Table 2. Detailed Experimental Conditions for Performance Evaluation of the Formulation as Corrosion Inhibitors Using the HPHT Autoclave for Different Applications.
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operational conditions |
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|---|---|---|---|---|---|---|---|---|---|
| field condition application | water geochemical analysis, mg/L | pressure (Psig) | temp. (°C) | gas composition, mole % | time (h) | RPM | KHCI conc. (ppm) | ||
| gas production test-1 | Cl | 607 | 1600 | 90 | CH4 | 79.6 | 24 | 500 | 2500 and 10,000 |
| Na | 393 | CO2 | 9.2 | ||||||
| acetic acid | 500 | N2 | 7.2 | ||||||
| formic acid | 250 | H2S | 2.3 | ||||||
| TDS | 1750 | ethane | 1.4 | ||||||
| pH | 6.5 | propane | 0.2 | ||||||
| n-butane | 0.1 | ||||||||
| sour crude processing | Na | 29,500 | 250 | 83 | CO2 | 7 | 24 | 400 | 20 & 100 |
| Ca | 8210 | N2 | 90 | ||||||
| Mg | 1080 | H2S | 3 | ||||||
| Cl | 61,800 | ||||||||
| SO4 | 1300 | ||||||||
| HCO3 | 662 | ||||||||
| TDS | 102,552 | ||||||||
| pH | 6.6 | ||||||||
| gas production test-2 | Na | 29,500 | 1600 | 90 | CH4 | 79.6 | 42 | 500 | 2500 |
| Cl | 61,800 | CO2 | 9.2 | ||||||
| acetic acid | 500 | N2 | 7.2 | ||||||
| formic acid | 250 | H2S | 2.3 | ||||||
| TDS | 1750 | ethane | 1.4 | ||||||
| pH | 6.6 | propane | 0.2 | ||||||
| n-butane | 0.1 | ||||||||