# US 11,027,290 B2 · Centrifugal separator having an intermittent discharge system with hydraulically operated sliding bowl bottom > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 11,027,290 B2 - Document ID: US11027290B2 - Status: Granted - Kind: B2 - Application number: 16/069,003 - Filed: 2017-02-16 - Published: 2018-12-13 - Granted: 2021-06-08 - Earliest claimed: 2016-02-22 - Assignees: Alfa Laval Corporate AB - Applicants: Alfa Laval Corporate AB - Inventors: Klas Hilding - Web page: https://patentgrep.com/patent/US11027290B2 ## CPC - B04B 1/14: with periodical discharge - B04B 11/02: Continuous feeding or discharging; Control arrangements therefor - B04B 11/04: Periodical feeding or discharging; Control arrangements therefor - B04B 2011/046: {Loading, unloading, manipulating sample containers} - B04B: CENTRIFUGES (high-speed drum mills B02C19/11; domestic spin driers D06F; analysing, measuring or monitoring physical or chemical properties of samples during centrifuging, see the relevant subclasses for these procedures, e.g. G01N) ## Abstract A centrifugal separator for separation of at least two components of a fluid mixture of different densities includes a centrifuge rotor with a sliding bowl bottom movable between a closed position, in which the peripheral ports are closed, and an open position, in which the peripheral ports are open, an inlet channel for supplying hydraulic fluid to a closing chamber between the sliding bowl bottom and the rotor casing in order to hold the sliding bowl bottom in the closed position. The centrifugal separator includes at least one hermetic seal at a second end, other than the first end, of a hollow spindle and the inlet channel for supplying hydraulic fluid to the closing chamber extends through the hollow spindle and is arranged such that the hydraulic fluid is in thermal contact with the at least one hermetic seal when the hydraulic fluid is supplied to the closing chamber. ## Claims ### Claim 1 A centrifugal separator for separation of at least two components of a fluid mixture which are of different densities, said centrifugal separator comprising: a frame; a hollow spindle rotatably supported by the frame; a centrifuge rotor mounted to a first end of the hollow spindle to rotate together with the hollow spindle around an axis of rotation, wherein the centrifuge rotor comprises a rotor casing enclosing a separation space in which a stack of separation discs is arranged; a duct arranged to be through-flown by process medium during operation of the centrifugal separator and extending through said hollow spindle and in fluid contact with said separation space; at least one liquid outlet for discharging a separated liquid phase from said separation space; and a plurality of peripheral ports extending from the separation space through the rotor casing to a surrounding space for discharging a phase from the periphery of said separation space, wherein said centrifuge rotor comprises: a sliding bowl bottom movable between a closed position, in which the peripheral ports are closed, and an open position, in which the peripheral ports are open; and an inlet channel for supplying hydraulic fluid to a closing chamber between the sliding bowl bottom and the rotor casing in order to hold the sliding bowl bottom in the closed position, wherein the centrifugal separator further comprises at least one hermetic seal at a second end, other than the first end, of the hollow spindle, and wherein said inlet channel for supplying hydraulic fluid to said closing chamber extends through the hollow spindle and is further arranged such that said hydraulic fluid is in thermal contact with said at least one hermetic seal when said hydraulic fluid is being supplied to said closing chamber. ### Claim 2 (depends on 1) The centrifugal separator according to claim 1, wherein said at least one hermetic seal is a mechanical seal. ### Claim 3 (depends on 2) The centrifugal separator according to claim 2, wherein the mechanical seal comprises: a stationary part arranged to be fitted onto a non-rotating member; and a rotating part arranged on the hollow spindle, wherein the inlet channel for supplying hydraulic fluid to the closing chamber is arranged such that said hydraulic fluid is in thermal contact with the interface between the stationary part and the rotating part of the mechanical seal when said hydraulic fluid is being supplied to said closing chamber. ### Claim 4 (depends on 2) The centrifugal separator according to claim 2, wherein said at least one hermetic seal is a seal that seals against said duct arranged to be through-flown by process medium during operation of the centrifugal separator. ### Claim 5 (depends on 1) The centrifugal separator according to claim 1, wherein said at least one hermetic seal is a seal that seals against said duct arranged to be through-flown by process medium during operation of the centrifugal separator. ### Claim 6 (depends on 5) The centrifugal separator according to claim 5, wherein the mechanical seal comprises: a stationary part arranged to be fitted onto a non-rotating member; and a rotating part arranged on the hollow spindle, wherein the inlet channel for supplying hydraulic fluid to the closing chamber is arranged such that said hydraulic fluid is in thermal contact with the interface between the stationary part and the rotating part of the mechanical seal when said hydraulic fluid is being supplied to said closing chamber. ### Claim 7 (depends on 1) The centrifugal separator according to claim 1, wherein the separator comprises: a first hermetic seal at said second end of the spindle, the first hermetic seal being arranged for sealing against a first stationary pipe that is in fluid contact with said duct of the hollow spindle that is arranged to be through-flown by process medium during operation; and a second seal for sealing against a second stationary pipe arranged for supplying said hydraulic fluid to said inlet channel of the hollow spindle. ### Claim 8 (depends on 7) The centrifugal separator according to claim 7, wherein the second seal is a second hermetic seal. ### Claim 9 (depends on 8) The centrifugal separator according to claim 8, wherein said inlet channel for supplying hydraulic fluid to said closing chamber is arranged such that said hydraulic fluid is in thermal contact with said first hermetic seal and said second hermetic seal when said hydraulic fluid is being supplied to said closing chamber. ### Claim 10 (depends on 1) The centrifugal separator according to claim 1, wherein the inlet channel for supplying hydraulic fluid is arranged in the hollow spindle as an annular space surrounding said duct arranged to be through-flown by process medium during operation of the centrifugal separator. ### Claim 11 (depends on 1) The centrifugal separator according to claim 1, wherein the inlet channel for supplying hydraulic fluid is arranged in the hollow spindle as a pipe extending in said duct arranged to be through-flown by process medium during operation of the centrifugal separator for feeding the fluid mixture into said separation space. ### Claim 12 (depends on 1) The centrifugal separator according to claim 1, further comprising a pressure generator arranged for supplying said hydraulic fluid under a pressure that is higher than atmospheric pressure. ### Claim 13 (depends on 1) The centrifugal separator according to claim 1, wherein said duct arranged to be through-flown by process medium during operation of the centrifugal separator is a duct for the fluid mixture that is to be separated. ### Claim 14 (depends on 1) The centrifugal separator according to claim 1, wherein said duct arranged to be through-flown by process medium during operation of the centrifugal separator is a duct for a separated liquid phase. ### Claim 15 (depends on 1) The centrifugal separator according to claim 1, further comprising a duct through the rotor casing for supply of liquid to open at least one outlet passage through which the hydraulic fluid of the closing chamber is drained, thereby initiating moving of the sliding bowl bottom to the open position. ### Claim 16 (depends on 1) The centrifugal separator according to claim 1, further comprising means that facilitates a continuous consumption of the hydraulic fluid or a circulation of the hydraulic fluid to a heat exchange unit. ### Claim 17 (depends on 1) A method for separation of at least two components of a fluid mixture which are of different densities, said method comprising the steps of: providing the centrifugal separator according to claim 1; supplying hydraulic fluid into the inlet channel to the closing chamber between the sliding bowl bottom and the rotor casing in order to hold the sliding bowl bottom in the closed position; and feeding the fluid mixture to be separated to the separation space of the centrifuge rotor via the duct arranged to be through-flown by process medium during operation of the centrifugal separator. ### Claim 18 (depends on 17) The method according to claim 17, wherein the hydraulic fluid is water. ### Claim 19 (depends on 17) The method according to claim 17, wherein the hydraulic fluid is supplied under pressure via the second end of the spindle. ### Claim 20 (depends on 1) The centrifugal separator according to claim 1, wherein the centrifuge rotor is mounted on a top of the hollow spindle and the duct extends from a bottom of the hollow spindle through the hollow spindle.