# US 12,110,775 B2 · Down-hole gas separator > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 12,110,775 B2 - Document ID: US12110775B2 - Status: Granted - Kind: B2 - Application number: 17/966,378 - Filed: 2022-10-14 - Published: 2023-02-09 - Granted: 2024-10-08 - Earliest claimed: 2017-09-18 - Assignees: Modicum, LLC - Applicants: Modicum, LLC - Inventors: Gary V. Marshall - Web page: https://patentgrep.com/patent/US12110775B2 ## CPC - B01D 19/0042: {modifying the liquid flow (B01D19/0021 takes precedence)} - E21B 43/38: in the well - E21B 43/121: {Lifting well fluids (monitoring of down-hole pump systems E21B47/008)} - E21B 43/35: {specially adapted for separating solids (down-hole drilling fluid separation systems E21B21/002; separating solids from drilling fluids E21B21/065)} - F04B 47/12: having free plunger lifting the fluid to the surface - 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) - E21B: EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS - F04B: POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS (machines for liquids, or pumps, of rotary-piston or oscillating-piston type F04C; non-positive-displacement pumps F04D; pumping of fluid by direct contact of another fluid or by using inertia of fluid to be pumped F04F) ## Abstract A method and apparatus for gas and solids separation from down-hole fluids is disclosed, including particular structural means for forcing the de-gassing of the gaseous liquid, including means for changing the velocity of the gaseous liquid (speed changes on each exit from the tubes owing to the volume difference between the tubes and the chamber), means for changing the direction of the gaseous liquid (owing to the flow changing direction from exiting one set of tubes to travel to the opening to enter the next set of tubes), and means for changing the pressure of the gaseous liquid (owing perhaps in part to evolution of gas upon entering increased volume). ## Claims ### Claim 1 An apparatus for separating of gas from a fluid in a wellbore, comprising: a first pipe configured to be disposed in a wellbore and define a wellbore annulus between the first pipe and the wellbore; a second pipe disposed in the first pipe, an inner annulus defined between the first pipe and the second pipe; a plurality of production separation chambers disposed in the first pipe; an orifice in an upper portion of each of the plurality of production separation chambers, the orifice configured to open into the wellbore annulus; one or more solids management tubes, the one or more solids management tubes having a top open end near a floor or lower portion of one of the production separation chambers and extending downward into a next lower production separation chamber; and thief jet orifices in the second pipe, each thief jet orifice positioned near a bottom of a respective production separation chamber and opening into the inner annulus, wherein the thief jet orifices restrict flow of the fluid to remove gas bubbles from the fluid. ### Claim 2 (depends on 1) The apparatus of claim 1, wherein each of the thief jet orifices is configured to restrict liquids flowing into the second pipe at a rate less than a flow rate in which gas bubbles out of the fluid prior to entering the thief jet orifice. ### Claim 3 (depends on 1) The apparatus of claim 1, wherein each thief jet orifice is sized to restrict downward velocity draw of the fluid within each production separation chamber to a rate less than six inches per second. ### Claim 4 (depends on 1) The apparatus of claim 1, wherein the second pipe is 316 stainless steel. ### Claim 5 (depends on 1) The apparatus of claim 1, wherein the first pipe is between two and three-eights inches to three and one-half inches in diameter. ### Claim 6 (depends on 1) The apparatus of claim 1, wherein the thief jet orifices of the second pipe in lower production separation chambers are larger than the thief jet orifices of the second pipe in higher production separation chambers. ### Claim 7 An apparatus for separating of gas from fluids in a wellbore, comprising: a first pipe in the wellbore and defining a wellbore annulus between the first pipe and the wellbore; a second pipe disposed in the first pipe and defining an inner annulus between the second pipe and the first pipe; a plurality of production separation chambers disposed in the first pipe; an orifice in an upper portion of each of the plurality of production separation chambers, the orifice opening into the wellbore annulus; and thief jet orifices in the second pipe, each thief jet orifice positioned near a bottom of a respective production separation chamber and opening into the inner annulus; and a tube extending through the plurality of production separation chambers, the tube having orifices within the plurality of production separation chambers and an upper opening disposed above the plurality of production separation chambers, wherein the thief jet orifices restrict flow of the fluid to remove gas bubbles from the fluid. ### Claim 8 (depends on 7) The apparatus of claim 7, wherein the thief jet orifices are configured to restrict liquids flowing into the second pipe at a rate less than a flow rate in which gas bubbles out of the fluid prior to entering the thief jet orifice. ### Claim 9 (depends on 7) The apparatus of claim 7, wherein each thief jet orifice is sized to restrict downward velocity draw of the fluid within each production separation chamber to a rate less than six inches per second. ### Claim 10 (depends on 7) The apparatus of claim 7, wherein the second pipe is 316 stainless steel. ### Claim 11 (depends on 7) The apparatus of claim 7, wherein the first pipe is between two and three-eights inches to three and one-half inches in diameter. ### Claim 12 (depends on 7) The apparatus of claim 7, wherein the thief jet orifices in lower production separation chambers are larger than the thief jet orifices in higher production separation chambers. ### Claim 13 (depends on 7) The apparatus of claim 7, wherein the upper opening of the tube is disposed in a pressure loss chamber. ### Claim 14 An apparatus for separating of gas from fluids in a wellbore, comprising: a first pipe configured to define a wellbore annulus between the first pipe and the wellbore; a second pipe disposed in the first pipe and defining an inner annulus between the first pipe and the second pipe; a plurality of production separation chambers disposed in the first pipe; an orifice disposed in an upper portion of each of the plurality of production separation chambers, the orifice opening into the wellbore annulus; thief jet orifices disposed in the second pipe, each thief jet orifice positioned near a bottom of a respective production separation chamber and opening into the inner annulus; and a pressure loss chamber above the plurality of production separation chambers, the pressure loss chamber having an opening to the wellbore and having another opening configured to receive gas from one or more of the plurality of production separation chambers; and wherein each of the thief jet orifices restricts flow of the fluid to remove gas bubbles from the fluid. ### Claim 15 (depends on 14) The apparatus of claim 14, wherein each of the thief jet orifices are sized to restrict liquids flowing into the second pipe at a rate less than a flow rate in which gas bubbles out of the fluid prior to entering the thief jet orifice. ### Claim 16 (depends on 14) The apparatus of claim 14, wherein each thief jet orifice is sized to restrict downward velocity draw of the fluid within each production separation chamber to a rate that is six inches per second. ### Claim 17 (depends on 14) The apparatus of claim 14, wherein the second pipe is 316 stainless steel. ### Claim 18 (depends on 14) The apparatus of claim 14, wherein the first pipe is between two and three-eights inches to three and one-half inches in diameter. ### Claim 19 (depends on 14) The apparatus of claim 14, wherein the thief jet orifices in lower production separation chambers are larger than the thief jet orifices in higher production separation chambers.