Glass fiber composition

Information

  • Patent Grant
  • 6034014
  • Patent Number
    6,034,014
  • Date Filed
    Monday, August 4, 1997
    27 years ago
  • Date Issued
    Tuesday, March 7, 2000
    24 years ago
Abstract
The glass compositions of the present invention contain at least 2.0 wt % Al.sub.2 O.sub.3 to give resulting glass fiber an acceptable chemical durability for product performance, but no more than 3.0 wt % to ensure the fiber maintains a relatively high biosolubility. The compositions further include relatively high amount of Na.sub.2 O+K.sub.2 O+MgO+CaO, which tends to increase fiber biosolubility and allows for the use of reduced amounts of B.sub.2 O.sub.3 in the composition. The glass compositions have KI values that generally equal or exceed a KI value of 40 and are suitable for rotary processing. The compositions have liquidus temperatures below about 1800.degree. F. and viscosities above 300 Poise at the liquidus temperature. For higher B.sub.2 O.sub.3 compositions the liquidus temperatures are below 1650.degree. F., and the viscosities are above 1,000 Poises at the liquidus temperatures.
Description

CROSS-REFERENCE TO RELATED APPLICATIONS
Not Applicable
STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT
Not Applicable
BACKGROUND OF THE INVENTION
The present invention is directed generally to glass compositions, and more particularly to glass fiber compositions having high KI values and structural durability.
Glass fiber, or fiberglass, insulation is well known and has been a commercial product for many years. Glass fiber insulation is widely used both residentially and commercially.
Generally, the insulation is made from intertwined soda lime alumina borosilicate glass fibers which are held together with a binder. The glass fibers are generally produced using SiO.sub.2 with a number of additives, such as Na.sub.2 O, K.sub.2 O, CaO, MgO, BaO, B.sub.2 O.sub.3, and Al.sub.2 O.sub.3, that enhance various properties of fibers. The binder may be any suitable material, but quite commonly is a phenol-formaldehyde resin or a urea formaldehyde resin.
A rotary process is often used to form the glass fibers. The rotary process typically involves the introduction of molten glass into a rotating device, called a spinner, which contains a plurality of holes circumferentially distributed around the spinner. The spinner is rotated about an axis to produce a centrifugal force on the molten glass. The rotation of the spinner forces the molten glass through the plurality of holes.
An annular stream of hot gases is passed around the spinner to contact and attenuate the fibers passing through the holes. A spray nozzle is positioned to coat the attenuated fibers with the binder.
A conveyer collects the binder-coated fibers in the form of a blanket, or batt, and the blanket is heat cured to produce the final insulation. The rotary process can be used to produce insulation having different densities by varying the conveyer speed and the thickness of the cured insulation.
Glass fiber insulation has been used to replace, or in lieu of, asbestos fiber insulation in many applications. It is generally believed that asbestos fibers, when inhaled, can result in significant disease in man. Though the exact mechanism responsible for the biological activity of asbestos fibers is unknown, it is widely believed that an important factor in the mechanism is the residence time of the fibers in the lungs.
Unlike asbestos fibers, glass fibers have not been linked to disease in man. Glass fiber also appears to have a much shorter residence time in the lungs than asbestos fibers.
The residence time of glass fibers in the lungs will depend, at least in part, upon chemical dissolution of the fiber. The rate of chemical dissolution of a material in biological fluid is generally referred to as the biosolubility or biological degradability of the material.
Despite the lack of a link between glass fibers and human disease, some countries, for example Germany, have proposed regulations for the use of glass fibers in insulation products. Glass fiber compositions that meet the standard in the proposed regulations are considered to be free of suspicion as a disease causing agent and can be used for both commercial and residential installations.
The regulations are based on a desire to minimize the residence time of the glass fiber in the lungs. It is a hope that minimizing the residence time of the glass fiber will decrease the possibility, if any, of subsequent disease.
The proposed German regulations for biosolubility require that glass fibers have a numerical index (KI) greater than or equal to 40 to be considered to be free of suspicion. The KI index, which is sometimes referred to as the Wardenbach Index, is described by the equation:
KI=.SIGMA.(Na.sub.2 O, K.sub.2 O, CaO, MgO, BaO, B.sub.2 O.sub.3)-2(Al.sub.2 O.sub.3)
where the values for each oxide correspond to the weight percentage of that oxide in the glass composition.
The index used in the regulation places severe constraints on the compositions of the glass, expressly on the levels of alumina (Al.sub.2 O.sub.3) and implicitly on the level of silica (SiO.sub.2)in the glass composition. Manufacturers must now produce glass fibers which meet the proposed regulations, while maintaining standard performance criteria for the products. The criteria include that the glass fiber must be producible using standard wool processes, have sufficient durability in use, and acceptable insulating properties.
Silica is the primary component in glass fiber and provides most of the structural and physical properties of the fiber. Alumina is primarily used in the fiber to provide additional durability to the fiber.
Initial attempts to produce glass fiber that complies with the regulations involved using reduced levels of alumina in the glass composition to increase the KI index. However, low alumina glass fibers tend to have poor durabilities.
A number of glass composition have been reported as having improved biosolubility or biodegradability. For example, Potter, U.S. Pat. No. 5,055,428, Cohen et al., U.S. Pat. No. 5,108,957, Nyssen, U.S. Pat. No. 5,332,698, and Bauer et al., U.S. Pat. No. 5,401,693, all describe glass fibers having improved biosolubility. Also, published PCT applications WO 95/31411, WO 95/32925, WO 95/32926, WO 95/32927, and WO 95/35265 and numerous published German applications have reported glass compositions having increased biodegradability.
Despite the improvements presented in the aforementioned patents and applications, the glasses failed to meet the KI.gtoreq.40 standard or significant processing and performance problems remain. The decreased performances and increased processing costs for glass compositions designed to meet the new biological standards is a clear shortcoming in the industry. In addition, higher alumina compositions of the prior art provide performance versatility, yet are either not acceptable in the emerging regulated marketplace or suffer from increased processing costs. Accordingly, there is still a need for a glass composition which has increased biosolubilities (KI value.gtoreq.40), while possessing acceptable processing properties, such as viscosity and liquidus temperatures, as well as acceptable performance and durability in use.
BRIEF SUMMARY OF THE INVENTION
The above objectives and others are accomplished by glass compositions in accordance with the present invention. The glass compositions contain at least 2.0 wt % Al.sub.2 O.sub.3 to give resulting glass fiber an acceptable chemical durability for product performance, but no more than 3.0 wt % to ensure the fiber maintains a relatively high biosolubility. The compositions further include relatively high amount of Na.sub.2 O+K.sub.2 O+MgO+CaO, which tends to increase fiber biosolubility and allows for the use of reduced amounts of B.sub.2 O.sub.3 in the composition.
The glass compositions have KI values that generally equal or exceed a KI value of 40 and are suitable for rotary processing. The compositions have liquidus temperatures below about 1800.degree. F., and have viscosities above 300 Poise at the liquidus temperatures.
In one aspect of the invention glasses are formulated with relatively high amounts of B.sub.2 O.sub.3 and low amounts of CaO+MgO. The high B.sub.2 O.sub.3 glasses were found to have very low liquidus temperatures (<1650.degree. F.) and higher viscosities (>1,000 Poise) at the liquidus temperature.
In another aspect of the invention, glasses are formulated with relatively low amounts of B.sub.2 O.sub.3 and high amounts of CaO+MgO. The low B.sub.2 O.sub.3 glasses were found to have slightly higher liquidus temperatures but still sufficiently low to be formed into fibers by the rotary process (liquidus temperatures <1800.degree. F., and viscosities at the liquidus temperature >300 Poise).
In some situations the low B.sub.2 O.sub.3 /high (CaO+MgO) glasses are highly advantageous. For example, lower amounts of B.sub.2 O.sub.3 can result in significantly lower batch costs.
Also, the lower B.sub.2 O.sub.3 level in the composition can result in lower volatile emissions both during melting and forming. When formed by the rotary process, the lower viscosity low B.sub.2 O.sub.3 glasses can be extruded through the spinner holes and attenuated without significant reheating of the fibers.
In another aspect of the invention, glasses are formulated with low amounts of MgO, generally below about 3.0 to 3.5 wt % have significantly improved chemical durabilities with respect to water. These compositions provide for an improved product performance in addition to improved biosolubility.
In another aspect of the invention, glasses are formulated with higher amounts of MgO, generally between about 2.0 and 6.0 wt %, and preferably between about 3.0 and 5.0 wt %. It was found that these glasses could be formulated with lower amounts of B.sub.2 O.sub.3, while still maintaining an acceptable liquidus temperature and viscosity at the liquidus temperature. Advantages of these glasses include lower cost and less volatile emissions during melting and forming.
The compositions of the present invention provides glass compositions that meet proposed biosolubility standards, while maintaining acceptable performance and durability as glass fiber insulation. Accordingly, the present invention overcomes the aforementioned difficulties of the prior art in meeting both public health standards and commercial requirements. These advantages and others will become apparent from the following detailed description of the invention.
DETAILED DESCRIPTION OF THE INVENTION
The present invention will be described generally with reference to present preferred embodiments of the invention only for the purpose of providing examples of the invention and not for purposes of limiting the same.
The applicants have found that acceptable glass processing and fiber biosolubility and durability can be maintained in glass fiber by providing compositions including alumina in a range of 2-3%, B.sub.2 O.sub.3 in the range of 6-15%, and increased levels of alkali and alkaline oxides over the prior art. Compositions of the present invention provide a balance between increased durability and biosolubility to address the shortcomings of the prior art.
The SiO.sub.2 content in compositions of the present invention ranges from 49-54%. The present invention provides for lower levels of silica to provide for increased levels of additives that are used to improve the biosolubility and the durability of the resulting glass fibers.
The Al.sub.2 O.sub.3 content in the composition should be approximately 2% or higher to provide sufficient performance durability. However, as the alumina content begins to exceed approximately 3%, the biosolubility of the composition will begin to deteriorate. It is preferable that the alumina content of the composition ranges from 2.1-2.9% and more preferably from 2.1-2.6% to provide a more balanced composition.
To compensate for the increased levels of alumina and its detrimental affect on the biosolubility, increased levels of alkali and alkaline oxides are included in the composition. Specifically, higher levels of MgO, CaO, Na.sub.2 O and K.sub.2 O can be used to improve the KI index and to lower the liquidus temperature of the compositions.
Na.sub.2 O is included in an amount ranging from approximately 16-22% depending on the desired properties. Na.sub.2 O will generally provide for lower viscosities and better melting characteristics for the glass. Preferably, the amount of Na.sub.2 O ranges from 18-21% and more preferably from 19-21% in the composition. In this range, the amount of B.sub.2 O.sub.3 in the composition can be reduced as further discussed within.
K.sub.2 O is included in lower amounts, generally 0-2%, depending upon the amount of Na.sub.2 O included in the composition. K.sub.2 O at low levels tends to enhance the characteristics associated with Na.sub.2 O. For example, somewhat lower liquidus temperatures can be achieved without substantial quantities of B.sub.2 O.sub.3, if the combined amount of K.sub.2 O and Na.sub.2 O is approximately 20% or higher.
MgO is included in the composition ranges from 0-8% to provide for somewhat lower liquidus temperatures and viscosities at a lower cost. When MgO is included in quantities less than approximately 3.5%, the resulting glass fibers have improved durability with respect to water.
In addition, when MgO is included in a range of about 2-6%, and more preferably 3-5%, the glass compositions can be formulated with lower B.sub.2 O.sub.3 quantities. When formed by the rotary process, the lower viscosity low B.sub.2 O.sub.3 glasses can be extruded through the spinner holes and attenuated without significant reheating of the fibers.
CaO is included in the composition in quantities ranging from 7-14%. The CaO provides for a lower viscosity and improved durability.
B.sub.2 O.sub.3 is included in the composition in quantities ranging from 5.5-15%. The B.sub.2 O.sub.3 primarily serves to significantly lower the liquidus temperature and the viscosity of the composition, but also provides durability in resulting fibers. The glass compositions formed with high concentration of B.sub.2 O.sub.3, e.g. 13%, were found to have very low liquidus temperatures (<1650.degree. F.) and higher viscosities (>1,000 Poise) at the liquidus temperature.
While including high concentrations of B.sub.2 O.sub.3 in the glass compositions tends to increase the cost, high B.sub.2 O.sub.3 glasses can be formed into fibers at quite low temperatures and at high viscosities. These forming conditions can greatly increase the spinner life which can compensate for the increased cost of the glass batch.
Prior art glass compositions conforming to the KI index regulations generally provide for increased levels of B.sub.2 O.sub.3 to compensate in part for the increased levels of alumina. However, a disadvantage of including increased levels of B.sub.2 O.sub.3 are higher costs associated with B.sub.2 O.sub.3. Another disadvantage is that B.sub.2 O.sub.3 is volatile and higher concentrations produce higher emissions that must be controlled, which can further lead to increased costs. For these reasons, it is preferred to limit the B.sub.2 O.sub.3 content to 15%.
In view of the disadvantages associated with the various constituents included in glass compositions, the present invention attempts to balance the composition to provide for more versatile and better performing glass compositions.
The following examples are provided to demonstrate the present invention and not to limit the same.





EXAMPLES
A number of compositions were prepared by methods known in the art to provide examples of compositions of the present invention. For each sample, the liquidus temperature of the composition was determined. Also, the temperature at which the viscosity of the glass is approximately 1000 poise was determined. The viscosity at the liquidus temperature (.eta..sub.TL) is shown for a number of compositions.
In addition, durability testing was performed on a number of samples. The durability test consisted of preparing 10 .mu.m diameter continuous fibers from each composition. A 1 g sample of the fiber was placed in 100 ml of water and maintained at a temperature of 96.degree. F. for 24 hours. Following the water exposure, the sample was removed from the water, dried and weighed. The post-test weight of the sample was compared to the pretest weight to calculate the % weight loss during testing.
______________________________________Constituent.backslash.Sample # 1 2 3______________________________________SiO.sub.2 53.69 53.69 50.72Al.sub.2 O.sub.3 2.0 2.0 3.0B.sub.2 O.sub.3 10.0 8.0 11.9Na.sub.2 O 19.3 19.3 19.3K.sub.2 O 0.7 0.7 0.7MgO 4.35 4.96 3CaO 9.88 11.27 11.3Fe.sub.2 O.sub.3 0.08 0.08 0.08KI Index 40.23 40.23 40.20Liquidus 1618 1707 1664Temperature T.sub.L (.degree. F.)Temp. @ .eta. = 1000 Poise 1632 1643 1600.eta..sub.TL (Poise) 1,170 540% weight loss 4.12 4.11______________________________________Constituent.backslash.Sample # 4 5 6 7______________________________________SiO.sub.2 53.42 53.42 53.42 53.42Al.sub.2 O.sub.3 2.1 2.1 2.1 2.1B.sub.2 O.sub.3 13.1 10.1 8.1 8.1Na.sub.2 O 19.3 19.3 19.3 19.3K.sub.2 O 0.7 0.7 0.7 0.7MgO 3.0 3.0 5.0 3.0CaO 8.3 11.3 11.3 13.3Fe.sub.2 O.sub.3 0.08 0.08 0.08 0.08KI Index 40.2 40.2 40.2 40.2Liquidus 1511 1661 1712 1759Temperature T.sub.L (.degree. F.)Temp. @ .eta. = 1000 Poise 1627 1630 1645 1639.eta..sub.TL (Poise)% weight loss 3.73 3.34 4.05______________________________________Constituent.backslash.Sample # 8 9 10 11______________________________________SiO.sub.2 52.22 52.22 52.22 52.22Al.sub.2 O.sub.3 2.5 2.5 2.5 2.5B.sub.2 O.sub.3 13.9 10.9 8.9 5.9Na.sub.2 O 19.3 19.3 19.3 19.3K.sub.2 O 0.7 0.7 0.7 0.7MgO 3.0 3.0 3.0 8.0CaO 8.3 11.3 13.3 11.3Fe.sub.2 O.sub.3 0.08 0.08 0.08 0.08KI Index 40.2 40.2 40.2 40.2Liquidus 1453 1667 1751 1793Temperature T.sub.L (.degree. F.)Temp. @ .eta. = 1000 Poise 1620 1619 1626 1661.eta..sub.TL (Poise)% weight loss 3.44______________________________________Constituent.backslash.Sample # 12 13 14 15______________________________________SiO.sub.2 53.69 53.69 53.69 53.69Al.sub.2 O.sub.3 2.0 2.0 2.0 2.0B.sub.2 O.sub.3 14.0 13.0 7.5 7.5Na.sub.2 O 19.3 19.3 17.3 21.3K.sub.2 O 0.7 0.7 0.7 0.7MgO 3.13 3.43 5.73 4.51CaO 7.10 7.80 13.0 10.22Fe.sub.2 O.sub.3 0.08 0.08 0.08 0.08KI Index 40.23 40.23 40.23 40.23Liquidus 1411 1456 1791 1777Temperature T.sub.L (.degree. F.)Temp. @ .eta. = 1000 Poise 1624 1624 1671 1616.eta..sub.TL (Poise) 30,200 12,300 300% weight loss 3.65 4.24______________________________________Constituent.backslash.Sample # 16 17 18______________________________________SiO.sub.2 53.42 53.42 52.22Al.sub.2 O.sub.3 2.1 2.1 2.5B.sub.2 O.sub.3 16.1 13.1 13.9Na.sub.2 O 19.3 19.3 19.3K.sub.2 O 0.7 0.7 0.7MgO 0 0 0CaO 8.3 11.3 11.3Fe.sub.2 O.sub.3 0.08 0.08 0.08KI Index 40.2 40.2 40.2Liquidus 1433 1627 1601Temperature T.sub.L (.degree. F.)Temp. @ .eta. = 1000 Poise 1620 1613 1608.eta..sub.TL (Poise)% weight loss 3.73 2.67______________________________________
As can be seen from the examples, compositions of the present invention provide for increased levels of alumina, while remaining within the proposed KI index biosolubility requirements and maintaining acceptable liquidus temperatures (<1800.degree. F.) and viscosities. Theoretically acceptable compositions for rotary process glass fiber production appear to be possible with 2.5% alumina and as little as 5.9% B.sub.2 O.sub.3.
In addition, the present invention provides for decreasing the amount of B.sub.2 O.sub.3 used in glass compositions. Increased levels of alkaline and alkali oxides are used to partly compensate for the decreased amounts of B.sub.2 O.sub.3 used in the present invention; thereby resulting in compositions that meet both the KI index regulations and can be processed by standard rotary methods.
The examples demonstrate that compositions within the present invention can be employed in various quantities to tailor specific properties of the compositions. Examples 1-3 show that compositions ranging from 2-3% Al.sub.2 O.sub.3 and 8-11.9% B.sub.2 O.sub.3 have acceptable liquidus temperatures and viscosities, when the high levels of alkali and alkaline oxides are used, (MgO+CaO)>14 and (K.sub.2 O+Na.sub.2 O).gtoreq.20.
Examples 4-7 show the effect of decreasing the amount of B.sub.2 O.sub.3 and compensating for the decrease by increasing the MgO and/or CaO concentrations. It appears that at lower levels of B.sub.2 O.sub.3, substituting MgO for B.sub.2 O.sub.3 may provide for a lower liquidus temperatures than substituting CaO.
Examples 8-11 show the range of B.sub.2 O.sub.3 concentrations with 2.5% Al.sub.2 O.sub.3 that have properties within the theoretically acceptable range for rotary processing. Examples 12-15 show a similar comparison for 2.0% Al.sub.2 O.sub.3.
Examples 16-18 show that substituting CaO for B.sub.2 O.sub.3 at higher levels of B.sub.2 O.sub.3 results in a composition with 2.0% Al.sub.2 O.sub.3. Example 16 is included as a comparative example to demonstrate the unexpectedly increased durability, in addition to an acceptable liquidus temperature and viscosity of the composition of Example 17. The sample composition of Example 18 containing 2.5% Al.sub.2 O.sub.3 also has an acceptable liquidus temperature and viscosity.
Generally, the compositions having the highest concentration of B.sub.2 O.sub.3 have the lowest liquidus temperatures (Examples 8, 12, 13, and 16). However, the higher B.sub.2 O.sub.3 concentrations used in the present invention are generally less than the B.sub.2 O.sub.3 concentrations used in the prior art.
Unexpectedly, higher durabilities were achieved for compositions in which MgO and/or CaO were substituted for B.sub.2 O.sub.3 (Examples 17 and 5, as compared with Examples 16 and 4, respectively). In addition, the highest durability was achieved in the composition of Example 17, which contained only 2.1% of Al.sub.2 O.sub.3 and had an increased CaO content and correspondingly decreased B.sub.2 O.sub.3 content compared to Example 16.
Those of ordinary skill in the art will appreciate that a number of modifications and variations that can be made to specific compositions of the present invention without departing from the scope of the present invention. Such modifications and variations are intended to be covered by the foregoing specification and the following claims.
Claims
  • 1. A glass fiber composition comprising the following ingredients in weight percent:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 5.5-15;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8;
  • CaO 7-14; and
  • CaO+MgO>14
  • wherein said composition has a liquidus temperature <1800.degree. F., has a viscosity at said liquidus temperature >300 Poise, exhibits a viscosity of 1000 Poise at a temperature of .ltoreq.1671.degree. F. and satisfies the equation:
  • (B.sub.2 O.sub.3 +Na.sub.2 O+K.sub.2 O+MgO+CaO)-2*Al.sub.2 O.sub.3 .gtoreq.40
  • 2. The composition of claim 1, wherein the B.sub.2 O.sub.3 content ranges from 6-15.
  • 3. The composition of claim 1, wherein said ingredients include:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 6-12;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8; and,
  • CaO 8-14.
  • 4. The composition of claim 3, wherein said ingredients include:
  • SiO.sub.2 50-53.5;
  • Al.sub.2 O.sub.3 2.1-2.9;
  • B.sub.2 O.sub.3 7-12;
  • Na.sub.2 O 18-21;
  • K.sub.2 O 0-1.5;
  • MgO greater than 0-6.0; and,
  • CaO 9-14.
  • 5. The composition of claim 4, wherein said ingredients include:
  • SiO.sub.2 51-53.5;
  • Al.sub.2 O.sub.3 2.1-2.6;
  • B.sub.2 O.sub.3 7-11;
  • Na.sub.2 O 19-21;
  • K.sub.2 O 0-1.5;
  • MgO greater than 0-6; and
  • CaO 9-14.
  • 6. The composition of claim 3, wherein said ingredients include:
  • SiO.sub.2 50-53.5;
  • Al.sub.2 O.sub.3 2.1-2.9;
  • B.sub.2 O.sub.3 7-12;
  • Na.sub.2 O 18-21;
  • K.sub.2 O 0-1.5;
  • MgO 2-6; and,
  • CaO 9-13.
  • 7. The composition of claim 6, wherein said ingredients include:
  • SiO.sub.2 51-53.5;
  • Al.sub.2 O.sub.3 2.1-2.6;
  • B.sub.2 O.sub.3 7-11;
  • Na.sub.2 O 19-21;
  • K.sub.2 O 0-1.5;
  • MgO 3-6; and
  • CaO 9-12.
  • 8. The composition of claim 7, wherein said B.sub.2 O.sub.3 ranges from 7-<10 weight % of the composition.
  • 9. The composition of claim 7, wherein the quantity (Na.sub.2 O+K.sub.2 O)>19.0 weight % of the composition.
  • 10. The composition of claim 1, wherein said ingredients include:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 10-15;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8; and
  • CaO 7-14,
  • wherein said composition has a liquidus temperature <1650.degree. F. and a viscosity at said liquidus temperature >1000 Poise.
  • 11. The composition of claim 10, wherein said ingredients include:
  • SiO.sub.2 50-53.5;
  • Al.sub.2 O.sub.3 2.1-2.9;
  • B.sub.2 O.sub.3 11-14;
  • Na.sub.2 O 18-21;
  • K.sub.2 O 0-1.5;
  • MgO 2-8; and,
  • CaO 7-14.
  • 12. The composition of claim 11, wherein said ingredients include:
  • SiO.sub.2 51-53.5;
  • Al.sub.2 O.sub.3 2.1-2.6;
  • B.sub.2 O.sub.3 11-13.5;
  • Na.sub.2 O 19-21;
  • K.sub.2 O 0-1.5;
  • MgO 3-8; and
  • CaO 7-12.
  • 13. The composition of claim 10, wherein said ingredients include:
  • SiO.sub.2 50-53.5;
  • Al.sub.2 O.sub.3 2.1-2.9;
  • B.sub.2 O.sub.3 11-14;
  • Na.sub.2 O 18-21;
  • K.sub.2 O 0-1.5;
  • MgO greater than 0-8; and
  • CaO 7-14.
  • 14. The composition of claim 13, wherein said ingredients include:
  • SiO.sub.2 51-53.5;
  • Al.sub.2 O.sub.3 2.1-2.6;
  • B.sub.2 O.sub.3 11.0-13.5;
  • Na.sub.2 O 19-21;
  • K.sub.2 O 0-1.5;
  • MgO greater than 0-8; and
  • CaO 7-14.
  • 15. A glass fiber composition comprising in weight percent:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 6-15;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8;
  • CaO 7-14; and
  • CaO+MgO>14
  • wherein said composition has a liquidus temperature <1800.degree. F., a has viscosity at said liquidus temperature >300 Poise, exhibits a viscosity of 1000 Poise at a temperature of .ltoreq.1671.degree. F. and satisfies the equation:
  • (B.sub.2 O.sub.3 +Na.sub.2 O+K.sub.2 O+MgO+CaO)-2*Al.sub.2 O.sub.3 .gtoreq.40
  • 16. The composition of claim 15, wherein said composition includes:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 6-12;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8; and,
  • CaO 8-14.
  • 17. The composition of claim 15, wherein said ingredients include:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 10-15;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8; and
  • CaO 7-14,
  • wherein said composition has a liquidus temperature <1650.degree. F. and a viscosity at said liquidus temperature >1000 Poise.
  • 18. A method of preparing a glass fiber comprising:
  • providing a composition comprising, in weight percent:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 6-15;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8;
  • CaO 7-14; and
  • CaO+MgO>14
  • wherein said composition has a liquidus temperature <1800.degree. F., a viscosity at said liquidus temperature >300 Poise, exhibits a viscosity of 1000 Poise at a temperature of .ltoreq.1671.degree. F. and satisfies the equation:
  • (B.sub.2 O.sub.3 +Na.sub.2 O+K.sub.2 O+MgO+CaO)-2*Al.sub.2 O.sub.3 .gtoreq.40;
  • heating the composition to at least its liquidus temperature to produce a molten composition; and,
  • forming the glass fiber from the molten composition.
  • 19. The method of claim 18, wherein said forming includes forming the glass fiber by a rotary process.
  • 20. The method of claim 18, wherein said providing includes providing a composition comprising in weight percent:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 6-12;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8; and,
  • CaO 8-14.
  • 21. The method of claim 18, wherein said providing includes providing a composition comprising in weight percent:
  • SiO.sub.2 49-54;
  • Al.sub.2 O.sub.3 2-3;
  • B.sub.2 O.sub.3 10-15;
  • Na.sub.2 O 16-22;
  • K.sub.2 O 0-2;
  • MgO greater than 0-8; and
  • CaO 7-14,
  • wherein the composition has a liquidus temperature <1650.degree. F. and a viscosity at the liquidus temperature >1000 Poise.
US Referenced Citations (81)
Number Name Date Kind
RE29388 Atkinson Sep 1977
RE35557 Thelohan et al. Jul 1997
1913242 McClure Jun 1933
2192939 Slayter et al. Mar 1940
2308857 Bowes Jan 1943
2426472 Stanworth Aug 1947
2877124 Welsch Mar 1959
2882173 Welsch Apr 1959
3008841 Tiede Nov 1961
3013888 de Lajarte Dec 1961
3060041 Loewenstein Oct 1962
3151966 Slayter Oct 1964
3328142 Levecque Jun 1967
3513002 Labino May 1970
3736162 Chvalovsky et al. May 1973
3753674 Ohlberg et al. Aug 1973
3764283 Hagedorn Oct 1973
3817764 Wolf Jun 1974
3853569 Laurent et al. Dec 1974
3922155 Broemer et al. Nov 1975
3981736 Broemer et al. Sep 1976
4090882 Rauschenfels May 1978
4106946 Ritze Aug 1978
4120730 Trojer et al. Oct 1978
4131597 Bluethgen et al. Dec 1978
4142907 Manring et al. Mar 1979
4159358 Hench et al. Jun 1979
4171544 Hench et al. Oct 1979
4177077 Gagin Dec 1979
4179300 Sagara Dec 1979
4189325 Barrett et al. Feb 1980
4234972 Hench et al. Nov 1980
4239113 Gross et al. Dec 1980
4243421 Kume Jan 1981
4264131 Sawamura et al. Apr 1981
4277286 Boyd et al. Jul 1981
4312952 Carbol Jan 1982
4325724 Froberg Apr 1982
4381347 Carbol Apr 1983
4437192 Fujiu et al. Mar 1984
4451276 Barthe et al. May 1984
4454238 Hobson et al. Jun 1984
4497629 Ogino et al. Feb 1985
4552850 Partington et al. Nov 1985
4562161 Mennemann et al. Dec 1985
4604097 Graves, Jr. et al. Aug 1986
4605415 Richez Aug 1986
4608350 Howard, Jr. Aug 1986
4615988 Le Moigne et al. Oct 1986
4652534 Kasuga Mar 1987
4652535 Mackenzie et al. Mar 1987
4655777 Dunn et al. Apr 1987
4756732 Barthe et al. Jul 1988
4759785 Barthe et al. Jul 1988
4759974 Barthe et al. Jul 1988
4768859 Kasori et al. Sep 1988
4775646 Hench et al. Oct 1988
4830989 Trivedi et al. May 1989
4851046 Low et al. Jul 1989
4867779 Meunier et al. Sep 1989
5013323 Kobayashi et al. May 1991
5037470 Matzen et al. Aug 1991
5055428 Porter Oct 1991
5108957 Cohen et al. Apr 1992
5108975 Schubert et al. Apr 1992
5120340 Ducheyne et al. Jun 1992
5121748 Ditz et al. Jun 1992
5206100 Muto et al. Apr 1993
5215563 LaCourse et al. Jun 1993
5250488 Thelohan et al. Oct 1993
5296026 Monroe et al. Mar 1994
5312806 Mogensen May 1994
5332698 Nyssen et al. Jul 1994
5332699 Olds et al. Jul 1994
5346864 Maugendre et al. Sep 1994
5401693 Bauer et al. Mar 1995
5420082 Maugendre et al. May 1995
5429996 Kaneko Jul 1995
5523264 Mattson Jun 1996
5523265 Rapp et al. Jun 1996
5622903 Rapp et al. Apr 1997
Foreign Referenced Citations (68)
Number Date Country
0 135 449 Mar 1980 EPX
0 009 418 Apr 1980 EPX
0 019 600 Nov 1980 EPX
0 206 726 Dec 1986 EPX
0 247 817 Dec 1987 EPX
0 319 578 Jun 1989 EPX
0 399 320 A1 Nov 1990 EPX
0 412 878 Feb 1991 EPX
0 588 251 A1 Mar 1994 EPX
0 586 797 A1 Mar 1994 EPX
0 591 696 A1 Apr 1994 EPX
0 459 897 B1 Apr 1995 EPX
0 739 862 A2 Oct 1996 EPX
1.149.289 Dec 1957 FRX
2 393 020 Jun 1978 FRX
2 521 547 Feb 1983 FRX
2 548 658 Jul 1984 FRX
2 658 182 Feb 1990 FRX
2 690 438 Apr 1992 FRX
39 17 045 A1 Nov 1990 DEX
44 06 923 A1 Aug 1995 DEX
72-117753 Nov 1972 JPX
73-101799 Sep 1973 JPX
73-130550 Nov 1973 JPX
54-148808 Nov 1979 JPX
60-155551 Aug 1985 JPX
63-14989 Apr 1988 JPX
5-77623 Mar 1993 JPX
6-116114 Apr 1994 JPX
80-2913604 Feb 1980 SUX
86-4071881 May 1986 SUX
1351896 Nov 1987 SUX
1 726 411 A1 Sep 1989 SUX
811243 Nov 1956 GBX
1096465 Dec 1964 GBX
2 041 910 Sep 1980 GBX
2 080 281 Feb 1982 GBX
2 178 422 Feb 1987 GBX
2 220 654 Jan 1990 GBX
2 279 942 Jan 1995 GBX
WO 8604807 Aug 1986 WOX
WO 8705007 Aug 1987 WOX
WO 8912032 Dec 1989 WOX
WO 9002713 Mar 1990 WOX
WO 9111403 Aug 1991 WOX
WO 9205121 Apr 1992 WOX
WO 9209536 Jun 1992 WOX
WO 9307741 Apr 1993 WOX
WO 9315028 Aug 1993 WOX
WO 9322251 Nov 1993 WOX
WO 9414718 Jul 1994 WOX
WO 9415883 Jul 1994 WOX
WO 9414717 Jul 1994 WOX
WO 9418134 Aug 1994 WOX
WO 9501941 Jan 1995 WOX
WO 9512554 May 1995 WOX
WO 9521799 Aug 1995 WOX
WO 9529135 Nov 1995 WOX
WO 9534514 Dec 1995 WOX
WO 9535265 Dec 1995 WOX
WO 9532927 Dec 1995 WOX
WO 9532926 Dec 1995 WOX
WO 9600196 Jan 1996 WOX
WO 9601793 Jan 1996 WOX
WO 9604213 Feb 1996 WOX
WO 9630313 Oct 1996 WOX
WO 9634836 Nov 1996 WOX
WO 9749643 Dec 1997 WOX
Non-Patent Literature Citations (24)
Entry
Nomenclature Committee of TIMA, Inc., "Nonmenclature of Man-Made Vitreous Fibers,"Apr. 15, 1991, pp. 1-72.
Stephanie M. Mattson, "Glass Fiber Dissolution in Simulated Lung Fluid and Measures Needed to Improve Consistency and Correspondence to In Vivo Dissolution," vol. 102, Supplement 5, Oct. 1994, pp. 87-90.
Stephanie M. Mattson, "Glass Fibres in Simulated Lung Fluid: Dissolution Behavior and Analytical Requirements," Ann. Occup. Hyg., vol. 38, No. 6, 1994, pp. 857-877 (No Month).
"Biological Effects of Man-Made Mineral Fibres," vol. 2, Sessions VI-IX and annexes, Apr. 20-22, 1982, pp. 26-99 and Figs. 3-4.
Chemical Abstracts, vol. 84, 1976. p. 306 (No month).
Dr. h.c. Werner Lehnhauser, "Glasuren und ihre Farben," 1973 Wilheim Knapp Verlag, pp. 50-51, 14-15, 56-57, 70-71, and 10-11 (No Month).
N.K. Mitra, M. Mukherjee and M. Samanta, "Effect of Minor Substitution of SiO2 in the Na20-Si02 Glass on the Leaching Characteristics in Aqueous Medium," vol. 13, No. 4, Jul. 1968, pp. 98-102
"Scientific Basis for Nuclear Waste Management VII," Materials Research Society Symposia Proceedings, Nov. 1983, vol. 26, pp. 755-761.
Hironori Ohta and Yoshiro Suzuki, "Chemical Durability of Glasses in the Systems SiO.sub.2 -CaO-Na.sub.2 O-Na.sub.2 O-R.sub.m O.sub.n, " Ceramic Bulletin, vol. 57, No. 6, 1978, pp. 602-604 (No Month).
V.R. Christensen, S. Lund Jensen, M. Guldberg, and O. Kamstrup, "Effect of Chemical Composition of Man-Made Vitreous Fibers on the Rate of Dissolution In Vitro at Different pHs," vol. 102, Supplement 5, Oct. 1994, pp. 83-86.
Orjan H. Andersson, Kaj H. Karlsson, Kan Kangasniemi, Anti Yli-Urpo, "Models for Physical Properties and Bioactivity of Phosphate Opal Glasses," Glastech, Ber. 61 (1988) Nr. 10, pp. 300-304 (No Month).
G.A. Cox, B.A. Ford, "The Corrosion of Glass on the Sea Bed," Journal of Materials Science 24 (1989) pp. 3146-3153 (No Month).
F. Pott, et al., "Nato Advanced Research Workshop on Mechanisms in Fibre Carcinogenesis", Albuquerque, NM, Oct. 22-25, 1990, pp. 1-6.
B. Bellmann, et al., "Study on the Durability of Chemically Different Glass Fibres in Lungs of Rats", Zbl. Hyg. 190, (1990), pp. 310-314 (No Month).
F. Pott, et al., "Carcinogenicity of Glass Fibres with Different Durability", Zbl. Hyg., 189, (1990), pp. 563-566 (No Month).
R. Potter and Stephanie M. Mattson, "Glass Fiber Dissolution in a Physiological Saline Solution", Glastechnische Berichte 64(1991) Jan., No. 1, Frankfurt, DE, pp. 16-28.
Draft "TRGS 906", "Justification for the Classification of Types of Inorganic Fibre Dust (Excluding Asbestos)," pp. 1-28 Date (Unknown).
"Inorganic Fibers", C.Z. Carroll-Potczynski, 1958, p. 125, U.S. Bureau of Mines (No Month).
"Erfahrungsaustausch", Martin Hubacher, Siikattechn, 20, 1960, No. 2, pp. 88-90 (No Month).
Jon F. Bauer, "Solubility and Durability of Manmade Mineral Fibers in Physiological Fluids", Presented at TAPPI Non-wovens Conference, Nashville, Ohio, 1988. pp. 1-8 (No Month).
Z. M. Syritakaya et al., "Glasses Free from Alkali and Borates for Machine Working", Institute of Glass, p. 289 (Date Unknown).
Thomas D. Callinan and Robert T. Lucas, "Some Special Fiber Glass Compositions," Research Disges, Oct. 1954.
C.R. Das and R.W. Douglas, "Studies on the Reaction Between Water and Glass. Part 3," Physics and Chemistry of Glasses, vol. 8, No. 5, Oct. 1967, pp. 178-184.
C.M. Jantzen and M.J. Plodinec, "Thermodynamic Model of Natural, Medieval and Nuclear Waste Durability," Journal of Non-Crystalline Solids 67, 1984, pp. 207-223 (No Month).