- Sumitomo Electric Industries, Ltd. v. United Technologies CorporationNo claims unpatentablePTAB · Sep 12, 2018 · IPR2017-00966 · APJ Christopher L Crumbley · IPR · Final written decision
Claims 1–4, 8–13, 16, and 17 were not shown unpatentable under either § 103 ground because SEI did not establish a sufficient reason to combine the references.
RulingsFinal written decision- Claim Construction › Intrinsic evidence (Phillips canons) › Preamble limiting or notPreamble not limitingNo construction neededDecided for petitioner
“We disagree. As the Federal Circuit has observed, “[a] preamble is not a claim limitation if the claim body ‘defines a structurally complete invention . . . and uses the preamble only to state a purpose or intended use for the invention.’” Georgetown Rail, 867 F.3d at 1236 (citing Rowe v. Dror, 112 F.3d 473, 478 (Fed. Cir. 1997)). The fact that the claims were amended to include storage tanks and recirculation loops actually cuts against UTC’s position, as the claim as amended describes a structurally complete invention and reliance on the preamble for this structure is unnecessary. UTC also points to the fact that the Examiner amended the preamble during prosecution, from merely reciting a “flow battery” to a “redox flow battery.” PO Resp. 15. While “clear reliance on the preamble during prosecution to distinguish the claimed invention from the prior art” (Catalina Mktg., 289 F.3d at 809) may be a reason to view the preamble as limiting, UTC directs us to no evidence here that the Examiner intended the amendment to distinguish the claims from the prior art. Indeed, as UTC acknowledges in its Response, a person of ordinary skill in the art would have understood the ’243 patent to use “‘redox flow battery’ and ‘flow battery’ to mean the same thing.” PO Resp. 13 (emphasis added). If, as UTC concedes, the Examiner’s amendment merely substituted one synonym for another, the amendment could not have changed the scope of the claim or distinguished over the prior art. For these reasons, we conclude that the preamble of the claims is not limiting, and, therefore, we need not construe the term redox flow battery.” slip op. at 10
- Skill levelSkill level petitioner adoptedDecided for petitioner
“SEI contends that the person of ordinary skill should not be limited to only a degree in chemistry or chemical engineering, because the claimed features of the flow batteries are not directed to chemistry. Pet. Reply 7. We agree, and adopt SEI’s definition of the relevant educational background. While the parties differ as to the number of years of experience in working with flow batteries, we do not consider the difference (one versus two years) to be significant. We find that a person of ordinary skill in the art at the time of invention would be a person with a degree in chemistry, physics, chemical engineering, electrical engineering, or mechanical engineering, who has at least one year of experience designing or testing flow batteries so as to obtain functional knowledge of their structure and operation. We have reviewed the level of skill reflected in the prior art and consider it consistent with this definition. See Okajima v. Bourdeau, 261 F.3d 1350, 1355 (Fed. Cir. 2001).” slip op. at 15
- ExcludeMotion to exclude, deniedDenied
“evidence. Our Rule 42.64 provides that a motion to exclude is necessary to preserve any objection, and refers to those objections as “objections to the admissibility” of evidence. See 37 C.F.R. § 42.64(a), (c). The Board’s Trial Practice Guide further explains that a motion to exclude “must explain why the evidence is not admissible.” See Office Patent Trial Practice Guide, 77 Fed. Reg. 48,756, 48,767. In other words, objections to the timing of late-arising evidence or procedural infirmities are not proper for a motion to exclude. For this reason, the objections raised in UTC’s motion to exclude are improper. First, UTC argues that Exhibit 1066 is untimely under 37 C.F.R. § 42.63(b), which requires a translation of a foreign-language document to be filed with the document. Mot. 5. By UTC’s reasoning, because the Supplemental Declaration revisits Mr. Yagaeshi’s prior translation, but was not submitted with the foreign-language document, it violates the Board’s rules. Id. As this is clearly a procedural objection to the timing of the evidence, as opposed to its admissibility, we deny the motion to exclude on this basis. In any event, even if it were procedurally proper, we would not exclude the Supplemental Declaration on this basis. The Board’s Rule requires only that the original foreign-language document be accompanied by a translation, and there is no dispute that is what happened here. We see nothing in Rule 42.63(b) that prohibits a party to revisit, or even modify, its translation at a later date, given sufficient notice and opportunity to respond by the opposing party. Here, we granted UTC the opportunity to submit its own responsive declaration and address the translation issue at the oral hearing, and UTC did so.” slip op. at 12
- Expert testimonyPetitioner expert discountedPatent owner expert creditedDecided for patent owner
“character as a minus sign, which is consistent with Mr. Yagaeshi’s original translation, makes more grammatical sense in the context of the sentence. We take note of the fact that SEI only changed its position on the translation—and asked Mr. Yagaeshi to correct his prior translation—once UTC made arguments based on the original translation that might be detrimental to SEI’s case. While it is conceivable that SEI only became aware of the alleged error once UTC called attention to it in the Response, we consider it fair to hold SEI to its original interpretation, especially given that that original interpretation is in agreement with Mr. Baldwin’s translation, which has remained consistent since at least 2016. For these reasons, we will interpret the disputed passage of JP228 to read “the potential was negative 0.4V.”” slip op. at 19
Patent outcomesUS 9,166,243 not shown unpatentableClaim construction§ 103 obviousnesscites KSR · GrahamPatents in suitUS 9,166,243 - Daicel Corporation v. Celanese International CorporationNo claims unpatentablePTAB · Jun 23, 2016 · IPR2015-00171 · APJ Linda M Gaudette · IPR · Final written decision
Claims 42–44, 47–51, 53, and 55–57 were not shown unpatentable: the ’095 patent did not establish the required amount of DME, and JP ’712 did not cure that deficiency.
RulingsFinal written decision- Claim Construction › Threshold & procedure › Whether a term needs construction (O2 Micro)Term construed patent owner constructionDecided for patent owner
“Based on our analysis of the intrinsic and extrinsic evidence, we agree with Patent Owner that a person of ordinary skill in the art would understand the ’507 patent to speak in terms of effects, not molecules. See PO Resp. 4– 5; Tr. 41:8–16. We, therefore, construe the recitation “distilling [a mixture comprising water, acetic acid, methyl iodide, methyl acetate, methanol, and at least one PRC] to separate the mixture into a plurality of streams, at least one of said streams being a PRC enriched overhead stream comprising dimethyl ether” in step (a) of claim 42 as requiring the presence of dimethyl ether in the PRC enriched overhead stream in an amount that one of ordinary skill in the art would recognize as being more than trace or insubstantial. Such amount would be, for example, more than the amount produced in a conventional, prior art, low water carbonylation process that used the same initial reactor contents and conditions, and the same processing equipment. We further interpret this language as requiring the presence of DME in the PRC enriched overhead stream in an amount sufficient to cause (1) a reduction in the solubility of methyl iodide in water during the extraction of the PRC enriched overhead stream (claim 42, step (b)) and (2) an increase in the amount of methyl iodide recoverable during a subsequent extraction of the raffinate stream, which increase in recoverable methyl iodide would be recognized as more than insubstantial by the ordinary artisan.” slip op. at 42
- Skill levelSkill level petitioner adoptedDecided for petitioner
“Mr. Jones and Dr. Porcelli agree the description in the ’507 patent implies that the inventive process is a low water process. Ex. 1039 ¶ 52; Ex. 2029 ¶ 26. As discussed in Section VI. B., below, these experts further agree that there are differences in the reactants and reaction products produced in high and low water processes. We find both Mr. Jones and Dr. Porcelli are qualified to give an opinion as to the level of ordinary skill in the art. Accordingly, for purposes of this proceeding we adopt Mr. Jones’s definition of the level of ordinary skill in the art, and add that the ordinary artisan also would have had a specific understanding of the low water carbonylation process for production of acetic acid and its implementation on an industrial scale.” slip op. at 27
- Novelty / Anticipation (§102) › Anticipation standard (single reference, every element) › Inherent disclosureNot shown unpatentableInherency not foundNot shown unpatentable
“We are not persuaded that Mr. Jones’s calculations provide a reliable method of determining the amount of DME present in a methanol carbonylation process. Mr. Miura and Dr. Porcelli agreed that it is extremely difficult to anticipate the presence or amount of a component such as DME in a methanol carbonylation system such as the one described in the ’095 patent. See Ex. 1046, 281:14–22; Ex. 2029 ¶ 112. Dr. Porcelli testified that Mr. Jones’s estimates of DME content in the ’095 patent Example were based on numerous assumptions that rendered his estimations of reactor and distillation overhead DME concentrations meaningless. See Ex. 2029 ¶¶ 137, 140, 151. Dr. Porcelli testified, for example, that it was “improper and incorrect” for Mr. Jones “to fail to account for DME lost with the vent stream in the reactor, especially because of the high volatility of DME.” Id. ¶ 148. Mr. Miura’s measured amount of DME present in the first overhead in Experiment 1 was less than half the amount Mr. Jones calculated would be present, supporting Dr. Porcelli’s testimony that the loss of DME via the vents would have had a marked impact on the actual amount of DME sent to distillation column 40 (from which the second overhead stream is produced) in the ’095 patent Example. See Ex. 1060 ¶ 153 (“(103 ppm (calc.) vs. 48 ppm (actual)) is likely to due to loss of DME with the vent gas from the splitter condenser, due to the very low boiling point of DME”); see also Ex. 1039 ¶ 99; Ex. 1060 ¶ 121 (wherein Mr. Jones agreed that the loss of DME from the vent stream in the separator (or decanter) after splitter column 14 in the ’095 patent process would be substantial).” slip op. at 56
- Obviousness (§103) › Motivation to combine / reasonable expectation of successNot shown unpatentableNot shown unpatentable
“In sum, we determine Petitioner has failed to meet its burden to show, by a preponderance of the evidence, that the ’095 patent describes a process that inherently results in dimethyl ether in a PRC enriched overhead stream (produced by distilling a mixture comprising water, acetic acid, methyl iodide, methyl acetate, methanol, and at least one PRC) in an amount that is (1) more than trace or insubstantial, and (2) sufficient to cause (a) a reduction in the solubility of methyl iodide in water during extraction of the PRC enriched overhead stream and (b) an increase in the amount of methyl iodide recoverable during a subsequent extraction of the raffinate stream, as required by the broadest reasonable interpretation of claim 42. Absent from the record is any evidence that DME is present in the second overhead in the ’095 patent Example in the amount required by independent claim 42 and its dependent claims 43, 44, 47–51, 53, and 55–57. Petitioner’s challenge with respect to claim 57 is based on obviousness over the combination of the ’095 patent and JP ’712. Petitioner relies on JP ’712 for a teaching that “methyl iodide concentration can be controlled by extraction temperature, . . . and that the concentration[] recited in [claim 57 is] well known in the art.” Pet. 55. Petitioner has not explained how JP ’712 cures the deficiency in the ’095 patent’s failure to describe step (a) of claim 42. Accordingly, we likewise determine Petitioner has failed to meet its burden to show unpatentability of claim 57 by a preponderance of the evidence. We conclude Petitioner has failed to meet its burden to show unpatentability of claims 42–44, 47–51, 53, and 55–57 of the ’507 patent.” slip op. at 59
Patent outcomesUS 8,076,507 not shown unpatentableClaim construction§ 102 anticipation§ 103 obviousnesscites KSRPatents in suitUS 8,076,507 - Daicel Corporation v. Celanese International CorporationNo claims unpatentablePTAB · Jun 23, 2016 · IPR2015-00173 · APJ Linda M Gaudette · IPR · Final written decision
Claims 58–60, 67, 69, and 71–72 were not shown unpatentable over the ’095 patent; claim 73 was not shown unpatentable over the ’095 patent and JP ’712 because the required amount of DME was not …
RulingsFinal written decision- Skill levelSkill level petitioner adoptedDecided for petitioner
“Petitioner relies on Mr. Jones’s testimony to establish the level of ordinary skill in the art. See Pet. 17. Mr. Jones testified that the person of ordinary skill in the art “as of March 2, 2004, the effective filing date of the ’507 Patent” (Ex. 1039 ¶ 15) would have been a chemist or chemical engineer with an advanced degree, or a Bachelor of Science degree and equivalent work experience (e.g., five years in an industrial setting producing acetic acid, acetic anhydride, or related chemicals), and would have generally understood acetic acid production on an industrial scale including the distillation processes and extraction processes that are used in acetic acid or acetic anhydride production. The person of ordinary skill in the art would have understood chemical reactions in general, and, particularly, the primary reactions and the side-reactions associated with acetic acid production (id. ¶ 16). Mr. Jones further testified that a person of ordinary skill in the art would have had separations experience, an understanding of industrial-scale processes, and experience in the production of acetic acid, acetic anhydride, or related chemicals. Id. ¶ 17. Dr. Porcelli, testified that he “generally agree[s]” with Mr. Jones’s opinion as to the level of ordinary skill in the art” (Ex. 2029 ¶ 15; see also Ex. 1065, 65:9–66:5). During cross-examination, however, Dr. Porcelli testified that one of ordinary skill in the art would require, more specifically, an understanding of the low water acetic process and its implementation on an industrial scale. See, e.g., Ex. 1065, 126:18–127:1.” slip op. at 26
- Claim Construction › Threshold & procedure › Whether a term needs construction (O2 Micro)Term construed patent owner constructionOther
“Based on our analysis of the intrinsic and extrinsic evidence, we agree with Patent Owner that a person of ordinary skill in the art would understand the ’507 patent to speak in terms of effects, not molecules. See PO Resp. 4– 5; Tr. 41:8–16. We, therefore, construe the recitation “distilling [a mixture comprising water, acetic acid, methyl iodide, methyl acetate, methanol, and at least one PRC] to separate the mixture into a plurality of streams, at least one of said streams being a PRC enriched overhead stream comprising dimethyl ether” in step (a) of claim 58 as requiring the presence of dimethyl ether in the PRC enriched overhead stream in an amount that one of ordinary skill in the art would recognize as being more than trace or insubstantial. Such amount would be, for example, more than the amount produced in a conventional, prior art, low water carbonylation process that used the same initial reactor contents and conditions, and the same processing equipment. We further interpret this language as requiring the presence of DME in the PRC enriched overhead stream in an amount sufficient to cause (1) a reduction in the solubility of methyl iodide in water during the extraction of the PRC enriched overhead stream and (2) an increase in the amount of methyl iodide recoverable during the subsequent extraction of the first raffinate stream (claim 58, step (b)), which increase in recoverable methyl iodide would be recognized as more than insubstantial by the ordinary artisan.” slip op. at 42
- Expert testimonyPetitioner expert discountedDecided for patent owner
“We are not persuaded that Mr. Jones’s calculations provide a reliable method of determining the amount of DME present in a methanol carbonylation process. Mr. Miura and Dr. Porcelli agreed that it is extremely difficult to anticipate the presence or amount of a component such as DME in a methanol carbonylation system such as the one described in the ’095 patent. See Ex. 1046, 281:14–22; Ex. 2029 ¶ 112. Dr. Porcelli testified that Mr. Jones’s estimates of DME content in the ’095 patent Example were based on numerous assumptions that rendered his estimations of reactor and distillation overhead DME concentrations meaningless. See Ex. 2029 ¶¶ 137, 140, 151. Dr. Porcelli testified, for example, that it was “improper and incorrect” for Mr. Jones “to fail to account for DME lost with the vent stream in the reactor, especially because of the high volatility of DME.” Id. ¶ 148. Mr. Miura’s measured amount of DME present in the first overhead in Experiment 1 was less than half the amount Mr. Jones calculated would be present, supporting Dr. Porcelli’s testimony that the loss of DME via the vents would have had a marked impact on the actual amount of DME sent to distillation column 40 (from which the second overhead stream is produced) in the ’095 patent Example. See Ex. 1060 ¶ 153 (“(103 ppm (calc.) vs. 48 ppm (actual)) is likely to due to loss of DME with the vent gas from the splitter condenser, due to the very low boiling point of DME”); see also Ex. 1039 ¶ 97; Ex. 1060 ¶ 121 (wherein Mr. Jones agreed that the loss of DME from the vent stream in the separator (or decanter) after splitter column 14 in the ’095 patent process would be substantial). Dr. Porcelli testified that he believed removal of DME by rapid carbonylation would have had a significant effect on the presence of DME in the ’095 patent Example and that this irreversible reaction should have been considered by Mr. Jones in his calculations. Ex. 2029 ¶¶ 130–131. Mr. Jones conceded “some DME will be carbonylated in the reactor” (Ex. 1060 ¶ 45), and that the carbonylation of DME to make acetic acid under low water conditions is an irreversible reaction (Ex. 2026, 227:19–228:1). See also Ex. 1060 ¶ 27 (arguing Exhibits 2032, 2034 evidence DME formation in a batch reactor during methanol carbonylation, but admitting that as the water and methyl acetate start to diminish, DME concentration begins to drop and DME is eventually carbonylated into either acetic acid or acetic anhydride). Mr. Jones disagreed with Dr. Porcelli’s testimony that “carbonylation of DME is . . . known to have a fast reaction rate” and “would be consumed by carbonylation faster than it would be formed by methanol dehydration, especially under low water conditions” (Ex. 2029 ¶ 130). Ex. 1060 ¶ 44. Mr. Jones provided testimony explaining why he believes “the carbonylation of DME is not particularly fast.” Id.; see id. ¶¶ 45–48. Mr. Jones relied on a textbook by Gauthier-Lafaye (Ex. 1062), published in 1987, as evidence that the carbonylation of DME proceeds more slowly than the carbonylation of methyl acetate. Ex. 1060 ¶ 47. Mr. Jones testified that because the reaction liquid in the ’095 patent Example is reported to contain 1.6 wt% methyl acetate, and the carbonylation rate of DME is even slower than that of methyl acetate, then “it stands to reason that the carbonylation rate of DME is not going to be so fast as to ‘immediately’ react away any DME that is formed via the methanol dehydration equilibrium reaction.” Id. ¶ 48. Mr. Jones further testified that consideration of this competing side reaction was “irrelevant to calculating equilibrium concentration” of DME in the reactor in the ’095 patent Example. Id. ¶ 51. The disclosure in Gauthier-Lafaye relied upon by Mr. Jones relates to the carbonylation of methyl acetate into acetic anhydride (Ex. 1062, 9), i.e., a different reaction system than the ’095 and ’507 patents (see Paper 73, 8 (Observation #F.1)). This evidence, therefore, does not support Mr. Jones’s testimony that the carbonylation of DME in the ’095 patent reaction system was irrelevant to his calculation of equilibrium DME concentration. Rather we credit Dr. Porcelli’s testimony that removal of DME by rapid carbonylation would have had an effect on the presence, or at least the quantity, of DME in the ’095 patent Example, and that this factor should have been taken into consideration by Mr. Jones in his calculations. See Ex. 2029 ¶ 130. Mr. Jones testified that in view of the low boiling point of DME (-23.7 ºC), most of the DME will immediately flash from the reactor product . . . and be concentrated in the overhead streams. In view of the relatively low amount of DME in the reactor and overhead, DME’s very low boiling point, and the elevated temperatures in the reactor, special handling techniques would be needed to sample for such a compound in the reaction mixture. It is therefore not surprising that the presence of DME was not measured in the ’095 patent, despite the fact that it was undoubtedly present. Ex. 1060 ¶ 118. Given Mr. Miura’s testimony that he believed DME, if present, would have been detectable (Ex. 1046, 280:9–281:1), and Paulik’s disclosure that insubstantial amounts of DME were measurable as early as 1970 (see, e.g., Ex. 2037, 13:47–49, 15:32–34), Mr. Jones’s testimony (see, e.g., Ex. 1060 ¶ 101 (“It should be clear to someone skilled in the art that very dilute and trace components are frequently not reported in chemical analytical results or in listed process stream compositions.”)) does not show convincingly that DME was present in the second overhead in more than a trace quantity, if at all. See id. ¶ 90 (“[T]he only issue is whether some amount of DME exists (which clearly it does).”).” slip op. at 56
- Novelty / Anticipation (§102) › Anticipation standard (single reference, every element) › Inherent disclosureNot shown unpatentableInherency not foundNot shown unpatentable
“have been present in the distillation overhead in the ’095 patent Example in an amount sufficient to reduce solubility of methyl iodide in water during subsequent water extraction steps. Mr. Miura testified that 1.2 wt% DME was present in the second overhead in Experiment 1. Ex. 1005 ¶ 13, Table 1. Mr. Jones testified that he would expect the amount of DME in the second overhead in the ’095 patent process to be about three times the amount of DME in the overhead in Miura Experiment 1 (Ex. 2040, 289:10–– 298:7), because Mr. Miura’s experiment was carried out under conditions less favorable to DME formation as compared to the conditions in the ’095 patent Example (see Ex. 1060 ¶¶ 130, 139). A preponderance of the evidence, however, does not support a finding that DME was present, if at all, in more than a trace quantity/insubstantial amount in the second overhead of the ’095 patent Example, for the following reasons: Although Mr. Miura reported that the second overhead in his Experiment 1 contained 1.2% DME (Ex. 1005 ¶ 13, Table 1), he did not testify that this quantity would be present in the ’095 patent Example despite acknowledged differences in quantities of reaction components and operating conditions (see id. ¶ 21). Rather, Mr. Miura testified that Experiment 1 provided evidence that DME simply was present in some amount in the second overhead in the ’095 patent Example. Id. (“[T]he deviations would not affect the outcome with respect to the presence of DME in the first and second overheads.”). Mr. Miura testified that he supervised the ’095 patent Example and believed DME was present and accounted for in the 0.9 wt% reported as “others.” Ex. 1046, 241:17–242:9. Therefore, we are not persuaded by Mr. Jones’s testimony that the amount of DME in the second overhead in the ’095 patent process would be about three times the amount of DME in the overhead in Miura Experiment 1, i.e. 3.6 wt% (Ex. 2040, 289:10––298:7). See Tr. 70:3–8 (wherein Patent Owner’s counsel raises this inconsistency). We are not persuaded by Mr. Jones’s testimony that an amount as high as 3.6 wt% DME could have been present in the ’095 patent Example, but not reported (see Ex. 2040, 301:18–303:2; Paper 73, 5–6 (Observation #C.4)), since the prior art, e.g., Paulik, clearly indicates DME was considered an undesirable reaction byproduct in a carbonylation process. Mr. Miura did not testify as to what portion of the 0.9 wt% reported as “others” in the ’095 patent Example constituted DME, or whether the amount of DME would be considered more than a trace quantity/insubstantial amount. Nor is there any testimony or evidence that 0.9 wt% or less DME in the overhead/feed to the extractor would have been an amount sufficient to cause a reduction in the solubility of methyl iodide in water during extraction of the PRC enriched overhead stream and an increase in the amount of methyl iodide recoverable during the subsequent extraction of the first raffinate stream as required under the broadest reasonable interpretation of claim 58 of the ’507 patent. We are not persuaded that Mr. Jones’s calculations provide a reliable method of determining the amount of DME present in a methanol carbonylation process. Mr. Miura and Dr. Porcelli agreed that it is extremely difficult to anticipate the presence or amount of a component such as DME in a methanol carbonylation system such as the one described in the ’095 patent. See Ex. 1046, 281:14–22; Ex. 2029 ¶ 112. Dr. Porcelli testified that Mr. Jones’s estimates of DME content in the ’095 patent Example were based on numerous assumptions that rendered his estimations of reactor and distillation overhead DME concentrations meaningless. See Ex. 2029 ¶¶ 137, 140, 151. Dr. Porcelli testified, for example, that it was “improper and incorrect” for Mr. Jones “to fail to account for DME lost with the vent stream in the reactor, especially because of the high volatility of DME.” Id. ¶ 148. Mr. Miura’s measured amount of DME present in the first overhead in Experiment 1 was less than half the amount Mr. Jones calculated would be present, supporting Dr. Porcelli’s testimony that the loss of DME via the vents would have had a marked impact on the actual amount of DME sent to distillation column 40 (from which the second overhead stream is produced) in the ’095 patent Example. See Ex. 1060 ¶ 153 (“(103 ppm (calc.) vs. 48 ppm (actual)) is likely to due to loss of DME with the vent gas from the splitter condenser, due to the very low boiling point of DME”); see also Ex. 1039 ¶ 97; Ex. 1060 ¶ 121 (wherein Mr. Jones agreed that the loss of DME from the vent stream in the separator (or decanter) after splitter column 14 in the ’095 patent process would be substantial).” slip op. at 55
Patent outcomesUS 8,076,507 not shown unpatentableClaim construction§ 102 anticipation§ 103 obviousnesscites KSRPatents in suitUS 8,076,507 - Daicel Corporation v. Celanese International CorporationNo claims unpatentablePTAB · Jun 23, 2016 · IPR2015-00170 · APJ Linda M Gaudette · IPR · Final written decision
Claims 1–4, 6–11, and 13 were not held unpatentable under § 103 because the evidence did not show the required amount of dimethyl ether in the second overhead.
RulingsFinal written decision- Claim Construction › Threshold & procedure › Whether a term needs construction (O2 Micro)Term construed patent owner constructionDecided for patent owner
“Based on our analysis of the intrinsic and extrinsic evidence, we agree with Patent Owner that a person of ordinary skill in the art would understand the ’507 patent to speak in terms of effects, not molecules. See PO Resp. 50–51; Tr. 41:8–16. We, therefore, construe the recitation “distilling at least a portion of [a] first overhead [comprising methyl iodide, water and at least one PRC] to produce a second overhead stream comprising . . . dimethyl ether” in step (a) of claim 1 as requiring the presence of dimethyl ether in the second overhead stream in an amount that one of ordinary skill in the art would recognize as being more than trace or insubstantial. Such amount would be, for example, more than the amount produced in a conventional, prior art, low water carbonylation process that used the same initial reactor contents and conditions, and the same processing equipment. We further interpret this language as requiring the presence of DME in the second overhead stream in an amount sufficient to cause (1) a reduction in the solubility of methyl iodide in water during the extraction of the second overhead (claim 1, step (b)) and (2) an increase in the amount of methyl iodide recoverable during the extraction of the first raffinate (claim 1, step (c)), which increase in recoverable methyl iodide would be recognized as more than insubstantial by the ordinary artisan.” slip op. at 43
- Skill levelSkill level petitioner adoptedDecided for petitioner
“Patent Owner substantially agrees with Mr. Jones’s opinion, stating: “a person of ordinary skill in the art may be a qualified chemist or chemical engineer, however separations experience, an understanding of industrial-scale processes, and experience in the production of acetic acid, acetic anhydride, or related chemicals is required.” PO Resp. 14. Dr. Porcelli, testified that he “generally agree[s]” with Mr. Jones’s opinion as to the level of ordinary skill in the art” (Ex. 2029 ¶ 15; see also Ex. 1065, 65:9–66:5). During cross-examination, however, Dr. Porcelli testified that one of ordinary skill in the art would require, more specifically, an understanding of the low water acetic process and its implementation on an industrial scale. See, e.g., Ex. 1065, 126:18–127:1. Mr. Jones and Dr. Porcelli agree the description in the ’507 patent implies that the inventive process is a low water process. Ex. 1039 ¶ 50; Ex. 2029 ¶ 26. As discussed in Section VI. B., below, these experts further agree that there are differences in the reactants and reaction products produced in high and low water processes. We find both Mr. Jones and Dr. Porcelli are qualified to give an opinion as to the level of ordinary skill in the art. Accordingly, for purposes of this proceeding we adopt Mr. Jones’s definition of the level of ordinary skill in the art, and add that the ordinary artisan also would have had a specific understanding of the low water carbonylation process for production of acetic acid and its implementation on an industrial scale.” slip op. at 27
- Obviousness (§103) › Graham factors (scope of art, differences, level of skill)Not shown unpatentableNot shown unpatentable
“at least one PRC] to produce a second overhead stream comprising . . . dimethyl ether” as requiring the presence of dimethyl ether in the second overhead stream in an amount that is (1) more than trace or insubstantial, and (2) sufficient to cause (a) a reduction in the solubility of methyl iodide in water during extraction of the second overhead and (b) an increase in the amount of methyl iodide recoverable during the extraction of the first raffinate. Neither Mr. Miura nor Mr. Jones testified that dimethyl ether would have been present in the second distillation overhead in the ’095 patent Example in an amount that is (1) more than trace or insubstantial, and (2) sufficient to cause (a) a reduction in the solubility of methyl iodide in water during extraction of the second overhead and (b) an increase in the amount of methyl iodide recoverable during the extraction of the first raffinate. Mr. Miura testified that 1.2 wt% DME was present in the second overhead in Experiment 1. Ex. 1005 ¶ 13, Table 1. Mr. Jones testified that he would expect the amount of DME in the second overhead in the ’095 patent process to be about three times the amount of DME in the overhead in Miura Experiment 1 (Ex. 2040, 289:10––298:7), because Mr. Miura’s experiment was carried out under conditions less favorable to DME formation as compared to the conditions in the ’095 patent Example (see Ex. 1060 ¶¶ 133, 139). A preponderance of the evidence, however, does not support a finding that DME was present, if at all, in more than a trace quantity/insubstantial amount in the second overhead of the ’095 patent Example, for the following reasons:” slip op. at 57
- Expert testimonyPetitioner expert discountedPatent owner expert creditedDecided for patent owner
“We are not persuaded that Mr. Jones’s calculations provide a reliable method of determining the amount of DME present in a methanol carbonylation process. Mr. Miura and Dr. Porcelli agreed that it is extremely difficult to anticipate the presence or amount of a component such as DME in a methanol carbonylation system such as the one described in the ’095 patent. See Ex. 1046, 281:14–22; Ex. 2029 ¶ 112. Dr. Porcelli testified that Mr. Jones’s estimates of DME content in the ’095 patent Example were based on numerous assumptions that rendered his estimations of reactor and distillation overhead DME concentrations meaningless. See Ex. 2029 ¶¶ 137, 140, 151. Dr. Porcelli testified, for example, that it was “improper and incorrect” for Mr. Jones “to fail to account for DME lost with the vent stream in the reactor, especially because of the high volatility of DME.” Id. ¶ 148. Mr. Miura’s measured amount of DME present in the first overhead in Experiment 1 was less than half the amount Mr. Jones calculated would be present, supporting Dr. Porcelli’s testimony that the loss of DME via the vents would have had a marked impact on the actual amount of DME sent to distillation column 40 (from which the second overhead stream is produced) in the ’095 patent Example. See Ex. 1060 ¶ 153 (“(103 ppm (calc.) vs. 48 ppm (actual)) is likely to due to loss of DME with the vent gas from the splitter condenser, due to the very low boiling point of DME”); see also Ex. 1039 ¶ 97; Ex. 1060 ¶ 121 (wherein Mr. Jones agreed that the loss of DME from the vent stream in the separator (or decanter) after splitter column 14 in the ’095 patent process would be substantial). Dr. Porcelli testified that he believed removal of DME by rapid carbonylation would have had a significant effect on the presence of DME in the ’095 patent Example and that this irreversible reaction should have been considered by Mr. Jones in his calculations. Ex. 2029 ¶¶ 130–131. Mr. Jones conceded “some DME will be carbonylated in the reactor” (Ex. 1060 ¶ 45), and that the carbonylation of DME to make acetic acid under low water conditions is an irreversible reaction (Ex. 2026, 227:19–228:1). See also Ex. 1060 ¶ 27 (arguing Exhibits 2032, 2034 evidence DME formation in a batch reactor during methanol carbonylation, but admitting that as the water and methyl acetate start to diminish, DME concentration begins to drop and DME is eventually carbonylated into either acetic acid or acetic anhydride). Mr. Jones disagreed with Dr. Porcelli’s testimony that “carbonylation of DME is . . . known to have a fast reaction rate” and “would be consumed by carbonylation faster than it would be formed by methanol dehydration, especially under low water conditions” (Ex. 2029 ¶ 130). Ex. 1060 ¶ 44. Mr. Jones provided testimony explaining why he believes “the carbonylation of DME is not particularly fast.” Id.; see id. ¶¶ 45–48. Mr. Jones relied on a textbook by Gauthier-Lafaye (Ex. 1062), published in 1987, as evidence that the carbonylation of DME proceeds more slowly than the carbonylation of methyl acetate. Ex. 1060 ¶ 47. Mr. Jones testified that because the reaction liquid in the ’095 patent Example is reported to contain 1.6 wt% methyl acetate, and the carbonylation rate of DME is even slower than that of methyl acetate, then “it stands to reason that the carbonylation rate of DME is not going to be so fast as to ‘immediately’ react away any DME that is formed via the methanol dehydration equilibrium reaction.” Id. ¶ 48. Mr. Jones further testified that consideration of this competing side reaction was “irrelevant to calculating equilibrium concentration” of DME in the reactor in the ’095 patent Example. Id. ¶ 51. The disclosure in Gauthier-Lafaye relied upon by Mr. Jones relates to the carbonylation of methyl acetate into acetic anhydride. Ex. 1062, 9. The ’095 patent, however, relates to production of acetic acid by a carbonylation process, wherein, according to Akinori, “intermediates [e.g. DME and methyl acetate] ultimately change into acetic acid” (Ex. 1013, 8, equations (2), (3)). Ex. 2029 ¶ 130; see Paper 79, 8–9 (Observation #G.1). In other words, the evidence relied on by Mr. Jones relates to a different reaction system and does not support his testimony that the carbonylation of DME in the ’095 patent reaction system was irrelevant to his calculation of equilibrium DME concentration. Rather we credit Dr. Porcelli’s testimony that removal of DME by rapid carbonylation would have had an effect on the presence, or at least the quantity, of DME in the ’095 patent Example, and that this factor should have been taken into consideration by Mr. Jones in his calculations. See Ex. 2029 ¶ 130.” slip op. at 59
Patent outcomesUS 8,076,507 not shown unpatentableClaim construction§ 103 obviousnesscites KSRPatents in suitUS 8,076,507
Holdings, summaries, rulings, issues, outcomes, winners and claim constructions shown for a decision were generated by a large language model reading the opinion. They are a guide to the decision, not the decision. Confirm every one against the court's own text before relying on it. Outcomes read from the patent owner’s side. Party names are extracted from the decision and are missing on about 900 short Director denials and scans, which carry the trial number instead.