Exhaust particulate controller and method

Information

  • Patent Grant
  • 6428609
  • Patent Number
    6,428,609
  • Date Filed
    Friday, September 8, 2000
    24 years ago
  • Date Issued
    Tuesday, August 6, 2002
    22 years ago
Abstract
An exhaust gas particulate controller is included between an exhaust of a barrel chemical vapor deposition reactor and the gas scrubber system. The exhaust gas particulate controller is positioned as close to the exhaust of the reactor as is practical. The exhaust gas particulate controller is a passive system that prevents generation of particulates associated with gas density changes that occur during processing within the reactor.
Description




FIELD OF THE INVENTION




This invention relates generally to reactors for processing semiconductor substrates, and more particularly, to exhaust systems for barrel epitaxial reactors.




BACKGROUND OF THE INVENTION




A variety of reactors has been used to process semiconductor substrates. Some of these reactors have incorporated extraction systems to process gases exhausted from the reactors.




U.S. Pat. No. 4,556,584, entitled “Method For Providing Substantially Waste-Free Chemical Vapor Deposition of Thin-Film on Semiconductor Substrates,” of Sarkozy issued on Dec. 3, 1985 disclosed a system that included a first comparatively low-efficiency thin-film deposition stage and a second comparatively high-efficiency effluent-waste stream removing stage for depositing substantially all of the effluent-waste stream produced by the deposition stage onto disposable baffles. As described by Sarkozy, the second stage was an ultraviolet enhanced vacuum chemical vapor deposition diffusion furnace.




U.S. Pat. No. 4,753,633, entitled “Method and System for Vapor Extraction From Gases,” of Chiu issued on Apr. 5, 1988 disclosed a plasma extraction reactor for removing vapor phase waste from effluent gas streams. This patent simply uses a different type of reactor in the exhaust stream.




Yet another type of heated reaction chamber is disclosed in U.S. Pat. No. 5,417,934, entitled “Dry Exhaust Gas Conditioning,” of Smith and Timms issued on May 23, 1995. In this apparatus, exhaust gases are exposed first to silicon, or a silicon-rich alloy or substance, and then exposed to calcium oxide or a calcium containing mixture. The apparatus was surrounded by a hollow cylindrical heater that incorporated an electrical resistance heater.




European Patent Application Publication No. EP 0 823 279 A2, entitled “Method and Apparatus for Treating Exhaust Gases From CVD, PECVD or Plasma Etch Reactors” taught yet another exhaust gas reactor configuration. Again, the exhaust gas reactor configuration included an electrically heated jacket.




U.S. Pat. No. 5,422,081, entitled “Trap Device for Vapor Phase Reaction Apparatus,” of Miyagi issued on Jun. 6, 1995 disclosed a trap that did not utilize a heater. Miyagi taught that for efficient removal a combination of small diameter discs (57 mm outer diameter and 52 mm inner diameter) and large diameter discs (119 mm outer diameter and 94 mm inner diameter) of stainless steel or aluminum. Miyagi taught that the spacing between the discs was critical in determining the collection efficiency.




Thus, these prior art disclosures show that while exhaust traps have been used, a given trap configuration is dependent both on the gases treated, the configuration of the trap, and characteristics of the particular reactor associated with the trap. Consequently, a particular trap design cannot be migrated to another reactor configuration. These prior art exhaust traps are intended to assist in the scrubbing of the exhaust gasses. The references are concerned. with the composition of the gas exiting from the trap and not particulate contamination in the processing reactor.




SUMMARY OF THE INVENTION




According to the principles of this invention, a novel exhaust particulate controller for receiving process gas from a substrate processing reactor has a housing with an inlet and an outlet. A liner is mounted within the housing. The liner has a first opening about the inlet and a second opening about the outlet. A plurality of baffles is mounted within the housing to form a plurality of chambers bounded by the liner and the plurality of baffles.




Each baffle includes a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension. The second dimension is smaller than the first dimension. An inner surface of the baffle extends from a boundary of the first opening to a boundary of the second opening to define a gas flow path through the baffle. Each baffle is positioned in the housing with the second surface closest to the outlet.




In one embodiment, the liner is selected from the group of liners consisting of a graphite liner, a silicon carbide liner, a silicon carbide coated graphite liner, a quartz liner, and a bead-blasted quartz liner. Similarly, the plurality of baffles is selected from the group of baffles consisting of graphite baffles, silicon carbide baffles, silicon carbide coated graphite baffles, quartz baffles, and bead-blasted quartz baffles.




The exhaust particulate controller has a longitudinal axis, and the gas flow path through a first baffle in the plurality of baffles is above the longitudinal axis, and the gas flow path through a second baffle located adjacent to, but separated from the first baffle is below the longitudinal axis.




The exhaust particulate controller of this invention may have any desired shape and in one embodiment, the controller has a cylindrical shape. The shape of the controller defines the shape of housing and consequently, the shape of the liner.




In another embodiment, the exhaust particulate controller for receiving process gas from a substrate processing reactor includes a cylindrical container having an inlet fixture extending from a closed end surface of the cylindrical container. The inlet fixture bounds an inlet opening. A first liner end element is mounted in an interior of the cylindrical container. The first liner end element is a cylinder with a closed end. The closed end bounds an opening substantially aligned with the inlet opening.




A first baffle is mounted in the interior of the cylindrical container adjacent the first liner end element. The first baffle includes a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where the second dimension is smaller than the first dimension. An inner surface of the first baffle extends from a boundary of the first opening to a boundary of the second opening to define a gas flow path through the first baffle.




A liner spacer element is mounted in the interior of the cylindrical container adjacent the first baffle and then a second baffle is mounted in the interior of the cylindrical container adjacent the first liner spacer element so that the second baffle is adjacent to, but separated from the first baffle. Like the first baffle, the second baffle includes a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where the second dimension is smaller than the first dimension. An inner surface of the second baffle extends from a boundary of the first opening to a boundary of the second opening to define a gas flow path through the second baffle.




A second liner end element is mounted in the interior of the cylindrical container after the second baffle. The second end element is a cylinder with a closed end that bounds an exhaust opening.




A cylindrical cover is removably attached to the cylindrical container. The cylindrical cover includes an outlet fixture extending from an end surface of the cylindrical cover. The outlet fixture bounds an exhaust opening substantially aligned with the exhaust opening of the second liner end element.




According to the principles of this invention, a method for controlling particulate generation by exhaust process gas from a substrate processing reactor includes:




directing the exhaust process gas through a liner having a plurality of surfaces wherein the liner is heated only by the exhaust process gas and deposits are formed on the heated liner; and




orienting the plurality of surfaces to dissipate backpressure created by the exhaust process gas.




In another embodiment, a method for controlling particulate generation by exhaust process gas from a substrate processing reactor includes:




passing the exhaust process gas into an inlet of an exhaust particulate controller;




passing the exhaust process gas from the inlet through a plurality of baffles




wherein each baffle includes a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where the second dimension is smaller than the first dimension;




an inner surface of the baffle extends from a boundary of the first opening to a boundary of the second opening to define a gas flow path through the baffle; and




passing the exhaust process gas from the plurality of baffles to an outlet of the exhaust particulate controller.




Each embodiment of this invention reduces the particulate contamination in the substrate processing reactor created by process gas changes in the exhausts lines. In one embodiment, the substrate processing reactor is a barrel epitaxial reactor. Consequently, the exhaust gas particulate controller and related methods result in better substrate production than prior art systems without the controller of this invention.











BRIEF DESCRIPTION OF THE DRAWINGS





FIG. 1

is a diagram of a semiconductor substrate processing system that includes the exhaust particulate controller of this invention.





FIG. 2

is a cross-sectional view of one embodiment of the exhaust particulate controller of this invention.





FIG. 3

is a more detailed cross-sectional view of one embodiment of the exhaust particulate controller of this invention.





FIG. 4A

is a side cut-away view of one embodiment of an exhaust particulate controller of this invention with clamps where one clamp is shown disassembled.





FIGS. 4B

to


4


D are a front view, cut-away view, and a back view respectively of one embodiment of a baffle of this invention.





FIGS. 4E and 4F

are a side and end view of one embodiment of a spacer according to the principles of this invention.





FIGS. 4G and 4H

are a front and side cut-away view, respectively, of one embodiment of liner end elements of this invention.





FIGS. 4I and 4J

are an end view and a side cut-away view, respectively, of one embodiment of a cylindrical container of this invention.





FIG. 4K

is a more detailed cut-away view of one embodiment of a bottom plate of this invention.





FIGS. 4L and 4M

are an end view and a side cut-away view, respectively, of one embodiment of a cylindrical cover of this invention.











In the following description, elements with the same reference numeral are the same element. Also, the first digit of each element's reference numeral indicates the Figure number in which that element first appeared.




DETAILED DESCRIPTION OF THE INVENTION




In accordance with the present invention, a novel exhaust gas particulate controller


100


is included between an exhaust


125


of a barrel chemical vapor deposition reactor


120


and the gas scrubber system (not shown). Exhaust gas particulate controller


100


is positioned as close to exhaust


125


as is practical, and so is said to be approximately adjacent to exhaust


125


. Exhaust gas particulate controller


100


is a passive system that prevents generation of particulates associated with gas density changes that occur during processing within reactor


120


.




As is known to those of skill in the art, during a process cycle different gases from reactor


120


passed through the exhaust to the scrubbers. For example, a process may have started with nitrogen, switched to hydrogen, and then switched to silane. During each process gas change, there was some mixing of the process gases until the earlier process gas was effectively completely purged. Each of the process gasses had a different density, and during the process gas purge, density variations created backpressure in the exhaust line of the prior art barrel reactors, which, in turn, dislodged deposits in the exhaust line. The intermixing of the process gasses during the purge coupled with the backpressure generated by the purge resulted in the transportation of the dislodged deposits, as particulates, back into the reaction chamber of the prior art barrel reactors.




Exhaust gas particulate controller


100


of this invention mitigates the particulate generation associated with process gas changes in two ways. First, a liner material of exhaust gas particulate control system


100


is selected so that any deposits formed on the surfaces of the liner adhere to the surfaces more strongly than the adherence of the deposits in the prior art exhaust lines. In particular, the liner is selected so that the liner is heated only by the exhaust process gas, and deposits are formed on the heated liner surfaces.




Second, the configuration of the liner surfaces of exhaust gas particulate controller


100


minimizes the effects of backpressures created during gas density changes. As explained more completely below, the plurality of surfaces are orientated to dissipate backpressure created by said exhaust process gas. The combination of reduced backpressure effects and the enhanced adhesion of the deposits effectively eliminates the prior art problem associated with particulate contamination associated with changing the process gas.





FIG. 2

is a more detailed diagram of an exhaust gas particulate controller


200


that is one embodiment of exhaust gas particulate controller


100


. Exhaust gas particulate controller


200


includes an outer container


210


having a right cylindrical container


201


and a cylindrical cover


202


that is removably attached to cylindrical container


201


. Cylindrical container


201


includes an inlet fixture


203


with an inlet opening


203


A. Cylindrical cover


202


includes an outlet fixture


204


with an outlet opening


204


A. In this embodiment, inlet fixture


203


and outlet fixture


204


are centered about, e.g., orientated about, a longitudinal axis


205


that is substantially parallel to and removed from a longitudinal axis


206


of outer container


210


.




Outer container


210


houses a liner


211


and a plurality of baffles


212


, which define a plurality of interior chambers


219


A to


219


D, i.e., a plurality volumes bound by liner surfaces. The baffles are considered as part of the complete liner. Liner


211


and each baffle


212


A,


212


B,


212


C of plurality of baffles


212


are made of graphite, silicon carbide or silicon carbide coated graphite. In another embodiment, liner


211


and plurality of baffles


212


are made of quartz, or bead-blasted quartz. An important aspect is to select the material such that for the type of deposits found in the exhaust line of reactor


100


, the deposits adhere better to the heated material than to the walls of the exhaust line, e.g., the material is heated only by the exhaust process gas, in this embodiment, and deposits are formed on the heated material.




While in this embodiment exhaust gas particulate controller


200


has a cylindrical shape, this is illustrative only and is not intended to limit the exhaust gas particulate controller of this invention to any particular shape. In view of this disclosure, those of skill in the art can implement the novel exhaust gas particulate controller in any desired shape. The shape of the controller defines the shape of housing and consequently, the shape of the liner and baffles.




Another important aspect is the geometric characteristics of each of baffles


212


A,


212


B,


212


C, which determine the gas flow patterns through controller


200


. In this embodiment, each of baffles


212


A to


212


C are identical.




Preferably, as illustrated in

FIG. 2

, each baffle


212




i,


where i equals A, B, or C, respectively, has a first diameter inlet opening aa in a first surface


214




i,


and a second diameter outlet opening bb in a second surface


215




i


opposite and removed from first surface


214




i


where second diameter bb is smaller than first diameter aa so that a conical shaped opening


216




i


is formed that extends from first surface


214




i


to second surface


215




i


and is bounded by inner surface of baffle


214




i


extending from a boundary of first diameter inlet opening aa to a boundary of second diameter outlet opening bb.




To prevent thru flow through exhaust particulate controller


200


, baffles


212


A to


212


C are oriented so that opening


216


C of baffle


212


C is removed from inlet opening


203


A and is positioned above longitudinal axis


206


, i.e., in a first location with respect to longitudinal axis


206


; opening


216


B of baffle


212


B is positioned below longitudinal axis


206


, i.e., in a second location with respect to longitudinal axis


206


; and opening


216


A of baffle


212


A is removed from outlet opening


204


A and is positioned above longitudinal axis


206


, i.e., in the first location with respect to longitudinal axis


206


. As the exhaust gas flows through exhaust particulate controller


200


, the greatest deposits are closest to inlet opening


203


A and the deposits decrease through controller


200


to outlet opening


204


A.




If backpressure and consequently back flow is generated during a process gas change, the back flow into outlet


204


, if it is of sufficient force, flows into a first chamber


219


A and conical edge surface


221


A deflects the flow towards the bottom of system


200


, i.e., in a first direction that is away from opening


218


A. Accordingly, some of the backpressure and associated velocity is dissipated by the configuration of first chamber


219


A. Further, since the back flow from chamber


219


A to


219


B is from a smaller opening


218


A to a larger opening


217


A, the speed of the back flow into chamber


2192


is further reduced.




Each of chambers


219


B,


219


C, and


219


D has a configuration that is equivalent to that of chamber


219


A. Hence, each subsequent chamber reduces the backpressure further. To further reduce the backpressure, chambers


219


A to


219


C are larger than chamber


219


D. Further, the deposits are smallest where the backpressure is the greatest. Thus, the combination of use of material within controller


200


such that any deposits adhere strongly to the material, and the dissipation of the backpressure within controller


200


reduces the likelihood of particulate generation associated with the backpressure, and reduces the likelihood that if any particulates are generated, the particulates are carried back up the exhaust line into the reaction chamber.




Note that unlike the prior art passive exhaust trap system of U.S. Pat. No. 5,422,081 that was designed to scrub the exhaust gasses, controller


200


does not require precise spacing of multiple elements to assure that the exhaust gas flow is not blocked, and to assure that the exhaust gas flow interacts with the multiple elements. Moreover, the materials used in the prior art passive exhaust trip do not form a strong bond with the deposits relative to the bonds formed within controller


200


.




Exhaust particulate controller


300


is a more detailed embodiment of controllers


200


and


100


. Accordingly, the description of controllers


200


and


100


is incorporated herein by reference.




Inlet fixture


303


includes a KF flange


303


B extending from a right cylindrical inlet channel


303


C that in turn extends from a closed end surface


301


A of cylindrical container


301


. Inlet opening


303


A extends through inlet channel


303


C and the bottom of cylindrical container


301


. Similarly, outlet fixture


304


includes a KF flange


304


B extending from a right cylindrical inlet channel


304


C that in turn extends from a circular outer end surface


302


A of cylindrical cover


302


. Outlet opening


304


A extends through inlet channel


304


C and through cover


302


.




Cover


302


includes a circular grove


302


B nears its outer circumference that is formed in a rim


302


C of cover


302


. Grove


302


B is positioned so that an O-ring


305


placed in grove


302


B forms a seal with a surface of a lip


301


B of cylindrical container


301


. Rim


302


is sized so that lip


301


B fits in rim


302


C and centers cover


302


on container


301


.




Cover


302


also includes three circular openings of which only one


308


is visible in the cut-away view of FIG.


3


. The three circular openings are positioned uniformly about the center of cover


302


. (See

FIG. 4L.

) A stainless steel spring is placed in each opening. The strength of the springs is selected to hold the liner in place, but also to allow thermal expansion of the liner.




In this embodiment, liner


311


is multiple pieces


211


A to


211


D, and baffles


312


A to


312


C are discrete circular elements. First liner end element


211


A is a cylinder with a closed end. In the closed end is a thru opening that is slightly larger than inlet opening


303


A. Liner end element


211


A is placed in container


301


so that the thru opening is substantially aligned with inlet opening


303


A, and then baffle


312


C is inserted in the position illustrated.




Next, cylindrical liner spacer element


211


B is inserted in container


301


and then baffle


312


B is inserted as shown. After baffle


312


B is inserted, another cylindrical liner spacer element


211


C is inserted in container


301


followed by another baffle


312


A. Finally, a second liner end element


211


D with a closed end is inserted. In the closed end is a thru opening that is slightly larger than outlet opening


304


A. Finally, the springs are placed in cover


302


and cover


302


is placed on container


301


to that outlet opening


304


A is substantially aligned with the thru opening in element


211


D. The openings are said to be substantially aligned in view of the different sizes of the openings. In this embodiment, C-clamps are placed in grooves


301


C and


302


D to secure cover


302


and container


301


together. The operation of controller


300


is identical to that described above for controller


200


.





FIGS. 4A

to


4


M are more detailed drawings of exhaust particulate controller


300


. The materials and dimensions given below are illustrative only and are not intended to limit the invention to the specific dimensions and materials described. The criteria for selecting the liner material and baffle material were given above. The materials for the housing can be selected from any material that is not adversely affected by exposure to the exhaust gasses.





FIG. 4A

is a side cut-away view of exhaust particulate controller


330


with clamps


410


where one clamp is shown disassembled with parts


411


, and


412


and bolt


413


. One clamp suitable for use with this invention is a double claw clamp with an aluminum body


411


,


412


and a steel bolt


413


. One source for such a clamp is MDC, 23842 Cabot Boulevard, Hayward, Calif., 94545, USA under Part No. 802000.





FIGS. 4B

to


4


D are a front view, cut-away view, and a back view respectively of baffle


312


i where i is A to C. Table 1 gives dimensions for one embodiment of baffle


312




i.


In this embodiment, baffle


312




i


is made of graphite.















TABLE 1












Dimension







Reference




Inches (cm)







No.




(Unless otherwise Specified)













4B1




4.810 (12.217)







4B2




1.906 radius (4.841)







4C1




0.125 (0.318)







4C2




90°







4C3




1.38 (3.505)







4C4




0.094 (0.239)







4C5




0.250 (0.635)







4C6




0.625 (1.588)







4D1




0.458 (1.163)







4D2




0.083 (0.211)







4D3




1.458 (3.703)







4D4




1.833 (4.656)







4D5




1.375 (3.493)







4D6




0.125 (0.318)







4D7




0.125 radius (0.318)







4D8




1.244 (3.160)







4D9




2.488 (6.320)
















FIGS. 4E and 4F

are a side and end view of spacer


211




i,


where i is B and C (See FIG.


3


). Table 2 gives dimensions for one embodiment of spacer


211




i.


In this embodiment, spacer


211




i


is made of graphite.















TABLE 2












Dimension







Reference




Inches (cm)







No.




(Unless otherwise Specified)













4E1




4.810 (12.217)







4E2




4.31 (10.947)







4F1




1.250 (3.175)
















FIGS. 4G and 4H

are a front and side cut-away view, respectively, of liner end elements


211




j,


where j is A and D (See FIG.


3


). Table 3 gives dimensions for one embodiment of liner end element


211


A, while Table 4 gives dimensions for one embodiment of liner end element


211


D. In this embodiment, end elements


211


A and


211


D are made of graphite.















TABLE 3












Dimension







Reference




Inches (cm)







No.




(Unless otherwise Specified)













4G1




4.810 (12.217)







4G2




2.00 (5.08)







4G3




0.875 (2.223)







4H1




0.060 Radius (0.152)







4H2




0.125 Radius (0.318)







4H3




4.310 (10.947)







4H4




0.250 (0.635)







4H5




1.125 (2.858)


























TABLE 4












Dimension







Reference




Inches (cm)







No.




(Unless otherwise Specified)













4G1




4.810 (12.217)







4G2




2.00 (5.08)







4G3




0.875 (2.223)







4H1




0.060 Radius (0.152)







4H2




0.125 Radius (0.318)







4H3




4.310 (10.947)







4H4




0.250 (0.635)







4H5




1.500 (3.810)
















FIGS. 4I and 4J

are an end view and a side cut-away view, respectively, of cylindrical container


301


. In this embodiment, cylindrical container is made of five parts


421


to


425


that are


316


stainless steel with an electro polish finish. TABLE 5 gives a name and a size of the material from which each part is made.














TABLE 5











Dimension






Ref.





Inches(cm)






No.




Name




(Unless otherwise Specified)











421




Bottom Plate




 6.00 (15.24) × 0.437 (1.110)






422




Body Tube




5.000 (12.700) O.D.,








0.065 (0.165) Thick Wall






423




Top Plate




 3.75 (9.525) Diameter ×








0.250 (0.635)






424




KP Flange




NW-50






425




Tubing




2.000 (5.080) O.D. ×








1.870 (4.750) I.D.











O.D. is outside diameter.










I.D. is inside diameter.













Table 6 gives dimensions for one embodiment of cylindrical container


301


as illustrated in FIG.


4


J.















TABLE 6












Dimension







Reference




Inches (cm)







No.




(Unless otherwise Specified)













4J1




6.84 (17.374)







4J2




0.124 (0.315)







4J3




6.22 (15.799)
















FIG. 4K

is a more detailed cut-away view of bottom plate


421


. Table 7 gives dimensions for one embodiment of bottom plate


421

















TABLE 7












Dimension







Reference




Inches (cm)







No.




(Unless otherwise Specified)













4K1




5.80 (14.732)







4K2




5.37 (13.640)







4K3




5.010 (12.725)







4K4




5.12 (13.005)







4K5




5.260 (13.360)







4K6




0.437 (1.110)







4K7




0.352 (0.894)







4K8




0.186 (0.472)







4K9




0.124 (0.315)
















FIGS. 4L and 4M

are an end view and a side cut-away view, respectively, of cylindrical cover


302


, sometimes called a flange end cap. In this embodiment, cylindrical cover


302


is made of three parts


431


to


433


(

FIG. 4M

) that are


316


stainless steel with an electro polish finish. TABLE 8 gives a name and a size of the material from which each part is made.
















TABLE 8













Dimension







Ref.





Inches(cm)







No.




Name




(Unless otherwise Specified)













431




Plate




6.00 (15.24) Diameter







432




KF Flange




NW-50







433




Tubing




2.000 (5.080) O.D. ×









1.870 (4.750) I.D.













O.D. is outside diameter.











I.D. is inside diameter.













Table 9 gives dimensions for one embodiment of cylindrical cover


302


as illustrated in FIG.


4


L.















TABLE 9












Dimension







Reference




Inches (cm)







No.




(Unless otherwise Specified)













4L1




0.875 (2.223)







4L2




105°







4L3




105°







4L4




0.750 (1.905) Diameter ×








0.375 (0.953) deep C'Bore on








a 3.38 (8.585) diameter B.C.







4L5




1.870 (4.750)







4L6




6.00 (15.240)















Table 10 gives dimensions for one embodiment of cylindrical cover


302


as illustrated in FIG.


4


M.















TABLE 10












Dimension







Reference




Inches (cm)







No.




(Unless otherwise Specified)













4M1




5.767 (14.648)







4M2




5.487 (13.937)







4M3




5.240 (13.310)







4M4




5.37 (13.640)







4M5




5.80 (14.732)







4M6




0.062 (0.157)







4M7




1.31 (3.327)







4M8




0.687 (1.745)







4M9




0.144 (.366)







4M10




0.09 (0.229)















For the embodiment of

FIGS. 4A

to


4


M, O-ring


305


is a silicone O-ring with a 5.50 inch inside diameter, a 5.68 inch outside diameter, and a 0.09 inch cross section width. A wave spring that is placed in holes


308


is a flat wire compression spring that has a 0.750 inch outside diameter, a 13 pound load, and a spring rate of 70 lbs/in. One wave stainless steel spring suitable for use in this invention is provided by Smalley Steel Ring Company of Wheeling, Ill., U.S.A., Part No. CS075-M4-S17. The characteristics of this spring are:






















Operates in Bore Diameter




0.750




inches







Load




13




pounds







Work Height




0.314




inches







Free Height




0.500




inches







Number of Turns




6








Number of Waves




3.5








Wire Thickness × Radial Wall




0.10




in. × 0.78 in.







Spring Rage




70




lbs/in















The drawings and the forgoing description gave examples of the present invention. The scope of the present invention, however, is not limited by these specific examples. Numerous variations, whether explicitly given in the specification, such as differences in structure, dimension, and use of material, are possible. The scope of the invention is at least as broad as given by the following claims.



Claims
  • 1. An exhaust particulate controller for receiving process gas from a substrate processing reactor, said exhaust particulate controller comprising:a housing having an inlet and an outlet; a liner mounted within said housing, said liner having a first opening about said inlet and a second opening about said outlet; and a plurality of baffles mounted within said housing to form a plurality of chambers bounded by said liner and said plurality of baffles, wherein each baffle includes a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where said second dimension is smaller than said first dimension; an inner surface of said baffle extends from said first opening to said second opening to define a gas flow path through said baffle; and each baffle is positioned in said housing with said second surface closest to said outlet.
  • 2. The exhaust particulate controller of claim 1 wherein said liner is selected from the group of liners consisting of graphite liners, silicon carbide liners, silicon carbide coated graphite liners, quartz liners, and bead-blasted quartz liners.
  • 3. The exhaust particulate controller of claim 1 wherein said plurality of baffles is selected from the group of baffles consisting of graphite baffles, silicon carbide baffles, silicon carbide coated graphite baffles, quartz baffles, and bead-blasted quartz baffles.
  • 4. The exhaust particulate controller of claim 1 further comprising a longitudinal axis wherein a gas flow path through a first baffle in said plurality of baffles is above said longitudinal axis, a gas flow path through a second baffle located adjacent to the first baffle is below said longitudinal axis.
  • 5. The exhaust particulate-controller of claim 1 wherein said housing is stainless steel.
  • 6. The exhaust particulate controller of claim 1 wherein said housing is cylindrical.
  • 7. An exhaust particulate controller for receiving process gas from a substrate processing reactor, said exhaust particulate controller comprising:a cylindrical container having an inlet fixture extending from a closed end surface of said cylindrical container wherein said inlet fixture bounds an inlet opening; a first liner end element mounted in an interior of said cylindrical container wherein said first liner end element comprises a cylinder with a closed end wherein said closed end bounds an opening substantially aligned with said inlet opening; a first baffle mounted in said interior of said cylindrical container adjacent said first liner end element, said first baffle comprising a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where said second dimension is smaller than said first dimension, and an inner surface of said first baffle extends from a boundary of said first opening to a boundary of said second opening to define a gas flow path through said first baffle; a liner spacer element mounted in said interior of said cylindrical container adjacent said first baffle; a second baffle mounted in said interior of said cylindrical container adjacent said first liner spacer element, said second baffle comprising a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where said second dimension is smaller than said first dimension, and an inner surface of said second baffle extends from said first opening to said second opening to define a gas flow path through said second baffle; a second liner end element mounted in said interior of said cylindrical container after said second baffle wherein said second liner end element comprises a cylinder with a closed end wherein said closed end bounds an exhaust opening; and a cylindrical cover removably attached to said cylindrical container, said cylindrical cover having an outlet fixture extending from an end surface of said cylindrical cover wherein said outlet fixture bounds an exhaust opening substantially aligned with said exhaust opening of said second liner end element.
  • 8. The exhaust particulate controller of claim 7 wherein said first and second liner end elements, said first and second baffles, and said liner spacer element are made of any one of graphite, silicon carbide, silicon carbide coated graphite, quartz, and bead-blasted quartz.
  • 9. The exhaust particulate controller of claim 7 wherein said first and second liner end elements, said first and second baffles, and said liner spacer element are graphite.
  • 10. The exhaust particulate controller of claim 7 further comprising a longitudinal axis wherein said gas flow path through said first baffle is above said longitudinal axis and said gas flow path through said second baffle is below said longitudinal axis.
  • 11. The exhaust particulate controller of claim 7 wherein said cylindrical container is stainless steel.
  • 12. A method for controlling particulate generation by exhaust process gas from a substrate processing reactor comprising:directing said exhaust process gas from said substrate processing reactor through a liner having a plurality of baffle surfaces wherein said liner is heated only by said exhaust process gas and deposits are formed on said heated liner from said exhaust process gas from said substrate processing reactor; and orienting said plurality of baffle surfaces to dissipate backpressure created by a density change of said exhaust process gas from said substrate processing reactor thereby controlling particulate generation from said deposits.
  • 13. The method of claim 12 wherein said liner is made of any one of graphite, silicon carbide, silicon carbide coated graphite, quartz, and bead-blasted quartz.
  • 14. A method for controlling particulate generation by exhaust process gas from a substrate processing reactor comprising:passing said exhaust process gas into an inlet of an exhaust particulate controller; passing said exhaust process gas from said inlet through a plurality of baffles wherein each baffle includes a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where said second dimension is smaller than said first dimension; an inner surface of said baffle extends from a boundary of said first opening to a boundary of said second opening to define a gas flow path through said baffle; and said plurality of baffles are heated by said exhaust process gas and deposits form on at least one baffle in said plurality of baffles from said exhaust process gas; and passing said exhaust process gas from said plurality of baffles to an outlet of said exhaust particulate controller wherein said plurality of baffles dissipate backpressure created by a density change of said exhaust process gas from said substrate processing reactor thereby controlling particulate generation from said deposits.
  • 15. A method for controlling particulate generation by exhaust process gas from a substrate processing reactor comprising:passing said exhaust process gas into an inlet of an exhaust particulate controller; passing said exhaust process gas from said inlet through a plurality of graphite baffles wherein each graphite baffle includes a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where said second dimension is smaller than said first dimension; an inner surface of said graphite baffle extends from a boundary of said first opening to a boundary of said second opening to define a gas flow path through said graphite baffle; and passing said exhaust process gas from said plurality of graphite baffles to an outlet of said exhaust particulate controller.
  • 16. A method for controlling particulate generation by exhaust process gas from a substrate processing reactor comprising:passing said exhaust process gas into an inlet of an exhaust particulate controller; passing said exhaust process gas from said inlet through a plurality of baffles wherein each baffle includes a first surface bounding a first opening with a first dimension and a second surface bounding a second opening of a second dimension where said second dimension is smaller than said first dimension; an inner surface of said baffle extends from a boundary of said first opening to a boundary of said second opening to define a gas flow path through said baffle; and said plurality of baffles are made of any one of silicon carbide, silicon carbide coated graphite, quartz, and bead-blasted quartz; and passing said exhaust process gas from said plurality of baffles to an outlet of said exhaust particulate controller.
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Foreign Referenced Citations (2)
Number Date Country
0 823 279 Feb 1998 EP
0 823 279 Oct 1998 EP