Evaporator for SAGD process
A closed loop contaminant control system for an evaporative water purification process at an oil recovery facility includes an evaporator having a water inlet, a distilled water discharge, and an oil and brine water discharge. A sump in the evaporator is divided by an oil skimming weir into a main sump and a blowdown sump, with the oil and brine water discharge located proximate the blowdown sump and the steam discharge located above the oil and brine discharge. A distillate tank receives distilled water from the evaporator and discharges the distilled water. The distillate tank has a level controller, other controllers provided for the system include a distilled water flow meter, a blowdown flow meter, a cycle controller, a total flow controller, a hardness controller, and a silica controller.
1. A process for evaporative water purification in an oil recovery facility, comprising:
providing an evaporator, including a sump, and a weir;
employing the weir to divide the sump into a main sump and a blowdown sump;
flowing a liquid including brine and oil in a continuous manner over the weir from the main sump into the blowdown sump in order to retard a foaming of the oil in the sump;
discharging brine from the main sump and circulating the brine to the evaporator;
discharging oil from the blowdown sump and removing the oil from the system; and
controlling a level of liquid in the blowdown sump.
2. The process of claim 1 further comprising the step of continuously discharging the oil from the blowdown sump.
3. The process of claim 1 further comprising the step of controlling a silica solubility in a circulating liquid.
4. The process of claim 3 wherein the step of controlling silica solubility includes adjusting a pH of the circulating liquid.
5. The process of claim 4 wherein the pH is adjusted by adding at least one chemical solvent to the circulating liquid.
6. The process of claim 1 further comprising controlling a hardness of a circulating liquid.
7. The process of claim 6 wherein the step of controlling the hardness of the circulating liquid includes adjusting a brine blow down rate.
8. The process of claim 2 further comprising the step of continuously removing the oil from the system.
9. An evaporative water purification process utilized in an oil recovery facility, comprising:
providing an evaporator, including a sump, and a weir;
employing the weir to divide the sump into a main sump portion a blowdown sump portion;
flowing in a continuous manner a liquid including brine and oil over the weir from the main sump portion into the blowdown sump portion, thereby retarding a foaming of the oil in the liquid;
discharging brine from the main sump portion and circulating the brine to the evaporator;
discharging oil from the blowdown sump portion;
removing the oil from the system; and,
discharging a steam from the evaporator into a distillate drum.
10. The process of claim 9 further comprising the step of continuously discharging the oil from the blowdown sump.
11. The process of claim 10 further comprising the step of continuously removing the oil from the system.
12. The process of claim 9 further comprising the step of controlling a silica solubility in the brine.
13. The process of claim 12 wherein the step of controlling silica solubility includes adjusting a pH of the brine.
14. The process of claim 8 further comprising calculating a ratio between a distilled water flow from the distillate drum and a blowdown flow from the blowdown sump portion.
15. The process of claim 9 further comprising controlling a hardness of the brine.
16. The process of claim 15 wherein the step of controlling the hardness of the brine includes adjusting a brine blow down rate.
17. A process for evaporative water purification in an oil recovery facility, comprising:
providing an evaporator, including a sump, and a weir;
employing the weir to divide the sump into a main sump portion and a blowdown sump portion;
flowing a liquid including brine and oil over the weir from the main sump portion into the blowdown sump portion;
discharging brine from the main sump portion and circulating the brine to the evaporator;
discharging oil from the blowdown sump portion;
allowing the liquid in the main sump portion to flow into the blowdown sump portion in an uninterrupted manner via a v-shaped notch disposed in the weir in order to retard a foaming of the oil in the liquid;
removing the oil from the system;
measuring a flow of the liquid from the blowdown sump portion; and
discharging a steam from the evaporator.
18. The process of claim 17 further comprising the step of continuously discharging the oil from the blowdown sump portion.
19. The process of claim 18 further comprising continuously removing the oil from the system.