U.S. patent number 3,622,071 [Application Number 04/644,610] was granted by the patent office on 1971-11-23 for crude petroleum transmission system.
This patent grant is currently assigned to Combustion Engineering Inc.. Invention is credited to Bill S. Burrus, Robert W. Coggins.
United States Patent |
3,622,071 |
Coggins , et al. |
November 23, 1971 |
CRUDE PETROLEUM TRANSMISSION SYSTEM
Abstract
A heater having an oil or gas fired burner is shown, tubes are
extended through the heater to conduct crude petroleum through the
heating zone and lower the viscosity of the petroleum. Conduits
connect the heater tubes to a section of transmission line arn are
valved to blend the heated petroleum with the petroleum in the
line, the resulting mixture being then transmitted a great
distance.
Inventors: |
Coggins; Robert W. (Tulsa,
OK), Burrus; Bill S. (Tulsa, OK) |
Assignee: |
Combustion Engineering Inc.
(New York, NY)
|
Family
ID: |
24585623 |
Appl.
No.: |
04/644,610 |
Filed: |
June 8, 1967 |
Current U.S.
Class: |
236/24; 137/92;
137/13; 236/12.11 |
Current CPC
Class: |
F17D
1/18 (20130101); Y10T 137/2506 (20150401); Y10T
137/0391 (20150401) |
Current International
Class: |
F17D
1/18 (20060101); F17D 1/00 (20060101); F17d
001/16 () |
Field of
Search: |
;137/13,92,90,94 ;158/36
;236/23,24 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Weakley; Harold W.
Claims
The invention having been described, what is claimed is:
1. A system for controlling the combustion of a direct fired heater
for fluids circulated through tube passes in the heater so as to be
exposed to products of combustion, including,
a bypass conduit connected across the heater to bypass fluid around
the tube passes of the heater,
a valve in the bypass conduit connected to respond to the
differential pressure across the heater tube passes,
means responsive to the flow of fluids through the passes,
means responsive to the temperature of the fluids heated in the
passes,
a combustion control system for the heater,
and means connected to the valve to select when the flow responsive
mean will be connected to the combustion control system and when
the means responsive to the temperature of the fluids heated with
be connected to the combustion control system,
whereby, when the heater is started and the valve is open the flow
of fluids through the passes regulates the combustion over a first
range of operation and when the valve is closed the temperature of
the fluids regulates the combustion over a second range of
operation.
2. The system of claim 1 wherein,
the fluid heated to blended into a larger body of unheated fluid to
form a mixture,
a means responsive to the temperature of the blended fluid mixture
generates a control signal,
and the means responsive to the temperature of the fluid heated in
the tube passes is connected to modify the control signal of the
blended fluid mixture temperature to control the combustion in the
heater as the alternate to control by the flow-responsive
means.
3. A system for controlling the viscosity of oil well production
fluids transported through a pipeline conduit, including,
a loop connected to the conduit at two spaced-apart points and
through which a portion of the fluids transported through the
conduit are diverted,
a pump included in the loop to force the fluids diverted from the
conduit through the loop,
means for heating the fluids flowing through the loop, the means
occupying a predetermined portion of the loop and removed from the
segment of pipeline conduit defined by its two points of connection
with the loop,
a first bypass conduit connecting a point in the loop downstream of
the heating means with a point in the loop upstream of the heating
means, whereby a portion of the heated fluids in the loop may be
recirculated,
a valve located in the loop,
means responsive to the temperature of the fluids flowing in the
loop, the temperature responsive means located in the loop and
connected to the valve so as to control which portion of the heated
fluids is recirculated in the loop and which portion of the heated
fluids is blended with the fluids being transported through the
pipeline conduit,
means in the loop responsive to the flow rate of fluids through the
heater passes,
and switching means connected to the flow rate responsive means and
the vale of the second bypass conduit to select when the flow
responsive means will be connected to a combustion control system
of the heater and when the valve of the second bypass conduit will
be connected to the combustion control system,
whereby when the heater is started and the valve of the second
bypass conduit is open, the heat output of the heating means is
established at a predetermined maximum by the flow-responsive
means.
4. The system of claim 3, including,
temperature-responsive means responsive to a combination of the
temperature of the fluids in the pipeline conduit at a point
downstream of the point at which heated products of the loop are
blended into the pipeline conduit and the temperature of fluid in
the loop, and connected to the combustion control system through
the switching means to regulate the heat output of the heating
means when the valve in the second bypass conduit is closed.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to controlled heating to reduce the
viscosity of crude petroleum oil in order to facilitate its
movement. More particularly, the present invention pertains to
apparatus for manipulating fluids in a program of heating and
blending which will reduce their viscosity quickly without the
overheating which results in petroleum fluids being cracked.
2. Description of the Prior Art
The production of low gravity, high viscosity crude petroleum has
always been a problem. Once produced, the transport of this
material to the refinery causes a further range of problems to
descend.
Generally, a pipeline is favored over trucking in crude transport.
It is cheaper. However, the pressure differential required to move
low gravity, high viscosity crude through a pipeline has been
either too expensive or mechanically impractical.
In general it is an old practice to heat crude fluids to lower
their viscosity. Also, in general, it is old to either immerse a
fired tube in the fluids or pass the fluids through tubes exposed
to products of combustion.
The immersed fired tube is the less attractive choice because of
the immediate danger of having coke formed on its surface which
will promote the overheating of local wall areas with eventual
rupture of the wall. Conducting the fluids through the tubes of a
direct fired heater is the selected technique. However, there are
several unique and severe problems associated with hating apparatus
of this type.
The heated, conducting tubes of the direct fired heater are
generally divided into one group in the main body of the heater
which absorbs heat of burner combustion by radiation, principally,
and a second group in the exhaust stack which absorbs heat by
convection, principally. The heat flux (BTU/square foot) on the
surface of the tubes must not be so great that heated fluid next
the internal wall will crack and coke on the wall surface. The
velocity of the heated fluids could be increased to avoid over
heating but viscosity becomes a factor in developing an economical
limit to the differential pressure required to increase the
velocity. Until the viscosity is reduced a predetermined amount,
the heat flux must be kept within predetermined limits.
SUMMARY OF THE INVENTION
The present invention contemplates raising the velocity of the
heated fluids to a maximum, limited by the economics of
differential pressure generation, and firing the burner of the
heater within a first low range until the differential pressure
reduces a predetermined amount. The viscosity of the fluids will
lower as they are heated. Their flow will then change from a
laminar form into a turbulent form. One result is a more even
distribution of these fluids within their individual tubes. Fewer
tube passes will be required in the heater; distribution of the
fluids among fewer tube passes will tend to be more even with
respect to the heat flux. As the differential pressure reduces to
the predetermined minimum amount, the burner is fired within a
second high range to reach the temperature ultimately desired for
the heated fluids.
The heat input program for the heater shifts the burner operation
from a low range to a higher range as quickly as possible. The
initial heat output range for the burner keeps the temperature of
the discharged flue gases from the stack in, or very close to, the
range where corrosive condensation will probably occur. Generally,
400.degree. F. is regarded as the minimum desirable temperature for
these flue gases; a lower temperature will result in condensation
of liquids containing highly corrosive sulfur compounds. It is
desirable that the convection group of the heated tubes be kept in
the lower temperature range for as short a time as possible.
The present invention limits the operation of the burner to the low
range for as short a time as compatible with the viscosity
reduction at the maximum throughput of heated fluids under the
available pressure differential. A bypass of the heated tubes is
provided to control the differential reducing below a predetermined
value. The heating is shifted into a predetermined upper range in
order to maintain the maximum heat flux on the tubes at the maximum
throughput flow capacity while raising the exhaust temperature of
the heater to a range including a minimum of substantially
400.degree. F.
The present invention further contplates a conduit loop including a
section of pipeline and a section heated by a source. The heat
source is bypassed for the reasons set forth above. The pipeline
section is bypassed for the time required to raise the temperature
of the fluids to their ultimate desired value. The heat source is
operated within a plurality of ranges coordinated with the
bypassing of the heat source and the pipeline section to avoid a
heat flux which will crack the petroleum fluids heated yet will
reach the on-stream condition quickly.
BRIEF DESCRIPTION OF THE DRAWINGS
The drawing is a simple, schematic diagram of a heater with a
conduit system between the heater and a section of pipeline
including the present invention.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The drawing prominently features a pipeline 1 which transports
petroleum fluids from a source not shown to a destination also not
shown. There are pumps for the pipeline fluids at stations between
the source and destination. There is no point in representing such
pumps on the drawing. It is sufficient to recognize that they are
necessary and that they consume enormous amounts of expensive power
in moving petroleum fluids in pipeline 1 when the gravity of the
fluids is low and their viscosity high. An embodiment of the
present invention will reduce this power and will start up quickly,
automatically and with a minimum of attendance.
BASIC CONDUIT LOOP
Apparatus in which invention is embodied is characterized by a
conduit for the fluids and which includes a section of pipeline 1.
Pipeline section 2 is to be taken with conduit section 3 forming
the input to pump 4.
The pump 4 delivers fluids to conduit section 5 which forms the
input to heater 6. The heated conduits in heater 6 are the heated
section of the loop and from this section the heated fluids are
discharged into conduit section 7.
Conduit section 7 connects to conduit section 8 to deliver heated
fluids to pipeline section 2. The loop is completed for withdrawing
fluids from the pipeline 1, pumping them through heater 6 and
delivering them, properly heated, to pipeline 1. The heated fluids
can then mix with the colder fluids of the pipeline to form a
mixture having a viscosity which will enable the undisclosed pumps
of the pipeline to move the material economically through the
pipeline.
GENERAL CONTROL OF HEATER 6
Heater 6 is fired with a burner 10 and supply of combustion air
from blower 11. The firing equipment is contemplated as
conventional, burning gas or oil to produce products of combustion
for contact with the heated conduit section which extends through
heater 6. The control of fuel and air can be embodied in many
different arrangements; a single valve in this disclosure
represents all such elements which respond to a control system
sensitive to primary elements established in the basic conduit
loop.
The input to the heater must be carefully controlled within a
plurality of ranges. Ultimately, this heater input is adjusted to
maintain a desired temperature for the mixture of fluids in the
pipeline section 2. In approaching this goal, the heater input must
be staged and coordinated with bypass programs for the sections of
the basic conduit loop to bring the complete system into full,
"on-line" operation as quickly and efficiently as possible.
GENERAL PROBLEMS OF HEATER 6
Heater 6, as a separate structure, is shown as having its burner 10
controlled to produce heat into a radiant section and a convection
section. The radiant section 12 is the main body of the heater and
the tubes mounted in this section are exposed to principally
radiant heat of combustion.
BEfore they reach the radiant section, the fluids to be heated flow
through tubes mounted in the exhaust stack of heater 6. This
convection section 13 is exposed to the heat of the combustion
which is principally convective. The products of combustion from
the burner discharge into the radiant section and then flow through
the convection section. The fluids to be heated are first heated in
section 13 and then section 12.
Heaters of the size contemplated for this pipeline heating are
expensive. Any reduction in this size is, of course, very
desirable. If the basic problems of cracking the fluids heated,
distributing the fluids within the heater tubes and corrosion of
the heated tube surface can be controlled, the heater will not only
resist deterioration, but can be built in smaller sizes than
otherwise possible.
The first problem could be considered one of corrosion. The heat
extracted from the flue gases should not lower their temperature to
the neighborhood of 400.degree. F. At 400.degree. F. and below,
condensation of sulfur-bearing compounds becomes a corrosive
threat. Certainly the heater 6 should be operated to maintain the
flue gas temperature in section 13 within this corrosive range for
as short a time as possible.
The second problem considered is the danger of cracking the
petroleum fluids heated within the tubes of section 12. If the heat
flux on the tube surface is high enough, and the absorption by the
fluids low enough, the thin outer layer of fluids in the tubes will
overheat and break down. Turbulence of the fluids heated is the
answer.
Heat will destroy laminar flow of low gravity oils by promoting
turbulence, resulting in an increase in heat transfer into the
fluids. However, this heating and viscosity reduction to obtain
turbulence takes a finite period of time. The heat flux must be
controlled within a predetermined low range with the fluid flow
maintained at a maximum as set by the economically available
pressure differential for maintaining flow. Once the differential
pressure reduces to a predetermined level, the heat input is
shifted into high gear without danger of cracking the fluids and
the temperature in the convection section is raised above the
condensation level.
HEATER BYPASS OPERATION
On initial startup of the system, the tubes of the heater 6 will
offer a tremendous resistance to the flow of fluid. Pump 4 will
develop a differential pressure between conduit section 5 and
conduit section 7 which causes the flow. This differential is
controlled by extending a bypass conduit 14 between conduit section
5 and conduit section 7 with a valve V-3 regulating flow and
responsive to the differential pressure.
Flow is established through the heated tubes in heater 6 under the
differential pressure set by The remainder of the output of pump 4
is shuttled around the heater, through bypass conduit 14.
As heat is added to the production fluids the differential pressure
begins to reduce. Less fluids are bypassed until valve V--3 closes.
Thereafter, all the pumped fluids flow through heater 6.
PIPELINE SECTION BYPASS
The bypass of heater 6 controls the differential pressure across
the heater while the viscosity of the heated fluids reduces and
generates turbulence in the fluids being heated. Until this
viscosity is lowered, turbulence generated and the temperature
level raised a significant amount, the fluids in the conduit loop
are not properly prepared for introduction into the pipeline 1.
The heating and recirculation with bypasses, are brought about in
overlapping stages. First, the heater bypass is operated as set
forth. Next, the pipeline section 2 is bypassed, then gradually fed
heated fluids until the viscosity of the pipeline 1 fluids is under
control. Bypass conduit 15 is connected between conduit section 7
and conduit section 3 to form the basic conduit loop into a
reservoir of heated fluids from which the fluids can be blended
into the cold fluids of pipeline section 2 in a desired
program.
Valve V-2 regulates the flow in bypass conduit 15 and valve V-1
regulates the flow in conduit section 8. As one valve opens the
other closes, thereby determining how much of the heated fluids
flow into pipeline section 2. In general, the valves are arranged
responsive to the temperature of all heated fluids pumped through
the loop. As this temperature approaches a desired value, valves
V-1 and V-2 open and close to inject more the heated fluids into
pipeline section 2.
SUMMATION OF FLOW PATTERN IN THE LOOP
The overall purpose of heating the basic conduit loop is to provide
a source of heated fluids which can be fed into a pipeline to
control the viscosity of the pipeline fluids into an economic
pumping range. Once "on-stream" this system is easily understood.
Fluids are continually withdrawn, heated and fed back into the
pipeline upstream of the draw-off point. The heating of the side
stream is regulated from the temperature attained in the pipeline.
What is not obvious, and readily understood, is the internal
workings of the heated basic conduit loop upon startup and when
there is a change in the viscosity of the material in the
pipeline.
At startup, the conditions met by the system are severe. The entire
loop is charged with the fluids of the pipeline. They lack the
desired characteristics for pumping or heating. A large amount of
heat must be introduced, but the low heat conductivity of such
fluids necessitates that this heat must be added at a lower than
what might be regarded as a normal rate in order to avoid extreme
temperature differences across their contact surface with the
products of combustion in the heater.
Heat is needed to break up the laminar flow of these fluids with
turbulence which will increase the absorption of heat by the fluids
and reduce the pressure drop required to move the fluids.
To speed the development of turbulence in the fluids they are
heated in a recirculation circuit of the loop which is isolated
from the pipeline. Bypass conduit 15 completes the recirculation
circuit with sections 5 and 7. Within this recirculation circuit a
bypass is maintained with conduit 14 while the fluids are heating
to a predetermined viscosity.
HEATING CONTROL
The eventual, on-line, control of the firing of burner 10 is set by
the temperature of the fluids in pipeline section 2. A primary
element 15A is placed in section 2 and in contact with these
fluids. TC-3 is connected to 15A as an instrument which develops a
control signal which can be sent some distance. TC-1 receives the
TC-3 signal and modifies it by a signal generated by a temperature
sensitive primary element at 16. This modified control signal is
applied to combustion control valve 17 when selected by switch
18.
Switch 18 receives the modified temperature signal from TC-1 as
well as a signal representative of flow in conduit section 7.
Switch 18 is shown as mechanically actuated by valve V-3 so that
the operation of combustion valve 17 is placed under either the
influence of fluid flow from heater 6 or the temperatures of the
fluids heated by the heater.
The startup control of the system can now be more comprehensively
analyzed. As explained heretofore, the differential across the
heater 6 keeps valve V-3 open a first. When open, valve V-3
positions switch 18 to apply the output of FC to combustion valve
17 while the heater is partially bypassed through valve V-3. At
such period, the heat input is logically geared to the actual flow
of fluid through the heater. Orifice 19 sets the output signal of
FC and the heat is matched to the amount of medium absorbing the
heat.
Once valve V-3 has closed (the differential has decreased below a
predetermined value) the system is shifted to temperature control.
The temperature at 15A is the final guide. However, the temperature
at 16 is an important immediate guide to the operation of heater 6.
This temperature at 16 must not exceed a predetermined maximum,
regardless of the ultimate temperature condition of 15A. Therefore,
the signal from 16 is led to TC-1 to modify the TC-3 (15A) signal
if necessary to control the temperature of the fluids from heater
6.
CONCLUSION
When designed under the concepts of the present invention, the
pipeline heater 6 is an efficient, compact direct fired heater.
Staged heating, with bypassing, enables the heater to bring low
gravity, high viscosity oil up to temperature with the minimum
number of heated tube passes.
Not only does the improved distribution of heated oil in the tube
passes enable the heater size to be reduced, but the exhaust gas
temperature remains in the corrosive range for the minimum time.
Finally, the control of the combustion and flow pattern minimizes
the danger from coking of overheated oil.
The storage of properly heated oil in the loop is fed into the
pipeline as rapidly as feasible, under the guidance from the
temperature attained by the fluids in the conduit. The combustion
control is shifted from one range to another under indices which
protect the heater and ultimately reflect the temperature of the
pipeline fluids which are pumped great distances.
The system is simple enough to be readily automated for remote
monitoring and adjustment. Temporary shutdowns are followed by
smooth startups which bring the pipeline up to full operation in a
minimum time with inexpensive equipment.
From the foregoing it will be seen that this invention is one well
adapted to attain all of the ends and objects hereinabove set
forth, together with other advantages which are obvious and which
are inherent to the apparatus.
It will be understood that certain features and subcombinations are
of utility and may be employed without reference to other features
and subcombinations. This is contemplated by and is within the
scope of the invention.
As many possible embodiments may be made of the invention without
departing from the scope thereof, it is to be understood that all
matter set forth above, or shown in the accompanying drawings is to
be interpreted as illustrative and not in a limiting sense.
* * * * *