U.S. patent number 3,908,763 [Application Number 05/444,564] was granted by the patent office on 1975-09-30 for method for pumpin paraffine base crude oil.
Invention is credited to Drexel W. Chapman.
United States Patent |
3,908,763 |
Chapman |
September 30, 1975 |
Method for pumpin paraffine base crude oil
Abstract
The method of inducing and maintaining the flow of paraffine
base oil in a well structure which comprises heating and
maintaining the well structure at a temperature below the
fracturing and melting temperature of the paraffine, within that
range of temperature where the paraffine is dissolved and/or
reabsorbed and carried, in fluid state by the oil and above that
chill temperature where the paraffine in the oil solidifies and
separates from the oil.
Inventors: |
Chapman; Drexel W. (Bellflower,
CA) |
Family
ID: |
23765441 |
Appl.
No.: |
05/444,564 |
Filed: |
February 21, 1974 |
Current U.S.
Class: |
166/302;
166/304 |
Current CPC
Class: |
E21B
37/00 (20130101); E21B 36/00 (20130101) |
Current International
Class: |
E21B
37/00 (20060101); E21B 36/00 (20060101); E21B
043/24 (); E21B 037/00 () |
Field of
Search: |
;166/302,304,57,311,61,62 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Novosad; Stephen J.
Attorney, Agent or Firm: Maxwell; Georges A.
Claims
I claim:
1. The method for maintaining continuous, uniform, free flow of
paraffine ladened crude oil in a well structure including an
elongate vertical well bore extending downwardly from ground level
to a production zone, a casing in the bore, a production tubing
extending freely through the casing, a pump related to the lower
end of the tubing and heating means at upper end of and extending
through the well structure, said method comprising heating and
maintaining the well structure and paraffine ladened crude oil
therein at a temperature above that chill temperature at which the
paraffine in the crude oil separates from the crude oil and
solidifies, within that temperature range in which the paraffine is
and remains dissolved in the crude oil, below the melting
temperature of the paraffine and below the fracturing temperature
at which the paraffine separates from the crude oil.
2. The method set forth in claim 1 which includes heating the well
structure without the introduction and admixing of water and
foreign fluids into and with the structure and crude oil.
3. The method set forth in claim 1 wherein the well structure and
the paraffine ladened crude oil is heated and maintained at a
temperature below 126.degree.F and above that minimum temperature
at which the paraffine dissolves in the oil.
4. The method as set forth in claim 1 wherein the well structure
and the paraffine ladened crude oil is heated and maintained at a
temperature below 125.degree.F and at least 10.degree.F above that
temperature at which the paraffine dissolves in the oil, said well
structure is heated without the introduction and admixing of water
and foreign fluids into the structure and crude oil.
5. A method as set forth in claim 1 wherein said heating means of
the well structure includes an elongate heat transfer conductor
tube extending downwardly into and thence upwardly through the well
structure, a fluid heating medium, heater means adjacent the top of
the well to heat said medium and means to circulate the medium
through the heater means and the tube, said method including
heating the oil by heat transfer between the oil and heated fluid
medium and through a heat transfer conductor therebetween, whereby
the oil is heated without the introduction of water.
6. The method set forth in claim 5 wherein the well structure and
the paraffine ladened crude oil is heated and maintained at a
temperature below 125.degree.F and at least 10.degree.F above that
temperature at which the paraffine is dissolved in the oil.
7. The method set forth in claim 5 wherein the well structure and
the paraffine ladened crude oil is heated and maintained at a
temperature below 125.degree.F and at least 10.degree.F above that
temperature at which the paraffine is dissolved in the oil, said
well structure and oil is heated by conduction of heat from a
heated fluid medium circulated through the well structure and
without the introduction of water into the crude oil.
Description
This invention has to do with oil production and is more
particularly concerned with a novel method of inducing the flow and
the pumping of paraffine ladened oil through well structures.
Throughout the world, there are a great number of oil deposits in
which the oil contains and is ladened with so much paraffine that
the oil cannot be effectively and economically pumped. As a result
of the above, many large oil reserves have been substantially
abandoned on the premise that the oil cannot be economically and
effectively pumped from the earth formation in which it is found,
through and by means of conventional well structures and production
equipment or means.
Paraffine, which is commonly found in crude oil, when chilled or
cooled, separates from the oil and jells or sets up. As a result of
the above, when crude oil containing paraffine is pumped from the
earth formation in which it is found, upwardly through a well
structure and cools as it rises in the well structure, the
paraffine therein separates and jells or sets up in the well,
creating a blockage which seriously impedes and often stops the
flow of fluid in the well structure.
As the amount or percentage of paraffine in crude oil increases,
the tendency for the paraffine to impede flow or plug a well
increase at a rapid rate.
In the past, efforts to unplug paraffine plugged wells and to
induce the flow and production of paraffine ladened crude oil, the
well structures and the oil-bearing formations about the well
structures have been heated to melt the paraffine and to thereby
cause it to flow and, at the same time, permit the oil to flow.
The melting point of paraffine is, subject to limited variations,
about 126.degree.F. Accordingly, the above noted efforts by the
prior art to unplug paraffine plugged wells and to induce the
free-flow of fluids in their formations and through the wells, the
plugged well structures and their related formations have to be
heated to over 126.degree.F, to melt the paraffine, and to provide
sufficient excess residual heat so that the oil and paraffine in
the formation and well remain fluid for a sufficiently protracted
period of time to effect adequate and rewarding production of
oil.
Heating of wells, as practiced by the prior art, for the purpose
set forth above has involved the injection of live steam into the
wells and into their related oil-bearing formations for a
sufficient period of time to melt the paraffine and to heat the
wells and the formations to a sufficient extent to induce the flow
of production fluids. Then the introduction of steam is ceased and
production flow commenced. Production is continued until the wells
have cooled sufficiently to permit the paraffine to set or jell and
until the wells are again plugged, whereupon steam is again
injected and the wells and their related formations are again
heated.
It will be apparent that in those cases where the temperature in
the oil-bearing formation is about 65.degree.F, a great amount of
steam must be injected into a well and the formation for an
exceedingly long period of time and at great expense, to raise the
temperature of the well structure and the formation adjacent
thereto to 126.degree.F and above. In practice, in most cases where
paraffine is present in sufficient amounts to create the problems
recited above, the cost of heating the well exceeds the revenues to
be gained from that production which can be induced.
Still further, paraffine, in the presence of water has a greater
tendency to separate from its carrier or mother crude oil and to
jell or set up. In the case of heating wells by steam injection,
the steam condenses in the well, as the heat is absorbing by the
well structure and the formation, leaving a considerable amount of
water in the well, which water augments the tendency for the
paraffine to separate from the oil and to set up.
It has been determined that the paraffine in most oil deposits
which are ladened with paraffine is dissolved and in solution in
the oil. This is true even when the temperature of the oil, in its
formation is, for example, at about 75.degree.F and well above the
melting point of paraffine.
In one known case, in an oil deposit below the Great Salt Lake in
the State of Utah, oil, heavily ladened with paraffine is at a
temperature 78.degree.F in the formation in which it is found and
the paraffine is in dissolved solution in the oil. In that case,
when the oil is cooled from between 10.degree.F. and 15.degree.F,
as it is pumped up through the well, the paraffine separates from
the oil and, being below its melting point of 126.degree.F,
solidifies or jells, plugging the well.
It has been further determined in the above noted case that upon
raising the temperature of the oil, 10.degree.F. or 15.degree.F.,
that is, back to its natural or original temperature, and slightly
above, the separated and solidified paraffine is dissolved and
re-absorbed by the oil and is carried thereby.
The oil with the paraffine dissolved therein and carried thereby is
considerably stiffer and flows more slowly than does paraffine and
oil heated above the melting point of the paraffine, but it flows
uniformly and continuously.
It has also been determined that upon heating paraffine ladened oil
to near and above the melting point of paraffine, that is to near
126.degree.F or above, fracturing takes place and the paraffine
separates from the oil and is presented in a separate state where
it readily solidifies upon a slight decrease in temperature.
From the foregoing, it is apparent and it is now understood that
there is a range of temperature, well below the melting point of
paraffine where the paraffine is readily absorbed and carried by
the mother crude oil, in a liquid state. It is further apparent and
it is now understood that there is a temperature range below the
formation temperature of the oil where the paraffine in the oil
will separate therefrom and, when thus separated, solidifies.
It is an object and feature of my invention to induce and maintain
the flow of paraffine ladened crude oil in a well structure by
heating and maintaining the temperature of the well structure at or
slightly above the temperature of the paraffine ladened oil in the
formation in which it is found and at a temperature well below the
melting point of paraffine and below that temperature where
fracturing of the oil and paraffine commences.
It is another object and feature of this invention to heat a well
structure as above noted by dry heat, free of water.
It is still another object and feature of my invention to heat a
well structure, as set forth above, by conducting steam through a
steam conducting line extending from the top of the well to the
bottom thereof and thence back to the top of the well, whereby the
entire well structure is suitably maintained at a temperature below
the fracturing temperature of the oil and paraffine and above that
low, chilled temperature where the paraffine separates from the
oil.
It is an object and a feature of my invention to provide a method
and apparatus of the character referred to above which is such that
a small amount of heat continuously and economically supplied to a
related well structure results in steady, continuous and profitable
production of well fluids.
Still another object and feature of my invention is to provide an
apparatus for heating a well structure wherein the steam and/or
water supply therefor is in a closed heat insulated circuit whereby
little or no water is consumed and a minimum of heat generated is
wasted.
The foregoing and other objects and features of my invention will
be fully understood from the following detailed description of a
typical preferred form and carrying out of the invention throughout
which description reference is made to the accompanying drawing in
which my apparatus is diagrammatically illustrated and is shown
related to a typical well structure and oil bearing formation.
The apparatus that I provide includes an elongate string of small
diameter pipe or tubing such as is commonly referred to in the
petroleum production art as macaroni tubing and which will
hereinafter be referred to as heating tubing T. The heating tubing
T enters the upper or top end of a related well structure W at a
suitable fitting 10 at the top of the well casing C. The tubing
extends downwardly through the casing to and through a perforated
liner L at the lower end of the casing and extending into or
through the oil producing zone Z with which the well structure
communicates and extends back, up through the liner and casing and
exits the well at said fitting 10.
The heating tubing T extends through the annulus defined by the
casing and liner and a string of production tubing P extending
longitudinally through said casing and liner and in which a
suitable well pump (not shown) is arranged. The well pump can be of
any suitable form and in the accompanying drawing, I have indicated
the provision of sucker rod R for the pump within the production
tubing P and have shown a polish rod R' for the rod R, projecting
upwardly from the top of the well structure.
The production tubing can, as indicated, connect with a fitting 11
atop the fitting 10. The fitting 11 carries a packing structure for
the rod R' and has a lateral outlet 11' with which a production
pipe 12 is connected, to conduct the production fluid from the well
structure and deposit it in a suitable receiver tank or the like
(not shown).
The apparatus next includes a receiver tank O adjacent the top of
the well in which a supply of thermal oil is contained. The thermal
oil can be any oil suitable as a heat transfer medium and is
adapted to be heated and circulated through the heating tubing
T.
The tank O has an outlet fitting 15 connected with the inlet end of
the tubing T, at the fitting 10 by a line 16.
The line 16 is provided with a motor driven circulating pump
17.
The tank O next has an inlet fitting 18' connected with the outlet
end of the tubing T, at the fitting 10 by a line 18.
Finally, the tank O has a heating coil 20 within it, which coil has
inlet and outlet ends 21 and 22.
In practice, the tank O can be provided with a thermo insulating
jacket or cover about its exterior.
The apparatus shown next includes a steam generator, boiler or
heater H adjacent the tank O. The heater H can be of any suitable
form of heating or steam-generating means. In practice, I have
employed a steam-generating means utilizing electric resistance
heating elements, with great success.
The heater H has an outlet 30 connected with the inlet 21 of the
coil 20 in the tank 0 by a line 31 and has an inlet 32 connected
with a return line 33, which line connects with the outlet end 34
of a heating jacket 35 about the production pipe 12. The inlet end
36 of the jacket 35 is connected with the outlet end 22 of the coil
20 in the tank O by a line 37.
The jacket 35 about the pipe 12 serves as a condenser for the steam
and, at the same time heats the production in the pipe and assures
its free flow therefrom and into the production receiving means
that is to be provided.
In practice, a feed pump 38 is provided in the line 33 to conduct
water from the condenser jacket 35 into the heater H.
With the apparatus set forth above, the thermal oil in the tank O
is heated by steam generated by the heater H and is conducted
through the coil 20 in the tank O. Heated thermal oil is circulated
by the pump 17 through the heating tubing T whereby the well
structure from the top thereof down to the pump, liner and
production formation is heated to a temperature below 126.degree.F
or the melting point of paraffine and above that minimum
temperature where paraffine is readily dissolved by the mother
crude oil.
The thermal oil flowing from the tubing T is conducted back to the
tank O for re-heating and recirculation through the well
structure.
The steam flowing from the coil 20 in the tank O is conducted into
the heat transfer and condensing jacket 35 where its residual heat
is used to maintain the temperature of the production at a
temperature where it remains fluid and free flowing.
The condensed steam or hot water in the jacket 34 is drawn from the
jacket and is fed back into the heater 11 by the feed pump 36.
By controlling the B.T.U. input into the heater H and/or by
controlling delivery rate of either or both of the pumps 17 and 38,
it will be apparent that easy and flexible control of the
temperature in the well structure can be achieved.
In practice, in addition to other conventional and suitable control
and monitoring means, temperature gauges 50 and 51 can be
advantageously placed at the inlet and outlet ends of the tubing T.
By use of such gauges, and noting the temperature of the thermal
oil introduced into the tubing T and the temperature of said oil
flowing therefrom, an adequate determination of the well structure
throughout its entire extent can be attained.
While it is not necessary that the production zone Z be heated, it
will be noted that due to the fact that the apparatus heats the
well structure to a notably higher temperature than the mean
temperature of the formation, and that said higher temperature is
maintained substantially constant, the formation will in fact
become heated to an extent that the well fluids will flow more
readily. This conductive heating of the formation will extend
slowly outwardly from the well, with the passage of time, thereby
assuring continuous production by the well.
It is to be noted that when practicing my invention, that is, when
heating the production to a temperature below the melting point of
paraffine, where the paraffine is dissolved in and carried by the
oil, the production fluid is stiffer and flows more slowly than the
crude oil would flow if the paraffine was removed. The production
flows more slowly than it would if it were heated above
126.degree.F, or the melting point of the paraffine in the oil.
Accordingly, in one respect, in practicing my invention, the
production is made noticeably stiffer and such that it flows more
slowly than it would flow if heated to above the melting point of
the paraffine.
It is the above fact which leads the inventor of this new method to
believe that no one in the prior art has conceived or practice the
method hereinabove described. The concept or mere idea of creating
a condition which stiffens and slows the flow of production in a
well is contrary to all normal and accepted practices. It is
generally believed that in order to induce the flow of production
in a well where blockage and plugging up of the well by solidified
paraffine is encountered, the temperature of the well must be
elevated to and/or above the melting point of the paraffine,
whereupon the well's production will flow freely and rapidly.
In the practice of the present invention, while fast or rapid flow
of production is not achieved, slow, steady, uniform and
economically profitable production is achieved by a steady
induction of a relatively small amount of heat.
The above end gained by the practice of my invention makes the
operation and production of many wells which cannot be profitably
operated by raising the temperatures thereof above the melting
point of paraffine, extremely profitable to operate.
To the best of the inventor's present knowledge, a well temperature
of about 100.degree.F. is satisfactory and will suffice to
establish and maintain economical and profitable production in most
wells where paraffine plugging or stoppage has proved to be a
problem. Such a temperature is sufficiently below the melting point
of paraffine (126.degree.F) to prevent its separating from the
crude oil, is sufficiently high so that the paraffine is readily
dissolved and/or reabsorbed into and carried by the crude oil and
is sufficiently warm or hot so that the combined paraffine and
crude oil production is not so stiff that it cannot be pumped and
caused to flow at a reasonable rate through the well structure.
An additional feature and advantage to be gained in carrying out of
the present invention resides in the fact that materially less heat
than is commonly employed in other methods or processes where heat
is employed to induce production flow, with the result that
considerably less volatile hydrocarbons are caused to separate from
the crude oil and said oil contains more values as it reaches the
technical process of refining.
While, for the purpose of this disclosure, I have described our
invention related to a well structure which includes a pumping
means for the oil production, it will be readily seen and
appreciated that this invention can be readily and satisfactorily
related in and with free-flowing wells.
In many instances where pumps are required to induce the flow of
production fluids, by employment and use of my invention, the flow
of production can be made sufficiently free so that the pumps can
be operated with less applied energy and/or can be put out of
service.
Having described only one typical preferred form and application of
my invention, I do not wish to be limited or restricted to the
specific details herein set forth, but wish to reserve to myself
any modifications and/or variations that may appear to those
skilled in the art to which this invention pertains.
* * * * *