US 12,215,276 B2
Ph control in fluid treatment
Sujeewa S. Palayangoda, San Ramon, CA (US); Kerry Kennedy Spilker, San Ramon, CA (US); Sumitra Subrahmanyan, San Ramon, CA (US); Gayani W. Pinnawala, San Ramon, CA (US); Sophany Thach, San Ramon, CA (US); Gregory A. Winslow, San Ramon, CA (US); Dennis Arun Alexis, San Ramon, CA (US); Harold Charles Linnemeyer, San Ramon, CA (US); Timothy P. Theriot, San Ramon, CA (US); Les Leszek Jackowski, San Ramon, CA (US); and Francesca Cibotti, San Ramon, CA (US)
Assigned to CHEVRON U.S.A. INC., San Ramon, CA (US)
Filed by CHEVRON U.S.A. INC., San Ramon, CA (US)
Filed on Jan. 27, 2023, as Appl. No. 18/160,710.
Application 18/160,710 is a continuation of application No. 17/287,734, granted, now 11,591,893, previously published as PCT/US2019/057462, filed on Oct. 22, 2019.
Claims priority of provisional application 62/748,897, filed on Oct. 22, 2018.
Prior Publication US 2023/0323193 A1, Oct. 12, 2023
This patent is subject to a terminal disclaimer.
Int. Cl. C09K 8/588 (2006.01); C09K 8/03 (2006.01); E21B 21/06 (2006.01); E21B 43/38 (2006.01)
CPC C09K 8/588 (2013.01) [C09K 8/032 (2013.01); E21B 21/068 (2013.01); E21B 43/385 (2013.01); C09K 2208/26 (2013.01); C09K 2208/28 (2013.01)] 20 Claims
OG exemplary drawing
 
1. A system of treating fluid, the system comprising:
a production wellbore for producing fluid comprising hydrocarbons, water, and polymer from a hydrocarbon-bearing formation;
a first injection apparatus for adding a concentration of a viscosity reducer to the fluid to degrade the polymer present in the fluid;
a second injection apparatus for adding a concentration of a neutralizer to the fluid to neutralize the viscosity reducer in the fluid; and
surface fluid processing equipment for separating the hydrocarbons from the fluid; wherein:
a pH of the viscosity reducer is lowered to a pH of 7 or less;
the addition of the concentration of the viscosity reducer is in a sufficient quantity to allow for complete chemical degradation of the polymer prior to the addition of the concentration of the neutralizer in the fluid such that excess viscosity reducer is present in the fluid; and
the addition of the concentration of the neutralizer is sufficiently upstream of any of the surface fluid processing equipment to allow for complete neutralization of the excess viscosity reducer such that excess neutralizer is present in the fluid prior to the fluid reaching any of the surface fluid processing equipment,
wherein the concentration of the viscosity reducer is added at a first location, and wherein the concentration of the neutralizer is added at a second location.