Abstract:
A process and apparatus to deliver both process chemical and solvent for cleaning the process chemical in a solvent purge refill system along with an integral solvent sorption module, in a single “assembly” that permits ease of shipping, minimal end-user interaction, sufficient solvent for the solvent purge operation, without residual solvent, requiring disposal. This eliminates customer handling of the solvent, and eliminates the customer&#39;s need to find a solvent waste facility, as residual solvent can be returned in the same package in one piece/one step.

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
   The present application claims benefit of Provisional patent applications 60/213,092 of 21 Jun. 2000 and 60/215,796 of 5 Jul. 2000. 

   STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT 
   Not applicable. 
   BACKGROUND OF THE INVENTION 
   The Present Invention is directed to the field of process chemical delivery in the electronics industry and other applications requiring high purity chemical delivery. More specifically, the present invention is directed to apparatus and processes for the cleaning of process chemical delivery lines, containers and associated apparatus, particularly during changeout of process chemical or process chemical containers in such process chemical delivery lines. 
   Evacuation and gas purge of process chemical lines has been used to remove residual chemicals from delivery lines. Both vacuum draw and inert gas purge are successful in quickly removing high volatility chemicals, but are not effective with low volatility chemicals. Safety is a problem when extracting highly toxic materials. 
   Use of solvents to remove residual chemicals is not new. Various patents have sought to clean systems using solvents, which are hereby specifically incorporated by reference in their entirety herein: 
   U.S. Pat. No. 5,045,117 describes a method and apparatus for cleaning printed wiring assemblies with a solvent and vacuum action. 
   U.S. Pat. No. 5,115,576 discloses an apparatus and method of cleaning semiconductor wafers using isopropyl alcohol solvent. 
   Additional patents regarding solvent cleaning include; U.S. Pat. No. 4,357,175, U.S. Pat. No. 4,832,753, U.S. Pat. No. 4,865,061, U.S. Pat. No. 4,871,416, U.S. Pat. No. 5,051,135, U.S. Pat. No. 5,106,404, U.S. Pat. No. 5,108,582, U.S. Pat. No. 5,240,507, U.S. Pat. No. 5,304,253, U.S. Pat. No. 5,339,844, U.S. Pat. No. 5,425,183, U.S. Pat. No. 5,469,876, U.S. Pat. No. 5,509,431, U.S. Pat. No. 5,538,025, U.S. Pat. No. 5,562,883 and Japanese 8-115886. 
   Various other prior art US patents are in the same technical field as the Present Invention and are specifically incorporated by reference herein in their entirety:
     U.S. Pat. No. 5,472,119—Dec. 5, 1995—Assembly for dispensing fluids from multiple containers;   U.S. Pat. No. 5,398,846—Mar. 21, 1995—Assembly for simultaneous dispensing of multiple fluids;   U.S. Pat. No. 5,297,767—Mar. 29, 1994—Multiple Container Holder;   U.S. Pat. No. 4,570,799—Feb. 18, 1986—Multiple Container Package;   U.S. Pat. No. 3,958,720—May 25, 1976—Adjustable Multiple container dispensing apparatus;   U.S. Pat. No. 5,557,381—Sep. 17, 1996—Develop supplying unit with multiple containers;   U.S. Pat. No. 5,573,132—Nov. 12, 1996—Dispensing Container;   U.S. Pat. No. 5,409,141—Apr. 25, 1995—Two component mixing and delivery system;   U.S. Pat. No. 5,565,070—Oct. 15, 1996—Solvent vapor sucking method and solvent recovering apparatus;   U.S. Pat. No. 4,537,660—Aug. 27, 1985—Vapor generating and recovering apparatus; and   U.S. Pat. No. 5,051,135—Sep. 24, 1991—Cleaning method using a solvent while preventing discharge of solvent vapors to the environment.   

   Current systems involving solvent purging of internal plumbing lines require separate solvent ampoules. These either take up space inside an existing cabinet or require a separate cabinet with associated plumbing, purging and control features. In addition, these require the use of a solvent capture system to trap the spent solvent for return to the producer&#39;s site, or that must be handled as solvent waste. 
   BRIEF SUMMARY OF THE INVENTION 
   The Present Invention is a process and apparatus to deliver both process chemical and solvent for cleaning the process chemical in a solvent purge refill system along with an integral solvent capture ampoule, in a single “assembly” that permits ease of shipping, minimal end-user interaction, sufficient solvent for the solvent purge operation, without residual solvent, requiring disposal. This eliminates customer handling of the solvent, and eliminates the customer&#39;s need to find a solvent waste facility, as residual solvent can be returned in the same package in one piece/one step. 

   
     BRIEF DESCRIPTION OF SEVERAL VIEWS OF THE DRAWINGS 
       FIG. 1  is a schematic cross-sectional illustration of a first embodiment of the Present Invention. 
       FIG. 2  is a schematic cross-sectional illustration of an embodiment of the Present Invention. 
       FIG. 3  is a schematic partial cross-sectional illustration of an embodiment of the Present Invention. 
       FIG. 4  is a schematic cross-sectional illustration of an embodiment of the Present Invention. 
       FIG. 5  is a perspective view of one of two mirror image mating bracket sections for holding the solvent ampoules on a source chemical container. 
       FIGS. 6A and B  are a plan view and a cross-sectional view of an embodiment of a solvent ampoule of the Present Invention. 
       FIG. 7  is a perspective view of a source chemical container, solvent support bracket, solvent ampoule and solvent capture ampoule of a preferred embodiment of the Present Invention. 
       FIG. 8  is a schematic illustration of a manifold for an embodiment of the Present Invention. 
   

   DETAILED DESCRIPTION OF THE INVENTION 
   The Present Invention comprises a plurality of vessels, minimally two vessels; typically, but not exclusively, made from stainless steel, or other suitable materials that are not reactive with the process chemical or solvents in question. The materials of construction of these containers can include, but is not limited to: various types of steel, 316 stainless steel, nickel, Hasteloy, aluminum, chromium or other metals; various types of plastics and polymers, including Teflon, polypropylene, polyethylene, and similar compounds; ceramic materials, including silicon carbide, alumina, and similar compunds; and glass containers, including borosilicate glass, fused quartz and similar compounds. 
   Either or both of the source chemical and solvent vessels may include liners, internal plating, and other materials of construction. The solvent and source chemical container vessels are not required to be manufactured from the same material, such that the source chemical container may be constructed from steel, while a solvent ampoule may be constructed from plastic, for example. 
   In addition, the solvent container may contain a plurality of chambers, fluidly communicating with a single outlet or a plurality of outlets, such that the solvent provided for solvent cleaning may be available for more than one cycle, and may be used for alternate chemistries, for example, one chamber may contain a washing ingredient, while another chamber may contain a rinsing ingredient. Finally, one or more chambers may contain a solvent sorption media, wherein one application is to convert a volatile organic chemical (VOC) residue into a solid waste for more convenient handling. 
   The main source chemical container comprises a large (from 1 liter to 200 or more liter) container, which comprises a sealed storage volume typically filled with process chemicals, a metallic or non-metallic diptube attached either permanently (welded) or removeably (bolted on) extending to near the bottom of the source chemical container, an internal or external level sense, with at least one of the level sensors placed in such a position, typically just above the bottom of the dip tube, that it can indicate low level in the source chemical container. This level sensor may comprise any of the following: metallic or non-metallic float sensors; discrete or continuous ultrasonic level sensors; continuous or discrete thermal sensors; capacitive and or conductivity based level sensors; RF based level sensors; and other similar internal level sensors; or external sensors such as scales, load cells, external ultrasonic or thermal sensors placed either on the container or around the chemical delivery lines; and other similar means for detecting low level. 
   The low level detection is routed to a solvent purge controller and/or to an operator in order to signal that a solvent purge process is required. The source chemical container will also comprise a plurality of valves, with a minimum of at least one outlet valve attached to the diptube, and in most cases will include a second valve for inert push gas, and/or a third valve for transfer of process chemical from an independent source of process chemical. Each of these valves can be connected integrally either permanently (welded on) or removably (bolted on, through a VCR connection for example). The valves may be manual, but preferably are automatic, comprising pneumatic, electric, hydraulic or solenoid actuated valves. 
   The source chemical container also comprises a chime ring that is placed on support structures and is used to protect the process valves during shipment. 
   Another attribute of the source chemical container is that it may integrally contain one or more smaller or secondary “solvent” ampoules either mounted entirely within or otherwise integral to the source chemical container, as opposed to a separate ampoule welded on or bolted on to the source chemical container. 
   The secondary “solvent” ampoule comprises a small (50 milliliter to one liter) container, which comprises a sealed storage volume typically filled with a solvent that is selected by nature of it&#39;s solubility for the process chemical, a metallic or non-metallic diptube either permanently (welded) or removably (bolted on) extending to near the bottom of the solvent ampoule. 
   An external or internal level sensor may optionally be used in this application also, although with less of a requirement than is needed with the source chemical container. The purpose of this level sensor would be to indicate that the solvent ampoule is empty and to cease further attempts at solvent washing. This level sensor may comprise any of the following: metallic or non-metallic float sensors; discrete or continuous ultrasonic level sensors; continuous or discrete thermal sensors; capacitive and or conductivity based level sensors; RF based level sensors; and other similar internal level sensors; or external sensors such as scales, load cells, external ultrasonic or thermal sensors placed either on the ampoule or around the chemical delivery lines; and other similar means for detecting low level. 
   The solvent ampoule also includes two openings in the ampoule, one connected to the diptube, and extending to the bottom of the ampoule such that all solvent may be used in the solvent purge process. The other opening extends only into the headspace of the solvent ampoule, and is used for alternately pressurizing, venting and depressurizing the solvent container during the solvent purge operation. These openings may be sealed with manual or pneumatically actuated valves, and attached to the solvent purge control manifold with standard VCR-type or other high purity connectors. The openings may also be sealed with automatically sealing quick disconnect fittings. Typically, the fittings on the solvent ampoule are keyed to prevent accidental crossing of the inlet (headspace) and outlet (diptube) volumes in the solvent ampoule. 
   This solvent ampoule may comprise a plurality of chambers separated by either vertical (longitudinal) or horizontal (lateral) barriers, which can be used to isolate various cleaning solvents reactive materials or rinse materials, and/or additional solvent for multiple cleaning operations, or for use as a solvent recovery ampoule, either by pushing the solvent into the chamber as a fluid, or by absorbing the solvent into a solid media, such as carbon, and any number of alternative solvent absorbing media, of which a number are available on the open market. This chamber or preferably ampoule is located such that solvent vapors or liquid can be drawn into it, either by process vacuum or through push gas pressure (fluidly communicating with the solvent ampoule), such elevated pressure potentially provided upon initial filling of the solvent ampoule. The sorbent media placed in the solvent capture ampoule can be a number of types of material suitable for trapping and holding the cleaning solvent. For example, activated carbon may be used to capture volatile organic compounds, while materials such as acrylic polymers and caustic and/or acid neutralizers may be used depending on the solvent types. The sorbent material may also comprise liquids that can be used to improve the hazard ratings of the used solvent. Such sorbent materials can be perfluorocarbons, chlorofluorocarbons, and hydrocarbons of either high volatility (such as the perfluorocarbons) or low volatility (such as oils, i.e., Fomblin type fluorocarbon vacuum pump oil), and similar inert compounds. Both low volatility and high volatility in inert sorbent materials may be used depending on process requirements. 
   Note that each chamber will have at least one, and in most cases a plurality of ports for the delivery of the solvent to the process, and to provide inert gas pressure for pushing the solvent out of the ampoules. In the case of an absorbent ampoule, at least one, but in most cases a plurality of valves are used to direct the spent solvent into the ampoule and to provide a venting or vacuuming of the ampoule to accelerate the absorption of the solvent onto the media. 
   Additionally, the source of the pressure for the solvent ampoule may come from a pre-pressurization prior to delivery of the solvent ampoule, thereby precluding the need for an inert gas source on the solvent ampoule inlet, and even minimizing the need for such an inlet. Additionally, the capture ampoule may be provided under pre-established vacuum so that spent solvent material may be directed into it without the requirement of a vent port on the solvent capture ampoule. 
   Additional ampoules can be used in order to accomplish the purposes of cleaning with a compound requiring a rinse and/or to accomplish the purpose of holding solvent absorbing media. Therefore, the use of multiple solvents and rinse solutions and absorbent media can all be envisioned using either multiple ampoules or ampoules with multiple chambers. 
   The secondary solvent ampoule is then attached to the main source chemical container for shipping purposes. The attachment may be through a direct welding of the secondary ampoule to a portion of the source chemical container, i.e., by welding it to the chime supports; or to the container walls; or to a mounting bracket that is attached to the source chemical container. The attachment can also include bolting the secondary ampoule to the primary (source chemical) container, either through means of a clamp that secures the small ampoule to the chime ring, chime ring support, or to the main body of the container, and through any means of mounting brackets, welded, clamped or bolted to the source chemical container. 
   In addition, the solvent ampoule may be placed internal to the larger source chemical container so that the only visible part of the solvent ampoule is the two tube connections. In this case, the solvent ampoule may be welded, clamped or bolted to the interior of the source chemical container, and may comprise any combination of separate ampoule walls or shared ampoule walls. 
   In operation, the source chemical container is connected to a chemical delivery line, such that process chemical may flow to a suitable reaction system. This chemical line includes valves and other components required to perform the solvent purge operation. The solvent ampoule also connects to the solvent purge manifold through additional valving, allowing the solvent to flow in a suitable manner, when commanded to by the operator or by an electronic control unit. The process line communicates with the solvent ampoule through this manifold. When installed, the valves on the solvent ampoule are connected to the solvent purge operation in a leak tight manner, such that the solvent can be transmitted throughout the key affected regions of the process chemical delivery line, that are isolated by the solvent purge manifold control valves. This control may be either manual or automatic and both manual, electrical, pneumatic and hydraulic valves are contemplated. 
   In one particular embodiment, the main source chemical container is one of the family of 4, 11, 19, and 38 liter stainless steel containers, comprising a variety of level sensors, and containing either two or three valves on the source chemical container. One of the valves communicates with a stainless steel diptube, that protrudes into the chemical volume and is used for dispensing the process chemical. These containers each may contain a chime ring and chime supports. However, a chime ring is not a requirement of this invention, and a suitable container with internal solvent and capture ampoules can be envisioned, without the need for a chime ring or chime ring supports. 
   The large container may contain any process chemicals or high purity source chemicals, including but not limited to: tantalum pentaethoxide (TAETO), tetrakis(diethylamino) titanium (TDEAT), tetrakis(dimethylamino) titanium (TDMAT), copper hexafluoroacetylacetonate-trimethylvinylsilane (Cu(hfac)TMVS) and similar CVD copper precursors, tetraethylorthosilicate (TEOS) and other chemical vapor deposition (CVD) silicon precursors such as tetramethylcyclotetrasiloxane (TMCTS), boron and phosphorus containing CVD precursors such as trimethylborate (TMB), triethylborate (TEB), trimethylphosphite (TMPi), and triethylphosphate (TEPO), bistertiarybutylaminosilane (BTBAS), tantalum tetraethoxidedimethylaminoethoxide (TAT-DMAE), t-butylimidotrisdiethylamido tantalum (TBTDET), triethyl arsenate (TEASAT) and similar arsenic precursors such as triethyl arsenite (TEOA), low-K spin on materials such as VELOX polyarylene ethers available from Air Products and Chemicals, Inc. of Allentown, Pa., FLARE fluorinated arylene ethers available from Honeywell, SILK aromatic hydrodcarbon resins available from Dow Chemical of Midland, Mich., and other related compounds, where rapid, complete removal of the process chemical benefits from washing of the process piping with a suitable solvent. 
   The source chemical solvent ampoule is filled with a quantity of source chemical solvent contained in said source chemical solvent ampoule comprising organic alcohols such as methanol, ethanol, propanol, butanol, acetone, tetrahydrofuran, dimethylsiloxane, water, aliphatic hydrocarbons such as hexane, heptane, octane, decane, and dodecane, aromatic hydrocarbons, ketones, aldehydes, hydrocarbons, ethers, esters, glymes, aromatic hydrocarbons, halogen containing alcohols, alkyl nitrites, alkanols, organic amines, fluorinated compounds and perfluorocarbons perfluorohexane, perfluoroheptane and mixtures thereof. 
   Note also that process chemicals that are reactive, but provide soluble byproducts are also amenable to the present Invention, and that the term solvent, in the present invention, is also contemplated in the broad definition of a “solvent” for purposes of the present invention. Included in this category of reactive “solvents” are acids, bases, and reactive solvents. Specific examples are; the use of ethanol with TDEAT, in which titanium ethoxide is produced, and which is soluble in ethanol, ensuring complete removal. Use of nitric acid solutions can be used to remove copper oxidation byproducts, while HF solutions can be used to remove oxidation byproduct materials, such as titanium oxide or tantalum oxide. Such reactive source chemical “solvents” are broadly contemplated as a quantity of source chemical acids or bases, that act in combination as a solvent for the high purity source chemical, or that may react with the high purity source chemical to create high solubility byproducts. This group may comprise HF, HNO 3 , HCl, H 2 SO 4 , NaOH, KOH, and various other oxidizing and/or reducing agents, as well as organic acids and alkalis that are suitable for reacting or removing the precursor material. 
   The sorbent media for the source chemical solvent, the residual source chemical cleaned from the solvent purge manifold and any byproducts of any reaction between the solvent and the source chemical may comprise zeolites, aluminosilicates, phosphosilicates, carbon, silica, alumina, molecular sieve, carbon molecular sieve, polymeric adsorbents, polyethylene, polypropylene, resin beds, clays, porous ceramics and other media that has a high surface area and has an affinity for such solvent, source chemical and resulting byproducts. Additionally, the sorbent media may comprise a material that renders the solvent and/or the source chemical inert or at least nonflammable when mixed together in the solvent capture ampoule. It is envisioned that various fluorinated and perfluorinated organic or hydrocarbon liquids or solids would be included in such class of sorbent media. Perfluorocarbons, such as; perfluorohexane, perfluoroheptane and mixtures thereof are exemplary of such sorbent media. Additionally, inert compounds such as vacuum pump oils and/or similar low volatility hydrocarbon or fluorocarbon oils may be used. 
   The smaller solvent ampoule consists of a small, approximately 150-250 ml stainless steel ampoule comprising two valves, no level sense and a diptube communicating to the outlet valve. The outlet valves are in two styles, one uses standard manual or pneumatic valves, while the other uses quick disconnect fittings to connect to the solvent purge manifold. The small container is mounted to the larger source chemical container through means of a bracket assembly welded or bolted to the smaller solvent ampoule. This bracket assembly is then bolted onto the chime ring supports or chime ring of the source chemical container. Alternatively, the bracket assembly may also be attached directly to the source chemical container, for example by clamping to the neck of source chemical container, or by attachment with bolts, nuts, clips, clamps or other securing means. The absorbent media is placed into a separate ampoule, and the ampoule is attached either removably (bolted on) or permanently (welded on) to the chime ring or chime ring supports. The bracket assembly may also be attached directly to the source chemical container, for example, by clamping to the neck of he container, or by attachment with bolts, nuts., clips, clamps or other securing devices. The sorbent media ampoule communicates with the solvent ampoule through valves and lines that permit either solvent vapor or solvent liquid to be pushed into the sorbent media ampoule. 
   In the Present Invention, the solvent wash, process chemical and solvent sorption/recovery containers are combined together into a single assembly suitable for shipping and replacing in one piece. This results in a reduced workload for the operator, by not having to replace a separate solvent ampoule; permits the use of fresh, clean solvent with each container replacement; minimizes waste of solvent; and provides the integrated circuit (IC) manufacturer with a mechanism by which he can remove residual quantities of potentially air sensitive or air sensitive, or low vapor pressure process chemicals from their delivery lines. It also eliminates or minimizes the need of the customer to provide any sort of toxic/solvent waste handling requirements. In systems that require separate solvent ampoules, the operator must cycle purge the solvent connections to prevent escape of solvent into the environment; dispose of waste or return a partially filled to filled ampoule of solvent under separate packaging; and must handle an additional vessel in their facility. Therefore, one of the primary benefits of the Present Invention is to reduce handling, increase safety, reduce shipping and waste costs, and confirm that the correct amount of solvent is present to perform the solvent purge task. 
   When a larger volume of solvent material is required to clean the solvent purge manifold, process lines, mass flow controllers, vaporizers and the like, these ampoules may need to be sized so large as to make it impractical to mount integrally to the source chemical container. The present invention also encompasses those systems in which the solvent ampoule and solvent capture ampoule and the source chemical container are physically separate but are capable of being placed into a single cabinet or adjoining cabinets with fluid communication between the various vessels as described in the present invention. 
   With reference to  FIG. 1 , an assembly is shown comprising a high purity source chemical container  10 , a source chemical solvent ampoule  36  and a solvent capture ampoule  30 . The assembly container  10  may be outfitted with a chime ring bracket  18 . The container  10  is outfitted with an outlet  22  and a pneumatic control valve  24 , which dispense high purity liquid source chemical from an attached diptube  12  which extends from the outlet  22  to near or a point adjacent the bottom of the container  10  opposite the outlet  22  at the top or chime ring bracket  20  side of the container  10 . This facilitates removal of high purity liquid source chemical  16 , whose level is typically kept above the diptube  12  and the level sensor  14  which extends to a point slightly above the end of the diptube  12  so that liquid withdrawal can occur after the lowest level signal of the level sensor  14 . The level sensor  14  exits the container  10  through a bung or inlet  42  typically closed by a threaded fitting. The level sensor  14  communicates electrically with an automated control unit or operator to control the valves of the assembly in cooperation with the level of high purity source chemical  16 . 
   High purity source chemical could be withdrawn by vacuum, but preferably, a source of pressurizing inert gas, such as nitrogen or helium. Is connected to pneumatic valve  28 , which controls inlet  26  that communicates with the vapor headspace above the level of the high purity source chemical  16 . The pressurizing gas forces liquid up the diptube  12  for downstream use, such as TEOS used in growing silicon oxide on silicon wafers patterned for integrated circuits in an electronics fab furnace. 
   The high purity source chemical is delivered through a manifold, not shown, to such furnace. During changeout of the container  10 , it is desireable to clean the manifold, and for low vapor pressure chemicals, merely drawing a vacuum or using pressurizing gas can be insufficient. Solvent cleaning is desireable. 
   Solvent compatible to dissolve the high purity source chemical is contained in source chemical solvent ampoule  36 , which is welded  44  to the support arm  18  of the chime ring bracket  20 . The ampoule  36  has an inlet  38  and outlet  40  which operate much the same as the inlet and outlet of the container  10  using pressurizing gas to force solvent out of the outlet  40  by means of the diptube  46 . 
   The solvent passes through the manifold, shown in  FIG. 8 , to remove residual high purity source chemical, which is collected as a waste stream of solvent and chemical in the solvent capture ampoule  30  via inlet  32 . The ampoule  30  is also fitted with an outlet  34  for convenience of regeneration. Ampoule  30  preferably has a diptube  35  connected to outlet  34  to facilitate cleanout of ampoule  30  and to reduce manufacturing parts so that ampoule  30  is interchangeable with ampoule  36 , but it is also contemplated that ampoule  30  would not have a diptube  35  attached to outlet  34 . The ampoule  30  can be an empty receiving ampoule or it can be filled with a sorbent for the solvent and chemical, such as silica. 
   The inlets and outlets of both ampoules can preferably be operated by valves connected to the automated control unit, not illustrated. 
   With reference to  FIG. 2 , common parts are labeled with the same part numbers as FIG.  1  and will not necessarily be repeated in this description of this second embodiment showing the ampoules situated in the interior of the container  10 . The source chemical solvent ampoule  48  has an inlet  50  and an outlet  52  that function similarly to the assembly of  FIG. 1 , with outlet  52  having an integral diptube  54 . Used solvent from ampoule  48  after passing through the manifold, not shown, is recovered in the interiorly situated solvent capture ampoule  56 , which has an inlet  58  and outlet  60 , which operate in a manner consistent with the assembly of FIG.  1 . Outlet  60  may have a diptube  61 , if desired. 
   With reference to  FIG. 3 , common parts are labeled with the same part numbers as FIG.  1  and will not necessarily be repeated in this description of this third embodiment showing a baffled  64  ampoule  62  having discrete solvents  88  and  90  or a solvent in one ampoule  66  and an empty ampoule  68  or sorbent filled ampoule  68 . Either ampoule  66  and  68  could serve either function depending only on connection to the manifold and programming of the automated control unit. Ampoule  68  is outfitted with an inlet  74  and an outlet  72 , the latter of which is integral to a diptube  70  for liquid out service. Pressurizing gas would be administered through inlet  74 . Ampoule  66  being below ampoule  68  has a diptube  76  and  80 , respectively, connected to each of its inlet  78  and outlet  82 . The extent of any diptube or the existence of such a diptube is dependent on whether the ampoule is being used for solvent such as dual solvent delivery or whether it is being use as the solvent capture ampoule, with or without sorbent. The ampoules are welded to the chime ring bracket  20  by welds  84  and  86 . 
   With reference to  FIG. 4 , an alternate embodiment of the assembly is shown. Container  100  comprises chambers  102  and  104  separated by baffle  106 . Each chamber has an inlet and an outlet. For instance, chamber  104  has an inlet  120  controlled by valve  122  and an outlet  118  controlled by valve  116  and ending in a diptube  114  functioning much as described with reference to  FIG. 1. A  level sensor  124  and  126  passes through bung  112  to service each chamber respectively. The lower chamber  102  has an inlet  132  and outlet  136  controlled by valves  134  and  138  respectively. Inlet tube  130  accesses the headspace of chamber  102 , and diptube  128  withdraws liquid source chemical based upon the pressure of the pressurizing gas entering via tube  130 , as described in similar circumstance with regard to FIG.  1 . This allows for several source chemicals to be transported and contained in one assembly. Although the ampoules for solvent and solvent capture are not illustrated, it is appreciated that the same configuration of ampoules can be used with container  100  as is described for  FIGS. 1-3 . 
   With reference to  FIG. 5 , one  140  of two mating sections of an ampoule bracket is shown. Ampoule bracket section  140  fits around the assembly bung  42  ( FIG. 1 ) and clamps by friction fit the outer edge of bung  42  by turning bolts which threadably engage engagement holes  148 . Edge  146  interfaces with the bung  42 . The source chemical solvent ampoule  36  ( FIG. 1 ) and the solvent capture ampoule  30  ( FIG. 1 ) fit into either of holders  142  and  144  which frictionally engage the ampoules by threaded engagement holes  150  and  152  using bolts, not illustrated. The ampoules rest on support surfaces  154  and  156 . 
   With reference to  FIGS. 6A and B , a source chemical solvent ampoule  158  is shown in greater detail. The ampoule  158  has inlet  164  and outlet  162  connected to diptube  160 . This allows liquid solvent to be removed, generally from level  166 , full, to level  168 , empty. 
   A perspective view of the assembly of the Present Invention is shown in FIG.  7 . Container  170  has ampoule bracket sections  174  and  176  holding ampoules  178  and  188 . Each ampoule has an inlet  180  and  190  and one outlet  184  and  192 , respectively. These are connected to quick disconnect fittings  194 ,  196 ,  186  and  182 , respectively. Container inlet  202  is controlled by pneumatic valve  204 . Container outlet  200  is controlled by pneumatic valve  198 . These components are generally protected by the chime ring bracket  172 . An optional level sense can be fitted through bung  206 . 
   With reference to  FIG. 8 , the manifold  214  in which the present invention&#39;s assembly operates and communicates is depicted. Source chemical solvent ampoule  208  is communicating with the solvent purge manifold  252  of high purity source chemical container  210  and solvent capture ampoule  212 . It is also contemplated that this manifold connection can be made with ampoules internally positioned in the container  210 . The solvent in ampoule  208  can either be under pressure from filling or can be pressurized by an inert push or carrier gas  222  introduced through valve  216  to inlet  230  to force solvent up through diptube  228  to outlet  226  and through valve  220 . Refill of the ampoule  208  can be accomplished through inlet  232  controlled by valve  218  in receiving fresh or recycled solvent  224 . Solvent from ampoule  208  passes through line  238  and valves  240  and  246  to clean the solvent purge manifold  252  which is defined by valves  246 ,  250 ,  266  and  254 . Vacuum can be applied to line  238  particularly during cleanout through valve  234  and vacuum source  236 . Additionally, inert purge gas can be administered from source  242  and valve  244  to clean out line  238 . High purity source chemical in container  210  is pushed out of diptube  260  by an inert push gas source  258  controlled by valve  256  communicating with container  210  through inlet  264 . An additional fill inlet to replenish source chemical is contemplated but not illustrated. Source chemical passes through valve  254  to solvent purge manifold  252  and through valve  250  to a point of use  248  or end use, such as an electronics fabrication process tool to make integrated circuits or computer chips. During clean out of the solvent purge manifold  252 , solvent is cycled through the manifold  252  from valve  246  through valve  266  by the force of the solvent&#39;s pressure or push gas or the vacuum that may exist in capture ampoule  212 . This forces solvent, residual source chemical or any decomposition products, if the solvent is reactive with the source chemical, to pass through line  268 , line  270 , valve  272 , inlet  274  and capture ampoule  212  which may be empty or it may contain a sorption media. The solvent capture is activated potentially by vacuum drawn on ampoule  212  through outlet  276 , valve  278 , lines  280  and  284  toward a source of vacuum  286 . That source may contain abatement or appropriate traps for various contemplated chemicals and solvents. Alternately, vacuum can be bypassed around ampoule  212  by opening valve  282  and closing valves  272  and  278 . It is contemplated that capture ampoule  212  does not need to be connected to a vacuum source  286 , but can rely on vacuum conditions pre-established in ampoule  212  in a sealed fashion upon manufacture or refilling or refurbishing, or reliance can be made on the pressurized solvent to move the chemicals to ampoule  212  with or without venting through line  284 . 
   The Present Invention provides a significant advantage in the use of high purity chemicals in a delivery system, such as in the electronics fabrication industry. Maintenance of the high purity of the source chemical requires not only the purity of the source chemical, but also the delivery system through which the chemical is dispensed. Traditionally, the industry has used multiple cycles of vacuum and purging with an inert pressurized gas to maintain cleanliness of the delivery system. However, with low volatility chemicals, such cyclic cleaning is not sufficient. Solvents for such low volatility chemicals are desirable. The Present Invention provides a unique system for providing such solvents and their disposal without adversely effecting the traditional way in which operators in the electronic fabrication industry utilize containers of source chemicals. This provides essentially a seamless system for providing ultra cleanliness for even difficult source chemicals, such as low volatility chemicals and overcomes a long standing problem of sustaining purity of source chemicals through process lines and changeout of containers of such source chemicals and sequential use of different source chemicals in the same delivery system. 
   The present invention has been set forth with regard to several preferred embodiments, but the full scope of the invention should be ascertained from claims which follow.