EP2680960A2 - Ultrasonic transducer assembly for applying ultrasonic acoustic energy to a glass melt - Google Patents

Ultrasonic transducer assembly for applying ultrasonic acoustic energy to a glass melt

Info

Publication number
EP2680960A2
EP2680960A2 EP12716107.3A EP12716107A EP2680960A2 EP 2680960 A2 EP2680960 A2 EP 2680960A2 EP 12716107 A EP12716107 A EP 12716107A EP 2680960 A2 EP2680960 A2 EP 2680960A2
Authority
EP
European Patent Office
Prior art keywords
ultrasonic
glass melt
probe
temperature
booster
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
EP12716107.3A
Other languages
German (de)
French (fr)
Inventor
Daniel Robert Boughton
Scott Michael Jarvis
Jonghak Kim
Zhiqiang Shi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Corning Inc
Original Assignee
Corning Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US13/036,568 external-priority patent/US9061928B2/en
Priority claimed from US13/036,668 external-priority patent/US8490433B2/en
Application filed by Corning Inc filed Critical Corning Inc
Publication of EP2680960A2 publication Critical patent/EP2680960A2/en
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/18Stirring devices; Homogenisation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F31/00Mixers with shaking, oscillating, or vibrating mechanisms
    • B01F31/80Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations
    • B01F31/85Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations with a vibrating element inside the receptacle
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/225Refining

Definitions

  • the present disclosure relates to glass manufacturing processes and systems including, but not limited to, glass mixing, homogenization, fining, or any process or system where the introduction of mechanical energy to the glass melt might be advantageous.
  • a method of applying ultrasonic acoustic energy to a glass melt by monitoring a glass melt temperature T Y and transferring ultrasonic acoustic energy from an ultrasonic transducer to the glass melt at a controller power P c and a controller frequency v c through an ultrasonic probe positioned in the glass melt is provided.
  • the controller power P c is controlled in response to at least (i) the monitored glass melt temperature T Y and (ii) a reference glass melt temperature T R .
  • the controller frequency v c is controlled in response to at least (i) one or more input parameters from a temperature-viscosity curve characterizing the glass melt, (ii) one or more input parameters from one or more temperature dependent impedance response models of the glass melt, and (iii) ⁇ , where ⁇ represents a degree to which an impedance condition Z Y of the ultrasonic probe differs from a reference impedance Z R when the ultrasonic probe is positioned in the glass melt.
  • Systems for applying ultrasonic acoustic energy to glass melts are also contemplated.
  • an ultrasonic transducer assembly comprising an ultrasonic transducer, an ultrasonic booster, an ultrasonic probe, and a booster cooling unit.
  • the ultrasonic booster is connected to the ultrasonic transducer to amplify acoustic energy generated by the ultrasonic transducer and transfer the amplified acoustic energy to the ultrasonic probe.
  • a seated end of the ultrasonic probe is positioned in a probe seat of the ultrasonic booster.
  • the booster cooling unit is positioned to regulate the temperature of the probe seat of the ultrasonic booster such that the assembly supports a temperature dependent press-fit engagement of the seated end of the ultrasonic probe and the probe seat of the ultrasonic booster.
  • the temperature dependent press-fit engagement is such that the seated end of the ultrasonic probe can be reversibly moved in and out of the probe seat at an elevated temperature THOT and is fixed in the probe seat at room temperature T C OLD-
  • ultrasonic processes and systems disclosed herein will help address the potential source of contamination introduced by known mechanical stirrers.
  • the use of ultrasonic energy may be advantageous in glass fining operations because ultrasonic energy can encourage the coalescence of bubbles, allowing for Stokes fining, and can encourage acoustic streaming, where gas bubbles move toward the glass air interface.
  • the ultrasonic processes and systems disclosed herein will enjoy applicability to a wide variety of additional manufacturing, diagnostic, and developmental processes utilizing glass melts.
  • the methodology of the present disclosure has applicability to a variety of glass compositions, we have recognized that the need for effective glass mixing and fining processes is particularly acute in the context of specialty glasses, such as
  • photovoltaic glasses LCD glasses, consumer electronics glasses, high purity fused silica glasses, and specialty glasses manufactured and sold under the Corning Incorporated trade names Eagle XG® glass and Gorilla® glass.
  • FIG. 2 is a schematic illustration of a method as disclosed herein for controlling ultrasonic frequency when applying ultrasonic acoustic energy to a glass melt;
  • FIG. 3 is a schematic illustration of a method as disclosed herein for controlling acoustic power when applying ultrasonic acoustic energy to a glass melt;
  • Fig. 4 illustrates modeled temperature dependent impedance responses of a glass melt
  • Fig. 5 illustrates an ultrasonic probe assembly including one or more features of the present disclosure
  • FIG. 6 is a cross sectional illustration of a booster cooling unit according to the present disclosure.
  • Fig. 7 is a partially exploded view of a portion of the ultrasonic probe assembly illustrated in Fig. 5;
  • Fig. 8 illustrates an alternative ultrasonic probe assembly including one or more features of the present disclosure.
  • Fig. 1 is a schematic illustration of a system for applying ultrasonic acoustic energy to a glass melt 10.
  • the system comprises an ultrasonic power supply 20, an ultrasonic transducer 30, and an ultrasonic probe 40.
  • the ultrasonic power supply is programmed to monitor a glass melt temperature T Y with the aid of one or more temperature sensors 50 and to transfer ultrasonic acoustic energy from the ultrasonic transducer 30, through the ultrasonic probe 40, to the glass melt 10 at a controller power P c and a controller frequency v c .
  • the following description addresses the manner in which the controller power P c and controller frequency v c are controlled.
  • the following description also introduces examples of ultrasonic probe assemblies that can be employed in the system and methodology disclosed herein. It is noted that the power and frequency control schemes contemplated herein are not limited to use with any specific types of hardware.
  • Pc is controlled in response to at least (i) the monitored glass melt temperature T Y and (ii) a reference glass melt temperature T R .
  • Fig. 3 which is discussed in further detail below, can be read in conjunction with Fig. 1 to illustrate various aspects of power control contemplated herein. It is noted that reference herein to a parameter being "controlled” is intended to cover a variety of parameter control conditions including, but not limited to, conditions where a parameter is established,
  • reference to a parameter being controlled "in response to" particular data is intended to cover a variety of uses of the data including, but not limited to instances where the parameter is a direct or indirect function of the data or, more broadly, where the parameter is somehow influenced by the data.
  • Fig. 1 can be read in conjunction with Fig. 2 to illustrate various aspects of frequency control contemplated herein. More specifically, the controller frequency v c is controlled in response to at least (i) one or more input parameters from a temperature-viscosity curve T, G characterizing the glass melt 10, (ii) one or more input parameters from one or more temperature dependent impedance response models of the glass melt 10, and (iii) ⁇ , where ⁇ represents a degree to which an impedance condition Z Y of the ultrasonic probe 40 differs from a reference
  • the input parameters from the impedance response models of the glass melt represent a selected resonance of the ultrasonic probe in the glass melt and are used for relatively coarse control of the controller frequency v c .
  • Fig. 4 illustrates a set of temperature dependent impedance response models for an ultrasonic probe at room temperature Ti and successively higher temperatures T 2 , T 3 , T in a glass melt.
  • these types of impedance response models can be used to identify resonance troughs that are relatively highly damped as temperature increases (see trough A) and resonance troughs that are relatively minimally damped as temperature increases (see trough B).
  • the temperature dependent impedance response models can be used to generate input parameters for the controller frequency Vc that identify the frequency characteristics of the relatively minimally damped resonance trough.
  • the modeled impedance responses illustrate primary A and secondary B low-impedance resonance troughs for the ultrasonic probe in the glass melt. Because the secondary troughs exhibit minimal temperature-dependent damping, the input parameters used for the controller frequency Vc will identify the frequency characteristics of the secondary low-impedance resonance trough B.
  • the input parameters can identify a frequency range because they can be used for coarse control but it is contemplated that the input parameters may comprise a single ultrasonic frequency value, multiple ultrasonic frequency values, an ultrasonic frequency range, or combinations thereof.
  • represents a degree to which the impedance condition Z Y of the ultrasonic probe 40 differs from the reference impedance Z R when the ultrasonic probe 40 is positioned in the glass melt 10.
  • can also be taken as a representation of the power factor of the ultrasonic probe 40 in the glass melt 10 because the transducer impedance represents the phase difference between the control voltage and current of the ultrasonic probe.
  • the impedance condition Z Y of the ultrasonic probe 40 is determined from measurements of electrical current I flowing through the transducer assembly and a voltage drop V across the transducer assembly.
  • can be a direct comparison of the impedance condition Z Y of the ultrasonic probe and the reference impedance Z R when the ultrasonic probe is positioned in the glass melt.
  • the reference impedance Z R is selected for as sharp a resonance as possible and will typically correspond to a particular frequency range, which depends on the temperature and glass viscosity. Typical frequency ranges will fall between approximately 15kHz and approximately 30kHz.
  • the control objective associated with controlling the frequency Vc is the delivery of maximum or condition-specific optimal power to the glass melt under variable system impedance. In some embodiments, this objective will be of primary importance during start-up/warm-up melt processing. Because glass melt properties vary significantly depending upon the composition of the glass, the condition-specific optimal power can be derived from the temperature-viscosity curve characterizing the glass melt. In many cases, the condition-specific optimal power will be above approximately 200W. It is noted that the phrase "condition-specific optimal power" is introduced herein to cover situations where the controller frequency v c is controlled to deliver an optimal amount of power to the glass melt, under specifications established by the user of the system, with the understanding that the optimal power may or may not be maximum power.
  • controller frequency v c can be further controlled in response to a heat loss parameter QSYS, representing an amount of heat lost in the glass melt, or a process disturbance parameter dz representing process
  • the control objective associated with controlling the controller power P c is the maintenance of glass temperature at a condition-specific optimal level under variable system thermal conditions. In some embodiments, this objective will be of primary importance after start-up/warm-up melt processing.
  • the controller power Pc can be controlled to maintain glass temperature at an optimal level for glass fining processes, e.g., above approximately 1000°C. Because glass melt properties vary significantly depending upon the composition of the glass, the optimal level of the glass temperature can be derived from the temperature-viscosity curve characterizing the glass melt.
  • the controller power Pc can be controlled in response to ⁇ , where ⁇ represents a degree to which the monitored glass melt temperature T Y differs from the reference glass melt temperature T R .
  • the controller power P c can be additionally controlled in response to one or more input parameters from one or more temperature models of the glass melt.
  • the temperature models make take a variety of forms but will generally represent the relationship between input power and glass temperature.
  • the monitored glass melt temperature T Y can be determined from single or multiple simultaneous temperature measurements in the glass melt.
  • can be a direct comparison of the monitored glass melt temperature T Y and the reference glass melt temperature T R .
  • the reference glass melt temperature T R can be selected according to condition-specific glass melt treatments and in some embodiments lies between approximately 800°C and approximately 1700°C, with the understanding that more likely temperature ranges will fall between approximately 1000°C and approximately 1650°C.
  • the monitored glass melt temperature T Y and the reference glass melt temperature T R may comprise single temperature values, a range of temperature values, or a representation of temperature profile.
  • controller power P c can be further controlled in response to a process disturbance parameter dj representing process disturbances that directly or indirectly affect ⁇ .
  • This parameter is illustrated schematically in Figs. 1 and 3.
  • Figs. 5-7 illustrate design components of a class of suitable ultrasonic transducer assemblies.
  • the assembly comprises an ultrasonic transducer 100, an ultrasonic booster 1 10, an ultrasonic probe 120, and a booster cooling unit 130.
  • the ultrasonic transducer 100 generates acoustic energy at frequencies above approximately 15 kHz.
  • the ultrasonic booster 1 10 amplifies acoustic energy generated by the ultrasonic transducer 100 and transfers the amplified acoustic energy to the ultrasonic probe 120.
  • a seated end 122 of the ultrasonic probe 120 is positioned in a probe seat 1 12 of the ultrasonic booster 1 10.
  • the seated end 122 of the ultrasonic probe 120 can have a slightly reduced circumference relative to the rest of the probe surface to aid in the probe seating operation.
  • the booster cooling unit 130 is positioned to regulate the temperature of the probe seat 1 12 of the ultrasonic booster 1 10 such that the assembly supports a temperature dependent press-fit engagement of the seated end 122 of the ultrasonic probe 120 and the probe seat 1 12 of the ultrasonic booster 1 10.
  • the temperature dependent press-fit engagement is such that the seated end 122 of the ultrasonic probe 120 can be reversibly moved in and out of the probe seat 1 12 when the probe seat 1 12 of the ultrasonic booster 1 10 is at an elevated temperature ⁇ ⁇ ⁇
  • the seated end 122 of the ultrasonic probe 120 can be fixed in the probe seat 1 12 at room temperature TCOLD, which is defined broadly herein as any temperature between approximately 0°C and approximately 100° because of the significantly higher temperatures associated with glass melts. The following relationship holds for the elevated temperature ⁇ ⁇ ⁇ and room temperature
  • the booster cooling unit 130 helps maintain the temperature of the probe seat 1 12 well below ⁇ ⁇ ⁇ , e.g., lower than approximately 50°C, to ensure that the seated end 122 of the probe 120 remains fixed in the probe seat 1 12 of the ultrasonic booster 1 10.
  • the resulting assembly is secure enough to avoid the use of threaded elements and adhesives in the assembly.
  • the ultrasonic booster 1 10 comprises a probe seat defining a probe seating dimension d and the geometry of the seated end 122 of the ultrasonic probe 120 is such that the ultrasonic probe defines a complementary seating dimension d' supporting a press-fit engagement of the seated end 122 of the ultrasonic probe 120 and the probe seat 1 12 of the ultrasonic booster 1 10.
  • the dimensions are diametrical but is contemplated that the probe 120 and booster 1 10 may define a variety of alternative geometries. It is also noted that the particular scale of the dimensions may vary from embodiment to embodiment, depending upon the requirements of the glass melting operation at hand.
  • the ultrasonic booster 1 1 0 is characterized by a coefficient of thermal expansion that is sufficient for expansion of the probe seating dimension d from a seating dimension dcoLD at room temperature T C OLD (less than 1 00°C) to a seating dimension d HOT at an elevated temperature ⁇ ⁇ ⁇ -
  • the probe seating dimension d of the ultrasonic booster and the complementary seating dimension d' of the seated end 1 22 of the ultrasonic probe 1 20 can be configured to approximate the following relation to help ensure the above noted reversibility and secure seating:
  • the relation is "approximated" in the sense that the complementary seating dimension d' may be slightly less than the seating dimension dcoLD or slightly greater than the seating dimension d HOT, as long as the aforementioned secure seating at room temperature TCOLD and reversible movement at the elevated temperature ⁇ ⁇ ⁇ is achieved.
  • the booster cooling unit 1 30 comprises a fluid cooling jacket surrounding a portion of the ultrasonic booster 1 1 0 or a component of the assembly thermally coupled thereto, i.e., a portion of the transducer 1 00 coupled to the booster 1 1 0.
  • the booster cooling unit is illustrated in cross section in Fig. 6 and may be configured in a variety of alternative ways to regulate the temperature of the ultrasonic booster.
  • contemplated transducer assemblies may be provided with additional cooling units 1 32, 1 34 thermally coupled to the ultrasonic probe 1 20 or the ultrasonic transducer 1 00 to contribute to temperature regulation throughout the assembly.
  • the ultrasonic transducer 1 00, the ultrasonic booster 1 1 0, the ultrasonic probe 1 20, and the booster cooling unit 1 30 can be conveniently assembled as a rigid, mechanically coupled assembly.
  • the ultrasonic transducer assembly is configured for operation above 200W and above 1 000°C.
  • the ultrasonic booster may comprise a Ti alloy ultrasonic booster and the ultrasonic probe may comprise a single wavelength probe or a multi-wavelength probe fabricated from alumina or molybdenum.
  • the probe is provided with an inner gas purging fixture to prevent oxidation of the ultrasonic probe in the glass melt.
  • the transducer assembly may comprise an alumina waveguide tightly fitted to a modified ultrasonic booster made with a titanium alloy.
  • a tight shrink fit is an OD 20mm rod with a U7 shaft, h6 tolerance hole.
  • the ceramic rod is inserted into the booster using conductive heating, i.e., heating the bottom end of the booster to 200 ⁇ 300°C.
  • the rod is then press fit with an overlap of approximately 1 inch. Cooling of the booster hot end to room temperature would then create a tight fit.
  • the same concept and design could be used to make probe-booster pairs of different sizes.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Investigating Or Analyzing Materials By The Use Of Ultrasonic Waves (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
  • Transducers For Ultrasonic Waves (AREA)

Abstract

An ultrasonic transducer assembly is provided comprising an ultrasonic transducer, an ultrasonic booster, an ultrasonic probe, and a booster cooling unit. The ultrasonic booster is connected to the ultrasonic transducer to amplify acoustic energy generated by the ultrasonic transducer and transfer the amplified acoustic energy to the ultrasonic probe. A seated end of the ultrasonic probe is positioned in a probe seat of the ultrasonic booster. The booster cooling unit is positioned to regulate the temperature of the probe seat of the ultrasonic booster such that the assembly supports a temperature dependent press-fit engagement of the seated end of the ultrasonic probe and the probe seat of the ultrasonic booster. The temperature dependent press-fit engagement is such that the seated end of the ultrasonic probe can be reversibly moved in and out of the probe seat at an elevated temperature ΤΗοτ and is fixed in the probe seat at room temperature TCOLD. A method of applying ultrasonic acoustic energy to a glass melt by monitoring a glass melt temperature TY and transferring ultrasonic acoustic energy from an ultrasonic transducer to the glass melt at a controller power Pc and a controller frequency Vc through an ultrasonic probe positioned in the glass melt is provided. Systems for applying ultrasonic acoustic energy to glass melts are also provided.

Description

ULTRASONIC TRANSDUCER ASSEMBLY FOR APPLYING ULTRASONIC ACOUSTIC ENERGY TO A GLASS MELT
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001]This application claims the benefit of priority under 35 U.S.C. §120 of U.S. Application Serial No. 13/036,568, filed on February 28, 201 1 , and U.S. Application Serial No. 13/036,668, filed on February 28, 201 1 , the contents of which are relied upon and incorporated herein by reference in their entirety.
BACKGROUND
Field
[0002]The present disclosure relates to glass manufacturing processes and systems including, but not limited to, glass mixing, homogenization, fining, or any process or system where the introduction of mechanical energy to the glass melt might be advantageous.
Technical Background
[0003] Mechanical stirrers are commonly employed to introduce mechanical energy to a glass melt. We have recognized that mechanical stirrers can, under some conditions, be a source of contamination in a glass melt.
BRIEF SUMMARY
[0004] In accordance with one embodiment of the present disclosure, a method of applying ultrasonic acoustic energy to a glass melt by monitoring a glass melt temperature TY and transferring ultrasonic acoustic energy from an ultrasonic transducer to the glass melt at a controller power Pc and a controller frequency vc through an ultrasonic probe positioned in the glass melt is provided. According to the method, the controller power Pc is controlled in response to at least (i) the monitored glass melt temperature TY and (ii) a reference glass melt temperature TR. The controller frequency vc is controlled in response to at least (i) one or more input parameters from a temperature-viscosity curve characterizing the glass melt, (ii) one or more input parameters from one or more temperature dependent impedance response models of the glass melt, and (iii) ΔΖ, where ΔΖ represents a degree to which an impedance condition ZY of the ultrasonic probe differs from a reference impedance ZR when the ultrasonic probe is positioned in the glass melt. Systems for applying ultrasonic acoustic energy to glass melts are also contemplated.
[0005] In accordance with another embodiment of the present disclosure, an ultrasonic transducer assembly is provided comprising an ultrasonic transducer, an ultrasonic booster, an ultrasonic probe, and a booster cooling unit. The ultrasonic booster is connected to the ultrasonic transducer to amplify acoustic energy generated by the ultrasonic transducer and transfer the amplified acoustic energy to the ultrasonic probe. A seated end of the ultrasonic probe is positioned in a probe seat of the ultrasonic booster. The booster cooling unit is positioned to regulate the temperature of the probe seat of the ultrasonic booster such that the assembly supports a temperature dependent press-fit engagement of the seated end of the ultrasonic probe and the probe seat of the ultrasonic booster. The temperature dependent press-fit engagement is such that the seated end of the ultrasonic probe can be reversibly moved in and out of the probe seat at an elevated temperature THOT and is fixed in the probe seat at room temperature TCOLD-
[0006]We contemplate that the ultrasonic processes and systems disclosed herein will help address the potential source of contamination introduced by known mechanical stirrers. In addition, we have recognized that the use of ultrasonic energy may be advantageous in glass fining operations because ultrasonic energy can encourage the coalescence of bubbles, allowing for Stokes fining, and can encourage acoustic streaming, where gas bubbles move toward the glass air interface. Finally, we contemplate that the ultrasonic processes and systems disclosed herein will enjoy applicability to a wide variety of additional manufacturing, diagnostic, and developmental processes utilizing glass melts. Although the methodology of the present disclosure has applicability to a variety of glass compositions, we have recognized that the need for effective glass mixing and fining processes is particularly acute in the context of specialty glasses, such as
photovoltaic glasses, LCD glasses, consumer electronics glasses, high purity fused silica glasses, and specialty glasses manufactured and sold under the Corning Incorporated trade names Eagle XG® glass and Gorilla® glass.
BRIEF DESCRIPTION OF THE DRAWINGS
[0007] The following detailed description of specific embodiments of the present disclosure can be best understood when read in conjunction with the following drawings, where like structure is indicated with like reference numerals and in which:
[0008] Fig. 1 is a schematic illustration of a system and method as disclosed herein for applying ultrasonic acoustic energy to a glass melt;
[0009] Fig. 2 is a schematic illustration of a method as disclosed herein for controlling ultrasonic frequency when applying ultrasonic acoustic energy to a glass melt;
[0010] Fig. 3 is a schematic illustration of a method as disclosed herein for controlling acoustic power when applying ultrasonic acoustic energy to a glass melt;
[0011] Fig. 4 illustrates modeled temperature dependent impedance responses of a glass melt; [0012] Fig. 5 illustrates an ultrasonic probe assembly including one or more features of the present disclosure;
[0013] Fig. 6 is a cross sectional illustration of a booster cooling unit according to the present disclosure;
[0014] Fig. 7 is a partially exploded view of a portion of the ultrasonic probe assembly illustrated in Fig. 5; and
[0015] Fig. 8 illustrates an alternative ultrasonic probe assembly including one or more features of the present disclosure.
DETAILED DESCRIPTION
[0016] The system and methodology of the present disclosure can be described with initial reference to Fig. 1 , which is a schematic illustration of a system for applying ultrasonic acoustic energy to a glass melt 10. The system comprises an ultrasonic power supply 20, an ultrasonic transducer 30, and an ultrasonic probe 40. The ultrasonic power supply is programmed to monitor a glass melt temperature TY with the aid of one or more temperature sensors 50 and to transfer ultrasonic acoustic energy from the ultrasonic transducer 30, through the ultrasonic probe 40, to the glass melt 10 at a controller power Pc and a controller frequency vc. The following description addresses the manner in which the controller power Pc and controller frequency vc are controlled. The following description also introduces examples of ultrasonic probe assemblies that can be employed in the system and methodology disclosed herein. It is noted that the power and frequency control schemes contemplated herein are not limited to use with any specific types of hardware.
[0017] According to the methodology of the present disclosure, the controller power
Pc is controlled in response to at least (i) the monitored glass melt temperature TY and (ii) a reference glass melt temperature TR. Fig. 3, which is discussed in further detail below, can be read in conjunction with Fig. 1 to illustrate various aspects of power control contemplated herein. It is noted that reference herein to a parameter being "controlled" is intended to cover a variety of parameter control conditions including, but not limited to, conditions where a parameter is established,
determined, adjusted, maintained, etc. In addition, reference to a parameter being controlled "in response to" particular data is intended to cover a variety of uses of the data including, but not limited to instances where the parameter is a direct or indirect function of the data or, more broadly, where the parameter is somehow influenced by the data.
[0018] Fig. 1 can be read in conjunction with Fig. 2 to illustrate various aspects of frequency control contemplated herein. More specifically, the controller frequency vc is controlled in response to at least (i) one or more input parameters from a temperature-viscosity curve T, G characterizing the glass melt 10, (ii) one or more input parameters from one or more temperature dependent impedance response models of the glass melt 10, and (iii) ΔΖ, where ΔΖ represents a degree to which an impedance condition ZY of the ultrasonic probe 40 differs from a reference
impedance ZR when the ultrasonic probe 40 is positioned in the glass melt 10. The controller frequency vc is selected for condition-specific glass melt treatment and typically lies between approximately 15 kHz and approximately 30 kHz. The input parameters from the temperature-viscosity curve characterizing the glass melt may comprise a single viscosity value, multiple viscosity values, a viscosity range, or combinations thereof. It is noted that the phrase "condition-specific glass melt treatment" is introduced herein to refer to treatment conditions where optimal process benchmarks are established by the user of the system.
[0019] From a broad perspective, the input parameters from the impedance response models of the glass melt represent a selected resonance of the ultrasonic probe in the glass melt and are used for relatively coarse control of the controller frequency vc. For example, Fig. 4 illustrates a set of temperature dependent impedance response models for an ultrasonic probe at room temperature Ti and successively higher temperatures T2, T3, T in a glass melt. We have recognized that these types of impedance response models can be used to identify resonance troughs that are relatively highly damped as temperature increases (see trough A) and resonance troughs that are relatively minimally damped as temperature increases (see trough B). To optimize performance, the temperature dependent impedance response models can be used to generate input parameters for the controller frequency Vc that identify the frequency characteristics of the relatively minimally damped resonance trough. For example, referring to the specific models illustrated in Fig. 4, the modeled impedance responses illustrate primary A and secondary B low-impedance resonance troughs for the ultrasonic probe in the glass melt. Because the secondary troughs exhibit minimal temperature-dependent damping, the input parameters used for the controller frequency Vc will identify the frequency characteristics of the secondary low-impedance resonance trough B. The input parameters can identify a frequency range because they can be used for coarse control but it is contemplated that the input parameters may comprise a single ultrasonic frequency value, multiple ultrasonic frequency values, an ultrasonic frequency range, or combinations thereof.
[0020] Returning specifically to Figs. 1 and 2, for fine control of the controller frequency Vc, reference can be made to ΔΖ, which represents a degree to which the impedance condition ZY of the ultrasonic probe 40 differs from the reference impedance ZR when the ultrasonic probe 40 is positioned in the glass melt 10. ΔΖ can also be taken as a representation of the power factor of the ultrasonic probe 40 in the glass melt 10 because the transducer impedance represents the phase difference between the control voltage and current of the ultrasonic probe. More specifically, the impedance condition ZY of the ultrasonic probe 40 is determined from measurements of electrical current I flowing through the transducer assembly and a voltage drop V across the transducer assembly. ΔΖ can be a direct comparison of the impedance condition ZY of the ultrasonic probe and the reference impedance ZR when the ultrasonic probe is positioned in the glass melt. For optimal glass melt treatment, the reference impedance ZR is selected for as sharp a resonance as possible and will typically correspond to a particular frequency range, which depends on the temperature and glass viscosity. Typical frequency ranges will fall between approximately 15kHz and approximately 30kHz.
[0021 ] Generally, the control objective associated with controlling the frequency Vc is the delivery of maximum or condition-specific optimal power to the glass melt under variable system impedance. In some embodiments, this objective will be of primary importance during start-up/warm-up melt processing. Because glass melt properties vary significantly depending upon the composition of the glass, the condition-specific optimal power can be derived from the temperature-viscosity curve characterizing the glass melt. In many cases, the condition-specific optimal power will be above approximately 200W. It is noted that the phrase "condition-specific optimal power" is introduced herein to cover situations where the controller frequency vc is controlled to deliver an optimal amount of power to the glass melt, under specifications established by the user of the system, with the understanding that the optimal power may or may not be maximum power.
[0022] It is contemplated that the controller frequency vc can be further controlled in response to a heat loss parameter QSYS, representing an amount of heat lost in the glass melt, or a process disturbance parameter dz representing process
disturbances that directly or indirectly affect ΔΖ. These parameters are illustrated schematically in Figs. 1 and 2. [0023]The control objective associated with controlling the controller power Pc is the maintenance of glass temperature at a condition-specific optimal level under variable system thermal conditions. In some embodiments, this objective will be of primary importance after start-up/warm-up melt processing. For example, the controller power Pc can be controlled to maintain glass temperature at an optimal level for glass fining processes, e.g., above approximately 1000°C. Because glass melt properties vary significantly depending upon the composition of the glass, the optimal level of the glass temperature can be derived from the temperature-viscosity curve characterizing the glass melt.
[0024] Referring specifically to Figs. 1 and 3, it is contemplated that the controller power Pc can be controlled in response to ΔΤ, where ΔΤ represents a degree to which the monitored glass melt temperature TY differs from the reference glass melt temperature TR. The controller power Pc can be additionally controlled in response to one or more input parameters from one or more temperature models of the glass melt. The temperature models make take a variety of forms but will generally represent the relationship between input power and glass temperature.
[0025]The monitored glass melt temperature TY can be determined from single or multiple simultaneous temperature measurements in the glass melt. ΔΤ can be a direct comparison of the monitored glass melt temperature TY and the reference glass melt temperature TR. Because glass properties and treatment requirements vary significantly from one glass composition to another, the reference glass melt temperature TR can be selected according to condition-specific glass melt treatments and in some embodiments lies between approximately 800°C and approximately 1700°C, with the understanding that more likely temperature ranges will fall between approximately 1000°C and approximately 1650°C. In any case, the monitored glass melt temperature TY and the reference glass melt temperature TR may comprise single temperature values, a range of temperature values, or a representation of temperature profile.
[0026] It is contemplated that the controller power Pc can be further controlled in response to a process disturbance parameter dj representing process disturbances that directly or indirectly affect ΔΤ. This parameter is illustrated schematically in Figs. 1 and 3.
[0027] As we note above, the methodology of the present disclosure may be executed with a variety of transducer and probe configurations. Nevertheless, Figs. 5-7 illustrate design components of a class of suitable ultrasonic transducer assemblies. In Figs. 5-7, the assembly comprises an ultrasonic transducer 100, an ultrasonic booster 1 10, an ultrasonic probe 120, and a booster cooling unit 130. The ultrasonic transducer 100 generates acoustic energy at frequencies above approximately 15 kHz. The ultrasonic booster 1 10 amplifies acoustic energy generated by the ultrasonic transducer 100 and transfers the amplified acoustic energy to the ultrasonic probe 120.
[0028] A seated end 122 of the ultrasonic probe 120 is positioned in a probe seat 1 12 of the ultrasonic booster 1 10. The seated end 122 of the ultrasonic probe 120 can have a slightly reduced circumference relative to the rest of the probe surface to aid in the probe seating operation. The booster cooling unit 130 is positioned to regulate the temperature of the probe seat 1 12 of the ultrasonic booster 1 10 such that the assembly supports a temperature dependent press-fit engagement of the seated end 122 of the ultrasonic probe 120 and the probe seat 1 12 of the ultrasonic booster 1 10. The temperature dependent press-fit engagement is such that the seated end 122 of the ultrasonic probe 120 can be reversibly moved in and out of the probe seat 1 12 when the probe seat 1 12 of the ultrasonic booster 1 10 is at an elevated temperature ΤΗοτ■ The seated end 122 of the ultrasonic probe 120 can be fixed in the probe seat 1 12 at room temperature TCOLD, which is defined broadly herein as any temperature between approximately 0°C and approximately 100° because of the significantly higher temperatures associated with glass melts. The following relationship holds for the elevated temperature ΤΗοτ and room temperature
TCOLD:
T COLD <— i 1o UoU° ^
1 HOT 1 COLD — J UU ^
In operation, the booster cooling unit 130 helps maintain the temperature of the probe seat 1 12 well below ΤΗοτ, e.g., lower than approximately 50°C, to ensure that the seated end 122 of the probe 120 remains fixed in the probe seat 1 12 of the ultrasonic booster 1 10. The resulting assembly is secure enough to avoid the use of threaded elements and adhesives in the assembly. The reference herein to
"reversible" movement of the seated end 122 of the ultrasonic probe 120 in and out of the probe seat 1 12 is intended to include unimpeded or unobstructed movement of the probe 120 and to exclude movement that would result in damage to the probe 120 or otherwise interfere with its functionality.
[0029] More specifically, as is illustrated in Fig. 7, the ultrasonic booster 1 10 comprises a probe seat defining a probe seating dimension d and the geometry of the seated end 122 of the ultrasonic probe 120 is such that the ultrasonic probe defines a complementary seating dimension d' supporting a press-fit engagement of the seated end 122 of the ultrasonic probe 120 and the probe seat 1 12 of the ultrasonic booster 1 10. In the illustrated case, the dimensions are diametrical but is contemplated that the probe 120 and booster 1 10 may define a variety of alternative geometries. It is also noted that the particular scale of the dimensions may vary from embodiment to embodiment, depending upon the requirements of the glass melting operation at hand. [0030]The ultrasonic booster 1 1 0 is characterized by a coefficient of thermal expansion that is sufficient for expansion of the probe seating dimension d from a seating dimension dcoLD at room temperature TCOLD (less than 1 00°C) to a seating dimension d HOT at an elevated temperature ΤΗοτ- The probe seating dimension d of the ultrasonic booster and the complementary seating dimension d' of the seated end 1 22 of the ultrasonic probe 1 20 can be configured to approximate the following relation to help ensure the above noted reversibility and secure seating:
It is noted that the relation is "approximated" in the sense that the complementary seating dimension d' may be slightly less than the seating dimension dcoLD or slightly greater than the seating dimension d HOT, as long as the aforementioned secure seating at room temperature TCOLD and reversible movement at the elevated temperature ΤΗοτ is achieved.
[0031] In the illustrated embodiment, the booster cooling unit 1 30 comprises a fluid cooling jacket surrounding a portion of the ultrasonic booster 1 1 0 or a component of the assembly thermally coupled thereto, i.e., a portion of the transducer 1 00 coupled to the booster 1 1 0. The booster cooling unit is illustrated in cross section in Fig. 6 and may be configured in a variety of alternative ways to regulate the temperature of the ultrasonic booster. As is illustrated in Fig. 8, contemplated transducer assemblies may be provided with additional cooling units 1 32, 1 34 thermally coupled to the ultrasonic probe 1 20 or the ultrasonic transducer 1 00 to contribute to temperature regulation throughout the assembly.
[0032] It is contemplated that the ultrasonic transducer 1 00, the ultrasonic booster 1 1 0, the ultrasonic probe 1 20, and the booster cooling unit 1 30 can be conveniently assembled as a rigid, mechanically coupled assembly. In some embodiments, the ultrasonic transducer assembly is configured for operation above 200W and above 1 000°C. [0033] The ultrasonic booster may comprise a Ti alloy ultrasonic booster and the ultrasonic probe may comprise a single wavelength probe or a multi-wavelength probe fabricated from alumina or molybdenum. In the case of molybdenum, in some embodiments the probe is provided with an inner gas purging fixture to prevent oxidation of the ultrasonic probe in the glass melt.
[0034] By way of illustration and not limitation, it is noted that the transducer assembly may comprise an alumina waveguide tightly fitted to a modified ultrasonic booster made with a titanium alloy. An example of a tight shrink fit is an OD 20mm rod with a U7 shaft, h6 tolerance hole. The ceramic rod is inserted into the booster using conductive heating, i.e., heating the bottom end of the booster to 200~300°C. The rod is then press fit with an overlap of approximately 1 inch. Cooling of the booster hot end to room temperature would then create a tight fit. The same concept and design could be used to make probe-booster pairs of different sizes.
[0035] It is noted that recitations herein of "at least one" component, element, etc., should not be used to create an inference that the alternative use of the articles "a" or "an" should be limited to a single component, element, etc.
[0036] It is noted that recitations herein of a component of the present disclosure being "configured" in a particular way or to embody a particular property, or function in a particular manner, are structural recitations, as opposed to recitations of intended use. More specifically, the references herein to the manner in which a component is "configured" denotes an existing physical condition of the component and, as such, is to be taken as a definite recitation of the structural characteristics of the component.
[0037] For the purposes of describing and defining the present invention it is noted that the terms "substantially" and "approximately" are utilized herein to represent the inherent degree of uncertainty that may be attributed to any quantitative comparison, value, measurement, or other representation.
[0038] It is noted that terms like "preferably," "commonly," and "typically," when utilized herein, are not utilized to limit the scope of the claimed invention or to imply that certain features are critical, essential, or even important to the structure or function of the claimed invention. Rather, these terms are merely intended to identify particular aspects of an embodiment of the present disclosure or to emphasize alternative or additional features that may or may not be utilized in a particular embodiment of the present disclosure.
[0039] Having described the subject matter of the present disclosure in detail and by reference to specific embodiments thereof, it is noted that the various details disclosed herein should not be taken to imply that these details relate to elements that are essential components of the various embodiments described herein, even in cases where a particular element is illustrated in each of the drawings that accompany the present description. Rather, the claims appended hereto should be taken as the sole representation of the breadth of the present disclosure and the corresponding scope of the various inventions described herein. Further, it will be apparent that modifications and variations are possible without departing from the scope of the invention defined in the appended claims.
[0040] It is noted that one or more of the following claims utilize the term "wherein" as a transitional phrase. For the purposes of defining the present invention, it is noted that this term is introduced in the claims as an open-ended transitional phrase that is used to introduce a recitation of a series of characteristics of the structure and should be interpreted in like manner as the more commonly used open-ended preamble term "comprising."

Claims

1 . An ultrasonic transducer assembly comprising an ultrasonic transducer, an ultrasonic booster, an ultrasonic probe, and a booster cooling unit, wherein:
the ultrasonic transducer generates acoustic energy at frequencies above approximately 15 kHz;
the ultrasonic booster is connected to the ultrasonic transducer to amplify acoustic energy generated by the ultrasonic transducer and transfer the amplified acoustic energy to the ultrasonic probe;
a seated end of the ultrasonic probe is positioned in a probe seat of the ultrasonic booster;
the booster cooling unit is positioned to regulate the temperature of the probe seat of the ultrasonic booster such that the assembly supports a temperature dependent press-fit engagement of the seated end of the ultrasonic probe and the probe seat of the ultrasonic booster; and
the temperature dependent press-fit engagement is such that the seated end of the ultrasonic probe can be reversibly moved in and out of the probe seat at an elevated temperature ΤΗοτ and is fixed in the probe seat at room temperature TCOLD, wherein
2. An ultrasonic transducer assembly comprising an ultrasonic transducer, an ultrasonic booster, an ultrasonic probe, and a booster cooling unit, wherein:
the ultrasonic transducer generates acoustic energy at frequencies above approximately 15 kHz; the ultrasonic booster amplifies acoustic energy generated by the ultrasonic transducer and transfers the amplified acoustic energy to the ultrasonic probe;
the ultrasonic booster comprises a probe seat defining a probe seating dimension d;
the booster cooling unit is positioned to regulate the temperature of the probe seat of the ultrasonic booster;
the ultrasonic probe extends from a seated end positioned in the probe seat of the ultrasonic booster to a leading end of the ultrasonic probe;
the geometry of the seated end of the ultrasonic probe is such that the ultrasonic probe defines a complementary seating dimension d' supporting a press-fit engagement of the seated end of the ultrasonic probe and the probe seat of the ultrasonic booster; and
the ultrasonic booster is characterized by a coefficient of thermal expansion that is sufficient for expansion of the probe seating dimension d from a seating dimension dcoLD at room temperature TCOLD to a seating dimension dHOT at an elevated temperature ΤΗοτ where the seating dimensions dcoLD and dHOT and the complementary seating dimension d' approximate the following relation
d, COLD < d'< d HOT
and the respective temperatures approximate the following relations
3. The ultrasonic transducer assembly of claim 1 wherein the booster cooling unit comprises a fluid cooling jacket surrounding a portion of the ultrasonic booster or a component of the assembly thermally coupled thereto.
4. The ultrasonic transducer assembly of claim 1 wherein the transducer assembly comprises an additional cooling unit thermally coupled to the ultrasonic probe.
5. The ultrasonic transducer assembly of claim 1 wherein the transducer assembly comprises an additional cooling unit thermally coupled to the ultrasonic transducer.
6. The ultrasonic transducer assembly of claim 1 wherein the ultrasonic transducer, the ultrasonic booster, the ultrasonic probe, and the booster cooling unit are assembled as a rigid, mechanically coupled assembly.
7. The ultrasonic transducer assembly of claim 1 wherein the ultrasonic transducer assembly is configured for operation above 200W and above 1000°C.
8. The ultrasonic transducer assembly of claim 1 wherein the ultrasonic booster comprises a Ti alloy ultrasonic booster.
9. The ultrasonic transducer assembly of claim 1 wherein the seated end of the ultrasonic probe and the probe seat of the ultrasonic booster are thread-free.
10. The ultrasonic transducer assembly of claim 1 wherein the seated end of the ultrasonic probe and the probe seat of the ultrasonic booster are adhesive-free.
1 1 . The ultrasonic transducer assembly of claim 1 wherein the ultrasonic probe comprises a single wavelength alumina probe.
12. The ultrasonic transducer assembly of claim 1 wherein the ultrasonic probe comprises a multi-wavelength molybdenum probe.
13. The ultrasonic transducer assembly of claim 1 wherein the controller frequency vc lies between approximately 15 kHz and approximately 30 kHz.
14. The ultrasonic transducer assembly of claim 1 wherein:
the ultrasonic transducer assembly further comprises an ultrasonic power supply;
the ultrasonic power supply is programmed to monitor a glass melt temperature TY of a glass melt and to transfer ultrasonic acoustic energy from the ultrasonic transducer to the glass melt at a controller power Pc and at a controller frequency vc through the ultrasonic probe positioned in the glass melt;
the controller power Pc is controlled in response to at least (i) the monitored glass melt temperature TY and (ii) a reference glass melt temperature TR;
the controller frequency vc is controlled in response to at least (i) one or more input parameters from a temperature-viscosity curve characterizing the glass melt, (ii) one or more input parameters from one or more temperature dependent impedance response models of the glass melt, and (iii) ΔΖ, where ΔΖ represents a degree to which an impedance condition ZY of the ultrasonic probe differs from a reference impedance ZR when the ultrasonic probe is positioned in the glass melt.
15. A method of applying ultrasonic acoustic energy to a glass melt by monitoring a glass melt temperature TY and transferring ultrasonic acoustic energy from an ultrasonic transducer to the glass melt at a controller power Pc and a controller frequency vc through an ultrasonic probe positioned in the glass melt, wherein: the controller power Pc is controlled in response to at least (i) the monitored glass melt temperature TY and (ii) a reference glass melt temperature TR;
the controller frequency vc is controlled in response to at least (i) one or more input parameters from a temperature-viscosity curve characterizing the glass melt, (ii) one or more input parameters from one or more temperature dependent impedance response models of the glass melt, and (iii) ΔΖ, where ΔΖ represents a degree to which an impedance condition ZY of the ultrasonic probe differs from a reference impedance ZR when the ultrasonic probe is positioned in the glass melt.
16. The method of claim 15 wherein:
the input parameters from one or more temperature dependent impedance response models of the glass melt represent a selected resonance of the ultrasonic probe in the glass melt and are used for relatively coarse control of the controller frequency vc; and
ΔΖ represents a power factor of the ultrasonic probe in the glass melt and is used for relatively fine control of the controller frequency vc.
17. The method of claim 15 wherein the controller frequency vc is controlled to deliver maximum power to the glass melt under variable system impedance.
18. The method of claim 15 wherein the controller frequency is controlled to deliver condition-specific optimal power to the glass melt under variable system impedance.
19. The method of claim 18 wherein the condition-specific optimal power is derived from the temperature-viscosity curve characterizing the glass melt.
20. The method of claim 15 wherein the controller power is controlled to maintain glass temperature at a condition-specific optimal level under variable system thermal conditions.
21 . The method of claim 20 wherein the controller power is controlled to maintain glass temperature at an optimal level for glass fining processes.
22. The method of claim 21 wherein the optimal level of the glass temperature is derived from the temperature-viscosity curve characterizing the glass melt.
23. The method of claim 15 wherein:
the impedance response models are configured to illustrate relatively highly damped and minimally damped resonance troughs for the ultrasonic probe in the glass melt; and
the input parameters from the temperature dependent impedance response models used for the controller frequency Vc identify the frequency characteristics of the relatively minimally damped resonance trough.
24. The method of claim 15 wherein:
the impedance response models are configured to illustrate primary and secondary low-impedance resonance troughs for the ultrasonic probe in the glass melt; and
the input parameters from the temperature dependent impedance response models used for the controller frequency Vc identify the frequency characteristics of the secondary low-impedance resonance trough.
25. The method of claim 24 wherein:
the impedance condition ZY of the ultrasonic probe is determined from measurements of electrical current I flowing through the transducer assembly and a voltage drop V across the transducer assembly; and
ΔΖ is a direct comparison of the impedance condition ZY of the ultrasonic probe and the reference impedance ZR when the ultrasonic probe is positioned in the glass melt.
26. The method of claim 24 wherein the input parameters from the temperature- viscosity curve characterizing the glass melt comprise a single viscosity value, multiple viscosity values, a viscosity range, or combinations thereof.
27. The method of claim 24 wherein the controller frequency vc is further controlled in response to a heat loss parameter QSYS representing an amount of heat lost in the glass melt.
28. The method of claim 24 wherein the controller frequency vc is further controlled in response to a process disturbance parameter dz representing process
disturbances that directly or indirectly affect ΔΖ.
29. The method of claim 24 wherein:
the controller power Pc is controlled in response to at least ΔΤ, where ΔΤ represents a degree to which the monitored glass melt temperature TY differs from the reference glass melt temperature TR; and
the controller power Pc is additionally controlled in response to one or more input parameters from one or more temperature models of the glass melt.
30. The method of claim 24 wherein:
the monitored glass melt temperature TY is determined from single or multiple temperature measurements in the glass melt; and
ΔΤ is a direct comparison of the monitored glass melt temperature TY and the reference glass melt temperature TR when the ultrasonic probe is positioned in the glass melt.
31 . The method of claim 30 wherein the monitored glass melt temperature TY and the reference glass melt temperature TR comprise single temperature values, a range of temperature values, or a representation of temperature profile.
32. The method of claim 29 wherein the controller power Pc is further controlled in response to a process disturbance parameter dj representing process disturbances that directly or indirectly affect ΔΤ.
33. The method of claim 15 wherein:
the ultrasonic transducer and the ultrasonic probe are configured as an ultrasonic transducer assembly comprising the ultrasonic transducer, an ultrasonic booster, the ultrasonic probe, and a booster cooling unit;
the ultrasonic transducer generates acoustic energy at frequencies above approximately 15 kHz;
the ultrasonic booster amplifies acoustic energy generated by the ultrasonic transducer and transfers the amplified acoustic energy to the ultrasonic probe;
a seated end of the ultrasonic probe is positioned in a probe seat of the ultrasonic booster;
the booster cooling unit is positioned to regulate the temperature of the probe seat of the ultrasonic booster such that the assembly supports a temperature dependent press-fit engagement of the seated end of the ultrasonic probe and the probe seat of the ultrasonic booster; and
the temperature dependent press-fit engagement is such that the seated end of the ultrasonic probe can be reversibly moved in and out of the probe seat at an elevated temperature ΤΗοτ and is fixed in the probe seat at room temperature TCOLD, wherein
34. A system for applying ultrasonic acoustic energy to a glass melt, the system comprising an ultrasonic power supply, an ultrasonic transducer, and an ultrasonic probe, wherein:
the ultrasonic power supply is programmed to monitor a glass melt temperature TY and transfer ultrasonic acoustic energy from the ultrasonic transducer to the glass melt at a controller power Pc and a controller frequency vc through the ultrasonic probe positioned in the glass melt;
the controller power Pc is controlled in response to at least (i) the monitored glass melt temperature TY and (ii) a reference glass melt temperature TR;
the controller frequency vc is controlled in response to at least (i) one or more input parameters from a temperature-viscosity curve characterizing the glass melt, (ii) one or more input parameters from one or more temperature dependent impedance response models of the glass melt, and (iii) ΔΖ, where ΔΖ represents a degree to which an impedance condition ZY of the ultrasonic probe differs from a reference impedance ZR when the ultrasonic probe is positioned in the glass melt.
EP12716107.3A 2011-02-28 2012-02-27 Ultrasonic transducer assembly for applying ultrasonic acoustic energy to a glass melt Ceased EP2680960A2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US13/036,568 US9061928B2 (en) 2011-02-28 2011-02-28 Ultrasonic transducer assembly for applying ultrasonic acoustic energy to a glass melt
US13/036,668 US8490433B2 (en) 2011-02-28 2011-02-28 Method for applying ultrasonic acoustic energy to a glass melt
PCT/US2012/026679 WO2012118722A2 (en) 2011-02-28 2012-02-27 Ultrasonic transducer assembly for applying ultrasonic acoustic energy to a glass melt

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EP2680960A2 true EP2680960A2 (en) 2014-01-08

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JP5894196B2 (en) 2016-03-23
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JP2014512321A (en) 2014-05-22
WO2012118722A2 (en) 2012-09-07

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