High density, low TCT monovalent brines and uses thereof
A method of using a suppression factor fluid during a well activity is provided. The method comprising the steps of introducing a suppression factor fluid into a wellbore, the suppression factor fluid comprising an untreated monovalent brine; and a suppression sugar alcohol, the suppression sugar alcohol in an amount operable to achieve a suppression factor, wherein a density upper limitation of the suppression factor fluid is greater than the density upper limitation of the monovalent brine; and completing the well activity in the wellbore, such that the suppression sugar alcohol inhibits crystallization during the well activity.
1. A method of using a suppression factor fluid during a well activity, the method comprising the steps of:
introducing a suppression factor fluid into a wellbore, the suppression factor fluid comprising:
50% by weight to 95% by weight of an untreated monovalent brine,
a suppression sugar alcohol, the suppression sugar alcohol in an amount operable to achieve a suppression factor of at least 1, wherein the suppression sugar alcohol is selected from the group consisting of sorbitol, xylitol, and combinations thereof,
wherein the suppression factor fluid has a density upper limitation that is greater than the density upper limitation of the untreated monovalent brine, and
a stabilization compound, wherein the stabilization compound is operable to inhibit degradation of the suppression sugar alcohol, wherein the stabilization compound comprises an amine base; and
completing the well activity in the wellbore, such that the suppression sugar alcohol inhibits crystallization during the well activity.
2. The method of claim 1 , wherein the well activity is selected from the group consisting of drilling activities, production activities, and completion activities.
3. The method of claim 1 , wherein the untreated monovalent brine is selected from the group consisting of a sodium bromide brine, a sodium chloride brine, a sodium formate brine, a potassium bromide brine, a potassium chloride brine, a potassium formate brine, a lithium bromide brine, a lithium chloride brine, cesium formate brine and combinations thereof.
4. The method of claim 1 , wherein the suppression factor is in the range between 1 and 10.
5. The method of claim 1 , wherein the true crystallization temperature of the suppression factor fluid is in the range between −40° F. and 70° F.
6. The method of claim 1 , wherein the amine base is selected from the group consisting of monoethanolamine (MEA), diethanolamine (DEA), triethanolamine (TEA), ethylenediamine (EDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), pentaethylenetetramine (PETA), pentaethylenehexamine (PEHA), aminoethylpiperazine (AEP), ethyleneamine E-100 (available from Huntsman Corporation), piperazine, diethylhydroxylamine (DEHA), diethylaminoethanol (DEAE), dimethylethanolamine (DMEA), methoxypropylamine (MOPA), morpholine, naminopropylmorpholine (APM), 4-[2-hydroxyethyl]morpholine, diglycolamine, N-[3-aminopropyl]diethanolamine, aminoethylethanolamine (AEEA), and combinations thereof.
7. A method of using a suppression factor fluid during a well activity, the method comprising the steps of:
introducing a suppression factor fluid into a wellbore, the suppression factor fluid comprising:
50% by weight to 94% by weight of a monovalent brine,
6% by weight on a dry weight basis to 50% by weight on a dry weight basis of a suppression sugar alcohol, wherein the suppression sugar alcohol is selected from the group consisting of sorbitol, xylitol, and combinations thereof, and
a stabilization compound, wherein the stabilization compound is operable to inhibit degradation of the suppression sugar alcohol, wherein the stabilization compound comprises an amine base; and
completing the well activity in the wellbore, such that the suppression sugar alcohol inhibits crystallization during the well activity.
8. The method of claim 7 , wherein the well activity is selected from the group consisting of drilling activities, production activities, and completion activities.
9. The method of claim 7 , wherein the untreated monovalent brine is selected from the group consisting of a sodium bromide brine, a sodium chloride brine, a sodium formate brine, a potassium bromide brine, a potassium chloride brine, a potassium formate brine, a lithium bromide brine, a lithium chloride brine, cesium formate brine and combinations thereof.
10. The method of claim 7 , wherein the suppression factor is in the range between 0.5 and 10.
11. The method of claim 7 , wherein the amine base is selected from the group consisting of monoethanolamine (MEA), diethanolamine (DEA), triethanolamine (TEA), ethylenediamine (EDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), pentaethylenetetramine (PETA), pentaethylenehexamine (PEHA), aminoethylpiperazine (AEP), ethyleneamine E-100 (available from Huntsman Corporation), piperazine, diethylhydroxylamine (DEHA), diethylaminoethanol (DEAE), dimethylethanolamine (DMEA), methoxypropylamine (MOPA), morpholine, naminopropylmorpholine (APM), 4-[2-hydroxyethyl]morpholine, diglycolamine, N-[3-aminopropyl]diethanolamine, aminoethylethanolamine (AEEA), and combinations thereof.
12. The method of claim 7 , wherein the true crystallization temperature of the suppression factor fluid is in the range between −40° F. and 70° F.