Method for Manufacturing Glass Frit

This invention relates to a Method of Manufacturing Glass Frit which can be utilized for the making of pellets for use in a laser fusion process.

There is much work being done presently to achieve a fusion reaction by exposing a quantity of fusion fuel, as, for example, deuterium or deuterium-tritium to a pulsed laser beam. Patents which disclose this process in a general way are:

Whittlesey -- U.S. Pat. No. 3,378,446 -- 4/16/68

Daiber -- U.S. Pat. No. 3,489,645 -- 1/13/70

Fraas -- U.S. Pat. No. 3,624,239 -- 11/30/71

Hedstrom -- U.S. Pat. No. 3,762,992 -- 10/02/73

In addition, there are a number of pending applications of Keith A. Brueckner which disclose such a process. One such application bears Ser. No. 377,508 and filing date July 10, 1973.

The above patents disclose the use of a droplet of deuterium on a pellet under cryogenic temperatures so that it can be treated as a solid. These patents contemplate dropping the fuel into a reaction chamber and timing the laser to meet the droplet at about the center of the reaction chamber. Another patent application of Robert J. Teitel and David E. Solomon, Ser. No. 339,558, filed March 9. 1973, discloses a fuel configuration in the form of a hollow, glass microsphere which is filled with fusion fuel, such as deuterium or deuterium-tritium, by utilizing the permeability characteristics of the glass walls of the microsphere and causing the fuel in gaseous form to move through the walls to the interior of the sphere. Once the fuel is charged, the microspheres can be stored for long periods under suitable conditions until used in the fusion process.

While hollow microspheres are available in commercial quantities, the non-uniformity of size and wall thickness makes them undesirable for use in the fusion process. It is an object of the present invention to provide a glass frit which is suitable for manufacturing hollow glass microspheres of high and uniform quality. It is a further object to provide a method and composition for the manufacturing of glass frit which results in a uniform product.

Other objects and features of the invention will be apparent in the following description and claims wherein are set forth the principles of the invention together with the best mode presently contemplated for the practice of the invention.

Drawings accompany the disclosure and the various views thereof may be briefly described as:

FIG. 1, a first flowchart illustrating a first method.

FIG. 2, a second flowchart illustrating a modified method.

Desirable microsphere specifications are as follows:

Ability to Withstand Thermal Cycle: 4.degree. K. - 600.degree. K.

Shear strength: > 100,00 psi

Tensile strength: > 1,000,000 psi

Resistance to abrasion: high

Permeability to hydrogen at 600.degree. K.: .about. 10.sup..sup.-8

Permeability to hydrogen at 300.degree. K.: .about. 10.sup..sup.-13

Permeability of hydrogen at 77.degree. K.: .about. 10.sup..sup.-17

Reflectivity from 10 to 50 microns: high

Reflectivity at 1.06 microns: low

Absorptivity at 1.06 microns: high

Outside diameter: 100-400 .mu.m .+-. 1 .mu.m

Wall thickness: 1-4% .+-. 0.4.mu.m of diameter

Wall uniformity: .+-.5%

Concentricity of ID and OD: .+-.10%

Sphericity: .+-.1%

Surface finish: < 2.mu.m rms

Specific gravity: < 0.3

The present method contemplates the synthesis of glass which is, first of all, fuel of elements deleterious to the fusion reaction, and, second, ideally suited for blowing into microspheres having the desired characteristics set forth in Table I above. The gel glass technique is used in the process. This method is described by Helmut Dislich, mainly in a report dated May 27, 1970 delivered at the 44th Glass-Technical Meeting in Lindau, the title of the report being "The Preparation of Multi-Component Glasses Without Passing Through the Melt Phase".

According to the first example, the starting components are:

The quantities are weighed and mixed, the SiO.sub.2 being in liquid (suspension) form. A quantity of urea (NH.sub.2 CO NH.sub.2) equal to about 10% by weight of the mix is added. The mixture sets up in the form of a gel in about one minute which is then dried at about 100.degree. C. for 24 hours. This drives off water (H.sub.2 O) and methanol (CH.sub.3 OH). This period of time yields the most desirable residual water content for the blowing process. After drying the gel, it is in the form of a block which is washed in water, dried, and then crushed with a pestle in a steel mortar. This system has been found superior to the ball mill grinding process since the object is to obtain granular particles as distinguished from a talc.

The C. frit is then dry sieved to -100, +120 U.S. Standard Sieve size (125 micrometer to 149 micrometer particle size) and then placed back in a furnace at 90.degree. C to maintain the same water content. Special multiple sieve sets having gradations as low as 5 micrometers are used in the sizing operation. These steps are diagrammed in FIG. 1. The resulting glass has a composition of SiO.sub.2, 73% by weight, Na.sub.2 O, 20% and B.sub.2 O.sub.3, 7%. The particular starting particle size is selected on the basis that, after determining a density of about 2.4 gm/cc and a mean size of 137 microns, it has a mean starting mass sufficient to yield a hollow glass sphere of the required dimension, as, for example, 200-300 microdiameter.

The sized frit material is washed in methanol to remove any fine powder that might be clinging to the particles. This will minimize the formation of bubbles in and on the walls of the resulting spheres. After this washing, the finished frit is oven dried at 100.degree. C. for two to four hours to obtain the desired water content before the introduction to the microsphere forming process (spheroidization).

In the modified second method, the starting materials might be:

The ingredients above listed are mixed with 10% by weight of urea (NH.sub.2 CONH.sub.2) and combined under a nitrogen atmosphere into a liquid mix and diluted with water or ethanol to facilitate gelation process. The diluted mixture is then allowed to gel over a period of about 12 hours and the water and ethanol allowed to evaporate leaving a solid block which is then crushed, sized, washed, and dried as previously described. The resulting glass has a composition of

PbO: 21% by weight

SiO.sub.2 : 63% by weight

NaO: 8% by weight

CaO: 2% by weight

K.sub.2 o: 6% by weight

The resulting frit from either Method 1 or Method 2 (or variations or combinations thereof) can then be subjected to the spheroidization or blowing process to produce hollow microspheres of the desired size. A process for forming the microspheres with desirable uniformity is described in a co-pending application of R. G. Budrick, F. T. King, A. J. Martin, R. L. Nolen, and D. E. Solomon, Ser. No. 463,860 filed Apr. 15, 1974.