IPR2015-00170, -00171, -00173
`
`DAICEL CORPORATION
`Petitioner
`v.
`CELANESE INTERNATIONAL CORP.
`Patent Owner
`
`Patent No. 8,076,507
`
`Petitioner’s Demonstrative Exhibit
`
`000001
`
`IPR2015-00171
`DAICEL v. CELANESE
`Exhibit 1074
`
`

`
`Grounds Instituted for Trial
`
`Reference
`
`Singh (Ex. 1011)
`‘095 Patent (Ex. 1010)
`Akinori (Ex. 1012)
`
`Reference
`
`IPR2015-00170
`Basis
`Challenged Claims
`
`§103(a)
`
`1-4, 6-11, and 13
`
`IPR2015-00171
`Basis
`Challenged Claims
`
`‘095 Patent (Ex. 1010)
`
`§102(b)
`
`42-44, 47-51, 53, 55, and 56
`
`‘095 Patent (Ex. 1010)
`JP ‘712 (Ex. 1020)
`
`§103(a)
`
`57
`
`Reference
`
`IPR2015-00173
`Basis
`Challenged Claims
`
`‘095 Patent (Ex. 1010)
`
`§102(b)
`
`58-60, 67, 69, 71, and 72
`
`‘095 Patent (Ex. 1010)
`JP ‘712 (Ex. 1020)
`
`§103(a)
`
`73
`
`000002
`
`

`
`‘507 Patent
`
`‘507 Patent
`
`(L2: United States Patent
`5C31£&S IEI 2'.
`
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`
`000003
`
`

`
`‘507 Patent, Figure 2
`
`Liquid-liquid
`Separator
`
`Light-ends
`(Splitter)
`Column
`
`Distillation
`Columns
`
`Liquid-liquid
`Extraction
`
`000004
`
`

`
`‘507 Patent, Figure 1
`
`000005
`
`

`
`‘507 Patent, Claim 1
`
`000006
`
`

`
`‘507 Patent, Claims 42, 47
`
`000007
`
`

`
`‘095 Patent Example – Flow Diagram
`
`“SECOND OVERHEAD”
`
`“FIRST OVERHEAD”
`
`LIQUID
`SEPARATOR
`
`000008
`
`

`
`Akinori (Translation) – Ex. 1013
`
`Main Carbonylation Reaction:
`
`Reactor conditions:
`Temp: 180° - 220° С
`Pressure: 15-40 atm
`Solvent: acetic acid
`
`000009
`
`

`
`Akinori (Translation) – Ex. 1013
`
`Equilibrium Side Reactions:
`
`000010
`
`

`
`Roth– Ex. 1061
`
`Authors (Roth, Paulik, etc.)
`are the “founders” of the
`Monsanto process, and
`“who you go to when you
`have questions about
`acetic acid.”
`
`Porcelli Depo. at 437:18-
`438:3 (Ex. 1065)
`
`000011
`
`

`
`Eby & Singleton– Ex. 1066
`
`“Under reaction conditions all components of Eqs. (1)-(5)
`are present in equilibrium concentrations. At normal
`reaction temperatures (> 150°C) these equilibria are
`established instantaneously….
`
`Dimethyl ether is normally present in the catalyst solution
`….”
`
`Eby at 8 (Ex. 1066)
`
`000012
`
`

`
`Torrence – Ex. 2032
`
`Torrence — Ex. 2032
`
`411
`
`mu
`
`12:1
`
`140
`
`150
`
`130 t[n'Lin]
`
`000013
`
`ED E
`
`.
`U
`
`

`
`‘095 Patent Example – Flow Diagram
`
`“SECOND OVERHEAD”
`
`“FIRST OVERHEAD”
`
`LIQUID
`SEPARATOR
`
`000014
`
`

`
`Torrence – Ex. 2032
`
`Torrence — Ex. 2032
`
`cf [CH3OH]
`d t
`
`= l: [HI1] [C-Hgl]
`
`IDDIDE CYCLE
`
`["”{°°:"""”_ warren ans SHIFT
`cg :\\\
`CYCLE
`
`[Hh[C D]gl3H]"
`
`‘N
`HI
`[FIl'I(CC|']-gIg_I'
`J -
`
`METHANOL
`°‘"‘;‘?,'.§”[';‘;“°”
`
`I-
`
`:0 ;mo-
`|‘
`
`H!
`X X
`HUM:
`
`tHh{coJ=Iz{L:1='
`
`’)kFIh(CO]I3
`
`[C H3-FIh[GO}gI3]’
`
`000015
`
`

`
`Fogler – Ex. 1063
`
`Fogler — Ex. 1063
`
`Channeling
`
`fl_
`
`—\j
`
`,:''r”
`
`Lung tail
`dead zcrne
`
`Dead lanes
`
`{E}
`
`000016
`
`

`
`Smith & Van Ness – Ex. 1067
`
`000017
`
`

`
`Rönnback – Ex. 1058
`
`“Since the fit of the model with the concentration-
`based description is very good, it appears that the
`use of activity coefficients for this
`[methanol/acetic acid/methyl acetate/water
`system] reaction is unnecessary.”
`
`Ex. 1058 at 11.
`(See also Jones Rep. Decl. ¶89 (Ex. 1060)).
`
`000018
`
`

`
`‘507 Patent, Claim 58
`
`000019
`
`

`
`‘507 Patent, Claims 3 & 4
`
`000020