Abstract:
A method for controlling the delivery of vapor from a bubbler containing a supply of chemical fluid through which a carrier gas is bubbled and from which bubbler vapors are delivered in a vapor stream entrained with the carrier gas. In general, the method involves equilibrating the pressure within the head space to that of the chemical fluid fill line to maintain a constant fluid level based on pressure and not relying on conventional level sensors and controllers.

Description:
RELATED APPLICATIONS 
   The present application is a division of U.S. patent application Ser. No. 10/663,123 filed on Sep. 16, 2003 entitled “Liquid Vapor Delivery System and Method of Maintaining a Constant Level of Fluid Therein,” which claims priority to U.S. Provisional Application No. 60/411,026 filed on Sep. 16, 2002, both of which are incorporated herein by reference in its entirety. 

   BACKGROUND OF THE INVENTION 
   1. Field of the Invention 
   This invention relates to liquid vapor delivery systems of the type employing bubblers and to methods of maintaining constant levels of reagent within bubblers. 
   2. Description of the State of Art 
   The semiconductor industry is very dependent upon sources of ultrahigh purity reagents. Other industries also have high purity requirements, but few compare with the purity requirements in the semiconductor industry. Liquid vapor delivery systems are used in a number of manufacturing processes. For example, liquid vapor delivery systems are used in the manufacture of optical wave-guides. Such systems are described in U.S. Pat. Nos. 3,826,560; 4,235,829; and 4,276,243, the disclosures of which are incorporated herein by reference. Thin films are sometimes produced by liquid vapor delivery system technology, see HANDBOOK OF THIN FILM TECHNOLOGY, Maissel and Glang, McGraw-Hill, N.Y. 1970. Film deposition techniques are generally described, as applicable to the semiconductor industry, in ENCYCLOPEDIA OF SEMICONDUCTOR TECHNOLOGY, Grayson (Ed) John Wiley, New York, 1984. 
   With particular application to the manufacture of semiconductor films and devices, it is known to provide semiconductor devices by reacting a silicon wafer, appropriately prepared with the semiconductor component pattern thereon, with the vapor from chemical liquid vapor source materials or dopants. Among these chemical vapor source materials are boron tribromide, phosphorous oxychloride, phosphorous tribromide, silicon tetrachloride, dichlorosilane, silicon tetrabromide, arsenic trichloride, arsenic tribromide, antimony pentachloride and various combinations of these. In the compound semiconductor industry, epitaxial III–V semiconductor films are commonly grown by metalorganic chemical vapor deposition (MOCVD) using liquid vapor source materials such as trimethylgallium, triethylgallium, trimethylaluminum, ethyldimethylindium, tertiary-butylarsine, tertiary-butylphosphine, and other liquid sources. Many II–VI compound semiconductor films are also fabricated using liquid sources. 
   A common technique used in vapor generating systems for delivering chemical vapor to a process chamber is to force a carrier gas to bubble through a chemical fluid in a bubbler and then deliver the resulting vapor from the bubbler to the process chamber. Traditional bubblers, including those utilized in presently available automatic refill systems, rely on relatively large fluid volumes to intrinsically compensate for deviations in fluid level which can negatively effect the resulting vapor concentration. Since vapor sources in the fiber optics and semiconductor industries are often hazardous fluids, there has been an increasing focus on the occupational safety and health concerns resulting from use of such fluids. This has resulted in reducing the maximum allowable volumes of many of these fluids within the work place. It is therefore desirable to reduce the required fluid volume at the point of vapor generation without compromising vapor concentration control. 
   Those familiar in the art recognize that absolute values of vapor delivered are not the prime importance, but the consistency of the vapor concentration is of utmost importance. Hence the value of source material delivered per unit of time is more important than source material delivered per unit of carrier gas. Therefore, temperature and carrier gas residence time (liquid level) become the prime variables in determining consistency. 
   Typically a bubbler container is comprised of a single vessel, which holds an expendable volume of vaporizable fluid. A carrier gas such as hydrogen, oxygen, argon, helium or nitrogen is introduced at the lower level of a fluid column, travels up through, and exits the fluid surface into a headspace. As the carrier gas passes through the fluid column it becomes entrained with vapor, which results in a corresponding reduction of the fluid volume. In some applications such decreases in the level of liquid within the bubbler would have little effect. In other applications, however, such as in vapor deposition procedures employed in constructing semiconductors and optical fiber preforms, significant variations in the level of liquid have a pronounced adverse effect. This is attributable to the fact that the rate of vaporization is not solely dependent upon the surface area of liquid within the bubbler which area can, of course, be maintained constant as by the use of cylindrically shaped vessels. The vaporization rate here however is also dependent upon several other factors including the flow characteristics of carrier gas bubbled through the liquid. For example, the size of the bubbles as they rise through the liquid has an effect on the rate of vaporization. The rate of flow of the carrier gas introduced into the bubbler itself has another effect on the rate of vaporization as also does the rise time of the bubbles, which, of course, depends on the depth at which they are introduced. The rate of heat transfer into the bubbler will also be affected by changes in the level of liquid. While theoretically possible to program a heat controller to account for these variables as changes in the level of liquid are continuously monitored, that approach is complex and fails to eliminate the need for some degree of level control to prevent complete depletion or flooding. Vaporization rate also defines the headspace present above and within the bubbler container, which has been found to negatively effect the vapor concentration and ultimate bubbler performance when not optimized. 
   Inasmuch as vapor extraction from a fluid volume results in depleting the fluid volume of a bubbler, causing variations in vapor concentration, a means of replenishing this fluid is desirable. Some methods include manually replacing the bubbler ampoule once the volume of fluid reaches a predetermined minimum acceptable level. Other manual methods rely on an auxiliary supply of fluid to replenish the bubbler during intermittent periods of non-use. These systems rely on weight scales, sight glasses, ultra sonic detection, infrared or mechanical float systems. All of which have serious drawbacks. Such methods can result in reducing many of the concerns associated with prior art expendable bubblers, such as reducing the risk of contamination during ampoule replacement or any necessary fluid replenishment, but create a host of potential problems including metal fatigue, sealing of dissimilar materials, and need for calibration procedures. With many of the advanced processes running short cycle times, the opportunity to refill the liquid level must be very fast and accurate, typically less than 20 cc&#39;s of source material. 
   In addition to manual replenishment of fluid, automatic bubbler refill systems are also available. However, such systems typically employ float coupled electronic devices, such as level controllers, to control the replenishment of fluid in the bubbler. Such devices are prone to failure, or inaccuracies and are generally the most common failure mechanism in the system. Other types of fluid level sensors such as optical, load cell monitoring of the contents, and resistance probes have been employed. However, the use of such devices can be costly, prone to error, and with many of the fluids being flammable, represent ignition sources if not properly rated and maintained. The corrosive and toxic nature of the materials commonly encountered greatly limits the materials and construction of sensors used in these demanding applications. 
   U.S. Pat. No. 4,235,829, which issued on Nov. 25, 1980 to Fred P. Partus is noted. In it, there is shown a liquid vapor delivery system, which comprises a deposition bubbler adapted to generate and to deliver vapor from a liquid contained therein and in a reservoir in fluid communication with the bubbler. Facilities are provided for sensing the level of the liquid contained within the bubbler and for providing gaseous head pressures in the reservoir of magnitudes dependent upon the sensed liquid level. The liquid level in the bubbler drops as liquid is vaporized and withdrawn from the bubbler whereupon the level is adjusted by increasing the pressure head in the reservoir to feed liquid to the bubbler. Although the system works well, perturbations in the deposition bubbler caused by a drop in liquid level and then a rise due to the changing of the pressure in the reservoir can to an extent affect adversely the rate of vaporization and hence the concentration level of the vapor. These level changes are increased as the rate of deposition and hence the rates of withdrawal of vapor are increased. 
   Additionally, commonly assigned U.S. Pat. No. 4,276,243, which issued on Jun. 30, 1981 to Fred P. Partus, discloses a similar liquid vapor delivery system, which utilizes the temperature of the liquid as the characteristic to be monitored and manipulated to control the concentration level at the desired value. However, while this system is effective, the slow rate at which the overall temperature of the liquid can be changed, particularly cooled, often results in an unwanted delay in achieving the desired concentration level corrections. 
   Accordingly, it is to the task of maintaining a substantial constant level of liquid within a bubbler while vapors from the liquid are being continuously or intermittently withdrawn to which the present invention is generally directed. More particularly, the invention is directed to level control systems and methods for use in vaporizing highly corrosive liquids which may easily become contaminated if brought into direct contact with materials of the type used in conventional level controllers such as floats and the like. 
   SUMMARY OF THE INVENTION 
   The foregoing problems have been overcome by the method and system of the present invention. In accordance with the present invention, a method and system is described for controlling the delivery of vapor from a bubbler containing a supply of chemical fluid or reagent through which a carrier gas is bubbled and from which bubbler vapors are delivered in a vapor stream entrained with the carrier gas. In general, the present invention involves adjusting the pressure within the headspace of the bubbler to that of the chemical fluid level line, thus creating a repeatable fluid level based on pressure and fluid dynamics and not relying on conventional level sensors and controllers. 
   In one form of the invention a liquid vapor delivery system is provided which comprises a bubbler adapted to generate and to deliver vapors from a vaporizable chemical fluid contained therein, and a reservoir in fluid communication with the bubbler from which liquid may be appropriately fed into the bubbler to replenish liquid vaporized within and withdrawn from the bubbler. The system further comprises means for equilibrating the pressure within the headspace of the bubbler to that of the pressure within the liquid source tube connected to the bulk supply reservoir. 
   In another form of the invention, the bubbler floor is adapted to drain all liquid or reagents out of the bubbler through the liquid source line thus allowing for ease in cleaning. 
   Additional objects, advantages, and novel features of this invention shall be set forth in part in the description and examples that follow, and in part will become apparent to those skilled in the art upon examination of the following or may be learned by the practice of the invention. The objects and the advantages of the invention may be realized and attained by means of the instrumentalities and in combinations particularly pointed out in the appended claims. 

   
     BRIEF DESCRIPTION OF THE DRAWINGS 
     The accompanying drawings, which are incorporated in and form a part of the specifications, illustrate the preferred embodiments of the present invention, and together with the description serve to explain the principles of the invention. 
     In the Drawings: 
       FIG. 1  is a schematic diagram of a preferred embodiment of a liquid vapor delivery system embodying the principles of this invention; and 
       FIG. 2  is a schematic diagram of the top plan view of the modular fluid-handling unit used in the liquid vapor delivery system of this invention. 
   

   DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT 
   The liquid vapor delivery system  10  according to the present invention is best seen in  FIG. 1 . The liquid vapor delivery system  10  is designed to provide a vapor stream of an easily vaporizable liquid or reagent  38  which is contained in a reservoir  94  and in a bubbler  12 . In general, the present invention involves adjusting the pressure within the headspace of bubbler  12  to that of the chemical fluid level line  37 , thus creating a repeatable fluid level based on pressure and fluid dynamics and not relying on conventional level sensors and controllers. This is accomplished in two stages. During the first stage, all inlets and outlets of the bubbler  12  are set in a closed position except valves  102 ,  104  and  106 . To begin the refill cycle, valves  120  and  110  are then opened to initiate the flow of liquid  38  from liquid source  94  to the bubbler  12 . The system, during the refill cycle, allows over-filling of the liquid level  38  in bubbler  12  to a level controlled by the pressure of the liquid delivery conduit  19 , thereby compressing the volume of vapor in bubbler  12  and creating a pressure approximating the liquid source line  19 . Construction and placement of vapor extraction tube  28  prevents liquid from being forced into it. During the second stage, valve  110  is closed, pressure supply is removed from the liquid source  94 , and valve  124  is opened forcing excess liquid through liquid level set tube  37  back to bulk liquid source  94 . 
   Liquid delivery system  10  can be essentially viewed as having two major components, bubbler  12  and conduits system  90 . When compared to traditional bubblers, bubbler  12  constitutes an upside down design in that all of the gas and liquid conduits that communicate with bubbler  12  are attached to bubbler floor  14 . This design arrangement of bubbler  12  led to an unexpected capability of cleaning bubbler  12  in-situ. Bubbler floor  14  is designed so that the lowest point occurs at opening  21  which is attached to liquid source line or conduit  19 . Thus, bubbler  12  can be readily cleaned in-situ without removing, disassembly, or contamination to the atmosphere. Cleaning is simply accomplished by closing all valves except valves  110 ,  128  and  130 . Vacuum generator  136  is actuated and reagent  38  is withdrawn through vent  152 . Alternatively valve  132  may be opened to withdraw reagent  38 . Valves  128  and  130  are then closed and a cleaning solvent (not shown) can be attached to conduit  19 , in place of reservoir  94 , and cleaning solvent may then be introduced into bubbler  12 . Once cleaned, the cleaning solvent is then withdrawn from bubbler  12  as discussed previously in the case of reagent  38 . Conduit system  90  essentially comprises a liquid source line  19 , vapor stream conduit  26 , level set line  37  and carrier gas conduit  92  all of which allow for fluid communication between bubbler  12  and carrier gas source  98 , liquid reagent source reservoir  94  and a vacuum system that comprises a vacuum generator  138 , purge gas supply  96 , vacuum generator supply  100  and vent  152 . It will be readily apparent to one of skill in the art that conduit system  90  would take on many permutations by simply changing the configuration of the valves consequently  FIG. 1  is exemplary of one configuration That will accomplish the methods of the present invention. 
   As discussed previously, bubbler  12  communicates with a fluid reagent source reservoir  94  by way of conduit  19 . Reservoir  94  is designed to maintain a large supply of ultrahigh purity chemical reagent  38  which is used to periodically replenish bubbler  12 , preferably after every run. Reservoir  94  may simply be in the form of a carboy, but it will be understood that specially designed refill reservoirs may be required. Any kind of reservoir  94  which is chemically inert to the contained reagent  38 , and which can be suitably connected to a conduit system for carrying reagent  38  to bubbler  12  may be used. Carrier gas intake conduit  92  extends from a source of pressurized carrier gas  98  into a flow controller unit  114 . After passing through the flow controller unit  114  conduit  92  is directed into bubbler  12  terminating with a lower outlet or orifice  24  located in the bottom of bubbler  12 . A vapor stream conduit  26  extends downwardly from a u-shaped neck intake orifice  28 , located in the headspace  30  in the top of bubbler  12 , through a number pneumatic valves to the process tool  154 . Level set line  37  is placed within bubbler  12  so that excesses reagent  30  can be dismissed from bubbler  12  as the head pressure is set. Furthermore, level set line  37  is adapted so that its height within bubbler  12  can be adjusted thus allowing one to set the depth of reagent  38 . 
   A typical operation of the system  10  is now described as merely exemplary of the invention. It will be understood that the precise sequence and mode of operation may vary somewhat, depending upon the type of treatment zoned or furnace, which is being fed, and upon the kind of product being produced. Thus, the following description is merely exemplary. 
   Considering the invention as designed to provide a stream of carrier gas  98 , which is either, saturated or partially saturated with reagent  38  to a processing tool  154 , the overall flow of gases and fluids will be as described. Taking the system  10  at an equilibrium operating state, with the processing tool  154  in operation, the flow of gases is as follows. Carrier gas  98  which may be an inert gas, such as and but not limited to argon, helium, oxygen, nitrogen or hydrogen is contained within a cylinder from which it flows through conduit system  92  thereby being introduced through orifice  24  into reagent  38  contained within bubbler  12 . Bubbler  12  includes a heater/chiller  16  which for example may be a strap heater that is jacketed about an outer surface of bubbler  12 . The heater/chiller  16  is used to provide energy to increase or decrease the temperature and to vaporize reagent  38  in bubbler  12 . 
   As carrier gas  98  travels up through reagent  38 , it becomes either saturated, or partially saturated, depending upon the rate of flow, the depth of reagent  38 , the temperature, etc., with reagent  38 . Reagent-ladened gas  40  then flows into headspace  30  and out vapor stream conduit  26 , which is connected to process tool  154 . Vapor stream conduit  26  is u-shaped so that as gas bubbles  40  break the surface  36  of reagent  38  splattered fluids will not drop down into inlet tube  26 . There may be provided, in addition to this gas flow, other streams. For example, other streams of inert gas, or reactive gas, or reagents, may also be provided. These are not part of this invention, however, and would be provided separately and independently of this invention, depending upon the precise reaction that was desired to be carried out. 
   The system, as thus described, may be considered the equilibrium system During the period of time process tool  154  is in a deposition mode, the reagent-laden gas  40  is being provided to processing tool  154 , and the fluid level  36  is decreasing an extremely small percentage of total bubbler volume. Consequently, after each run the refill cycle is activated. As discussed previously all inlets and outlets of bubbler  12 , as shown in  FIG. 1 , are switched into a closed position except valves  102 ,  104  and  106 . To begin the refill cycle, valves  120  and  110  are then opened to initiate the flow of reagent  38  from reservoir  94  to bubbler  12 . Alternatively, valves  120  and  122  or  124  may be opened to fill bubbler  12 . The system, during refill cycle, allows over-filling of the liquid level in bubbler  12  to a level controlled by the pressure of the liquid delivery conduit  19 , thereby compressing the volume of vapor in the bubbler and creating a pressure approximating the liquid source line  19 . Construction and placement of vapor extraction tube  28  prevents liquid from being forced into it. During the second stage, valve  110  is closed, pressure supply is removed from reservoir  94 , and valve  124  is opened forcing excess liquid within bubbler  12  out through fluid level set line  37  back to bulk liquid source  94 . The length of the refill cycle is thus dependent on the total bubbler volume. During filling sequence, pressure in the head space  30  is dependent upon the pressure of conduit  19 , reagent  38  will automatically flow from reservoir  94  into bubbler  12  until the pressure in head space  30  equilibrates with that of conduit  19 . Thus the level of reagent  38  in bubbler  12  is replenished to an overfilled state, in preparation for the leveling sequence described earlier. 
   Once the liquid pressure in bubbler  12  reaches an equilibrium state, a valve is closed to liquid flow, and is opened to gas flow, thus flushing out of the conduit system all of the liquid reagent. This provides important safety protection, since the liquid is maintained in the conduit system  90  only during the refill cycle, and, also, minimizes contamination since the reagent is not held in the conduit system, which has large surface area exposure. The conduit system  90  is maintained at a positive pressure with inert gas. Because the principle of operation works on pressure differences, not absolute pressures we can easily deliver very low pressure fluids and much higher pressure condensed fluids. The absolute vapor pressure of the fluid we are trying to deliver is not as critical as it is in other conventional bubblers. 
   Once bubbler  12  is refilled, the valve returns to its operating position. Inert gas from conduit  92  flows through the inlet bubbler tube  24 , through the outlet tube  26  and to processing tool  154  as previously described. 
   In a highly unique and novel arrangement, the system includes means including a conduit system  90  for transferring vapor or liquid reagent  38  during a first time period from the refill reservoir  94  through the conduit system  90  into the bubbler  12 , flushing reagent  38  out of the conduit system  90 , filling the conduit system  90  with inert gas, and maintaining a predetermined pressure of inert gas in said conduit system  90  between the periodic transfer of reagent  38  there through, a substantially gas tight enclosure for the refill reservoir  94  and means for providing inert gas  98  at a predetermined pressure to the enclosure to maintain the refill reservoir in an inert atmosphere, and may also include means for providing inert gas  98  at a predetermined pressure and rate to the refill reservoir, and means for feeding a stream of inert gas into bubbler  12  to be at least partially saturated with chemical fluid only during a second time period, the first and second time periods alternating with time. 
   In the embodiment shown in  FIG. 1 , optional heater/chiller  16  may be added to control the temperature of the liquid in the supply and deposition bubbler  12 , respectively, to vaporize liquid therein. 
   A modular fluid handling assembly, shown in  FIG. 2  and similar to that disclosed in U.S. Pat. No. 6,298,881 which is incorporated herein by reference, includes a plurality of fluid handling units. Each fluid handling unit includes a fluid passage and associated port, a vacuum passage and associated port, a vacuum pressure source, and a containment seal. The fluid passage ports and vacuum passage ports of adjacent fluid handling units respectively communicate. The containment seal is disposed between adjacent fluid handling units and surrounds the communicating fluid passage ports and vacuum passage ports. The vacuum pressure source is in continuous communication with the vacuum passages of the fluid handling units, generates an urging force, which aids in sealing adjacent fluid handling units together, and draws off any fluid that may leak from a fluid passage port. A sensor can be tapped into the vacuum line to sense whether any fluid has leaked from a fluid passage port. 
   It is to be understood with respect to the enclosed conduit system, which comprises both the conduit and valving enclosed in suitable gas tight, or substantially gas tight enclosure mechanisms, and filled with inert gas, that the specific configuration, construction and operation of the valve is of secondary significance, and any valve may be used. What is significant is that the entire conduit system, or a substantial portion of the conduit portion, sufficient to protect the conduit system and prevent contamination through the walls of the conduit system, is enclosed in one or more envelopes filled with inert gas. 
   The foregoing description is considered as illustrative only of the principles of the invention. The words “comprise,” “comprising,” “include,” “including,” and “includes” when used in this specification and in the following claims are intended to specify the presence of one or more stated features, integers, components, or steps, but they do not preclude the presence or addition of one or more other features, integers, components, steps, or groups thereof. Furthermore, since a number of modifications and changes will readily occur to those skilled in the art, it is not desired to limit the invention to the exact construction and process shown described above. Accordingly, all suitable modifications and equivalents may be resorted to falling within the scope of the invention as defined by the claims, which follow.