`
`
`Ian Donald, et al.
`In re Patent of:
`8,540,018 Attorney Docket No.: 29188-0024IP1
`U.S. Patent No.:
`September 24, 2013
`
`Issue Date:
`Appl. Serial No.: 13/536,433
`
`Filing Date:
`June 28, 2012
`
`Title:
`APPARATUS AND METHOD FOR RECOVERING
`FLUIDS FROM A WELL AND/OR INJECTING FLUIDS
`INTO A WELL
`
`DECLARATION OF ROBERT HERRMANN
`
`I.
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`Personal Work Experience and Awards
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`1. My name is Robert P. Herrmann. I am currently an industry
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`
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`consultant in the field of offshore oil operations and a Licensed Professional
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`Engineer. In addition to the below summary, a copy of my current curriculum vitae
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`more fully setting forth my experiences and qualifications is submitted herewith as
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`Appendix A.
`
`2.
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`I have more than 42 years of professional experience in Mechanical
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`Engineering, particularly in the area of offshore oil operations. I received a B.S. in
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`Mechanical Engineering from the University of Houston in 1972 and a M.S. in
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`Mechanical Engineering from the University of Houston in 1973. Further, I have
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`authored numerous published technical papers, delivered lectures and moderated
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`professional conferences in the area of offshore oil operations. In 2015, I was
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`inducted into the Ocean Energy Offshore Hall of Fame.
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`3.
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`From 1973-1990, I held various positions with Sonat Offshore
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`Drilling, working on several deep water design projects including all aspects of
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`offshore oil operations. From 1973-1976, I was Project Manager for the design and
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`construction of the Discoverer Seven Seas deep water drillship. From 1976 to
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`1977, I was Technical Supervisor, managing operation of a dynamically positioned
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`drillship, identifying and developing solutions to technical issues. From 1977 to
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`1979, I was Engineering Manager and Managing Director for Sonat’s foreign
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`branch. From 1979 to 1984, I was Division Manager, Discoverer Seven Seas,
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`managing all aspects of offshore operations for a dynamically positioned drilling
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`vessel, including developing new operations and techniques to improve
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`performance and efficiency in deepwater operations. From 1984 to 1985, I was
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`Operations Manager-Contracts, providing technical and operational input for all
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`project bids. From 1985 to 1988, I was Senior Contracts and Sales Representative,
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`directing engineering, planning and supervision of offshore operation for various
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`deepwater installations. From 1989 to 1990, I was International Contracts & Sales
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`Manager, managing bids internationally.
`
`4.
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`In 1991, I served as a consultant to Conoco, Wilrig, Huthnance and
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`Odfjell in the area of offshore oil operations.
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`5.
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`From 1991 to 1993 I was General Manager at Wilrig, running a two
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`rig deep water drilling operation off Brazil.
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`6.
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`From 1993 to 2015, I served as a Consult in the field of offshore oil
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`operations to a number of companies including BPAmoco, Transocean, Repsol,
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`Encana, Petrobras, Japan Drilling Co. and Cobalt International, providing expertise
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`in areas such as flow assurance and field development concepts, running flowlines
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`and other subsea equipment from drillships, drillship design, field development,
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`well extension, and subsea tree and jumper design, installation and operation.
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`7.
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`In 1990, I served as an expert witness in a dispute involving
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`ConocoPhillips and Reading & Bates Corporation in the field of offshore oil
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`operations.
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`8.
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`Throughout my career, I have been actively involved in numerous
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`professional organizations. I was the Session Chairman/Session Moderator for the
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`Deep Ocean Technology Conferences in Spain (1981), Malta (1983), Italy (1985),
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`and Monaco (1987). I was a member of the American Bureau of Shipping British
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`Technical Committee and United States Congressional Committee of the Office of
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`Technology Assessment - Subcommittee for Deepwater Drilling Evaluation.
`
`9.
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`Based on my above-described 42 years of experience in Mechanical
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`Engineering in the area of offshore oil operations, and the acceptance of my
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`publications and professional recognition by societies in my field, I believe that I
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`am considered to be an expert in the field of offshore oil operations.
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`II. Materials Considered
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`10.
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`In writing this Declaration, I have considered the following: my own
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`knowledge and experience, including my work experience in the field of offshore
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`oil operations; my industry experience this field; and my experience in working
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`with others involved in this field. I have also analyzed the following publications
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`and materials, in addition to other materials I cite in my declaration:
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` U.S. Pat. No. 8,540,018 and its accompanying prosecution history (“the
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`’018 Patent”, Exs. 1001, 1002)
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` U.S. Pat. No. 4,589,493 (“Kelly”, Ex. 1004)
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` U.S. Pat. Pub. No. 2002/0070026 (“Fenton”, Ex. 1005)
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` U.S. Pat. No. 6,481,504 (“Gatherar”, Ex. 1006)
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` U.S. Pat. No. 5,010,956 (“Bednar”, Ex. 1007)
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` U.S. Pat. No. 4,190,114 (“Fisher”, Ex. 1008)
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` U.S. Pat. No. 8,776,893 (“Donald”, Ex. 1010)
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` U.S. Pat. No. 2,638,917 (“Clair”, Ex. 1011)
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` U.S. Pat. No. 6,782,949 (“Cove”, Ex. 1012)
`
`11.
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`I am not currently and have not at any time in the past been an
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`employee of FMC, Inc. I have been engaged in the present matter to provide my
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`independent analysis of the issues raised in the petition for inter partes review of
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`the ’018 Patent. I received no compensation for this declaration beyond my normal
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`hourly compensation based on my time actually spent studying the matter, and my
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`compensation does not depend on the outcome of this inter partes review of the
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`’018 Patent.
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`III. Person of Ordinary Skill in the Art
`
`12.
`
`I am familiar with the content of the ’018 Patent. Additionally, I have
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`reviewed the other references cited above in this declaration. Counsel has informed
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`me that I should consider these materials through the lens of one of ordinary skill
`
`in the art related to the ’018 Patent at the time of the invention, which for the
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`purposes of this analysis I am treating as 2004 (although in many cases the same
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`analysis would hold true even at an earlier time). I believe that a person having
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`ordinary skill in the art of the ’018 Patent (“POSITA”) would have had a Bachelor
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`of Science Degree in Mechanical Engineering with at least two years of related
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`work experience in subsea oil and gas production systems. Individuals with
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`different education and additional experience could still be of ordinary skill in the
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`art if that additional experience compensates for a deficit in their education stated
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`above. I base my evaluation of a person of ordinary skill in this art on my own
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`personal experience, including my knowledge of colleagues and related
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`professionals at the time of interest.
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`IV. Claim Construction
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`13.
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`I understand that, for the purposes of my analysis in this matter, the
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`claims of the ‘018 Patent must be given their broadest reasonable interpretation
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`consistent with the specification. Stated another way, it is contemplated that the
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`claims are understood by their broadest reasonable interpretation except where
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`construed in the specification. I also understand that this “broadest reasonable
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`interpretation” is with respect to how one of ordinary skill in the art would
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`interpret the claim language. I have followed these principles in my analysis. In a
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`few instances, I have discussed my understanding of the claims in the relevant
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`paragraphs below.
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`V. Kelly
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`14. Kelly describes a subsea system, and in particular, “subsea wellhead
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`production apparatus including a retrievable subsea choke.” Kelly, Abstract. The
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`choke is landable and retrievable. Kelly, 1:60-65. A choke is a type of valve that
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`controls the flow by constricting a flow area. Historically, pressure drop across a
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`choke was used to measure the flow rate.
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`15. Kelly’s system includes a manifold that communicates with the bore
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`of the well. In particular, Kelly describes a “Christmas tree 18.” Kelly 2:21-22. A
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`Christmas tree can be called a manifold, and typically includes a production branch
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`and an annulus branch in communication with the well bore. This is true of Kelly’s
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`tree. The tubing defining the production and annulus branches of Kelly’s tree are
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`unnumbered, but shown extending left to right in FIG. 2. Kelly shows a “subsea
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`choke assembly 26” on the production branch. The production and annulus
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`branches are called “branches,” because they are like branches of a tree that branch
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`out from its trunk. In FIG. 1, the concentric circles on the “Christmas tree 18” and
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`its branches represent valves. I can see several valves in FIG. 2, as well as a
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`crossover valve spanning between the production and annulus branches. Kelly’s
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`“Christmas tree 18” is connected to the well’s “casing 12.” Kelly 2:16-29. Inside
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`that casing are concentric strings of pipe, some of which communicate with the
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`production reservoir; thus Kelly’s “Christmas tree 18” is connected to the well
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`bore.
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`16.
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`In operation, fluids flow upwardly from the well through “well casing
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`12,” into the vertical portion of “Christmas tree 18,” laterally out through the
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`production branch from the “Christmas tree 18” and into “line 20” and a “collet
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`body 22.” Kelly, 2:22-27. The flow of fluids is turned by the bend in “line 20” and
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`directed by “collet body 22” to flow into “subsea choke assembly 26.” Fluids
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`exiting “subsea choke assembly 26” are returned by “collet body 22” to the branch
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`at “line 24.” Fluids flowing through the branch are directed, i.e. diverted, away
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`from the branch by “line 20” and “collet body 22” such that the fluids must pass
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`through “subsea choke assembly 26,” before fluids are returned to the branch at
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`“line 24.” “Line 20” and “collet body 22” are directly coupled to the “Christmas
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`tree 18” and “line 24.”
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`17. As I mentioned above, a choke is a type of valve that controls flow by
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`constricting a flow area. Kelly’s choke, for example, constricts flow between a
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`“valve member 80” and a “valve seat 78.” Kelly, 1:43-54; 2:66-3:9; 3:13-19. In
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`other words, “valve member 80” of “subsea choke assembly 26” is adjustable to
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`control the fluid flow and pressure of the production fluids. As such, Kelly’s
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`“subsea choke assembly 26” is a processing apparatus, because it processes fluid
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`by reducing fluid flow and pressure. Additionally, Kelly’s choke processes fluid by
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`operating as a gas separator. Chokes are used to reduce the pressure of the high
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`pressure fluids produced from the well. Kelly concerns oil and gas, where the
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`fluids are multiphase, i.e., liquid and gas, and include water, oil and natural gas.
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`The pressure and temperature change experienced by the fluid passing through the
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`choke flashes the fluid and changes the ratio of liquid to gas. Also, because the
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`fluid received into Kelly’s choke passes near the fluid leaving the choke, the higher
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`temperature fluid entering the choke heats the fluid exiting the choke, which has
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`been flashed and is at a lower temperature. Changing the gas to liquid ratio and
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`heating the fluid are, in my opinion, processing the fluid.
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`18.
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` “Line 20” and “collet body 22” include internal passages that allow
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`fluid to pass from the branch to “subsea choke assembly 26” and back to the
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`branch at “line 24.” The internal passages are in fluid communication with the
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`branch to allow such fluid flow.
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`19. Kelly describes “line 24 connects from collet body 22 to the subsea
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`flowline,” and provides a branch outlet where “line 24” connects to the flowline.
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`Kelly, 2:22-25; FIG. 2. The flow path through the assembly provided at least by
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`portions of “inlet 68,” “passage 94,” “passage 74,” and “outlet 70,” is in fluid
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`communication with the branch outlet at the outlet of line 24. Fluid flows from
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`“line 20” and “collet body 22” through the passage through the “subsea choke
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`assembly 26” and back to the branch at “line 24” before fluids proceed through
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`“line 24” to the branch outlet.
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`20.
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` “Collet body 22,” and the web of solid material of “collet body 22”
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`between passages 64 and 66, functions as a barrier that separates a branch inlet at
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`an interface between the vertical portion of “Christmas tree 18” and the horizontal
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`tubing of “Christmas tree 18,” and a branch outlet at an interface between “line 24”
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`and the “flowline.” Due at least in part to the separate flow paths of passages 64
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`and 66 defined by “collet body 22,” produced fluids must flow from “passage 64”
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`to “subsea choke assembly 26” before entering “passage 66” and continuing to
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`“line 24.” Kelly, 2:22-65. The separate flow paths of “collet body 22” prevent
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`direct flow between the branch inlet and the branch outlet by directing flow into
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`“subsea choke assembly 26” and from there to a portion of the branch near the end
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`of “line 24” in communication with the branch outlet.
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`21. The assembly defined by “line 20” and “collet body 22” is sealed
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`between first and second regions of the branch to block direct fluid communication
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`between the first and second regions. If it were not sealed, the fluids passing
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`through the branch would leak into the surrounding sea.
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`22. As discussed previously, fluids are directed by “line 20” and “collet
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`body 22” into “subsea choke assembly 26” before returning to the branch at “line
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`24” and continuing to the branch outlet at an interface between “line 24” and the
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`“flowline.” During construction of Kelly’s system, “line 20” and “collet body 22”
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`are installed into the flow path.
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`VI. Kelly and Fenton
`
`23. Both Kelly and Fenton describe subsea well systems that include
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`retrievable choke components. As discussed previously, Kelly describes a
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`“Christmas tree 18” connected to “subsea choke assembly 26” (i.e., a retrievable
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`processing apparatus). Adjustable choke assemblies, such as "choke assembly 77"
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`described by Fenton, were traditionally used in the art for controlling flow and
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`pressure in subsea well equipment, and were widely used with temperature and
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`pressure sensors to monitor fluid flow to allow the choke to be appropriately
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`adjusted. See Fenton, Abstract; [0005]-[0007].
`
`24. Fenton describes a “production module 61” having a “tree connector
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`63 on its lower end” and adapted to land on a Christmas tree. Fenton, Abstract;
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`[0003]; [0007]; [0011-0014]; [0017]. “Production module 61” includes one or
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`more devices “for controlling or measuring flow, such as a choke, a pressure or
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`temperature sensor, or a flow meter.” Fenton, [0018].
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`
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`25.
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`In practice, Kelly’s “subsea choke assembly 26” would have included
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`upstream and downstream temperature and pressure sensors, and the pressure drop
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`would have been used to measure the flow rate through the assembly. In my
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`opinion, one of ordinary skill would have understood Kelly’s subsea choke
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`assembly to include temperature and pressure sensors, like the sensors taught by
`
`Fenton, that provide information on the fluid flow through the subsea choke
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`assembly, which would, in turn, allow precise control of the choke to achieve
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`target flow characteristics. See Fenton, [0018]. Fenton’s “production module 61”
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`includes both an “upstream pressure and temperature sensor 79 locate[d] on the
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`upstream side of choke 77,” and a “downstream pressure and temperature sensor
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`81 locate[d] on the downstream side of choke assembly 77,” allowing flow
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`characteristics to be monitored on each side of choke assembly 77. Such an
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`arrangement is commonplace in subsea choke devices to monitor the pressure drop
`
`and temperature drop across the choke. See, e.g., Fenton, [0005]; Cove, 2:18-31.
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`26. Furthermore, a person of ordinary skill would position the one or
`
`more sensors within “subsea choke assembly 26” (i.e. instead of elsewhere on
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`Kelly’s subsea production wellhead apparatus) in order to measure the parameters
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`at the relevant locations in the flow, i.e., near the flow constriction caused by the
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`choke. Additionally, providing the sensors within the “subsea choke assembly 26”
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`would facilitate retrieval and maintenance of the sensors. Fenton, in fact, advocates
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`positioning the components that are “more active and more susceptible to failure,”
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`including “choke 77, flow meter controls 83 and the pressure and temperature
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`sensors 79, 81,” in “production module 61.” Fenton, [0022]. Accordingly, a person
`
`of ordinary skill would likewise position one or more sensors in Kelly’s “subsea
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`choke assembly 26,” which similarly can be “retrieved from its connection to a
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`subsea wellhead independent of the remainder of the components to which it is
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`connected.” Kelly, 1:55-59.
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`27. As an alternative, a person of ordinary skill would have readily
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`substituted the entire “subsea choke assembly 26” of Kelly with the entire
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`“production module 61” of Fenton. See Fenton, [0014]-[0020]. For example,
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`similar to Kelly’s description of “subsea choke assembly 26,” Fenton describes
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`that “production module 61” includes a “[c]hoke assembly 77” for “variably
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`restricting the flow of production fluid flowing through cross-over passage 73” and
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`that may be “readily retrieved.” Fenton, [0018]; [0022]. In part because Fenton’s
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`“production module 61” is so similar to Kelly’s “subsea choke assembly 26,” the
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`person of ordinary skill would readily know to replace “subsea choke assembly
`
`26” with “production module 61” to provide the added functionality of one or more
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`temperature, pressure or flow sensors for improved flow monitoring and/or more
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`precise control of fluid flow and pressure parameters. Furthermore, the structure of
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`“production module 61” facilitates easy substitution with “subsea choke assembly
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`26.” “Production module 61” includes a connector on its lower end similar to that
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`of “subsea choke assembly 26” and suitable for connection with the existing
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`“collet body 22” described by Kelly. “Production module 61” of Fenton is
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`described as having an “upward-flow passage 71” and a “downward-flow passage
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`75” oriented to be aligned with upward-flow and downward-flow production
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`passages 37 and 51 of tree 31 that could readily be aligned with passages 64 and 66
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`of Kelly. See Fenton, FIG. 2; [0014]; [0015]; [0021]; Kelly, FIG. 3; 2:34-3:35.
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`Given the similarities in connection between “subsea choke assembly 26” and
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`“production module 61,” hardly any further adjustments are necessary to ensure a
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`sealed connection and could be readily anticipated by a person of ordinary skill to
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`prevent fluid leakage into the subsea environment.
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`28. Fenton’s “production module 61” includes a “flow loop” defined by
`
`an “upward-flow passage 71,” “cross-over passage 73,” and “downward-flow
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`passage 75.” Fenton, [0017]. The choke and sensors are positioned “in
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`communication with the flow loop of module 61,” which allows fluid
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`communication between the well bore and flowline.
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`29. Kelly describes that, “[w]hen body 30 has been landed on collet body
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`22, passage 64 is aligned with inlet 60 and passage 66 is aligned with outlet 70.”
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`Kelly, 2:61-63. “[S]uitable sealing means, as shown, are provide to maintain sealed
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`communication between these connections.” Kelly, FIG. 3; 2:63-65. The seal
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`(unnumbered) between “passage 64” and “inlet 60” connects the passages 64 and
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`60, sealing against leakage between “subsea choke assembly 26” and the “collet
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`body 22.” The seal between “passage 66” and “outlet 70” connects the passages 66
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`and 70, sealing against leakage between “subsea choke assembly 26” and the
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`“collet body 22.” The seals would be associated with and carried by the “subsea
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`choke assembly 26,” during retrieval and landing, to allow the seals to be replaced
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`when the “subsea choke assembly 26” is retrieved. Such seals are generally not
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`reusable, and even if they were, if the seal were somehow damaged and it was not
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`retrieved, the “subsea choke assembly 26” could not be re-landed without further
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`remediation.
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`VII. Kelly and Bednar
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`30. Bednar describes another manner of incorporating a choke to a subsea
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`tree. Bednar, 2:57-61; see also Abstract; 2:3-39; 3:60-4:10; 4:58-17. In Bednar’s
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`system, fluid from the well is directed through the tree, out the tree cap to a choke
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`assembly, and returned to a connector on the wing of the tree. Bednar, 2:66-3:2;
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`5:15-17; FIG. 2. The flow of fluids through the system can be altered by
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`selectively opening and closing various valves. Produced fluids can either pass
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`through and out the wing branch, “production line 32,” through valves 56 and 34,
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`or can instead be directed upwards through the tree cap and choke assembly before
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`returning to “production line 32” by closing “flow loop isolation valve 56,” and
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`opening “production crown valve 22” and “hub isolation valve 54.” See Bednar,
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`2:66-3:2; 5:15-17; FIG. 2.
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`31. A selectively accessible alternative flow path in parallel with a
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`retrievable choke to allow the production of fluids without passing through the
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`choke, was well known, as illustrated by Bednar. In my opinion, a person of
`
`ordinary skill would have readily modified the system of Kelly to include such a
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`flow path between Kelly’s “line 20” and “line 24” in parallel with “subsea choke
`
`assembly 26,” as taught by Bednar. For example, a person of ordinary skill would
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`have incorporated an additional conduit and a series of valves, such as Bednar’s
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`“production crown valve 22,” “hub
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`isolation valve 54,” and “flow loop
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`isolation valve 56.” The additional
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`valves could readily be incorporated
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`in “line 20,” “line 24” and a line
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`connecting “line 20” and “line 24,” or incorporated in “collet body 22” itself. The
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`modified figure, embedded here, was prepared by Counsel based on my
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`explanation and shows what I think the modification to Kelly might look like.
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`32. Modifying Kelly’s subsea wellhead production apparatus by adding a
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`fluid flow path in parallel with “subsea choke assembly 26,” for example, would
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`provide an alternative to the flow path through “subsea choke assembly 26.” The
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`results of such a combination would have been predictable to a person of ordinary
`
`skill, because adding a flow path parallel to a component that could experience
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`failure was common in the art, as taught by Bednar. See, e.g., Bednar, 5:5-17.
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`Kelly recognized the problem of “high wear rates” presented by chokes, and
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`Bednar expressly described that an advantage of its flowpaths is allowing
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`production “even after subsea choke 38 experiences a failure.” Kelly, 1:17-19;
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`Bednar, 5:7-11. Including a direct path from “line 20” to “line 24” would improve
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`reliability and flexibility in Kelly’s subsea wellhead production apparatus by
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`allowing fluid to flow directly to the flowline in the event “subsea choke assembly
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`26” has failed or is absent. Moreover, providing the valves as in Bednar is
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`necessary to make full use of the alternate flowpath, and would further allow a
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`shorter portion of the internal flowpaths of Kelly’s subsea wellhead production
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`apparatus to be exposed to seawater when the “subsea choke assembly 26” is
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`absent, and thus reduce the amount of clean up flushing required when retrieving
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`and installing the “subsea choke assembly 26.”
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`33. Kelly’s system modified like Bednar, as discussed above, includes a
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`diverter assembly provided by Kelly’s “collet body 22,” and “production crown
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`valve 22,” (which functions as an inlet isolation valve), “hub isolation valve 54,”
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`(which functions as an outlet isolation valve), “flow loop isolation valve 56,” and
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`the flow paths proximate valves 22 and 54, incorporated as taught by Bednar. With
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`the valves selectively opened or closed, fluids may alternatively be directed away
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`from the branch through “collet body 22” into “subsea choke assembly 26,” or
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`flow directly from “line 20” to the branch and on to the “flowline.” For example,
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`when “valve 56,” positioned along a path in parallel with “subsea choke assembly
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`26,” is in a closed positioned, fluids are directed upwards into “collet body 22” and
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`through “subsea choke assembly 26,” instead of flowing directly to “line 24”
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`towards a branch outlet without passing through “subsea choke assembly 26.”
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`34.
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` Kelly describes a flow path through “subsea choke assembly 26”
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`provided by “inlet 68,” “passage 94,” “passage 74,” and “outlet 70.” See Kelly,
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`2:58-3:11; 3:20-28. In the combination of Kelly’s and Bednar’s systems discussed
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`above, the “subsea choke assembly 26” bypasses the branch flow path between
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`“line 20” and “line 24,” and is thus a bypass conduit that bypasses a portion of the
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`branch.
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`35. As discussed previously, fluids may flow either directly from “line
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`20” through the branch and to the flowline, or alternatively may flow through
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`“collet body 22” to “subsea choke assembly 26” such that fluids bypass a portion
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`of the branch. The embodiment described by the ’018 Patent with reference to FIG.
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`34, for example, is nearly identical to the system of Kelly modified like Bednar.
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`The ’018 Patent indicates that “[t]his embodiment therefore enables fluids to travel
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`between the well bore and the aperture 1118 of the wing branch 1114, whilst
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`bypassing the wing branch 1114 itself,” and may be “especially [useful] in wells in
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`which the wing branch valve V2 has stuck in the closed position.” ’018 Patent,
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`31:27-31. The system of Kelly modified like Bednar provides similar advantages
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`by allowing flow directly between “line 20” and the flowline if “subsea choke
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`assembly 26” experiences a failure. See Bednar, 5:5-17.
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`36. Kelly modified like Bednar as described above includes a valve in the
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`branch, analogous to Bednar’s “valve 56,” that provides an internal passage of the
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`diverter assembly that extends within the interior of the branch. “Valve 56” is in
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`fluid communication with the branch flow path, allowing fluid to flow directly to
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`the “flowline” without passing through “subsea choke assembly 26,” when “valve
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`56” is in an open position.
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`37. As discussed previously, Kelly describes “line 24 connects from collet
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`body 22 to the subsea flowline,” and provides a branch outlet where “line 24”
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`connects to the flowline. Kelly, 2:22-25; FIG. 2. The flow path through Kelly’s
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`subsea choke assembly provided at least by portions of “inlet 68,” “passage 94,”
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`“passage 74,” and “outlet 70,” and providing a bypass conduit as discussed
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`previously, is in fluid communication with the branch outlet, in the system of Kelly
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`modified like Bednar.
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`38. Kelly modified like Bednar includes a valve, analogous to Bednar’s
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`“flow loop isolation valve 56,” in parallel with “subsea choke assembly 26.” When
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`in a closed position, “valve 56” provides a barrier that prevents fluid flow directly
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`from “line 20” to the “flowline,” and may be selectively opened to allow fluids to
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`pass to the “flowline” if “subsea choke assembly 26” has failed or is absent. See
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`Bednar, 5:15-17. In my opinion, the arrangement disclosed by Kelly in view of
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`Bednar is functionally equivalent with respect to the elements of claim 4 to the
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`embodiment described by the ’018 Patent with reference to FIG. 34. The ’018
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`Patent indicates that fluids “cannot pass [to] the wing branch 1114 because of the
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`V2 valve which is closed, and they are instead diverted into the cap 1140.” ’018
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`Patent, 31:12-20. “Valve 56” positioned in parallel with “subsea choke assembly
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`26,” when in a closed position, would similarly prevent passage of fluid directly to
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`the “flowline” without first passing through “subsea choke assembly 26.”
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`39.
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`“Flow loop isolation valve 56,” positioned in parallel with “subsea
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`choke assembly 26” in Kelly’s apparatus modified like Bednar, is sealed between a
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`portion of the branch and blocks fluid communication between the first region of
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`the branch adjacent “Christmas tree 18” and the second rejoin adjacent the outlet,
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`when in a closed position.
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`40.
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` Kelly modified in view of Bednar, as discussed previously, includes
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`“flow loop isolation valve 56” positioned in parallel with “subsea choke assembly
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`26” between first and second regions of the branch. Furthermore, during
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`installation of the system, “flow loop isolation valve 56” is installed into the flow
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`path in parallel with “subsea choke assembly 26.” “Valve 56” thus separates first
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`and second regions of the branch and prevents fluid from flowing directly from the
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`well head to the branch outlet when in a closed position.
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`VIII. Kelly, Bednar and Fenton
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`41. One of skill in the art would readily modify the system taught by
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`Kelly and Bednar, discussed above, with Fenton to incorporate one or more
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`pressure, temperature or flow sensors. In my opinion, a person of ordinary skill
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`would be motivated to incorporate Fenton’s sensors or “production module 61”
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`into the system of Kelly, modified in view of Bednar, for the same reasons as set
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`forth above with respect to Kelly alone modified in view of Fenton.
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`IX. Bednar
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`42. As discussed above, Bednar describes another manner of
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`incorporating a choke to a subsea tree. Bednar, 2:57-61; see also Abstract; 2:3-39;
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`3:60-4:10; 4:58-5:17. Fluid from the well is directed through the tree, out the tree
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`cap to a choke assembly, and returned to a connector on the wing of the tree.
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`Bednar, 2:55-3:2; 5:15-17; FIG. 2. The flow of fluids through the system can be
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`altered by selectively opening and closing various valves. Produced fluids can
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`either pass through and out the wing branch, “production line 32,” through valves
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`56 and 34, or can instead be directed upwards through the tree cap and choke
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`assembly before returning to “production line 32” by closing “flow loop isolation
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`valve 56,” and opening “production crown valve 22” and “hub isolation valve 54.”
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`See Bednar, 2:66-3:2; 5:15-17; FIG. 2.
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`43. Bednar’s subsea tree has multiple flow paths including a “tree flow
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`passage 18” and a “tree annulus passage 26,” with a branch provided by
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`“production line 32.” Bednar, FIG. 2. As I have said before, a Christmas tree can
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`be called a manifold, and Bednar’s tree is no exception.
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`44.
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` Fluid “flows through tree flow passage 18 and valves 20 and 22 into
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`tree cap 24,” through “choke 38,” and to “production line 32” through “choke
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`return hub connection 50,” “choke return line 52,” and “hub isolation valve 54.”
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`Bednar 4:1-3; Bednar, 4:13-24. In a closed position, “flow loop isolation valve 56”
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`prevents flow directly into “production line 32,” and instead fluid is diverted
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`through “tree cap 24” and “choke 38.” Bednar's system, with respect to the
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`elements of the ’018 Patent’s claim 1, is functionally equivalent to the embodiment
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`described by the ’018 Patent with reference to FIG. 34. The '018 Patent describes
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`that "tree 1116 h