|Publication number||US2368306 A|
|Publication date||Jan 30, 1945|
|Filing date||May 2, 1941|
|Priority date||May 2, 1941|
|Publication number||US 2368306 A, US 2368306A, US-A-2368306, US2368306 A, US2368306A|
|Inventors||Kiefer Edwin F, Krellner Walter G|
|Original Assignee||Stackpole Carbon Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Referenced by (38), Classifications (7)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Patented Jan. 30, 1945 METHOD OF TREATING ELECTRODES Edwin F. Kiei'er and Walter G. Krellner, St.
Marys, Pa., assignors to Staclnmle Carbon Company, St. Marys, Pa., a corporation of Pennsylvania No Drawing. Application May 2,1941,
- Serial No. 391,551
comma. (or. 117-167) This invention relates to carbon electrodes and amethod of treating them to make them more durable, and more particularly to such electrodes for use in the electrolysis of aqueous solutions of v alkali metal halides.
For the above-mentioned purpose carbon electrodes, which include graphite electrodes, have in the past been impregnated with a. drying oil, such as linseed oil, which was then allowed or caused to dry or harden. the oil was to merely set the electrodes aside for several months, but of course thatmethod required a lot of time and space. The reason for treating electrodes with a drying oil is to make them more durable and resistant to the electrolytes in which they are used, but the difficulty with the methods used in the past has been that, in addition to requiring considerable time, the drying oil has not been entirely cured so that full advantage of the benefits of properly treated electrodes couldbe realized.
It is among the objects of this invention to provide a treated carbon electrode of this character which can be'rn'ade in a short time, which is more durable and has a longer and more useful life than similar electrodes known hereto fore, which does not spell or crumble during electrolysis, which corrodes more slowly and uniformly than heretofore, which materially reduces the fouling and plugging of alkali chlorine cells, and fromwhich the drying oil does not ooze or exude when the electrode is in service.
Another object is to provide a method for making such an electrode by which a uniform cure from batch to batch is obtained.
In accordance with thi invention a carbon electrode is impregnated with a drying oil of a character to be described presently, and is then heated at a temperature high enough to harden the oil into a gel which will remain solid or in situ even though the electrode later is heated to a temperature high enough to cause the gelatinized oil to smoke. Sucha gel is known as a temperature-irreversible gel. The drying oils P that can be used should be those that are susceptible to being cured in air at a high temperature to a state in which they will not ooze out of the electrode even though the electrodes are later heated to a temperature at which the oils will smoke. The electrodes are not subjected to such a high temperature in service, but it has been found that if the gelatinized oil will 1 not ooze out of the. electrodes when heated to a temperature at which they will smoke, the gel is temperature-irreversible and the electrodes at A common way of drying ice.
will have the long life and other desirable properties that it is the object of this invention to obtain. The smoke test thus is a convenient way of determining whether or not the electrodes will have the desired properties when placed in serv- Suitable oils for this purpose are linseed oil and oiticica oil, or mixtures of the suitable oils.
The electrodes are impregnated with the drying oil in any suitable manner, such as by the vacuum-pressure method or merely by soaking them in a, vat of hot or cold drying oil. The amount of drying oil that an electrode should contain is from about 4 to 9 percent by weight of oil. The percentage of oil can be controlled by the impregnating method employed and also by diluting the drying oil with a solvent or by using an emulsion of drying oil and water. For example, the electrodes may be impregnated in an autoclave by subjecting them to a vacuum of about 25 inches of mercury and then introducing the oil in sufilcient quantity to completely immerse the electrodes while under vacuum. The vacuum is then released and the electrodes allowed to soak in the drying oil at atmospheric or super-atmospheric pressure until they are saturated, whereupon the oil is removed from. the autoclave and a vacuum again applied to remove a portion of the oil from the pores of .the carbon. By controlling the conditions, such and thereby force a portion of the oil to the surface where it drains ofi.
A further manner of securing partial impregnation by a drying oil is to use either a solu-,
tion of oil in a solvent, or an emulsion of oil and water with a suitable emulsifying agent such as triethanolamine. The carbon electrodes a fully saturated with the oil solution or the oi emulsion after which the solvent or water is evaporated from the electrodes by reduced pressure, by heat or by a combination of both, the
amount of oil in the electrodes being controlled y the ratio .01 oil tosolvent or of oil to water.
A preferred procedure for producing our electrodes is to impregnate them by the vacuumpressure method with a solution consisting of about 60 per cent byweight of linseed oil and 40 per cent by weight of acetone. When the electrodes are removed from the impregnating autoclave they will contain from 11 to 15 per cent by weight of linseed oil-acetone solution. These electrodes are then introduced into a vacuum dryer where they are subjected to a vacuum. When the greater portion of the acetone is volaaseaaoe or the varieties of linseed oil can be used in practicing this invention, either alone or with the addition of dryers such as lead, manganese or cobalt compounds.
According to the provisions of the patent statutes, we have explained the principle and mode of practicing our invention and have detilized low pressure steam is admitted to the steam jacket of the dryer in order to completely temperature-irreversible gel, 1. e., one that will remain in situ and not ooze out of the electrodes even though they are later heated to a temperature high enough to cause the gelatinized oil to smoke. .In the case of electrodes impregnated with linseed oil as referred to above they are preferably gradually heated to a temperature of 260 C. and maintained at that temperature for about l5'hours to convert the oil from a liquid state to a substantially completely hardened or gel state. In effecting this transition of the oil both the chemical and physical properties are appreciably altered. For example, with linseed oil the acid value is greatly increased while the iodine value is decreased. Linseed oil can be cured in this manner when heated to a temperature between 200 and 350 C. by varying the heating time, a longer heating'period being required for the lower temperatures. The temperature range for properly curing oiticica oil is between about 225 and 350 C. However, the maximum temperature at which an oil is cured should be limited by volatilization of the 011 because, otherwise, all of the oil might be volatilized out of the electrodes. We prefer to limit ourselves to a temperature which will not result in a loss of more than 1 per cent of the weight or the electrode.
Electrodes prepared in accordance with this in-' vention have a. much longer service life and their performance in conventional types of chlorine cells is much better than electrodes treated by other known methods. Laboratory tests conducted in an electrolytic cell for the electrolysis of sodium chloride solution show a very pronounced improvement hi the life of our electrodes. Thus, electrodes treated with linseed oil in accordance with this invention showed an average loss or reduction in size of li of an inch per thousand hours as compared with 00 for untreated electrodes and 9in 'ior electrodes treated with linseed oil by the methods known heretofore. Any
scribed what we now consider to represent its best embodiment. However, we desire to have it understood that, within the scope of the appended claims, the invention may be practiced otherwise than as specifically described.
1. The method of treating a carbon electrode, comprising impregnating it with linseed oil and then curing the oil by heating the electrode in air at a temperature above 200 C. but below a temperature at which an appreciable amount of the oil will volatilize, whereby to convert the oil to a temperature-irreversible gel.
2. The method of treating a carbon electrode, comprising impregnating it with linseed oil and then heating the electrode in air at a temperature between 200 C. and 350 C. to cure it whereby to convert the oil into a temperature-irreversible gel, said oil constituting between 4 per cent and 9 per cent of the weight of the electrode.
3. The method of treating a carbon electrode, comprising impregnating it with linseed oil and then heating the electrode in air at a temperature between 200 C. and 350 C. long enough to set the oil into a temperature-irreversible gel.
4. The method of treating a carbon electrode, comprising impregnating it with boiled linseed oil and then heating the electrode in air at about 260 C. for about 15 hours to cure the oil and thereby harden it into a stable gel that is temperature-irreversible.
5. The method of treating a carbon electrode, comprising impregnating it with oiticica oil and then heating the electrode in air at a temperature between 225 C. and 350 C. long enough to set the oil into a temperature-irreversible gel.
6. The method of treating a carbon electrode, comprising impregnating it with a solution consisting of about per cent by weight oi linseed oil and about 40 per cent by weight of volatile solvent, volatilizing the volatile solvent from the electrode whereby the oil therein constitutes about 6 to 8 per cent oi. the weight of the electrode, and heating the electrode in air at a temperature of about 260 C. until the oil is converted from a fluid state to a temperature-irreversible gel.
' 7. The method of treating a carbon electrode comprising impregnating it with a drying oil from the class consisting of linseed and oiticica oils, and then curing the oil by heating the electrode'in air at a temperature above 200 C. but below a temperature at which an appreciable amount of the oil will volatilize whereby to convert the oil into a temperature-irreversible gel.
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US2522750 *||Nov 26, 1946||Sep 19, 1950||Lorraine Carbone||Method for preparing carbon brushes for electrotechnical purpose|
|US2774108 *||Sep 16, 1952||Dec 18, 1956||Gulf Research Development Co||Method of making low-resistance ion-exchange membranes|
|US2820728 *||Jun 21, 1955||Jan 21, 1958||Diamond Alkali Co||Method of treating carbon electrodes with polymerizable oil|
|US2881100 *||Jun 21, 1955||Apr 7, 1959||Diamond Alkali Co||Method of impregnating a carbon electrode with a drying oil|
|US2902386 *||Oct 22, 1956||Sep 1, 1959||Diamond Alkali Co||Carbon electrode oil impregnation method|
|US3120454 *||Mar 7, 1960||Feb 4, 1964||Great Lakes Carbon Corp||Drying oil impregnation of carbon electrodes|
|US3167447 *||Aug 18, 1961||Jan 26, 1965||Dwight E Davis||Carbon body treatment|
|US4255466 *||Feb 14, 1977||Mar 10, 1981||Mitsubishi Chemical Industries, Limited||Carbon electrode and manufacture thereof|
|US8124127 *||Oct 16, 2006||Feb 28, 2012||Atrium Medical Corporation||Hydrophobic cross-linked gels for bioabsorbable drug carrier coatings|
|US8263102||Sep 28, 2005||Sep 11, 2012||Atrium Medical Corporation||Drug delivery coating for use with a stent|
|US8312836||Jul 30, 2008||Nov 20, 2012||Atrium Medical Corporation||Method and apparatus for application of a fresh coating on a medical device|
|US8367099||Sep 22, 2006||Feb 5, 2013||Atrium Medical Corporation||Perforated fatty acid films|
|US8501229||Feb 24, 2012||Aug 6, 2013||Atrium Medical Corporation||Hydrophobic cross-linked gels for bioabsorbable drug carrier coatings|
|US8574627||Oct 30, 2007||Nov 5, 2013||Atrium Medical Corporation||Coated surgical mesh|
|US8795703||Sep 28, 2005||Aug 5, 2014||Atrium Medical Corporation||Stand-alone film and methods for making the same|
|US8858978||Sep 28, 2005||Oct 14, 2014||Atrium Medical Corporation||Heat cured gel and method of making|
|US9000040||Feb 3, 2009||Apr 7, 2015||Atrium Medical Corporation||Cross-linked fatty acid-based biomaterials|
|US9012506||Dec 1, 2008||Apr 21, 2015||Atrium Medical Corporation||Cross-linked fatty acid-based biomaterials|
|US9278161||Oct 19, 2009||Mar 8, 2016||Atrium Medical Corporation||Tissue-separating fatty acid adhesion barrier|
|US9427423||Mar 10, 2009||Aug 30, 2016||Atrium Medical Corporation||Fatty-acid based particles|
|US9492596||Feb 2, 2007||Nov 15, 2016||Atrium Medical Corporation||Barrier layer with underlying medical device and one or more reinforcing support structures|
|US9592324||Oct 30, 2007||Mar 14, 2017||Atrium Medical Corporation||Tissue separating device with reinforced support for anchoring mechanisms|
|US9682175||Apr 14, 2014||Jun 20, 2017||Atrium Medical Corporation||Coating material and medical device system including same|
|US20060067983 *||Sep 28, 2005||Mar 30, 2006||Atrium Medical Corporation||Stand-alone film and methods for making the same|
|US20060078586 *||Sep 28, 2005||Apr 13, 2006||Atrium Medical Corporation||Barrier layer|
|US20060110457 *||Sep 28, 2005||May 25, 2006||Atrium Medical Corporation||Heat cured gel and method of making|
|US20070071798 *||Sep 22, 2006||Mar 29, 2007||Atrium Medical Corporation||Perforated bioabsorbable oil film and methods for making the same|
|US20070202149 *||Oct 16, 2006||Aug 30, 2007||Atrium Medical Corporation||Hydrophobic cross-linked gels for bioabsorbable drug carrier coatings|
|US20080109017 *||Feb 2, 2007||May 8, 2008||Atrium Medical Corporation||Barrier layer with underlying medical device and one or more reinforcing support structures|
|US20080113001 *||Oct 30, 2007||May 15, 2008||Atrium Medical Corporation||Tissue separating device with reinforced support for anchoring mechanisms|
|US20080118550 *||Oct 30, 2007||May 22, 2008||Atrium Medical Corporation||Coated surgical mesh|
|US20080206305 *||Mar 10, 2008||Aug 28, 2008||Atrium Medical Corporation||Implantable barrier device|
|US20090011116 *||Jul 30, 2008||Jan 8, 2009||Atrium Medical Corporation||Reducing template with coating receptacle containing a medical device to be coated|
|US20090047414 *||Jul 30, 2008||Feb 19, 2009||Atrium Medical Corporation||Method and apparatus for application of a fresh coating on a medical device|
|US20090181937 *||Dec 1, 2008||Jul 16, 2009||Atrium Medical Corporation||Cross-linked fatty acid-based biomaterials|
|US20090208552 *||Feb 3, 2009||Aug 20, 2009||Atrium Medical Corporation||Cross-linked fatty acid-based biomaterials|
|US20100233232 *||Mar 10, 2009||Sep 16, 2010||Swanick Thomas M||Fatty-acid based particles|
|DE1282626B *||Jul 6, 1962||Nov 14, 1968||Great Lakes Carbon Corp||Verfahren zur Behandlung poroeser Kohlenstoffelektroden fuer die Chlor-Alkali-Elektrolyse|
|U.S. Classification||427/113, 204/294, 106/252|
|International Classification||C25B11/14, C25B11/00|