`
`
`Ian Donald, et al.
`In re Patent of:
`8,776,893 Attorney Docket No.: 29188-0025IP1
`U.S. Patent No.:
`July 15, 2014
`
`Issue Date:
`Appl. Serial No.: 13/591,443
`
`Filing Date:
`August 22, 2012
`
`Title:
`APPARATUS AND METHOD FOR PROCESSING
`FLUIDS FROM 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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`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.
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`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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`Page 1 of 28
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`FMC 1003
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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.
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`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.
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`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. 8,776,893 and its accompanying prosecution history (“the
`
`’893 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. No. 2,638,917 (“Clair”, Ex. 1005)
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` WO 00/47864 (“Andersen”, Ex. 1006)
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`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 ’893 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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`’893 Patent.
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`III. Person of Ordinary Skill in the Art
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`12.
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`I am familiar with the content of the ’893 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
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`in the art related to the ’893 Patent at the time of the invention, which for the
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`purposes of this analysis I am treating as 2007 (although in many cases the same
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`analysis would hold true even a year or two or more earlier). I believe that a person
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`having ordinary skill in the art of the ’893 Patent (“POSITA”) would have had a
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`Bachelor of Science Degree in Mechanical Engineering with at least two years of
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`related 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 ’893 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. Christmas trees are used in a subsea environment.
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`14. Subsea Christmas trees having subsea production flowlines were well
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`known and deeply rooted in the oil and gas field by 2007. For example, Kelly and
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`Andersen each discuss subsea Christmas trees with subsea production flowlines.
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`See, e.g., Kelly at 2:16-33, see also “Christmas tree 18” of Figs. 1 and 2; see also
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`Andersen at: 21:16-20, see also “christmas tree 242” of Fig. 24. I have personally
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`had experience with subsea trees and subsea production flowlines dating back into
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`the 1980s. Thus, the person of ordinary skill in the art would readily appreciate that
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`these generic elements, such as trees and flowlines, could be integrated in a subsea
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`installation using routine techniques and associated components. The adaptations
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`necessary to do so were conventional and well within the ordinary skill of the time.
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`VI. A production choke is a processing apparatus.
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`15. A choke is a type of valve that controls fluid flow by constricting a
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`flow area. Kelly’s choke, for example, constricts the flow area between a valve
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`member 80 and a valve seat 78. Kelly at 1:43-54; 2:66-3:9; 3:13-19. Thus, the
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`valve member 80 of the subsea choke assembly 26 is adjustable to control the fluid
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`flow, and therefore the pressure of production fluids. As such, Kelly’s subsea
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`choke assembly 26 is a “processing apparatus,” because it processes fluid by
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`affecting (e.g., reducing) fluid flow and pressure. Indeed, chokes are routinely
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`used to reduce the pressure of the fluids produced from a high pressure wellbore.
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`Thus, a choke can be considered a specific type of processing apparatus – namely,
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`a “pressure regulation apparatus” as referred to in claim 7 and elsewhere in the
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`’893 patent. Clair similarly describes a choke that constricts the flow area between
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`a choke seat 15 and a moving valve 16. Clair at 4:27-59.
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`16.
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`It is also important to appreciate that oil wells or gas wells do not
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`typically produce just oil or gas, but rather produce a multiphase fluid that is some
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`part oil, some part gas and some part other constituents (e.g., water or sand). The
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`pressure drop through a choke flashes the multiphase fluid, changing its ratio of oil
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`and gas, as well as decreasing the temperature of the multiphase fluid. In fact,
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`Clair’s choke is specifically designed to reduce hydrate formation and freezing of
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`the multiphase fluid resulting from the temperature drop. Clair at 1:6-14. Indeed,
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`according to Clair, production fluid that flows through the inner expansion
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`chamber 12 is warmed by production fluid flow through the concentric outer
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`warming chamber 5. Clair at 1:22-31 and 5:15-51. Thus, Clair’s reduction choke
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`provides a processing apparatus operable to regulate the temperature, pressure, and
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`fluid flow parameters of flowing production fluid.
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`17. Freezing, and more acutely, hydrate formation is a formidable
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`problem faced by the designers of subsea well systems, because the downstream
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`choke pressure of subsea wells is higher due to the hydrostatic pressure in the
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`flowline riser and the cooler temperatures at the seabed. Clair’s non-freezing
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`reduction choke is well suited for a subsea environment, as it addresses the
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`freezing and hydrate formation experienced subsea. Thus, one of ordinary skill in
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`the art would readily apply Clair’s non-freezing reduction choke to a subsea tree.
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`VII. Kelly
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`18. Kelly described a “subsea wellhead production apparatus including a
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`retrievable subsea choke.” Kelly at Abstract. The choke is independently landable
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`on, and retrievable from, subsea wellhead equipment (e.g., a subsea Christmas
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`tree) as a pre-packaged assembly (choke assembly 26). Kelly at 1:60-65; see also
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`Fig. 1. To say that something is “landable on” and “retrivable” from a tree
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`indicates that it is configured to be installed and removed from the tree while the
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`tree is installed on the well. Kelly’s apparatus includes a Christmas tree 18
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`connected to the upper end of the well casing 12 that receives production fluid
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`from the well in a production bore (often called a “trunk”). Kelly at 2:16-22. As
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`shown in Figs. 1 and 2 of Kelly, a laterally oriented port of the trunk leads to a sub-
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`assembly of production branch components including a fluid line 20. Kelly at
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`2:22-25. The production branch also includes a production wing valve (not
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`numbered or discussed, but represented schematically in Kelly’s Fig. 1 by
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`concentric circles) located immediately adjacent the lateral port of the tree trunk.
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`The wing valve’s actuator is shown extending towards the bottom of the page in
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`Kelly’s Fig. 2, where the leader for reference number 18 points. These lateral
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`production branch components are directly attached to the tree 18, and form a
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`production fluid flowpath extending from the trunk of the tree 18 to the choke
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`assembly 26. So, considered collectively, these components (i.e., the Christmas
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`tree 18 and the line 20) provide “a subsea tree,” with the branch components
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`providing a “production line” of the subsea tree.
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`19. Another fluid line 24 extends from the collet body 22 to a subsea
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`flowline. Kelly at 2:22-25. Both the line 24 and the subsea flowline to which it
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`extends are downstream fluid conduits that receive fluids produced from the
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`wellbore and processed by the choke assembly 26 mounted to the “subsea tree.”
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`As such, the line 24 and the subsea flowline are each “production flowlines.”
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`Thus, Kelly’s choke assembly 26 is capable of being mounted between an
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`upstream “subsea tree” and a downstream “production flowline.” In fact, this is
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`the exact arrangement shown in Figs. 1 and 2 of Kelly.
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`20. The choke assembly 26 includes a choke body 30, a remotely
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`controlled collet connector 28, and a choke actuator 36.” Kelly at 2:34-37. A
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`collet flange 32 surrounds the lower surface 34 of the choke body 30. The choke
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`body 30 itself includes a valve chamber 76 defining a valve seat 78 for receiving a
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`valve member 80, with the valve member 80 mounted to move towards and away
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`from the valve seat 78 to control the flow of production fluids. Kelly at 2:66 to
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`3:4; see also Fig. 3. The choke assembly 26, which as I noted above is
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`independently landable on, and retrievable from the “subsea tree” as a package,
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`provides a “module.” And the choke body 30, the valve member 80, and other
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`associated components provide a “production choke” included in the pre-packaged
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`module. Notably, while Kelly’s retrievable module includes a production choke
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`including a valve member 80, it does not include a production wing valve. Instead,
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`as I discussed above, Kelly’s wing valve is integrated on the production branch of
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`the Christmas tree 18.
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`21. As I discussed in detail above, the “production choke” functions as
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`“processing apparatus” that processes production fluid by regulating fluid flow rate
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`and pressure. The module and its packaged components (including the
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`components forming the production choke/processing apparatus) are “on the
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`production flowline,” when the choke assembly 26 is landed on the collet body 22.
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`Here, the module’s production choke would be interpreted by one of ordinary skill
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`in the art as being “on the production flowline” from two perspectives – first, the
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`production choke is physically coupled to the production flowlines via the collet
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`body 22, and second, it is placed in the flowpath leading to the production
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`flowlines via the collet body 22. The production choke would also be interpreted
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`by the person of ordinary skill as being “disposed on the subsea tree,” because the
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`choke is physically supported on tree’s lateral branch and receives fluid flow from
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`the tree via the collet body 22.
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`22. As shown in Kelly’s Fig. 3, when the choke assembly 26 is landed on
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`the collet body 22 of the Christmas tree 18, the internal fluid passages 64 and 66 of
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`the collet body 22 are aligned with the internal fluid passages 68 and 70 of the
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`choke body 30. Kelly at 2:58-65. Through this alignment, the choke body 30 is
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`placed in fluid communication with the “production line” (i.e., the fluid line 20 and
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`the collet body 22) via passages 68 and 64, and the “production flowlines” (i.e., the
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`fluid line 24 and the subsea flowline) via passages 70 and 66.
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`23. As I noted above, the collet body 22 is part of a lateral production
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`branch extending from the trunk of the Christmas tree 18. Therefore, when the
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`choke body 30 is aligned with the collet body 22, the sealing means and the sleeve
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`84 are disposed on a lateral branch of the “subsea tree.” Here, these sealing means
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`would be interpreted by one of ordinary skill in the art as being “disposed on the
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`lateral branch” from two perspectives – first, they are physically supported on the
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`branch via the collet body 22, and second, they receive flow from the branch via
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`the collet body 22.
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`24. The choke body 30 includes an inlet 68, passages 94 and 74 leading
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`from the inlet 68 to a valve chamber 76, and an outlet 70 leading from the valve
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`chamber. Kelly at 2:66 to 3:19. When the choke body 30 has been landed on the
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`collet body 22, and the respective fluid passages are aligned (as I discussed above),
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`the inlet 68, passages 94 and 74, valve chamber 76 and outlet 70 form a fluid flow
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`passageway for conveying production fluid from the collet body 22 through the
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`choke body 30. As a practical matter, because the choke assembly 26 is located in
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`Kelly’s apparatus between the “subsea tree” and the “production flowline” (see
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`discussion above and Kelly’s Figs. 1 and 2), there can be no fluid communication
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`between these upstream and downstream components without the choke assembly
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`26 being landed on the collet body 22. Stated simply, when Kelly’s subsea choke
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`assembly 26 is connected on the collet body 22, it completes the fluid path between
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`the tree and the production flowline. Kelly at 2:16-33. Accordingly, the subsea
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`choke assembly 26 provides access to the upstream “subsea tree” (via the collet
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`body 22) by various other downstream “members” of the installation, such as the
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`subsea flowline and any other components connected to the subsea flowline,
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`including the production platform. Kelly at 1:7-10 and 1:20-24.
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`VIII. Kelly and Andersen
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`25. Both Kelly and Andersen described subsea installations featuring
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`retrievable choke components. As previously discussed, Kelly described a subsea
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`wellhead production apparatus including a retrievable subsea choke assembly 26,
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`which is mountable between an upstream subsea tree and a downstream flowline.
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`Kelly’s apparatus further includes a collet body 22 and associated seal assemblies
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`that provide the necessary components for fluidically coupling the choke assembly
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`26 between a “subsea tree” and a “production flowline.” Similar to Kelly,
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`Andersen described a subsea completion apparatus including a wellhead and a flow
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`control package removably located externally of the wellhead. Andersen at 4:6-8
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`and 16:10-17. In my opinion, a person of ordinary skill in the art would
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`immediately recognize that the apparatus described by Andersen is designed to
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`function very similarly to Kelly’s. For example, the flow control package is
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`described by Andersen as comparable component to Kelly’s subsea choke
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`assembly. In fact, Andersen’s flow control package would be considered an
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`upgraded unit, including not only a production choke, but also any other
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`processing equipment needed to control or monitor flowing production fluid.
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`Andersen at 5:29 to 6:9. For example, the flow control package may include “flow
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`meters, detectors, sensors and chemical injection ports.” Andersen at 6:7-9. Like
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`Kelly’s choke assembly 26, Andersen’s flow control package 83 carrying the
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`production choke is structurally integrated into the subsea apparatus between an
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`upstream production line leading from the main bore of the tree and a downstream
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`flowline, such that these upstream and downstream components are only in fluid
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`communication when the module is installed. Further, similar to Kelly’s
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`description of the subsea choke assembly 26, Andersen’s flow control package 83
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`is shown in Fig. 17 as being installed offset from the main bore of the wellhead 10
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`and disposed on a lateral branch. Andersen at 16:16:10.
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`26. Andersen’s flow control package 83 is coupled at one end to the
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`wellhead 10 via a hub connector 84, which is complementary to a corresponding
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`wellhead hub connector 34. Andersen at 16:10-17; see also 10:9-15, 11:20-21, and
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`12:30 to 13:4. The flow control package 83 is coupled at an opposite end to a
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`downstream flowline 178 via a flowline connector 180. Andersen at 16:18-21.
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`Further, while not shown in the illustrative Figure 17, a person of ordinary skill in
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`the art would certainly appreciate that Andersen’s flowline 178 also includes a
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`corresponding hub for coupling with the flowline connector 180 to provide a
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`connection between the flowline 178 and the flow control package 83. Thus,
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`Andersen provides a module including a “production line connector” and
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`“production flowline connector,” along with corresponding “hubs” on the upstream
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`production line a downstream flowline for mating with those connectors.
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`27. One of ordinary skill in the art would have found it obvious, in view
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`of Andersen, to provide a module mountable between an upstream subsea tree and
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`a downstream production flowline with connectors and hubs at opposing sides of
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`the module, in lieu of Kelly’s arrangement with both connectors near the same
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`location at the lower end of the module. For example, the person of ordinary skill
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`would have been motivated to modify Kelly’s choke assembly 26 to include the
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`production line and production flowline connectors on opposing sides of the
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`module, because the modified arrangement provides a predictable improvement to
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`the choke assembly. The skilled person would have recognized that such a
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`modification would have maintained the benefits achieved by Kelly – a pre-
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`packaged module independently landable on, and retrievable from, a subsea tree –
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`and provided the further benefit of increased flexibility, allowing the subsea
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`flowline to be connected and disconnected from the module separately from
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`connecting and disconnecting the module from the tree. Such separate
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`connectablity would facilitate installation of the system by allowing the tree,
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`module and flowline to be installed as smaller, more easily handled, separate
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`pieces. As another example, the ordinarily skilled person would have considered
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`modifying Kelly’s apparatus by simply substituting the entire subsea choke
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`assembly 26 of Kelly with the entire flow control package 83 of Andersen –
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`including, of course, the requisite hubs and connectors. Here, the person of
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`ordinary skill would have been motivated to pursue this substitution in order to
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`obtain the added functionality provided by Andersen’s upgraded flow package 83,
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`which includes further processing apparatuses – e.g., one or more flow monitoring
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`devices that would enable more precise control of the choke because fluid flow and
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`pressure parameters would be known.
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`28. A further modification of Kelly’s choke assembly 26 in view of
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`Andersen that would have been obvious to the person of ordinary skill in the art
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`would be to simply upgrade the choke assembly by incorporating one or more flow
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`measuring devices (e.g., flow meters, detectors, and/or sensors – see Andersen at
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`6:7-9). Historically (and well before 2007), pressure drop across a choke was used
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`to measure the flow rate of production fluid at the discharge end of the choke.
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`Indeed, those of skill in the art would appreciate that it would be very difficult to
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`operate a subsea adjustable choke without flow measuring devices. Thus, the
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`ordinarily skilled person would have plainly foreseen the predictable improvement
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`of Kelly’s choke assembly 26 by incorporating the further measurement
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`functionality of Andersen’s flow control package 83. Indeed, providing the
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`additional flow meters, detectors and sensors described by Anderson, would enable
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`more precise control of Kelly’s production choke, because fluid flow and pressure
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`parameters would be known. Moreover, an ordinarily skilled artisan considering
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`the modification of Kelly in view of Andersen would position the flow
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`measurement devices within the subsea choke assembly in order to facilitate
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`convenient retrieval of these relatively delicate devices for repair or replacement.
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`Indeed, Kelly discussed that subsea choke assembly is installed or retrieved
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`independently of other completion components specifically to facilitate repair or
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`replacement. Kelly 1:6-34. As such, the person of ordinary skill would likewise
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`position one or more flow-monitoring devices directly on the subsea choke
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`assembly described by Kelly, so that the device can be conveniently installed and
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`retrieved as a comprehensive and self-contained modular package.
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`IX. Clair
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`29. Clair described a non-freezing reduction choke for use in oil and gas
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`well systems. Clair at 1:1-5. As shown in Figures 2 and 6 of Clair, the non-
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`freezing reduction choke (which provides a “processing apparatus,” as I discussed
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`above) can be applied to a Christmas tree 31 of an oil or gas well as a pre-packaged
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`“module” Kelly at 23-31 and Clair 5:52-56. As shown in Fig. 6, the tree 31
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`includes a production bore (or “trunk”) and a wing branch including a production
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`wing valve extending laterally from the trunk (similar to Kelly’s tree 18). The
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`production wing valve is shown in Clair’s Figure 6 as a circular structure located
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`on the branch (and therefore, not on the reduction choke/module) immediately
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`adjacent a lateral port of the trunk. The wing branch receives production fluid
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`from the trunk, and therefore provides a “production line.” In this arrangement,
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`the reduction choke receives fluid from the production line of the tree 31 and
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`discharges the fluid through a discharge pipe 14. Clair at 5:9-15. In my opinion,
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`the Christmas tree 31 corresponds to a “subsea tree” and the discharge pipe 14
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`corresponds to a “subsea production flowline.” As I discussed above, subsea trees
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`having subsea production flowlines were well known and deeply rooted in the oil
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`and gas field by 2007. So, even though Clair is silent as to whether the Christmas
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`tree 31 and discharge pipe 14 are deployed in a “subsea” environment or on land,
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`the person of ordinary skill in the art would have found it obvious to implement
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`Clair’s non-freezing reduction choke in a subsea installation including a subsea
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`tree and a subsea flowline/discharge pipe. Moreover, as Clair’s non-freezing
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`reduction choke addresses hydrate formation in the production fluids (freezing),
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`problems often encountered when producing from subsea wells, the person of
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`ordinary skill in the art would have particularly sought to implement Clair’s non-
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`freezing reduction choke on a subsea tree with a subsea production flowline.
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`
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`30. Clair’s modular reduction choke includes an inlet connection 4
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`coupled to the laterally extending production line of the tree 31. Clair at 4:5-8 and
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`5:53-56. Therefore, the inlet connection 4 provides a “production line connector”
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`that is disposed on a lateral branch of the tree. The reduction choke further
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`includes a header 7 coupled to the discharge pipe 14 (i.e., the “production
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`flowline”). Clair at 4:5-8 and 5:53-56. Therefore, the header 7 provides a
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`“production flowline connector.” Similar to the discussion above regarding Kelly,
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`Clair’s inlet connection 4 (i.e., the “production line connector”) would be
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`interpreted by one or ordinary skill in the art as being “disposed on the lateral
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`branch,” because it is physically coupled to the branch and also receives fluid flow
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`from the branch. Clair’s Figure 7 illustrates complementary hub structures that
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`mate with the inlet connection 4 and header 7 to provide respective couplings for
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`conveying fluid from the subsea tree to the reduction choke, and from the
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`reduction choke to the production flowline.
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`31. As previously discussed, Clair’s apparatus includes a non-freezing
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`reduction choke coupled between a subsea tree 31 and a discharge pipe 14
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`providing a downstream flowline extending from the tree. Similar to Kelly’s
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`choke assembly 26, one of ordinary skill in the art would interpret the reduction
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`choke as being “on the production flowline,” because it is physically coupled to the
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`discharge pipe 7 and placed in a flowpath leading to the production flowpath (as
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`discussed below). The reduction choke would also be interpreted by the ordinarily
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`skilled person as being “disposed on the subsea tree,” because the choke is
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`physically coupled to the tree’s lateral branch and receives fluid flow from the tree
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`via the inlet connection 4.
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`32. Figure 7 of Clair depicts a serious of arrows illustrating the fluid
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`flowpath through the choke. As shown, Clair’s reduction choke receives
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`production fluid from the tree at the inlet connection 4 of the cylindrical warming
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`chamber 5. Clair at 4:74 to 5:15. The production fluid is then directed in a spiral
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`path around the tubular expansion chamber 12 by the spiral baffle 11 and received
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`by the turn tube 10. Clair at 4:74 to 5:15. The turn tube 10 conveys the fluid into
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`the choke cylinder 8 where it is introduced to the choke valve 16. Clair at 4:74 to
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`5:15. After passing through the choke valve 16, the fluid is directed to the
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`discharge pipe 14 via the expansion chamber 12. Clair at 4:74 to 5:15. Again,
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`similar to Kelly’s choke assembly 26, Clair’s reduction choke is structurally
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`integrated into the apparatus between an upstream production line leading from the
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`main bore of the tree and a downstream flowline, meaning that the fluid flow
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`passageway through the reduction choke provides the only fluid communication
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`between the tree 31 and the discharge pipe 14, and fluid communication is only
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`possible when the reduction choke is installed. Further, because the reduction
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`choke completes the fluid path between the upstream tree and the downstream
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`flowline, it provides access to the tree by various other downstream “members” of
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`the installation (e.g., the flowline itself and other downstream structures).
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`X. Clair and Andersen
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`33. Both Kelly and Andersen described completion apparatuses featuring
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`modular choke components that are offset from the production bore of the tree. As
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`previously discussed, the apparatus described by Clair includes a non-freezing
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`reduction choke coupled between a tree 31 and a discharge pipe 14. Similar to
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`Clair, Andersen described a completion apparatus featuring a flow control package
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`located between a wellhead and a flowline. Andersen at 4:6-8 and 16:10-17.
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`34. Andersen further described a manifold 162 downstream of a flow
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`control package 82 that has access to a wellhead 10 via a jumper 166 connecting
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`the manifold 162 to the flow control package 82. Andersen at 16:1-8; see also Fig.
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`16. This downstream manifold 162 is “member” of the completion apparatus that
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`is separate and distinct from the “module” (i.e., the flow control package 82), yet
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`has access to the wellhead 10 through a physical connection with the module.
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`Indeed, such multi-module configurations were commonly used in subsea wellhead
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`installations prior to 2006, and it would have been obvious to provide a second
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`module (e.g., a manifold downstream of Clair’s reduction choke in view of the
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`disclosure of Andersen. In my opinion, the person of ordinary skill in the art
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`would have plainly recognized that modifying Clair’s apparatus to include the
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`manifold 162 and the jumper 166 as taught by Andersen is merely a combination
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`of well-known subsea installation components that perform the same function in
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`combination as they did separately. Indeed, the ordinarily skilled person would
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`have appreciated that this routine combination of conventional components would
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`be an obvious way to improve the performance of the apparatus described by Clair,
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`because it permits production fluid from multiple wells in a field to be gathered at
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`a common manifold hub after local fluid processing at has been completed at the
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`individual wells. Accordingly, Andersen notes that one favored solution is where
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`several single wells are drilled and completed with respective flowlines extending
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`to a centrally located manifold unit placed on the seabed. Andersen at 2:11-19.
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`35. Similar to Kelly’s choke assembly 26, a further modification of
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`Clair’s reduction choke in view of Andersen that would have been obvious to the
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`person of ordina