throbber
Page 1 of 16
`
`Samsung Exhibit 1017
`Samsung Electronics Co., Ltd. v. Daniel L. Flamm
`
`

`
`5,883,778
`Page 2
`
`
`
`
`US, PATENT DOCUMENTS
`
`
`
`
`‘
`1/1993 1“1“g119S~
`5.-181559
`
`
`
`4/1993 Ha111bu1'ge11 et al.
`5,203,401
`
`
`
`5/1993 Barnes eta1..
`5,207,437
`
`
`
`
`
`7/1993 Van de V611 et al.
`5,230 741
`
`
`
`
`'
`’
`
`
`
`
`5,252,132 10/1993 Oda etal..
`
`
`
`5,252,850 10,1995 schempp.
`10/1993 Nozawa et al.
`5,255,153
`
`
`
`
`.
`5,270,266
`12/1993 Hiram) el al.
`
`
`
`
`5,275,683
`1/1994 Ammi et al. N
`
`
`
`
`5,280,156
`1/1994 Niori ct a1.
`
`
`
`
`5,287,914
`2/1994 I-Iughes ,
`
`
`
`4/1994 Ivlaeda et al.
`5,302,209
`.
`
`
`
`
`5,303,938
`4/1994 Ivliller et al.
`.
`
`
`
`
`5/1994 Fschbach .
`5,312,509
`
`
`
`
`.
`
`
`
`,
`
`
`
`
`
`
`
`....................... .. 361/234
`
`
`
`
`156/345
`219/385
`
`
`
`
`
`
`
`
`
`
`
`
`
`361/234
`165/80.2
`279/128
`
`
`
`
`
`
`
`
`
`5,315,473
`5/1994 Collins et al.
`
`
`
`5,345,999
`9/1994 Hosokawa
`
`
`
`5350 479
`9/1994 Collins et a1.
`
`
`
`
`595569476
`10,1994 Foster et al
`
`
`
`
`_
`’
`’
`"
`’
`.
`322392;; 1/:1::::::::::::;:;1 777777777777777777777~ 133::
`
`
`
`
`
`
`'
`_’
`’
`'
`,
`'
`_ l
`
`
`
`
`
`
`6/1995 T0m1ta et al.
`..
`5,423,936
`156/345
`
`
`
`
`
`
`_
`55
`,
`5
`h
`,
`
`
`
`
`
`8
`s erman
`.361,234
`5,426,
`6,199
`3/1995 14911919 9191-
`3»445»709
`159/345
`
`
`
`
`
`9/1995 Barnes et 8.1.
`3,452,510
`29/825
`
`
`
`
`
`7/1996 Nozawa 01 6.1.
`5,539,179
`219/121.43
`
`
`
`
`.-
`7/1996 Collins et a1-
`361/234
`5,539,609
`
`
`
`
`
`
`8/1996 Kawakami et al.
`5,542,559
`216/67
`
`
`
`
`
`
`6/1997 Sherstinsky el al.
`. 361/234
`5,634,266
`
`
`
`
`
`
`........ ..
`8/1997 Burkhart et £11.
`5,656,093
`279/128
`
`
`
`
`
`
`
`9/1997 Sherstinsky et a1.
`................... 361/234
`5,671,117
`
`
`
`
`
`
`
`Page 2 of 16
`
`

`
`U.S. Patent
`
`Mar. 16, 1999
`
`Sheet 1 of 6
`
` %933%H.3
`
`i\\.i
`
`S».8S~uU_:&§&.m_
`
`Ebu
`
`%_.3__E:
`§o.uSM..
`
`umufisEm
`
`858%
`
`Page 3 of 16
`
`

`
`U.S. Patent
`
`Mar. 16, 1999
`
`Sheet 2 of 6
`
`5,883,778
`
`83$8?
`
`.§&§K
`
`
`
`KS88838.RE
`
`$523Em
`
`Sham.
`
`“$88;38
`
`8.5%.
`
`§.n§&.m
`
`§.§m5
`
`‘HE
`
`§>‘..~.._LI‘h‘..~.._IuI‘~§
`
`sflPflllrfl.WI!
`I.IIII.I.IIIIul-I.we
`
`Page 4 of 16
`
`

`
`U.S. Patent
`
`Mar. 16, 1999
`
`Sheet 3 of 6
`
`5,883,778
`
`7 if '
`
`W
`
`.
`
`Page 5 of 16
`
`

`
`
`U.S. Patent
`
`
`
`
`
`
`Mar. 16, 1999
`
`
`Sheet 4 of 6
`
`5,883,778
`
`
`
`150
`
`
`
`
`
`
`
`
`40
`
`
`
`128811 35
`
`
`
`
`
`
`.
`110
`‘*
`
`
`
`
`
`LIIIIJTIIIIIIZ
`
`
`
`
`
`
`Page 6 of 16
`
`

`
`
`U.S. Patent
`
`
`
`
`
`
`Mar. 16, 1999
`
`
`Sheet 5 of 6
`
`
`
`5,883,778
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`\\\‘ mg‘!
`
`
`
`AL’-35;‘-'1
`
`
`
`
`
`
`
`
`
`
`
`Page 7 of 16
`
`

`
`
`U.S. Patent
`
`
`
`r..aM
`99916:1
`
`
`
`
`
`Sheet 6 of 6
`
`
`
`
`
`Page 8 of 16
`
`

`
`5,883,778
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`1
`
`ELECTROSTATIC CHUCK WITH FLUID
`
`
`
`FLOW REGULATOR
`
`CROSS-RJ:'FERl:'N CE
`
`
`
`This application is a continuation—in—part of U.S. patent
`
`
`
`
`
`
`application Ser. No. 08/203,111, entitled “Electrostatic
`
`
`
`
`
`
`Chuck,” filed on Feb. 28, 1994 now abandoned; and is
`
`
`
`
`
`
`
`
`
`related to U.S. Pat. No. 5,634,266, patent application Ser.
`
`
`
`
`
`
`
`
`
`No. 08/449,135, filed on May 24, 1995, both of which are
`
`
`
`
`
`
`
`
`incorporated herein by reference.
`
`
`
`BACKGROUND
`
`
`The present invention is directed to an electrostatic chuck
`
`
`
`
`
`
`for holding, and maintaining substantially uniform ten1pera-
`
`
`
`
`
`
`
`tures across a substrate during processing of the substrate,
`
`
`
`
`
`
`
`and for increasing the life of the chuck in erosive process
`
`
`
`
`
`
`
`
`
`
`environments.
`
`In semiconductor fabrication processes, electrostatic
`
`
`
`
`
`chucks are used to hold substrates for processing of the
`
`
`
`
`
`
`
`
`
`substrate. Electrostatic chucks are particularly useful
`in
`
`
`
`
`
`
`
`vacuum processing environments where there is insuflicient
`
`
`
`
`
`
`differential pressure to hold the substrate using a vacuum
`
`
`
`
`
`
`
`chuck. A typical electrostatic chuck comprises an electro-
`
`
`
`
`
`
`static member supported by a support adapted to be secured
`
`
`
`
`
`
`in a process chamber. The electrostatic member comprises
`
`
`
`
`
`
`
`an electrically insulated electrode. An electrical connector
`
`
`
`
`
`
`
`electrically connects the electrode to a voltage supply source
`
`
`
`
`
`
`
`in the process chamber. When the electrode is electrically
`
`
`
`
`
`
`
`biased with respect
`to the substrate held on the chuck,
`
`
`
`
`
`
`
`
`
`
`opposing electrostatic charge accumulates in the electrode
`
`
`
`
`
`
`and substrate, resulting in attractive electrostatic forces that
`
`
`
`
`
`
`
`hold the substrate to the chuck. Electrostatic chucks are
`
`
`
`
`
`
`
`
`
`generally described in, for example U.S. patent application
`
`
`
`
`
`
`
`
`Ser. Nos. 08/278,787 by Cameron, et al.; 08/276,735 by
`
`
`
`
`
`
`
`
`Shamouilian, et al.; and 08/189,562, by Shamouilian, et
`
`
`
`
`
`
`al.—all of which are incorporated herein by reference.
`
`
`
`
`
`
`Conventional electrostatic chucks can also have tempera-
`
`
`
`
`
`
`
`ture controlling systems to regulate the temperatures across
`
`
`
`
`
`
`
`the substrate held on the chuck. However, conventional
`
`
`
`
`
`
`
`
`temperature controlling systems often do not maintain uni-
`
`
`
`
`
`
`
`form temperatures across the substrate, particularly at the
`
`
`
`
`
`
`
`perimeter or edge of the substrate. Excessively high tem-
`
`
`
`
`
`
`
`peratures at portions of the substrate can damage the inte-
`
`
`
`
`
`
`
`
`grated circuit chips formed on the substrate, and low tem-
`
`
`
`
`
`
`
`
`
`peratures can result
`in non—uniform processing of the
`
`
`
`
`
`
`
`
`substrate.
`
`A typical conventional
`temperature controlling system
`
`
`
`
`
`
`functions by introducing a heat
`transfer fluid, such as
`
`
`
`
`
`
`
`
`helium, below the substrate via a single central aperture in _
`
`
`
`
`
`
`
`
`the chuck. The single central aperture is often used to supply
`
`
`
`
`
`
`
`
`
`helium to recessed cavities below the substrate, such as an
`
`
`
`
`
`
`
`
`open trough or pattern of interconnected grooves, to distrib-
`
`
`
`
`
`
`ute helium below the substrate. The trough or patterned
`
`
`
`
`
`
`
`
`
`grooves often stop short of the perimeter of the chuck
`
`
`
`
`
`
`
`
`
`
`forming a relatively large edge gap between the trough
`
`
`
`
`
`
`
`
`edges, or groove tips, and the perimeter of the substrate held
`
`
`
`
`
`
`
`
`
`on the electrostatic member, the gap often exceeding 10 to
`
`
`
`
`
`
`
`
`20 mm. The large edge gap is provided to allow the
`
`
`
`
`
`
`
`
`
`
`overlying perimeter of the substrate to cover and seal the
`
`
`
`
`
`
`
`
`
`trough or grooves so that the heat transfer fluid does not leak
`
`
`
`
`
`
`
`
`
`
`out into the process environment. However, because no heat
`
`
`
`
`
`
`
`
`transfer fluid is held below the perimeter of the substrate
`
`
`
`
`
`
`
`
`
`overlying the edge gap, the temperature of the substrate
`
`
`
`
`
`
`
`
`
`perimeter is controlled less effectively compared to central
`
`
`
`
`
`
`portions of the substrate, resulting in non—uniform tempera-
`
`
`
`
`
`
`tures across the substrate.
`
`
`
`
`
`,
`
`2
`
`Conversely, extending the edges of the trough or tips of
`
`
`
`
`
`
`
`
`the grooves all the way to the perimeter of the chuck causes
`
`
`
`
`
`
`
`
`
`other problems. The small gap between the trough edges, or
`
`
`
`
`
`
`
`
`
`groove tips, and the overlying substrate perimeter, can result
`
`
`
`
`
`
`
`
`
`in excessive leakage of helium at portions of the trough
`
`
`
`
`
`
`
`
`
`edges or groove tips. The accompanying reduction in tem-
`
`
`
`
`
`
`
`perature control of the overlying portions of the substrate
`
`
`
`
`
`
`
`
`
`perimeter, causes the substrate to exhibit hot or cold spots,
`
`
`
`
`
`
`
`
`and results in reduced yields of integrated circuits formed on
`
`
`
`
`
`
`
`the substrate.
`
`
`Another limitation of conventional chucks results from
`
`
`
`
`
`
`
`the structure of the electrostatic member 10 of the chuck 11,
`
`
`
`
`
`
`
`which typically comprises a copper electrode layer 12
`
`
`
`
`
`
`
`sandwiched between two polymer insulator layers 13a, 13b
`
`
`
`
`
`
`
`
`as shown in FIG. 1. The polymer layers 1311, 13b overlap
`
`
`
`
`
`
`
`
`
`beyond the edge of the copper electrode 12 at an outer
`
`
`
`
`
`
`
`
`
`
`periphery 14 of the electrostatic member to electrically
`
`
`
`
`
`
`
`insulate and seal the electrode 12. Typically, the overlapping
`
`
`
`
`
`
`
`
`
`portions of the polymer layers form a lower annular step 15
`
`
`
`
`
`
`
`
`of approximately 0.5 to 2 mm, and more typically 1.25 to
`
`
`
`
`
`
`
`
`1.50 mm width around the circumference of the raised
`
`
`
`
`
`
`
`
`
`electrode 12. The annular step 15 has several detrimental
`
`
`
`
`
`
`
`
`
`effects on the electrostatic chuck 11. First, because of the
`
`
`
`
`
`
`
`
`
`annular step 15, only a small portion of the outer periphery
`
`
`
`
`
`
`
`
`
`14 of the electrostatic member 10 contacts the perimeter 16
`
`
`
`
`
`
`
`of the substrate 17 beyond the circumference of the elec-
`
`
`
`
`
`
`
`
`
`
`trode 12. As a result, there is an increased probability of
`
`
`
`
`
`
`
`
`
`helium leakage from groove tips 18 near the outer periphery
`
`
`
`
`
`
`
`
`
`14 contributing to excessive overheating of the substrate 17.
`
`
`
`
`
`
`
`A second effect is that the relatively small width of polymer
`
`
`
`
`
`
`
`
`
`insulator 10 separating the circumference of the electrode 12
`
`
`
`
`
`
`from the process environment can cause a higher failure rate
`
`
`
`
`
`
`
`
`of the chuck 11, because the small insulator portion 19 can
`
`
`
`
`
`
`
`
`
`
`be rapidly eroded by the erosive process environment,
`
`
`
`
`
`
`
`
`exposing the electrode 12 and causing short—circuiting of the
`
`
`
`
`
`
`
`chuck 11. Erosion of insulator portion 19 is particularly
`
`
`
`
`
`
`
`
`rapid in oxygen or halogen containing gases and plasmas,
`
`
`
`
`
`
`
`which are used for a variety of tasks, such as for example,
`
`
`
`
`
`
`
`
`
`etching of substrates and cleaning of process chambers.
`
`
`
`
`
`
`
`
`Failure of the chuck during processing of the substrate can
`
`
`
`
`
`
`
`
`
`damage the substrate, and necessitates frequent replacement
`
`
`
`
`
`
`of short-circuited chucks.
`
`
`
`Thus, it is desirable to have an electrostatic chuck having
`
`
`
`
`
`
`a temperature controlling system that allows maintaining
`
`
`
`
`
`
`substantially uniform temperatures across the substrate, and
`
`
`
`
`
`
`in particular the perimeter of the substrate, to provide higher
`
`
`
`
`
`
`
`integrated circuit chip yields from the substrate. It is also
`
`
`
`
`
`
`
`
`desirable to have an electrostatic chuck which demonstrates
`
`
`
`
`
`improved erosion resistance, and reduced failure rates, in
`
`
`
`
`
`
`
`erosive process environments.
`
`
`
`SUMMARY
`
`
`
`
`
`
`
`
`
`
`invention provides an electrostatic chuck
`The present
`
`
`
`
`
`
`
`capable of maintaining substantially uniform temperatures
`
`
`
`
`
`
`across a substrate and having improved erosion resistant in
`
`
`
`
`
`
`
`an erosive process environment. One version of the electro-
`
`
`
`
`
`
`
`
`static chuck comprises an electrostatic member that includes
`
`
`
`
`
`
`
`(i) an insulator covering an electrode, (ii) a substantially
`
`
`
`
`
`
`
`
`planar and conformal contact surface capable of conforming
`
`
`
`
`
`
`
`to the substrate, and (iii) conduits terminating at the contact
`
`
`
`
`
`
`
`
`
`surface for providing heat
`transfer fluid to the contact
`
`
`
`
`
`
`
`
`surface. Application of a voltage to the electrode of the
`
`
`
`
`
`
`
`
`
`electrostatic member electrostatically holds the substrate on
`
`
`
`
`
`
`the conformal contact surface to define an outer periphery
`
`
`
`
`
`
`
`having (1) leaking portions where heat transfer fluid leaks
`
`
`
`
`
`
`
`
`
`out, and (2) sealed portions where heat transfer fluid sub-
`
`
`
`
`
`
`
`
`
`
`stantially does not leak out. A fluid flow regulator is pro-
`
`
`
`
`
`
`
`
`
`Page 9 of 16
`
`

`
`5,883,778
`
`
`
`3
`
`vided for flowing heat transfer fluid at different flow rates
`
`
`
`
`
`
`
`
`
`through the conduits in the electrostatic member to provide
`
`
`
`
`
`
`
`(i) first flow rates of heat transfer fluid through the conduits
`
`
`
`
`
`
`
`
`
`
`adjacent to the sealed portions of the outer periphery of the
`
`
`
`
`
`
`
`
`electrostatic member, and (ii) second flow rates of heat
`
`
`
`
`
`
`
`
`
`transfer fluid through the conduits adjacent to the leaking
`
`
`
`
`
`
`
`
`portions, the second flow rates being higher than the first
`
`
`
`
`
`
`
`
`
`
`flow rates, to maintain substantially uniform temperatures
`
`
`
`
`
`
`
`across the substrate held on the chuck.
`
`
`
`
`
`
`Preferably, the fluid flow regulator includes a heat transfer
`
`
`
`
`
`
`
`
`fluid reservoir having at least one of the following charac-
`
`
`
`
`
`
`
`
`teristics
`the reservoir is positioned proximate to the
`
`
`
`
`
`
`
`electrostatic member, (ii) the reservoir extends across all the
`
`
`
`
`
`
`
`
`
`conduits, and (iii) the reservoir is sized and configured to
`
`
`
`
`
`
`
`
`hold a suflicient volume of heat transfer fluid at a sufliciently
`
`
`
`
`
`
`
`elevated pressure relative to the pressure in the process
`
`
`
`
`
`
`
`
`
`chamber,
`to provide the second higher flow rates of heat
`
`
`
`
`
`
`
`
`
`transfer fluid to the conduits adjacent to the leaking portions
`
`
`
`
`
`
`
`
`of the outer periphery of the electrostatic member.
`
`
`
`
`
`
`
`
`Preferably,
`the heat
`transfer fluid reservoir is sized and
`
`
`
`
`
`
`
`
`configured to hold heat transfer fluid at a pressure P in the
`
`
`
`
`
`
`
`range of from about PL to about PH,
`the pressure PHbeing
`
`
`
`
`
`
`
`
`sufficiently low that flow of heat transfer fluid through the
`
`
`
`
`
`
`
`
`
`conduits does not dislodge the electrostatically held
`
`
`
`
`
`
`
`substrate, and (ii) the pressure PL being sufliciently high to
`
`
`
`
`
`
`
`
`provide the second higher [low rates of heat transfer fluid to
`
`
`
`
`
`
`
`
`
`the conduits adjacent to the leaking portions of the outer
`
`
`
`
`
`
`
`
`
`periphery substantially without reducing the first lower flow
`
`
`
`
`
`
`
`
`rates of heat transfer fluid to the conduits adjacent to the
`
`
`
`
`
`
`
`
`
`sealed portions.
`
`
`In another version useful for maintaining uniform tem-
`
`
`
`
`
`
`
`
`peratures across the substrate held on the chuck, the elec-
`
`
`
`
`
`
`
`
`
`
`trostatic chuck comprises a support with an electrostatic
`
`
`
`
`
`
`
`member thereon. The electrostatic member comprises an
`
`
`
`
`
`
`
`insulated electrode laminate capable of holding a substrate
`
`
`
`
`
`
`upon application of a voltage to tl1e electrode. Aplurality of
`
`
`
`
`
`
`conduits extend through the support and the electrostatic
`
`
`
`
`
`
`
`
`member for providing heat transfer fluid below the substrate,
`
`
`
`
`
`
`
`at least some of the conduits terminating near an outer
`
`
`
`
`
`
`
`
`
`periphery of the electrostatic member. The multiple conduits
`
`
`
`
`
`
`
`at the outer periphery of the electrostatic member distribute
`
`
`
`
`
`
`
`
`heat transfer fluid at multiple sources below the perimeter of
`
`
`
`
`
`
`
`the substrate improving temperature control of the substrate.
`
`
`
`
`
`
`
`Another version of the electrostatic chuck is substantially
`
`
`
`
`
`
`erosion resistant and is useful for holding a substrate in an ’
`
`
`
`
`
`
`
`
`erosive process environment.
`In this version,
`the chuck
`
`
`
`
`
`
`
`
`comprises a support with an electrostatic member thereon.
`
`
`
`
`
`
`The electrostatic member comprises a laminate including
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`a first insulator layer,
`an electrode on the first insulator
`layer, and (iii) a second insulator layer over the electrode and
`
`
`
`
`
`
`
`
`
`
`merging with the first insulator layer around the circumfer-
`
`
`
`
`
`
`
`
`
`ence of the electrode to electrically insulate the electrode.
`
`
`
`
`
`
`
`The laminate has a contact surface for contacting the sub-
`
`
`
`
`
`
`
`
`
`strate that is substantially planar over the entire width of the
`
`
`
`
`
`
`
`
`
`electrostatic member so that when a substrate is electrostati-
`
`
`
`
`
`
`cally held on the contact surface, the planar contact surface
`
`
`
`
`
`
`
`
`
`provides continuous contact with the substrate to widely
`
`
`
`
`
`
`
`
`separate the electrode from the erosive process environment,
`
`
`
`
`
`
`
`providing enhanced erosion resistance. Preferably, the sup-
`
`
`
`
`
`
`
`port includes an upper surface having a recess therein, and
`
`
`
`
`
`
`
`
`the electrode on the first insulator layer is sized to substan-
`
`
`
`
`
`
`
`
`tially fill the recess so that the laminate forms a substantially
`
`
`
`
`
`
`
`
`
`planar contact surface.
`
`
`
`DRAWINGS
`
`
`These and other features, aspects, and advantages of the
`
`
`
`
`
`
`
`
`present invention will become better understood with regard
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`
`4
`
`to the following description, appended claims, and accom-
`
`
`
`
`
`
`
`
`panying drawings which provide illustrative examples of the
`
`
`
`
`
`
`
`invention, where:
`
`
`FIG. 1 (Prior Art) is a partial cross—section side schematic
`
`
`
`
`
`
`
`View of a prior art electrostatic chuck showing the annular
`
`
`
`
`
`
`
`
`step around the electrode where the polymer insulator rap-
`
`
`
`
`
`
`
`
`
`idly erodes in an erosive environment;
`
`
`
`
`
`FIG. 2a is a partial cross—section side schematic View of
`
`
`
`
`
`
`a process chamber showing operation of a monopolar elec-
`
`
`
`
`
`
`
`trostatic chuck of the present invention,
`
`
`
`
`
`FIG. 2b is a partial cross—section side schematic View of
`
`
`
`
`
`
`a process chamber showing operation of a bipolar electro-
`
`
`
`
`
`
`
`static chuck of the present invention;
`
`
`
`
`
`FIG. 3a is a cross—section side schematic view of a version
`
`
`
`
`
`of the chuck comprising a fluid flow regulator in the support;
`
`
`
`
`
`
`
`
`FIG. 3b is a top view of the chuck shown in FIG. 3:1;
`
`
`
`
`
`
`
`
`FIG. 4a is a partial cross—section side schematic View of
`
`
`
`
`
`
`another version of the chuck of the present invention;
`
`
`
`
`
`
`
`FIG. 4b is a top view of the chuck shown in FIG. 4a;
`
`
`
`
`
`
`
`
`FIG. 5a is a partial cross—section side schematic view of
`
`
`
`
`
`
`another version of the chuck of the present invention;
`
`
`
`
`
`
`
`FIG. 5b is a top View of the chuck shown in FIG. 5a, and
`
`
`
`
`
`
`
`
`
`FIG. 6 is a partial cross—section side schematic view of an
`
`
`
`
`
`
`erosion resistant chuck of the present invention.
`
`
`
`
`
`
`DESCRlP'l'l()N
`
`
`
`
`
`With reference to FIGS. 2a and 2b, operation of an
`
`
`
`
`
`
`
`
`
`
`electrostatic chuck 20 of the present invention in a process
`
`
`
`
`
`
`chamber 25 suitable for processing a substrate 30 will be
`
`
`
`
`
`
`
`
`generally described. The particular embodiment of the pro-
`
`
`
`
`
`
`
`cess chamber 25 shown herein is suitable for plasma pro-
`
`
`
`
`
`
`
`
`cessing of substrates 30 and is provided only to illustrate
`
`
`
`
`
`
`
`
`operation of the chuck 20 and should not be used to limit the
`
`
`
`
`
`
`
`
`
`scope of the invention.
`
`
`
`the electrostatic chuck 20
`With reference to FIG. 2a,
`
`
`
`
`
`
`
`
`
`comprises an electrostatic member 35 having
`a single
`
`
`
`
`
`
`
`electrode 40 with an insulator 45 covering the electrode 40,
`
`
`
`
`
`
`
`and (ii) a substantially planar and conformal contact surface
`
`
`
`
`
`
`
`
`50 capable of conforming to a substrate 30. An electrical
`
`
`
`
`
`
`
`
`connector 55 connects the electrode 40 to a voltage supply
`
`
`
`
`
`
`
`terminal 60 in the chamber 25, to conduct a voltage suitable
`
`
`
`
`
`
`
`for operating the chuck 20. A first voltage supply 65 con-
`
`
`
`
`
`
`
`
`
`nected to the terminal 60 typically comprises a high voltage
`
`
`
`
`
`
`
`DC source of about 1000 to 3000 volts, connected to a high
`
`
`
`
`
`
`
`
`voltage readout through a 1 M9 resistor. A 1 M9 resistor is
`
`
`
`
`
`
`
`provided in the circuit to limit the current flowing through
`
`
`
`
`
`
`
`
`
`the circuit and a 500 pF capacitor is provided as an alter-
`
`
`
`
`
`
`
`
`nating current filter.
`
`
`
`Typically, the electrostatic member 35 is supported by a
`
`
`
`
`
`support 70 that provides structural rigidity to the electro-
`
`
`
`
`
`
`
`
`
`static member 35, and is designed to be secured to a process
`
`
`
`
`
`
`electrode, commonly known as a cathode 80, in the process
`
`
`
`
`
`
`
`chamber 25. Asecond voltage supply 90 is connected to the
`
`
`
`
`
`
`
`cathode 80 in the process chamber 25. At least a portion of
`
`
`
`
`
`
`
`the cathode 80 is electrically conductive,
`typically
`
`
`
`
`
`
`aluminum, and functions as a negatively biased electrode
`
`
`
`
`
`
`
`with respect to an electrically grounded surface 95 in the
`
`
`
`
`
`
`
`
`chamber 25. The second voltage supply 90 is conventional
`
`
`
`
`
`
`
`and electrically biases the cathode 80 by a circuit comprising
`
`
`
`
`
`
`
`an RF impedance that matches the impedance of the process
`
`
`
`
`
`
`
`
`chamber 25 to the impedance of the line voltage, in series
`
`
`
`
`
`
`
`with an isolation capacitor, as shown in FIG. 251.
`
`
`
`
`
`
`
`To operate the chuck 20,
`the process chamber 25 is
`
`
`
`
`
`
`
`
`
`evacuated to a pressure ranging from about 1 to about 500
`
`
`
`
`
`
`
`
`
`Page 10 of 16
`
`

`
`5,883,778
`
`
`
`5
`
`mTorr, and more typically from about 10 to about 100
`
`
`
`
`
`
`
`
`
`mTorr. A semiconductor substrate 30, such as a silicon
`
`
`
`
`
`
`
`is transferred to the chamber 25 from a load lock
`wafer,
`
`
`
`
`
`
`
`
`transfer chamber (not shown), and placed on the conformal
`
`
`
`
`
`
`
`
`contact surface 50 of the electrostatic member 35. Process
`
`
`
`
`
`
`
`gas for etching or depositing material on the substrate 30 is
`
`
`
`
`
`
`
`introduced in the chamber 25. Suitable process gases are
`
`
`
`
`
`
`
`
`generally described in S. Wolf and R. N. Tauber, Silicon
`
`
`
`
`
`
`
`
`Processing for the VLSI Era, Vol. I, Lattice Press, Sunset
`
`
`
`
`
`
`
`
`
`Beach, Calif. (1986), which is incorporated herein by ref-
`
`
`
`
`
`
`
`erence. A plasma is formed from the process gas by acti-
`
`
`
`
`
`
`
`
`vating the second voltage supply 90 to electrically bias the
`
`
`
`
`
`
`
`
`cathode S0 with respect to the grounded surface 95 of the
`
`
`
`
`
`
`
`
`chamber 25.
`
`
`The voltage applied to the mono polar electrode 40 causes
`
`
`
`
`
`
`
`electrostatic charge to accumulate in the electrode 40, and
`
`
`
`
`
`
`
`the plasma in the chamber 25 provides electrically charged
`
`
`
`
`
`
`
`species having opposing polarity which accumulate in the
`
`
`
`
`
`
`
`substrate 30. The accumulated opposing electrostatic charge
`
`
`
`
`
`
`
`results in an attractive electrostatic force between the sub-
`
`
`
`
`
`
`
`
`
`strate 30 and the electrode 40 in the chuck 20, causing the
`
`
`
`
`
`
`
`
`
`
`substrate 30 to be electrostatically held to the chuck 20.
`
`
`
`
`
`
`
`
`Instead of a single electrode 40, the electrostatic member
`
`
`
`
`
`
`
`35 of the chuck 20 can comprise two bipolar electrodes 40a,
`
`
`
`
`
`
`
`
`
`40b, as shown in FIG. 2b. The two bipolar electrodes 40a,
`
`
`
`
`
`
`
`
`
`40b are typically coplanar to one another and have substan-
`
`
`
`
`
`
`
`
`tially equivalent areas to generate equivalent electrostatic
`
`
`
`
`
`
`forces. The first voltage supply 65 powering the bipolar
`
`
`
`
`
`
`
`
`
`electrodes in the chuck 20 can have several alternative
`
`
`
`
`
`
`
`
`
`configurations. In a preferred configuration, the first voltage
`
`
`
`
`
`
`supply 65 comprises first and second voltage sources 65a,
`
`
`
`
`
`
`
`
`65b, which provide negative and positive voltages to the first
`
`
`
`
`
`
`
`
`
`and second electrodes 40a, 40b, respectively to maintain the
`
`
`
`
`
`
`
`
`electrodes 40a, 40b at negative and positive electric poten-
`
`
`
`
`
`
`
`
`tials. The opposing electric potentials induce opposing elec-
`
`
`
`
`
`
`
`
`trostatic charges in the electrodes 4011, 40b and in the
`
`
`
`
`
`
`
`
`
`substrate 30 held to the chuck 20, Without use of a plasma
`
`
`
`
`
`
`
`
`in the process chamber 25, causing the substrate 30 to be
`
`
`
`
`
`
`
`
`
`
`electrostatically held to the chuck 20. Bipolar electrode
`
`
`
`
`
`
`
`
`configurations are advantageous for non-plasma processes
`
`
`
`
`
`
`in which there are no charged plasma species to serve as
`
`
`
`
`
`
`
`
`
`
`charge carriers for electrically biasing the substrate.
`
`
`
`
`
`
`
`The chuck 20 further comprises a plurality of conduits
`
`
`
`
`
`
`
`105 terminating at the contact surface 50 of the electrostatic
`
`
`
`
`
`
`
`member 35 to provide heat transfer fluid, typically helium,
`
`
`
`
`
`
`
`below the substrate 30 to maintain uniform temperatures
`
`
`
`
`
`
`
`across the substrate 30. When the monopolar electrode 40,
`
`
`
`
`
`
`
`
`or the bipolar electrodes 40a, 40b are activated to impart
`
`
`
`
`
`
`
`
`
`opposing electrostatic charge to the substrate 30 and the
`
`
`
`
`
`
`
`
`electrode 40, the substrate 30 is attracted toward and presses _
`
`
`
`
`
`
`
`
`against the conformal contact surface 50 of the electrostatic
`
`
`
`
`
`
`
`member 35. Typically, on a microscopic level, only a small
`
`
`
`
`
`
`portion of the substrate 30 actually contacts the contact
`
`
`
`
`
`
`
`
`
`surface 50. Heat transfer fluid below the substrate 30 flows
`
`
`
`
`
`
`
`
`
`into the microscopic gap between the substrate 30 and the
`
`
`
`
`
`
`
`
`
`contact surface 50, providing thermal coupling by gas con-
`
`
`
`
`
`
`
`
`duction between the substrate 30 and the contact surface 50,
`
`
`
`
`
`
`
`
`
`allowing enhanced thermal
`transfer between the non-
`
`
`
`
`
`
`
`contacting portions of the substrate 30 and the contact
`
`
`
`
`
`
`
`
`
`surface 50. The substrate 30 presses against the contact
`
`
`
`
`
`
`
`
`
`leaking
`surface 50 to define an outer periphery 110 having
`
`
`
`
`
`
`
`portions ll5 where heat
`transfer fluid leaks out
`to the
`
`
`
`
`
`
`
`
`
`
`process environment 120 from between gaps 125 in the
`
`
`
`
`
`
`
`
`outer periphery 110, and
`non-leaking or sealed portions
`
`
`
`
`
`
`
`
`130 where there are substantially no gaps in the outer
`
`
`
`
`
`
`
`
`
`periphery 110 and substantially no heat transfer fluid leaks
`
`
`
`
`
`
`
`
`out.
`
`
`/
`
`
`
`
`
`
`
`
`
`8
`
`
`
`
`
`
`
`6
`
`The heat transfer fluid can be any liquid or gas capable of
`
`
`
`
`
`
`
`
`
`transferring heat to the substrate 30, or removing heat from
`
`
`
`
`
`
`
`
`the substrate 30. Preferably, the heat transfer fluid comprises
`
`
`
`
`
`
`
`
`
`a non-reactive gas that is substantially non-reactive to the
`
`
`
`
`
`
`
`process environment
`in the process chamber 25 so that
`
`
`
`
`
`
`
`
`leaking heat
`transfer fluid does not adversely aifect
`the
`
`
`
`
`
`
`
`
`
`processes performed on the substrate 30. The non-reactive
`
`
`
`
`
`
`
`gas should also be non-reactive to the materials used to
`
`
`
`
`
`
`
`
`
`fabricate the chuck 20, and in particular, to the conformal
`
`
`
`
`
`
`
`
`
`contact surface 50 which is in contact with the non-reactive
`
`
`
`
`
`
`
`
`gas.
`
`For example, when polymeric materials such as polyim-
`
`
`
`
`
`
`
`ide are used to fabricate the conformal Contact surface 50,
`
`
`
`
`
`
`
`
`
`reactive gases that erode polyimide, such as
`oxygen, or
`
`
`
`
`
`
`
`(ii) halogen—containing gases, such as CF4 or CZF6, should
`
`
`
`
`
`
`
`be avoided. Preferably, the heat transfer fluid has an elevated
`
`
`
`
`
`
`
`
`
`thermal conductivity to provide optimal thermal transfer
`
`
`
`
`
`
`
`rates between the substrate 30 and the chuck 20. Preferred
`
`
`
`
`
`
`
`
`
`transfer fluids that are non-reactive to the process
`heat
`
`
`
`
`
`
`
`
`
`environment and conformal contact surface, and that have
`
`
`
`
`
`
`
`
`elevated thermal conductivity comprise helium, argon,
`
`
`
`
`
`
`nitrogen and the like. The thermal conductivity at about
`
`
`
`
`
`
`
`
`room temperature of argon is about 43><1U‘6, nitrogen is
`
`
`
`
`
`
`
`about 62><l0'6, and helium is about 360><10'5 in cal/(sec)
`
`
`
`
`
`
`
`(cm2)(°C./cm). Thus, by elevated thermal conductivity, it is
`
`
`
`
`
`
`meant a room temperature thermal conductivity of about 40
`
`
`
`
`
`
`to about 360 cal/(sec)(cm2)(°C./cm).
`
`
`
`
`The heat transfer fluid can be used to cool or heat the
`
`
`
`
`
`
`
`
`
`substrate 30 to achieve uniform temperatures on the sub-
`
`
`
`
`
`
`
`
`strate 30. When cooling of the substrate is needed, the chuck
`
`
`
`
`
`
`
`
`
`20 is maintained at a lower temperature than the substrate
`
`
`
`
`
`
`
`30, so that the heat transfer fluid can transfer heat from the
`
`
`
`
`
`
`
`
`
`
`
`substrate 30 to the chuck 20. Alternatively, when the sub-
`
`
`
`
`
`
`
`
`strate is to be heated, the chuck 20 is maintained at a higher
`
`
`
`
`
`
`
`temperature than the substrate 30, so that the heat transfer
`
`
`
`
`
`
`
`
`
`fluid can transfer heat from the chuck 20 to the substrate 30.
`
`
`
`
`
`
`
`
`
`
`The electrostatic chuck 20 of the present invention pro-
`
`
`
`
`
`
`
`vides improved temperature control of the substrate 30 by
`
`
`
`
`
`
`
`use of a fluid flow regulator 135 capable of flowing heat
`
`
`
`
`
`
`
`
`
`
`transfer fluid at different flow rates through the conduits 105
`
`
`
`
`
`
`
`
`
`to offset leakage of he at transfer fluid from leaking portions
`
`
`
`
`
`
`
`
`
`115 of the outer periphery 110 of the electrostatic member
`
`
`
`
`
`
`
`
`35. This reduces the formation of “hot spots” or “cold spots”
`
`
`
`
`
`
`
`
`
`on the portions of the substrate 30 overlying the leaking
`
`
`
`
`
`
`
`
`
`
`portions 11 5, allowing maintaining the substrate 30 at
`
`
`
`
`
`
`
`
`uniform temperatures. The fluid flow regulator 135 provides
`
`
`
`
`
`
`
`
`(i) first lower volumetric flow rates of heat transfer fluid
`
`
`
`
`
`
`
`
`
`
`through the conduits 105 adjacent to the sealed portions 130
`
`
`
`
`
`
`
`
`
`of the outer periphery 110 of the electrostatic member 35,
`
`
`
`
`
`
`
`
`and (ii) second higher volumetric flow rates of heat transfer
`
`
`
`
`
`
`
`
`
`fluid through the conduits 105 adjacent
`to the leaking
`
`
`
`
`
`
`
`
`
`portions 115, without reducing the flow rates of heat transfer
`
`
`
`
`
`
`
`
`
`fluid to the non-leaking portions of the outer periphery 110.
`
`
`
`
`
`
`
`
`Preferably, the second flow rates of heat transfer fluid to the
`
`
`
`
`
`
`
`
`
`conduits 105 adjacent to the leaking portions 115 of the outer
`
`
`
`
`
`
`
`
`
`periphery 110 are at least about 2 seem higher, and more
`
`
`
`
`
`
`
`
`
`
`preferably at least about 5 sccm higher, than the first flow
`
`
`
`
`
`
`
`
`
`rates of heat transfer fluid to the conduits 105 adjacent to the
`
`
`
`
`
`
`
`
`
`sealed portions 130. Typically, the first flow rates range from
`
`
`
`
`
`
`
`
`
`
`about 0 to about 1 sccm, and the second flow rates range
`
`
`
`
`
`
`
`
`
`from about 1 seem to about 10 sccm.
`
`
`
`
`
`Typical heat transfer fluid flow regulator structures 135
`
`
`
`
`
`
`
`
`will now be described. One version of the fluid flow regu-
`
`
`
`
`
`
`
`
`
`lator 135 includes a heat transfer fluid reservoir 140 formed
`
`
`
`
`
`
`
`
`
`in the support 70 below the electrostatic member 35, the
`
`
`
`
`
`
`
`
`
`
`length of the reservoir 140 extending across all of the
`
`
`
`
`
`
`
`
`
`
`conduits 105 to provide a short flow path between the
`
`
`
`
`
`
`
`
`
`Page 11 of 16
`
`

`
`5,883,778
`
`7
`
`transfer fluid reservoir 140.
`conduits 105 and the heat
`
`
`
`
`
`
`
`
`
`Multiple conduits 105, typically from about 50 to about 500
`
`
`
`
`
`
`
`
`conduits, and more typically 100 to 200 conduits, extend
`
`
`
`
`
`
`
`
`from the heat transfer fluid reservoir 140 to the contact
`
`
`
`
`
`
`
`
`
`surface 50 of the electrostatic member 35. As shown in FIG.
`
`
`
`
`
`
`3a, the conduits 105 include peripheral conduits 105a near
`
`
`
`
`
`
`
`
`
`a perimeter 150 of the substrate 30, as well as central
`
`
`
`
`
`
`
`
`
`
`conduits 105b at central portions 155 of the substrate 30.
`
`
`
`
`
`
`
`
`Typically, the peripheral conduits 105a are located within
`
`
`
`
`
`
`
`
`about 10 mm, and more preferably within 5 mm from the
`
`
`
`
`
`
`
`
`
`perimeter 150 of the substrate 30. The peripheral conduits
`
`
`
`
`
`
`
`
`105a and central conduits 105b are uniformly spaced apart
`
`
`
`
`
`
`
`
`
`and distributed across substantially the entire Contact surface
`
`
`
`
`
`
`
`
`50 to provide multiple sources of heat transfer fluid below
`
`
`
`
`
`
`
`
`the substrate 30. The multiple sources of heat transfer fluid
`
`
`
`
`
`
`
`
`
`allow the heat
`transfer fluid to be uniformly distributed
`
`
`
`
`
`
`
`
`below th

This document is available on Docket Alarm but you must sign up to view it.


Or .

Accessing this document will incur an additional charge of $.

After purchase, you can access this document again without charge.

Accept $ Charge
throbber

Still Working On It

This document is taking longer than usual to download. This can happen if we need to contact the court directly to obtain the document and their servers are running slowly.

Give it another minute or two to complete, and then try the refresh button.

throbber

A few More Minutes ... Still Working

It can take up to 5 minutes for us to download a document if the court servers are running slowly.

Thank you for your continued patience.

This document could not be displayed.

We could not find this document within its docket. Please go back to the docket page and check the link. If that does not work, go back to the docket and refresh it to pull the newest information.

Your account does not support viewing this document.

You need a Paid Account to view this document. Click here to change your account type.

Your account does not support viewing this document.

Set your membership status to view this document.

With a Docket Alarm membership, you'll get a whole lot more, including:

  • Up-to-date information for this case.
  • Email alerts whenever there is an update.
  • Full text search for other cases.
  • Get email alerts whenever a new case matches your search.

Become a Member

One Moment Please

The filing “” is large (MB) and is being downloaded.

Please refresh this page in a few minutes to see if the filing has been downloaded. The filing will also be emailed to you when the download completes.

Your document is on its way!

If you do not receive the document in five minutes, contact support at support@docketalarm.com.

Sealed Document

We are unable to display this document, it may be under a court ordered seal.

If you have proper credentials to access the file, you may proceed directly to the court's system using your government issued username and password.


Access Government Site

We are redirecting you
to a mobile optimized page.





Document Unreadable or Corrupt

Refresh this Document
Go to the Docket

We are unable to display this document.

Refresh this Document
Go to the Docket