In re Johnson

94 F.2d 978, 25 C.C.P.A. 948, 1938 CCPA LEXIS 61
CourtCourt of Customs and Patent Appeals
DecidedMarch 7, 1938
DocketNo. 3866
StatusPublished

This text of 94 F.2d 978 (In re Johnson) is published on Counsel Stack Legal Research, covering Court of Customs and Patent Appeals primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
In re Johnson, 94 F.2d 978, 25 C.C.P.A. 948, 1938 CCPA LEXIS 61 (ccpa 1938).

Opinion

Jackson, Judge,

delivered the opinion of the court:

Appellants have appealed to this court from the decision of the Board of Appeals of the United States Patent Office affirming that [949]*949of the examiner which rejected claims 1 to 16, inclusive, 23 to 27, inclusive, and 29 to 4.6, inclusive. Claims 17 to 22, inclusive, and 28 were previously cancelled.

The claimed invention relates to the product and to a process of producing a stable borate from hydrous boron bearing natural ore. The process comprises first separating impurities from the ore by means of a magnetical and mechanical separator. The purified ore is then heated at a temperature of from 230° to 250° F. which is-slightly above the boiling point of water. Appellants’ purpose is, to obtain a purified and stable borate substantially equivalent octohedral borax. This borax contains 47.81 per centum B203 (a borate radical), five molecules of water, and is quite stable. Other hydrous borates contain varying percentages of B203 and are unstable; that is, they will, under some conditions, dry out and throw off moisture, and under others will absorb moisture. Appellants do not contend they first discovered that octohedral borax is stable. The drawing discloses a machine for performing the process, in which the natural ore is fed from a hopper through a magnetic separator including three successive rotors. There is a'liopper for the cleaned borate materials which run from the hopper through a spout into a rotary dryer.

The references relied upon are:

Thomas (British), 2,414, of 1879.
Rowand, 1,068,453, July 29, 1913.
Dutton et al., 1,146,140, July 13, 1915.
Rasor, 1,487,806, March 25, 1924.
British patent, 330,146, June 5, 1930.
British patent, 342,174, January 29, 1931.
French patent, 726,813, March 14, 1932.

Claims 1 and 38 are typical, and are as follows:

1. The process of producing a highly purified and concentrated, stable, boraLe ore from hydrous boron bearing ore which comprises removing, naturally occurring constituents therefrom by first magnetically separating impurities from the borate in the ore, and thereafter separating water of crystallization from the borate to increase the original stability thereof.
38. A highly purified and concentrated, stable borate ore, produced from naturally occurring boron bearing material containing impurities and hydrous borato material having an unstable content of water of crystallization, said stable ore being characterized by the fact that it does not contain in excess of approximately three tenths of one per cent iron content, that its water content is approximately 10% less than that of the material employed in producing the stable borate ore, and that the apparent density thereof is substantially less than that of the employed material.

Method claims 1, 11, 12, 16, 23 to 27, inclusive, and 29 to 37, inclusive, all involve .magnetic separation followed by dehydration, some of the claims showing details of the magnetic separation step and others details of the dehydration step. They were all rejected [950]*950as unpatentable over the patent to Rasor or British patent 330,146, in view of the Rowand patent or the French patent.

The Rasor patent discloses a process of, first, calcining colemanite, :a borate ore; second, dividing it from its gangue by screening; and then separating the borate from impurities by flotation or other mechanical means.

The French patent and the Rowand patent appear to disclose magnetic separators substantially similar in every detail to the separator which is recited in the claims. The separation of magnetizable matter from other material by means of the magnet, however, is old and well known. It is shown by British patent 342,174, British patent 2,414 of 1879, and the Dutton patent.

We can see no force to the argument of appellants in which they urge that “There is a big distinction between treatment of iron ore to recover the iron and treatment of hydrous borate mineral ore to eliminate iron impurities, together with mica and shale.” It seems to us that it would make no difference, as far as the issue here is concerned, whether the magnetizable material goes to waste or is saved, so long as the separation takes place.

The British patent 330,146 discloses dehydration of borate ore. This patent has to do entirely with a process of dehydrating borate dekahydrate (Na2B4O7.10H2O), which is borax with ten molecules of water. The dekahydrate is changed to a monohydrate by passing the material successively through a series of five chambers under controlled conditions of temperature and humidity.

The board sets out the process of British patent 330,146 in its ■opinion, as follows:

Borax * * * is introduced into the first dehydrating chamber and heated from 50 to 100° C., which removes two molecules of water.. This product is then dehydrated in the second chamber by heating from 65 to 150° O. to remove two additional molecules of water. In the third chamber two more molecules of water are removed by heating from 125 to 200° O. In the fourth chamber two more molecules of water are removed by heating from 175 to 260° O. In the last chamber one molecule of water is removed by heating from 225 to 825° C. The final product from the last chamber is NaaBiOr.H-O. In all of the chambers the temperature is controlled so that it is always below the melting point of the borax or below the point that the borax goes into solution in the remaining water of crystallization.

It is disclosed in British patent 330,146 that instead of a series of chambers, a single long chamber may be used. In the use of the single chamber the borax and air are passed from end to end, countercurrent to each other, and the borax subjected to dehydrating conditions from about 1 to 3 hours. In the instant application, a single long chamber is provided for the dehydration. It is not necessary here to translate the centigrade degrees of the British patent 330,146 into Fahrenheit, since it is by the application of heat that the water of crystallization [951]*951Is reduced by both the process in the patent and the process claimed in the application. The patent seems to clearly disclose a process of dehydration by which the ore is reduced to a stable condition, as may be seen from the following extract of the patent :

While the process of the present invention is suitable for dehydrating borax-to any desired' extent■ so as to secure a borax haying less water than the dekahydrate, which contains about 47 per cent of water, the process of the present invention is of special value in dehydrating borax to reduce the percentage of water in the borax to between the limits of 8 per cent and 21 per cent, or to dehydrate the borax so that it possesses less water of crystallization than three molecules and contains at least one molecule of water. [Italics supplied.]

The board held:

It is obvious from the above that the patentee contemplates dehydrating to any desired degree. Obviously, therefore, this would include dehydrating so as to obtain octahedral borax containing five molecules of water.

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Bluebook (online)
94 F.2d 978, 25 C.C.P.A. 948, 1938 CCPA LEXIS 61, Counsel Stack Legal Research, https://law.counselstack.com/opinion/in-re-johnson-ccpa-1938.