Agitating – Mortar mixer type – Methods
Reexamination Certificate
2000-11-29
2002-12-10
Soohoo, Tony G. (Department: 1723)
Agitating
Mortar mixer type
Methods
C366S017000, C366S018000, C366S136000, C366S141000, C366S153100
Reexamination Certificate
active
06491421
ABSTRACT:
FIELD OF THE INVENTION
The present invention relates to a system for mixing fluids containing solid and liquid materials such as cement. In particular the invention provides a system for the continuous mixing of cements or other fluids used in the drilling, completion or stimulation of boreholes such as oil or gas wells.
BACKGROUND OF THE INVENTION
When a well such as an oil or gas well has been drilled, it is often desired to isolate the various producing zones form each other or from the well itself in order to stabilise the well or prevent fluid communication between the zones or shut off unwanted fluid production such as water. This isolation is typically achieved by installing a tubular casing in the well and filling the annulus between the outside of the casing and the wall of the well (the formation) with cement. The cement is usually placed in the annulus by pumping a slurry of the cement down the casing such that it exits at the bottom of the well and passes back up the outside of the casing to fill the annulus. While it is possible to mix the cement as a batch prior to pumping into the well, it has become desirable to effect continuous mixing of the cement slurry at the surface just prior to pumping into the well. This has been found to provide better control of cement properties and more efficient use of materials.
The cement slurries used in such operations comprise a mixture of dry and liquid materials. The liquid phase is typically water and so is readily available and cheap. The solid materials define the slurry and cement properties when added to the water and mixed, the amount of solid materials in the slurry being important. Since the liquid phase is constant, the amount of solid material added is usually monitored by measuring the density of the slurry and maintaining this at the desired level by controlling the amount of the solid material being added.
FIG. 1
shows a schematic diagram of a prior art mixing system. In the system of
FIG. 1
, mix water is pumped from a feed supply
10
via a pump
12
to a mixer
14
which feeds into a mixing tub
16
. Solid materials are delivered to the mixer
14
from a surge can
18
via a flow control valve
20
and are carried into the mixing tub
16
with the mix water. The contents of the mixing tub
16
are recirculated through a recirculation pipe
22
and pump
24
to the mixer
14
. The recirculation pipe
22
also includes a densitometer
26
which provides a measurement of the density of the slurry in the mixing tub
16
. An output
28
is provided for slurry to be fed from the mixing tub
16
to further pumps (not shown) for pumping into the well. Control of the slurry mixture is achieved by controlling the density in the mixing tub
16
as provided by the densitometer
26
by addition of solid material to stay at a predetermined level for the slurry desired to be pumped. The densitometer
26
is typically a non-radioactive device such as a Coriolis meter.
While this system is effective for slurries using materials of much higher density than water, it is not effective for slurries using low density solid materials, especially when the density of the solids is close to that of water. In such cases, a density measurement is not sensitive enough to control the amounts of solid material added to the necessary accuracy.
The present invention seeks to provide a mixing system which avoid the problem of density measurement described above.
SUMMARY OF THE INVENTION
In its broadest aspect, the present invention comprises using a measurement of the solid fraction of a fluid as it is being mixed to determine the ratio of the solid and liquid components added to the slurry.
The invention is particularly applicable to the mixing of borehole cement slurries, in which case, solids fraction is determined as (slurry vol−water vol)/slurry vol. An alternative but related parameter is porosity, determined as water vol/slurry vol (porosity+solids fraction=1).
A system for mixing cement in accordance with the invention comprises a water supply including a flow meter; a solid material supply; a mixer which receives the water and solid materials and includes an output for delivering materials from the mixer to a delivery system; a device for measuring the amount of material in the mixer; and a flow meter in the output; wherein measurements from the flow meters and the device for measuring the amount of material in the mixer are used to control the amount of solid material added to the mixer.
The flow meters can be mass flow meters or volumetric flow meters. Any suitable form of meter can be used, for example Coriolis meters or electromagnetic meters.
The mixer will typically include a tank or tub, in which case the device for measuring the amount of material in the mixer can be a level sensor. Such a level sensor is preferably a time domain reflectometry- or radar-type device although acoustic or float devices can also be used. It is preferred to mount such a device in an arrangement for damping transient fluctuations in the tank level, for example in an arrangement of concentric slotted tubes. An alternative or additional form of sensor can be a load cell which can be used to indicate the weight of the tank, or a pressure sensor.
Where the mixer includes some form of recirculation of the slurry through the tank, it is important that the output flow meter is downstream of this recirculation.
Where the solid materials comprise cement and other solid additives added separately to the mixer, separate flow meters can also be provided for each separate supply of additives.
In its simplest form, the measurement of solid fraction is used as a guide for the operator to add solids, particularly cement, to the slurry as it is mixed. In more advanced versions, the calculation of solids fraction is used to control the addition of solids directly by means of an automatic control system.
REFERENCES:
patent: 3379421 (1968-04-01), Putman
patent: 4327759 (1982-05-01), Millis
patent: 4353482 (1982-10-01), Tomlinson et al.
patent: 4397561 (1983-08-01), Strong et al.
patent: 4475818 (1984-10-01), Bialkowski
patent: 4490044 (1984-12-01), Saito et al.
patent: 4764019 (1988-08-01), Kaminski et al.
patent: 4779186 (1988-10-01), Handke et al.
patent: 4863277 (1989-09-01), Neal et al.
patent: 4881819 (1989-11-01), Blees
patent: 4886367 (1989-12-01), Bragg et al.
patent: 4896968 (1990-01-01), Baillie
patent: 5018868 (1991-05-01), Baillie
patent: 5570743 (1996-11-01), Padgett et al.
patent: 5590976 (1997-01-01), Kilheffer et al.
patent: 5775803 (1998-07-01), Montgomery et al.
patent: 195 12 416 (1995-04-01), None
patent: 0 403 283 (1990-12-01), None
Rondeau Joel
Vigneaux Pierre
Jeffery Brigitte
Menes Catherine
Schlather Stephen F.
Schlumberger Technology Corporation
Soohoo Tony G.
LandOfFree
Fluid mixing system does not yet have a rating. At this time, there are no reviews or comments for this patent.
If you have personal experience with Fluid mixing system, we encourage you to share that experience with our LandOfFree.com community. Your opinion is very important and Fluid mixing system will most certainly appreciate the feedback.
Profile ID: LFUS-PAI-O-2973486