`
`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