SOLVAY S.A., Plaintiff-Appellant, v. HONEYWELL INTERNATIONAL, INC., Defendant-Appellee.
No. 2009-1161
United States Court of Appeals, Federal Circuit
Oct. 13, 2010.
The government asserts that Amber Resources broadly held that “where parties ‘right[ly] or wrong[ly]’ interpret a statutory provision one way, only to learn through an intervening court decision that the court views the provision differently, the court‘s decision should become the operative time from which the parties should be on notice of the correct interpretation. Nothing in Amber purports to limit this principle to concepts unique to contract law.” Gov‘t Br. 26-27 (quoting Amber Resources, 538 F.3d at 1370) (alteration in original). To the contrary, the holding in Amber Resources is explicitly tied to its context. The Amber Resources court explains the general rule that “court decisions construing statutes are typically viewed as not changing the law but merely announcing what the law has meant since its enactment,” but then states that this rule is not useful “in a case such as this one.” 538 F.3d at 1370. The entire discussion of how the parties interpreted the statute is in the context of contract repudiation and breach and is analyzed with these concepts in mind. See id. (“It would ignore the reality of the situation in this case to suggest that the interpretation of the 1990 CZMA amendments, as ultimately announced by the courts more than a decade later, was clear to the parties from the moment of enactment or that the governing principles of contract law should be applied as if it were. The fact of the matter is that, right or wrong, the parties interpreted the 1990 CZMA amendments in a way that would not have resulted in a breach.“).
Apart from the contract-specific language in Amber Resources, the government‘s proposed expansion of Amber Resources would change existing law and eliminate remedies for any party affected by the misinterpretation of a statute. Even if Amber Resources could be stretched to excuse noncompliance with the notice provisions of
For the foregoing reasons, the judgment of the Court of International Trade is affirmed.
AFFIRMED
Robert G. Krupka, Kirkland & Ellis LLP, of Los Angeles, CA, argued for defendant-cross appellant. With him on the brief were Laura M. Burson, Guy Ruttenberg; and Gregory F. Corbett, of Washington, DC. Of counsel were Sean M. McEldowney, of Washington, DC; and Shani A. Moore Weatherby, of Los Angeles, CA.
Before DYK, MAYER, and SCHALL, Circuit Judges.
SCHALL, Circuit Judge.
This is a patent case. It arises out of a suit by Solvay S.A. (“Solvay“) against Honeywell Specialty Materials LLC and Honeywell International, Inc. (collectively, “Honeywell“) in the United States District Court for the District of Delaware for infringement of U.S. Patent No. 6,730,817 (“the ‘817 patent“) owned by Solvay. Solvay now appeals the final judgment of the district court in favor of Honeywell dismissing Solvay‘s suit. The court‘s judgment in favor of Honeywell was based on two rulings on summary judgment. First, the court held that although asserted
For the reasons set forth below, we hold that the district court erred in ruling claims 1, 5, 7, 10, and 11 of the ‘817 patent invalid. We do so because we conclude that Honeywell was not a prior inventor for purposes of
BACKGROUND
I.
Solvay‘s ‘817 patent has a priority date of October 23, 1995. The ‘817 patent is directed to methods for making 1,1,1,3,3-pentafluoropropane (“HFC-245fa“). HFC-245fa has been found to be advantageous as a blowing and insulation agent in the preparation of expanded polymeric materials, of the type commonly used in refrigeration and heat storage systems. See ‘817 patent, col.1 ll.12-14. HFC-245fa is one of a group of non-ozone-depleting hydrofluorocarbons that were legislatively mandated to replace ozone-depleting chlorofluorocarbons and hydrochlorofluorocarbons. The ‘817 patent discloses methods for making HFC-245fa by reacting 1,1,1,3,3-pentachloropropane (“HCC-240fa“) with hydrogen fluoride (“HF“) in the presence of a hydrofluorination catalyst. Specifically, the patent claims processes for making HFC-245fa that include continuously drawing off gaseous HFC-245fa and hydrogen chloride (“HCl“) from the reaction mixture.
Claims 1 and 12 are the patent‘s two independent claims. Claim 1 reads as follows:
In a process for the preparation of [HFC-245fa] comprising reaction of [HCC-240fa] with [HF] in the presence of a hydrofluorination catalyst, the improvement which comprises carrying out the reaction at a temperature and under a pressure at which [HFC-245fa] is gaseous and isolating and [sic] [HFC-245fa] from the reaction mixture by drawing off [HFC-245fa] and [HCl] in a gaseous phase as each of said [HFC-245fa] and [HCl] is being formed.
‘817 patent, col.5 ll.36-46.
Claim 12 reads as follows:
In a process for the preparation of [HFC-245fa] comprising reaction of [HCC-240fa] with [HF] in the presence of a hydrofluorination catalyst, the improvement which comprises carrying out the reaction in a reactor equipped with a
device for drawing off a gas stream at a temperature and under a pressure at which [HFC-245fa] is gaseous and wherein said device is controlled (a) to draw off a gas stream comprising [HFC-245fa] and [HCl] as each of said [HFC-245fa] and [HCl] is being formed thereby isolating said [HFC-245fa] from the reaction mixture (b) to keep in the reactor in the liquid state the unconverted [HCC-240fa], most of the [HF] and most of the products of partial fluorination of [HCC-240fa].
Id. at col.6 ll.15-30.
II.
Honeywell produces HFC-245fa in its plant located in Geismar, Louisiana, by reacting HCC-240fa and HF in the presence of a hydrofluorination catalyst (“the Geismar process“). The Geismar process is a continuous process, where HFC-245fa, HCl, unreacted HF, and other by-products are drawn off from the reactor in gaseous form. Except for the catalyst that escapes from the reactor and that is returned to the reactor by the reflux in the catalyst stripper, the other components of the process exit the reactor as a gas stream for further processing. Notably, most of the HF (approximately 70%) that enters the reactor subsequently leaves the reactor as part of the gas stream. The gas stream then enters downstream equipment, including an HF recovery unit which recovers unreacted HF. The unreacted HF is later recycled and refed, as a gas, to the reactor.
III.
Solvay brought suit against Honeywell in the District of Delaware, alleging that the Geismar process infringed claims 1, 5, 7, 10-18, 21, and 22 of the ‘817 patent. In due course, Honeywell moved for summary judgment of invalidity of claims 1, 5, 7, 10, and 11 of the ‘817 patent. Honeywell moved on the ground that, under
In early 1994, Honeywell (then Allied-Signal, Inc.) entered into a research contract with the Russian Scientific Center for Applied Chemistry (“RSCAC“). Pursuant to the contract, RSCAC engineers performed process development studies for the commercial production of HFC-245fa. See Invalidity Ruling, 591 F.Supp.2d at 732. In July 1994, RSCAC sent a report to Honeywell in the United States documenting that it had carried out the liquid phase synthesis of HFC-245fa from HCC-240fa using a continuous process. Id. The report documented that RSCAC had carried out a reaction of HCC-240fa and HF in the presence of an antimony pentachloride catalyst using temperatures between 80-130 degrees Celsius and pressures between 2-40 bar. Id. The report also documented the resulting product yield, and it contained a diagram of the equipment that RSCAC had used to carry out the process. Id. It is undisputed that the process the RSCAC engineers performed and reported to Honeywell in July 1994 corresponds to the invention claimed in Solvay‘s ‘817 patent, and that RSCAC engineers both conceived the invention and reduced it to practice in Russia.
In early 1995, Honeywell used the information that RSCAC had provided to dupli-
Throughout the summer of 1995, Honeywell continued working to develop and perfect its process for the preparation of HFC-245fa. Id. at 733. The work included finding optimum operating conditions for the process, as well as designing and enabling downstream purification of the HFC-245fa product. Id. Development of a pilot plant to test a commercially viable manufacturing process for HFC-245fa was begun by Honeywell, and the plant was in successful operation by February 1996. In March 1996, Honeywell began drafting a patent application on an improvement process for making HFC-245fa. The application was filed on July 3, 1996, and eventually issued as U.S. Patent No. 5,763,706 (“the ‘706 patent“). The ‘706 patent discloses a process for the continuous preparation of HFC-245fa, using optimal conditions for downstream purification, so that the HFC-245fa recovered by distillation has a high purity (at least about 99.5%). See ‘706 patent, col.1 l.60-col.2 l.25; col.4 ll.40-42.
On December 9, 2008, the district court granted Honeywell‘s motion for summary judgment of invalidity of claims 1, 5, 7, 10, and 11 of the ‘817 patent and denied Solvay‘s motion for summary judgment of no invalidity. See Invalidity Ruling, 591 F.Supp.2d at 743. The court ruled that Honeywell had previously made the invention of the ‘817 patent in the United States in August 1995, prior to the ‘817 patent‘s priority date, and that the asserted claims thus were invalid based on Honeywell being a prior inventor under
In arriving at its ruling, the court rejected Solvay‘s contention that Honeywell was not an “inventor” under
The district court concluded that “Honeywell conceived the invention at issue in the United States upon receipt of RSCAC‘s instructions, because it was at
The parties also cross-moved for summary judgment on the issue of infringement of the ‘817 patent. Solvay filed a motion for summary judgment of infringement of claims 1, 5, 7, 10, and 11. Honeywell, in turn, moved for summary judgment of non-infringement of those claims and also for summary judgment of non-infringement of claims 12-18, 21, and 22. On December 9, 2008, the district court ruled on the infringement issue. First, as an alternative to its ruling that claims 1, 5, 7, 10, and 11 were invalid, the court granted Solvay‘s motion for summary judgment of infringement of those claims and denied Honeywell‘s cross-motion for summary judgment of non-infringement. Second, the court granted Honeywell‘s motion for summary judgment of non-infringement of claims 12-18, 21, and 22.
Following its summary judgment decisions, the district court entered judgment in favor of Honeywell and against Solvay, thereby dismissing Solvay‘s suit. This appeal followed. We have jurisdiction pursuant to
DISCUSSION
I.
We review a district court‘s grant of summary judgment de novo. Revolution Eyewear, Inc. v. Aspex Eyewear, Inc., 563 F.3d 1358, 1365 (Fed.Cir.2009). Summary judgment is appropriate where there is no genuine issue of material fact and the moving party is entitled to judgment as a matter of law.
On appeal, Solvay argues that the district court erred in holding that claims 1, 5, 7, 10, and 11 of the ‘817 patent are invalid under
II.
A.
Solvay challenges on two grounds the district court‘s ruling that claims 1, 5, 7, 10, and 11 of the ‘817 patent are invalid due to prior inventorship. First, Solvay argues that Honeywell could not be “another inventor” under
Second, Solvay argues that, even if Honeywell does qualify as “another inventor” under
Honeywell responds that we should affirm the judgment of invalidity of claims 1, 5, 7, 10, and 11. First, Honeywell argues that it is “another inventor” under
Honeywell argues that we should reject Solvay‘s contention that Honeywell is precluded by
In addition, in Dow Chemical Co. v. Astro-Valcour, Inc., 267 F.3d 1334 (Fed.Cir.2001), Honeywell argues, we rejected the contention that “another inventor” under
Honeywell further argues that, once it established that the claimed invention was made in the United States by “another inventor” before the ‘817 patent‘s priority date, Solvay bore the burden of producing “evidence sufficient to create a genuine issue of material fact as to whether the prior inventor abandoned, suppressed, or concealed the invention.” Id. at 31, citing Dow Chemical, 267 F.3d at 1339. According to Honeywell, Solvay failed to carry that burden.
B.
A person is not entitled to a patent if “before the applicant‘s invention thereof the invention was made in this country by another inventor who had not abandoned, suppressed or concealed it.”
As just seen, in Kimberly-Clark, we stated that
We have regularly applied “the rules governing the determination of priority of invention” in cases involving the question of prior inventorship under
Honeywell is not “another inventor” under
The district court concluded, however, that Honeywell conceived the invention because, “upon receipt of RSCAC‘s instructions ... Honeywell possessed a definite and permanent idea of the complete and operative invention, such that it appreciated the fact of its invention.” Id. at 738. The district court further concluded that Honeywell had “demonstrated conception by clear and convincing evidence” and “that its receipt of RSCAC‘s instructions facilitated Honeywell‘s actual reduction to practice of the invention.” Id. The court stated that
Conception is “the formation in the mind of the inventor, of a definite and permanent idea of the complete and operative invention, as it is hereafter to be applied in practice.” Burroughs Wellcome Co. v. Barr Labs., Inc., 40 F.3d at 1228 (quoting Hybritech Inc. v. Monoclonal Antibodies, Inc., 802 F.2d at 1376). The test for conception is whether the inventor had an idea that was definite and permanent enough that one skilled in the art could understand the invention. Burroughs Wellcome, 40 F.3d at 1228. In this case, Honeywell did not have, or formulate, a definite and permanent “idea” of its own capable of being reduced to practice. Rather, it reproduced the invention previously conceived and reduced to practice by RSCAC in Russia. Such reproduction cannot be conception because, if it were, the result would be that one who simply followed another inventor‘s instructions to reproduce that person‘s prior conceived invention would, by so doing, also become an “inventor.” Although the district court declined to read the “originality” requirement of
Honeywell relies on Mycogen Plant Sci., Inc. v. Monsanto Co. and Henkel Corp v. Procter & Gamble Co. for the proposition that prior inventorship under
Honeywell‘s reliance on Henkel also is misplaced. Henkel involved an appeal from a patent interference decision awarding priority of invention to the party that demonstrated an earlier actual reduction to practice based on “an appreciation” that the invention at issue worked for its intended purpose. 560 F.3d at 1289. Henkel did not involve the situation presented here: an accused infringer claiming to be “another inventor” under
Similarly unhelpful to Honeywell is its reliance on Dow Chemical Co. v. Astro-Valcour, Inc. for the proposition that “someone qualifies as a prior inventor under
Finally, Honeywell argues that, as a matter of policy, it would contradict the purpose of
Whether this holding ignores the realities of globalization and outsourcing by modern-day research companies, as Honeywell contended at oral argument, is not the question before us. The question before us is whether, under the undisputed facts, Honeywell qualifies as “another inventor” under
In sum, because Honeywell does not qualify as “another inventor” under
III.
“An infringement analysis entails two steps. The first step is determining the meaning and scope of the patent claims asserted to be infringed. The second step is comparing the properly construed claims to the device accused of infringing.” Markman v. Westview Instruments, Inc., 52 F.3d 967, 976 (Fed.Cir.1995) (en banc) (citations omitted), aff‘d, 517 U.S. 370 (1996). Claim construction is a question of law, which we review de novo. Cybor Corp. v. FAS Techs., Inc., 138 F.3d 1448, 1456 (Fed.Cir.1998) (en banc).
A.
Honeywell contends the district court erred in its alternative ruling granting
The district court construed the limitation “isolating ... [HFC-245fa] from the reaction mixture by drawing off [HFC-245fa] and [HCl] in a gaseous phase as each of said [HFC-245fa] and [HCl] is being formed” in independent claim 1 as follows:
The process for making HFC-245fa includes a reaction at a temperature and under a pressure whereby HFC-245fa and HCl are produced in gaseous form and separated from the reaction mixture in a gas stream that can include other compounds, such as unconverted reactants and chlorofluoropropanes possibly formed by incomplete fluorination of HCC-240fa.
Solvay, S.A. v. Honeywell Specialty Materials LLC, No. 06-557, 2008 WL 5155629, at *2 (D.Del. Dec. 9, 2008) (“Claim Construction Ruling“) (emphasis added).
The corresponding limitation in independent claim 12 of the ‘817 patent reads “isolating said [HFC-245fa] from the reaction mixture ... to keep in the reactor in the liquid state the unconverted [HCC-240fa], most of the [HF] and most of the products of partial fluorination of [HFC-245fa].” In construing this limitation, the district court stated:
I conclude that the “isolating” limitation found in claims 1 and 12 should be construed consistently. The fact that claim 12 discloses a device to accomplish the process, while claim 1 only describes the process, does not convince me that the patentee meant to use the same word (“isolate“) to describe different processes.
Claim Construction Ruling, 2008 WL 5155629, at *3. The court construed the “isolating” limitation of claim 12 as follows: “As the HFC-245fa and HCl are produced in gaseous form, they are separated from the reaction mixture in a gas stream by the device.” Id. at *4. Thus, the court construed “isolating” in independent claims 1 and 12 as meaning “separating.”
In arriving at its construction of claim 1, the district court considered whether the term “isolating,” as used in the claim, means that “only” HFC-245fa and HCl are drawn off from the reaction mixture in a gas stream as they are being formed, or whether the gas stream can include other components. The court reasoned that the patent specification uses “isolate,” “separate,” and “to draw off” interchangeably, as did the inventors during prosecution, and that “isolate” thus should not be construed to mean only HFC-245fa and HCl, even if the dictionary definition of “isolate” suggests separation of a “pure chemical substance.” Id. at *3. The court also reasoned that because claim 12‘s use of
In its infringement ruling, the district court held that the Geismar process infringed claim 1 because it draws off a gas stream from the reaction mixture and thereby isolates, or separates, HFC-245fa from the mixture. See Non-infringement Ruling, 591 F.Supp.2d at 727. The court noted that “although the gas stream in the Geismar process includes many compounds other than HFC-245fa and HCl,” the process still infringed because “claim 1 has been construed very broadly....” Id. at 727-28.
Honeywell urges that the district court failed to appreciate that claim 1 requires that the gaseous product leaving the reactor include only “residual amounts of other non-reacting compounds,” along with HFC-245fa and HCl. According to Honeywell, that is also what claim 12 requires. In support of its argument, Honeywell points to the expert testimony of Michael Doherty interpreting “isolating” as “purifying” HFC-245fa from all other reaction mixture components so that there are only residual, i.e., not measurable, amounts of other compounds in the gas stream. See Appellee‘s Br. at 59-60. Honeywell also points to dictionary definitions of “isolation” as “separation of a pure chemical substance from a compound or mixture,” contending “isolating” thus means completely separating HFC-245fa from all other reaction mixture components, including HF. Id. at 60-61. Finally, Honeywell asserts that, during prosecution, the inventors limited the “isolating” step to being one that separates HFC-245fa and HCl from all reaction mixture components the first (and only) time they leave the reactor in a gas stream. Id. at 62.8 Honeywell concludes that the district court‘s error—either in claim construction or claim construction application—resulted in an incorrect finding of infringement with respect to Honeywell‘s Geismar process because, in that process, more than “residual amounts” of other compounds leave the reactor. Honeywell contends that the Geismar process does not isolate from the reaction mixture the HFC-245fa and HCl as they are being formed, but, rather, draws off a gas stream which is mostly HF and which also contains partially fluorinated compounds. Id. at 58.
Solvay responds that the district court erred in neither its claim construction nor its application of that claim construction. Solvay argues that the district court correctly construed claim 1 when it concluded that “isolating” does not mandate that HFC-245fa and HCl are the only materials in the gas stream that are drawn off, or isolated, from the reaction mixture. See Non-infringement Ruling, 591 F.Supp.2d at 727-28. Solvay asserts that the district court correctly understood that the ‘817 patent teaches a process that separates gaseous HFC-245fa from the reaction mix-
We see no error in the district court‘s infringement ruling. In our view, claim 1 is not limited to “isolating” only HFC-245fa and HCl and residual amounts of other compounds. The claim does not recite isolating HFC-245fa from all other components involved in the process, and it does not recite isolating HFC-245fa from everything beyond residual amounts of reaction mixture components in the gas stream. Neither does the specification require that the gaseous stream separated from the reaction mixture contain only HFC-245fa and HCl. The patent specification uses the terms “isolating,” “separating,” and “drawing off” interchangeably, as the district court noted. At the same time, we do not think any of the statements made during prosecution call for a construction of claim 1 that requires only “residual amounts” of other components in the gas stream. In the prosecution amendment to which Honeywell points, see footnote 8 above, the inventors simply described their process as isolating HFC-245fa and HCl by drawing off each from the reaction mixture as they are being formed. Such a description does not constitute a statement that the invention of the ‘817 patent involves a process in which only certain reactants (and no others) can be isolated from reaction mixture components or, in other words, one in which only residual amounts of other compounds are contained in the gas stream.
Honeywell‘s reliance on the testimony of Michael Doherty interpreting “isolating” as “purifying” HFC-245fa from all other reaction mixture components is misplaced. The term “purifying” is not used in the patent and is not to be considered synonymous with “isolation” based on extrinsic expert testimony alone. See Phillips v. AWH Corp., 415 F.3d 1303, 1317 (Fed.Cir.2005) (en banc) (extrinsic evidence such as expert testimony is “less significant than the intrinsic record in determining the legally operative meaning of claim language“) (internal citations omitted); Kara Tech. Inc. v. Stamps.com Inc., 582 F.3d 1341, 1348 (Fed.Cir.2009) (“extrinsic sources like expert testimony cannot overcome more persuasive intrinsic evidence.“); Ultimax Cement Mfg. Corp. v. CTS Cement Mfg. Corp., 587 F.3d 1339, 1347 (Fed.Cir.2009) (district court erroneously relied on expert testimony and a dictionary definition to the exclusion of the intrinsic evidence of the specification language).
Finally, we do not view the district court‘s construction and application of claim 1 as inconsistent with its construction of claim 12. As noted, in construing claim 12‘s “isolating” limitation, the court stated that “[a]s the HFC-245fa and HCl are produced in gaseous form, they are
The district court construed a different claim 12 limitation, “to keep in the reactor in the liquid state the unconverted [HCC-240fa], most of the HF and most of the products of partial fluorination of [HCC-240fa],” as follows:
The gas stream can include residual amounts of other compounds, such as unconverted reactants and chlorofluoropropanes possibly formed by incomplete fluorination of HCC-240fa. However, the unconverted HCC-240fa, more than 50% of the HF, and more than 50% of the partially fluorinated intermediates must remain in the reactor vessel in the liquid state.
Claim Construction Ruling, 2008 WL 5155629, at *4 (emphasis added). In urging an inconsistency between the court‘s construction of the “isolating” limitations in claims 1 and 12, Honeywell points to this claim construction language. It apparently contends that this construction of claim 12‘s “to keep in the reactor in the liquid state” limitation, combined with the court‘s statement that claims 1 and 12 are to be construed “consistently,” means that “isolating” in claim 1 means that only “residual” amounts of compounds other than HFC-245fa and HCl may be in the gas stream. This language, however, does not relate to the “isolating” limitation of claim 12. Rather, it relates to the “keep in the reactor in the liquid state” limitation of the claim. As the discussion in section B below makes clear, this is a fundamentally different limitation from the “isolating” limitation.
We therefore reject Honeywell‘s argument with respect to claim 1, whether viewed as asserting an incorrect claim construction or the erroneous application of a correct claim construction. Because Honeywell does not dispute that its accused Geismar process has a gas stream with more than residual amounts of reaction mixture components, the district court did not err in ruling that claims 1, 5, 7, 10, and 11 of the ‘817 patent were infringed.
B.
Solvay argues that the district court erred in granting summary judgment of non-infringement of claims 12-18, 21, and 22 of the ‘817 patent, see Non-infringement Ruling, 591 F.Supp.2d at 728. Specifically, Solvay contends the district court erred in its construction of the limitation “to keep in the reactor in the liquid state the unconverted [HCC-240fa], most of the [HF] and most of the products of partial fluorination of [HCC-240fa]” in independent claim 12. Solvay urges that, under the correct construction of the limitation, there is no dispute that the Geismar process infringes claims 12-18, 21, and 22. According to Solvay, all other limitations of claim 12 and dependent claims 13-18, 21, and 22 are met in the Geismar process.
As noted, the district court construed this limitation as follows:
The gas stream can include residual amounts of other compounds, such as unconverted reactants and chlorofluoro-
propanes possibly formed by incomplete fluorination of HCC-240fa. However, the unconverted HCC-240fa, more than 50% of the HF, and more than 50% of the partially fluorinated intermediates must remain in the reactor vessel in the liquid state.
Claim Construction Ruling, 2008 WL 5155629, at *4. In so ruling, the court looked to the prosecution history, in which claim 12 was described by the inventors as being “limited” to a process whereby the reaction is carried out in a reactor “equipped with a device for drawing off a gas stream which is controlled ... to keep in the reactor in the liquid state the unconverted HCC-240fa, most of the HF and most of the products of partial fluorination of HCC-240fa.” Id. The court concluded that, on this prosecution record, “claim 12 is a more limited, narrow claim than claim 1 and should be construed accordingly.” Id.
Armed with its claim construction, the court ruled that the Geismar process did not infringe claim 12, or dependent claims 13-18, 21, and 22, because the Geismar process does not keep more than 50% of the HF in the reactor vessel in the liquid state, as required by the claim. See Non-infringement Ruling, 591 F.Supp.2d at 728. The court cited the portion of the record referring to Honeywell‘s description of its Geismar process, which Solvay did not dispute, characterizing the Geismar gas stream as containing unreacted HF and partially fluorinated intermediates, along with other components. Id. at 726. The record also reflects that the gas stream in the Geismar process is fed, inter alia, into an HF recovery unit to recover the unreacted HF, which is later re-fed to the reactor as a gas, not a liquid.
In arguing against the district court‘s claim construction, Solvay breaks up the limitation into two parts; first addressing the “to keep in the reactor” clause and then addressing the “in the liquid state” clause. Solvay contends that the “to keep in the reactor” clause should be read to include unconverted and partially converted reactants that are either “kept in” or “returned to” the reactor for further use in the process, and that it was error for the court to conclude that the reactants must always remain in the reactor vessel. See Appellant‘s Br. at 29-30. Solvay points to language in the specification which teaches that “it is advantageous to separate the [HFC-245fa] and the [HCl] from the reaction mixture as they are being formed and to keep in, or return to, the reactor the unconverted reactants....” See ‘817 patent, col.2 ll.64-67 (emphasis added); Appellant‘s Br. at 28-29.
As for the “in the liquid state” clause, Solvay argues that a correct construction of the limitation overall should include HF that leaves the reactor but then returns (in any state, either liquid or gaseous) and thereby becomes available to react in the liquid phase reaction to produce HFC-245fa, as disclosed in the specification. See Appellant‘s Br. at 28-30. Solvay maintains that the district court‘s non-infringement ruling should be reversed, because it is based upon an erroneous claim construction and that the Geismar process infringes claim 12 under a correct claim construction that permits reactants to remain in the process by being returned to the reactor.
For its part, Honeywell contends the district court correctly construed the claim 12 limitation based on the plain language of the claim, the ‘817 patent specification and the prosecution history. Honeywell contends that its Geismar process does not infringe claim 12 of the ‘817 patent under
Here, again, we agree with the district court‘s claim construction. In our view, the limitation “to keep in the reactor in the liquid state” means that the reactants must stay in the reactor in the liquid state until they leave as a gas and cannot return after being re-processed. It is true that the disclosure in the specification is broad enough to include unconverted and partially converted reactants that return to the reactor for further use in the process, because the “or” in the phrase “to keep in, or return to, the reactor the unconverted reactants” suggests an alternative description of the process rather than either/or, in the disjunctive sense. However, the prosecution history should also be considered, and here we think the issue is decided. See, e.g., Phillips, 415 F.3d at 1317 (“the prosecution history can often inform the meaning of the claim language by demonstrating how the inventor understood the invention and whether the inventor limited the invention in the course of prosecution, making the claim scope narrower than it would otherwise be.“).
During prosecution, the inventors distinguished the prior art ‘192 patent from their invention on the ground that, in their invention, the reactants are not recycled and returned to the reactor, but rather have the advantage of remaining in the reactor vessel in the liquid state. The statements made during prosecution reflect a distinction between, on the one hand, the claimed invention having reactants remain in the reactor in liquid form and, on the other hand, the prior art having unconverted and partially converted reactants leave and then return to the reactor for re-processing. The claim 12 limitation excludes the step of having reactants return to the reactor. It is undisputed that, under this construction, the term “keep in the reactor in the liquid state” is not met by the Geismar process. See Non-infringement Ruling, 591 F.Supp.2d at 726 (“[t]he record also reflects that the gas stream is fed, inter alia, into an HF recovery unit to recover the unreacted HF, which is later re-fed, as a gas, to the reactor“). Thus, we see no error in the district court‘s ruling that the Geismar
CONCLUSION
We reverse the district court‘s grant of summary judgment that claims 1, 5, 7, 10, and 11 of the ‘817 patent are invalid under
COSTS
Each party shall bear its own costs.
AFFIRMED-IN-PART, REVERSED-IN-PART, and REMANDED.
