# US 11,441,368 B2 · Split-flow degasser > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 11,441,368 B2 - Document ID: US11441368B2 - Status: Granted - Kind: B2 - Application number: 16/545,798 - Filed: 2019-08-20 - Published: 2021-02-25 - Granted: 2022-09-13 - Earliest claimed: 2019-08-20 - Assignees: Harry L. Burgess - Applicants: Burgess Manufacturing, Ltd. - Inventors: Harry L. Burgess - Web page: https://patentgrep.com/patent/US11441368B2 ## CPC - E21B 21/067: {Separating gases from drilling fluids} - B01D 19/0036: {Flash degasification (the other groups take precedence)} - B01D 19/0052: {in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused (B01D19/0026 takes precedence)} - E21B 43/34: Arrangements for separating materials produced by the well - E21B: EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) ## Abstract Techniques for improving a drilling fluid flow rate of a drilling fluid degasser by splitting the flow of the drilling fluid (e.g., drilling mud) are provided. An exemplary apparatus for degassing drilling fluid generally includes a pressure vessel; a vacuum blower in fluid communication with the pressure vessel; a slotted centrifuge tube having a cross-sectional area; a motor configured to power the vacuum blower and rotate the slotted centrifuge tube; an evacuation pump having an impeller connected with a lower end of the slotted centrifuge tube; and an inlet pipe spaced a distance away from the lower end of the slotted centrifuge tube, wherein the distance is based on a relationship between a cross-sectional area of the inlet pipe and the cross-sectional area of the slotted centrifuge tube. ## Claims ### Claim 1 An apparatus for degassing drilling fluid, comprising: a pressure vessel comprising: a top portion; and a bottom portion; a vacuum blower in fluid communication with the pressure vessel; a slotted centrifuge tube having a cross-sectional area; a motor configured to rotate the slotted centrifuge tube; an evacuation pump having an impeller connected with a lower end of the slotted centrifuge tube; and an outlet conduit connected to the evacuation pump; a drilling fluid inlet providing an opening between the bottom portion of the pressure vessel and the outlet conduit; an inlet pipe having an internal diameter, the inlet pipe spaced a distance away from the lower end of the slotted centrifuge tube, a region between an upper end of the inlet pipe and the lower end of the slotted centrifuge tube having a circumferential surface area, the circumferential surface area of the region being A2=πDH where D is the internal diameter of the inlet pipe and H is the distance of the inlet pipe away from the lower end of the slotted centrifuge tube; a mud tank, the pressure vessel being contained within the mud tank, the mud tank comprising: a first reservoir in fluid communication with the inlet pipe; and a second reservoir in fluid communication with the outlet conduit; a threaded fastener connected to the inlet pipe to adjust the distance between the slotted centrifuge tube and the inlet pipe, wherein adjusting the distance adjusts fluid flow, wherein an internal diameter of the inlet pipe is selected according to a ratio between a cross-sectional area of the inlet pipe and the cross-sectional area of the slotted centrifuge tube, and wherein the distance between the upper end of the inlet pipe and the lower end of the slotted centrifuge tube is determined according to a ratio between the circumferential surface area of the region and the cross-sectional area of the slotted centrifuge tube; a partition separating the first reservoir and the second reservoir of the mud tank, the partition having a gap therein to allow excess degassed drilling fluid to flow over the partition from the second reservoir to the first reservoir to avoid high pressure; and a handling bracket attached to the motor allowing the pressure vessel to be lifted out of the mud tank. ### Claim 2 (depends on 1) The apparatus of claim 1, wherein the ratio between the cross-sectional area of the inlet pipe and the cross-sectional area of the slotted centrifuge tube comprises the cross-sectional area of the inlet pipe being about 1.8 times the cross-sectional area of the slotted centrifuge tube. ### Claim 3 (depends on 1) The apparatus of claim 1, wherein: the inlet pipe has an internal diameter of about 8 inches; and the slotted centrifuge tube has an internal diameter of about 6 inches. ### Claim 4 (depends on 1) The apparatus of claim 1, wherein the ratio between the circumferential surface area of the region and the cross-sectional area of the slotted centrifuge tube comprises the circumferential surface area of the region being about 0.8 times the cross-sectional area of the slotted centrifuge tube. ### Claim 5 (depends on 1) The apparatus of claim 1, wherein the distance between the upper end of the inlet pipe and the lower end of the slotted centrifuge tube is about 0.875 inches. ### Claim 6 (depends on 1) The apparatus of claim 1, wherein: the evacuation pump has a pump cover having a lower opening, the lower opening having an internal radius at a lowermost extrema thereof; an annulus between the inlet pipe and the internal radius of the lower opening of the pump cover has a cross-sectional area extending between an outer surface of the inlet pipe and an inner surface of the pump cover at the lowermost extrema of the lower opening; and the internal radius of the lowermost extrema of the lower opening of the pump cover is determined according to a ratio between the cross-sectional area of the annulus and the cross-sectional area of the slotted centrifuge tube. ### Claim 7 (depends on 6) The apparatus of claim 6, wherein the ratio between the cross-sectional area of the annulus and the cross-sectional area of the slotted centrifuge tube comprises the cross-sectional area of the annulus being about 3.2 times the cross-sectional area of the slotted centrifuge tube. ### Claim 8 (depends on 6) The apparatus of claim 6, wherein the internal radius of the lowermost extrema of the lower opening of the pump cover is about 6.8 inches.