Patent Abstract:
A system and a method for recovering and increasing the pressure of seal leak gas for recycle or passage to further processing.

Full Description:
FIELD OF THE INVENTION 
     The present invention relates to a system and a method for recovering and increasing the pressure of seal leak gas for recycle or passage to further processing. 
     BACKGROUND OF THE INVENTION 
     In many industrial processes it is necessary that gases be compressed. Typically turbine compressors, centrifugal compressors, pumps, screw compressors and the like may be used for this purpose. Such equipment is referred to herein generally as compressors. The compressors typically include seals for the passage of rotary components through sidewalls, ends or the like of the compressors. These seals are typically designed to permit leakage of small amounts of compressed gases through the seal. Many times the passage of the gas is due to wear of the seal but in many instances seals are designed to permit leakage of a selected quantity of gas in normal operation. 
     The seal leak gas in many instances may be harmful to the environment or constitute a valuable product which is desired to be recovered. In either event, it is typically recovered by positioning covers over the seal areas to sealingly contain the area around the seal with the cover positioned so that the seal leak gas is collected inside the cover. The cover may include a passageway, including a seal, for a rotary component passing through the cover into the compressor. Covers can be of a wide variety of configurations so long as they are effective to sealingly contact the unit containing the seal so that the gas is recovered in the cover. The cover typically has included a line for the passage of the gas into the atmosphere or more frequently to a stack or the like where the gas can be burned or passed to a gas processing system. The seal at the passageway does not present a leakage problem since the gas inside the cover is typically at a low pressure. 
     Since this seal gas is at relatively low pressures, it typically does not flow readily to further treatment. Usually the seal gas is vented or combusted at atmospheric or near atmospheric pressure. Accordingly, a pump or a fan system is typically required to move the seal leak gas to a treatment area, stack area, or the like if the system is at any level of positive pressure. It is difficult to economically recompress the gas for reuse, if it is a desirable gas. The economics dictate that the gases be sent to a flare for burning or the like even if they are valuable in view of the expense to recover the gases and pass them back for reuse. 
     Accordingly, a continuing search has been directed to the development of a method and system for economically collecting such gases and increasing their pressure so that they may be either reused or readily passed to further treatment. 
     SUMMARY OF THE INVENTION 
     According to the present invention, a system is provided for collecting seal leak gas and increasing the pressure of the seal leak gas, the system comprising: at least one source of seal leak gas having a gas inlet at a first pressure and a pressurized gas outlet at a second pressure and including at least one seal having a gas leak; a cover positioned to collect seal leak gas from at least one gas leak from the source and having a seal leak gas outlet; a venturi having a pressurized gas inlet at a third pressure, a mixed gas outlet at a fourth pressure and a seal leak gas inlet; a first line in fluid communication with the gas outlet and with the pressurized gas inlet; and, a second line in fluid communication with the at least one gas leak and the seal leak gas inlet to produce a mixed gas through the mixed gas outlet at the fourth pressure, the fourth pressure being greater than the first pressure. 
     The invention further includes a method for collecting seal leak gas from leaks at seals in compression equipment and increasing the pressure of the seal leak gas, the method comprising: compressing an inlet gas stream at a first pressure in the compressor equipment to produce a compressed gas stream at a second pressure; collecting seal leak gas from at least one seal in the compressor equipment; passing a minor amount of the compressed gas stream through a venturi to create a reduced pressure inlet into the venturi; and, passing the seal leak gas to the reduced pressure inlet to produce a mixed gas stream at a third pressure, the third pressure being greater than the first pressure. 
    
    
     
       BRIEF DESCRIPTION OF THE FIGURES 
         FIG. 1  is a schematic diagram of a system for the practice of a method for recovering seal leak gas, recompressing the gas and returning it economically and efficiently to the inlet of a compressor, according to the present invention; 
         FIG. 2  is a schematic diagram of an alternative embodiment of the present invention wherein a separation zone is used to separate undesirable liquid and/or solid components from a seal leak gas stream; and, 
         FIG. 3  is a schematic diagram of the use of the method and system of the present invention in conjunction with a natural gas liquefaction process. 
     
    
    
     DESCRIPTION OF PREFERRED EMBODIMENTS 
     In the discussion of the Figures, the same numbers will be used throughout to refer to the same or similar components. Many valves, controls and the like which will be necessary in the practice of the present invention have not been shown since the use of these components and the components themselves are well known and do not require further description for the disclosure of the present invention. 
     The present invention is useful with a compression system which may include compressors, i.e., either axial, positive displacement, centrifugal, screw, and the like or simply pumps, which pump gas from a first pressure to a second higher pressure. In such instances there are seals involved in the equipment which may be designed to leak controlled amounts of seal leak gas through the seal either for purposes of cooling or the like. In other instances the leakage is the result of simple wear. In any event, according to the present invention, the seal leak gases are collected by the use of covers over the seal areas to recover the escaping seal leak gas. The compression system is used to increase the pressure of a gaseous stream. According to the present invention, a small slip stream of the compressed stream is withdrawn and passed through a venturi which enables the suction of the seal leak gas into the venturi for mixture with the higher pressure slip stream. The recovered mixed gas stream is at a significantly higher pressure than the seal leak gas and is readily passed back to the inlet to the compressor so that both the slip stream and the seal leak gas may be recovered. 
     The invention is shown in  FIG. 1 , which shows a compressor  10  having a gas inlet  12  fed by a gas line  14 . A compressed gas outlet  16  is shown and represents a compressed gaseous stream. Seal leak gas escaping the compression system is shown through a plurality of lines  18 , line  23  and a line  20 , having seals  18 ′. Line  20  via covers  19  is connected to venturi  24  which enables the suction of the seal leak gas into the venturi for return to the process as described. In venturi  24  a slip stream from high pressure line  22  is mixed with the seal leak gas from line  20  and passed through a line  26  and a line  28  to line  14 . A line  30  is shown to indicate that the compressed gas may be passed to other treatment, such as flaring and the like. Valves  21 ,  25  and  27  regulate flow through lines  22 ,  28  and  30 . Particularly in processes, such as processes for the liquefaction of natural gas, the lost gas is a valuable mixed refrigerant. The use of the present invention allows the recovery and return of this mixed refrigerant to the process. The application of the present invention is by no means limited to mixed refrigerants but can be used with any gas pumped through a compression system where it is desirable to recover the seal leak gas. 
     In  FIG. 2  a similar embodiment is shown but line  20  passes the seal leak gas to a separator  32  where liquids and solids can be separated from the seal leak gas with the solids and liquids being recovered through line  36  and the seal leak gases being passed via a line  34  to venturi  24 . Vessel  32  may also be employed as a surge vessel, allowing storage of the seal leak gas for a period of time with no flow passing through lines  22  and  26 . At an appropriate time, flow can be established through lines  22  and  26  to recover the seal leak gas stored in vessel  32 . Seals  18 ′ and covers  19  are positioned on lines  18  and  23  and valves  25  and  27  have been shown in lines  28  and  30 . 
     Venturi systems are considered to be extremely well known as shown for instances in  Chemical Engineer&#39;s Handbook, Third Edition , Perry, John H. PhD, Editor, McGraw-Hill Book Company, Inc., 1950 pp. 1285. 
     In  FIG. 3  a schematic diagram of the use of the present invention in combination with a natural gas liquefaction process is shown. A gas liquefaction facility  40  is shown having a natural gas inlet  42  and a liquefied natural gas outlet  44 . In this embodiment inlet gas stream  14  is the spent refrigerant from the gas liquefaction facility  40  with the compressed stream in line  16  comprising the compressed refrigerant for use in the gas liquefaction facility. It is well known to those skilled in the art that such compressed gas typically requires cooling prior to passing it to the gas liquefaction facility or in the gas liquefaction facility so that the compressed, cooled refrigerant may be vaporized to provide cooling in the gas liquefaction facility. Many such processes are known to those skilled in the art and the present invention is considered to be suitable for use with all such processes since it primarily relates to the recovery and repressurization of seal leak gas from the compression system. 
     The system of the present invention may include a plurality of compression units and the venturi can receive seal leak gas from a plurality of seals. The seals may be contained either in a single unit or a plurality of units. All such embodiments are considered suitable for the recovery of the seal leak gas by means well known to those skilled in the art. In other words, such gas streams have previously been recovered for treatment by either flaring or the like. The same collection system for the gases can be used for the present invention with the difference being the recovery of the gases for passage to the venturi so that the seal leak gases can be recovered at a sufficient pressure for reinjection into the system or passage to other treatment. 
     According to the present invention, the pressure of the gas stream in line  22  is at or slightly below the pressure in line  16  and flows through venturi  24 , drawing seal leak gas from line  20  into the gas stream from line  22  to produce a mixed gas stream which is recovered through line  26  at a pressure somewhat lower than the pressure in line  22  but greater than the pressure in line  14 . Wide variations in the process pressures are possible so long as the relationship between the pressures is maintained as described above. For instance, in processes for the liquefaction of natural gas the pressure of the refrigerant (line  16 ) may be relatively high (200 to about 1000 psi) and the pressure of the returned, spent refrigerant (line  14 ) may be relatively low (0 to about 200 psi). It is clear that when a slipstream of gas is taken through line  22  in an amount sufficient to produce the desired suction from line  20 , either directly or via separator  32 , that the pressure of the mixed stream will be well above the pressure in line  14 . The flow of high pressure gas through line  22  is desirably regulated by a valve  21  as known to those skilled in the art. The flow through line  22  will typically be limited to only that amount necessary to produce the required suction and the required pressure in line  26 . Since this gas is recovered along with the seal leak gas, there is no net loss of gas to the process. Further there is no requirement for additional compression equipment with the resulting maintenance and power requirements. 
     While the present invention has been described above primarily with respect to natural gas liquefaction processes, it is equally useful with other processes, such as pumping stations for gaseous products of various kinds. The present invention can generally be used in any process in which a gaseous stream is compressed and which experiences the loss of gas through seals. 
     While the present invention has been described by reference to certain of its preferred embodiments, it is pointed out that the embodiments described are illustrative rather than limiting in nature and that many variations and modifications are possible within the scope of the present invention. Many such variations and modifications may be considered obvious and desirable by those skilled in the art based upon a review of the foregoing description of preferred embodiments.

Technology Classification (CPC): 8