US1906757A - Method of producing piezo-electric crystals - Google Patents

Description

B. KJELLGREN METHOD OF PRODUCING PIEZO ELECTRIC CRYSTALS .May 2, 1933.

Original Filed May 19, 1928 INVENTQR ATTORNEYS Patented May 2, 1933 UNITED STATES PATENT OFFICE BENGT KJ'ELLGBEN, OF CLEVELAND, OHIO, ABSIGNOR TO THE IBBUPH DEVELOPIENI COMPANY, 01 CLEVELAND, OHIO, A CORPORATION 01 OHIO METHOD 0! i PBODUCIN G PIEZO-ELEC'IRIC CRYSTALS R S S U E D Application filed Kay 19, 1928, Serial N0. 279,176. Renewed June 29, 1982.

This invention relates to an improved method for the production of large clear well developed crystals such as Rochelle salt crystals for use in the construction of piezo-electrie devices.

An object of this invention is to provide a method whereby such crystals can be pr0- duced in a comparatively short period of time.

A further object of this invention is to provide a simple and practical apparatus suitable for a large scale production of such crystals.

Another object is to provide a method of growing such crystals which will yield perfeet symmetrical crystals of the desired shape without parasitic agglomerations of crystalline material attached thereto.

Afurther object of this invention is to provide a method whereby the proportions of a growing crystal may be modified or controlled.

Other objects of the invention will be apparent to those skilled in the art from the description of it hereinafter given.

In the methods used at present for making large. clear well developed crystals, the crystallization is carried out either by lowering the temperature of the crystallizing solution or by evaporation of the solvent. The crystallizing solution may be in movement or at rest.

If the crystallizing solution is at rest the time required for growing large clear crystals will be comparatively long due to the slow diffusion of saturated solution throu h the layer of weak solution surrounding t e growing crystal, since if time is not allowed for this diffusion irregular growth takes place and mother liquor is occluded in the crystal, ,and. when Rochelle salt crystals are being i igifor ned, for example, crystals known as composite crystals will be formed. These crystals are those having hour glass structure at the ends thereof in which considerable mother liquor is occluded and the crystals are not solid crystalline material throughout.

If the crystallizing solution is in movement, the weak solution around the crystal is continuously replaced with saturated solution, thus making it possible to grow solid I clear crystals in a shorter time than in a solutron at rest. However, difficulties are ex rienced' in the present methods of circulating the solution, due to the tendency of mechanical vibrations to start parasitic crystals and in the case of corrosive solutions to the tendency of these solutions to attack the pumping or circulating mechanism and conducting pipes. Moreover, if the solution moves only in one direction, there is a tendency of the crystals to grow larger on the sides from which the current is flowing as the saturated solution reaches those sides first.

I have found it particularly advantageous to grow large clear crystals from a crystallizing solution while it is in a to and fro movement in relation to the growin c stal. In other words the crystal is maintalne sub stantially stationary in the direction of flow of the solution, that is, relative to the flow of the solution over the same. This method secures a comparatively rapid growth Without distortion or irregular development of the crystal.

The progressive saturation of the solution necessary for the production of crystals may be produced either by evaporation of the sol-.

vent at a constant temperature, or by lowering the temperature without evaporation or by a-combination of both. I prefer to produce the .crystals by lowering the temperature of the solution because of its convenience, but the methods hereinafter outlined are equally a plicable if the evaporation method is emp oyed or a combinationiof the two.

I have also found that clear perfect crystals may be grown more rapidly by maintaining a predetermined hydrogen ion concentration not in the-neutral range, which of course, can

be controlled by the addition of a suitable acid or alkali. However, it will be understood that the hydrogen ion concentration must be such that the crystalline material in solution will not be precipitated. For the eflicient production of clear Rochelle salt crystals I have found that the addition of an alkali, such as sodium or potassium hydroxide, for example, corresponding to a. onetenth normal solution of sodium or potassium hydroxide is advantageous in promoting the relatively rapid growth of clear crystals.

Since not only the speed of growth but also the shape and characteristics of growth of the crystal are influenced by the amount of the to and fro movement of the solution past the crystal being formed, it is essential to produce this to and fro movement in such a manner that it may be easily adj ustcd to the production of desired crystal characteristics. One of the most efficien't means of doing this is by subjecting the trays containing the solution to a slow rocking motion, the amount of which is governed by the type of crystal that it is desired to produce from a certain type of seed. For example, if a crystal is desired having the C or major axis long with respect to the B or minor axis at right angles to the major axis, the rocking should be in such a direction that the solution will flow back and forth parallel to the C axis, in which case a crystal will be produced having the C axis relatively long as compared with the B axis.

Furthermore, two crystals grown from substantially indentical seeds under identical conditions except that the rocking is greater in one case than in the other, will develop so that the one subjected to the greater rocking will be longer on the axis parallel to the direction of rocking than the other one.v If, for

example, the rocking takes place so that the solution flows back and forth in the direction of the B axis, the tendency is to increase the dimension of the crystal being grown in the direction of the B axis. Furthermore, if the depth of the crystallizing solution is not too great, and if the rocking is of an amount great enough so that the top of the crystal is left uncovered during a portion of the time, growth in the direction of the upright axis may be largely suppressed, yielding a flatter type of crystal.

Another advantage of the rocking is that if the cycle of movement is long enough the solution reverses itself very gradually and the tendency to produce ripples and high frequency agitations in the solution is reduced to a minimum. It is moreover desirable to produce the rocking by a slow uniform sinusoidal movement whereby the reversal of direction will take place very gradually so that there will be a minimum tendency to produce shocks or ripples in the solution. Means must also be provided for keeping the vibrations of the actuating mechanism of the rocker from reaching the crystallizing vessel.

The following is a description of the apparatus and method used in producing large clear crystals according to my method.

In Figure 1 is shown a vertical cross section of the apparatus used for production of the crystals.

In Figs. 2 to 4 are shown the plan views of crystals grown with the minor axis or B axis parallel with the movement of the solution.

In Fig. 5 is shown a plan view of a'crystal grown with the major axis or C axis parallel with the movement of the solution. 7

Figs. 6 and 7 are perspective views of two types of crystal grown by my process.

Fig. 8 is a diagrammatic view of the heating element and thermostat.

In Fig. 1 is shown a tray 1 which contains the erystallizing solution 2 and in which are mounted the seeds 3a from which the crystals 3 are grown. The tray is preferably covered with a suitable transparent cover 4 such as a sheet of glass which is supported on a suitable gasket 5, such as thick sponge rubber so that the tray is substantially airtight. The glass may be held into close contact with the gasket 5 by any suitable means such as weight 6. The tray 1 is preferably mounted on suit able supports such as long angle iron supports 7, which are supported above the bottom of the box 8 by suitable members 9 so that the heating and temperature regulating apparatus may be mounted under the tray.

The top 10 of the box is preferably provided with an observation window 11 and the top is readily removable for access to the trays. The trays are preferably supplied with heat by any suitable means such as the electric heating element 12 which is disposed near th bottom of the box. The heat is supplied to replace heat lost by radiation so that the temperature may be controlled. The temperature is preferably automatically controlled by a suitable adjustable thermostat 13. A thermometer 14 may be provided for observing the temperature. The thermostat is indicated diagrammatically as this construction forms no part of this invention. A knob 15 on the rod 16 is shown for regulating the thermostat.

The box surrounding the tray is carefully insulated with cork or other suitable insulatlng material so that the temperature of the trays may be substantially uniform.

The box 8 is supported by a suitable platform 17 which in turn is mounted on bearings 18 which engage the shaft 19. The platform is given a rocking motion by the eccentric 22 which causes the rod 20 to move back and forth and this gives the platform a rocking motion by means of the arms 21 which are connected to the platform and to the rod 20. The eccentric 22 may be actuated by any suitable means such as an electric motor 23 and reducing gears 24.

The production of large clear Rochelle salt crystals in this rocking apparatus is described hereinafter as an example of how the apparatus may be used for crystallization by the to and fro movement of a crystallizing solution and a lowering of the temperature of the same whereby the desired precipitation may be obtained.

The box or oven containing the thoroughly cleaned and covered trays is first heated to predetermined temperature, for example, about 35. degrees C. and held at this temperature until conditions have become constant.

A filtered Rochelle saltsolution made alka-' line corresponding to about 0.1 normality of sodium or potassium h droxide and containing enough Rochelle sa t to be slightly supersaturated at 35 degrees C. is heated to at about 50 or 55 degrees C. and then poured into the trays and allowed to cool slowly by having the oven open and the heat shut off. It is desirable to pour the solution into the trays at a temperature above the saturation temperature to prevent the formation of accidental crystals. Such crystals if formed at the pourin of the solution, for exam 1e by dust partic es fallin down on the sur ace of the solution, are rapidly dissolved on account of the high temperature. Moreover, it is also preferable to have the trays covered during the cooling period so as to protect the surface of the solution from the settling of dust particles and to prevent evaporation.

In order to start the rowth of the crystals, pieces of the crystal ine material usually known as seeds are planted in the solution on the bottom of the tray, when the temperature has dropped for example to 5 or 10 degrees C. above the saturation temperature of the solution, i. e. to about 40 or 45 degrees C. for the above solution. To avoid cracking of the seeds at the planting they are preferably preheated to the planting temperature.

The exact amount of temperature above the saturation temperature at which the seeds are planted depends upon the rate of cooling of the solution, since if the seeds are subjected too long to the unsaturated solution they will entirely dissolve. It is preferable to plant the seeds at a temperature sufiiciently high to dissolve a small part of the seeds while the solution is cooling down to the saturation temperature. The reason for this is that when the surface of the seed is slightly dissolved before it begins to grow, the seed and the or stal grow together more intimately. oreover, if the surface of the seed is slightly dissolved, small parasitic crystals 'that may have been formed at the planting also are dissolved and thereby irregular crystallization avoided.

After planting, the trays are covered so as to maintain an atmosphere saturated with moisture above the solution and prevent evaporation.

When the temperature of the solution has dropped to the saturation temperature, or to slightly above this temperature, the top of the oven is put on and the heat turned on, and the saturation temperature maintained for some time, for example, 6 to 12 hours, or until conditions in the solution are in equilibrium.

At this time a very slow reduction of the solution temperature is begun. The exact amount of this reduction depends upon the concentration and volume of the solution and the number and size of the seeds. For example, if 20 seeds of about 5 grams are planted in a Rochelle salt solution of a specific gravity of 1.380 at 60 degrees C., and having a volume of 20 liters, the temperature may be dropped about 0.2 degrees C. the first day. As the crystals grow larger the temperature maybe dropped by a greater amount each day. or example, if crystals weighing about one pound apiece are produced in three weeks, the rate of temperature drop may be increased until at the last it is about 1.5 degrees per day, thus reducing the time required to grow the crystals to the desired size. If larger crystals aremade, say two pound crystals, the rate of temperature drop may be increased still further. This increase is a functionof the crystal surface per liter of solution.

The temperature drop is accomplished either by turning the thermostatic control knob 15 by hand at suitable intervals or by any suitable automatic mechanical device, for example, a timing mechanism.

It may also be noted that the heat is supplied beneath the tray containing the solution so that the lower portion of the solution will have a temperature slightly higher than the upper portion of the solution, and this is advantageous because it overcomes a tendency of the crystals to grow more rapidly at the bottom and raise themselves in the solu tion on an irregular crystalline formation.

When the crystals are of the desired size they are taken out, wiped oil with a soft cloth and if further cleaning is desired rinsed in dilute alcohol.

Crystals of a predetermined shape may be obtained from a crystalline fragment or seed. For example, by planting a seed, so that a plane going through its major or C axis and its minor or B axis isparallel with the bottom of the tray, a half developed crystal as shown in Fig. 6 is produced. On the other hand, a fully developed crystal or complete or stal is formed if the seed 3c is planted so that a plane through its A and B axis is parallel to the bottom of the tray, as in Fig. 7. The pro ortions of the so formed crystal are greatly influenced by the proportions of the seed from which the crystal isf grown. For

example, a seed that is two inches long will long crystal from a short seed and a short or wide crystal from a comparatively long seed.

Figs. 2 and 3 illustrate two crystals grown from identical seeds. In Fig. 2 the C axis is longer than the B axis, while in Fig. 3 the C axis is shorter than the B axis. This difference in the proportions of the crystal is due to the rocking to which the crystalline solution was subjected. Fig. 2 illustrates the effect of a small rocking motion parallel with the B axis and Fig. 3 the effect of a large rocking motion. Thus rocking tends to increase the proportions of the crystal that are parallel with the movement. This fact can be utilized for making square, very wide or very long crystals. Fig. 4 illustrates a comparatively wide crystal grown from a long seed 36. Fig. 5 shows a long crystal grown from an identical seed with the C axis parallel with the movement.

The production of crystals of desired proportions and orientation of crystalline axes is facilitated by the use of seeds of predetermined dimension and orientation which can be located in the trays with their axes in the desired relation to the direction of rocking.

It will thus be seen that by this method, I have provided an efiicient procedure for controlling the growth and production of large solid clear Well developed crystals of desired form.

Furthermore, it is to be understood that the particular forms of apparatus shown and described, and the particular procedure set forth, are presented for purposes of explanation and illustration and that various modifications of said apparatus and procedure can be made without departing from my invention as defined in the appended claims.

What I claim is:

1. The method of producing clear solid crystals, which consists in planting pieces 'of crystalline material in a concentrated solution of the crystalline material, imparting to the solution a movement backward and forward with respect to the pieces of crystalline material while maintaining said pieces substantially stationary relative to the flow of the solution thereover, and causing the so lution to crystallize by permitting the temperature of the solution to drop.

2. The method of producing clear solid crystals of Rochelle salt, which consists in inserting pieces of crystalline material in a Rochelle salt solution imparting to the solution a motion relative to the pieces of crystalline material while maintaining said pieces substantially stationary relative to the flow of the solution thereover, and keeping the solution supersaturated.

3. The method of producing clear solid crystals, which consists in placing pieces of crystalline material in a solution of isomorphous crystalline material, causing the solution to have a to and fro motion with respect to said pieces while maintaining said pieces substantially stationary relative to the flow of the solution thereover, and keeping the solution supersaturated.

4. The method of producing clear solid crystals, which consists in placing pieces of crystalline material in a solution of the said material, causing a motion of the solution toward and from said pieces while maintaining said pieces substantially stationary relative to the flow of the solution thereover, and lowering the temperature of the solution at a progressively increasing rate, whereby the desired degree of supersaturation of the solution is maintained.

, 5. The method of growing Rochelle salt crystals, which consists in planting pieces of crystalline material in a solution of R0- chelle salt rocking the solution while maintaining said pieces substantially stationary relative to the flow of the solution thereover, and causing the solution to crystallize.

6. The method of growing Rochelle salt crystals, which consists in placing pieces of crystalline material in a concentrated solution of Rochelle salt, rocking the solution while maintaining said pieces substantially stationary relative to the flow of the solution thereover, and automatically lowering the temperature in progressively increasing amounts.

7. The method of growing crystals, which consists in placing pieces of crystalline material in a concentrated solution of the crystalline material, imparting movement to the solution in a direction parallel to certain axes of the pieces of crystalline material supplying heat to the solution, and automatically reducing the temperature at the desire-d rate.

8. The method of growing solid clear crystals, which comprises placing pieces of the crystalline material in a solution of the crystalline material, imparting a to-and-fro motion to the solution while maintaining said pieces substantially stationary relative to the flow of the solution thereover, and causing crystallization of the material by decreasing the temperature of the solution, whereby only regular crystallization occurs as the supersaturation of the solution tends to increase and solid clear crystals are formed.

9. The method of producing crystals, which consists in placing fragments of crystalline material in a concentrated solution, causing the solution to move to and fro with respect to the fragments at relatively rapid intervals while maintaining the fragments of crystalline material substantially stationary relative to the flow of the solution thereover, and causing progressive supersaturation of the solution.

10. The method of producing clear solid crystals of Rochelle salt, which consists in inserting crystalline material in an alkaline Rochelle salt solution, and causing the solution to crystallize.

11. The method of producing. clear solid crystals, which consists in inserting homogeneous crystalline material in an alkaline solution of the crystalline material, imparting to the solution a to-and-fro motion in a predetermined direction relative to the er stalline material, maintaining the c stalhne material substantially stationary re ative to the flow of the solution thereover, and keeping the solution supersaturated.

12. The method of producin clear solid crystals of Rochelle salt, whic consists in inserting seeds of crystalline material and of predetermined direction and orientation in a Rochelle saltsolution of a predetermined hydrogen ion concentration, rocking the solution in a direction parallel with certain of r the axes of said seeds, maintaining the seeds substantiall stationary relative to the flow of the solution thereover during the rocking of the solution and causing the solution to crystallize.

13. The method of producing crystals, which consists in placing pieces-of crystalline material in a solution of the crystalline material which is at a temperature above saturation temperature, reducing the'temperature at least to the saturation oint, and-then rocking the solution in the irection of certain axes of the pieces of crystalline material.

14. The method of producing crystals, which consists in placing pieces of crystalline material in a solution-of the crystalline material which is at a temperature above the saturation point, imparting a movement to the solution 1n the direction of certain axes of the pieces of crystalline material, permitting the pieces of crystalline material to partially dissolve in the solution, rapidly reducing the temperature of the solution to the saturation point, and slowly reducing the tem erature thereafter.

15. T e method of growing Rochelle salt crystals, which consists in placing pieces of crystalline material in a concentrated solu? tion of Rochelle salt, rocking the solution in the direction certain axes of the pieces of crystalline material while maintaining said pieces substantially stationary relative'to the bottom of the tray and as to the flow of the solution thereover, and lowering the temperature in' progressively increasmg amounts.

'16. The method of growin crystals, which consists in planting pieces 0 crystalline material in a solution of the crystalline material at a predetermined temperature above the saturation temperature, rocking the solution in the direction of certain axes of the ieces of crystalline material, cooling the soution to t e saturation temperature, and then reducing the temperature of the solution from this point at a predetermined rate.

17. The met 0d of growing Rochelle salt solution of the material ina heat" insulated v chamber, supplying heat and maintaining the lower portion of the solution at a slightly higher .temperature than the upper part of the solution, and imparting to the solution a to and-fro movement in the direction of certam axes of the crystal being grown while maintaining the crystal substantially stationary relative to the flow of the solution thereover.

In testimony whereof I afiix my signature.

BENGT KJELLGREN.

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