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You are here: BAILII >> Databases >> England and Wales High Court (Patents Court) Decisions >> Compactgtl Plc v Oxford Catalysts Group Plc & Ors [2013] EWHC 3935 (Pat) (22 November 2013) URL: http://www.bailii.org/ew/cases/EWHC/Patents/2013/3935.html Cite as: [2013] EWHC 3935 (Pat) |
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HC 13 B 01040 |
CHANCERY DIVISION
PATENTS COURT
The Rolls Building 7 Rolls Buildings Fetter Lane London EC4A 1NL |
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B e f o r e :
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COMPACTGTL PLC |
Claimant |
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- and - |
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(1) OXFORD CATALYSTS GROUP PLC (2) VELOCYS INC (3) BATTELLE MEMORIAL INSTITUTE |
Defendants |
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And Between: |
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VELOCYS INC |
Claimant |
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- and - |
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(1) COMPACTGTL PLC (2) BATTELLE MEMORIAL INSTITUTE |
Defendants |
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1st Floor, Quality House, 6-9 Quality Court, Chancery Lane, London WC2A 1HP.
Telephone No: 020 7067 2900. Fax No: 020 7831 6864
e-mail: [email protected])
MR. IAIN PURVIS QC and MR. HENRY WARD (instructed by Bird and Bird LLP) appeared the Defendants.
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Crown Copyright ©
MR. JUSTICE BIRSS :
"A method of Fischer-Tropsch reaction, comprising the steps of:
"(a) providing a catalyst structure having a first porous structure with a first pore surface area and a first pore size of at least 0.1 µm;
"a porous interfacial layer with a second pore surface area and a second pore size less than said first pore size, said porous interfacial layer disposed upon said pore surface area; and
"a Fischer-Tropsch catalyst selected from the group consisting of cobalt, ruthenium, iron, nickel, rhenium, osmium and combinations thereof placed upon said second pore surface area; and
"(b) passing a feed stream having a mixture of hydrogen gas with carbon monoxide gas through said catalyst structure and heating said catalyst structure to at least 200° C at an operating pressure, said feed stream having a residence time within said catalyst structure less than 5 seconds, thereby obtaining a product stream of at least 25% conversion of carbon monoxide, and at most 25% selectivity toward methane."
"A catalyst structure for Fischer-Tropsch synthesis, comprising:
"said catalyst structure comprising a first porous structure with a first pore surface area and a first pore surface area and a first pore size of at least 0.1 µm;
"a buffer layer disposed on said porous structure;
"a porous interfacial layer with a second pore surface area and a second pore size less than said first pore size, said porous interfacial layer disposed upon said buffer layer;
"a Fischer-Tropsch catalyst selected from the group consisting of cobalt, ruthenium, iron, rhenium, nickel, osmium and combinations thereof placed upon said second pore surface area."
For the 508 Patent:
"Of paragraph 1 and paragraphs 3.1 and 3.2 of the Particulars of Infringement:
"3. Please identify the processes relied on as being claimed in at least claims 1, 2, 4 and 6 of the 508 Patent. In particular please identify:
"(a) the 'catalyst structure' which it is alleged is used in the alleged infringing processes;
"(b) the 'first porus structure' which it is alleged the catalyst structure comprises;
"(c) the 'pores' which are alleged to exist in the said first porus structure;
"(d) the 'porus interfacial layer' which it is alleged is disposed on the 'first pore surface area';
"(e) the 'pores' which are alleged to exist in the said porous interfacial layer;
"(f) the Fischer-Tropsch catalyst which it is alleged is placed upon the 'second pore surface area';
"(g) the basis for asserting that the process conditions relied upon fall within the claims alleged to be infringed including the required degree of conversion of carbon monoxide and selectivity towards methane."
For the 509 patent:
"5. Please identify the products relied on as being claimed in at least claims 1-4, 6, 7 and 15 of the 509 Patent. In particular please identify:
"(a) the 'catalyst structure' which it is alleged has been imported, used and kept in the United Kingdom;
"(b) the 'first porous structure' which it is alleged the catalyst comprises;
"(c) the 'pores' which are alleged to exist in the said first porous structure;
"(d) the 'buffer layer' which it is alleged is disposed on the said porous structure;
"(e) the 'porous interfacial layer' which it is alleged is disposed upon the said buffer layer;
"(f) the 'pores' which it is alleged exist in the said porous interfacial layer;
"(g) the Fisher-Tropsch catalyst which it is alleged is placed upon the said 'second pore surface area';
"(h) the basis for asserting that the alleged infringing catalyst structure has a porous structure with a geometry claimed in claim 2;
"(i) the basis for asserting that the process conditions relied upon fall within the claims alleged to be infringed including the required degree of conversion of carbon monoxide and selectivity towards methane."
"Velocys shall, by 22 July 2013, provide full particulars in response to each and every one of the requests for clarification and/or additional information made in CGTL's Request For Further Information as served on 18 April 2013."
"The above plant structure is such as to fall within the claims of the patent identified in the request above. The various elements of CompactGTL's plant sufficient to enable CompactGTL to identify the issues in dispute are set out above. It is neither necessary nor appropriate to argue issues of construction (such as whether holes in the catalyst structure which allow the feed gas to flow through the reactor formed by the corrugations in the structure constitute pores within the meaning of the claim) at this stage in the proceedings."
"So far as Velocys is aware CompactGTL has not made public any details of its process conditions in the FT reaction. However it infers from patent information that has been made available in relation to both the SMR and FT reactors as well as other publicly available information that the process conditions of the FT reactor described above would be such as to fall within the scope of the claims. By way merely of example, the SMR reactor process described in Accentus WO03048035A1 (and the reactor described therein is consistent with that described in the CompactGTL material outlined above) specifies a residence time of less than 0.5secs and preferably 20-100 msec, showing that reactors on this construction are capable of such reduced contact times, and that the system comprising both the SMR and FT reactors is operated with a high feed gas throughput and correspondingly low residence time."
"Velocys do set out a summary of its case on infringement by providing a breakdown of the integers of the relevant claims of European patents EP(UK) 1 206 508 and EP(UK) 1 206 509 (the patents) in issue relative to the alleged infringement,"
"It is not in dispute that the accused CGTL process performs a Fischer-Tropsch reaction. Further, heating a Fischer-Tropsch catalyst structure to at least 200 degrees C and obtaining a product stream of at least 25% conversion of carbon monoxide, and at most 25% selectivity toward methane, is, I am informed by CGTL, standard practice, and it is not in dispute that the CGTL Process operates under these conditions. However, the CGTL Process is not within the claimed residence time of less than 5 seconds. It is CGTL's case, therefore, that the CGTL Process clearly does not fall within claim 9 of the 509 patent."