Striae-Free Chalcogenide Glasses
20170267574 ยท 2017-09-21
Assignee
Inventors
- Vinh Q. Nguyen (Fairfax, VA, US)
- Mikhail Kotov (Silver Spring, MD, US)
- Daniel J. Gibson (Falls Church, VA, US)
- Shyam S. Bayya (Ashburn, VA, US)
- Jasbinder S. Sanghera (Ashburn, VA, US)
Cpc classification
C03B5/16
CHEMISTRY; METALLURGY
C03B2201/86
CHEMISTRY; METALLURGY
International classification
C03C3/32
CHEMISTRY; METALLURGY
Abstract
A striae-free chalcogenide glass with uniform refractive index.
Claims
1. A product of the process comprising the steps of: melting chalcogenide glass inside a sealed silica ampoule; providing a 2-zone furnace comprising an upper zone and a lower zone wherein the upper zone is at a higher temperature than the lower zone and wherein the zones are independently controllable temperature zones; mixing by rocking the sealed silica ampoule inside the 2-zone furnace; placing the sealed silica ampoule in a vertical position; forming a glass melt as the upper zone is at a higher temperature than the lower zone; positioning the glass melt such that the glass melt is within the lower zone; and cooling slowly and quenching the temperature; reducing the temperature of the upper zone at a rate of 0.6 C./min to 370 C.; reducing the temperatures of the lower zone at a rate of 0.6 C./min to 260 C.; holding these temperatures for 12 hours; and thereby forming the striae-free chalcogenide glass.
2. The product of the process of claim 1 further comprising the step of preventing convection currents within the glass melt as the glass melt solidifies forming the chalcogenide glass.
3. The product of the process of claim 2 further comprising the step of preventing condensation of glass on the ampoule as the glass melt cools.
4. The product of the process of claim 1 further comprising the steps of: allowing for an initial melting of the chalcogenide glass prior to the step of mixing by rocking; and allowing for homogenization of the chalcogenide glass.
5. The product of the process of claim 4 further comprising the step of avoiding abrasion of the ampoule during the rocking step.
6. The product of the process of claim 1 further comprising the steps of: maintaining the temperature of the lower zone at a temperature of about 700 C. for about 24 hours; and maintaining the temperature of the upper zone at a temperature of about 100 C. greater than the temperature of the lower zone for about 24 hours.
7. A product of the process comprising the steps of: loading arsenic and sulfur precursors sufficient to constitute a 120 gram batch of glass with the composition of 39% at. arsenic (As) and 61% at. sulphur (S) or about 71.88 grams As and 48.12 grams S into a silica ampoule under an inert gas atmosphere; connecting the ampoule to a vacuum pump; evacuating the ampoule for 4 hours at 110.sup.5 Torr; sealing the ampoule; placing the ampoule inside a rocking furnace with a 45 angle of inclination wherein the furnace has a top zone and a bottom zone and wherein the zones are independently controllable temperature zones; heating and rocking the ampoule; heating the top zone and the bottom zone of the furnace at a rate of 3 C./min from room temperature; heating the top zone to 850 C.; heating the bottom zone to 750 C.; holding constant the temperature of the top zone (850 C.) and bottom zone (750 C.) for 10 hours; rocking the furnace at an inclination angle of 45 to facilitate mixing and homogenization of the elemental components; stopping the furnace motion; setting the furnace to a vertical position or 90 fixed angle; decreasing the temperature of the top zone at a rate of 1 C./min to 800 C.; decreasing the temperature of the bottom zone at a rate of 1 C./min to 700 C.; holding the furnace position and temperature profile for 24 hours to facilitate fining and settling of the glass melt; reducing the temperature of the top zone at a rate of 0.6 C./min to 370 C.; reducing the temperatures of the bottom zone at a rate of 0.6 C./min to 260 C.; holding these temperatures for 12 hours; forming a chalcogenide glass; removing the ampoule from the furnace; submerging the ampoule in a room temperature water bath for 10 seconds to quench the chalcogenide glass; annealing the chalcogenide glass by placing the ampoule in another furnace at 180 C. for 10 hours; and forming a striae-free chalcogenide glass.
8. A chalcogenide glass comprising a striae-free and high optical quality chalcogenide glass that is uniform and homogeneous.
9. The chalcogenide glass of claim 8 wherein the striae-free chalcogenide glass has no refractive index perturbations.
10. The product of the method to synthesize striae-free chalcogenide glass using melt processing comprising melting chalcogenide glass inside a sealed silica ampoule, providing a 2-zone furnace comprising an upper zone and a lower zone wherein the upper zone is at a higher temperature than the lower zone, mixing by rocking the sealed silica ampoule inside the 2-zone furnace, placing the sealed silica ampoule in a vertical position, forming a boule as the upper zone is at a higher temperature than the lower zone, positioning the boule such that the chalcogenide glass is within the lower zone, and cooling slowly and quenching the temperature and thereby forming the striae-free chalcogenide glass.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0022]
[0023]
[0024]
[0025]
[0026]
[0027]
[0028]
[0029]
[0030]
[0031]
DETAILED DESCRIPTION
[0032] Described herein is a new method to synthesize striae-free chalcogenide glass using melt processing.
[0033] One embodiment is described in the example using As.sub.39S.sub.61 glass.
Example 1
Process of the Present Invention to Make Striae-Free Arsenic Sulfide Glasses
[0034] Arsenic and sulfur precursors sufficient to constitute a 120 gram batch of glass with the composition of 39% at. As and 61% at. S (71.88 grams and 48.12 grams respectively) were loaded in a silica ampoule under an inert gas atmosphere.
[0035] The ampoule was connected to a vacuum pump and evacuated for 4 hours at 110.sup.5 Torr.
[0036] The ampoule was sealed using a methane/oxygen torch and placed inside a rocking furnace with a 45 angle of inclination and two independently controllable temperature zones (shown in
[0037] In Step 1, the top and bottom zones of the furnace were heated at a rate of 3 C./min from 20 C. (room temperature) to 850 C. (top) and 750 C. (bottom).
[0038] In Step 2, the temperature of the top zone (850 C.) and bottom zone (750 C.) were held constant for 10 hours while the furnace was rocked at an inclination angle of 45 to facilitate mixing and homogenization of the elemental components.
[0039] In Step 3, the furnace motion was stopped and the furnace was set to a vertical position (90 fixed angle). At the same time, the temperatures of the top zone and bottom zone were decreased at a rate of 1 C./min to 800 C. (top) and 700 C. (bottom). This furnace position and temperature profile were held for 24 hours to facilitate fining and settling of the glass melt.
[0040] In Step 4, the temperatures of the top zone and the bottom zone were reduced at a rate of 0.6 C./min to 370 C. (top) and 260 C. (bottom). These temperatures were held for 12 hours.
[0041] In Step 5, the hot ampoule was removed from the furnace, submerged in a room temperature water bath for 10 seconds to quench the glass, and was placed in another furnace at 180 C. for 10 hours to anneal the solid glass.
TABLE-US-00002 TABLE 2 Glass melting schedule for As.sub.39S.sub.61 glass composition in a two-zone furnace using the present invention. Temper- Temperature Heating ature ( C.) Rate ( C.) Bottom Dwell Step ( C./min) Top Zone Zone (Hours) Furnace Position 1 3 850 750 1 Horizontal 0 fixed 2 850 750 10 Rocking at 45 inclination 3 1 800 700 24 Vertical 90 fixed 4 0.6 360 260 12 Vertical 90 fixed 5 Water quench
[0042] Step 1 of the present invention allows for an initial melting of precursor materials prior to rocking for homogenization and reduces the potential of abrasion of the ampoule by solid precursors during the next step, which is not a part of the prior art process.
[0043] Step 2 here allows for a temperature gradient in the ampoule to encourage mixing and homogenization during rocking.
[0044] In Step 3 of the process of the present invention, the ampoule containing the glass melt is positioned such that the glass melt is largely confined within the bottom zone of the furnace and it is being fined at high temperature (700 C.) for a longer time than in the prior art method (24 hours in this example compared to 1 hour in the prior art method) which encourages homogenization.
[0045] The temperature of the top zone in this step is set to a higher temperature (800 C.) than the bottom zone, which has two benefits: 1) convection currents within the glass melt are reduced and 2) condensation and mass fluxing within the glass melt are prevented.
[0046] This temperature gradient eliminates the main causes of striae and therefore reduces compositional variations in the molten glass compared with the prior art.
[0047] In Step 4, the temperatures of the top zone and bottom zones are decreased slowly (0.6 C./min compared to 5 C./min in Step 3 of the prior art method) while keeping the top zone (360 C.) 100 C. hotter than the bottom zone (260 C.). Note that this differs from Step 3 of the prior art method, which allows for a natural temperature gradient within the furnace permitting the bottom of the glass to be hotter than the top as shown in
[0048] This slow ramp rate and a consistent 100 C. higher temperature in the top zone prevent thermal convection within the glass in this stage which allows the uniform conditions in the molten glass to remain as the glass cools and prevents the reincorporation of surface glass into the bulk glass during this step.
[0049]
[0050] During water quenching of Step 5, the viscosity of the glass increases rapidly as the glass melt cools but thermal stresses are less compared to the method of the prior art due to the slow cool rate and long dwell in Step 4 and the shorter quench time in the method of the present invention.
[0051]
[0052] The process of the present invention produces striae-free and high optical quality chalcogenide glasses. The uniform and homogeneous glasses are free from refractive index perturbations.
[0053] The process of the present invention has several advantages over the conventional process of the prior art. For example, thermal convection heat loss, convection current and mass flux are eliminated within the bulk molten glass by setting the temperature of the top zone at least 100 C. (or thereabouts) higher than the bottom zone through all steps of the process.
[0054] Another advantage is the controlled slow cooling enables thermal equilibrium and steady state to occur in the molten glass melt throughout the process. This contributes to a striae-free, lower energy, and stable state of the glass melt just before quenching.
[0055] Still another advantage is striae-free and uniform compositions in the bulk glass eliminate refractive index perturbations enabling glass with higher optical quality for high-performance IR fibers and refractive optical elements.
[0056] This invention has been demonstrated using As.sub.39S.sub.61 glass in the above example but can also be applied to other chalcogenide glasses such as, but not limited to, AsS-based glasses with different compositions, AsSe, GeAsSe and GeAsSeTe-based glasses and other multi-component chalcogenide and chalcohalide glasses. The present invention could also be applied to the fabrication of other glasses, for example silicates, borates, fluorides, phosphates and others, or processing of viscous liquids, for example polymer melts, metals, salts and other liquids, where homogeneity is desired.
[0057] Many modifications and variations of the present invention are possible in light of the above teachings. It is therefore to be understood that the claimed invention may be practiced otherwise than as specifically described. Any reference to claim elements in the singular, e.g., using the articles a, an, the, or said is not construed as limiting the element to the singular.