un verte soluble et en un laitier ou autre matériau qui, avec le verre soluble, forme
un lien hydraulique.
9. Procédé selon la revendication 8, caractérisé en ce que les additifs pour le durcissement,
la modification, le traitement antipoussière ou l'hydrophobisation ultérieurs du produit,
sont appliqués sur la laine de fibres minérales sous forme d'une solution distincte,
ou mélangés à la solution du liant, immédiatement avant que celle-ci ne soit appliquée
sur la laine de fibre minérale.
10. Procédé selon la revendication 8 ou 9, caractérisé en ce que le liant et les éventuels
additifs sont appliqués sur la laine de fibres minérales immédiatement après la formation
des fibres et/ou plus tard, pendant la préparation.
11. Procédé selon l'une quelconque des revendications 8 à 10, caractérisé en ce que
la toile de fibres minérales traitée avec le liant est durcie à température ambiante,
entre des feuilles métalliques par exemple, ou à une température élevée dans une chambre
de durcissement, à la suite de quoi la toile est découpée selon les produits désirés,
en feuilles isolantes par exemple.
12. Procédé selon l'une quelconque des revendications 8 à 10, caractérisé en ce que
la toile de fibres minérales traitée avec le liant est formée en produits, en bols
tubulaires par exemple, qui sont durcis dans leurs moules.
13. Procédé selon l'une quelconque des revendications 8 à 10, caractérisé en ce que
la toile de fibres minérales traitée avec le liant est stockée dans un environnement
non durcissant et que ce durcissement est effectué au moment désiré in situ, le produit
ayant été appliqué sur un objet isolant.