Introduction
1. Drilling characteristics and challenges in the Antarctic region
1.1. Drilling characteristics in the Antarctic region
Table 1. Mechanical properties of rock under frozen and ablation states [16] |
| Lithology | Frozen state | Ablation state | ||||
|---|---|---|---|---|---|---|
| Internal friction coefficient | Cohesion force/MPa | Elastic modulus/MPa | Internal friction coefficient | Cohesion force/MPa | Elastic modulus/MPa | |
| Granite, diorite, andesite | 0.78 | 0.60 | 200 | 0.75 | 0.30 | 110 |
| Granite*, diorite*, andesite * | 0.73 | 0.35 | 140 | 0.70 | 0.15 | 90 |
| Gneiss | 0.84 | 0.65 | 330 | 0.80 | 0.35 | 180 |
| Limestone | 0.67 | 0.30 | 120 | 0.65 | 0.20 | 80 |
| Sandstone | 0.23 | 0.40 | 160 | 0.70 | 0.25 | 100 |
| Sandstone * | 0.68 | 0.24 | 120 | 0.65 | 0.15 | 75 |
| Clay*, shale | 0.62 | 0.20 | 100 | 0.60 | 0.10 | 50 |
| Clay, shale * | 0.57 | 0.15 | 40 | 0.55 | 0.07 | 20 |
Note: *—The water content of the sample was increased during sample preparation and then frozen to increase the ice content of the sample. |
1.2. Drilling challenges in the Antarctic region
2. Performance requirements of low-temperature drilling fluids in the Antarctic region
Table 2. Primary performance of low-temperature drilling fluids in the Antarctic region [20] |
| Performance | Impacts on drilling | Requirements for drilling fluids |
|---|---|---|
| Density | Improper density can lead to wellbore instability and even stuck drill pipe | Density equal to or slightly higher than the density of ice layer at -55 °C |
| Viscosity | High viscosity reduces the tripping speed of drilling tools, increases total drilling time while increasing drilling costs | Viscosity below 23.75 mPa·s at -55 °C |
| Frost resistance | Freezing point above -55 °C may result in drilling fluid to freeze during storing or circulation | Freezing point lower than -55 °C |
| Stability | Unstable chemical properties can lead to changes in drilling fluid performance during storage, transportation and operation | Chemically stable |
| Compatibility with polymers and metals | Corrosion can cause damage to drill pipe, cables or other drilling tools | Non-corrosive |
| Volatility and flammability | High volatility pollutes work environment, clothes, ice cores, while low ignition point brings fire risk | Low volatility, high ignition point |
| Water (ice) solubility | Water solubility can lead to dissolution of well wall and formation of ice mud, even stuck drill pipe | Water-insoluble |
| Toxicity | Toxicity may pose a threat to the health of wellsite personnel | Non-toxic or low toxicity |
| Environmental performance | Poor environmental friendliness leads to pollution to environment | Environmentally friendly |
| Economy | High prices lead to higher drilling costs | Low price, easily available |
3. Research progress of low-temperature drilling fluids in the Antarctic region
3.1. Petroleum-based drilling fluids
Table 3. Primary performance parameters of solvents ExxsolTM D series and IsoparTM K [31] |
| Solvent | Density at 15 °C/ (kg•m-3) | Viscosity at 20 °C/ (mPa•s) | Pour point/°C | Flash point/°C | Mass fraction of aromatic hydrocarbon/% | Aniline point/°C | Evaporation rate/% |
|---|---|---|---|---|---|---|---|
| ExxolTM D30 | 762 | 0.572 | <-55 | 29 | 0.001 | 64 | 44.0 |
| ExxolTM D40 | 775 | 0.744 | <-55 | 42 | 0.003 | 67 | 14.0 |
| ExxolTM D60 | 792 | 1.022 | <-55 | 63 | 0.060 | 70 | 3.4 |
| IsoparTM K | 763 | 1.404 | <-18 | 54 | 0.003 | 83 | 6.0 |
Table 4. Physicochemical properties of weighting agents with halogenated hydrocarbons used for drilling in the Antarctic [20, 31] |
| Halogenated hydrocarbons weighting agents | Density at 20 °C/ (kg•m-3) | Viscosity at 25 °C/ (mPa•s) | Ozone consumption coefficient | Greenhouse coefficient |
|---|---|---|---|---|
| C2HCl3 | 1464 | 0.791 | 1.00 | 4850 |
| C2Cl4 | 1625 | 1.363 | 1.00 | 4700 |
| CFC-11 | 1487 | 0.625 | 1.00 | 4600 |
| CFC-113 | 1575 | 1.024 | 0.90 | 5000 |
| HCFC-141b | 1240 | 0.516 | 0.11 | 630 |
3.2. Alcohol-based drilling fluid
3.3. Ester-based drilling fluid
Table 5. Physical parameters of esters with low molecular weight [49] |
| Description | CAS No. | Molecular formula | Relative molecular mass | Freezing point/°C | Boiling point/ °C | Density at 20 °C/ (kg•m-3) | Viscosity at 25 °C/ (mPa•s) | Vapor pressure/ kPa | Flash point/ °C | Mass concentration in water at 20 °C/% |
|---|---|---|---|---|---|---|---|---|---|---|
| Butyl acetate | 123-86-4 | C6H12O2 | 116 | -76.8 | 126.1 | 882.4 | 0.73 | 1.20 | 22.0 | Slightly soluble |
| Ethyl butyrate | 105-54-4 | C6H12O2 | 116 | -93.3 | 121.3 | 879.0 | 0.71 | 1.51 | 25.0 | 0.7 |
| Propyl propionate | 106-36-5 | C6H12O2 | 116 | -76.0 | 122.4 | 881.0 | 0.70 | 1.43 | 24.4 | 0.5 |
| Butyl butyrate | 109-21-7 | C8H16O2 | 144 | -91.5 | 166.6 | 869.0 | 1.01 | 0.24 | 53.0 | Insoluble |
| N-amyl butyrate | 540-18-1 | C9H18O2 | 158 | -73.2 | 186.4 | 870.0 | 1.20 | 0.08 | 57.0 | Soluble |
| N-hexyl acetate | 142-92-7 | C8H16O2 | 144 | -80.9 | 171.5 | 871.8 | 1.10 | 0.19 | 43.0 | 0.4 |
Table 6. Physical properties of ESTISOLTM esters [31] |
| ESTISOLTM classification | Raw material source | Viscosity at 25 °C/ (mPa•s) | Density at 20 °C/ (kg•m-3) | Pour point/°C | Flash point/°C | Boiling point/°C |
|---|---|---|---|---|---|---|
| 140 | Synthesis | 1.3 | 870 | -93 | 75 | 199 |
| 165 | Synthesis | 3.0 | 1100 | <-30 | 81 | 180-190 |
| 240 | Vegetable | 4.0 | 855 | <-50 | 730 | 250-290 |
| F2887 | Synthesis | 7.0 | 1083 | <-10 | 167 | >280 |