Reduction of breakdown pressure by filter cake removal using thermochemicals
A method for the simultaneous removal of filter cake from a wellbore and fracturing of the wellbore using a mixture including a chelating agent and a thermochemical. The method including feeding a mixture into the wellbore, contacting the filter cake with the mixture, reacting the chelating agent and the thermochemical to produce heat and pressure, removing the filter cake from the wellbore, and creating microfractures in the wellbore using pressure produced from the reacting.
1. A method for the simultaneous removal of filter cake from a wellbore and fracturing of the wellbore, the method comprising:
feeding a mixture into the wellbore, the mixture consisting of:
a chelating agent;
a thermochemical, wherein the thermochemical comprises ammonium persulfate; and
a water- or oil-based fluid;
contacting the filter cake with the mixture;
reacting the chelating agent and the thermochemical to produce heat and pressure;
removing the filter cake from the wellbore; and
creating microfractures in the wellbore using pressure produced from the reacting.
2. The method as claimed in claim 1 , wherein the chelating agent is one or more selected from the group consisting of ethylenediaminetetraacetic acid (EDTA); diethylenetriaminepentaacetic acid (DTPA); N(hydroxyethyl)ethylenediaminetriacetic acid (HEDTA); nitrilotriacetic acid (NTA); ethylenediamine-N,N′-disuccinic acid (EDDS); L-glutamic acid N,N-diacetic acid (GLDA); and methylglycinediacetic acid (MGDA); 6-[[16-[(6-carboxypyridin-2-yl)methyl]-1,4,10,13-tetraoxa-7,16-diazacyclooctadec-7-yl]methyl]-4-isothiocyanatopyridine-2-carboxylic acid (MACROPA), hydrochloric acid, formic acid, acetic acid, and citric acid.
3. The method of claim 2 , wherein the chelating agent has a concentration of 0.2M to 0.8M.
4. The method of claim 3 , wherein the chelating agent is DTPA.
5. The method as claimed in claim 1 , wherein the thermochemical further comprises one or more selected from the group consisting of ammonium chloride and sodium nitrate.
6. The method of claim 5 , wherein the thermochemical is ammonium persulfate and sodium nitrate.
7. The method of claim 6 , wherein the ratio of ammonium persulfate to sodium nitrate is from 1:4 to 4:1 based on %/wt.
8. The method of claim 1 , wherein the filter cake is a water-based filter cake or an oil-based filter cake.
9. The method of claim 1 , further comprising feeding the chelating agent and the thermochemical at a chelating agent to thermochemical molar ratio of 2:1 to 1:2.
10. The method of claim 1 , wherein the chelating agent and the thermochemical are fed separately into the wellbore.
11. The method of claim 1 , wherein the removal of filter cake from the wellbore results in a reduction of a breakdown pressure by 85% compared to the breakdown pressure without a formation of filter cake on the wellbore.