# US 12,222,268 B1 · Non-intrusive rheometer for use in well operations > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 12,222,268 B1 - Document ID: US12222268B1 - Status: Granted - Kind: B1 - Application number: 18/486,717 - Filed: 2023-10-13 - Published: 2025-01-23 - Granted: 2025-02-11 - Earliest claimed: 2023-07-20 - Assignees: Weatherford Technology Holdings, LLC - Applicants: Weatherford Technology Holdings, LLC - Inventors: Paul R. Northam; John E. Busteed - Web page: https://patentgrep.com/patent/US12222268B1 ## CPC - G01N 11/08: by measuring pressure required to produce a known flow - E21B 21/08: Controlling or monitoring pressure or flow of drilling fluid, e.g. automatic filling of boreholes, automatic control of bottom pressure (valve arrangements therefor E21B21/10) - E21B 44/00: Automatic control systems specially adapted for drilling operations, i.e. self-operating systems which function to carry out or modify a drilling operation without intervention of a human operator, e.g. computer-controlled drilling systems; Systems specially adapted for monitoring a plurality of drilling variables or conditions - G01N: INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES (measuring or testing apparatus or processes other than immunoassay, involving enzymes or microorganisms C12M, C12Q) - E21B: EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS ## Abstract A method of determining viscosity can include connecting a bypass flow passage in parallel with a main flow passage, connecting a mass flowmeter and a variable flow restrictor in the bypass flow passage, and connecting at least one viscometer to the bypass flow passage. A rheology measurement apparatus can include a bypass flow passage connected in parallel with a main flow passage, a mass flowmeter connected in the bypass flow passage, and a pipe viscometer connected in the bypass flow passage. Another bypass flow passage may be connected in parallel with the main flow passage, with another mass flowmeter connected in the second bypass flow passage. ## Claims ### Claim 1 A method of determining a viscosity of a fluid in real time as the fluid flows in a subterranean well, the method comprising: connecting a main flow passage between a pump and a tubular string extending into the well, so that the fluid flows from the pump to the tubular string through the main flow passage; connecting a flow restrictor in the main flow passage; connecting a bypass flow passage in parallel with the main flow passage, so that an inlet of the bypass flow passage is in communication with a first section of the main flow passage and an outlet of the bypass flow passage is in communication with a second section of the main flow passage downstream of the first section; connecting a mass flowmeter and a variable flow restrictor in the bypass flow passage, so that the fluid flows through the mass flowmeter and the variable flow restrictor; and connecting at least one viscometer to the bypass flow passage. ### Claim 2 (depends on 1) The method of claim 1, further comprising determining parameters of a Herschel Bulkley viscosity curve by measuring differential pressures across the mass flowmeter at relatively low flow rates of the fluid through the bypass flow passage, and measuring a viscosity of the fluid at a relatively high flow rate through the bypass flow passage. ### Claim 3 (depends on 2) The method of claim 2, in which the determining comprises operating the variable flow restrictor to permit flow of the fluid through the bypass flow passage at the relatively low and relatively high flow rates, without changing an output of the pump. ### Claim 4 (depends on 2) The method of claim 2, in which the determining comprises operating the variable flow restrictor to permit flow of the fluid through the bypass flow passage at the relatively low and relatively high flow rates, without changing a flow rate of the fluid from the pump to the tubular string. ### Claim 5 (depends on 2) The method of claim 2, in which the relatively low flow rates comprise first, second and third relatively low flow rates, and in which the measuring differential pressures comprises measuring the differential pressure across the mass flowmeter at the first relatively low flow rate, then measuring the differential pressure across the mass flowmeter at the second relatively low flow rate, then measuring the differential pressure across the mass flowmeter at the first relatively low flow rate, then measuring the differential pressure across the mass flowmeter at the third relatively low flow rate, and then measuring the differential pressure across the mass flowmeter at the first relatively low flow rate. ### Claim 6 (depends on 5) The method of claim 5, in which the connecting the flow restrictor in the main flow passage further comprises connecting the flow restrictor in the main flow passage between the inlet and the outlet of the bypass flow passage. ### Claim 7 (depends on 6) The method of claim 6, in which the measuring the pressure differentials across the mass flow meter comprises measuring the pressure differentials across the mass flow meter with a first differential pressure sensor, and further comprising measuring pressure differentials across the flow restrictor in the main flow passage with second and third differential pressure sensors. ### Claim 8 (depends on 7) The method of claim 7, further comprising evaluating measurement outputs of the first, second and third differential pressure sensors, and determining a flow rate of the fluid through the main flow passage while excluding from the determining of the flow rate any of the outputs of the first, second and third differential pressure sensors that are outside of a predicted range. ### Claim 9 (depends on 2) The method of claim 2, in which the fluid exhibits non-Newtonian behavior at the relatively low flow rates, and the fluid approaches pseudo-Newtonian or approximate Newtonian and/or Newtonian behavior at the relatively high flow rate. ### Claim 10 (depends on 2) The method of claim 2, in which at the relatively high flow rate a shear stress in the fluid approaches proportionality to a shear rate in the fluid. ### Claim 11 (depends on 1) The method of claim 1, in which the at least one viscometer comprises a first pipe viscometer, and the method further comprises measuring a differential pressure across a reduced flow area of the first pipe viscometer. ### Claim 12 (depends on 11) The method of claim 11, in which the at least one viscometer comprises a second pipe viscometer, and the method further comprises measuring a differential pressure across a reduced flow area of the second pipe viscometer, the flow area of the second pipe viscometer being less than the flow area of the first pipe viscometer. ### Claim 13 (depends on 1) The method of claim 1, further comprising controlling a well operation in response to outputs of the mass flowmeter and the viscometer. ### Claim 14 A rheology measurement apparatus for use with a subterranean well, the rheology measurement apparatus comprising: a main flow passage configured to connect between a pump and a tubular string extending into the well; a flow restrictor connected in the main flow passage; a first bypass flow passage connected in parallel with the main flow passage, an inlet of the first bypass flow passage in communication with a first section of the main flow passage, and an outlet of the first bypass flow passage in communication with a second section of the main flow passage downstream of the first section; a first mass flowmeter connected in the first bypass flow passage; and a first pipe viscometer connected in the first bypass flow passage. ### Claim 15 (depends on 14) The apparatus of claim 14, further comprising a second pipe viscometer connected in the first bypass flow passage, the second pipe viscometer having a flow area that is less than a flow area of the first pipe viscometer. ### Claim 16 (depends on 14) The apparatus of claim 14, further comprising a first variable flow restrictor connected in the first bypass flow passage. ### Claim 17 (depends on 16) The apparatus of claim 16, in which the flow restrictor connected in the main flow passage comprises a second variable flow restrictor connected in the main flow passage between the first and second main flow passage sections. ### Claim 18 (depends on 14) The apparatus of claim 14, further comprising: a second bypass flow passage connected in parallel with the main flow passage, an inlet of the second bypass flow passage in communication with the first section of the main flow passage, and an outlet of the second bypass flow passage in communication with the second section of the main flow passage; and a second mass flowmeter connected in the second bypass flow passage. ### Claim 19 (depends on 18) The apparatus of claim 18, further comprising a variable flow restrictor connected in the second bypass flow passage. ### Claim 20 (depends on 14) The apparatus of claim 14, in which the flow restrictor connected in the main flow passage comprises a variable flow restrictor connected in the main flow passage between the first and second sections of the main flow passage; and further comprising: a first differential pressure sensor configured to measure a differential pressure across the variable flow restrictor; a second differential pressure sensor configured to measure the differential pressure across the variable flow restrictor; and a control system configured to determine a flow rate of fluid flow through the main flow passage and to exclude from the flow rate determination any of the outputs of the first and second differential pressure sensors that are outside of a predicted range.