U.S. patent number 3,733,476 [Application Number 05/257,644] was granted by the patent office on 1973-05-15 for means and method for automatically controlling the hydrogen to hydrocarbon mole ratio during the conversion of a hydrocarbon.
This patent grant is currently assigned to Texaco Development Corporation. Invention is credited to Luther F. Champion, Walker L. Hopkins, William D. White.
United States Patent |
3,733,476 |
Hopkins , et al. |
May 15, 1973 |
MEANS AND METHOD FOR AUTOMATICALLY CONTROLLING THE HYDROGEN TO
HYDROCARBON MOLE RATIO DURING THE CONVERSION OF A HYDROCARBON
Abstract
In a hydrocarbon converting unit in a petroleum refinery, the
hydrogen to hydrocarbon mole ratio is controlled in accordance with
the following equation: where V.sub.H is the volume percent
hydrogen in recycle gas, G.sub.g is the specific gravity of the
recycle gas, F.sub.g is the flow rate of the recycle gas, G.sub.c
is the specific gravity of charge oil, F.sub.c is the charge oil
flow rate, M.sub.c is the average molecular weight of the charge
oil and the term 13261.21 is a conversion factor. Signal means
sample the charge oil and the recycle gas and provide signals
corresponding to the specific gravity of the charge oil G.sub.c and
of the recycle gas G.sub.g, the average molecular weight M.sub.c of
the charge oil and the quantity of hydrogen V.sub.H in the recycle
gas. Flow transmitters sense the flow rates F.sub.c and F.sub.g of
the charge oil and the recycle gas, respectively, and provide
corresponding signals. An analog computer computes the hydrogen to
hydrocarbon mole ratio in accordance with the aforementioned
equation and the signals from the signal means and the flow
transmitters and provides an output corresponding thereto. An error
signal is developed using an output from the analog computer and a
reference signal corresponding to a desired value for the hydrogen
to hydrocarbon mole ratio. The error signal is used to control the
hydrogen entering the hydrocarbon converting unit so as to maintain
the hydrogen to hydrocarbon mole ratio at the desired value.
Inventors: |
Hopkins; Walker L. (Houston,
TX), White; William D. (Nederland, TX), Champion; Luther
F. (Cherry Hill, NJ) |
Assignee: |
Texaco Development Corporation
(New York, NY)
|
Family
ID: |
22977138 |
Appl.
No.: |
05/257,644 |
Filed: |
May 30, 1972 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
|
97571 |
Dec 14, 1970 |
|
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|
Current U.S.
Class: |
700/272;
208/DIG.1; 208/134; 422/110; 700/89 |
Current CPC
Class: |
C10G
35/24 (20130101); Y10S 208/01 (20130101) |
Current International
Class: |
C10G
35/24 (20060101); C10G 35/00 (20060101); C10g
035/04 (); G06g 007/58 () |
Field of
Search: |
;235/151.12,151.1,150,150.1,151.3,151.34,151.35
;208/134,138,139,DIG.1 ;196/132 ;23/23R,232R,252R,254E,255E |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Ruggiero; Joseph F.
Parent Case Text
CROSS REFERENCE TO RELATED APPLICATIONS
This application is a continuation as to all subject matter common
to U.S. application Ser. No. 97,571 filed Dec. 14, 1970, and now
abandoned, by Walker L. Hopkins, William D. White and Luther F.
Champion and assigned to Texaco Inc., assignee of the present
invention, and a continuation-in-part for all additional subject
matter.
Claims
What is claimed is:
1. A system for controlling the hydrogen to hydrocarbon mole ratio
during the operation of a hydrocarbon converting unit, comprising
means for sensing the flow rate F.sub.c of the hydrocarbon and
providing a corresponding signal, a pair of meters receiving some
of the hydrocarbon, one meter providing a signal corresponding to
the boiling point of the hydrocarbon, the other meter providing a
signal corresponding to the API gravity of the hydrocarbon, means
connected to the one meter for converting the signal from the one
meter to a signal corresponding to the 50 percent boiling point of
the hydrocarbon, computing means connected to the other meter and
to the converting means for providing signal corresponding to the
specific gravity G.sub.c and the average molecular weight M.sub.c
of the hydrocarbon in accordance with the output from the other
meter and from the converting means and the following
equations:
G.sub.c = (141.5/API + 131.5)
M.sub.c = X + Y(API-30) + Z(API-30).sup.2,
X = 10.sup. (1.60783.sup.+.0016007(50%BP).sup.-.45(10 .sup.)(50%BP)
.sup.)
Y = 10.sup. (.sup.-.4244.sup.+.00152X.sup.+.45 .sup.)X .sup.) ,
Z = -.0133+.516(10.sup.-.sup.4)(50% BP),
where API is the API gravity, means for sensing hydrogen entering
the hydrocarbon converting unit and providing corresponding
signals, means connected to the computing means and to the
hydrocarbon sensing means for providing a ratio signal
corresponding to the hydrogen to hydrocarbon mole ratio in
accordance with the signals from the hydrogen sensing means and the
computing means, means for providing a reference signal
corresponding to a predetermined hydrogen to hydrocarbon mole
ratio, means connected to the ratio signal means and to the
reference signal means for providing a signal corresponding to the
difference between the ratio signal and the reference signal, and
means connected to the signal difference means for controlling one
of the entrants to the hydrocarbon converting unit in accordance
with the signal so as to control the hydrogen to hydrocarbon mole
ratio.
2. A system as described in claim 1 in which the controlled entrant
is the hydrogen and is a constituent of a gas entering the
hydrocarbon converting unit.
3. A system as described in claim 2 in which the hydrogen sensing
means includes means connected to the ratio signal means for
sensing the flow rate F.sub.g of the gas containing the hydrogen
and providing a corresponding signal to the ratio signal means,
chromatographic means for sampling the gas and providing signals
corresponding to the percent volumes of different constituents of
the gas, means connected to the chromatograph means and to the
ratio signal means for conducting the signal corresponding to the
percent volume of hydrogen V.sub.H in the gas from the
chromatographic means to the ratio signal means, and first
computing means connected to the chromatographic means and to the
ratio signal for providing a signal corresponding to the specific
gravity G.sub.g of the gas in accordance with the signals from the
chromatographic means and the following equation:
4. A system as described in claim 3 in which the ratio signal means
provides the ratio signal in accordance with the signal from the
hydrocarbon flow rate sensing means, the gas flow rate sensing
means and the first and second computing means and the following
equation:
where V.sub.H is the percentage volume of hydrogen in the gas,
G.sub.g is the specific gravity of the gas, F.sub.g is the rate of
flow of the gas, G.sub.c is the specific gravity of the
hydrocarbon, F.sub.c is the rate of flow of the hydrocarbon, and
M.sub.c is the average molecular weight of the hydrocarbon.
5. A method for controlling the hydrogen to hydrocarbon mole ratio
in a hydrocarbon converting unit, which comprises providing signals
corresponding to hydrogen entering the hydrocarbon converting unit,
sensing the flow rate F.sub.c of hydrocarbon entering the
hydrocarbon converting unit, providing a signal corresponding to
the sensed hydrocarbon flow rate F.sub.c, sensing the boiling point
of the hydrocarbon, providing a signal corresponding to the 50
percent boiling point in accordance with the sensed boiling point,
sensing the API gravity of the hydrocarbon, providing a signal
corresponding to the sensed API gravity, providing a signal
corresponding to the specific gravity G.sub.c of the hydrocarbon in
accordance with the API gravity signal in the following
equation:
G.sub.c = (141.5/API+131.5)
where API is the API gravity, providing a signal corresponding to
the average molecular weight M.sub.c of the hydrocarbon in
accordance with the API gravity signal, the 50 percent boiling
point and the following equations:
M.sub.c = X + Y(API-30)+Z(API-30).sup.2 ,
X = 10.sup. (1.60783.sup.+.0016007(50%) .sup.-.45(10 .sup.)(50%)
.sup.) ,
Y = 10.sup. (.sup.-.4244.sup.+.00152X.sup.+.45(10 .sup.)X .sup.)
,
Z = .0133+.516(10.sup.-.sup.4)(50%)
determining the ratio of hydrogen to hydrocarbon in accordance with
the sensed hydrogen signals, the hydrocarbon flow rate F.sub.c
signal and the hydrocarbon specific gravity G.sub.c and molecular
weight M.sub.c signals; providing a reference signal corresponding
to a predetermined hydrogen to hydrocarbon mole ratio, providing an
error signal corresponding to the difference between the ratio
signal and the reference signal; and controlling the quantity of
one of the entrants to the hydrocarbon converting unit in
accordance with the error signal.
6. A method as described in claim 5 in which the controlled entrant
is the hydrogen and the hydrogen is a constituent of a gas entering
the hydrocarbon converting unit.
7. A method as described in claim 6 in which the step of providing
signals corresponding to the hydrogen entering the hydrocarbon
converting unit includes sensing the flow rate F.sub.g of the gas
containing the hydrogen, providing a signal corresponding to the
sensed flow rate F.sub.g of the gas, sensing the percent volume of
different constituents of the gas, providing a signal corresponding
to the sensed percent volume V.sub.H of hydrogen in the gas,
providing signals corresponding to the percent volumes of the other
constituents of the gas, providing a signal corresponding to the
specific gravity G.sub.g of the gas in accordance with the
constituents signals and the following equation:
8. A device adapted to receive oil and to receive voltages for
providing signals substantially corresponding to the molecular
weight and to the specific gravity of the oil, comprising means for
sensing the 50 percent boiling point and the API gravity of the
received oil and providing signals thereto, a pair of sample and
hold circuits, connected to the sensing means and controlled by a
received voltage, one sample and hold circuit periodically samples
and holds the signal from the sensing means corresponding to the 50
percent boiling point of the oil to provide an output, while the
other sample and hold circuit periodically samples and holds the
signal from the sensing means corresponding to API gravity of the
oil to provide an output, and a computing network connected to the
pair of sample and hold circuits for providing the signal
substantially corresponding to the molecular weight M.sub.c of the
received oil in accordance with the outputs from the sample and
hold circuits, some of the received voltages and the following
equations:
M.sub.c = X + Y(API-30) + Z(API-30).sup.2
Z = -.0133 + .0000516(50%)
X = 10.sup. (1.60783 .sup.+ .sup..0016007(50%).sup.-.45(10
.sup.)(50%) .sup. ),
and
Y = 10.sup. (.sup.-.4244 .sup.+ .sup..00152X .sup.+ .sup..45(10
.sup.)X .sup.)
where API is the API gravity of the received oil, and 50 percent is
the 50 percent boiling point of the received oil; and a second
computing network connected to the other sample and hold circuit
for a signal corresponding to the specific gravity G.sub.c of the
oil in accordance with the output corresponding to the API gravity
from the other sample and hold circuit, some of the received
voltages and the following equation:
G.sub.c = (141.5/API+131.5) .
where API is the API gravity of the hydrocarbon.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to controlling hydrocarbon converting
units and, more particularly, to controlling the hydrogen to
hydrocarbon mole ratio during the hydrocarbon conversion.
2. Description of the Prior Art
Previously, control of the hydrogen to hydrocarbon mole ratio of a
catalytic reforming operation in an oil refinery was done manually.
An article appearing in the "Oil and Gas Journal," Volume 58, No.
13 on Mar. 28, 1960 and entitled Computer Control of Catalytic
Reforming Processes by Mr. Reuben Silver, stated that catalytic
reforming could be controlled by a computer and mentions that the
hydrogen to hydrocarbon mole ratio was a variable in the catalytic
reforming operation. However, the subject article did not disclose
the apparatus for automatically controlling the hydrogen to
hydrocarbon mole ratio. Furthermore, it is not obvious to one
skilled in the art in reading the article how the hydrogen to
hydrocarbon mole ratio may be automatically controlled.
The device of the present invention monitors some of the operating
parameters of a hydrocarbon converting operation, such as catalytic
reforming, and regulates the recycle gas flow in accordance with
the monitored parameters to provide automatic control of the
hydrogen to hydrocarbon mole ratio.
SUMMARY OF THE INVENTION
A system for controlling the hydrogen to hydrocarbon mole ratio of
a mixture in a hydrocarbon converting unit in which the hydrogen
and the hydrocarbon entering the hydrocarbon converting unit are
sensed and corresponding signals are provided. A signal
corresponding to the hydrogen to hydrocarbon ratio is developed in
accordance with the hydrogen and the hydrocarbon signals. A circuit
provides an error signal corresponding to the difference between
the ratio signal and a reference signal corresponding to a
predetermined hydrogen to hydrocarbon mole ratio. The error signal
is used to control one of the entrants to the hydrocarbon
converting unit.
One object of the present invention is to automatically control the
hydrogen to hydrocarbon mole ratio during the conversion of
hydrocarbon.
Another object of the present invention is to control the hydrogen
to hydrocarbon mole ratio during the conversion of the hydrocarbon
in accordance with the equation
Another object of the present invention is to automatically control
the hydrogen to hydrocarbon mole ratio in an operating hydrocarbon
converting unit in accordance with sensed quantities of charge oil
and gas entering the hydrocarbon converting unit so that said
control is substantially instantaneous.
Another object of the present invention is to improve the economy
of the hydrocarbon converting operation by maintaining the hydrogen
to hydrocarbon mole ratio at a predetermined optimum value.
The foregoing and other objects and advantages of the invention
will appear more fully hereinafter from a consideration of the
detailed description which follows, taken together with the
accompanying drawings wherein one embodiment of the invention is
illustrated by way of example. It is to be expressly understood,
however, that the drawings are for illustration purposes only and
are not to be construed as defining the limits of the
invention.
DESCRIPTION OF THE DRAWINGS
FIG. 1 shows a block diagram of a system, constructed in accordance
with the present invention, for controlling the hydrogen to
hydrocarbon mole ratio during the catalytic reforming operation in
a refinery.
FIGS. 2 and 3 are detailed block diagrams of the two signal means
shown in FIG. 1.
DESCRIPTION OF THE INVENTION
During catalytic reforming processing of oil, gas containing
hydrogen is recycled from a product separator to the catalytic
reforming reactor. The gas is used to reduce the rate of coke
formation on the catalyst in the catalytic reforming reactor to
retard the reduction in effectiveness of the catalyst due to the
coke formation. The recycling of the gas requires the use of steam
power which represents an economic cost, the rate of flow of the
oil in the process represents another economic cost, and the
effectiveness of the catalyst represents yet another economic
cost.
It is not practical for the recycle gas to have a constant rate
since the charge oil's molecular weight, composition and flow rate
as well as the composition of the gas may vary. An important facet
of the process is to control the hydrogen to hydrocarbon mole ratio
as a function of the aforementioned economic costs. The hydrogen to
hydrocarbon mole ratio controls the build-up of coke on the
catalyst.
Referring to FIG. 1, charge oil enters a catalytic reactor 5 by way
of a line 6 while recycle gas enters line 6 by way of a line 7. The
reformate from reactor 5 enters a product separator 10 where it is
separated into gas, part of which is discharged through a line 15,
and into a liquid which is discharged through a line 16. A portion
of the gas in line 14 is fed back to reactor 5 as recycle gas by a
compressor 17 driven by a steam motivated turbine 20. The hydrogen
to hydrocarbon mole ratio is controlled by controlling the steam
being applied to turbine 20 thereby controlling the amount of
hydrogen entering reactor 5, as hereinafter explained.
When activated to the `on` position, an on-off switch 22 passes
sampling pulse from a clock 21 to signal means 24, 87 for
controlling signal means 24, 87 to provide for the operation of the
device of the present invention, as hereinafter explained. Switch
22 blocks the sampling pulses from clock 21 when in the `off`
position.
Signal means 24 samples the charge oil in line 6 and provides
signal E.sub.1, E.sub.2 corresponding to the average molecular
weight M.sub.c and the specific gravity G.sub.c, respectively, of
the sample charge oil in accordance with direct current voltages
E.sub.a through E.sub.n, from a source 25 of direct current
voltages, and the following equations:
M.sub.c = X + Y (API-30) + Z(API-30).sup.2 (2)
where
X = 10.sup. (1.60783 .sup.+ .sup..0016007(50%) .sup.- .sup..45(10
.sup.)(50%) .sup.) (3)
y = 10 .sup.(.sup.-.4244 .sup.+ .sup..00152x .sup.+ .sup..45(10
.sup.)x .sup.) (4)
z = -.0133 + .516(10.sup.-.sup.4)(50%) (5)
g.sub.c = (141.5/API+131.5) (6)
where 50 percent is the ASTM 50 percent boiling point in .degree.F,
and API is the API gravity at 60.degree.F.
Signal means 24, shown in detail in FIG. 2, includes analyzers 28,
29 which provide signals E.sub.3 and E.sub.4 corresponding to the
boiling point and the API gravity of the charge oil. The effluent
from analyzers 28, 29 may be returned to line 6 or disposed of as
slop.
Analyzer 28 may be a boiling point analyzer of the type
manufactured by the Technical Oil Tool Corporation as their model
6500. Analyzer 29 is a Dynatol density analyzer. A suitable
analyzer for the density analysis is the series 300G manufactured
by the Automation Products, Inc. and which is temperature
compensated so that signal E.sub.4 corresponds to the API gravity
at 60.degree.F.
Signal E.sub.3 from analyzer 28 is applied to a conventional type
sample and hold circuit 34 which is controlled by the sampling
pulses passed by switch 22. The output from sample and hold circuit
34 is summed with direct current calibration voltage E.sub.a by
summing means 35 to provide a signal E.sub.6 corresponding to the
50 percent boiling point.
A signal E.sub.7 corresponding to Z in the equation 5 is developed
by a multiplier 38 and subtracting means 40. Multiplier 38
multiplies signal E.sub.6 with direct current voltage E.sub.6
corresponding to the term 0.516(10.sup.-.sup.4) in equation 5 to
provide a product signal to summing means 40. Subtracting means 40
subtracts direct voltage E.sub.c corresponding to the term .0133 in
equation 5 from the product signal to provide signal E.sub.7.
A signal E.sub.8 corresponding to X in equation 3 is developed by
multipliers 43, 44 and 45, summing means 48, 49 and an antilog
circuit 50. Multiplier 43 multiplies the 50 percent boiling point
signal E.sub.6 with direct current voltage E.sub.d, corresponding
to the coefficient .0016007 in equation 3, to provide a product
signal to summing means 48 where it is summed with direct current
voltage E.sub.e corresponding to the term 1.60783 in equation 3.
Multiplier 44 in effect squares signal E.sub.6 and provides a
corresponding signal to multiplier 45. Multiplier 45 multiplies the
signal from multiplier 44 with direct negative current voltage
E.sub.f, corresponding to the term -.45(10.sup.-.sup.6) in equation
3, to provide a signal. Summing means 49 sums the signal from
multiplier 45 with the signal from summing means 48. Antilog
circuit 50 provides signal E.sub.8 in accordance with the sum
signal from summing means 49. Antilog circuits 50, 59 are
operational amplifiers, each having a function generator type
feedback element, which may be of the PC-12 type manufactured by
Electronics Associates.
A signal E.sub.9 corresponding to Y in equation 4 is developed by
multipliers 54, 55 and 56, summing means 58, and antilog circuit
59. Signal E.sub.8 from antilog circuit 50 is multiplied with
direct current voltage E.sub.g, corresponding to the coefficient
.00152 in equation 4, by multiplier 56 to provide a corresponding
signal. Signal E.sub.8 is effectively squared by multiplier 54 and
the resulting signal is multiplied with direct current voltage
E.sub.h, corresponding to the coefficient .45 .times.
10.sup.-.sup.5 in equation 4, by multiplier 55 to provide a
corresponding signal. Antilog circuit 59 provides signal E.sub.9 in
accordance with a sum signal from summing means 58 relating to the
summation of the signals from multipliers 55, 56 and negative
direct current voltage E.sub.j corresponding to the term -.4244 in
equation 4.
A conventional type circuit 63 samples and holds signal E.sub.4
from analyzer 29. The output from hold circuit 63 has direct
current voltage E.sub.k, corresponding to term 30 in equation 2,
subtracted from it by subtracting means 64. The output from
subtracting means 64 is squared by a multiplier 68 and the
resulting signal is multiplied with signal E.sub.7 from subtracting
means 40 by a multiplier 69. The output from subtracting means 64
is also multiplied with signal E.sub.9 from antilog circuit 59 by a
multiplier 70. Outputs from multipliers 69, 70 and signal E.sub.8
from antilog circuit 50 are summed by summing means 72 to provide
signal E.sub.1.
Signal E.sub.2 is developed by converting signal E.sub.4
corresponding to the API gravity at 60.degree. to specific gravity
G.sub.c in accordance with equation 6.
Signal E.sub.4 has direct current voltage E.sub.m, corresponding to
the term 131.5 in equation 6, added to it by summing means 75. A
divider 78 divides direct current voltage E.sub.n, corresponding to
the term 141.5 in equation 6, by the output from adding means 75 to
provide signal E.sub.2.
Referring again to FIG. 1, conventional types sensing means 75 and
flow transmitter 76 cooperate to provide a signal E.sub.14
corresponding to the flow rate of the charge oil in line 6. Signals
E.sub.2, E.sub.14 are multiplied by a multiplier 80 to provide a
product signal to a divider 81. Divider 81 divides the product
signal from multiplier 80 with signal E.sub.1 from signal means 24
to provide a signal E.sub.16 corresponding to the term F.sub.c
G.sub.c /M.sub.c in equation 1.
Signal means 87 provides signals E.sub.19, E.sub.20 corresponding
to the percent volume of hydrogen V.sub.h in the recycle gas and to
the specific gravity G.sub.g of the recycle gas, respectively.
Signal means 87 is shown in detail in FIG. 3. Chromatographic means
88 which includes a chromatograph that may be of the type
manufactured by Beckman Instruments with a Beckman model 620
programmer and a Beckman model D analyzer, providing signals
E.sub.22 through E.sub.22H corresponding to the hydrogen, methane,
ethane, propane, normal butane, isobutane, normal pentane,
isopentane, and the hexanes and heavier constituents, respectively,
of the recycle gas. Sample and hold circuits 90 through 90H
periodically sample and hold signals E.sub.22 through E.sub.22H in
response to the sampling pulses from switch 22 to provide signals
E.sub.19 through E.sub.19H, respectively. The specific gravity of
the recycle gas is determined in accordance with the following
equation:
Signals E.sub.19 through E.sub.19H are applied to multipliers 94
through 94H, respectively, where they are multiplied with a direct
current voltage E.sub.o corresponding to 0.01 to provide product
signals. The product signals from multipliers 94 through 94H are
multiplied with direct current voltages E.sub.p through E.sub.pH,
respectively, by multipliers 95 through 95H. The product signals
from multipliers 95 through 95H correspond to the molecular weights
of hydrogen, methane, ethane, propane, normal butane, isobutane,
normal pentane, isopentane and the hexanes constituents,
respectively, and are summed by summing means 99 to provide a sum
signal. The sum signal from summing means 99 is divided by direct
current voltage E.sub.q, corresponding to the term 29 in equation
6, by a divider 100 to provide specific gravity signal
E.sub.20.
Referring to FIG. 1, signals E.sub.19, E.sub.20 are multiplied with
each other by a multiplier 102 to provide a product signal,
corresponding to the product V.sub.H G.sub.g to a multiplier 103. A
conventional type sensing element 104 and a flow transmitter 105,
which may also be of a conventional type, senses the flow rate
F.sub.g of the recycle gas and provides a corresponding signal
E.sub.25 to multiplier 103 where signal E.sub.25 is multiplied with
the signal from multiplier 102 to provide a signal E.sub.26
corresponding to product V.sub.H G.sub.g F.sub.g of equation 1.
Signal E.sub.26 is divided by signal E.sub.16 from divider 81 by a
divider 110 to provide an output to an amplifier 112 having a gain
corresponding to 1/13261.21. Although an amplifier is used, a
multiplier for multiplying the output from divider 110 with a
direct current voltage corresponding to 1/13261.21 may also be
used. The output from amplifier 112 corresponds to the actual
hydrogen to hydrocarbon mole ratio.
Source 25 provides a variable amplitude direct current reference
voltage E.sub.9 which corresponds to a desired hydrogen to
hydrocarbon mole ratio such as the current economical optimum
hydrogen to hydrocarbon mole ratio. Ratio controller 116 provides
an output signal to a conventional type speed controller 120, in
accordance with output from amplifier 112 and voltage E.sub.9, to
change its set point accordingly. Speed controller 120 also
receives a signal E.sub.27 from a tachometer 121 corresponding to
the rotational speed of turbine 20. Speed controller 120 acts as a
safety device to prevent turbine 20 from exceeding its speed
limitation. When the speed of turbine 20 differs from the set point
speed of speed controller 120, speed controller 120 provides a
signal to flow recorder controller 125 receiving a signal E.sub.28,
which corresponds to the flow rate of the steam to turbine 20, from
a sensing element 126. The signal from speed controller 120 adjusts
the set point of flow recorder controller 125. Flow recorder
controller 125 provides a pneumatic control signal to a valve 130
corresponding to the difference between the signal from sensing
element 126 and the set point to control the flow of the steam
thereby controlling the flow rate of the recycle gas.
The device of the present invention was heretofore described in
terms of analog computing elements. It would be obvious to one
skilled in the art to use a digital computer to control the
hydrogen to hydrocarbon mole ratio. Analog signals E.sub.3,
E.sub.4, E.sub.14, E.sub.19, E.sub.20 and E.sub.25 are converted to
digital signals by conventional type analog-to-digital converters.
The digital computer is programmed to solve the aforementioned
equations, using the digital signals, to provide a digital output
corresponding to the difference between the actual hydrogen to
hydrocarbon mole ratio and the target hydrogen to hydrocarbon mole
ratio. The digital output is converted to an analog signal by a
conventional type digital-to-analog converter, which is applied to
speed controller 120.
Although a hydrogen to hydrocarbon mole ratio control system for a
catalytic reforming unit has been disclosed, the control system may
also be used for the hydrogenation of middle distillates (kerosine
and light gas oils). If the charge oil is lube oil, which requires
processing by a hyfinishing unit, signal means 24 would have to be
modified to provide a signal corresponding to the molecular weight
of the lube oil. However, the overall control concept would not
change.
The device of the present invention as heretofore described
automatically maintains the hydrogen to hydrocarbon mole ratio
during a hydrocarbon converting operation in accordance with the
equation disclosed in the abstract and a desired hydrogen to
hydrocarbon mole ratio. The device of the present invention
economically controls the hydrogen to hydrocarbon mole ratio in an
operating catalytic reforming unit in accordance with a
predetermined optimum value using sensed conditions of charge oil
and gas entering the catalytic reforming unit so that said control
is substantially instantaneous.
* * * * *