Mineral wool insulation

Abstract

A method of manufacturing a mineral fiber thermal insulation product comprises the sequential steps of: Forming mineral fibers from a molten mineral mixture; spraying a substantially formaldehyde free binder solution on to the mineral fibers, the binder solution comprising: a reducing sugar, an acid precursor derivable from an inorganic salt and a source of nitrogen; Collecting the mineral fibers to which the binder solution has been applied to form a batt of mineral fibers; and Curing the batt comprising the mineral fibers and the binder which is in contact with the mineral fibers by passing the batt through a curing oven so as to provide a batt of mineral fibers held together by a substantially water insoluble cured binder.

Description

This application is a U.S. national counterpart application of International Application Serial No. PCT/EP2008/060178, filed Aug. 1, 2008 under 35 USC §371, which claims priority to GB Patent Application Serial Number 0715100.4, filed Aug. 3, 2007, European GB Patent Application Serial Number 0807777.8, filed Apr. 29, 2008, and GB Patent Application Serial Number 0810297.2, filed Jun. 6, 2008, the entire disclosures of each of which are hereby incorporated herein by reference.

TECHNICAL FIELD

This invention relates to the manufacture of mineral wool insulation, for example glass wool or stone wool insulation, and to mineral wool insulation products.

BACKGROUND

WO 2007/014236 (incorporated herein by reference) discloses manufacture of mineral wool insulation products using binders which comprise Maillard reactants. One particular binder disclosed is based on a triammonium citrate-dextrose system derived from mixing dextrose monohydrate, anhydrous citric acid, water and aqueous ammonia. One of the many advantages of this binder system is that it is formaldehyde free.

SUMMARY

One aspect of the present invention provides a method of manufacturing a mineral fibre thermal insulation product in accordance with claim 1; further aspects of the inventions are defined in other independent claims. The dependent claims define alternative and/or preferred embodiments.

Binder solutions used in accordance with the present invention may be “substantially formaldehyde free”, that is to say that they liberate less than 5 ppm formaldehyde as a result of drying and/or curing (or appropriate tests simulating drying and/or curing). Such binder solutions are preferably “formaldehyde free”, that is the say they liberate less than 1 ppm formaldehyde in such conditions.

Insulation materials in accordance with the invention which incorporate binders may be “substantially formaldehyde free”, that is to say that they comprise less than 5 ppm or less than detectable limits of free formaldehyde and/or consist of materials which together comprise less than these amounts of free formaldehyde and/or release levels of formaldehyde in standardised tests adapted to simulate their ordinary use which allows them to be classified as having no or undetectable levels of formaldehyde release. Preferably, such products release less than 10 μg/m³, more preferably less than 5 μg/m³ of formaldehyde during the period of 24-48 hours from the start of testing in accordance with ISO 16000.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows a plan view of a mineral fibre test sample, where r is radius=12.7 mm, DC is distance between centers=44.5 mm, a=25.4 mm, and b=121 mm.

DETAILED DESCRIPTION

It has been found that insulation materials made according to the present invention may have at least equivalent and indeed improved properties compared to, for example, products made using the tri-ammonium citrate-dextrose system of WO 2007/014236. WO 2007/014236 teaches binder systems based, inter alia, on a combination of a carbohydrate (for example a reducing sugar), ammonia and a carboxylic acid and suggests that a Maillard type reaction may form the basis of the curing chemistry. It would have been thought that the nature of the acid used would have a significant effect upon the properties of the cured binder, particularly if the acid precursor and/or a derivative therefrom is incorporated into the structure of the cured binder. It is thus surprising that an acid precursor derivable from an inorganic salt should provide a suitable acid precursor in an otherwise apparently similar binder system.

Use of an acid precursor derivable from an inorganic salt may have significant advantages in terms of cost, availability and ease of handling. A particular advantage can be achieved by use of one or more inorganic ammonium salts, for example, an ammonium sulphate, an ammonium phosphate or an ammonium carbonate. An ammonium salt may provide the or part of the acid precursor and/or the or part of the source of nitrogen and/or the or part of a pH control system. An ammonium nitrate may also work; however, ammonium nitrate may oxidise aldehyde groups of the carbohydrate (for example in the case of dextrose) and/or require precautions to avoid explosions.

An ammonium sulphate is particularly advantageous but ammonium phosphate may be used in addition to or instead of this. Ammonium phosphate may be mono ammonium phosphate, di ammonium phosphate or tri ammonium phosphate; it may be an ammonium hydrogen phosphate. An ammonium carbonate, alone or in combination with the other materials disclosed herein, may also provide good results. The ammonium carbonate may be an ammonium bicarbonate.

The acid precursor, particularly when this consists essentially of inorganic ammonium salt(s), may make up

• • at least 5%, preferably at least 7%, more preferably at least 9% by dry weight of the uncured binder solution; and/or
  • less than 20%, preferably less than 18%, more preferably less than 16% by dry weight of the uncured binder solution.

The acid may comprise: a sulphuric acid, a phosphoric acid, a nitric acid or a weak acid.

The binder may comprise between 5%-25%, preferably 10% to 20%, more preferably 15% to 20% by dry weight of acid precursor (particularly where this is an inorganic ammonium salt) to carbohydrate (particularly when this is a sugar).

Where the binder comprises both an acid precursor derivable from an inorganic salt and an organic acid with the carbohydrate (particularly where this is a sugar), these may be present in the following amounts by dry weight with respect to the carbohydrate:

	Preferred	More preferred	Most preferred
acid precursor	At least 2.5%	At least 5%
derivable from an
inorganic salt
organic acid	At least 2.5%	At least 5%
Combination of	5-25%	10-20%	15-20%
organic acid and
acid precursor
derivable from an
inorganic salt

Where an organic acid is used, this is preferably derived from an ammonium salt. For example, an ammonium citrate, particularly tri-ammonium citrate may be used as a source of citric acid.

Prior art phenol formaldehyde binder systems for mineral wool insulation have been used with the addition of about 2% by weight ammonium sulphate as a curing agent. However, the chemistry of such phenol formaldehyde binder systems is not comparable to the binder systems of the present invention which are not based on phenol and/or formaldehyde and/or on other phenolics.

A carbohydrate may be used in the binder solution rather than specifically a reducing sugar and may comprise a monosaccharide, for example in its aldose or ketose form. Preferably, the carbohydrate comprises a sugar, more preferably a reducing sugar or a reactant that yields a reducing sugar in situ under thermal curing condition; it may comprise glucose (ie dextrose). The carbohydrate may comprise a carbohydrate having a reducing aldehyde. It is believed that the use of a reducing sugar and particularly dextrose gives particularly good results for the manufacture of mineral wool insulation products. The dextrose need not be 100% pure but use of a material having a dextrose equivalent value of at least 0.85, preferably at least 0.9 and more preferably at least 0.95 is thought to be advantageous. The dextrose equivalent value DE can be thought of as i) a measure of de-polymerization and is roughly: DE=100/dp where dp stands for degree of polymerization or ii) the total amount of reducing sugars calculated as D-glucose (dextrose) on a dry basis.

Preferably, the binder solution and/or the binder is free or substantially free of starch; the presence of substantial quantities of starch is thought to increase the curing time and/or reduce the strength of the cured binder. The binder solution and/or the binder may be free or substantially free of proteins.

Industrial, non-food grade dextrose may be used as the reducing sugar; products such as Sirodex331 which is a 75% solids sugar solution obtainable from Tate and Lyle with a DE value of 94.5 may be used.

Particularly in the case where the reducing sugar consists essentially of dextrose and the acid precursor consists essentially of an ammonium salt, for example an ammonium sulphate, the ratio by dry weight of the amount of reducing sugar/the amount of acid precursor may be greater than or equal to 2.5 and/or less than or equal to 13.

The source of nitrogen may be an amine or an amine reactant; it may be derivable from the same source as the acid precursor, for example, from an inorganic ammonium salt. It is preferably ammonia in solution.

Precursors for and/or reactants which give the materials referred to may be used.

In one embodiment, the binder is derived essentially from a reducing sugar and an inorganic ammonium salt in aqueous solution.

In another embodiment, the binder may also comprise an organic acid, particularly a carboxylic acid; this may be a polycarboxylic acid, particularly a bi-carboxylic acid or tri-carboxylic acid, preferably citric acid; it is preferably monomeric. The combination of an organic acid (or a precursor a salt or an anhydride thereof) with an acid precursor derivable from an inorganic salt may present various advantages. Firstly, such a combination may reduce the risk of punking (which has been observed with such binders based solely on organic acids) whilst providing acceptable strength. Punking is a term of art in the mineral fibre insulation area which generally denotes a comparatively rapid oxidation of a binder with a concomitant generation of heat in a finished and generally packaged insulation product. Punking generally causes generation of fumes and discolouring of the insulation material. It may be associated with exothermic reactions which increase the temperatures through the thickness of the insulation material; this may destroy the integrity of the insulation product and/or present a fire hazard.

Alternatively or additionally, the combination of an organic acid (or a precursor, a salt or an anhydride thereof) with an acid precursor derivable from an inorganic salt may moderate acid conditions occurring during curing and thus reduce the risk or tendency of such conditions to cause significant damage to the material being bound. Such a combination may be particularly advantageous as a binder for stone wool insulation whose fibres may be more susceptible to potential damage by acid than, for example, glass wool insulation.

In a further embodiment, the binder is derived essentially from: a carbohydrate; an inorganic ammonium salt; and an organic acid and/or organic acid precursor; in aqueous solution.

The term “consist or consisting essentially of” is intended to limit the scope of a claim to the specified materials or steps and those that do not materially affect the basic and novel characteristic(s) of the claimed invention.

Binders which comprise or consist essentially of the components described herein may include additives, for example, additives selected from: silanes, mineral oils, coupling agents, silicones or siloxanes (particularly for water repellency), silicon containing compounds, surfactants, hydrophilic additives, hydrophobic additives, waxes, substances useful for controlling the pH (e.g. ammonium hydroxide) and ammonia. Ammonium hydroxide when used, and indeed other additives, may provide the and/or an additional source of nitrogen.

Preferably, the total quantity of additives (excluding ammonia) is less than 5% by weight (excluding the weight of water present), more preferably less than 3% or less than 2% by weight.

It is preferred to include a silane as an additive. The binder and/or binder solution may comprise at least 0.1% and/or less than 1% of a silane by dry weight. The silane may be amino substituted; it may be a silyl ether and it is believed that its presence may significantly improve the long term strength of the binder, particularly after weathering.

Preferences for the pH of the binder are:

	Preferred	More preferred	Most preferred
	pH of binder	≧7	≧8	≧9

at least in the state in which the binder is applied to a material to be bound and/or recovered in a waste water recuperation system. Such a neutral or alkaline pH of the binder may alleviate problems of corrosion of manufacturing equipment which have been encountered with some essentially acidic prior art binder systems. Such prior art binders include binders consisting essentially of polyacrylic acids or polymer polycarboxylic acids. One particular advantage of the present invention is thus the use of a binder system that can operate in such neutral or alkaline conditions. When cured, the binder may become acidic during the curing process. However, equipment corrosion considerations are less significant in this case due to the minimal contact between the manufacturing equipment and the binder when in this state. The pH of the binder may be less than or equal to 13, preferably less than or equal to 12, 11 or 10. A preferred pH may be in the range of 7.5 to 9.5, particularly 8 to 9.

It is preferred to arrange the pH of the binder solution at an appropriate level to prevent precipitation of its constituents and particularly to ensure that the acid precursor derivable from an inorganic salt remains in solution. This is particularly the case where ammonium phosphate provides the acid precursor. Better dry and/or weathered strengths and/or more homogeneous products may be achieved by using homogeneous binder solutions comprising ammonium salt acid precursors which are free from precipitates, particularly when ammonium phosphate is used and the binder solution is free from phosphate precipitates.

The binder composition may be provided in the form of an aqueous solution; it may contain free ammonia or excess ammonia in solution. A neutral or alkaline pH of the binder may be generated by an excess of alkaline groups compared with acid groups present in the binder solution, for example, due partially or substantially to the presence of ammonia in the solution. Additional ammonia may be added to the binder solution, for example 0.2%-1% by weight, or indeed more; this may help to keep a wash water system used in the manufacture of mineral wool insulation alkaline over the long term.

When binder solution is sprayed on to hot mineral wool fibres just after they have been formed, the residual heat of the mineral wool fibres may cause a significant portion of any water in the binder solution to evaporate. Consequently, the mineral wool fibres which are then collected to form a batt may have binder present on them in the form of a sticky, viscous or tacky liquid. This may facilitate bonding between individual fibres via the binder.

One of the many advantages of this binder system is that it is sprayed onto the mineral wool fibers in a substantially unreacted state. The ability to spray the binder solution onto the mineral wool fibers in a substantially unreacted state may alleviate problems associated with pre-reacting the binder components in solution which have been encountered with some prior art binder systems in which the components are pre-reacted. Such prior art binders include binders consisting essentially of pre-reacted polymers or resins which are applied to the materials to be bound. With substantially unreacted binder present on the mineral wool fibers in the form of a sticky, viscous or tacky liquid, the reaction between the binder components may occur in a substantially dry state. One may describe the reaction as a bulk polymerization because it is occurring without the benefit of a solvent. A particular advantage of the present invention is thus the use of a binder system that can polymerise in a substantially dry state or through a bulk polymerisation.

The mineral fibres may be formed by internal or external spinning. They may have a temperature in the range 20° C. to 200° C., generally 30° C. to 100° C. or 150° C., when sprayed with the binder solution. The quantity of binder solution sprayed may be used with or without additional water sprays to assist in cooling the mineral fibres to a desired temperature between their formation and their collection to form a bat.

A particular advantage of using ammonia in solution to control the pH of the binder solution applied to the mineral fibres is that at least part of the ammonia of binder solution that sticks to the fibres may flash off due to the residual heat of the mineral wool fibres. Consequently, the binder solution that coats the fibres may have a lower pH than the binder solution sprayed.

The binder may be curable; it may be cured, for example in a curing oven; it may form a thermoset binder. In its cured form, the binder may: comprise melanoidins; and/or be thermoset; and/or be water insoluble or substantially water insoluble. The binder solution may be substantially colourless or white to off-white; upon curing, the binder may take on a dark colour, particularly a dark brown colour. The cured product may be dark in colour, particularly dark brown in colour. The binder may be free of proteins; it may be free of cellulosic feedstock. One of the many advantages of this binder system is that the extent of curing can be determined by the colour. Substantially dehydrated binder appears white or off-white. Progressively cured to a greater extent, the binder appears progressively darker in colour (a darker shade of brown). When applied to mineral fibers, the extent to which the mineral wool insulation has cured can be determined by its colour.

When applied to the mineral fibres and/or prior to passing through the curing oven, the binder may be free or substantially free of melanoidins and/or other reaction products derived from curing. Curing of the binder may produce glucosylamine, particularly as an intermediate product. Consequently, a cured or particularly a partially cured product may comprise glucosylamine.

The reaction of the binder upon curing may be essentially a Maillard type reaction as described for example in US Patent Application 20070027283 or WO2007/14236. The binder may comprise polymerisation products of a mixture that comprises a reducing sugar and a material selected from the group consisting of ammonium sulphate, ammonium phosphate, ammonium nitrate and ammonium carbonate.

The binder solution may be formulated by combining:

• • A carbohydrate, preferably a reducing sugar;
  • An acid precursor derivable from an inorganic salt, preferably an ammonium sulphate or ammonium phosphate;
  • A source of nitrogen; and
  • water.

The formulation may comprise optional or additional ammonia provided in the form of an aqueous ammonia solution. The water may comprise wash water.

Forming the binder solution from a carbohydrate and an acid precursor comprising an inorganic ammonium salt provides one particular advantageous preparation method. This may be achieved in a simple mixing chamber which may be open and/or at atmospheric pressure. The carbohydrate and/or the acid precursor may be added in powder or liquid form. The preparation is preferably carried out at room temperature. Preferably it is not necessary to supply heat to prepare the binder solution; nevertheless, the binder solution may be heated during its preparation, for example to a temperature with the range 20° C. to 80° C., particularly where this facilitates dissolving and/or mixing of its ingredients.

The binder solution may comprise:

• • at least 5% 10%, 15% or 18% solids and/or
  • less than 50%, 40% or 20% solids particularly determined as bake out solids by weight after drying at 140° C. for 2 hours.

The binder solution and/or the binder are preferably organic.

The mineral fibre insulation may be shaped and/or dimensioned and/or moulded with the aid of the binder.

The binder solution, particularly when applied to the mineral fibres, may have a viscosity appropriate for application by spraying or pouring. Its viscosity at 20° C. may be:

• • Less than about 1.5 Pa·s, preferably less than about 1×10⁻² Pa·s; and/or
  • Greater that about 2×10⁻⁴ Pa·s, preferably greater than about 5×10⁻⁴ Pa·s

Curing of the binder may occur in a curing oven, for example using forced hot air circulation; it may occur in a press. Curing may comprise a dehydration of the binder; it may comprise a polymerisation. Curing may comprise a bulk polymerisation reaction. Curing may be carried out for duration of 20 minutes or less, preferably 10 minutes or less. Curing of the binder preferably occurs when the binder solution (from which water may have been evaporated) is in contact with the mineral fibres; it may occur at substantially atmospheric pressure. The curing may be a substantially dry curing, that is to say by application of dry heat and/or substantially dry or heated atmospheric air rather than using steam or heated water vapour.

The curing temperature and time may be selected as a function of the product density and/or thickness. The curing oven in such cases may have a plurality of heating zones having temperatures within the range 200° C. to 350° C. (typically 230° C. to 300° C.). A thin, low density product (12 kg/m³ or less) may be cured by passing through the curing oven in as little as 20 seconds; a thick, high density product (80 kg/m³ or more) may require a passage of 15 minutes or more in the curing oven. The product may reach a temperature in the range 180° C.-220° C. during the curing process.

The cured binder may comprise greater than 2% and/or less than 8% nitrogen by mass as determined by elemental analysis.

The binder in its uncured state may comprise the following levels of sulphates, phosphates carbonates and/or nitrates by dry weight:

• • Greater than 2.5%, 3% or 5%; and/or
  • Less than 25%, 22%, or 20%

Finished materials manufactured using binder systems according to the present invention may have residual levels of sulphates, phosphates, carbonates and/or nitrates derived notably from the inorganic salt serving as the acid precursor. Such species may be present in the following quantities:

• • Greater than 500, 750, 1000 or 1500 mg/kg; and/or
  • Less than 5000, 4000 or 3000 mg/kg.

The presence of such species may be assessed in a leach test and provide an indication in the final product of the binder system used.

The quantity of binder in the finished product may be:

• • Greater than: 1%, 2%, 2.5%, 3%, 3.5% or 4%; and/or
  • Less than: 20%, 15%, 10% or 8%measured by dry weight of the finished product.

The mineral wool insulation may have one or more of the following parting strengths:

Ordinary Parting Strength of

• • At least 120 g/g, preferably at least 150 g/g; and/or
  • Less than 400 g/g

Weathered Parting Strength of

• • At least 120 g/g, preferably at least 150 g/g; and/or
  • Less than 400 g/g

% loss between Ordinary and Weathered Parting Strength of

• • Less than 10%, preferably less than 5%

The mineral wool insulation may have one or more of the following characteristics:

• • A density greater than 5, 8 or 10 kg/m³;
  • A density less than 200, 180 or 150 km/m³
  • Comprise glass wool fibres and have a density greater than 5, 8 or 10 kg/m³ and/or less than 80, 60 or 50 kg/m³;
  • Comprise stone wool fibres and have a density greater than 15, 20 or 25 kg/m³ and/or less than 220, 200 or 180 kg/m³;
  • A thermal conductivity A of less than 0.05 W/mK and/or greater than 0.02 W/mK
  • Comprise less than 99% by weight and/or more than 80% by weight mineral fibres.
  • A thickness of greater than 10 mm, 15 mm or 20 mm and/or less than 400 mm, 350 mm or 300 mm.

Embodiments of the invention will now be described by way of example with reference to FIG. 1 which is a plan view of a test sample.

Shell Bone Testing:

Binders were prepared as aqueous solutions by

• • combining the ingredients of a desired binder formulation in an open, unheated reaction vessel
  • adding distilled water
  • subsequently adding a silane solution
  • agitating during addition of liquids and afterwards for several minutes to achieve complete dissolution of solidssuch that the binder solution contained approximately 45% dissolved solids as a percentage of total weight of solution. A 2-g sample of this solution, upon thermal curing at about 200° C. to 210° C. for 8 minutes, would yield 30% solids (the weight loss being attributed to dehydration during thermoset binder formation).

An evaluation of dry and “weathered” tensile strength of glass bead-containing shell bones provided an indication of the likely tensile strength and the likely durability of fibreglass insulation or other materials prepared with that particular binder. Predicted durability is based on the ratio of a shell bone's weathered tensile strength to its dry tensile strength.

To prepare the shell bones, an electric mixer was used for about two minutes to mix approximately 75 g of binder with 727.5 g of glass beads (equivalent to Quality Ballotini Impact Beads, Spec. AD, US Sieve 70-140, 106-212 micron-#7, from Potters Industries, Inc.). Any clumps from the sides of the mixer whisk and from the sides and bottom of the mixing bowl were mixed in manually using a spatula about half way through the mixing and also at the end of the mixing.

The prepared glass beads/binder mixture was added to the mould cavities of a shell bone mould (Dietert Foundry Testing Equipment; Heated Shell Curing Accessory, Model 366) which had been pre-heated to about 218° C. (425° F.). The surface of the mixture in each cavity was flattened out, while scraping off the excess mixture to give a uniform surface area to the shell bone. Any inconsistencies or gaps that existed in any of the cavities were filled in with additional glass beads/binder mixture and then flattened out. The top platen was quickly placed onto the bottom platen (to avoid producing shell bones with two differentially cured layers). The cured shell bones were removed after seven minutes, cooled to room temperature on a wire rack, labelled and placed individually in plastic storage bags. If shell bones could not be tested on the day they were prepared, the shell bone-containing plastic bags were placed in a dessiccator unit. During curing the temperature of the bottom platen ranged from about 204° C. to about 221° C. (about 400° F. to about 430° F.), while the temperature of the top platen ranged from about 227° C. to about 243° C. (about 440° F. to about 470° F.).

Procedure for Testing Breaking Strength:

• • Equipment: 5500 R Instron machine
  • Immediately prior to testing, each shell bone was removed from is plastic bag and its weight and thickness recorded.Weathering Procedure for Shell Bones:
  • 16 hours weathering in a pre-heated humidity chamber (65° C., 95% relative humidity)
  • upon removal shell bones were sealed in individual plastic storage bags and taken immediately for testing.Procedure for Measuring Gel Time:

A small amount of binder (2.0 ml) is added to the centre of a hot plate set to 150° C. and a stop watch is started. The binder is worked with a spatula until it is possible to draw the sample into a long string. The time taken from the addition of the binder to the string formation is the gel time.

Binder Formulations Tested—Inorganic Acid Precursors Compared with Citric Acid:

Test ref: Binder formulation (by dry weight)
A         85% DMH + 15% CA + 4.8% NH4OH + 0.3% ISI0200
B         90% DMH + 10% AmSO4 + 4.8% NH4OH + 0.3% ISI0200
C         85% DMH + 15% AmSO4 + 4.8% NH4OH + 0.3% ISI0200
D         80% DMH + 20% AmSO4 + 4.8% NH4OH + 0.3% ISI0200
E         90% DMH + 10% AmPO4 + 4.8% NH4OH + 0.3% ISI0200
F         85% DMH + 15% AmPO4 + 4.8% NH4OH + 0.3% ISI0200
G         80% DMH + 20% AmPO4 + 4.8% NH4OH + 0.3% ISI0200

Binder Formulations Tested—Combined Inorganic Acid Precursor and Citric Acid Compared with Citric Acid Alone and Inorganic Acid Precursor Alone:

Test ref: Binder formulation (by dry weight)
H         85% DMH + 15% CA + 4.8% NH4OH + 0.3% ISI0200
I         85% DMH + 10% CA + 5% AmSO4 + 4.8% NH4OH + 0.3%
          ISI0200
J         85% DMH + 5% CA + 10% AmSO4 + 4.8% NH4OH + 0.3%
          ISI0200
K         85% DMH + 15% AmSO4 + 4.8% NH4OH + 0.3% ISI0200
Key:
DMH = Dextrose monohydrate
CA = citric acid
NH4OH = ammonium hydroxide
ISIO200 = silane
AmSO4 = ammonium sulphate
AmPO4 = ammonium phosphate

Test Results—Inorganic Acid Precursors Compared with Citric Acid:

			Loss in		pH of
			breaking		binder
	Dry	Weathered	strength	Gel	solution
	breaking	breaking	from	time of	just before
Test	strength	strength	weathering/	binder	mixing with
ref	(MN/m2)	(MN/m2)	%	solution (s)	beads
A	1.455	1.567	−7.70	343	9.54
B	1.271	0.895	29.57	280	10.28
C	1.550	0.856	44.79	362	10.24
D	1.877	1.156	38.39	327	10.13
E	1.499	1.069	28.68	356	10.18
F	1.281	0.848	33.82	334	9.99
G	1.123	0.801	28.74	287	9.73

Test Results—Combined Inorganic Acid Precursor and Citric Acid Compared with Citric Acid Alone and Inorganic Acid Precursor Alone:

			Loss in		pH of
			breaking		binder
	Dry	Weathered	strength	Gel	solution
	breaking	breaking	from	time of	just before
Test	strength	strength	weathering/	binder	mixing with
ref	(MN/m2)	(MN/m2)	%	solution (s)	beads
H	1.69	1.50	11.32	363	9.39
I	1.50	1.18	21.37	341	9.71
J	1.21	1.05	13.19	375	9.99
K	1.47	1.02	30.33	376	9.97

Results from tests carried out together (test A to G were carried out in one session and tests H to K carried out during another session) provide a useful indication of results relative to other results obtained during the same test session. It may not be reliable to compare tests results from different test sessions.

First Comparative Testing on Insulation Product:

Comparative testing of binder systems on a mineral fibre insulation product gave the following results:

Binder tested	Description	Formulation
PF1	Comparative example -	Resin, Urea, Lignin,
	standard phenol formaldehyde	Ammonia, Silane
	binder
AC1	Comparative example -	Dextrose 85% Citric Acid
	ammonium citrate based	15% Ammonia 4.8% Silane
	binder	0.3%
Ex1	Example 1 of the present	Dextrose 85% Ammonium
	invention	Sulphate 15% Ammonia
		4.8% Silane 0.3%
Product	glass wool fibre insulation product, nominal density
used for	16 kg/m3, nominal thickness 75 mm, nominal width 455 mm
test:

Binder Content of Test Product LOI (Loss on Ignition) % Weight:

       Mean
Binder LOI
PF1    6.22%
AC1    6.91%
Ex1    6.78%

Drape Test (Mean Average in mm Measured after the Periods Specified):

			Week	Week	Week
	Binder	Day 1	1	3	6
	PF1	55	68	60	71
	AC1	83	99	80	72
	Ex1	66	76	66	75

Thickness (Mean Average in mm Measured after the Periods Specified in accordance with British Standard BS EN 823:1995)

			Week	Week	Week
	Binder	Day 1	1	3	6
	PF1	76.4	75.1	75.1	75.2
	AC1	75.3	73.6	72.5	74
	Ex1	76	76.7	74.9	74.3

Density (Mean Average in kg/m³ Measured After the Periods Specified)

			Week	Week	Week
	Binder	Day 1	1	3	6
	PF1	16.44	16.7	16.35	16.44
	AC1	16.68	16.41	16.33	16.48
	Ex1	16.5	16.9	16.5	16.5

Quantity of Sulphates Present mg/kg

		Sample	Sample
	Binder	1	2
	AC1	240	240
	Ex1	2000	2200

Parting Strength (g/g)

	Binder	Ordinary	Weathered	% loss
	PF1	248	107	56.85
	AC1	230	199	13.47
	Ex1	196	189	3.57

Test Procedures:Binder Content LOI (Loss on Ignition)

A weighed sample of wool plus binder is placed in a muffle furnace set to 550° C. After a set time the wool is removed from the furnace, placed in a desiccator to cool and re-weighed. The weight loss is expressed as a percentage of the original sample weight and is known as the binder content or Loss On Ignition (LOI).

Drape Test

A single batt (or slab) is placed across two poles (each 500 mm long, 20 mm diameter) set into a wall 1 meter apart. The degree of sag in the centre of the batt is recorded. This is repeated for all of the batts in a pack and for several packs. Packs are measured at set points over a period of time to determine the long term effects of compression on the batts.

Density: Measured for the Samples Subjected to the Drape Test

Quantity of sulphates present: leaching test for granular wastes in water with eluate analysis according to British standard BS EN 12457-2 at L/S10

Parting Strength

The parting strength is expressed in grams/gram being the total breaking load of six test specimens divided by their total weight.

The test is carried out on mineral fibre mats as received for testing (Ordinary Parting Strength) and after an accelerated weathering test as explained below

(Weathered Parting Strength).

A first set of six samples of the form and dimensions shown in FIG. 1 are cut from the mineral fibre mat to be tested. The dimensions are:

r: radius 12.7 mm;

DC: distance between centres 44.5 mm;

a: 25.4 mm;

b: 121 mm.

The long axis of the samples should be parallel to the conveyor direction and the samples should be taken across the full width of the mineral mat. A second set of six samples is then taken in the same way.

The total weight of the first group of six samples W1 in grams is recorded. The total weight of the second group of six samples W2 in grams is recorded; these samples are then placed in a preheated autoclave and conditioned on a wire mesh shelf away from the bottom of the chamber under wet steam at 35 kN/m² for one hour. They are then removed, dried in an oven at 100° C. for five minutes and tested immediately for parting strength.

To test the parting strength, each sample is mounted in turn on the jaws of a 5500 Instron tensile strength machine and the maximum breaking load in grams or Newtons is recorded. If the breaking load is measured in Newtons it is converted to grams by multiplying it by 101.9. Six results in grams are obtained for each set of samples: G1 G2 G3 G4 G5 and G6 for the first set of samples and G7 G8 G9 G10 G11 and G12 for the second set of samples. The Ordinary Parting Strength is calculated from the first set of samples using the formula Ordinary Parting Strength=(G1+G2+G3+G4+G5+G6)/W1.

The Weathered Parting Strength is calculated from the second set of samples using the formula Weathered Parting Strength=(G7+G8+G9+G10+G11+G12)/W2.

Second Comparative Testing on Insulation Product:

Product used glass wool fibre insulation product, nominal density
for test:    7.2 kg/m3, nominal thickness 159 mm

Samples: The Following Samples of Fibreglass Batts were Tested:

		Target binder
		content (LOI)
Example	Binder Description	for product
PF2	standard phenol formaldehyde binder of	4.5%
	Resin, Urea, Ammonia, Silane
2.1	Dextrose 85% Ammonium Sulphate 15%	4.5%
	Silane 0.3% (10.6% solids in binder
	solution)
2.2	Dextrose 85% Ammonium Sulphate 15%	4.5%
	Silane 0.3% Norjohn oil (11.4% solids in
	binder solution)
2.3	Dextrose 85% Ammonium Sulphate 15%	4.5%
	Silane 0.3%, 2.4% NH3 (10.6% solids in
	binder solution)
2.4	Dextrose 85% Ammonium Sulphate 15%	6.0%
	Silane 0.3%, 2.4% NH3 (10.6% solids in
	binder solution)

Results

	PF2	2.1	2.2	2.3	2.4
Recovery	158	mm	157	mm	163	mm	160	mm	166	mm
Recovery. % nominal	99.4%	99.0%	102.8%	100.6%	104.8%
Parting Strength	190.8	g/g	131.7	g/g	146.7	g/g	159.9	g/g	143.9	g/g
(ASTM C-686)
Parting strength after	145.9	g/g	100.0	g/g	110.3	g/g	124.9	g/g	114.3	g/g
weathering (ASTM C-686
following conditioning
for 7 days at 90° F., 90%
relative humidity)

Claims

1. A method of manufacturing a glass fibre thermal insulation product which comprises less than 99% by weight and more than 80% by weight glass fibres and has a density greater than 5 kg/m3 and less than 80 kg/m3, the method comprising sequentially: forming glass fibres from a molten mineral mixture;spraying a substantially formaldehyde-free binder solution onto the glass fibres;collecting the glass fibres to which the binder solution has been applied to form a batt of glass fibres; andcuring the batt comprising the glass fibres and the binder by passing the batt through a curing oven so as to provide a batt of glass fibres held together by a cured, thermoset, substantially formaldehyde-free, nitrogenous polymer-containing binder,wherein the binder solution consists essentially of (i) a carbohydrate reactant comprising a reducing sugar or a carbohydrate reactant that yields a reducing sugar in situ under thermal curing conditions and (ii) an acid precursor, in aqueous solution,wherein the acid precursor provides (i) ionic species selected from the group consisting of sulphates, phosphates, nitrates and combinations thereof and ii) an amine or amine reactant.

2. The method of claim 1, in which wash water is sprayed onto the glass fibres between their formation and their collection to form a batt, at least a part of the wash water having been sprayed onto glass fibres and subsequently returned to a wash water system to be reused as wash water.

3. The method of claim 1, in which the binder solution is sprayed onto the glass fibres when the glass fibres are at a temperature of between 30° C. and 150° C.

4. The method of claim 1, in which curing of the binder is carried out by passing the batt through at least one zone of a curing oven at a temperature within the range 230° C.—300° C. with an oven residence time in the range 30 seconds to 20 minutes.

5. The method of claim 1, in which the binder solution has a pH of greater than 7 when sprayed onto the glass fibres.

6. The method of claim 1, in which the acid precursor makes up between 5% and 25% by dry weight of the binder solution.

7. The method of claim 1, in which the acid precursor comprises an inorganic salt.

8. The method of claim 1, in which the carbohydrate reactant of the binder solution comprises a reducing sugar which has a dextrose equivalent value of at least 0.85.

9. The method of claim 1, in which the carbohydrate reactant of the binder solution consists essentially of dextrose.

10. The method of claim 1, in which the binder solution comprises a silicon containing compound.

11. The method of claim 1, in which the binder solution comprises a material selected from the group consisting of a polycarboxylic acid, a salt of a polycarboxylic acid, and an anhydride of a polycarboxylic acid.

12. The method of claim 1, in which the binder solution comprises excess ammonia.

13. The method of claim 12, in which the binder solution has a pH which, in its conditions of use, prevents precipitation of sulphates or phosphates.

14. The method of claim 1, in which there is at least 7% by dry weight of the acid precursor with respect to reducing sugar.

15. The method of claim 1, in which the ratio by dry weight of reducing sugar to acid precursor (expressed as dry weight of reducing sugar/dry weight of acid precursor) is in the range 2.5 to 13.

16. The method of claim 1, in which the cured binder comprises melanoidins.

17. The method of claim 1, in which the quantity of binder in the glass fibre thermal insulation product is greater than 1% and less than 15% measured by dry weight of the glass fibre thermal insulation product.

18. The method of claim 1, wherein the glass fibre thermal insulation product comprises residual levels of more than 500 mg of ionic species per kg of product, said species selected from the group consisting of sulphates, phosphates, nitrates and combinations thereof, in which the residual levels are assessed in a leach test.

19. The method of claim 1, wherein the glass fibre thermal insulation product comprises residual levels of more than 750 mg of ionic species per kg of product, said species selected from the group consisting of sulphates, phosphates, nitrates and combinations thereof, in which the residual levels are assessed in a leach test.

20. The method of claim 1, wherein the glass fibre thermal insulation product comprises residual levels of less than 5000 mg of ionic species per kg of product, said species selected from the group consisting of sulphates, phosphates, nitrates and combinations thereof, in which the residual levels are assessed in a leach test.

21. The method of claim 1, in which the cured binder is substantially water insoluble.

22. The method of claim 1, in which the cured binder has a dark brown color.

23. The method of claim 1, in which the cured binder comprises greater than 2% nitrogen by mass.

24. The method of claim 1, in which the cured binder comprises less than 8% nitrogen by mass.

25. The method of claim 1, in which the reaction of the binder upon curing is essentially a Maillard type reaction.

26. The method of claim 1, in which the binder solution as sprayed onto the glass fibres comprises at least 5% solids.

27. The method of claim 1, in which the binder solution as sprayed onto the glass fibres comprises at least 10% solids.

28. The method of claim 1, in which the binder solution as sprayed onto the glass fibres comprises levels of sulphates, phosphates, nitrates, or combinations thereof by dry weight that are greater than 2.5%.

29. The method of claim 1, in which the binder solution as sprayed onto the glass fibres comprises levels of sulphates, phosphates, nitrates, or combinations thereof by dry weight that are greater than 3%.

30. The method of claim 1, in which the binder solution as sprayed onto the glass fibres comprises levels of sulphates, phosphates, nitrates, or combinations thereof by dry weight that are greater than 5%.

31. The method of claim 1, in which the binder solution as sprayed onto the glass fibres comprises less than 40% solids.

32. The method of claim 1, in which the binder solution as sprayed onto the glass fibres comprises levels of sulphates, phosphates, nitrates, or combinations thereof by dry weight that are less than 25%.

33. The method of claim 1, in which the acid precursor comprises an ammonium salt.

34. The method of claim 1, in which the glass fibre thermal insulation product has an Ordinary Parting Strength of at least 120 g/g and less than 400 g/g.

35. The method of claim 1, in which the spraying of substantially formaldehyde-free aqueous binder solution onto the glass fibres comprises spraying the substantially formaldehyde-free aqueous binder solution onto the glass fibres just after the glass fibres have been formed so that the residual heat from the glass fibres causes a significant portion of the water in the aqueous binder solution to evaporate.

36. The method of claim 1, in which glass fibres are formed by internal spinning.

37. The method of claim 1, in which the glass fibre thermal insulation product has i) an ordinary parting strength which is at least 120 g/g and less than 400 g/g and ii) a weathered parting strength which is at least 120 g/g and less than 400 g/g.

38. The method of claim 1, in which the glass fibre thermal insulation product has a thickness of greater than 15 mm and less than 350 mm.

39. The method of claim 1, in which the glass fibre thermal insulation product has a thermal conductivity λ of less than 0.05 W/mK and greater than 0.02 W/mK.

40. The method of claim 1, further comprising compressing the cured bans in a pack.

41. The method of claim I, wherein the binder solution includes at least one additive selected from: silanes, mineral oils, coupling agents, silicones, siloxanes, surfactants, hydrophilic additives, hydrophobic additives and waxes.

42. The method of claim 41, wherein the total quantity of the additives is less than 5% by weight excluding the weight of water present.

43. The method of claim 1, wherein the binder solution comprises between 0.1% and 1% of a silane or silicon-containing coupling agent calculated as dissolved binder solids.

44. A method of manufacturing a glass fibre thermal insulation product which comprises less than 99% by weight and more than 80% by weight glass fibres and has a density greater than 5 kg/m3 and less than 80 kg/m3, the method comprising sequentially: forming glass fibres from a molten mineral mixture; spraying a substantially formaldehyde-free aqueous binder solution onto the glass fibres just after they have been formed so that the residual heat from the glass fibres causes a significant portion of the water in the aqueous binder solution to evaporate;collecting the glass fibres to which the binder solution has been applied to form a batt of glass fibres; andcuring the batt comprising the glass fibres and the binder by passing the batt through a curing oven for a duration of 20 minutes or less using forced hot air convection so as to provide a batt of glass fibres held together by a cured, thermoset, substantially formaldehyde-free, nitrogenous polymer-containing binder,wherein the binder solution consists essentially of (i) a carbohydrate reactant comprising a reducing sugar or a carbohydrate reactant that yields a reducing sugar in situ under thermal curing conditions and (ii) an acid precursor, in aqueous solution;wherein the acid precursor makes up at least 7% by dry weight of the uncured binder solution,and wherein the acid precursor provides (i) ionic species comprising sulphates and/or phosphates and ii) an amine or amine reactant.

45. The method of claim 44, in which the ratio by dry weight of the reducing sugar to the acid precursor (expressed as dry weight of reducing sugar/ dry weight of acid precursor) is in the range 2.5 to 13.

46. The method of claim 44, further comprising compressing the cured bans in a pack.

47. The method of claim 44, in which the acid precursor comprises an ammonium salt.

48. The method of claim 47, wherein the ammonium salt comprises an ammonium sulphate salt.

49. The method of claim 47, wherein the ammonium salt comprises an ammonium phosphate salt.

50. The method of claim 33, wherein the ammonium salt comprises an ammonium sulphate salt.

51. The method of claim 33, wherein the ammonium salt comprises an ammonium phosphate salt.