# US 11,905,955 B1 · Extending life cycles of vacuum pumps used in manufacturing processes > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 11,905,955 B1 - Document ID: US11905955B1 - Status: Granted - Kind: B1 - Application number: 16/864,885 - Filed: 2020-05-01 - Granted: 2024-02-20 - Earliest claimed: 2019-05-01 - Assignees: Kashiyama Industries, Ltd. - Applicants: Yoshinori Christopher Dokko - Inventors: Yoshinori Christopher Dokko - Web page: https://patentgrep.com/patent/US11905955B1 ## CPC - F04C 19/005: {Details concerning the admission or discharge} - F04C 23/005: {of dissimilar working principle} - F04C 25/02: for producing high vacuum (sealing arrangements F04C27/00; silencing F04C29/06) - F04C 29/0092: {Removing solid or liquid contaminants from the gas under pumping, e.g. by filtering or deposition; Purging; Scrubbing; Cleaning} - F04C 2220/30: Use in a chemical vapor deposition [CVD] process or in a similar process - F04C 2280/02: Preventing solid deposits in pumps, e.g. in vacuum pumps with chemical vapour deposition [CVD] processes - H10P 72/04: {Apparatus for manufacture or treatment} - H10W 72/07125: {Means for controlling the bonding environment, e.g. valves or vacuum pumps} - F04C: ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS (engines F03C); ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS - H10P: GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10 - H10W: GENERIC PACKAGES, INTERCONNECTIONS, CONNECTORS OR OTHER CONSTRUCTIONAL DETAILS OF DEVICES COVERED BY CLASS H10 ## Abstract An abatement system with liquid-ring pump maintains an exhaust line at a negative pressure during operation of a vacuum pump. The vacuum pump operates to exhaust process gas and by-products from a process chamber through a foreline. The vacuum pump exhausts the process gas to the abatement system with liquid-ring pump through the exhaust line. The overall life of the vacuum pump is increased significantly because the exhaust line is maintained at a negative pressure which reduces precipitation of gases in the vacuum pump thereby reducing by-product accumulation and damage to the vacuum pump. The liquid-ring pump receives the exhaust process gas from the vacuum pump and outputs gas to a burn chamber and liquid to a recirculation tank. Liquid is recycled through the liquid-ring pump thereby reducing accumulation of precipitated gas and by-product. The overall life of the liquid-ring pump and vacuum pump are increased. ## Claims ### Claim 1 A method comprising: generating a vacuum condition in a process chamber using a vacuum pump, wherein the vacuum pump has an inlet port and an outlet port, and wherein the vacuum pump is coupled to extract gas from the process chamber via the inlet port and exhaust gas through an exhaust line via the outlet port; generating a negative pressure condition along the exhaust line while gas is exhausted from the vacuum pump through the exhaust line and to a liquid-ring pump; supplying a gas portion of an exhaust process gas from liquid-ring pump to a burn chamber; supplying abated liquid from the burn chamber to a tank; filtering liquid stored in the tank thereby generating filtered liquid; and recycling filtered liquid back into the liquid-ring pump or the burn chamber. ### Claim 2 (depends on 1) The method of claim 1, the liquid-ring pump has a first inlet port, a second inlet port, a first outlet port, and a second outlet port, wherein the first inlet port of the liquid-ring pump is coupled to receive gas from the vacuum pump via the exhaust line, wherein the first outlet port of the liquid-ring pump outputs gas, and wherein the second outlet port of the liquid-ring pump is coupled to output liquid. ### Claim 3 (depends on 2) The method of claim 2, further comprising: supplying liquid collected during an abatement process to the second inlet port of the liquid-ring pump. ### Claim 4 (depends on 3) The method of claim 3, further comprising: exhausting gas from the abatement process to a factory exhaust system. ### Claim 5 (depends on 2) The method of claim 2, wherein the second inlet port of the liquid-ring pump is coupled to receive liquid from part of an abatement system. ### Claim 6 (depends on 5) The method of claim 5, wherein the liquid received via the second inlet port of the liquid-ring pump is supplied from frail the tank of an abatement system, and wherein the tank receives liquid output by the burn chamber during an abatement process. ### Claim 7 (depends on 2) The method of claim 2, wherein the first inlet port of the liquid-ring pump is a gas inlet port, wherein the second inlet port of the liquid-ring pump is an operating liquid inlet port, wherein the first outlet port of the liquid-ring pump is a gas discharge outlet port, and wherein the second outlet port of the liquid-ring pump is a liquid drain outlet port. ### Claim 8 (depends on 2) The method of claim 2, wherein the first outlet port of the liquid-ring pump is coupled to supply gas to the burn chamber of an abatement system. ### Claim 9 (depends on 2) The method of claim 2, wherein the second outlet port of the liquid-ring pump is coupled to supply liquid to the burn chamber of the abatement system. ### Claim 10 (depends on 2) The method of claim 2, wherein the second outlet port of the liquid-ring pump is coupled to supply liquid to frail the tank of an abatement system, and wherein the tank is coupled to receive liquid output by the burn chamber of the abatement system. ### Claim 11 (depends on 1) The method of claim 1, wherein during the generating of the negative pressure condition, the inlet port of the vacuum pump has a first pressure level and the outlet port of the vacuum pump has a second pressure level, wherein the first pressure level is lower than the second pressure level, and wherein the second pressure level is lower than atmospheric pressure. ### Claim 12 (depends on 1) The method of claim 1, wherein the vacuum pump is a dry vacuum pump, and wherein the liquid-ring pump is part of an abatement system. ### Claim 13 A system comprising: a chamber; a foreline; a vacuum pump having an inlet port and an outlet port, wherein the inlet port of the vacuum pump is coupled to extract gas from the chamber via the foreline; an exhaust line; a liquid-ring pump having a first inlet port, a second inlet port, a first outlet port, and a second outlet port, wherein the first inlet port of the liquid-ring pump is coupled to receive gas from the vacuum pump via the exhaust line thereby causing a negative pressure condition along the exhaust line; a burn chamber; a storage tank, wherein the storage tank is coupled to receive liquid from the burn chamber; and a filter that filters liquid stored in the storage tank and generates filtered liquid, wherein the filtered liquid is input to the liquid-ring pump or the burn chamber. ### Claim 14 (depends on 13) The system of claim 13, wherein liquid stored in the tank is supplied to the second inlet port of the liquid-ring pump. ### Claim 15 (depends on 14) The system of claim 14, wherein the first outlet port of the liquid-ring pump is coupled to supply gas to the burn chamber of the abatement system. ### Claim 16 (depends on 14) The system of claim 14, wherein the second outlet port of the liquid-ring pump is coupled to supply liquid to the burn chamber of the abatement system. ### Claim 17 (depends on 13) The system of claim 13, wherein the vacuum pump is a dry vacuum pump, and wherein the liquid-ring pump is part of an abatement system. ### Claim 18 (depends on 13) The system of claim 13, wherein the first inlet port of the liquid-ring pump is a gas inlet port, wherein the second inlet port of the liquid-ring pump is an operating liquid inlet port, wherein the first outlet port of the liquid-ring pump is a gas discharge outlet port, and wherein the second outlet port of the liquid-ring pump is a liquid drain outlet port. ### Claim 19 A system comprising: a vacuum pump having an inlet port and an outlet port, wherein the inlet port of the vacuum pump is coupled to extract gas from a process chamber, and wherein the outlet port is coupled to exhaust gas exhausted from the process chamber through an exhaust line; and means for generating a negative pressure along the exhaust line while the gas is exhausted from the vacuum pump through the exhaust line, wherein liquid stored in a storage tank is filtered and recycled back into the means or back into a burn chamber of the system, and wherein the liquid is supplied from the burn chamber to the storage tank. ### Claim 20 (depends on 19) The system of claim 19, wherein the means is a liquid-ring pump.