US20020028145A1 - Gas compression system and method utilizing gas seal control - Google Patents
Gas compression system and method utilizing gas seal control Download PDFInfo
- Publication number
- US20020028145A1 US20020028145A1 US09/930,860 US93086001A US2002028145A1 US 20020028145 A1 US20020028145 A1 US 20020028145A1 US 93086001 A US93086001 A US 93086001A US 2002028145 A1 US2002028145 A1 US 2002028145A1
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- Prior art keywords
- gas
- conduit
- compressor
- valves
- trapped
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- 238000000034 method Methods 0.000 title claims abstract description 21
- 230000006835 compression Effects 0.000 title claims abstract description 10
- 238000007906 compression Methods 0.000 title claims abstract description 10
- 230000004044 response Effects 0.000 claims abstract description 6
- 230000009849 deactivation Effects 0.000 claims abstract description 3
- 238000007599 discharging Methods 0.000 claims description 11
- 238000004064 recycling Methods 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims 7
- 230000003213 activating effect Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 126
- 230000008569 process Effects 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000011109 contamination Methods 0.000 description 4
- 238000011144 upstream manufacturing Methods 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000007373 indentation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/08—Sealings
- F04D29/16—Sealings between pressure and suction sides
- F04D29/161—Sealings between pressure and suction sides especially adapted for elastic fluid pumps
- F04D29/162—Sealings between pressure and suction sides especially adapted for elastic fluid pumps of a centrifugal flow wheel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
- F04D27/02—Surge control
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/08—Sealings
- F04D29/10—Shaft sealings
- F04D29/102—Shaft sealings especially adapted for elastic fluid pumps
- F04D29/104—Shaft sealings especially adapted for elastic fluid pumps the sealing fluid being other than the working fluid or being the working fluid treated
Definitions
- This invention relates to a gas seal control system and method for a gas compressor, and, more particularly, to such a system and method according to which a seal gas is applied to a gas seal in the compressor.
- Gas compressors are well known, and include a housing for receiving a product gas to be compressed, a shaft rotatably mounted in the housing, and an impeller fixed to the shaft and cooperating with stationary vanes for compressing the gas before the compressed gas is discharged from the housing.
- one or more gas seals are often provided around the shaft between the impeller and the respective ends of the shaft for minimizing leakage of the gas from the high pressure area.
- the product gas from the compressor is introduced to the seals to maintain a high pressure sealing effect.
- this product gas often contains foreign matter, such as dirt, iron filings, and other solid particles which can contaminate the seals. Therefore, a seal gas from an external source is sometimes introduced to the seals to prevent possible contamination of the seals.
- the external seal gas which is usually nitrogen, is relatively expensive and must be stored and transported from the external source to the compressor, which further adds to the cost.
- a product gas is introduced into and compressed in, a compressor.
- a portion of the compressed gas is discharged to external equipment, and a portion of the gas is trapped in response to deactivation of the compressor.
- the trapped gas is passed back to the deactivated compressor and functions as a seal gas.
- This embodiment enjoys the advantages of utilizing product gas as a seal gas to eliminate the costs associated with a separate seal gas.
- FIG. 1 is a schematic view of a gas compression system according to an embodiment of the present invention.
- FIG. 2 is a schematic view of a gas compression system according to an alternate embodiment of the present invention.
- the reference numeral 10 refers, in general, to a gas compression system according to an embodiment of the present invention.
- the system 10 includes a gas compressor 12 which can be of a convention design and, as such, includes a shaft 14 rotatably mounted in a housing 16 .
- a gas compressor 12 which can be of a convention design and, as such, includes a shaft 14 rotatably mounted in a housing 16 .
- an impeller is fixed to the shaft 14 and cooperates with stationary vanes for compressing the gas when the compressor 12 is activated in a conventional manner.
- a seal 18 is provided on the shaft 14 and extends between the impeller and the upstream end of the shaft.
- the seal 18 is also of a conventional design and, as such, is adapted to seal against the leakage of the high pressure gas developed by the compressor during its operation and is adapted to receive a high pressure gas in a manner to be described to promote its sealing action.
- a typical seal of this type includes a rotating member that mounted on the shaft 14 for rotation with the shaft, and a fixed member positioned in very close proximity to the rotating member.
- One of the seal members, usually the rotating member has minute indentations or pockets machined in its outer face so that, when it rotates, pressure is created between it and the corresponding face of the other member which separates the two faces.
- the compressor 12 is connected in a closed loop conduit, shown in general, by the reference numeral 20 , extending from the outlet of the compressor and back to its inlet for recycling at least a portion of the compressed gas under conditions to be described.
- a conduit 22 is connected to the conduit 20 for introducing product gas from an internal source, and at a predetermined pressure, in the direction indicated by the flow arrow under the control of a block valve 24 connected in the conduit 22 . The gas then flows through a portion of the conduit 22 to a cooler 26 for the cooling the gas, in a conventional manner.
- the relatively cool gas from the cooler 26 is introduced into an inlet of the compressor 12 which operates in a conventional manner to compress the gas to a pressure higher than the inlet pressure utilizing the impeller and vanes discussed above.
- the compressed gas discharges from the compressor 12 through an outlet and passes back into the conduit 20 downstream of the compressor.
- a discharge conduit 30 is connected to the conduit 20 downstream of the compressor 12 for receiving at least a portion of the compressed gas.
- the conduit 30 discharges the compressed gas to external equipment (not shown) under the control of a valve 32 connected in the conduit.
- a recycle control valve 36 is connected in the conduit 20 downstream of the conduit 30 for reasons to be described.
- a conduit 40 is connected to the conduit 20 just downstream of the outlet of the compressor 12 and extends parallel to a section of the latter conduit.
- the conduit 40 is connected back to the conduit 20 upstream of the conduit 30 .
- Two spaced block valves 42 and 44 are connected in the conduit 40 and are normally open to permit the flow of some of the compressed gas from the outlet of the compressor 12 into the conduit 40 through which it flows parallel to the flow of the remaining gas through the latter portion of the conduit 20 .
- the block valves 42 and 44 are normally open but can be closed to capture some of the gas in that portion of the conduit 40 extending between them, under conditions to be described.
- One end of a conduit 50 is connected to a section of the conduit 40 extending between the block valves 42 and 44 .
- the conduit 50 extends through an inlet of the compressor 12 and to the seal 18 .
- a normally open control valve 52 is connected in the conduit 50 for controlling the flow of gas through the conduit.
- a filter 54 is also connected in the conduct 50 for filtering foreign matter, such as dirt, iron filings, liquid, etc. from the gas as it passes through the latter conduit under conditions to be described.
- valves 24 , 32 , 42 , 44 , and 52 are opened and the valve 36 is closed.
- Product gas at a predetermined inlet pressure, is introduced into the conduit 22 for passage to the conduit 20 , through the cooler 30 , and into the compressor 12 .
- the compressor 12 is activated by turning on its motor switch, or the like, to compress the gas to a pressure above the inlet pressure, and the compressed gas exits the compressor outlet and passes back into, and flows through, the conduit 20 . Since the valves 42 and 44 are open, some of this gas passes from the conduit 20 into the conduit 40 through which it flows parallel to the flow of the remaining gas through the corresponding, parallel portion of the conduit 20 .
- this gas passes from the conduit 40 , into and through the conduit 50 , and through the filter 54 under the control of the valve 52 .
- the gas is cleaned in the filter 54 in the manner discussed above, exits the filter 54 and passes through the open control valve 52 and to the seal 18 in the compressor 12 .
- This clean gas functions to prevent pressure loss and to keep the dirty process gas out of the area between the faces of the seal 18 to minimize contamination of the seal.
- valves 42 , 44 , and 52 are open to permit gas flow through the conduits 40 and 50 as discussed above.
- the valve 36 is opened and the valve 32 is set at a position to output gas from the conduit 20 at the relatively low flow.
- the portion of the gas outputted by the compressor 12 in the conduit 20 that does not flow into the conduit 30 is recycled back through the conduit 20 , the open valve 36 , and to the cooler 26 for passage back to the compressor 12 .
- the remaining gas needed to meet the minimum output flow of the compressor 12 is supplied from the incoming process gas through the conduit 22 , as discussed above.
- This recycle loop can also be used during start up and shut down of the system 10 .
- valves 24 , 32 , 42 and 44 are closed and the valve 36 is opened. This can be done automatically in a conventional manner in response to the tripping off of the motor.
- the closing of the valves 24 and 32 isolates the system 10 from the flow of the process gas into, and the discharge of the gas from, the conduit 20 and the inlet and discharge gas pressure from the compressor are thus the same.
- the opening of the valve 36 allows any gas remaining in the system to recycle back through the remaining portion of the conduit 20 to the compressor 12 .
- the closing of the valves 42 and 44 in response to the tripping of the compressor motor discussed above traps the gas in that section of the conduit 40 extending between the latter valves.
- This trapped gas is at the same pressure and temperature as the gas discharging from the compressor 12 , and the open valve 52 allows the latter gas to flow, at a pressure that is above the inlet pressure of the compressor 12 , through the filter 54 .
- Foreign matter is removed from the gas in the filter 54 and the clean gas then passes to the gas seal 18 in the compressor 12 to prevent the dirty process gas from contaminating the gas seal and prevents any pressure loss, as discussed above.
- the system 10 thus enables relatively clean process gas to be introduced to the gas seal 18 in the compressor 12 after shut down of the compressor without incurring the expense of providing clean gas from an external source.
- the reference numeral 60 refers, in general, to a gas compression system according to another embodiment of the present invention.
- the system 60 includes a gas compressor 62 which can be of a convention design and, as such, includes a shaft 64 rotatably mounted in a housing 66 .
- a gas compressor 62 which can be of a convention design and, as such, includes a shaft 64 rotatably mounted in a housing 66 .
- an impeller is fixed to the shaft 64 and cooperates with stationary vanes for compressing the gas when the compressor 62 is activated in a conventional manner.
- a seal 68 is provided on the shaft 64 and extends between the impeller and the upstream end of the shaft. Since the seal 68 is identical to the seal 18 of the previous embodiment, it will not be described in any further detail.
- the compressor 62 is connected in a closed loop conduit, shown in general, by the reference numeral 70 , extending from the outlet of the compressor and back to its inlet for recycling at least a portion of the compressed gas under conditions to be described.
- a conduit 72 is connected to the conduit 70 for introducing product gas from an internal source and at a predetermined pressure in the direction indicated by the flow arrow under the control of a block valve 74 connected in the conduit 72 . The gas then flows through a portion of the conduit 72 to a cooler 76 for the cooling the gas, in a conventional manner.
- the relatively cool gas from the cooler 76 is introduced into an inlet of the compressor 62 which operates in a conventional manner to compress the gas to a pressure higher than the inlet pressure utilizing the impeller and vanes discussed above.
- the compressed gas discharges from the compressor 62 through an outlet and passes back into the conduit 70 downstream of the compressor.
- a discharge conduit 80 is connected to the conduit 70 downstream of the compressor 62 for receiving at least a portion of the compressed gas, under conditions to be described, and discharging the compressed gas to external equipment (not shown).
- a pair of spaced block valves 82 and 84 are provided in the conduit 80 for controlling the flow of the gas through the conduit. The block valves 82 and 84 can be closed to capture some of the gas in that portion of the conduit 80 extending between the block valves 82 and 84 , as will be described.
- a recycle control valve 86 is connected in the conduit 70 downstream of the conduit 80 for controlling the flow of gas through the latter conduit under conditions to be described.
- One end of a conduit 90 is connected to the conduit 70 at a point just upstream of the connection of the conduit 80 to the conduit 70 .
- the conduit 90 extends from the conduit 70 , through an inlet of the compressor 62 , and to the seal 68 .
- a pair of spaced valves 92 and 94 are provided in the conduit 90 for controlling the flow of gas through the latter conduit, and a filter 94 is also connected in the conduct 90 between the latter valves for filtering foreign matter, such as dirt, iron filings, liquid, etc. from the gas as it passes through the conduit 90 .
- a conduit 100 extends from the conduit 80 between the valves 82 and 84 to the conduit 90 just downstream of the valve 92 .
- a block valve 102 is connected in the conduit 90 for controlling the flow of gas from the conduit 80 to the conduit 90 under conditions to be described.
- valves 86 and 102 are closed and the valves 72 , 82 , 84 92 , and 94 are opened.
- Product gas at a predetermined inlet pressure, is introduced into the conduit 72 for passage to the conduit 70 , through the cooler 80 , and into the compressor 62 .
- the compressor 62 is activated by turning on its motor switch, or the like, to compress the gas to a pressure above the inlet pressure, and the compressed gas exits the compressor outlet and passes back into, and flows through, the conduit 70 .
- valves 82 , 84 , 92 and 94 are open, some of the compressed gas from the compressor 62 passes from the conduit 70 , into the conduit 80 , and passes through the open valves 82 and 84 and discharges from the system 60 for passage to external equipment for further processing or use. Another portion of the compressed gas from the compressor 62 passes from the conduit 70 , into the conduit 90 , and into and through the open valve 92 and the filter 96 under the control of the valve 94 .
- the filter 96 operates to clean the gas as discussed above, and the relatively clean gas passes to the seal 68 in the compressor 62 .
- the relatively clean gas functions to prevent pressure loss and to keep the dirty process gas out of the area between the faces of the seal 68 and thus minimizes contamination of the seal.
- valves 92 and 94 are opened to permit the flow through the conduit 90 as described above.
- the valves 82 and 84 are set at a position to output gas from the conduit 70 at a relatively low flow rate and the valve 86 is opened. This permits the remaining portion of the gas in the conduit 70 downstream of the conduit 90 to be recycled back through the valve 86 to the cooler 76 for passage back to the compressor 62 .
- the remaining gas needed to meet the minimum output flow of the compressor 62 is supplied from the incoming process gas through the conduit 72 , as discussed above.
- This recycle loop can also be used during start up and shut down of the system 60 .
- valves 74 , 82 , 84 and 92 are closed and the valves 86 , 94 , and 102 are opened. This can be done automatically in response to the tripping off of the motor in a conventional manner.
- the closing of the valves 74 , 82 and 84 isolates the system 60 from the flow of the process gas into, and the discharge of the gas from, the conduit 70 and the inlet and discharge gas pressure from the compressor are the same.
- the opening of the valve 86 allows any gas remaining in the system to recycle back through the remaining portion of the conduit 70 to the compressor 62 .
- FIG. 2 enjoys all of the advantages of the embodiment of FIG. 1.
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Abstract
A gas compression system and method according to which product gas is introduced into and compressed in, a compressor. A portion of the compressed gas is discharged to external equipment, and a portion of the gas is trapped in response to deactivation of the compressor. The trapped gas is passed back to the deactivated compressor.
Description
- This invention relates to a gas seal control system and method for a gas compressor, and, more particularly, to such a system and method according to which a seal gas is applied to a gas seal in the compressor.
- Gas compressors are well known, and include a housing for receiving a product gas to be compressed, a shaft rotatably mounted in the housing, and an impeller fixed to the shaft and cooperating with stationary vanes for compressing the gas before the compressed gas is discharged from the housing.
- In many of these arrangements, one or more gas seals are often provided around the shaft between the impeller and the respective ends of the shaft for minimizing leakage of the gas from the high pressure area. During operation of the compressor, at least a portion of the product gas from the compressor is introduced to the seals to maintain a high pressure sealing effect. However this product gas often contains foreign matter, such as dirt, iron filings, and other solid particles which can contaminate the seals. Therefore, a seal gas from an external source is sometimes introduced to the seals to prevent possible contamination of the seals. However, the external seal gas, which is usually nitrogen, is relatively expensive and must be stored and transported from the external source to the compressor, which further adds to the cost.
- Therefore, what is needed is gas compressor in which relative clean seal gas can be applied to the seals without significantly adding to the cost.
- According to the system and method of an embodiment of the present invention, a product gas is introduced into and compressed in, a compressor. A portion of the compressed gas is discharged to external equipment, and a portion of the gas is trapped in response to deactivation of the compressor. The trapped gas is passed back to the deactivated compressor and functions as a seal gas.
- This embodiment enjoys the advantages of utilizing product gas as a seal gas to eliminate the costs associated with a separate seal gas.
- FIG. 1 is a schematic view of a gas compression system according to an embodiment of the present invention.
- FIG. 2 is a schematic view of a gas compression system according to an alternate embodiment of the present invention.
- Referring to FIG. 1 of the drawings, the
reference numeral 10 refers, in general, to a gas compression system according to an embodiment of the present invention. Thesystem 10 includes agas compressor 12 which can be of a convention design and, as such, includes ashaft 14 rotatably mounted in ahousing 16. Although not shown in the drawing for the convenience of presentation, it is understood that an impeller is fixed to theshaft 14 and cooperates with stationary vanes for compressing the gas when thecompressor 12 is activated in a conventional manner. - A
seal 18 is provided on theshaft 14 and extends between the impeller and the upstream end of the shaft. Theseal 18 is also of a conventional design and, as such, is adapted to seal against the leakage of the high pressure gas developed by the compressor during its operation and is adapted to receive a high pressure gas in a manner to be described to promote its sealing action. A typical seal of this type includes a rotating member that mounted on theshaft 14 for rotation with the shaft, and a fixed member positioned in very close proximity to the rotating member. One of the seal members, usually the rotating member, has minute indentations or pockets machined in its outer face so that, when it rotates, pressure is created between it and the corresponding face of the other member which separates the two faces. This creates a very small through area through which gas can flow. Examples of these type of seals, or similar seals, are disclosed in U.S. Pat. Nos. 5,441,283; 5,492,341; 5,498,007; 5,700.013; and 5,713,576 the disclosures of all of which are incorporated by reference. - The
compressor 12 is connected in a closed loop conduit, shown in general, by thereference numeral 20, extending from the outlet of the compressor and back to its inlet for recycling at least a portion of the compressed gas under conditions to be described. Aconduit 22 is connected to theconduit 20 for introducing product gas from an internal source, and at a predetermined pressure, in the direction indicated by the flow arrow under the control of ablock valve 24 connected in theconduit 22. The gas then flows through a portion of theconduit 22 to acooler 26 for the cooling the gas, in a conventional manner. - The relatively cool gas from the
cooler 26 is introduced into an inlet of thecompressor 12 which operates in a conventional manner to compress the gas to a pressure higher than the inlet pressure utilizing the impeller and vanes discussed above. The compressed gas discharges from thecompressor 12 through an outlet and passes back into theconduit 20 downstream of the compressor. - A
discharge conduit 30 is connected to theconduit 20 downstream of thecompressor 12 for receiving at least a portion of the compressed gas. Theconduit 30 discharges the compressed gas to external equipment (not shown) under the control of avalve 32 connected in the conduit. Arecycle control valve 36 is connected in theconduit 20 downstream of theconduit 30 for reasons to be described. - A
conduit 40 is connected to theconduit 20 just downstream of the outlet of thecompressor 12 and extends parallel to a section of the latter conduit. Theconduit 40 is connected back to theconduit 20 upstream of theconduit 30. Two spacedblock valves 42 and 44 are connected in theconduit 40 and are normally open to permit the flow of some of the compressed gas from the outlet of thecompressor 12 into theconduit 40 through which it flows parallel to the flow of the remaining gas through the latter portion of theconduit 20. Theblock valves 42 and 44 are normally open but can be closed to capture some of the gas in that portion of theconduit 40 extending between them, under conditions to be described. - One end of a
conduit 50 is connected to a section of theconduit 40 extending between theblock valves 42 and 44. Theconduit 50 extends through an inlet of thecompressor 12 and to theseal 18. A normallyopen control valve 52 is connected in theconduit 50 for controlling the flow of gas through the conduit. Afilter 54 is also connected in theconduct 50 for filtering foreign matter, such as dirt, iron filings, liquid, etc. from the gas as it passes through the latter conduit under conditions to be described. - In the initial, normal operation of the
system 10, the 24, 32, 42, 44, and 52 are opened and thevalves valve 36 is closed. Product gas, at a predetermined inlet pressure, is introduced into theconduit 22 for passage to theconduit 20, through thecooler 30, and into thecompressor 12. Thecompressor 12 is activated by turning on its motor switch, or the like, to compress the gas to a pressure above the inlet pressure, and the compressed gas exits the compressor outlet and passes back into, and flows through, theconduit 20. Since thevalves 42 and 44 are open, some of this gas passes from theconduit 20 into theconduit 40 through which it flows parallel to the flow of the remaining gas through the corresponding, parallel portion of theconduit 20. A portion of this gas passes from theconduit 40, into and through theconduit 50, and through thefilter 54 under the control of thevalve 52. The gas is cleaned in thefilter 54 in the manner discussed above, exits thefilter 54 and passes through theopen control valve 52 and to theseal 18 in thecompressor 12. This clean gas functions to prevent pressure loss and to keep the dirty process gas out of the area between the faces of theseal 18 to minimize contamination of the seal. - The remaining portion of the gas in the
conduit 40 is reintroduced into theconduit 20 and thus mixes with the gas flowing through the latter portion of the conduit. This mixed gas then passes from theconduit 20, into theconduit 30, and passes 2 through theopen valve 32 to external equipment for further processing or use. - There are certain conditions when it is desired to recycle at least some of the compressed gas from the
compressor 12. For example, design requirements may require that the gas discharged from theconduit 30 must be at a relatively low flow, in terms of cubic feet per minute, for example, which flow is lower than the lowest flow that is possible from thecompressor 12. In this case, the 42, 44, and 52 are open to permit gas flow through thevalves 40 and 50 as discussed above. Theconduits valve 36 is opened and thevalve 32 is set at a position to output gas from theconduit 20 at the relatively low flow. Thus, the portion of the gas outputted by thecompressor 12 in theconduit 20 that does not flow into theconduit 30 is recycled back through theconduit 20, theopen valve 36, and to thecooler 26 for passage back to thecompressor 12. The remaining gas needed to meet the minimum output flow of thecompressor 12 is supplied from the incoming process gas through theconduit 22, as discussed above. This recycle loop can also be used during start up and shut down of thesystem 10. - When the
compressor 12 is deactivated by the tripping off of its motor, either on purpose to shut down the system, or due to an electrical or system failure, or the like, the 24, 32, 42 and 44 are closed and thevalves valve 36 is opened. This can be done automatically in a conventional manner in response to the tripping off of the motor. The closing of the 24 and 32 isolates thevalves system 10 from the flow of the process gas into, and the discharge of the gas from, theconduit 20 and the inlet and discharge gas pressure from the compressor are thus the same. The opening of thevalve 36 allows any gas remaining in the system to recycle back through the remaining portion of theconduit 20 to thecompressor 12. - According to a feature of the invention, the closing of the
valves 42 and 44 in response to the tripping of the compressor motor discussed above traps the gas in that section of theconduit 40 extending between the latter valves. This trapped gas is at the same pressure and temperature as the gas discharging from thecompressor 12, and theopen valve 52 allows the latter gas to flow, at a pressure that is above the inlet pressure of thecompressor 12, through thefilter 54. Foreign matter is removed from the gas in thefilter 54 and the clean gas then passes to thegas seal 18 in thecompressor 12 to prevent the dirty process gas from contaminating the gas seal and prevents any pressure loss, as discussed above. - The
system 10 thus enables relatively clean process gas to be introduced to thegas seal 18 in thecompressor 12 after shut down of the compressor without incurring the expense of providing clean gas from an external source. - Referring to the alternate embodiment depicted in FIG. 2 of the drawings, the
reference numeral 60 refers, in general, to a gas compression system according to another embodiment of the present invention. Thesystem 60 includes agas compressor 62 which can be of a convention design and, as such, includes ashaft 64 rotatably mounted in ahousing 66. Although not shown in the drawing for the convenience of presentation, it is understood that an impeller is fixed to theshaft 64 and cooperates with stationary vanes for compressing the gas when thecompressor 62 is activated in a conventional manner. - A
seal 68 is provided on theshaft 64 and extends between the impeller and the upstream end of the shaft. Since theseal 68 is identical to theseal 18 of the previous embodiment, it will not be described in any further detail. - The
compressor 62 is connected in a closed loop conduit, shown in general, by thereference numeral 70, extending from the outlet of the compressor and back to its inlet for recycling at least a portion of the compressed gas under conditions to be described. Aconduit 72 is connected to theconduit 70 for introducing product gas from an internal source and at a predetermined pressure in the direction indicated by the flow arrow under the control of a block valve 74 connected in theconduit 72. The gas then flows through a portion of theconduit 72 to a cooler 76 for the cooling the gas, in a conventional manner. - The relatively cool gas from the cooler 76 is introduced into an inlet of the
compressor 62 which operates in a conventional manner to compress the gas to a pressure higher than the inlet pressure utilizing the impeller and vanes discussed above. The compressed gas discharges from thecompressor 62 through an outlet and passes back into theconduit 70 downstream of the compressor. - A
discharge conduit 80 is connected to theconduit 70 downstream of thecompressor 62 for receiving at least a portion of the compressed gas, under conditions to be described, and discharging the compressed gas to external equipment (not shown). A pair of spaced 82 and 84 are provided in theblock valves conduit 80 for controlling the flow of the gas through the conduit. The 82 and 84 can be closed to capture some of the gas in that portion of theblock valves conduit 80 extending between the 82 and 84, as will be described.block valves - A
recycle control valve 86 is connected in theconduit 70 downstream of theconduit 80 for controlling the flow of gas through the latter conduit under conditions to be described. - One end of a
conduit 90 is connected to theconduit 70 at a point just upstream of the connection of theconduit 80 to theconduit 70. Theconduit 90 extends from theconduit 70, through an inlet of thecompressor 62, and to theseal 68. A pair of spaced 92 and 94 are provided in thevalves conduit 90 for controlling the flow of gas through the latter conduit, and afilter 94 is also connected in theconduct 90 between the latter valves for filtering foreign matter, such as dirt, iron filings, liquid, etc. from the gas as it passes through theconduit 90. - A
conduit 100 extends from theconduit 80 between the 82 and 84 to thevalves conduit 90 just downstream of thevalve 92. Ablock valve 102 is connected in theconduit 90 for controlling the flow of gas from theconduit 80 to theconduit 90 under conditions to be described. - In the initial, normal operation of the
system 60, the 86 and 102 are closed and thevalves 72, 82, 84 92, and 94 are opened. Product gas, at a predetermined inlet pressure, is introduced into thevalves conduit 72 for passage to theconduit 70, through the cooler 80, and into thecompressor 62. Thecompressor 62 is activated by turning on its motor switch, or the like, to compress the gas to a pressure above the inlet pressure, and the compressed gas exits the compressor outlet and passes back into, and flows through, theconduit 70. - Since the
82, 84, 92 and 94 are open, some of the compressed gas from thevalves compressor 62 passes from theconduit 70, into theconduit 80, and passes through the 82 and 84 and discharges from theopen valves system 60 for passage to external equipment for further processing or use. Another portion of the compressed gas from thecompressor 62 passes from theconduit 70, into theconduit 90, and into and through theopen valve 92 and thefilter 96 under the control of thevalve 94. Thefilter 96 operates to clean the gas as discussed above, and the relatively clean gas passes to theseal 68 in thecompressor 62. The relatively clean gas functions to prevent pressure loss and to keep the dirty process gas out of the area between the faces of theseal 68 and thus minimizes contamination of the seal. - If it is desired to recycle at least some of the compressed gas from the
compressor 62, for the reasons set forth above in connection with the embodiment of FIG. 1, the 92 and 94 are opened to permit the flow through thevalves conduit 90 as described above. The 82 and 84 are set at a position to output gas from thevalves conduit 70 at a relatively low flow rate and thevalve 86 is opened. This permits the remaining portion of the gas in theconduit 70 downstream of theconduit 90 to be recycled back through thevalve 86 to the cooler 76 for passage back to thecompressor 62. The remaining gas needed to meet the minimum output flow of thecompressor 62 is supplied from the incoming process gas through theconduit 72, as discussed above. This recycle loop can also be used during start up and shut down of thesystem 60. - When the
compressor 12 is deactivated by the tripping off of its motor, either on purpose to shut down the system, or due to an electrical or system failure, or the like, the 74, 82, 84 and 92 are closed and thevalves 86, 94, and 102 are opened. This can be done automatically in response to the tripping off of the motor in a conventional manner. The closing of thevalves 74, 82 and 84 isolates thevalves system 60 from the flow of the process gas into, and the discharge of the gas from, theconduit 70 and the inlet and discharge gas pressure from the compressor are the same. The opening of thevalve 86 allows any gas remaining in the system to recycle back through the remaining portion of theconduit 70 to thecompressor 62. - According to a feature of the invention, when the
82 and 84 close as a result of the shut off of the motor of thevalves compressor 68 as described above, some of the gas in that section of theconduit 80 extending between the latter valves is trapped. This gas, which is at the same temperature and elevated pressure as the gas discharging from thecompressor 62, then flows through theopen valve 102, into theconduit 90 downstream of thevalve 92, and into thefilter 96. Foreign matter is removed from the gas by thefilter 96 before the clean gas flows through theopen valve 94 and to thegas seal 68 in thecompressor 62 to prevent pressure loss and possible contamination of the seal by the process gas in the compressor, as discussed above. - Thus the embodiment of FIG. 2 enjoys all of the advantages of the embodiment of FIG. 1.
- It is understood that variations may be made to each of the above embodiments without departing from the scope of the invention. For example, more than one gas seal be provided in the compressor and any other type of device, other than a filter can be used to clean the gas. Further, although the flow lines were referenced as being in the form of “conduits” it is understood that any type of flow line can be used.
- Since other modifications, changes, and substitutions are intended in the foregoing disclosure, it is appropriate that the appended claims be construed broadly and in a manner consistent with the scope of the invention.
Claims (30)
1. A gas compression system comprising a compressor for receiving product gas and compressing the gas, a first conduit for receiving compressed gas from the compressor, a second conduit for receiving some of the compressed gas and trapping the latter gas when the compressor shuts down, a third conduit connecting the second conduit to the compressor for passing the trapped gas back to the compressor, and a cleaning device disposed in the third conduit for cleaning the trapped gas before it is passed to the compressor.
2. The system of claim 1 further comprising two spaced valves in the second conduit, the valves being movable from an open position in which gas flows through the second conduit to the third conduit, and a closed position in which gas is trapped in the second conduit between the valves.
3. The system of claim 2 wherein the valves are open during operation of the compressor and closed when the compressor shuts down.
4. The system of claim 3 wherein the trapped gas passes from the second conduit to the third conduit for passage back to the compressor after the compressor shuts down.
5. The system of claim 1 further comprising a gas seal disposed in the compressor and wherein the clean gas passes from the third conduit to the gas seal.
6. The system of claim 1 wherein the second conduit receives some of the compressed gas from the first conduit.
7. The system of claim 1 further comprising a fourth conduit connected to the first conduit for discharging the compressed gas in the first conduit from the system.
8. The system of claim 7 wherein the fourth conduit discharges a portion of the compressed gas and wherein the first conduit is connected to the inlet of the compressor for passing another portion of the gas back to the compressor.
9. The system of claim 1 further comprising a fourth conduit connected to the second conduit for discharging the compressed gas in the first conduit from the system.
10. The system of claim 9 wherein the fourth conduit discharges a portion of the compressed gas and wherein the first conduit is connected to the inlet of the compressor for passing another portion of the gas back to the compressor.
11. The system of claim 1 wherein the compressor has an inlet for receiving the gas from an external source, and an outlet for discharging the compressed gas, the first conduit connected to the inlet and the outlet of the compressor for receiving compressed gas from the outlet, passing the gas in a loop, and returning the gas back to the inlet.
12. A gas compression system comprising a compressor having an inlet for receiving product gas and an outlet for discharging the compressed gas; a first conduit connected to the inlet for receiving compressed gas; a second conduit connected to the first conduit for discharging at least a portion of the gas from the system; a third conduit connected to the first conduit for receiving some of the compressed gas and trapping the latter gas when the compressor shuts down; a fourth conduit connecting the third conduit to the compressor for passing the trapped gas back to the compressor when the compressor shuts down, and a cleaning device disposed in the fourth conduit for cleaning the trapped gas before it is passed to the compressor.
13. The system of claim 12 further comprising two spaced valves in the third conduit, the valves being movable from an open position in which gas flows through the third conduit back to the first conduit, and a closed position in which gas is trapped in the third conduit between the valves.
14. The system of claim 13 wherein the valves are open during operation of the compressor and closed when the compressor shuts down.
15. The system of claim 14 wherein the trapped gas passes from the third conduit to the fourth conduit for passage back to the compressor after the compressor shuts down.
16. The system of claim 12 further comprising a gas seal disposed in the compressor and wherein the clean gas passes from the fourth conduit to the gas seal.
17. The system of claim 12 wherein the first conduit is also connected to the inlet of the compressor and passes a portion of the gas in a loop before returning the gas back to the inlet.
18. A gas compression system comprising a compressor having an inlet for receiving product gas and an outlet for discharging the compressed gas; a first conduit connected to the inlet for receiving compressed gas; a second conduit connected to the first conduit for discharging at least a portion of the gas from the system; a third conduit connected to the second conduit for receiving some of the compressed gas and trapping the latter gas when the compressor shuts down; a fourth conduit connecting the third conduit to the compressor for passing the trapped gas back to the compressor when the compressor shuts down, and a cleaning device disposed in the fourth conduit for cleaning the trapped gas before it is passed to the compressor.
19. The system of claim 18 further comprising two spaced valves in the third conduit, the valves being movable from an open position in which gas flows through the third conduit back to the second conduit, and a closed position in which gas is trapped in the third conduit between the valves.
20. The system of claim 19 wherein the valves are open during operation of the compressor and closed when the compressor shuts down.
21. The system of claim 20 wherein the trapped gas passes from the third conduit to the second conduit for passage back to the compressor after the compressor shuts down.
22. The system of claim 18 further comprising a gas seal disposed in the compressor and wherein the clean gas passes from the fourth conduit to the gas seal.
23. The system of claim 18 wherein the first conduit is also connected to the inlet of the compressor and passes a portion of the gas in a loop before returning the gas back to the inlet.
24. A gas compression method comprising the steps introducing product gas into a compressor, activating the compressor for compressing the gas in the compressor, receiving the compressed gas and discharging a portion of the compressed gas to external equipment, trapping a portion of the compressed gas in response to deactivation of the compressor, and passing the trapped gas back to the deactivated compressor.
25. The method of claim 24 wherein the trapped gas is passed to a gas seal in the compressor to prevent product gas being compressed from entering the gas seal.
26. The method of claim 25 further comprising the step of cleaning the trapped gas before it passes to the gas seal.
27. The method of claim 24 wherein the step of trapping comprising the steps of providing a conduit for receiving a portion of the compressed gas during operation of the compressor, connecting two spaced valves in the conduit and closing the valves when compressed gas is in the conduit.
28. The method of claim 27 wherein the valves are normally open to permit compressed gas to flow through the conduit and wherein the valves are closed when the compressor is deactivated to trap the gas.
29. The method of claim 28 wherein the step of passing comprising the steps of opening the valves to allow the trapped gas to pass back to the deactivated compressor.
30. The method of claim 24 further comprising the step of recycling a portion of the compressed gas back to the inlet of the compressor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/930,860 US20020028145A1 (en) | 2000-03-30 | 2001-08-16 | Gas compression system and method utilizing gas seal control |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/539,453 US6394764B1 (en) | 2000-03-30 | 2000-03-30 | Gas compression system and method utilizing gas seal control |
| US09/930,860 US20020028145A1 (en) | 2000-03-30 | 2001-08-16 | Gas compression system and method utilizing gas seal control |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US09/539,453 Division US6394764B1 (en) | 2000-03-30 | 2000-03-30 | Gas compression system and method utilizing gas seal control |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20020028145A1 true US20020028145A1 (en) | 2002-03-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US09/539,453 Expired - Lifetime US6394764B1 (en) | 2000-03-30 | 2000-03-30 | Gas compression system and method utilizing gas seal control |
| US09/930,860 Abandoned US20020028145A1 (en) | 2000-03-30 | 2001-08-16 | Gas compression system and method utilizing gas seal control |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US09/539,453 Expired - Lifetime US6394764B1 (en) | 2000-03-30 | 2000-03-30 | Gas compression system and method utilizing gas seal control |
Country Status (2)
| Country | Link |
|---|---|
| US (2) | US6394764B1 (en) |
| WO (1) | WO2001075305A1 (en) |
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| US9200643B2 (en) * | 2010-10-27 | 2015-12-01 | Dresser-Rand Company | Method and system for cooling a motor-compressor with a closed-loop cooling circuit |
| US9726196B2 (en) * | 2010-10-27 | 2017-08-08 | Dresser-Rand Company | System and cooling for rapid pressurization of a motor-bearing cooling loop for a hermetically sealed motor/compressor system |
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Also Published As
| Publication number | Publication date |
|---|---|
| US6394764B1 (en) | 2002-05-28 |
| WO2001075305A1 (en) | 2001-10-11 |
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Legal Events
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