Abstract:
A mechanical seal system for a pump or other rotary shaft equipment has three, four, five or more mechanical seals installed in and about the seal chamber, replacing and improving upon the conventional or cartridge, single, double, dual or tandem mechanical seal arrangements. In embodiments, a plurality of barrier liquids and/or barrier gases are provided separately to the seal faces.

Description:
BACKGROUND OF THE INVENTION 
       [0001]    1. Field of the Invention 
         [0002]    The invention is in the field of mechanical seal technology. In particular, the invention is directed to a mechanical seal system having three, four or five mechanical seals adapted to be used with rotating shaft equipment to prevent leakage. 
         [0003]    2. Description of the Related Art 
         [0004]    Mechanical seals are widely used to prevent leakage in rotary shaft equipment, such as pumps, mixers, agitators, and compressors, in which a rotating shaft passes through an opening in the housing of the equipment. This type of equipment is characterized by a housing in which process fluid is maintained at pressure and therefore prone to leakage where the shaft enters the housing. The mechanical seals are housed in a seal chamber bolted to the face of the pump housing. 
         [0005]    A mechanical seal is characterized by a rotating sealing face, a stationary sealing face and a loading mechanism such as a spring, coil or bellows maintaining the sealing faces compressed against each other. The sealing faces are machined smooth—such that surface roughness often may not exceed 2 millionths of an inch. Mechanical seal manufacturers often provide installation parameters which specify the position where an individual seal on the shaft or shaft sleeve must be installed to maintain the proper spring loading tension and proper force on the delicate sealing faces to prevent leakage. The seal system is also provided with secondary seals, such as O-rings, gaskets, wedges, sealing rings and the like compressed around the primary sealing faces to close off secondary leakage paths around the sealing faces. 
         [0006]    The mechanical seal systems in use today are single seal and dual seal systems. A dual seal system typically includes two seal assemblies mounted on a shaft with a barrier fluid filling a space between them. Thus, the upstream (most inboard) seal is situated between the process fluid and the barrier fluid. And the downstream seal (most outboard) is between the barrier fluid and the atmosphere. The barrier fluid is maintained at a higher pressure so as to maintain a positive flow of clean barrier fluid across the downstream seal faces, while the upstream seal is lubricated by both the barrier fluid and the process fluid. The barrier fluid is used where the process fluid is corrosive or abrasive and likely to damage the sealing faces over time. Examples of dual seal systems are disclosed in U.S. Pat. No. 4,290,611 to Sedy, which is incorporated by reference in its entirety. 
         [0007]    Another type of barrier system is a gas barrier. In these systems, a suitable gas (such as nitrogen) under pressure is used to prevent seepage of process fluid through the mechanical seal to the atmosphere. It is known in the gas barrier systems to provide a sealing face with spiral grooves, such that as an inert barrier gas is provided between the seals, and as the shaft rotates, gas flows into the grooves and creates an opening force between the sealing faces. This force causes the sealing faces to separate a few thousandths of an inch. As a result of reduced or eliminated contact between the sealing faces, wear is reduced and the need to cool the sealing faces is largely eliminated while maintaining the same or better leakage prevention as a “wet barrier seal.” Gas flow to the seal faces is regulated with a gas panel—the barrier gas circulates through the system at a measured pressure and flow rate and ultimately is vented to the process or atmosphere. A gas barrier system having a sealing face with a spiral groove is disclosed in U.S. Pat. No. 5,375,853 to Wasser, et al., which is incorporated by reference for this purpose. 
         [0008]    Staged seal assemblies for extreme duty applications are also known, such as described in U.S. Pat. No. 3,360,272 to Blom and U.S. Pat. No. 7,300,060 to Zagres, which are incorporated by reference. These assemblies are characterized by having a plurality of staged seals disposed in series along a shaft, each provided with a seal bypass. The seal bypass is configured to direct a portion of fluid through a pressure breakdown device around the respective seal. This diversion of process fluid reduces the severity of the duty requirement on each seal. 
         [0009]    U.S. Pat. No. 5,901,965 to Ringer et al. is incorporated by reference for its description of bellows and seal ring construction, which is known in the art. The Ringer et al. patent discloses an improvement on a conventional bellows seal, including a stationary seal ring fitted against a stationary seal ring shell and a bellows attached to the side of the seal ring shell opposite the seal ring, in which undesired stresses on the seal ring and seal ring shell are avoided by decoupling the seal ring and the seal ring shell and using a seal element between the seal ring shell and the seal ring to balance load. 
         [0010]    One object of the invention is to increase the service life of a mechanical seal system and reduce or eliminate leakage of process or barrier fluid from the equipment housing. 
         [0011]    A further object of the invention is to provide a mechanical seal system with three or more mechanical seals that fits existing standard pumps, mixers and other rotating shaft equipment without modification. 
         [0012]    A further object of the invention is to provide a mechanical seal system with three, four, five or more mechanical seals which is not a pressure staging system and which does not include a pressure reducing flow path between upstream and downstream seals. 
         [0013]    A further object of the invention is to provide a mechanical seal system with extended operational life using individual seals having relatively low pressure rating to accommodate the application. 
         [0014]    A further object of the invention is to provide a mechanical seal system having a plurality of barrier fluid sources each providing the same or different barrier fluid to a plurality of seal faces via different fluid pathways. In embodiments, a gas barrier may be used in combination with a liquid barrier fluid. 
       SUMMARY OF THE INVENTION 
       [0015]    In one aspect, the invention is a three-seal mechanical seal system for containing a fluid in rotary shaft equipment. The mechanical seal system comprises three seals, two inboard of the seal gland and one outboard. The inboard seals comprise: (1) a first rotating seal face, a first stationary seal face, and a first biasing member urging the first rotating seal face toward the first stationary seal face; and (2) a second rotating seal face downstream of the first rotating seal face, a second stationary seal face, and a second biasing member urging the second rotating seal face toward the second stationary seal face. A seal chamber surrounds the rotating shaft and has an opening at an upstream end thereof where the rotating shaft enters the stationary housing. An axial end wall of the seal chamber is formed by the seal gland, which has an opening for the rotating shaft at the downstream end. The outboard seal comprises (3) a third rotating seal face downstream of the first and second rotating seal faces, a third stationary seal face, and a third biasing member urging the third rotating seal face toward the third stationary seal face. The third rotating seal face, third stationary seal face, and third biasing member are located outboard of and integrated with the seal gland. 
         [0016]    In another aspect, the invention is a four seal mechanical seal system which includes all of the seals in the three-seal system and further includes an additional upstream seal comprising a fourth rotating seal face, a fourth stationary seal face and a fourth biasing member urging the fourth rotating seal face toward the fourth stationary seal face. 
         [0017]    The invention also contemplates a five-seal mechanical seal system which includes all of the seals in the four-seal system and further includes an additional upstream seal comprising a fifth rotating seal face, a fifth stationary seal face and a fifth biasing member urging the fifth rotating seal face toward the fifth stationary seal face. 
         [0018]    In a further aspect of the invention, the three, four or five-seal mechanical seal system according to the invention, may be provided as a cartridge in which the first, second and third rotating and stationary seal faces are pre-mounted on a sleeve, which is attached to the shaft with a drive collar and set screw. The sleeve is attached to the seal gland so that the sleeve is installed over the shaft and the seal gland is attached to the seal chamber with the first, second and third stationary seal faces and associated rotating seal faces and biasing members being positioned in predetermined axial spacing on the shaft upon installation. 
         [0019]    In a further aspect of the invention, a plurality of barrier fluid sources (i.e., at least two separate barrier fluids) are provided separately to the mechanical seal faces, and may comprise a combination of gas barrier and liquid barrier fluid. As used herein, the term “barrier fluid” encompasses both a liquid barrier fluid and a gas barrier. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0020]      FIG. 1  depicts a three-seal mechanical seal system according to the invention. 
           [0021]      FIG. 2  depicts a four-seal mechanical seal system according to the invention. 
           [0022]      FIG. 3  depicts a five-seal mechanical seal cartridge system according to the invention. 
           [0023]      FIG. 4  depicts bellows for use with a mechanical seal according to the invention. 
           [0024]      FIG. 5  depicts a seal face according to an embodiment of the invention employing a bidirectional cross groove design. 
       
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
       [0025]    The mechanical seal systems of the invention comprise three, four, five, or more mechanical seals installed around a rotating shaft. A “mechanical seal” as used herein means a seal having a rotating sealing face, a stationary sealing face and a loading mechanism including, but not limited to, a spring, coil or bellows maintaining the sealing faces compressed against each other. In the case where a gas barrier is used, some small separation between the seal faces may be maintained by the gas barrier, as described below. The systems may be used with pumps (centrifugal and positive displacement), compressors, mixers, and agitators, or any number of rotating equipment types with a rotating shaft—all of which are characterized by a process fluid contained within a housing under pressure. As used herein, “upstream” is the direction toward the higher pressure pressure in the housing and “downstream” is the opposite direction along the shaft away from the housing. 
         [0026]    The mechanical seal systems of the invention may be installed as a cartridge system or as a component system. As used herein, a “component system” means that individual mechanical seals are mounted inside or outside a seal chamber provided with the equipment, as specified by the design. A “cartridge system” means that the mechanical seals of the system are preinstalled with mounting hardware, including a sleeve and gland plate which are mounted to the shaft. In this way the axial alignment of the seals in the system is ensured upon installation. Each mechanical seal according to the present invention closes off the respective portion of the seal chamber, and a pressure reducing flow path between upstream and downstream seals is not provided. 
         [0027]    The space in which mechanical seals are provided is referred to as the “stuffing box” or “seal chamber,” which is the area surrounding the shaft between the motor and the pump&#39;s volute housing. The seal chamber is defined by the volute pump housing at one end, a seal chamber wall bolted to and extending from the pump housing, and a seal gland at the opposite end, where the shaft enters the seal chamber. As used herein, “inboard” means inside the seal gland or in a direction toward the pump housing, and “outboard” means outside the seal gland or in a direction away from the pump housing toward the atmosphere and motor. The “outboard” mechanical seal of the invention is integrated with the gland plate. 
         [0028]    In practice, the ability to modify or re-design the seal chamber space is quite limited. In preferred embodiments, seal systems according to the invention are compatible with International Organization for Standardization (“ISO”) pump standards, Deutsches Institut für Normung (“DIN”) pump standards, American National Standards Institute (“ANSI”) pump standards and/or American Petroleum Institute (“API”) pump standards. These standards typically specify the size, position, and distance above the ground of a pump flange, pump foot print, the distance above the ground of the shaft, and the length of the shaft from the motor gear box to the housing. These standards are provided so that equipment from different manufacturers may be integrated with existing piping and floor plans. As the pump size increases, the standard specifications change also. API standards, directed to more demanding applications, may add to the ANSI specifications: requiring a thicker shaft, or bearing isolation in place of a radial seal. ANSI standards are relevant herein because the person of ordinary skill in the art recognizes the limited space available to install three, four, five or more seals in a seal chamber of specified ANSI pump dimensions. Reference herein to ANSI or API specifications or any individual ANSI or API specification refers to the specification in current use on the filing date hereof. 
         [0029]    A “process fluid” is the fluid being pumped, mixed or compressed by the rotating shaft&#39;s impeller, propeller, mixing blade, wheels, buckets, or other pieces of equipment, which may be a liquid, gas or slurry at the process temperature. A “barrier fluid” is a circulating fluid different from the process fluid, inert or less toxic and damaging to people, environment and the equipment than the process fluid, which is also provided to lubricate the non-process seal faces (i.e. all seal faces downstream of the first seal face contacting the process fluid.) Barrier fluid is typically maintained at a pressure greater than the process fluid to impede migration of process fluid past the seal faces and may be gas or liquid. In a very few cases, the barrier fluid or gas is at a lower pressure then the process fluid—usually in instances where barrier fluid contamination of the process fluid is unacceptable for various reasons. 
         [0030]    A triple mechanical seal system according to the invention for a centrifugal ANSI pump housing is depicted in  FIG. 1 . Many commercially available centrifugal pumps meet this description and their construction and operation will not be described except as it impacts the mechanical seal system. In a centrifugal pump, an upstream process fluid enters pump housing at axial inlet  30 , is compressed by impeller  32 , and is expelled from the pump housing at a radial outlet port  34 . Arrows depict the flow of pressurized process fluid around the impeller in the direction of the seal system—to be impeded by the seal system. The purpose of the seal system is to contain the process fluid within a seal chamber  102 , defined by seal chamber wall  36  extending from the face of the housing to the gland plate  38 , which is bolted to the seal chamber wall with bolts and sealed with O-rings, gaskets or other secondary sealing elements. One of ordinary skill in the art will appreciate that the size of the seal chamber in an ANSI pump is limited because the length of the shaft from the motor to the pump housing is set by standard. An adapter plate  198  is provided inboard of the gland plate  38  and secured with bolt  189 . Gland adapter  98  is attached to the gland  38  with bolt  89 . 
         [0031]    First mechanical seal  40  constitutes a first rotating seal face  46  biased against first stationary seal face  48  by bias element  42  such as a bellows or spring. The first mechanical seal  40  is sometimes referred to as the first inboard upstream mechanical seal because it is inboard of the seal gland. Stationary face  48  is secured to the housing with adapter  47  behind snap ring  53 . Thus, a process fluid flow path is not provided around the first mechanical seal, as in a pressure staged system. Process fluid that migrates beyond the first mechanical seal encounters second inboard mechanical seal  60 , which is in a staggered arrangement with respect to the first mechanical seal, having a larger diameter than the first mechanical seal. Preferably, the second and third biasing elements have the same inside and outside diameter, and the same length in the axial direction. Likewise, mechanical seals upstream of the second mechanical seal (one, two or three seals) preferably all have the same inside and outside diameter and the same length in the axial direction. This is referred to as a “staggered” arrangement. 
         [0032]    A second inboard mechanical seal  60  comprises a rotating face  66 , stationary face  64 , and a biasing element  62 . A third mechanical seal  70 , sometimes referred to as the outboard mechanical seal because it is positioned outboard of the gland plate  38 , comprises a third (or outboard) rotating face  76 , a third (or outboard) stationary face  78  and a third (or outboard) bias member  72 . The third stationary face  78  is a “dual duty” sealing face, in that opposite sides of element  78  serve as stationary sealing faces for two different mechanical seals. In the embodiment depicted, in the case where a liquid barrier fluid is used, a pumping ring  176  is optionally provided which uses the centrifugal force generated by the rotating sealing face to circulate the liquid barrier fluid back to the source, as described in greater detail below. Second biasing member  62  and first biasing member  42  are optionally in back-to-back relationship. Thus, in the three-seal embodiment, the inside diameter of the first mechanical seal  40  runs in the process fluid and the outside diameter operates in a pressurized or non-pressurized barrier fluid or gas from circulating holding tank reservoir  92  or gas injection panel. The outside diameter of the second mechanical seal  60  also operates in the same circulating barrier fluid or barrier gas from a gas injection panel. The inside diameter of the second mechanical seal  60  may operate in a second barrier fluid or gas again maintained at a pressure lower or higher than the process fluid. The inside diameter of outboard mechanical seal  70  operates in the second circulating barrier fluid or gas from a separate gas injection panel. This configuration provides a back up mechanical seal and third protection mechanical seal so that when leakage occurs past the first mechanical seal  40 , and the barrier fluid is lost through that seal, the second mechanical seal continues to be lubricated by second barrier fluid providing further protection from hazardous or abrasive pumped fluids from leaking into the atmosphere or into the process fluid. 
         [0033]    In an embodiment depicted in  FIG. 2 , a fourth mechanical seal  50  may be added upstream of the first mechanical seal  40 , including a dual duty or fourth stationary sealing face  52  (on the opposite side of the first stationary seal face  48 ) and fourth rotating sealing face  54 . The fourth biasing member is located between a radial extension of the sleeve  80  and the fourth rotating sealing face. In operation, the fourth mechanical seal operates only in the process fluid. The downstream mechanical seals may be lubricated by another source of barrier fluid, as described above. An optional drill through port can be added so that the fourth seal can also be lubricated by a barrier fluid or gas in addition to the process fluid. 
         [0034]    In an embodiment depicted in  FIG. 3 , a fifth mechanical seal  20  is added upstream of the fourth mechanical seal  50 . In this embodiment, the fifth mechanical seal would be the first seal contacted by process fluid entering the seal chamber  102 . Fifth stationary seal face  22  is held in place between a pair of snap rings  63 ,  65  and bellows  24  biases rotating face  28  against stationary face  22 . The sealing faces of each of the seals  20 ,  40 ,  50 ,  60 , and  70  are preferably made of silicon carbide or tungsten carbide or other suitable materials known in the art. 
         [0035]    The present invention utilizes multiple mechanical seals within the limited space of the seal chamber as described above by utilizing seals having shorter overall length. The inventors have recognized that the sealing faces of individual seals do not need to be compressed so tightly to prevent leakage in an ordinary duty pump. For example, a pump rated for a given pressure will operate most of the time well below the rated pressure. Rather than using one or two seals rated at the rated pressure of the pump, as in the prior art, longer life and a greater efficiency preventing leakage is achieved with more seals having a lower maximum pressure rating. Such seals have shorter overall length and thus more of them can be used. 
         [0036]    In the case where bellows are used as the biasing members for the mechanical seals, it is preferred that all of the bellows have the same length. To be operable with the three-, four-, five- or more seal systems of the invention, and fit within standard seal chambers, the bellows should have at least one convolution and have a length in a range of about 0.2 inches to about 0.3 inches. A presently preferred configuration utilizes asymmetric non-welded bellows having three convolutions and a length of about 0.280 inches. Welded bellows may be used, especially if a specific design requires specialty materials such as 316 stainless steel, Hastelloy C or other. Welded members may be shorter, having a larger number of convolutions. If other loading members are utilized, such as a spring, the artisan having ordinary skill can arrive at an appropriate length such that two to four or more seals fit in the seal chamber and still provide the appropriate compression on each seal face relative to the size of the shaft and the pressure rating of the pump. 
         [0037]    In the three-seal system depicted in  FIG. 1 , two of the seals are inboard of the seal gland with an additional third seal outboard of the seal gland. In a four-seal system, three seals are inboard of the seal gland with an additional fourth seal outboard of the seal gland. And in a five-seal system, four seals are inboard of the seal gland with an additional fifth seal outboard of the seal gland. None of these configurations has been practiced in the prior art. Further, the seals are in a staggered arrangement, so that the seals on either side of the seal gland have a larger diameter than the one, two or three seals further inboard of the seal gland. 
         [0038]    In a five-seal arrangement, the first three seals encountered downstream of the pump housing have the same diameter and the two seals arranged on opposite sides of the seal gland plate have the same diameter. In an exemplary five-seal embodiment, utilizing a 1.375 inch shaft, the three inboard seals have a bellows with a 1.510 inch inside diameter and the two seals arranged on opposite sides of the seal gland have inside diameter of 1.688 in. The sizing of the biasing members for the pumps is explored in Tables 1 and 2 below. In the preferred examples, all of the seals biasing members have the same bellows length. 
         [0039]      FIG. 4  depicts the convention used in this application for measuring the length of a bellows seal. The bellows  202  is positioned between the seal ring shells  204 ,  206 , such that the length of the bellows refers to the distance “d 1 ” between the seal ring shells. The length of the entire bellows assembly including the seal ring shells  204 ,  206  is “d 2 ”, and the length of the seal ring shell  206  is referred to as “d 3 ”. The construction of a bellows seal is known in the art. A less preferred bellows design, used with certain cartridge seals known in the art, comprises a plurality of rings welded together to make the convolutions (as opposed to being electroformed). In a preferred embodiment of the invention, the bellows are electroformed, made of gold plated electrodeposited nickel. Other chemically resistant materials are known in the art and may be used. 
         [0040]    The following Tables 1 and 2 identify the dimensions of representative bellows used in connection with preferred embodiment of the invention according to shaft size of an ANSI pump. In each case all five seals have the same length. For a given shaft size, the three inboard seals have the same diameter and the two seals on opposite sides of the seal gland have the same diameter. 
         [0000]    
       
         
               
               
               
               
               
             
               
               
               
               
               
             
           
               
                 TABLE 1 
               
               
                   
               
               
                   
                 Seals 
                 Bellows Length 
                 Seals 
                 Bellows Length 
               
               
                 Shaft Size 
                 20, 50, 40 
                 Inboard 
                 60 &amp; 70 
                 Outboard 
               
               
                   
               
             
             
               
                   
               
             
          
           
               
                 1.125 
                 1.385 
                 0.28 
                 1.563 
                 0.28 
               
               
                 1.125 
                 1.385 
                 0.28 
                 1.563 
                 0.28 
               
               
                 1.375 
                 1.51 
                 0.28 
                 1.688 
                 0.28 
               
               
                 1.437 
                 1.572 
                 0.28 
                 1.751 
                 0.28 
               
               
                 1.625 
                 1.76 
                 0.28 
                 1.938 
                 0.28 
               
               
                 1.75 
                 1.885 
                 0.28 
                 2.063 
                 0.28 
               
               
                 1.875 
                 2.01 
                 0.28 
                 2.188 
                 0.28 
               
               
                 2.125 
                 2.26 
                 0.28 
                 2.438 
                 0.28 
               
               
                 2.437 
                 2.572 
                 0.28 
                 2.751 
                 0.28 
               
               
                 2.5 
                 2.635 
                 0.28 
                 2.813 
                 0.28 
               
               
                 2.625 
                 2.76 
                 0.28 
                 2.938 
                 0.28 
               
               
                 2.75 
                 2.885 
                 0.28 
                 3.063 
                 0.28 
               
               
                 3.44 
                 3.572 
                 0.28 
                 3.751 
                 0.28 
               
               
                 4.5 
                 4.635 
                 0.28 
                 4.813 
                 0.28 
               
               
                 1.375 
                 1.885 
                 0.28 
                 2.188 
                 0.28 
               
               
                 1.75 
                 2.26 
                 0.28 
                 2.438 
                 0.28 
               
               
                 1.875 
                 2.572 
                 0.28 
                 2.751 
                 0.28 
               
               
                 2.125 
                 2.635 
                 0.28 
                 2.813 
                 0.28 
               
               
                 2.5 
                 2.635 
                 0.28 
                 2.813 
                 0.28 
               
               
                 2.625 
                 2.885 
                 0.28 
                 3.063 
                 0.28 
               
               
                 2.75 
                 3.572 
                 0.28 
                 3.751 
                 0.28 
               
               
                 1.063 
                 1.385 
                 0.28 
                 1.563 
                 0.28 
               
               
                 1.188 
                 1.51 
                 0.28 
                 1.688 
                 0.28 
               
               
                 1.313 
                 2.635 
                 0.28 
                 1.813 
                 0.28 
               
               
                 1.438 
                 1.76 
                 0.28 
                 1.938 
                 0.28 
               
               
                 1.563 
                 1.885 
                 0.28 
                 2.063 
                 0.28 
               
               
                 1.688 
                 2.01 
                 0.28 
                 2.188 
                 0.28 
               
               
                 1.813 
                 2.26 
                 0.28 
                 2.438 
                 0.28 
               
               
                 1.938 
                 2.26 
                 0.28 
                 2.438 
                 0.28 
               
               
                   
               
             
          
         
       
     
         [0000]    
       
         
               
               
               
               
               
             
               
               
               
               
               
             
           
               
                 TABLE 2 
               
               
                   
               
               
                 Shaft 
                 Seals 
                 Bellows Length 
                 Seals 
                 Bellows Length 
               
               
                 Size 
                 20, 50, 40 
                 Inboard 
                 60 &amp; 70 
                 Outboard 
               
               
                   
               
             
             
               
                   
               
             
          
           
               
                 2.063 
                 2.572 
                 0.28 
                 2.251 
                 0.28 
               
               
                 2.188 
                 2.572 
                 0.28 
                 2.251 
                 0.28 
               
               
                 2.438 
                 2.76 
                 0.28 
                 2.938 
                 0.28 
               
               
                 2.563 
                 2.885 
                 0.28 
                 3.063 
                 0.28 
               
               
                 2.688 
                 3.01 
                 0.28 
                 3.188 
                 0.28 
               
               
                 2.813 
                 3.135 
                 0.28 
                 3.313 
                 0.28 
               
               
                 2.938 
                 3.26 
                 0.28 
                 3.438 
                 0.28 
               
               
                 3.063 
                 3.385 
                 0.28 
                 3.563 
                 0.28 
               
               
                 3.188 
                 3.51 
                 0.28 
                 3.688 
                 0.28 
               
               
                 3.313 
                 3.635 
                 0.28 
                 3.813 
                 0.28 
               
               
                 3.438 
                 3.76 
                 0.28 
                 3.938 
                 0.28 
               
               
                 3.563 
                 3.885 
                 0.28 
                 4.063 
                 0.28 
               
               
                 3.688 
                 4.01 
                 0.28 
                 4.188 
                 0.28 
               
               
                 3.813 
                 4.135 
                 0.28 
                 4.313 
                 0.28 
               
               
                 3.938 
                 4.26 
                 0.28 
                 4.438 
                 0.28 
               
               
                 4.063 
                 4.385 
                 0.28 
                 4.563 
                 0.28 
               
               
                 4.188 
                 4.51 
                 0.28 
                 4.688 
                 0.28 
               
               
                 4.313 
                 4.635 
                 0.28 
                 4.813 
                 0.28 
               
               
                 4.438 
                 4.76 
                 0.28 
                 4.938 
                 0.28 
               
               
                 4.563 
                 4.885 
                 0.28 
                 5.063 
                 0.28 
               
               
                 4.688 
                 5.01 
                 0.28 
                 5.188 
                 0.28 
               
               
                 4.813 
                 5.135 
                 0.28 
                 5.313 
                 0.28 
               
               
                   
               
             
          
         
       
     
         [0041]    The seal systems depicted in  FIG. 1  through  FIG. 3 , are cartridge seal systems in which the mechanical seals  20 ,  40 ,  50 ,  60 , and  70  are provided in a fixed position on a sleeve  80 . Sleeve  80  is attached to the shaft  14  via set screw  16  and drive collar  18 . In another aspect of the invention, drive collar  18  utilizes a cross drive  103  which provides double protection inside diameter O-rings  105 ,  107  before the atmosphere. As a practical necessity, first O-ring  162 , is an outside diameter (OD) O-ring. However, according to the invention, it is preferred to utilize inside diameter (ID) O-rings, i.e., O-rings which are provided in a radially inward facing groove machined into the equipment. Thus, O-rings  164  and  166 , providing ID seals between the sleeve  80  and the shaft  14 . Likewise, ID O-ring  168  provides a seal between pumping ring adapter  170  and seal adapter  172  to prevent migration of barrier fluid or barrier gas. Another ID O-ring  169  is provided between the seal adapter and the sleeve. O-rings are made of polytetrafluoroethylene or other chemically resistant material. To reduce inventory and simplify installation, the same sleeve  80  is provided for three, four and five seal systems, providing predetermined axial positions to place the sealing faces and biasing members. The cartridge is provided with the tension of the biasing members pre-set with clip spacers  101 . To install the cartridge, the mechanic lubricates the sleeve O-ring and slides it over the shaft, tightens the seal chamber bolts setting the seal gland in place, tightens the seal drive collar mechanism to the shaft in order to drive the seal and removes the cartridge clip spacers so that the seals and sleeve can spin with the shaft. 
         [0042]    The prior art does not teach a mechanical seal system in which two different barrier fluid sources may be used at the same time. According to the invention, a plurality of barrier fluids may be used. In one embodiment, the invention encompasses a low-pressure, light duty multi-seal cartridge operating with both a liquid and a gas barrier at the same time. 
         [0043]    An exemplary barrier fluid flow scheme for a five seal system is depicted in  FIG. 3 . A first barrier fluid source  92  provides circulating barrier fluid to the first and second seal faces  40  and  60 ; while a second barrier fluid source  94  provides circulating barrier fluid to the second seal face  60  and third seal face  70 . A third barrier fluid source  96  provides circulating barrier fluid to the fourth and fifth seal faces  50  and  20 . With the scheme according to the invention, the barrier fluids employed do not have to be the same fluid or maintained at the same pressure. In contrast, the double seal systems known in the art comprise a single chamber for barrier fluid between the seals, and only a single barrier fluid or gas may be used. 
         [0044]    In another aspect, the invention is directed to a seal having a bi-directional cross groove design as shown in  FIG. 5 . In this embodiment, rotating seal  500  includes grooves  502  in polished face  504 . With the prior art spiral grooves, the face is adapted for rotation in one direction only to accommodate flow of gas in the grooves. The grooves according to this embodiment are bi-directional, in the sense that the grooves will operate identically regardless of the direction of rotation. 
         [0045]    The above description of the preferred embodiments is not to be deemed to limit the invention, which is defined by the following claims.