US2790731A

US2790731A - Method and apparatus for the production of electrically resistant films

Info

Publication number: US2790731A
Application number: US398000A
Authority: US
Inventors: Ostrofsky Bernard; Ballard James William
Original assignee: Commonwealth Engineering Company of Ohio
Current assignee: Commonwealth Engineering Company of Ohio
Priority date: 1953-12-14
Filing date: 1953-12-14
Publication date: 1957-04-30
Anticipated expiration: 1974-04-30

Description

Apnl 30, 1957 a. OSTROFSKY ETAL 2,790,731

METHOD AND APPARATUS FOR THE PRODUCTION 0F ELECTRICALLY RESISTANT FILMS Filed Dec. 14, 195:: 2 Sheets-Sheet 1 III 'Q'.\III Illllllllllll INVENTORS BERNARD OSTROFSKY' JAMES w. BALLARD' BY 0- v- ATTORNEYS P" 30, 1957 B. OSTROFSKY arm. 2,790,731

METHOD AND APPARATUS FOR THE PRODUCTION 0F ELECTRICALLY RESISTANT FILMS Filed Dec. 14, 1953 2 Sheets-Sheet 2 United States Patent METHOD AND APPARATUS FOR THE PRODUC- TION OF ELECTRICALLY RESISTANT FILMS Bernard Ostrofsky and James William Ballard, Dayton, Ohio, assignors to The Commonwealth Engineering Company of Ohio, Dayton, Ohio, a corporation of Ohio Application December 14, 1953, Serial No. 398,000

15 Claims. (Cl. 117-107) This invention relates to the production of electrically resistant films and to apparatus and methods for attaining the same. More particularly the invention relates to the production of electrically resistant elements by the thermal decomposition of chromium hexacarbonyl from the vapor state to produce chromium containing deposits of a low temperature coefficient of resistance upon ceramic insulating material.

A primary object of the invention is the provision of a novel method of gas plating ceramic bases.

An important object of the invention is the provision of novel apparatus useful in carrying out the methods of invention.

Another and a principal object of the invention is the provision on ceramic bases of novel electrically resistant chromium hexacarbonyl is employed. This carbonyl is 99 percent volatilizable, only about 1 percent of the weight of the material forming a residue.

commercial'variety, by subliming the same at about 100 C. and collecting the volatilized vapors on a cold, clean The carbonyl is at tained by purifying hexacarbonyl samples, such as the surface. The collected samples will be found to be particularly useful'in this invention in the attainment of the temperature ranges stated.

erence to the following detailed description and accompanying drawings wherein:

The invention will be more fully understood by ref- Figure 1 is a view illustrating apparatus useful in the practice of the invention;

Figure 2 is a view of a portion of the apparatus of Figure 1; v

Figure 3 is another view of a portion of the apparatus of Y Figurel;

Figure 4 is a plan view of a portion of the apparatus of Figure l; and

Figure 5 illustrates a completed resistant element hav ing terminal bands and leads fitted thereto.

Referring to the drawings there is shown in Figure 1 2,790,73l Patented Apr. 30, 1957 ICE.

top of the closure member the same is provided with six glass protuberances each of which has sealed therethrough a tungsten electrode. These electrodes are conveniently provided in pairs indicated respectively at 5, 7; 9, 11; and 13, 15.

For purposes hereinafter described the

electrodes

13, 15 may be considered as spares utilizable to take any desired measurement and not necessary to the practice of the invention. The electrodes themselves extend well down into the vessel 1 and the lower end of each is provided with an electrically conductive collar of brass having an aperture through which the electrode passes vertically; each collar also is provided with a threaded passage in which a set screw is engaged in contact with the electrode to securely hold the collar in position on the electrode.

A second threaded passage is provided in each collar for the passing of a second set screw which communicates with a second aperture in which electrical leads are secured by the set screws. These collars will be referred to more particularly hereinafter.

Collars

17, 19 on the upper ends of the electrodes 9, 11 are connected to a 6.3 source of A. C. voltage; at the lower ends of these electrodes a coil of nichrome wire 21 is connected to the electrodes by set screws on

collars

20, 22, respectively. This coil is adapted to receive thereover a tubular ceramic member 23 having a length of about 1 inch and a diameter of inch which is to be plated with the film deposited from the vapors of the chromium hexacarbonyl. A second and smaller tubular ceramic piece 25 is retained on the coil 21 in adjacent relationship to the member 23. Secured against the piece 25 is the hot juncture 27 of a Chromel-Alumel thermal couple the cold ends of which are respectively connected to

collars

29, 31 on

electrodes

5, 7, the leads being retained by set screws threaded into the collar.

The upper ends of

electrodes

5, 7 have connected thereto a milli-volt meter (not shown) and the voltage developed between

electrodes

5, 7 is accordingly a measure of the temperature at the ceramic material 25 and also 27 which is closely adjacent to the member 23. Such equipment for temperature measure is not described in further detail herein since the practice and equipment involved are well known standard industrial procedures.

The closure member 3 above the mouth of the vessel 1 is also provided on opposed sides thereof with tubular laterally extending

arms

33, 35 which communicate with e the hollow interior of the member 3 and accordingly with the interior of the vessel 1 (Figure 1).

Arm 33 is provided with a three-way (glass) valve 37 which permits of connecting the arm and accordingly the vessel 1 with the atmosphere through the conduit 39; the arm 33 may also be connected through valve 37 with arm extension 41, the lower end of which is provided with a ground glass surface secured to an upper ground glass surface of conduit 43; or valve 37 may be closed to seal oh" the arm 33 and the vessel 1 from the atmosphere and conduit 43 at the same time.

Conduit 43 has the lower end thereof closed to define a receiver contained in a trap, which trap comprises a casing 45. Casing 45 and the receiver have therebetween a cooling medium, preferably a mixture of Dry Ice and acetone, and the trap functions to eifectively condense and retain vapors passing through the conduit 43.

Conduit 43 above the trap is connected to a pump 47 through line 49, the pump when driven by motor 51 being effective to create a vacuum pressure to occasion the control of gases through conduit 43 and arm extension 41 from the vessel 1.

Extending rightwardly from the closure member 3 as shown in Figure 1 arm 35 is provided with a valve 53 and the lower end of arm extension 55 has a ground glass surface which is securable with the upper ground glass surface of a container 57.

In order to securely and removably position container 57 on the arm extension 55 projections indicated at 59, 59' are provided on arm 55 and

projections

61, 61 are provided on container 57, and rubber bands may be extended between arms to securely and removably retain the container in association with the arm extension.

Container 57 is provided in the base thereof with a supply of substantially pure chromium hexacarbonyl in solid form. In actual practice it has been found that chromium hexacarbonyl which leaves a solid residue of approximately one percent by weight is entirely suitable for the practice of the invention. The carbonyl when heated to about l C. volatilizes readily and when the vaporized material is brought into contact with a surface heated to a temperature in the range of 125 to 200 C. the composition decomposes to produce a metallic deposit.

Conduit 63 of glass is positioned between closure member 3 and valve 53 and is connected by suitable means such as rubber hosing 65 to a manometer indicated genorally at 67. This manometer is of standard construction, provided with mercury and is adapted to indicate low pressures, and it is not considered necessary to specifically describe the manometer in detail since the same is merely an indicating instrument in the process of invention and the procedures of employing the same are well known, but it may be noted for the sake of clarity that the manometer tubings are mounted on a board 69, the longer mercury column being contained in the left tubing 71 (Figure 1), the shorter column being in tubing 73 which is connected to tube 75 provided with valve 77; the horizontal tubing connected to valve 77 is closable at the left hand end (Figure 1). Gas pressure exerted through conduit 65 accordingly passes through column 75 to alter the height of the column of the manometer when valve 77 is open. Normally in the practice of the invention valve 77 is maintained open at all times.

Brackets, portions of which are indicated at 79, S1 suitably and adjustably support the vessel 1 and conduit 43. Positioned below the vessel 1 and the container 57 is a receptacle 83 which is adapted as a water bath and which may be heated by gas flame indicated at 85, the Water, in the practice of the invention, being brought to practically 100 C., that is the boiling point. The bath is suitably supported by bracket 87 and may be raised or lowered to immerse the vessel 1 and the closure member 3 in such manner that the

arms

33, 35 and the vessel 57 are completely within the bath.

In the practice of the invention the apparatus is connected as shown in Figure l with valve 37 open to the conduit 43 and valve 53 open to the container 57, the ceramic workpiece 23 being supported on the Nichrolne wire 21. In this condition the vacuum pump is operated to completely clear the system of air. At the same time the 6.3 volt A. C. source is connected across the electrodes 9, 11 to supply thereto a current which heats the coil element 21 and thereby also heating the ceramic member 23 and the ceramic piece 25. This heating takes place preferably as the evacuation occurs in order that any oceluded gases included in the ceramic material may be expelled from the system. The ceramic materials themselves are cleaned prior to their introduction into the vessel 1 the cleaning being effected in any suitable manner known to the art as with alcohol.

When the apparatus has been substantially completely exhausted of gases the valve 53 is closed and the vessel 1 and container 57 are lowered into the water bath to such an extent that the

arms

33 and 55 are substantially completely covered by the water, which has in the meanwhile been heated to about 100 C. Valve 37 is at this time open to conduit 43 and the motor and pump continue to operate and accordingly any further material which .may be contained, for example, in the vessel 1 is expelled by the heating. Also the heated water occasions a development of a high vapor pressure in the container 57 and. the arm extension 55, but the gases cannot pass the tightly fitting glass valve 53.

When the temperature of the

ceramic pieces

23, 25 as indicated by the terminal couple positioned at 27 have reached a temperature of approximately 150 C. valve 53 is opened to admit to the vessel 1 and the hollow closure member 3 vapors of chromium hexacarbonyl. Prior to opening valve 53 valve 37 is closed to shut off arm 33 from the atmosphere and the arm extension 41. The conduit 63 however is open and some very slight condensation of chromium hexacarbonyl may appear on the glass wall of this conduit, this is not however of serious eflFect.

When the pressure within the vessel 1 and closure member 3 has reached a point of one-half centimeter of mercury valve 53 is closed to prevent further ingress of carbonyl to the vessel 1. Then with the substantially static atmosphere of carbonyl in the vessel the same is maintained in the water bath for a period of five minutes. During the course of this period the carbonyl decomposes depositing a film over the ceramic member 23 which due to its suspended condition and the uniform heating of the closely wound coil 21 is uniformly coated with the deposit. The deposition which also takes place to some extent upon the piece 25 is not deleterious to the temperature measurement.

In this connection it is to be noted that the prime requisite is that the temperature of the ceramic pieces be brought to a temperature within the range of 125- 200 C. prior to the introduction of the carbonyl and that the heating be continued at substantially the same rate during the deposition. As the carbonyl decomposes the pressure as indicated by the manometer 67 will be observed to increase slightly as gaseous products of the decomposition, such as C0, are formed.

At the termination of five minutes in the above specific example the valve 37 was opened to connect the arm 33 to the pumping apparatus and the same was evacuated of substantially all gases. The vessel 1 and container 57 were removed from the water bath and valve 37 was operated to connect conduit 39 and the atmosphere with the arm 33 and the vessel 1. The closure member 3 and the ceramic piece suspended from the electrodes were then removed from the vessel. Upon removal and cooling to room temperature the coated ceramic tubular member 23 is provided, as shown in Figure 5, with silver terminal caps 89 and 91 having axial terminal leads 93 and 95, respectively; substantially negligible contact resistance is thus achieved.

The resistance of the ceramic tubular base member, which has a length of about 1 inch and an outside diameter of about of an inch, was found to be about 140.6 ohms at room temperature or 27.7 C.

The same procedure described above was then repeated with a new ceramic member, with the exception that valve 53 was closed off when the manometer indicated a pressure of 2 centimeters of mercury in vessel 1. The resistors produced at 27.7 C. had a value of 5.31 ohms.

Resistors produced under varying conditions of time were checked for the effect of higher temperature on resistance characteristics. This was done by placing the resistors in an oven, the resistors having leads of suitable length soldered thereto to permit extension of the leads through a small opening in the oven.

The method employed is standard practice and need not be discussed in detail, but it should be noted that each resistor was held at a given elevated temperature for one hour before measuring the resistance. By way of example, the resistance which measured 5.31 ohms at 27.7 C. had a value of 5.33 ohms at 65 C., and a value of 5.35 ohms at C. Upon cooling again to 28.9 C. the resistance exhibited a value of 5.31 ohms again indicating a high degree of stability in the resistance of the deposited coating.

Similar tests were made with the same resistors at temperatures below the freezing point and the resistance of the coating at minus 15 C. was found to be 5.33 ohms, and at minus 55 C. the resistance was 5.26 ohms. Upon return to a temperature of 22 C. the resistance was found to be 5.33, further illustrating high stability in the coating.

The average temperature coeflicient of resistance was then found by determining the temperature coeflicient of resistance at each temperature with respect to room temperature and then averaging the coefficients for each of the above specifically set forth temperatures.

Similar data was prepared for a variety of resistors produced by varying the time and the pressure conditions in vessel 1 and the following data was secured for a series of resistors:

It is to be noted that the resistors which exhibit the above characteristics of low temperature coefficient of resistance over a relatively wide temperature range are .a dull gray or gray black in color and thus are not the shiny mirror surfaces which are frequently characteristic of gas plated articles.

'Ihe depth of coating is controllable by controlling the time of exposure of the ceramic base to the hexacarbonyl atmosphere; a longer time gives a greater coating depth as long as sufficient carbonyl is present to deposit. Control is also effected by control of the hexacarbonyl pressure in vessel 1 and increased pressure contributes to an increased depth and vice versa. Increasing the temperature increases the rate of plating and accordingly the depth attainable in a given time. Time, temperature and pressure are accondingly correlative factors, each of which may be varied to permit the attainment of particular resistance values.

The carbonyl pressure attained upon opening of valve 53 should be low and generally it has been found that pressure of /2 centimeter to 2 centimeters of mercury are very effective, although pressures outside of this range are useful under particular time and temperature conditions.

The temperature of the ceramic material preferably is between 125 and 200 C.; below 120 C. very little plating occurs and above 200 C., that is at about 205 C., the plating tends to become non-uniform, resulting in poorer products. The optimum temperature is about 150 C. in the method described.

The ceramic pieces may be masked to provide particular patterns on the resistors, as for example, a spiral formation if desired. Further the films may be mechanically cut to etfect control over the resistance value of a resistor. Such processes generally are known.

The films deposited on the ceramic base are bonded well and permanent. The value of the temperature coefficient of resistance is as noted about 0.01 percent/ C. and for many applications the temperature coeflicient may be considered to be substantially zero.

It will be understood that this invention is susceptible to modification in order to adopt it to different usages and conditions and accordingly, it is desired to comprehend such modifications within this invention as may fall within the scope of the appended claims.

We claim:

1. A gas plating process which comprises the steps of introducing volatilized chromium hexacarbonyl at a temperature below the decomposition temperature thereof into a plating chamber into contact with a ceramic base to be plated, heating the base to the decomposition temperature of chromium hexacarbonyl to cause a film to be deposited on said base by thermal decomposition of the carbonyl, and during the decomposition surrounding the plating chamber with a fluid medium heated to a temperature of approximately C. and above the volatilization temperature of the carbonyl. v

2. A gas plating process which includes the step of surrounding the chamber in which the plating is effected with a fluid heated to a temperature of approximately 100 C. and above the volatilization point of the plating gas.

3. The method of plating which comprises the steps of enclosing a plating chamber in a fluid heated to a temperature of boiling water and above the vaporization point of chromium hexacarbonyl, and contacting a heated ceramic base material within the chamber with heated;

chromium hexacarbonyl vapors to effect thermal decomposition of the carbonyl and deposition of an electrically resistive coating of chromium on the base.

4. The method of plating as in claim 3 which comprises the steps of enclosing a plating chamber in a water bath heated to about 100 C., and contacting a ceramic base material which is electrically resistance heated to a temperature in the range of -200 C. with chromium hexacarbonyl vapors heated to just below the decomposition temperature thereof to eflect thermal decomposition of the carbonyl and deposition of an electrically resistive coating of chromium on the ceramic base.

5. The method of plating as in claim 4 which comprises the steps of enclosing a plating chamber in a water bath heated to about 100 C. and contacting a ceramic base material which is electrically resistance heated to a temperature of about C. with chromium hexacarbonyl vapors heated to just below the decomposition temperature thereof to effect thermal decomposition of the carbonyl and deposition of an electrically resistive coating of chromium on the ceramic base.

6. The method of gas plating which comprises the steps of inserting a ceramic base material within a plat ing chamber, which is connected for the selective passage of fluid between the plating chamber and an enclosed source of solid chromium hexacarbonyl, immersing the chamber and enclosed source of chromium hexacarbonyl in a fluid heated to a temeprature above the volatilization temperature of the chromium hexacarbonyl, heating the ceramic base material by passing electric current therethrough to a temperature in the range of between about 125 C. and 200 C., and then contacting the heated ceramic base material with vapors of chromium hexacarbonyl volatilized by the immersion of the solid chromium source.

7. A gas plating process for the production of electrically resistant films which process comprises surrounding the combination of a chamber having suspended therein a ceramic base material and communicating therewith an enclosed source of chromium hexacarbonyl with a fluid bath which is heated above the volatiliaztion point of the chromium hexacarbonyl, heating the ceramic base material while it is within the plating chamber to a temperature between about 125 and 200 C., introducing chromium hexacarbonyl volatilized by the heat of the fluid into contact with the heated base material while limiting the pressure of the chromium hexacarbonyl within the chamber.

8. A gas plating process for the production of electrically resistant films which process comprises surrounding the combination of -a chamber having therein a ceramic base material and an enclosed source of chromium hexacarbonyl with a fluid bath which is heated. above the volatilization point of the chromium hexacarbonyl, heating the ceramic base material to a temperature between about 125 and 200 C., introducing chromium hexacarbonyl volatilized by the heat of the fluid into contact with the heated base material while limiting the pressure of the chromium hexacarbonyl within the chamber to a pressure Within the range of about /2 to 2 centimeters of mercury.

9. The gas plating process which comprises the steps of heating the ceramic base material contained in the plating chamber to a temperature above the decomposition point of chromium hexacarbonyl, surrounding the chamber with a fluid bath heated to a temperature above the volatilization point of chromium hexacarbonyl, and contacting the heated ceramic base material with a static heated atmosphere of chromium hexacarbonyl.

10. A gas plating process which includes the steps of immersing a plating chamber and communicating chamber containing chromium carbonyl in a heated fluid bath, and depositing a film of chromium on an electrically non-conductive base by heating the same in a static atmosphere of chromium hexacarbonyl to a temperature causing thermal decomposition of said chromium hexacarbonyl and deposition of chromium onto said base, and removingthe resultant chromium coated base from the decomposition zone.

11. In a gas plating process the steps of supporting a ceramic body axially on a heating element in a plating chamber, heating the element by electrical resistance to the decomposition temperature of chromium hexacarbonyl, surrounding the plating chamber with a fluid medium heated to a temperature above the volatilization point of chromium hexacarbonyl, and contacting the heated ceramic body in a static atmosphere of chromium hexacarbonyl.

12. In apparatus for gas plating, in combination, a plating vessel, a temperature bath, means to suspend a body to be plated in said vessel, means to substantially close said vessel, means to supply an atmosphere of a plating gas to said vessel, and means to support said vessel in said temperature bath.

13. In apparatus for gas plating, in combination, a plating vessel, a temperature bath, means to suspend a body to be plated in said vessel, means to heat a body suspended in the vessel, means to substantially close said vessel, means communicable with the vessel to supply a plating gas thereto, and means to support said vessel and supply means in the temperature bath.

14. in apparatus for gas plating, in combination, a plating vessel, a closure member for the vessel, said member having electrodes passing therethrough, a heating coil element adapted to receive thereover a rectangular tubular object to be plated, means to pass an electrical heating current through said element, container means connected to said plating vessel for holding chromium hexacarbonyl, means for heating said container and plating vessel, and means for flowing heat decomposable chromium hexacarbonyl gas into said plating vessel and into contact with said tubular object to be plated.

15. In apparatus for gas plating, in combination, a plating vessel, a closure member for the plating vessel, said closure member having tubular arm means extending therefrom, a temperature bath, means to enclose a source of a plating gas connected to said tubular arm means for supplying an atmosphere of plating gas to said arm means and vessel, and means to immerse said vessel and arm means in said temperature bath.

References Cited in the file of this patent UNITED STATES PATENTS 1,717,712 Loewe June 18, 1929 1,964,322 Hyde June 26, 1934 2,344,138 Drummond Mar. 14, 1944 2,357,473 lira Sept. 5, 1944 2,516,058 Lander July 18, 1950 2,552,626 Fisher et al. May 15, 1951 2,602,033 Lander July 1, 1952

Claims

1. A GAS PLATING PROCESS WHICH COMPRISES THE STEPS OF INTRODUCING VOLATILIZED CHROMIUM HEXACARBONYL AT A TEMPERATURE BELOW THE DECOMPOSITION TEMPERATURE THEREOF INTO A PLATING CHAMBER INTO CONTACT WITH A CERAMIC BASE TO BE PLATED, HEATING THE BASE TO THE DECOMPOSITION TEMPERATURE OF CHROMIUM HEXACARBONYL TO CAUSE A FILM TO BE DEPOSITED ON SAID BASE BY THERMAL DECOMPOSITION OF THE CARBONYL, AND DURING THE DECOMPOSITION SURROUNDING THE PLATING CHAMBER WITH A FLUID MEDIUM HEATED TO A TEMPERATURE OF APPROXIMATELY 100*C. AND ABOVE THE VOLATILIZATION TEMPERATURE OF THE CARBONYL.