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Patent 2783392 Summary

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(12) Patent Application: (11) CA 2783392
(54) English Title: OIL-GAS WELL STRUCTURE FOR FACILITATING EXTRACTING A DOWNHOLE FILTER STRING AND METHOD FOR EXTRACTING THE STRING
(54) French Title: STRUCTURE DE PUITS DE PETROLE ET DE GAZ FACILITANT L'EXTRACTION D'UNE RAME DE FILTRE DE FOND DE PUITS ET PROCEDE D'EXTRACTION DE RAME
Status: Dead
Bibliographic Data
(51) International Patent Classification (IPC):
  • E21B 43/10 (2006.01)
  • E21B 43/02 (2006.01)
(72) Inventors :
  • PEI, BAILIN (China)
  • FANG, NA (China)
(73) Owners :
  • ANTON BAILIN OILFIELD TECHNOLOGIES (BEIJING) CO., LTD. (China)
(71) Applicants :
  • ANTON OILFIELD SERVICES (GROUP) LTD. (China)
(74) Agent: RIDOUT & MAYBEE LLP
(74) Associate agent:
(45) Issued:
(86) PCT Filing Date: 2010-12-10
(87) Open to Public Inspection: 2011-06-16
Examination requested: 2013-11-21
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): Yes
(86) PCT Filing Number: PCT/CN2010/002015
(87) International Publication Number: WO2011/069340
(85) National Entry: 2012-06-06

(30) Application Priority Data:
Application No. Country/Territory Date
200910250794.6 China 2009-12-11

Abstracts

English Abstract

An oil-gas well structure for facilitating extracting a downhole filter string and a method for extracting the downhole filter string from the oil-gas well are provided. The oil-gas well structure includes a borehole wall (1) of the oil-gas well and a downhole filter string (2) lowered into the oil-gas well. The end of the downhole filter string (2) close to the wellhead is fixedly connected with the borehole wall (1). An annulus is formed between the downhole filter string (2) and the borehole wall (1), and the annulus is filled with ultra light particles, wherein, the density of ultra light particles approaches to or is equal to the density of the carrier fluid which carries the ultra light particles. The method for extracting the downhole filter string includes the following steps: 1) establishing channels; 2) injecting the carrier fluid for ultra light particles so as to remove the ultra light particles from the annulus completely; 3) extracting the downhole filter string. The structure can conveniently extract the downhole filter string from the oil-gas well, thus facilitating the replacement and maintenance of the downhole filter string and the parameter regulation of the flow-control filter.


French Abstract

L'invention concerne une structure de puits de pétrole et de gaz facilitant l'extraction d'une rame de filtre de fond de puits, ainsi qu'un procédé d'extraction de la rame de filtre de fond de puits hors du puits de pétrole et de gaz. La structure de puits de pétrole et de gaz comprend une paroi (1) de trou de forage du puits de pétrole et de gaz, et une rame de filtre de fond de puits (2) abaissée dans le puits de pétrole et de gaz. L'extrémité de la rame de filtre de fond de puits (2) à proximité de la tête de puits est connectée rigidement à la paroi (1) du trou de forage. Un anneau est formé entre la rame de filtre de fond de puits (2) et la paroi (1) du trou de forage, et l'anneau est rempli de particules ultralégères dont la densité est proche de ou égale à la densité du fluide porteur qui transporte les particules ultralégères. Le procédé d'extraction de la rame de filtre de fond de puits comprend les étapes suivantes : 1) établir des canaux ; 2) injecter un fluide porteur de particules ultralégères afin d'éliminer complètement les particules ultralégère de l'anneau ; 3) extraire la rame de filtre de fond de puits. La structure permet d'extraire de façon pratique la rame de filtre de fond de puits hors du puits de pétrole et de gaz, ce qui facilite le remplacement et l'entretien de la rame de filtre de fond de puits ainsi que l'ajustement des paramètres du filtre de commande de débit.

Claims

Note: Claims are shown in the official language in which they were submitted.



What is claimed is:

1. An oil-gas well structure for facilitating extracting a downhole filter
string,
comprising a borehole wall and a downhole filter string run into the oil-gas
well,
one end of the downhole filter string close to the wellhead being an upper end
of the filter string which end is fixedly connected with the borehole wall, an
annulus being formed between the downhole filter string and the borehole wall;
characterized in that: the annulus between the downhole filter string and the
borehole wall is filled with ultra light particles whose density approaches or
is
equal to the density of a carrier fluid for carrying the ultra light
particles, the
carrier fluid for carrying the ultra light particles is a liquid for carrying
and
conveying the ultra light particles into the annulus or backwashing and
conveying the ultra light particles out of the annulus.

2. The oil-gas well structure for facilitating extracting a downhole filter
string
according to claim 1, characterized in that: the ultra light particles are
particles
which have an average particle diameter of 0.05-1.2 mm, and a real density of
0.7-1.3 g/cm3.

3. The oil-gas well structure for facilitating extracting a downhole filter
string
according to claim 2, characterized in that: the ultra light particles are
particles
which have an average particle diameter of 0.05-0.8 mm, and a real density of
0.94-1.08 g/cm3.

4. The oil-gas well structure for facilitating extracting a downhole filter
string
according to claim 2 or 3, characterized in that: the ultra light particles
are
macromolecule polymer particles.

5. The oil-gas well structure for facilitating extracting a downhole filter
string
according to claim 2, characterized in that: the ultra light particles are
high
density polyethylene particles which have an average particle diameter of
0.05-0.8 mm, and a real density of 0.90-0.98 g/cm3.

6. The oil-gas well structure for facilitating extracting a downhole filter
string
according to claim 2, characterized in that: the ultra light particles are
polypropylene and PVC macromolecule polymer particles which have an
average particle diameter of 0.05-0.8 mm, and a real density of 0.7-1.3 g/cm3.
12


7. The oil-gas well structure for facilitating extracting a downhole filter
string
according to claim 4, characterized in that: the ultra light particles are
styrene
and divinylbenzene cross-linked copolymer particles which have an average
particle diameter of 0.05-0.8 mm, and a real density of 0.94-1.08 g/cm3.

8. The oil-gas well structure for facilitating extracting a downhole filter
string
according to claim 1, characterized in that: the ultra light particles and the
carrier fluid for the ultra light particles have a density difference within a
range
of from -0.35 to +0.35, which range contains two endpoint values.

9. The oil-gas well structure for facilitating extracting a downhole filter
string
according to claim 8, characterized in that: the ultra light particles and the
carrier fluid for the ultra light particles have a density difference within a
range
of from -0.3 to +0.3, which range contains two endpoint values.

10. A method for extracting a downhole filter string from the oil-gas well
structure for facilitating extracting a downhole filter string according to
any one
of claims 1-9, characterized in that, the method including the following
steps:
1) establishing channels by opening an annulus between an upper end of a
downhole filter string and a borehole wall;

2) removing ultra light particles by a carrier fluid for backwashing:
injecting a
carrier fluid for ultra light particles into the downhole filter string in
order to
backwash and carry the ultra light particles away from the annulus;

3) extracting the downhole filter string.

11. The method for extracting a downhole filter string from the oil-gas well
structure for facilitating extracting a downhole filter string according to
claim 10,
characterized in that: the downhole filter string is a flow-control filter
string, the
step of removing ultra light particles by a carrier fluid for backwashing is
in a
way such as to connect a fluid injection pipe with the downhole filter string
and
directly inject the carrier fluid for ultra light particles into the flow-
control filter
string.

12. The method for extracting a downhole filter string from the oil-gas well
structure for facilitating extracting a downhole filter string according to
claim 10,
characterized in that: the step of removing ultra light particles by a carrier
fluid
for backwashing is in a way such as to run a fluid injection pipe into the
downhole filter string, said fluid injection pipe performs fluid injection; a
lower
13


portion of the fluid injection pipe has an opening an upper portion of which
is
provided with a seal ring having an outside diameter substantially identical
to
an inside diameter of the downhole filter string, the fluid injection being in
a
sectional manner.

13. The method for extracting a downhole filter string from the oil-gas well
structure for facilitating extracting a downhole filter string according to
any one
of claims 10-12, characterized in that: the carrier fluid for ultra light
particles is
water or water solution.

14

Description

Note: Descriptions are shown in the official language in which they were submitted.



CA 02783392 2012-06-06

OIL-GAS WELL STRUCTURE FOR FACILITATING EXTRACTING A
DOWNHOLE FILTER STRING AND METHOD FOR EXTRACTING THE
STRING
Technical Field

The present invention relates to the oil exploitation field, and specifically
relates
to an oil-gas well structure for facilitating extracting a downhole filter
string and
a method for extracting the downhole filter string from the oil-gas well. The
oil-gas well here refers to a production well in a broader sense in oil-gas
field
development, which includes an oil well, a gas well, a natural gas well, an
injection well, etc.

Background Art

The completion structure of most mechanically sand control oil-gas wells
comprises an oil-gas well and a downhole filter string run into the oil-gas
well,
and the oil-gas well includes a vertical well, a deviated well, a highly-
deviated
well and a horizontal well. As shown in Figure 1, the reference sign 1 in
Figure
1 indicates a borehole wall of an oil-gas well, the reference sign 2 indicates
a
downhole filter string, the reference sign 3 indicates an annulus between the
downhole filter string and the borehole wall, the reference sign 4 indicates a
packer for hanging the downhole filter string. The downhole filter string here
is
a downhole filter string in a broader sense and has a plurality of forms, for
instance, in a first circumstance there is a downhole filter string having no
flow-restrict function which at this same is only a sand control filter, which
is
also called as a sand control screen. In a second circumstance, there is a
filter
having a flow-control function, i.e. a flow-control filter string, which is
also
called as a flow-control screen. The flow-control filter has a flow-control
function, and at the same time has a filtering function, which function is
sometimes to prevent anti-channeling particle medium outside the flow-control
filter from entering a wellbore and also has the function of preventing
formation
sand from entering a wellbore for a sand production well. The flow-control
function of the flow-control filter embodies a flow-restrict function as well.
The downhole filter string refers to a string formed by connecting one or more
downhole filters in series. For example, a sand control screen with a total
length
of 300 meters which is placed into a horizontal well is formed by connecting
30
sand control screens of about 10 meters in series.

1


CA 02783392 2012-06-06

In an oil-gas well containing the downhole filter string, there exist the
following
two circumstances outside the downhole filter string: one circumstance in
which outside the downhole filter string there are artificially filled with
gravels
which include quartz sands or ceramsites; the other circumstance in which
outside the downhole filter string there are no fillers, if there are no
fillers
outside the downhole filter string, after a period of production by a sand
production well, the produced formation sand may also fill up the annulus
between the downhole filter string and the borehole wall, as shown in Figure
1,
the reference sign 5 in Figure 1 represents formation sands or artificially
filled
gravels accumulated outside the downhole filter string. Both naturally filled
formation sands and artificially filled gravels produce a great resistance for
pulling a downhole filter string such that it is difficult to extract a
downhole filter
string in an oil-gas well, in particular a well having a long downhole filter
string,
such as a highly-deviated well and a horizontal well, in which it is almost
impossible to extract a downhole filter string.

However, it is necessary to extract a downhole filter string under a number of
circumstances, such as the following several circumstances:

1. It is necessary to repair a damaged downhole filter string, or to replace a
downhole filter string;

2. It is necessary to recycle extracted downhole filter strings so as to save
much
expenditure.

3. When a flow-control filter string is used, the extraction of a flow-control
filter
string in the production process may facilitate conveniently regulating the
flow-control parameters of the flow-control filter string such as to adapt to
the
flow requirements of different exploitation stages and improve the production
efficiency of an oil-gas well.

At present, there is still no oil-gas well structure facilitating extracting a
downhole filter string and a particularly effective method for extracting a
downhole filter string from an oil-gas well.

Summary of the Invention

The technical problem required to be solved by the present invention is to
provide an oil-gas well structure facilitating extracting a downhole filter
string
and a method for extracting a downhole filter string from the oil-gas well.

2


CA 02783392 2012-06-06

In order to solve the aforementioned problem, the present invention uses the
following technical solution:

The oil-gas well structure for facilitating extracting a downhole filter
string of
the present invention comprises a borehole wall and a downhole filter string
run
into the oil-gas well, one end of the downhole filter string close to the
wellhead
being an upper end of the filter string which end is fixedly connected with
the
borehole wall, an annulus being formed between the downhole filter string and
the borehole wall; the annulus between the downhole filter string and the
borehole wall is filled with ultra light particles, wherein the density of the
ultra
light particles approaches or is equal to the density of a carrier fluid for
carrying
the ultra light particles, the carrier fluid for carrying the ultra light
particles is a
liquid for carrying and conveying the ultra light particles into the annulus
or
backwashing and conveying the ultra light particles out of the annulus.

The ultra light particles and the carrier fluid for the ultra light particles
have a
density difference within a range of from -0.35 to +0.35, which range contains
two endpoint values.

Preferably, the ultra light particles and the carrier fluid for the ultra
light
particles have a density difference within a range of from -0.3 to +0.3, which
range contains two endpoint values.

The ultra light particles are particles which have an average particle
diameter of
0.05-1.2 mm, and a real density of 0.7-1.3 g/cm3.

Preferably, the ultra light particles are particles which have an average
particle
diameter of 0.05-0.8 mm, and a real density of 0.94-1.08 g/cm3.

Preferably, the ultra light particles are macromolecule polymer particles.
Preferably, the ultra light particles are high density polyethylene particles
which
have an average particle diameter of 0.05-0.8 mm, and a real density of
0.90-0.98 g/cm3.

Or, the ultra light particles are polypropylene and PVC macromolecule polymer
particles which have an average particle diameter of 0.05-0.8 mm, and a real
density of 0.7-1.3 g/cm3.

3


CA 02783392 2012-06-06

Or, the ultra light particles are styrene and divinylbenzene cross-linked
copolymer particles which have an average particle diameter of 0.05-0.8 mm,
and a real density of 0.94-1.08 g/cm3.

The present invention also discloses a method for extracting a downhole filter
string from the oil-gas well structure for facilitating extracting a downhole
filter
string, which method includes the following steps:

1) Establishing channels: opening an annulus between an upper end of a
downhole filter string and a borehole wall;

2) Removing ultra light particles by a carrier fluid for backwashing:
injecting a
carrier fluid for ultra light particles into the downhole filter string in
order to
backwash and carry the ultra light particles away from the annulus;

3) Extracting the downhole filter string.

When the downhole filter string is a flow-control filter string, the step of
removing ultra light particles by a carrier fluid for backwashing is in way
such as
to connect a fluid injection pipe with the downhole filter string and directly
inject the carrier fluid for ultra light particles into the flow-control
filter string,
due to a flow-control effect of the flow-control filter string, the injection
fluid is
uniformly injected into ultra light particles from various segments of the
flow-control filter string, and ultra light particles accumulated outside the
downhole filter string are removed by means of an upper fluid flow passage of
the downhole filter string.

When the downhole filter string is a flow-control filter string, the step of
removing ultra light particles by a carrier fluid for backwashing is in a way
such
as to run a fluid injection pipe into the downhole filter string, said fluid
injection
pipe performs fluid injection; a lower portion of the fluid injection pipe has
an
opening an upper portion of which is provided with a seal ring having an
outside
diameter substantially identical to an inside diameter of the downhole filter
string, the fluid injection being in a sectional manner; the fluid injection
pipe is
gradually run into a bottom of the downhole filter string for sectional fluid
injection and sectional removal of ultra light particles outside the downhole
filter string from the top of the downhole filter string, when ultra light
particles
outside an anterior segment of the downhole filter string close to a wellhead
are
removed, the fluid injection pipe is penetrated into the downhole filter
string for
another segment until those outside the downhole filter string are completely
removed; or it is possible to continuously move the fluid injection pipe to
4


CA 02783392 2012-06-06

perform fluid injection until ultra light particles outside the downhole
filter
string are removed.

When the downhole filter string is a downhole filter string having no
flow-restrict function, the step of removing ultra light particles by a
carrier fluid
for backwashing is in a way such as to run a fluid injection pipe into the
downhole filter string, said fluid injection pipe performs fluid injection; a
lower
portion of the fluid injection pipe has an opening an upper portion of which
is
provided with a seal ring having an outside diameter substantially identical
to
an inside diameter of the downhole filter string, the fluid injection being in
a
sectional manner; the fluid injection pipe is gradually penetrated into a
bottom
of the downhole filter string for sectional fluid injection and sectional
removal of
ultra light particles outside the downhole filter string from the top of the
downhole filter string, when ultra light particles outside an anterior segment
of
the downhole filter string close to the wellhead are removed, the fluid
injection
pipe is penetrated into the downhole filter string for another segment until
those outside the downhole filter string are completely removed. The fluid
injection pipe may be moved in a manner such as to continuously move the
fluid injection pipe to perform fluid injection until ultra light particles
outside the
downhole filter string are removed.

Preferably, the carrier fluid for ultra light particles as defined in the
present
invention is water or water solution.

The present invention utilizes a carrier fluid for ultra light particles
having a
density of about 1 g/cm3 and chooses ultra light particles having a real
density
very close to that of a carrier fluid so that the carrier fluid may easily
carry the
ultra light particles for filling into an annulus between the downhole filter
string
and the borehole wall, filling in and filling up the annulus between the
downhole
filter string and the borehole wall, a part of the carrier fluid enters the
downhole
filter string and returns to the ground surface and a further part of the
carrier
fluid penetrates into the formation through the borehole wall; and finally
form
a completion structure which fill up ultra light particles in the annulus
between
the downhole filter string and the borehole wall.

At the same time, the ultra light particles occupy the space of the annulus
between the downhole filter string and the borehole wall, and also obstruct a
accumulating of the formation sand in the space of the annulus between the
downhole filter string and the borehole wall.



CA 02783392 2012-06-06

The present invention chooses particles having an average particle diameter of
0.05-1.2 mm, and a real density of 0.7-1.3 g/cm3 as ultra light particles for
filling the annulus between the downhole filter string and the borehole wall,
when it is necessary to extract the downhole filter string, it is possible to
easily
remove ultra light particles accumulated outside the downhole filter string,
and
as the density of the ultra light particles is very close to that of the
carrier fluid,
the carrier fluid circulating in a low speed may conveniently take the ultra
light
particles to the ground and remove the ultra light particles in the annulus
outside the downhole filter string so that the downhole filter string may be
conveniently extracted from the oil well. The requirements for extracting a
downhole filter string are satisfied.

The method as defined in the present invention, which is easy to carry out,
overcomes the difficulties in extracting a downhole filter string in an oil
well and
thus facilitates the production, and moreover, the removed ultra light
particles
may be recycled, thereby greatly reducing the production cost.

Description of the Drawings

Figure 1 is a view of the completion structure as defined in the Background
Art.
Figure 2 is a view of the completion structure as defined in the embodiment 1
of
the present invention.

Figure 3 is a view of a flow path of the carrier fluid for backwashing and
removing ultra light particles outside the filter string as defined in the
embodiment 2 of the present invention.

Figure 4 is a view of a flow path of the carrier fluid for backwashing and
removing ultra light particles outside the filter string as defined in the
embodiment 3 of the present invention.

Figure 5 is a view of a flow path of the carrier fluid for backwashing and
removing ultra light particles outside the filter string as defined in the
embodiment 4 of the present invention.

Figure 6 is a view of the oil-gas well structure after removing ultra light
particles
as defined in the present invention.

6


CA 02783392 2012-06-06

Detailed description of the preferable embodiments
Embodiment 1

As shown in Figure 2, an oil-gas well structure for facilitating extracting a
downhole filter string as defined in the present invention comprises an oil-
gas
well borehole wall 1 and a downhole filter string 2 run into the oil-gas well,
a
packer 4 for hanging the downhole filter string is provided between one end of
the downhole filter string close to the wellhead and the borehole wall, an
annulus is formed between the downhole filter string and the borehole wall;
the
annulus between the downhole filter string and the borehole wall is filled
with
ultra light particles 6.

Embodiment 2 A method for extracting a control-flow filter string

In the completion structure as shown in Figure 2 and as defined in the
embodiment 1, the ultra light particles are polypropylene and PVC
macromolecule polymer particles which have an average particle diameter of
0.05-0.8 mm, and a real density of 0.7-1.3 g/cm3.

As shown in Figure 3, the downhole filter string, which is a flow-control
string
filter 2, is provided with a flow-control filter 2-1; the method for
extracting the
downhole filter string is as follows:

1) Opening a packer for hanging the downhole filter string: for a packer unset
by pulling, the opening method is in a way such that the packer is unset
automatically when the packer is pulled. For a packer unset by rotating, the
packer is unset automatically when the packer is rotated. Between the unset
packer and the borehole wall there exists a gap which becomes a fluid
circulating passage.

2) Removing ultra light particles by a carrier fluid for backwashing: connect
a
fluid injection pipe with the downhole filter string and directly inject the
carrier
fluid for ultra light particles into the flow-control filter string, due to a
flow-control effect of the flow-control filter string, the injection fluid is
uniformly
injected into ultra light particles from various segments of the flow-control
filter
string; in Figure 3, the arrow direction indicates a flow method of the
carrier
fluid.

7


CA 02783392 2012-06-06

3) Removing: ultra light particles are taken out of the well by the carrier
fluid
until the ultra light particles accumulated outside the downhole filter string
are
removed; the structure of oil-gas well after removal is as shown in Figure 6.
4) Extracting the downhole filter string.

Embodiment 3 A method for extracting a control-flow filter string

In the completion structure as shown in Figure 2 and as defined in the
embodiment 1, the ultra light particles are styrene and divinylbenzene
cross-linked copolymer particles which have an average particle diameter of
0.05-0.8 mm, and a real density of 0.94-1.08 g/cm3.

As shown in Figure 4, the downhole filter string, which is a flow-control
string
filter 2, is provided with a flow-control filter 2-1; the method for
extracting the
downhole filter string is as follows:

1) Opening a packer for hanging the downhole filter string: for a packer unset
by pulling, the opening method is in a way such that the packer is unset
automatically when the packer is pulled. For a packer unset by rotating, the
packer is unset automatically when the packer is rotated. Between the unset
packer and the borehole wall there exists a gap which becomes a fluid
circulating passage.

2) Removing ultra light particles by a carrier fluid for backwashing: running
a
fluid injection pipe 7 into the downhole filter string, said fluid injection
pipe 7
performs fluid injection; a lower portion of the fluid injection pipe has an
opening an upper portion of which is provided with a seal ring 8 having an
outside diameter substantially identical to an inside diameter of the downhole
filter string, the fluid injection being in a sectional manner; the fluid
injection
pipe is gradually penetrated into a bottom of the downhole filter string for
sectional fluid injection and sectional removal of ultra light particles
outside the
downhole filter string from a top of the downhole filter string, due to an
effect
of the seal ring, the seal ring may block the carrier fluid injected into the
downhole filter string by the fluid injection pipe at a lower side of the seal
ring
and concentrate the carrier fluid to impact parts deposited with ultra light
particles, when ultra light particles outside an anterior segment of the
downhole filter string close to a wellhead are removed, the fluid injection
pipe
is penetrated into the downhole filter string for one further segment until
those
outside the downhole filter string are completely removed; such also avoids
that the carrier fluid does not produce the effect of the deposited ultra
light
8


CA 02783392 2012-06-06

particles and saves much carrier fluid. The arrow direction in Figure 4
indicates
a flow direction of the carrier fluid. The dotted line in Figure 4 presents
that the
fluid injection pipe is gradually penetrated into the downhole filter string
for
sectional fluid injection. The fluid injection pipe may be penetrated into the
downhole filter string in a continually uniform-speed penetrating manner. As
the continually uniform-speed moving injection pipe gradually injects fluid,
the
depth after ultra light particles are removed gradually increases until the
ultra
light particles outside the downhole filter string are completely removed. The
arrow direction in Figure 4 indicates a flow method of the carrier fluid.

3) Removing: ultra light particles are taken out of the well by the carrier
fluid
until the ultra light particles accumulated outside the downhole filter string
are
removed; the structure of oil-gas well after removal is as shown in Figure 6.
4) Extracting the downhole filter string.

Embodiment 4 A method for extracting a downhole filter string having no
flow-restrict function

In the completion structure as shown in Figure 2 and as defined in the
embodiment 1, the ultra light particles are high density polyethylene
particles
which have an average particle diameter of 0.1-0.5 mm, and a real density of
0.94 g/cm3.

As shown in Figure 5, the downhole filter string is a downhole filter string 2
having no flow-restrict function, and the method for extracting the downhole
filter string is as follows:

1) Opening the annulus between one end of the downhole filter string close to
the wellhead and the borehole wall, establishing a fluid circulating passage
at
an upper portion of the annulus between one end of the downhole filter string
close to the wellhead and the borehole wall: for a packer unset by pulling,
the
opening method is in a way such that the packer is unset automatically when
the packer is pulled. For a packer unset by rotating, the packer is unset
automatically when the packer is rotated. Between the unset packer and the
borehole wall there exists a gap which becomes a fluid circulating passage.

2) Removing ultra light particles by a carrier fluid for backwashing: running
a
fluid injection pipe 7 into the downhole filter string, said fluid injection
pipe 7
performs fluid injection; at the end of the fluid injection pipe there is
provided
with a seal ring 8 having an outside diameter substantially identical to an
inside
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CA 02783392 2012-06-06

diameter of the downhole filter string, a fluid outlet 9 of the fluid
injection pipe
is at a position slightly lower than the seal ring of the fluid injection
pipe, the
fluid injection being in a sectional manner; the fluid injection pipe is
gradually
penetrated into a bottom of the downhole filter string for sectional fluid
injection and sectional removal of ultra light particles outside the downhole
filter string from the top of the downhole filter string, due to an effect of
the seal
ring, the seal ring may block the carrier fluid injected into the downhole
filter
string by the fluid injection pipe at a lower side of the seal ring inside the
downhole filter string so that it is difficult for the carrier fluid to enter
the upper
side of the seal ring and thus at places where the ultra light particles are
removed at an upper side there are no more carrier fluid entering from the
filter
string, and concentrate the carrier fluid to remove ultra light particles that
are
required to be removed, when ultra light particles outside an anterior segment
of the downhole filter string close to a wellhead are removed, the fluid
injection
pipe is penetrated into the downhole filter string for another segment until
those outside the downhole filter string are completely removed; such also
avoids the run-up of the carrier fluid and thus saves much carrier fluid and
maintains a higher flow speed of impacting ultra light particles. The arrow
direction in Figure 5 indicates a flow direction of the carrier fluid. The
dotted line
in the figure presents that the fluid injection pipe is gradually penetrated
into
the downhole filter string for sectional fluid injection. The fluid injection
pipe
may be penetrated into the downhole filter string in an intermittently
penetrating manner. The intermittently moving injection pipe gradually injects
fluid until the ultra light particles outside the downhole filter string are
completely removed.

3) Removing: ultra light particles are taken out of the well by the carrier
fluid
until the ultra light particles accumulated outside the downhole filter string
are
removed; the structure of oil-gas well after removal is as shown in Figure 6.
4) Extracting the downhole filter string.

The carrier fluid as defined in the embodiments 2-4 may be water or a water
solution added with common additives for an oil field.

The method as defined in the present invention, which is easy to carry out,
overcomes the difficulties in extracting a downhole filter string in an oil
well and
thus facilitates the production, and moreover, the removed ultra light
particles
may be recycled, thereby greatly reducing the production cost.



CA 02783392 2012-06-06

The density of the particles in the present patent refers to a real density of
particles.

The present patent also contains a circumstance in which a thinner downhole
filter string is secondarily run into an initial downhole filter string of a
well that
is already present with a downhole filter string. It contains circumstances in
which a filter string is run into a casing perforated well, a well with a
porous
pipe and an open-hole well.

Finally, it is imperative to explicate that: apparently, the aforementioned
embodiments only pertain to exemplifications made to clearly present the
present invention rather than definitions on the embodiments. On the basis of
said descriptions, a person skilled in the art may also make changes or
variations of other different forms. Hereby, it is unnecessary and impossible
to
list all the embodiments. However, the obvious changes or variations deriving
therefrom still fall into the protection scope of the present invention.

11

Representative Drawing
A single figure which represents the drawing illustrating the invention.
Administrative Status

For a clearer understanding of the status of the application/patent presented on this page, the site Disclaimer , as well as the definitions for Patent , Administrative Status , Maintenance Fee  and Payment History  should be consulted.

Administrative Status

Title Date
Forecasted Issue Date Unavailable
(86) PCT Filing Date 2010-12-10
(87) PCT Publication Date 2011-06-16
(85) National Entry 2012-06-06
Examination Requested 2013-11-21
Dead Application 2017-07-05

Abandonment History

Abandonment Date Reason Reinstatement Date
2015-05-19 R29 - Failure to Respond 2015-08-26
2016-07-05 R30(2) - Failure to Respond
2016-12-12 FAILURE TO PAY APPLICATION MAINTENANCE FEE

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $400.00 2012-06-06
Maintenance Fee - Application - New Act 2 2012-12-10 $100.00 2012-11-15
Maintenance Fee - Application - New Act 3 2013-12-10 $100.00 2013-11-14
Request for Examination $800.00 2013-11-21
Registration of a document - section 124 $100.00 2014-01-10
Maintenance Fee - Application - New Act 4 2014-12-10 $100.00 2014-11-13
Reinstatement for Section 85 (Foreign Application and Prior Art) $200.00 2015-08-26
Maintenance Fee - Application - New Act 5 2015-12-10 $200.00 2015-11-06
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
ANTON BAILIN OILFIELD TECHNOLOGIES (BEIJING) CO., LTD.
Past Owners on Record
ANTON OILFIELD SERVICES (GROUP) LTD.
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
Documents

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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Abstract 2012-06-06 1 27
Claims 2012-06-06 3 111
Drawings 2012-06-06 3 52
Description 2012-06-06 11 528
Representative Drawing 2012-08-03 1 8
Cover Page 2012-08-10 2 54
Claims 2012-10-10 3 126
Abstract 2012-10-10 1 27
Description 2012-10-10 12 581
Claims 2015-05-15 3 81
Prosecution-Amendment 2015-05-15 10 321
PCT 2012-06-06 11 456
Assignment 2012-06-06 5 128
Prosecution-Amendment 2012-10-10 36 1,613
Prosecution-Amendment 2013-11-21 1 37
Prosecution-Amendment 2014-11-17 5 303
Assignment 2014-01-10 7 225
Assignment 2014-03-03 3 105
Amendment 2015-08-26 18 772
Examiner Requisition 2016-01-05 3 241