Method and apparatus for removal of particulate matter from a multiphase stream
A system for removing particulate matter from a multiphase stream comprising gas, liquid and the particulate matter. The system comprises a first vessel for receiving the multiphase stream and separating a majority of gas from the multiphase stream and collecting a slurry of liquid and particulate matter; a second vessel for receiving the slurry and causing separation of the particulate matter from the liquid and for generating a pressure head of liquid against the particulate matter; a third vessel for receiving the particulate matter from the second vessel and collecting the particulate matter until a pre-determined mass or volume of particulate matter is collected; and an outlet in the third vessel for conveying the particulate matter out of the third vessel.
1. A method for removing a particulate matter from a multiphase stream comprising a gas, a liquid and the particulate matter, the method comprising:
a) conveying the multiphase stream to a first vessel; separating a majority of the gas from the multiphase stream and removing the separated gas from the first vessel; and collecting a slurry of the liquid and the particulate matter from the multiphase stream in the first vessel;
b) conveying the slurry to a second vessel and separating the particulate matter from the liquid by generating a pressure head of the liquid above the particulate matter to cause the particulate matter to settle in the bottom of the second vessel and compress the particulate matter to force out entrained liquid; and
c) conveying the particulate matter out of the second vessel,
wherein step a) occurs continuously, and wherein step b) is halted when step c) occurs.
2. The method of claim 1 , further comprising:
increasing the pressure head by inclusion of a pressure head element in liquid flow communication with the second vessel via a first conduit connecting the pressure head element with the second vessel; and
controlling fluid flow between the second vessel and the pressure head element utilizing a valve between the second vessel and the pressure head element.
3. The method of claim 1 , wherein in step c), the particulate matter is conveyed to a third vessel, and steps a) to c) are repeated until a pre-determined volume of the particulate matter is contained in the third vessel, after which the particulate matter is conveyed out of the third vessel.
4. The method of claim 1 , wherein the first vessel is spherical and the multiphase stream is diverted in a downward direction in the first vessel.
5. The method of claim 1 , wherein the particulate matter comprises sand and the multiphase stream is production from a hydraulically fractured well.
6. The method of claim 1 , wherein in step a), the multiphase fluid is diverted into a plurality of streams flowing downwards in the first vessel.
7. The method of claim 1 , wherein in step a), the multiphase stream is conveyed into the first vessel to impact a curved interior wall of the first vessel.
8. The method of claim 1 , further comprising measuring the particulate matter settled in the second vessel and upon reaching a predetermined threshold measurement, conveying the particulate matter out of the second vessel.
9. The method of claim 1 , wherein the method does not rely on cyclonic flow to remove the particulate matter from the multiphase stream.
10. A method for removing a particulate matter from a multiphase stream comprising a gas, a liquid and the particulate matter, the method comprising:
conveying the multiphase stream to a first vessel, separating a majority of the gas from the multiphase stream and removing the separated gas from the first vessel;
collecting a slurry of the liquid and the particulate matter from the multiphase stream in the first vessel;
conveying the slurry to a second vessel and separating the particulate matter from the liquid by generating a pressure head of the liquid above the particulate matter to cause the particulate matter to settle in the bottom of the second vessel and compress the particulate matter to force out entrained liquid, wherein the pressure head is increased by inclusion of a pressure head element in liquid flow communication with the second vessel via a first conduit connecting the pressure head element with the second vessel;
controlling fluid flow between the second vessel and the pressure head element utilizing a valve between the second vessel and the pressure head element; and
conveying the particulate matter out of the second vessel.
11. The method of claim 10 , wherein the pressure head element is positioned to contain the liquid at a higher point than the liquid in the second vessel.
12. The method of claim 10 , further comprising:
setting the valve to allow fluid flow during a first phase of operations when the particulate matter is accumulating within the second vessel; and
setting the valve to prevent fluid flow during a second phase of operations when the particulate matter is being conveyed out of the second vessel.
13. The method of claim 10 , wherein the pressure head element is a pipe having an inner diameter greater than an inner diameter of the conduit, and a height that is higher than a maximum height of the second vessel.
14. The method of claim 10 , wherein the multiphase fluid is diverted into a plurality of streams flowing downwards from the first vessel.
15. A method for removing a particulate matter from a multiphase stream comprising a gas, a liquid and the particulate matter, the method comprising:
a) conveying the multiphase stream to a first vessel, wherein the multiphase fluid is diverted into a plurality of streams flowing downwards from the first vessel; separating a majority of the gas from the multiphase stream and removing the separated gas from the first vessel; and collecting a slurry of the liquid and the particulate matter from the multiphase stream in the first vessel;
b) conveying the slurry to a second vessel and separating the particulate matter from the liquid by generating a pressure head of the liquid above the particulate matter to cause the particulate matter to settle in the bottom of the second vessel and compress the particulate matter to force out entrained liquid; and
c) conveying the particulate matter out of the second vessel.
16. The method of claim 15 , wherein in step a), the multiphase stream is conveyed into the first vessel to impact a splitter wall that divides the multiphase stream into the plurality of streams.
17. The method of claim 16 , wherein the plurality of streams are directed by the splitter wall against a backplate angled to direct the flow downwards.
18. The method of claim 17 , wherein the plurality of streams are blocked from flowing upwards by an upper plate.
19. The method of claim 15 , wherein in step a), the multiphase stream is conveyed into the first vessel to impact a curved interior wall of the first vessel.
20. The method of claim 15 , wherein the first vessel is spherical and the multiphase stream is diverted in a downward direction in the first vessel.