Application of Ferdinand Markert, Willibald Funk, Gottfried Richter and Otto Frey

396 F.2d 477, 55 C.C.P.A. 1319
CourtCourt of Customs and Patent Appeals
DecidedOctober 10, 1968
DocketPatent Appeal 7967
StatusPublished

This text of 396 F.2d 477 (Application of Ferdinand Markert, Willibald Funk, Gottfried Richter and Otto Frey) 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
Application of Ferdinand Markert, Willibald Funk, Gottfried Richter and Otto Frey, 396 F.2d 477, 55 C.C.P.A. 1319 (ccpa 1968).

Opinion

SMITH, Judge.

The present appeal relates to a process for the production of gaseous olefins by cracking hydrocarbons. The asserted improvement resides in rapidly cooling the reaction gases “without side reactions and without troublesome coke formation.” Appellant asserts that this result is obtained:

* * * by supplying to the current of reaction gases which are at the reaction temperature, in a cooling chamber, one or more compact jets of liquid containing an amount of liquid sufficient to cool the gas current by at least 100°C, the said jet or jets being supplied laterally at such a pressure-head that the jet or jets penetrate the gas current and are disintegrated therein.

The board 1 affirmed the examiner’s final rejection of appealed claims 1-9, inclusive, as “obvious over” the references :

Forward 2,144,488

January 17, 1939

Kosbahn et al. 2,719,184

September 27, 1955

While the examiner in his Answer rejected all the claims on this basis, the board’s opinion of December 21, 1965 seems to treat the claims somewhat differently. Thus, its opinion refers to the final rejection of claims 1 to 3 and 5 and a refusal “to allow claims 4 and 6 to 9 which were amended after final rejection.” The board, however, did not comment further on the rejection and proceeded to treat all the claims as being rejected under 35 U.S.C. § 103, stating:

Claims 1 to 9 are rejected as being “obvious over either of Forward or Kosbahn et al.” The Examiner holds that the gas quenching by “lateral” water injection, which is employed in an old cracking procedure, is shown by each of the references. We agree. We see nothing unobvious in this procedure as applied to ordinary gas-quenching operations and we will sustain the rejection.

The foregoing recital of the background of the present appeal highlights the apparent failure of the appellants, the examiner, and the board to have joined issue on the grounds of rejection. As will be noted later, this extends also to the question as to precisely what limi *479 tations were present in appealed claims 4-9 when rejected by the examiner and when this rejection was affirmed by the board.

As we view the claims on appeal, claims 1-3 stand or fall together on the obviousness rejection, while claims 4-9 stand or fall together on the same rejection, but for somewhat different reasons.

Claim 1, selected by us as representative of the first group, is:

1. An improvement in a process for the preparation of gaseous olefines wherein hydrocarbons are cracked in a fluidized bed at temperatures between about 650° and 850 °C which comprises: passing a current of said gaseous olefines from a cracking zone through an outlet pipe and into a cooling chamber, the diameter of said cooling chamber being substantially greater than the diameter of said pipe, and thereafter cooling said gaseous ole-fines by injecting a single compact jet of liquid into said current, the area of contact between said current and said jet of liquid being spaced inwardly from the walls of said cooling chamber, said jet of liquid being supplied laterally to said current of gaseous olefines under sufficient pressure to enable said jet of liquid to penetrate the current a predetermined amount, whereby said jet of liquid is tom apart by the gas current and the gases are thereby rapidly cooled.

Claim 4, selected by us as representative of the second group, is:

4. An improvement in a process for the preparation of gaseous olefines wherein hydrocarbons are cracked in a fluidized bed at temperatures between about 650° and 850° C which comprises: passing a current of said gaseous olefines from a cracking zone through an outlet pipe and into a cooling chamber said gaseous olefines entering said cooling chamber with a pressure-head of 20 to 1,000 millimeter water column, the diameter of said cooling chamber being substantially greater than the diameter of said pipe, and thereafter cooling said gaseous olefines by injecting at least one compact jet of liquid into said current, the area of contact between said current and said jet of liquid being spaced inwardly from the walls of said cooling chamber, said jet of liquid being supplied laterally to said current of gaseous olefines wherein the product of the ratio of the pressure-head of the jet of liquid to the pressure-head of the gas current and the ratio of the diameter of the jet of liquid to the diameter of the gas current lies within the range of from about 0.01 to about 3, all four variables being measured at the points of entry into the cooling chamber, whereby said jet of liquid penetrates said current a predetermined amount and is torn apart by the gas current and the gases are thereby rapidly cooled.

Comparison of the claims establishes that the principal difference between the two groups resides in the inclusion of certain so-called “numerical parameters” in claims 4-9 which are missing in claims 1-3.

We affirm the obviousness rejection of claims 1-3, 2 assuming that claims 1-3 were not cancelled. In reaching this conclusion, we do so after reviewing the references and finding ourselves in agreement with the examiner’s “brief description” thereof which we here adopt. The examiner’s Answer contains a description of the references relied upon which is as follows:

Forward relates to the cracking of heavy hydrocarbon oils to produce *480 lighter hydrocarbon oils. The hot oil vapors are cooled by lateral injection of a quenching liquid under pressure in the form of a jet * * *.
Kosbahn et al. relates to the production of acetylene by partial oxidation of hydrocarbons with oxygen. The reaction mixture is quenched by injection of water through jets * * *.

As stated in their brief, it is appellants’ position as to claims 1 and 3 that:

* * * There are at least five specific features of the process which are neither disclosed nor suggested in either of the cited references. With respect to Claim 1 * * * these features are as follows:
(1) Highly reactive gaseous olefins are produced.
(2) The diameter of the cooling chamber is substantially greater than the diameter of the pipe carrying the gaseous olefins (preferably at least seven times as large).
(3) A compact jet of liquid is injected into the current of olefins.
(4) The area of contact between the compact jet of liquid and the olefin current is spaced inwardly from the walls of the chamber.
(5) The compact jet of liquid is supplied laterally to the olefin current under sufficient pressure to enable the compact jet of liquid to penetrate the current a predetermined amount whereby the jet of liquid is torn apart and the gases are rapidly cooled.
In Claim 3, element No.

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396 F.2d 477, 55 C.C.P.A. 1319, Counsel Stack Legal Research, https://law.counselstack.com/opinion/application-of-ferdinand-markert-willibald-funk-gottfried-richter-and-ccpa-1968.