This instruction manual provides installation,
operating, maintenance, and parts information for
the Fisher C1 Series pressure controllers and
transmitters shown in figure 1. Refer to separate
instruction manuals for information regarding the
control valve, actuator, and accessories.
Do not install, operate, or maintain C1 Series
pressure controllers and transmitters without first
being fully trained and qualified in valve, actuator,
and accessory installation, operation, and
maintenance. To avoid personal injury and property
damage, it is important to carefully read, understand,
and follow all the contents of this manual, including
all safety cautions and warnings. If you have any
questions about these instructions, contact your
Emerson Process Management sales office before
proceeding.
Description
The C1 Series pneumatic pressure controllers and
transmitters use a bellows or Bourdon tube sensing
element to sense the gauge pressure, vacuum,
compound pressure, or differential pressure of a
liquid or gas. The controller or transmitter output is a
pneumatic pressure signal that can be used to
operate a final control element, indicating device, or
recording device.
Unless otherwise noted, all NACE references are to
NACE MR0175−2002.
September 2009
Educational Services
For information on available courses for C1 Series
controllers and transmitters, as well as a variety of
other products, contact:
Emerson Process Management
Educational Services, Registration
P.O. Box 190; 301 S. 1st Ave.
Marshalltown, IA 50158−2823
Phone: 800−338−8158 or
Phone: 641−754−3771
FAX: 641−754−3431
e−mail: education@emersonprocess.com
Installation
WARNING
To avoid personal injury or property
damage resulting from the sudden
release of pressure:
D Always wear protective clothing,
gloves, and eyewear when performing
any installation operations.
D Personal injury or property
damage may result from fire or
explosion if natural gas is used as the
supply medium and appropriate
preventive measures are not taken.
Preventive measures may include, but
are not limited to, one or more of the
following; remote venting of the unit,
re−evaluating the hazardous area
classification, ensuring adequate
ventilation, and the removal of any
ignition sources. For information on
remote venting of this controller/
transmitter, refer to page 8.
D If installing into an existing
application, also refer to the WARNING
at the beginning of the Maintenance
section in this instruction manual.
D Check with your process or safety
engineer for any additional measures
that must be taken to protect against
process media.
Specifications
Specifications for the C1 Series controllers and
transmitters are listed in table 1. Table 2 explains
available configurations and options.
2
Standard Installation
The instruments are normally mounted vertical with
the case/cover as shown in figure 1. If installing the
instrument in any other position, be sure that the
vent opening shown in figure 2 is facing downward.
Page 3
Instruction Manual
September 2009
Available Configurations
See table 2
Input Signal
Type: J Gauge pressure, J vacuum,
J compound pressure, or J differential pressure
of a liquid or gas
Limits: See table 3 or 4
Output Signal
Proportional−Only or Proportional−Plus−Reset
Controllers and Transmitters:
J 0.2 to 1.0 bar (3 to 15 psig) or
J 0.4 to 2.0 bar (6 to 30 psig) pneumatic
pressure signal
Differential Gap Controllers:
J 0 and 1.4 bar (0 and 20 psig) or
J 0 and 2.4 bar (0 and 35 psig) pneumatic
pressure signal
Action: Control action is field reversible between
J direct (increasing sensed pressure produces
increasing output signal) and J reverse
(increasing sensed pressure produces decreasing
output signal).
Supply Pressure Requirements
(1)
See table 5
C1 Controllers and Transmitters
Table 1. Specifications
Supply and Output Connections
1/4 NPT internal
Common Signal Pressure Conversions
See table 6
Proportional Band Adjustment
For Proportional−Only Controllers: Full output
pressure change adjustable from J 2% to 100%
of the sensing element range for 0.2 to 1.0 bar (3
to 15 psig) or J 4% to 100% of the sensing
element range for 0.4 to 2.0 bar (6 to 30 psig)
For Proportional−Plus−Reset Controllers: Full
output pressure change adjustable from J 3% to
100% of the sensing element range for 0.2 to 1.0
bar (3 to 15 psig), or J 6% to 100% of the
sensing element range for 0.4 to 2.0 bar (6 to 30
psig)
Differential Gap Adjustment
For Differential Gap Controllers:
Full output pressure change adjustable from
15% to 100% of sensing element range
Reset Adjustment
For Proportional−Plus−Reset Controllers:
Adjustable from 0.01 to 74 minutes per repeat
(100 to 0.01 repeats per minute)
Supply Pressure Medium
Air or natural gas
Air Quality: Supply pressure must be clean, dry air
that meets the requirements of ISA Standard
7.0.01. A maximum 40 micrometer particle size in
the air system is acceptable. Further filtration
down to 5 micrometer particle size is
recommended. Lubricant content is not to exceed
1 ppm weight (w/w) or volume (v/v) basis.
Condensation in the air supply should be
minimized
Natural Gas: Natural gas must be clean, dry,
oil−free, and noncorrosive. H2S content should
not exceed 20 ppm.
Steady−State Air Consumption
(2,3)
0.2 to 1.0 bar (3 to 15 psig): 0.08 normal m3/hour
(3 scfh)
0.4 to 2.0 bar (6 to 30 psig): 0.12 normal m3/hour
(4.5 scfh)
−continued−
Zero Adjustment (Transmitters Only)
Continuously adjustable to position span of less
than 100% anywhere within the sensing element
range
Span Adjustment (Transmitters Only)
Full output pressure change adjustable from 6 to
100% of sensing element range
Performance
Repeatability: 0.5% of sensing element range
Deadband (Except Differential Gap
Controllers)
(4)
: 0.1% of process sensing element
span
Typical Frequency Response at 100%
Proportional Band
Output to Actuator: 0.7 Hz and 110 degree phase
shift with 1850 cm3 (113 inches3) volume,
actuator at mid−stroke
Output to Positioner Bellows: 9 Hz and 130
degree phase shift with 0.2 to 1.0 bar (3 to 15
psig) output to 33 cm3 (2 inches3) bellows
3
Page 4
Instruction Manual
C1 Controllers and Transmitters
Table 1. Specifications (continued)
Ambient Operating Temperature Limits
J Standard Construction:−40 to 71_C (−40 to
160_F)
J High Temperature Construction:−18 to
104_C (0 to 220_F)
Anti−reset windup (differential pressure relief) and
process pressure gauge options are only
available in the standard construction
If the process temperature is outside the ambient
operating range of the controller, the length of the
capillary tube run from the sensor point to the
controller process input may be adjusted to
protect the controller from the process
temperature
Typical Ambient Temperature Operating
Influence
Proportional Control only:
Output pressure changes $3.0% of sensing
element range for each 28_C (50_F) change in
temperature between −40 and 71_C (−40 and
160_F) for a controller set at 100% proportional
band
Proportional−Plus−Reset Control:
Output pressure changes $2.0% of sensing
element range for each 28_C (50_F) change in
temperature between −40 and 71_C (−40 and
160_F) for a controller set at 100% proportional
band
(1)
September 2009
Transmitters only:
Output pressure changes $3.0% of sensing
element range for each 28_C (50_F) change in
temperature between −40 and 71_C (−40 and
160_F) for a transmitter set at 100% span
Hazardous Area Classification
Complies with the requirements of ATEX Group II
Category 2 Gas and Dust
Refer to figure 25 for location of ATEX marking
Approximate Weight
8.2 kg (18 pounds)
Options
Case pressure tested to 0.14 bar (2 psig)
Declaration of SEP
Fisher Controls International LLC declares this
product to be in compliance with Article 3
paragraph 3 of the Pressure Equipment Directive
(PED) 97 / 23 / EC. It was designed and
manufactured in accordance with Sound
Engineering Practice (SEP) and cannot bear the
CE marking related to PED compliance.
However, the product may bear the CE marking to
indicate compliance with other applicable
European Community Directives.
1. The pressure/temperature limits in this document and any applicable standard or code limitation should not be exceeded.
2. Normal m3/hr: normal cubic meters per hour (m3/hr, 0_C and 1.01325 bar, absolute). Scfh: standard cubic feet per hour (ft3/hr, 60_F and 14.7 psig).
3. To convert from air flow rate to natural gas flow rate multiply by 1.29.
4. An adjustable differential gap (differential gap controllers) is equivalent to an adjustable deadband.
Table 2. Available Configurations
TYPE NUMBER
DESCRIPTION
Proportional−only controller
Proportional−plus−reset controller
Differential gap controller− − −
TransmitterC1D
4
Bourdon Tube Sensing
Element (Gauge Pressure Only)
Without anti−reset windup
With anti−reset windup− − −
C1PC1B
Bellows Sensing Element
Gauge PressureDifferential Pressure
C1D
Page 5
Instruction Manual
September 2009
C1 Controllers and Transmitters
Table 3. Bourdon Tube Pressure Range and Materials
PRESSURE RANGES
(1,2)
MAXIMUM ALLOWABLE STATIC PRESSURE LIMITS
StandardWith Optional Travel Stop
BarPsigBarPsigBarPsig
0 to 2.0
0 to 4.0
0 to 7.0
0 to 14
0 to 20
0 to 40
0 to 70
0 to 100
0 to 200
0 to 350
0 to 550
0 to 700
1. If the process can trip to a pressure outside of the operating range of the sensing element, a commercially available device, such as an overpressure protector, may be used to
protect against pressure surges and pulsations.
2. Range marked on Bourdon tube may be in kPa (1 bar = 100 kPa)
3. Bourdon tube may be pressurized to limit shown without permanent zero shift.
4. With travel stop set at 110% of the range.
5. Bourdon tubes are also available in NACE compliant material. Contact your Emerson Process Management sales office for additional information.
0 to 30
0 to 60
0 to 100
0 to 200
0 to 300
0 to 600
0 to 1000
0 to 1500
0 to 3000
0 to 5000
0 to 8000
0 to 10.000
2.0
4.0
7.0
14
20
40
70
100
200
350
550
700
30
60
100
200
300
600
1000
1500
3000
5000
8000
10,000
3.3
6.6
11
19
29
50
83
115
230
380
550
700
(3)
48
96
160
280
420
720
1200
1650
3300
5500
8000
10,000
(4)
MATERIAL
(5)
316 stainless steel
Table 4. Bellows Pressure Ranges and Materials
PRESSURE RANGES
(1)
0 to 150 mbar (0 to 60 inch wc)
Vacuum
0 to 340 mbar (0 to 10 inch Hg)
0 to 1.0 bar (0 to 30 inch Hg)
75 mbar vac. to 75 mbar (30 inch wc vac. to 30 inch wc)
Compound Pressure
500 mbar vac. to 500 mbar (15 inch Hg vac. to 7.5 psig)
1.0 bar vac. to 1.0 bar (30 inch Hg vac. to 15 psig)
Gauge Pressure
0 to 150 mbar (0 to 60 inch wc)
0 to 250 mbar
0 to 350 mbar
(3)
(0 to 100 inch wc)
(4)
(0 to 140 inch wc)
0 to 0.35 bar (0 to 5 psig)
Positive pressure
0 to 0.5 bar (0 to 7.5 psig)
0 to 0.7 bar (0 to 10 psig)
0 to 1.0 bar (0 to 15 psig)
0 to 1.4 bar (0 to 20 psig)
0 to 2.0 bar (0 to 30 psig)
0 to 300 mbar (0 to 80 inch wc)
Differential Pressure
(5)
0 to 0.7 bar (0 to 10 psi)
0 to 1.4 bar (0 to 20 psi)
0 to 2.0 bar (0 to 30 psi)
1. If the process can trip to a pressure outside of the operating range of the sensing element, a commercially available device, such as an overpressure protector, may be used to protect against
pressure surges and pulsations.
2. Bellows may be pressured to limit shown without permanent zero shift.
3. Transmitter only.
4. Except transmitter.
5. The overrange limit for these sensing elements is a differential pressure equal to the maximum allowable static pressure limit.
MAXIMUM ALLOWABLE STATIC
PRESSURE LIMITS
Brass
Construction
(2)
Stainless Steel
Construction
BarPsigBarPsig
1.4
2.8
2.8
1.4
2.8
2.8
1.4
1.4
2.8
2.8
2.8
2.8
2.8
2.8
2.8
1.4
2.8
2.8
−−−
20
40
40
20
40
40
20
20
40
40
40
40
40
40
40
20
40
40
−−−
−−−
−−−
6.9
−−−
6.9
6.9
−−−
−−−
−−−
−−−
−−−
−−−
6.9
−−−
6.9
−−−
−−−
−−−
6.9
−−−
−−−
100
−−−
100
100
−−−
−−−
−−−
−−−
−−−
−−−
100
−−−
100
−−−
−−−
−−−
100
OUTPUT SIGNAL RANGE
Bar
Psig
1. If this pressure is exceeded, control may be impaired.
0.2 to 1.0 or 0 and 1.4 (differential gap)1.42.8
0.4 to 2.0 or 0 and 2.4 (differential gap)2.42.8
3 to 15 or 0 and 20 (differential gap)2040
6 to 30 or 0 and 35 (differential gap)3540
Table 5. Supply Pressure Requirements
NORMAL OPERATING SUPPLY
PRESSURE
(1)
MAXIMUM ALLOWABLE SUPPLY PRESSURE
TO PREVENT INTERNAL PART DAMAGE
5
Page 6
Instruction Manual
C1 Controllers and Transmitters
Panel Mounting
Refer to figure 2.
Cut a hole in the panel surface according to the
dimensions shown in figure 2. Remove the cap
screws (key 252), brackets (key 251), and vent
assembly (key 28). Slide the controller or transmitter
into the cutout and reattach the brackets. Tighten the
cap screw located in the center of each bracket to
draw the case snugly and evenly against the panel.
Reinstall the vent unless a remote vent will be used.
Wall Mounting
Refer to figure 2.
Drill four holes in the wall using the dimensions
shown in figure 2. In the bracket (key 251) are 8.7
mm (0.3438 inch) diameter holes. Back out the cap
screw located in the center of each bracket. (The
screws are used for panel mounting but are not
required for wall mounting.) If tubing runs through
the wall, drill holes in the wall to accommodate the
tubings. Figure 2 shows the pressure connection
locations in the back of the case.
Mount the controller to the bracket using the four cap
screws (key 252) provided. Attach the bracket to the
wall, using suitable screws or bolts.
Pipestand Mounting
Refer to figure 2.
Use a hammer and punch to knock out the blanks in
the two holes indicated in the back view of figure 2.
Attach the spacer spools (key 228) and the mounting
plate (key 213) to the controller with cap screws,
lock washers, and nuts (keys 215, 221, and 216).
Attach the controller to a 2−inch (nominal) pipe with
pipe clamps (key 250).
Actuator Mounting
Refer to figure 3.
Controllers specified for mounting on a control valve
actuator are mounted at the factory. If the instrument
is ordered separately for installation on a control
valve actuator, mount the instrument according to
the following instructions.
Mounting parts for the different actuator types and
sizes vary. Two typical actuator−mounting
installations are shown in figure 3; see the parts list
for parts required for the specific actuator type and
size involved.
September 2009
Use a hammer and punch to knock out the blanks in
the two holes indicated in the back view of figure 2.
Attach the spacer spools (key 228) and the mounting
plate (key 213) to the controller with machine
screws, lock washers, and nuts (keys 215, 221, and
216).
Attach the mounting bracket to the actuator yoke
with cap screws (key 222) and, if needed, spacer
spools. On some designs, the mounting bracket is
attached to the actuator diaphragm casing rather
than to the yoke.
Pressure Connections
WARNING
To avoid personal injury or property
damage resulting from the sudden
release of pressure, do not install any
system component where service
conditions could exceed the limits
given in this manual. Use
pressure−relieving devices as required
by government or accepted industry
codes and good engineering practices.
All pressure connections on C1 Series instruments
are 1/4 NPT internal. Use 6 mm (1/4−inch) or 10 mm
(3/8−inch) pipe or tubing for supply and output
piping. The pressure connection locations are shown
in figure 2.
Supply Pressure
WARNING
Severe personal injury or property
damage may occur from an
uncontrolled process if the instrument
supply medium is not clean, dry,
oil−free and noncorrosive. While use
and regular maintenance of a filter that
removes particles larger than 40
micrometers in diameter will suffice in
most applications, check with an
Emerson Process Management field
office and industry instrument supply
medium quality standards for use with
hazardous gas or if you are unsure
about the proper amount or method of
air filtration or filter maintenance.
6
Page 7
Instruction Manual
September 2009
180.8
(7.12)
VENT ASSEMBLY
(KEY 28)
PIPESTAND MOUNTING
2 INCH
(NOMINAL)
PIPE
C1 Controllers and Transmitters
142.7
(5.62)
65.8
(2.59)
23.1
(0.91)
KNOCK−OUT
63.5
(2.50)
63.5
(2.50)
69.1
(2.72)
BACK VIEW
KNOCK−OUT
244.3
(9.62)
215.9
(8.50)
8.7
(11/32)
MOUNTING
HOLES
PANEL MOUNTINGWALL MOUNTING
NOTES:
1. ALL CONNECTIONS ARE 1/4 NPT INTERNAL.
2
HIGH−PRESSURE CONNECTION FOR DIFFERENTIAL−PRESSURE UNITS.
3
LOW−PRESSURE CONNECTION FOR DIFFERENTIAL−PRESSURE UNITS.
E1052
Figure 2. Panel, Wall, and Pipestand Mounting
Supply pressure must be clean, dry air that meets
the requirements of ISA Standard 7.0.01. A
maximum 40 micrometer particle size in the air
system is acceptable. Further filtration down to 5
micrometer particle size is recommended. Lubricant
content is not to exceed 1 ppm weight (w/w) or
volume (v/v) basis. Condensation in the air supply
should be minimized. Alternatively, natural gas may
be used as the supply pressure medium. Gas must
be clean, dry, oil−free, and noncorrosive. H2S
content should not exceed 20 ppm.
Use a suitable supply pressure regulator to reduce
the supply pressure source to the normal operating
218.9
(8.62)
CUTOUT FOR
PANEL MOUNTING
14.3
(0.56) R
FOUR HOLES
FOR WALL
MOUNTING
101.6
(4.00)
mm
(INCH)
supply pressure shown in table 5. Connect supply
pressure to the SUPPLY connection at the back of
the case.
WARNING
To avoid personal injury or property
damage resulting from the sudden
release of process pressure, use a
high pressure regulator system when
operating the controller or transmitter
from a high pressure source.
7
Page 8
Instruction Manual
C1 Controllers and Transmitters
If operating the controller or transmitter from a high
pressure source [up to 138 bar (2000 psig)], use a
high pressure regulator system, such as the Fisher
1367 High Pressure Instrument Supply System. For
1367 system installation, adjustment, and
maintenance information, refer to the 1367
High−Pressure Instrument Supply System with
Overpressure Protection instruction manual,
D100343X012.
Process Pressure
WARNING
To avoid personal injury or property
damage resulting from the sudden
release of pressure when using
corrosive media, make sure the tubing
and instrument components that
contact the corrosive medium are of
suitable noncorrosive material.
Also refer to the Installation Warning
at the beginning of this section.
The pressure connections to the controller depend
upon the type of pressure sensing, gauge or
differential. Gauge pressure controllers use either a
Bourdon tube or bellows as the sensing element, as
indicated in table 2. Differential pressure controllers
use two bellows to sense differential pressure.
For gauge pressure instruments: The control
pressure block (key 10 in figure 21) has two
connections. Process pressure can be connected
either to the CONTROL connection on the back of
the case, or to the connection on the left side of the
case, shown in figure 2, depending on the
instrument application. Plug the unused connection.
For differential pressure instruments: Connect
the low pressure line to the CONTROL connection
on the side of the case and the high pressure line to
the CONTROL connection on the back of the case
as shown in figure 2.
When installing process piping, follow accepted
practices to ensure accurate transmission of the
process pressure to the controller or transmitter.
Install shutoff valves, vents, drains, or seal systems
as needed in the process pressure lines. If the
instrument is located such that the adjacent process
pressure lines will be approximately horizontal, the
lines should slope downward to the instrument for
liquid−filled lines and upward to instruments for
gas−filled lines. This will minimize the possibility of
September 2009
Table 6. Common Signal Pressure Conversions
Mpskg/cm
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.10
0.12
0.14
0.15
0.17
0.18
0.20
0.22
0.23
0.24
0.34
0.55
0.69
1.03
1. Values as listed in ANSI/S7.4.
2. Values as listed in IEC Standard 382.
3. Values rounded to correspond with kPa values.
0.2
0.3
0.4
0.5
0.6
0.8
0.8
1.0
1.0
1.3
1.4
1.5
1.8
1.9
2.0
2.2
2.3
2.5
3.5
5.6
7.0
10.5
2
(3)
barkPaPsi
0.2
0.3
0.4
0.5
0.6
0.8
0.8
1.0
1.0
1.2
1.4
1.5
1.7
1.9
2.0
2.2
2.3
2.4
3.4
5.5
6.9
10.3
(2)
(2)
(3)
20
35
40
50
60
75
80
95
100
125
140
150
170
185
200
220
230
240
345
550
690
1035
(1)
(1)
(1)
(1)
3
5
6
7
9
11
12
14
15
18
20
22
25
27
30
32
33
35
50
80
100
150
air becoming trapped in the sensor with liquid−filled
lines or of condensation becoming trapped with
gas−filled lines. The recommended slope is 83 mm
per meter (1 inch per foot).
If a controller is being used in conjunction with a
control valve to control pipeline pressure, connect
the process pressure line in a straight section of pipe
approximately 10 pipe diameters from the valve but
away from bends, elbows, and areas of abnormal
fluid velocities. For pressure−reducing service, the
process line must be connected downstream of the
valve. For pressure−relief service, the process
pressure line must be connected upstream of the
control valve. Install a needle valve in the process
pressure line to dampen pulsations.
Vent Assembly
WARNING
Personal injury or property damage
could result from fire or explosion of
accumulated gas, or from contact with
hazardous gas, if a flammable or
hazardous gas is used as the supply
pressure medium. Because the
instrument case and cover assembly
do not form a gas−tight seal when the
assembly is enclosed, a remote vent
8
Page 9
Instruction Manual
September 2009
line, adequate ventilation, and
necessary safety measures should be
used to prevent the accumulation of
flammable or hazardous gas. However,
a remote vent pipe alone cannot be
relied upon to remove all flammable
and hazardous gas. Vent line piping
should comply with local and regional
codes, and should be be as short as
possible with adequate inside diameter
and few bends to reduce case
pressure buildup.
CAUTION
When installing a remote vent pipe,
take care not to overtighten the pipe in
the vent connection. Excessive torque
will damage the threads in the
connection.
The vent assembly (key 28, figure 2) or the end of a
remote vent pipe must be protected against the
entrance of all foreign matter that could plug the
vent. Use 13 mm (1/2−inch) pipe for the remote vent
pipe, if one is required. Check the vent periodically
to be certain it has not become plugged.
C1 Controllers and Transmitters
SUPPLY PRESSURE
REGULATOR
GE33946−A
TYPICAL ROTARY ACTUATOR
Controller Operation
Proportional−Only Controllers
This section describes the adjustments and
procedures for calibration and startup. Adjustment
locations are shown in figure 4 unless otherwise
specified. All adjustments must be made with the
cover open. When the adjustments and calibration
procedures are complete, close and latch the cover.
To better understand the adjustments and overall
operation of the controller, refer to the Principle of
Operation section in this manual for
proportional−only controllers. Refer also to the
schematic diagram in figure 13.
Adjustments
Adjustment: Set Point
Adjust the pressure setting knob by turning the knob
clockwise to increase the set point and
counterclockwise to decrease the set point. Note
that the dial setting and actual process pressure may
vary significantly, especially with a wide proportional
band setting.
SUPPLY PRESSURE
REGULATOR
GE33947−A
TYPICAL SLIDING STEM ACTUATOR
Figure 3. Actuator Mounting
Adjustment: Proportional Band
To adjust the proportional band, rotate the
proportional band adjustment knob to the desired
value.
The proportional band adjustment determines the
amount of change in controlled pressure required to
cause the control valve to stroke fully. It may be
adjusted from 2 to 100 percent for 0.2 to 1.0 bar (3
to 15 psig) or 4 to 100 percent for 0.4 to 2.0 bar (6 to
30 psig) of the nominal sensing element pressure
rating.
Unless otherwise indicated, key number locations
are shown in figure 4.
Provide a process pressure source capable of
simulating the process pressure range of the
controller. If an output pressure gauge is not
provided, install a suitable pressure gauge for
calibration purposes.
Connect a pressure source to the supply pressure
regulator and be sure the regulator is delivering the
correct supply pressure to the controller. The
controller must be connected open loop (Open loop:
The controller output pressure changes must be
dead ended into a pressure gauge). The following
procedures use a 0.2 to 1.0 bar (3 to 15 psig) output
pressure range as an example. For a 0.4 to 2.0 bar
(6 to 30 psig) output range, adjust the values as
appropriate.
1. Complete the above connections and provide a
process pressure equal to the sensing element
range.
2. Rotate the proportional band adjustment knob,
shown in figure 4, to 1.5 (15 percent proportional
band).
3. Verify that the calibration adjuster screws
(key 48) are at mid−position in the calibration
adjuster (key 36) slots.
IF OUTPUT IS:
NOZZLE
BELOW
8 TO 10 PSIG
(0.6 TO 0.7 BAR)
MOVE ADJUSTER
RIGHT
ABOVE
8 TO 10 PSIG
(0.6 TO 0.7 BAR)
MOVE ADJUSTER
NOTE:
3 TO 15 PSIG (0.2 TO 1.0 BAR) OUTPUT SHOWN.
FOR 6 TO 30 PSIG (0.4 TO 2.0 BAR) OUTPUT, ADJUST
VALUES AS APPROPRIATE.
Depending upon the controller action, perform one
or the other of the following procedures.
For reverse−acting controllers:
4. Apply an input pressure equal to the sensing
element upper range value.
10
Page 11
Instruction Manual
September 2009
5. Rotate the pressure setting knob to the maximum
value.
6. Adjust the nozzle (key 54) until the controller
output pressure is between 0.6 and 0.7 bar (8
and 10 psig).
7. Apply an input pressure equal to the sensing
element lower range value.
8. Rotate the pressure setting knob to the minimum
value.
Note
When performing the span adjustment
in step 9, do not watch the output
gauge while changing the calibration
adjuster. The change in output is not a
good indication of the change in span.
While moving the calibration adjuster,
the output pressure may change in the
opposite direction than expected. For
example, while moving the calibration
adjuster to increase span, the output
pressure may decrease. This should
be disregarded since even though the
output pressure decreases, the span is
increasing.
Proper controller response depends
on nozzle−to−flapper alignment.
When performing span adjustments,
carefully loosen both calibration
adjuster screws while holding the
calibration adjuster in place. Then
move the calibration adjuster slightly
in the required direction by hand or
using a screwdriver. Verify proper
nozzle−to−flapper alignment and hold
the calibration adjuster in place while
tightening both adjustment screws.
9. If the output is not between 0.6 and 0.7 bar (8
and 10 psig), adjust the controller span by loosening
the two adjusting screws (key 48) and moving the
calibration adjuster (key 36) a small distance as
indicated in figure 5.
10. Repeat steps 4 through 9 until no further
adjustment is necessary.
11. Proceed to the startup procedure for
proportional controllers.
For direct−acting controllers:
4. Apply an input pressure equal to the sensing
element lower range value.
C1 Controllers and Transmitters
IF OUTPUT IS:
BELOW
8 TO 10 PSIG
(0.6 TO 0.7 BAR)
MOVE ADJUSTER
NOTE:
3 TO 15 PSIG (0.2 TO 1.0 BAR) OUTPUT SHOWN.
FOR 6 TO 30 PSIG (0.4 TO 2.0 BAR) OUTPUT, ADJUST
VALUES AS APPROPRIATE.
A6154 / IL
LEFT
FLAPPER
Figure 6. Direct−Acting Controller Span
Adjustment—Proportional−Only Controllers
5. Rotate the pressure setting knob to the minimum
value.
6. Adjust the nozzle (key 54) until the controller
output pressure is between 0.6 and 0.7 bar (8
and 10 psig.)
7. Apply an input pressure equal to the sensing
element upper range value.
8. Rotate the pressure setting knob to the maximum
value.
Note
When performing the span adjustment
in step 9, do not watch the output
gauge while changing the calibration
adjuster. The change in output is not a
good indication of the change in span.
While moving the calibration adjuster,
the output pressure may change in the
opposite direction than expected. For
example, while moving the calibration
adjuster to increase span, the output
pressure may decrease. This should
be disregarded since even though the
output pressure decreases, the span is
increasing.
Proper controller response depends
on nozzle−to−flapper alignment.
When performing span adjustments,
carefully loosen both calibration
MOVE ADJUSTER
RIGHT
NOZZLE
ABOVE
8 TO 10 PSIG
(0.6 TO 0.7 BAR)
11
Page 12
Instruction Manual
C1 Controllers and Transmitters
adjuster screws while holding the
calibration adjuster in place. Then
move the calibration adjuster slightly
in the required direction by hand or
using a screwdriver. Verify proper
nozzle−to−flapper alignment and hold
the calibration adjuster in place while
tightening both adjustment screws.
9. If the output is not between 0.6 and 0.7 bar (8
and 10 psig), adjust the controller span by loosening
the two adjusting screws (key 48) and moving the
calibration adjuster (key 36) a small distance as
indicated in figure 6.
10. Repeat steps 4 through 9 until no further
adjustment is necessary.
11. Proceed to the startup procedure for
proportional controllers.
1. Be sure that the supply pressure regulator is
delivering the proper supply pressure to the
controller.
2. Rotate the pressure setting knob to the desired
set point.
3. Set the proportional band adjustment to 100
percent for fast processes (example: liquid pressure
or liquid flow). For slow processes (example:
temperature), calculate the percentage from the
equation below:
For a slow process, determine the initial proportional
band setting in percent from the following equation:
September 2009
2 Allowable Overshoot
Pressure Span
For example:
2 0.14 bar
2.1 bar
2 2 psig
(
30 psig
1.3 proportional band setting
4. Proportional Action
Disturb the system by tapping the flapper lightly or
change the set point a small amount and check for
system cycling. If the system does not cycle then
lower the proportional band (raising the gain) and
disturb the system again. Continue this procedure
until the system cycles. At that point, double the
proportional band setting.
Proportional band adjustment affects
the set point. Proportional−only
controllers will show some offset from
set point depending upon proportional
band setting and process demand.
After adjusting the proportional band,
re−zero by carefully rotating the nozzle
(key 54) until the steady−state process
pressure equals the pressure setting
dial reading.
This tuning procedure may be too conservative for
some systems. The recommended proportional band
setting should be checked for stability by introducing
a disturbance and monitoring the process.
This section describes the adjustments and
procedures for calibration and startup. The
adjustment locations are shown in figure 7 unless
otherwise specified. All adjustments must be made
with the cover open. When the adjustments and
calibration procedures are complete, close and latch
the cover. To better understand the adjustments and
overall operation of the controller, refer to the
Principle of Operation section in this manual for
proportional−plus−reset controllers. Refer also to the
schematic diagram in figure 13.
Adjustments
Adjustment: Set Point
Adjust the pressure setting knob by turning the knob
clockwise to increase the set point and
counterclockwise to decrease the set point.
Rotate the knob until the indicator points to the
desired set point pressure value. The pressure
setting dial will reflect the desired set point if the
controller is accurately calibrated.
Adjustment: Proportional Band
To adjust the proportional band, rotate the
proportional band adjustment knob to the desired
value.
The proportional band adjustment determines the
amount of change in controlled pressure required to
cause the control valve to stroke fully. It may be
adjusted from 3 to 100 percent for 0.2 to 1.0 bar (3
to 15 psig) or 6 to 100 percent for 0.4 to 2.0 bar (6 to
30 psig) of the nominal sensing element pressure
rating.
Adjustment: Reset
To adjust reset action turn the knob clockwise to
decrease the minutes per repeat. Turn the knob
counterclockwise to increase the minutes per repeat.
Increasing the minutes per repeat provides a slower
reset action.
The reset adjustment dial is calibrated in minutes per
repeat. By definition, this is the time in minutes
required for the reset action to produce an output
change which is equal to the change produced by
proportional control action. This is in effect, the time
in minutes required for the controller to increase (or
decrease) its output pressure by an amount equal to
a proportional increase (or decrease) caused by a
change in set point or process pressure.
13
Page 14
Instruction Manual
C1 Controllers and Transmitters
Adjustment: Anti−Reset Windup
The externally mounted differential relief valve can
be mounted to relieve on increasing or decreasing
output pressure.
Calibration
Calibration: Proportional−Plus−Reset Controllers
Unless otherwise indicated, key number locations
are shown in figure 7.
Before starting this procedure:
D Provide a process pressure source capable of
simulating the process pressure range of the
controller.
D If an output pressure gauge is not provided,
install a suitable pressure gauge for calibration
purposes. The controller must be connected open
loop (Open loop: The controller output pressure
changes must be dead ended into a pressure
gauge).
Note
C1P and C1B controllers with
anti−reset windup are supplied with
two O−rings (key 81), an anti−reset
windup cover (key 80), and two
machine screws (key 82). Use these
parts in the next step.
1. For C1P and C1B controllers with anti−reset
windup record the direction of the arrow on the
anti−reset windup assembly (key 190, in figure 22).
Remove the assembly and install the two O−rings
(key 81), and cover (key 80) supplied with the
controller. Secure the cover with the two machine
screws (key 82) provided.
2. Connect regulated supply pressure to the
controller. Do not exceed the normal operating
pressure in table 5.
3. Rotate the reset knob to 0.01 minutes per repeat
(fastest setting).
4. Rotate the proportional band adjustment knob
to 1.5 (15 percent proportional band).
5. Verify that the calibration adjuster screws
(key 48) are at mid−position in the calibration
adjuster (key 36) slots.
Depending upon the controller action, perform one
or the other of the following procedures.
September 2009
IF OUTPUT IS:
ABOVE
8 TO 10 PSIG
(0.6 TO 0.7 BAR)
MOVE ADJUSTER
NOTE:
3 TO 15 PSIG (0.2 TO 1.0 BAR) OUTPUT SHOWN.
FOR 6 TO 30 PSIG (0.4 TO 2.0 BAR) OUTPUT, ADJUST
VALUES AS APPROPRIATE.
6. Apply an input pressure equal to the sensing
element upper range value.
7. Rotate the pressure setting knob to the maximum
value.
8. Adjust the nozzle (key 54) until the controller
output pressure is between 0.6 and 0.7 bar (8
and 10 psig).
9. Apply an input pressure equal to the sensing
element lower range value.
10. Rotate the pressure setting knob to the
minimum value.
Note
When performing the span adjustment
in step 11, do not watch the output
gauge while changing the calibration
adjuster. The change in output is not a
good indication of the change in span.
While moving the calibration adjuster,
the output pressure may change in the
opposite direction than expected. For
example, while moving the calibration
adjuster to increase span, the output
pressure may decrease. This should
be disregarded since even though the
output pressure decreases, the span is
increasing.
14
Page 15
Instruction Manual
September 2009
Proper controller response depends
on nozzle−to−flapper alignment.
When performing span adjustments,
carefully loosen both calibration
adjuster screws while holding the
calibration adjuster in place. Then
move the calibration adjuster slightly
in the required direction by hand or
using a screwdriver. Verify proper
nozzle−to−flapper alignment and hold
the calibration adjuster in place while
tightening both adjustment screws.
11. If the output pressure is not between 0.6 and 0.7
bar (8 and 10 psig), adjust the controller span by
loosening the two adjusting screws (key 48) and
moving the calibration adjuster (key 36) a small
distance as indicated in figure 8.
12. Repeat steps 6 through 11 until no further
adjustment is necessary.
13. For C1P and C1B controllers with anti−reset
windup, remove the two machine screws, anti−reset
windup cover, and two O−rings installed in step 1 of
this procedure. Install the anti−reset windup
assembly (key 190) with the arrow pointing in the
direction recorded in step 1.
14. Proceed to the Startup procedures for
proportional−plus−reset controllers.
For direct−acting controllers:
6. Apply an input pressure equal to the sensing
element lower range value.
7. Rotate the pressure setting knob to the minimum
value.
8. Adjust the nozzle (key 54) until the controller
output pressure is between 0.6 and 0.7 bar (8
and 10 psig).
9. Apply an input pressure equal to the sensing
element upper range value.
10. Rotate the pressure setting knob to the
maximum value.
Note
When performing the span adjustment
in step 11, do not watch the output
gauge while changing the calibration
adjuster. The change in output is not a
good indication of the change in span.
While moving the calibration adjuster,
C1 Controllers and Transmitters
IF OUTPUT IS:
BELOW
8 TO 10 PSIG
(0.6 TO 0.7 BAR)
MOVE ADJUSTER
NOTE:
3 TO 15 PSIG (0.2 TO 1.0 BAR) OUTPUT SHOWN.
FOR 6 TO 30 PSIG (0.4 TO 2.0 BAR) OUTPUT, ADJUST
VALUES AS APPROPRIATE.
the output pressure may change in the
opposite direction than expected. For
example, while moving the calibration
adjuster to increase span, the output
pressure may decrease. This should
be disregarded since even though the
output pressure decreases, the span is
increasing.
Proper controller response depends
on nozzle−to−flapper alignment.
When performing span adjustments,
carefully loosen both calibration
adjuster screws while holding the
calibration adjuster in place. Then
move the calibration adjuster slightly
in the required direction by hand or
using a screwdriver. Verify proper
nozzle−to−flapper alignment and hold
the calibration adjuster in place while
tightening both adjustment screws.
11. If the output pressure is not between 0.6 and 0.7
bar (8 and 10 psig), adjust the controller span by
loosening the two adjusting screws (key 48) and
moving the calibration adjuster (key 36) a small
distance as indicated in figure 9.
12. Repeat steps 6 through 11 until no further
adjustment is necessary.
13. For C1P and C1B controllers with anti−reset
windup remove the two machine screws, anti−reset
windup cover, and two O−rings installed in step 1 of
this procedure. Install the anti−reset windup
assembly (key 190) with the arrow pointing in the
direction recorded in step 1.
ABOVE
8 TO 10 PSIG
(0.6 TO 0.7 BAR)
MOVE ADJUSTER
RIGHT
NOZZLE
15
Page 16
Instruction Manual
C1 Controllers and Transmitters
14. Proceed to the Startup procedures for
proportional−plus−reset controllers.
Calibration: Anti−Reset Windup
Controllers with anti−reset windup have a differential
relief valve assembly (figure 22). This relief valve is
set at the factory to relieve at a 0.3 bar (5 psi)
pressure difference between the reset bellows
pressure and the proportional bellows pressure. The
valve can be adjusted to relieve from 0.14 to 0.4 bar
(2 to 7 psig).
The relief valve can relieve on either rising controller
output pressure or falling controller output pressure.
If the arrow on the relief valve points toward the
bottom of the controller case as shown in figure 22,
the valve will relieve on falling output pressure. If the
arrow points in the opposite direction, the valve will
relieve on rising output pressure. The valve can be
removed and reinstalled with the arrow pointing in
the opposite direction to change the relief action.
1. Be sure that the supply pressure regulator is
delivering the proper supply pressure to the
controller.
2. Rotate the pressure setting knob to the desired
set point.
3. Start with a reset setting of 0.05 minutes per
repeat (m/r) for fast processes, and 0.5 m/r for slow
processes.
4. Set the proportional band adjustment to 100
percent for fast processes (example: liquid pressure
or liquid flow). For a slow process (example:
temperature), calculate the percentage from the
equation below:
For a slow process, determine the initial proportional
band setting in percent from the following equation:
2 Allowable Overshoot
Pressure Span
100% + P.B.
September 2009
5. Proportional Action:
Disturb the system by tapping the flapper lightly or
change the set point a small amount and check for
system cycling. If the system does not cycle then
lower the proportional band (raising the gain) and
disturb the system again. Continue this procedure
until the system cycles. At that point, double the
proportional band setting and begin tuning the reset.
6. Reset Action:
Disturb the system. If the system does not cycle then
speed up the reset and disturb the system again.
Continue this procedure until the system cycles.
When the system cycles multiply the reset time
setting by a factor of three (3) and slow the reset
down to the new value. The reset is now tuned.
This tuning procedure may be too conservative for
some systems. The recommended proportional band
and reset setting should be checked for stability by
introducing a disturbance and monitoring the
process as previously described. For some
applications, tighter control may be desirable.
Differential Gap Controllers
This section describes the adjustments and
procedures for calibration and startup. The
adjustment locations are shown in figure 4 unless
otherwise specified. The output of each controller is
checked at the factory before the instrument is
shipped.
To convert a differential gap controller to a
proportional−only controller or vice versa, refer to the
appropriate procedure in the Maintenance section.
If the process pressure can be varied through all or
part of the sensing element range or through the two
desired switching points, use the process pressure
for calibration. If not, provide a pressure source to
simulate the process pressure range for calibration
procedures.
To better understand the adjustments and overall
operation of the controller, refer to the Principle of
Operation section in this manual for differential gap
controllers and the schematic diagram in figure 13.
For example:
2 0.14 bar
2.1 bar
2 2 psig
()
30 psig
1.3 proportional band setting
16
100% ^ 13%
100% ^ 13%
Adjustments
Adjustment: Set Point
The position of the pressure setting knob determines
the location of the differential gap within the range of
the pressure sensing element. Move the pointer to
the desired pressure where the output of the
controller should switch from zero to full supply
Page 17
Instruction Manual
September 2009
PROPORTIONAL BAND KNOB SETTING
A2202−3 / IL
Figure 10. Differential Gap Adjustment for Differential Gap
DIFFERENTIAL GAP (PERCENT OF ELEMENT RANGE)
Controllers
pressure with rising process pressure (direct−acting
controllers) or with falling process pressure
(reverse−acting controllers).
Adjustment: Proportional Band
C1 Controllers and Transmitters
b. Unscrew the spring adjustor (key 65),
removing the bias spring (key 70) and washers
(key 62) with it.
c. Unclip the lock spring (key 72). Remove the
indicator scale (key 69) and proportional band
adjustment knob (key 73).
d. Remove the gain adjustment bar (key 63). Flip
it over so it attaches to the opposite side of the
cantilever spring (key 8) as shown in figure 16
and screw it back down.
e. Flip over the indicator scale (key 69); install it
and the proportional band adjustment knob
(key 73) as a unit. Snap in the lock spring
(key 72).
f. Tighten down the spring adjustor (key 65) with
the bias spring (key 70) and washers (key 62)
until it stops against the gain adjustment bar
(key 63).
The proportional band adjustment shown in figure 4
determines the width of the differential gap. The
width of the gap is the difference between the
process pressures at which the controller output will
switch from zero to full supply pressure, or from full
supply pressure to zero. The relationship between
the proportional band dial setting and the differential
gap is shown in figure 10.
Calibration: Differential Gap Controllers
The output of each controller is checked at the
factory before the unit is shipped. Before placing the
controller in control of a process loop, check to verify
that the controller is calibrated correctly for the
application. The controller must be connected open
loop (Open loop: The controller output pressure
changes must be dead ended into a pressure
gauge).
1. Temporarily convert the differential gap controller
to proportional−only controller by disconnecting the
proportional tubing (key 25, figure 16) from the
mounting base. Reinstall the tubing into the other
connection in the mounting base. Remove the
proportional band assembly and invert it as shown in
figure 16. Do not invert the reversing block (key 37,
figure 16).
2. Temporarily invert the proportional band
assembly (refer to figure 18):
a. Turn the proportional band assembly (key 73)
to 10.
g. Turn the proportional band adjustment knob to
the 10 setting. If it cannot be turned to the 10
setting, loosen the spring adjustor (key 65).
3. Calibrate using the calibration procedure for
proportional−only controllers found on page 10 of
this manual.
4. When calibration is complete, return the tubing
(key 25) and the proportional band assembly to their
original locations and continue on with step 5 of this
procedure.
Note
After reinstalling the tubing (key 25)
and proportional band assembly a
slight offset of the output pressure will
be noticed due to a combination of
switching from the proportional
bellows to the reset bellows and the
repositioning of the cantilever spring.
Performing step 6b below adjusts for
this offset.
5. Refer to figure 10 to determine the proportional
band dial setting required for the desired differential
gap.
For example, assume that a 0 to 100 psig sensing
element is being used and the controller is to switch
from zero to full supply pressure at a process
17
Page 18
Instruction Manual
C1 Controllers and Transmitters
ADJUSTER SCREWS (KEY 48)
GE34729−B
E1061
CALIBRATION ADJUSTER (KEY 36)
Figure 11. Transmitter Adjustment Locations
FLAPPER (KEY 40)
NOZZLE (KEY 54)
September 2009
ZERO ADJUSTMENT KNOB
(KEY 58)
PRESSURE SETTING
DIAL (KEY 6)
SPAN ADJUSTMENT KNOB
pressure of 80 psig with rising process pressure and
from full supply pressure to zero at 20 psig with
falling pressure. (This is for a direct−acting
controller.) The differential gap is:
5.5 bar * 1.3 bar
6.9 bar
80 psig * 20 psig
(
100 psig
100% + 60%
100% + 60%
)
From figure 10, the proportional band dial setting
should be approximately 4.5; rotate the proportional
band adjustment knob to 4.5.
6. Setting the process pressure
For a Direct−Acting Controller:
a. Rotate the pressure setting knob to the
pressure at which the controller output is to
switch to the upper switching point (zero to full
supply pressure) with rising process pressure. In
the above example, this pressure is 5.5 bar (80
psig).
b. Increase pressure to the sensing element
while monitoring the output pressure gauge. The
controller output pressure should switch from
zero to full supply pressure when the upper
switching point is reached with rising input
pressure.
Note
If the upper switching point is not
correct, adjust the nozzle to correct
the error. Repeat step 6b until the
input pressure and upper switching
point are at the desired setting.
c. With falling input pressure, the output should
switch from full supply pressure back to zero
when the lower switching point is reached.
Reverse−acting controllers produce the opposite
response.
7. Vary the process pressure and observe the
switching points. Widen or narrow the differential
gap by rotating the proportional band adjustment
knob, then repeat the above steps.
If the output is within the limits stated, refer to the
startup procedures in this section. If the output
pressure cannot be adjusted within the limits stated,
refer to the maintenance procedures.
18
Page 19
Instruction Manual
September 2009
Startup: Differential Gap Controllers
Calibrate the controller prior to this procedure.
1. Be sure that the supply pressure regulator is
delivering the proper supply pressure to the
controller.
2. Adjust the proportional band setting for the proper
differential gap (see figure 10).
3. If the controller is used in conjunction with a
control valve, slowly open the upstream and
downstream manual shutoff valves, and close the
bypass valves.
4. To change the differential gap, perform steps 1
through 5 of the calibration for differential gap
controllers procedure.
Transmitter Operation
This section describes the adjustments and
procedures for calibration and startup. Refer to
figure 11 for the adjustment locations. All
adjustments must be made with the cover open.
When the adjustments and calibration procedures
are complete, close and latch the cover.
To better understand the adjustments and overall
operation of the transmitter, refer to the Principle of
Operation section in this manual for transmitters.
Refer also to the schematic diagram in figure 13.
Adjustments
Adjustment: Zero
The pressure setting dial is marked ZERO
ADJUSTMENT PRESSURE SETTING. Zero is in the
center of the dial, and the pressure values increase
to the right and left of the center as shown in figure
11. To set the zero, rotate the pointer around the
pressure setting dial. Rotate the pointer clockwise to
increase or counterclockwise to decrease the output
depending on transmitter action and desired setting.
For direct−acting transmitters, zero adjustment
determines the process pressure at which the
transmitter output signal will be at its lower range
limit.
The dial (key 6) graduations are approximate
indications of the transmitter zero setting. When
making adjustments, do not rely solely on the dial
setting. Monitor the process pressure and output
pressure to be sure the desired settings are attained.
C1 Controllers and Transmitters
Adjustment: Span
The span adjustment is graduated from 0 to 10. A
setting of 10 represents a span setting of 100
percent of the process sensing element range. The
transmitter achieves the highest accuracy when the
span is 100 percent.
The transmitter span adjustment shown in figure 11
is the same as the controller proportional band
adjustment.
Calibration: Transmitters
The output of each transmitter is checked at the
factory before the unit is shipped. The transmitter
provides an output signal that is proportional to the
pressure applied to the sensing element. The output
pressure has no direct effect on the process
pressure.
The transmitter is calibrated at the factory and
should not need additional adjustment. Use the
following calibration procedures when the sensing
element has been changed or other maintenance
procedures have altered the calibration of the
transmitter. The following procedures use a 0.2 to
1.0 bar (3 to 15 psig) output pressure range as an
example. For other output pressure ranges [such as
0.4 to 2.0 bar (6 to 30 psig)] adjust the values to
match the application.
Provide a process pressure source capable of
simulating the process pressure range of the
transmitter. If an output pressure gauge is not
provided, install a suitable pressure gauge for
calibration purposes. Connect a pressure source to
the supply pressure regulator and be sure the
regulator is delivering the correct supply pressure to
the transmitter.
Note
For stability, some transmitter
applications will require additional
volume than just the gauge. Provide a
minimum volume of approximately 25
cm3 (1.5 in3) or greater if stability is a
problem.
Unless otherwise indicated, key number locations
are shown in figure 11.
1. Complete the above connections and provide a
process pressure equal to the sensing element
range.
2. Rotate the span adjustment knob to the
maximum setting on the dial (100 percent span).
19
Page 20
Instruction Manual
C1 Controllers and Transmitters
IF OUTPUT IS:
BELOW
15 PSIG
(1.0 BAR)
MOVE ADJUSTER
NOTE:
3 TO 15 PSIG (0.2 TO 1.0 BAR) OUTPUT SHOWN.
FOR 6 TO 30 PSIG (0.4 TO 2.0 BAR) OUTPUT, ADJUST
VALUES AS APPROPRIATE.
A6156 / IL
LEFT
Figure 12. Transmitter Span Adjustment
3. Verify that the calibration adjuster screws
(key 48) are at mid−position in the calibration
adjuster (key 36) slots.
Depending upon the transmitter action, perform one
or the other of the following procedures.
For reverse−acting transmitters:
4. Rotate the zero adjustment knob to zero.
5. Apply an input pressure equal to the sensing
element upper range limit.
6. Adjust the nozzle (key 57) until the transmitter
output pressure is at 0.2 bar (3 psig).
7. Set the input pressure equal to zero.
Note
Proper transmitter response depends
on nozzle−to−flapper alignment.
When performing the span adjustment
in step 8, carefully loosen both
calibration adjuster screws while
holding the calibration adjuster in
place. Then move the calibration
adjuster slightly in the required
direction by hand or using a
screwdriver. Verify proper
nozzle−to−flapper alignment and hold
the calibration adjuster in place while
tightening both adjustment screws.
ABOVE
15 PSIG
(1.0 BAR)
MOVE ADJUSTER
RIGHT
September 2009
8. If the output pressure is not 15 psig, adjust the
span by loosening the two adjusting screws (key 48)
and moving the calibration adjuster (key 36) a small
distance as indicated in figure 12.
9. Repeat steps 4 through 8 until no further
adjustment is necessary.
10. Proceed to the startup procedure for
transmitters.
For direct−acting transmitters:
4. Rotate the zero adjustment knob to zero.
5. Set the input pressure to zero.
6. Adjust the nozzle (key 54) until the transmitter
output pressure is at 0.2 bar (3 psig).
7. Apply an input pressure equal to the sensing
element upper range value.
Note
Proper transmitter response depends
on nozzle−to−flapper alignment.
When performing the span adjustment
in step 8, carefully loosen both
calibration adjuster screws while
holding the calibration adjuster in
place. Then move the calibration
adjuster slightly in the required
direction by hand or using a
screwdriver. Verify proper
nozzle−to−flapper alignment and hold
the calibration adjuster in place while
tightening both adjustment screws.
8. If the output pressure is not 15 psig, adjust the
span by loosening the two adjusting screws (key 48)
and moving the calibration adjuster (key 36) a small
distance as indicated in figure 12.
9. Repeat steps 4 through 8 until no further
adjustment is necessary.
10. Proceed to the startup procedure for
transmitters.
Startup: Transmitters
1. Be sure that the supply pressure regulator is
delivering the proper supply pressure to the
transmitter.
2. Refer to the calibration procedures for the
transmitter initial settings.
Figure 13. Schematic of Reverse−Acting Proportional−Only and Proportional−Plus−Reset Controllers
EXHAUST
NOZZLE
SENSED
PRESSURE
PROPORTIONAL-ONLY
CONTROLLER
RESET BELLOWS
PROPORTIONAL
BELLOWS
C1 Controllers and Transmitters
INLET END OF
RELAY VALVE
SMALL DIAPHRAGM
LARGE DIAPHRAGM
RESTRICTION
VENT
CANTILEVER
SPRING
PRESSURE SETTING KNOB
PRESSURE SETTING DIAL
RESET
PROPORTIONAL
BAND ADJUSTMENT
KNOB
BELLOWS
PROPORTIONAL
BELLOWS
PROPORTIONAL-PLUS-RESET
CONTROLLER
RESET
VALVE
3. If the transmitter is used in conjunction with a
control valve, slowly open the upstream and
downstream manual shutoff valves, and close the
bypass valves.
Principle of Operation
The following sections describe the operation of a
controller or transmitter using a Bourdon tube
sensing element. The operation is the same for an
instrument using a bellows sensing element (key 71,
figure 24) except that movement of the beam is
caused by expansion or contraction of the bellows or
differential bellows.
Proportional−Only Controllers
As shown in figure 13, supply pressure enters the
relay and bleeds through the fixed orifice before
escaping through the nozzle. Nozzle pressure also
registers on the large relay diaphragm, and loading
pressure (controller output pressure) registers on the
small relay diaphragm.
A change in the process pressure moves the beam
and flapper with respect to the nozzle by either
expanding or contracting the Bourdon tube arc. An
increasing process pressure with direct action (or
decreasing pressure with reverse action) produces a
nozzle−flapper restriction that increases the loading
on the large relay diaphragm and opens the relay
valve. Additional supply pressure flows through the
relay chamber to increase the loading pressure on
the control valve actuator. A decreasing process
pressure with direct action (or increasing pressure
with reverse action) produces a nozzle−flapper
opening that bleeds off pressure on the large relay
diaphragm and opens the relay valve to exhaust
controller output pressure from the actuator.
This controller output pressure change feeds back to
the proportional bellows, countering the pressure
change in the nozzle and equalizes the relay
diaphragm pressure differential. The relay valve
maintains a new loading pressure according to the
change in sensed pressure.
If the proportional band adjustment is at its
maximum setting (10), the cantilever spring in the
proportional band assembly has a low spring rate,
allowing more feedback motion to be transferred
from the proportional bellows for a change in output
pressure. As the effective length of the cantilever is
reduced, its spring rate increases, causing less
feedback motion from proportional bellows. Setting
the cantilever spring to its maximum length results in
a proportional band of 100%. The lower the
Figure 14. Schematic of Reverse−Acting Proportional−Plus−Reset Controller with Anti−Reset Windup
proportional band adjustment, the shorter the
effective length of the cantilever spring. The spring
rate of the cantilever spring increases as its length
shortens, allowing less motion to be transferred from
the bellows to the beam and flapper for a given
change in output pressure.
Proportional−Plus−Reset Controllers
Action of a proportional−plus−reset controller is
similar to that of a proportional−only controller
except that feedback from the controller output
pressure is piped to a reset bellows as well as to the
proportional bellows as shown at the right in
figure 13.
With an increasing controller output pressure,
pressure in the reset bellows increases. Increases in
CANTILEVER
SPRING
PROPORTIONAL
BELLOWS
RESET VALVE
reset bellows pressure moves the beam and flapper
closer to the nozzle, starting another increase of
pressure throughout the system. Pressure buildup
continues until the controlled pressure is brought
back to the set point. The reset valve is adjustable to
vary the amount of delay in the reset action. Closing
the reset valve increases the delay in reset action.
Controllers with Anti−Reset Windup
During a prolonged difference between set point and
the controlled variable, such as encountered with
intermittent control applications (e.g., batch
temperature control or wide open monitors on
pressure control), reset ramps the controller output
to either zero or full supply pressure; this condition is
reset windup. When the controlled variable crosses
the set point, there will be a delay before the
22
Page 23
Instruction Manual
September 2009
controller output responds to the change in
controlled variable. Anti−reset windup minimizes this
delay and permits returning the controlled variable to
set point more quickly with minimal overshoot.
As shown in figure 14 a proportional−plus−reset
controller with anti−reset windup includes a
differential relief valve. The valve consists of two
pressure chambers separated by a spring−loaded
diaphragm.
For the controller shown in figure 14, proportional
pressure registers rapidly on the spring side of the
relief valve diaphragm as well as in the proportional
bellows, and reset pressure registers on the
opposite side of the relief valve diaphragm. As long
as controlled pressure changes are slow enough for
normal proportional and reset action, the relief valve
spring will keep the relief valve diaphragm from
opening. However, a large or rapid decrease in
controller pressure will cause the relay to exhaust
loading pressure from the control device rapidly, and
also from the proportional system and spring side of
the relief diaphragm. If this decrease on the spring
side of the diaphragm is greater than the relief valve
spring setting, the diaphragm will move off the relief
valve orifice and permit the proportional pressure on
the opposite side of the relief valve diaphragm to
bleed rapidly into the reset bellows. The anti−reset
windup action also can be reversed to relieve with
an increasing proportional pressure.
Differential Gap Controllers
With a differential gap controller, feedback pressure
does not counteract the change in flapper position
as it does in a proportional−only controller. Instead,
feedback pressure is piped to the bellows located on
the side of the beam and flapper opposite the nozzle
(the proportional bellows in figure 13). Then, as
controller output pressure increases, feedback
pressure moves the flapper closer to the nozzle to
again increase controller output pressure. This
process continues rapidly until the controller output
pressure is at the upper range limit. The action of a
differential gap controller is so rapid that output
pressure changes from zero to maximum as soon as
the switching point is reached. The action is similar
with falling output pressure. Lower feedback
pressure lowers the bellows pressure, which moves
the flapper away from the nozzle. This again
reduces the output pressure and continues until the
output pressure is zero.
C1 Controllers and Transmitters
Transmitters
Action of a pneumatic transmitter is similar to that of
a proportional−only controller. Since the output
pressure of the transmitter has no effect on the
process pressure, transmitter output pressure is a
proportional measure of the process pressure. The
proportional band adjustment determines the span of
the transmitter, and the pressure setting mechanism
determines the zero of the transmitter.
Maintenance
If the installation includes a Fisher 67 Series filter
regulator, periodically open the drain on the filter
regulator to drain accumulated moisture. Also, push
the spring−out cleaning wire on the relay orifice.
Check the opening of the vent assembly (key 28,
figure 2) or the opening of the remote vent pipe, if
one is used. If necessary, clean the openings.
Parts are subject to normal wear and must be
inspected and replaced as necessary. The
frequency of inspection and parts replacement
depends upon the severity of the service conditions.
WARNING
The following maintenance procedures
require taking the controller out of
service. To avoid personal injury and
property damage caused by the
release of pressure or process fluid,
observe the following before starting
maintenance:
D Always wear protective clothing,
gloves, and eyewear.
D Provide some temporary means
of control for the process before
taking the controller out of service.
D Provide a means of containing the
process fluid before removing any
measurement devices from the
process.
D Use lock−out procedures to be
sure that the above measures stay in
effect while you work on the
equipment.
D Personal injury or property
damage may result from fire or
explosion if natural gas is used as the
supply medium and appropriate
23
Page 24
Instruction Manual
C1 Controllers and Transmitters
preventative measures are not taken.
Preventative measures may include,
but are not limited to, one or more of
the following; Remote venting of the
unit, re−evaluating the hazardous area
classification, ensuring adequate
ventilation, and the removal of any
ignition sources. For information on
remote venting of this controller/
transmitter, refer to page 8.
D Check with your process or safety
engineer for any additional measures
that must be taken to protect against
process media.
Replacing Gauges
Refer to figures 21 and 22 for key number locations
unless otherwise directed.
Three gauge configurations are available for C1
units.
D Output and supply pressure indications
September 2009
correct range so they are not damaged
by overpressure.
Note
Key 2 is used as both a supply gauge
and an output gauge on units without
a process pressure gauge. A quantity
of 2 is required for these units. On
units with a process pressure indicator
gauge (key 4), key 2 is used for the
output gauge. A quantity of 1 is
required for these units.
Use key 3 for supply pressure
indication when a process pressure
gauge is installed. Key 3 installs on the
supply pressure regulator.
1. Shut off the supply pressure and process lines to
the controller or transmitter.
2. Remove the gauge to be replaced:
D Unscrew the output or supply gauge (key 2)
from the relay base.
D Output and process pressure indications
D Output, process, and supply pressure
indications
One gauge type (key 2) is used for both output and
supply pressure indications when the gauges are
installed inside the controller case. Key 2 features a
1/8−inch connecting stem that matches the threaded
gauge boss extending from the relay base.
In some cases, a process pressure gauge (key 4)
covers the position of the internal supply pressure
gauge. The supply pressure gauge has been
removed and replaced with a pipe plug (key 15). The
pressure control block (key 10) is different to
accommodate a different control tubing assembly
(key 23) with a pressure connection (key 14) for a
process pressure gauge. If a supply pressure gauge
is required, a gauge with a 1/4−inch connecting stem
(key 3) must be mounted on the supply pressure
regulator.
CAUTION
Before performing this procedure, be
sure the replacement gauges are the
D Unscrew the process pressure gauge (key 4)
from the process connection (key 14).
D Unscrew the supply gauge (key 3) from the
supply pressure regulator.
3. Coat the threads of the replacement gauge with a
sealant.
4. Screw the replacement gauge into the relay base,
process connection, or supply pressure regulator.
5. Check for leaks by applying the correct supply
pressure with the nozzle capped to produce full
output pressure.
Replacing Bourdon Tube
Refer to figure 23 for key number locations unless
otherwise directed.
1. Shut off the supply pressure and process lines to
the controller or transmitter.
2. Unscrew the machine screw (key 56) to
disconnect the link (key 16) and bearing (key 31)
from the beam (key 39). Be careful to avoid losing
the bearing (key 31). Washer(s) (key 62) for the
machine screw (key 56) are at times furnished for
insertion at the beam (key 39) connection to ensure
alignment of the connecting link (key 16).
24
Page 25
Instruction Manual
September 2009
PROPORTIONAL TUBING
RELAY TUBING
(KEY 24)
FLAPPER/SCREW
(KEYS 40 AND 46)
REVERSE
ACTING POSITION
REVERSING BLOCK
GE28263−A
E1064
(KEY 37)
RESET VALVE
(KEY 256)
(KEY 25)
REVERSE ACTING
C1 Controllers and Transmitters
PROPORTIONAL TUBING
RELAY TUBING
REVERSING BLOCK
PROPORTIONAL
BAND ASSY
BELLOWS
(KEY 52)
DIRECT ACTING POSITION
FLAPPER/SCREW
(KEYS 40 AND 46)
PROPORTIONAL-ONLY CONTROLLER OR TRANSMITTER
(KEY 24)
(KEY 37)
RESET VALVE
(KEY 256)
(KEY 25)
DIRECT ACTING
BELLOWS
(KEY 52)
PROPORTIONAL
BAND ASSY
RESET TUBING
RELAY TUBING
FLAPPER/SCREW
(KEYS 40 AND 46)
REVERSE ACTING
POSITION
REVERSING BLOCK
GE34722−A
E1065
(KEY 37)
(KEY 24)
REVERSE ACTING
(KEY 27)
PROPORTIONAL TUBING
(KEY 27)
PROPORTIONAL
BAND ASSY
BELLOWS
(KEY 52)
PROPORTIONAL-PLUS-RESET CONTROLLER
Figure 15. Reverse/Direct Acting Tubing Connections for Proportional Controllers or Transmitter
3. Disconnect the control tubing (key 23, figure 22).
Unscrew the two screws (key 55) and washers
(key 45), and remove the Bourdon tube (key 5).
4. Unscrew the machine screw (key 56), and
remove the link and bearing (keys 16 and 31) from
the Bourdon tube. Be careful to avoid losing the
bearing.
5. Attach the link and bearing to the replacement
Bourdon tube.
6. Attach the Bourdon tube with two machine
screws and washers (keys 55 and 45).
RELAY TUBING
(KEY 24)
REVERSING BLOCK
(KEY 37)
DIRECT ACTING
POSITION
FLAPPER/SCREW
(KEYS 40 AND 46)
RESET TUBING
(KEY 27)
PROPORTIONAL TUBING
(KEY 27)
BELLOWS
(KEY 52)
PROPORTIONAL BAND ASSY
DIRECT ACTING
7. Connect the link and bearing to the beam
(key 39).
8. After connecting the link to the beam, make sure
that the link is parallel to the sensing element (key 5)
and the beam (key 39) so that it does not bind
against the sensing element of the beam. Figure 17
shows a properly aligned connecting link; the
connecting link is not in contact with the Bourdon
tube or or washers. When properly configured, the
connecting link moves freely when touched.
Washers (key 62) are used as shims to set
parallelism.
25
Page 26
Instruction Manual
C1 Controllers and Transmitters
PROPORTIONAL TUBING
RELAY TUBING
(KEY 24)
FLAPPER/SCREW
(KEYS 40 AND 46)
REVERSE ACTING
POSITION
REVERSING BLOCK
GE34724−
A
E1066
(KEY 37)
Figure 16. Reverse/Direct Acting Tubing Connection for Differential Gap Controller
9. Check to be sure that the beam is parallel with
the bottom of the case and that the link (key 16) is in
tension. If the beam is not parallel with the case,
loosen the machine screws (key 55), reposition the
Bourdon tube to get the beam parallel, and retighten
the screws.
10. If a Bourdon tube with a different range was
installed, remove the machine screw and washer
(keys 61 and 60) and dial (key 6). Install a new dial
having an adjustment range corresponding to the
range of the Bourdon tube. If an optional process
pressure gauge (key 4, figure 21) is being used,
install a new gauge with the appropriate
measurement capability.
11. Check all tubing connections for leaks and the
Bourdon tube machine screws, tighten as
necessary. Perform the appropriate calibration
procedures.
(KEY 25)
REVERSE ACTING
BELLOWS
(KEY 52)
PROPORTIONAL BAND ASSY
DIFFERENTIAL-GAP CONTROLLER
September 2009
RELAY TUBING
(KEY 24)
REVERSING BLOCK
(KEY 37)
DIRECT ACTING
POSITION
FLAPPER/SCREW
(KEYS 40 AND 46)
PROPORTIONAL TUBING
(KEY 25)
DIRECT ACTING
PROPORTIONAL BAND
ASSY
BELLOWS
(KEY 52)
block (key 8, figure 21) to the bellows assembly
(key 71), at the pressure block end.
3. Unscrew the four machine screws (key 41,
figure 21 or 22), and remove the pressure sensing
subassembly from the case.
4. Remove the bellows yoke machine screws and
washers (keys 98 and 99), and move the bellows
yoke to the right to permit access to the link screw.
5. Disconnect the link (key 71M) and bearing
(key 71L) from the beam. Be careful to avoid losing
the bearing.
6. Loosen the nuts that secure the bellows
assembly (key 71), and remove this assembly from
the bellows yoke (key 100).
7. For a gauge−pressure sensing element (only one
bellows in the assembly), install the proper bellows
spring (key 104) into the bellows assembly if the
input signal range is being changed.
Replacing Bellows Sensing Element
Refer to figure 24 for key number locations unless
otherwise directed.
1. Shut off the supply pressure and process lines to
the controller or transmitter.
2. Disconnect the tubing from the mounting base
(key 57) and calibration adjuster (key 36).
Disconnect the tubing that connects the pressure
26
8. Install the new bellows assembly into the bellows
yoke.
9. Attach the link and bearing to the bellows
assembly. Position the bellows yoke (key 100) on
the mounting base (key 57), and attach the link and
bearing to the beam. Start but do not tighten the four
machine screws (key 98) with washers (key 99) that
attach the yoke to the mounting base. Slide the yoke
up or down as necessary to position the beam
horizontally, as shown in figure 24. Tighten the
machine screws.
Page 27
Instruction Manual
September 2009
BOURDON TUBE
(KEY 5)
LINK BEARING
(KEY 31)
WASHER (QTY 2)
(KEY 62)
BEAM
(KEY 39)
CONNECTING LINK
(KEY 16)
BINDING CONNECTING LINK
(IMPROPERLY ALIGNED)
GE37119
Figure 17. Connecting Link
10. Replace the subassembly in the case and
secure with the four machine screws (key 41,
figure 21 or 22). Reconnect all tubing.
11. If a bellows assembly with a different range is
installed, remove the machine screw and washer
(keys 61 and 60) and dial (key 6), and install a new
dial having an adjustment range corresponding to
the range of the bellows. If an optional process
pressure gauge (key 4, figure 21) is being used,
install a new gauge with the appropriate
measurement capability.
12. Check all tubing connections for leaks and the
bellows yoke machine screws, tighten as necessary.
Perform the appropriate calibration procedures.
C1 Controllers and Transmitters
BOURDON TUBE
(KEY 5)
WASHER
(KEY 62)
LINK BEARING
(KEY 31)
WASHER
(KEY 62)
BEAM
PROPERLY ALIGNED
CONNECTING LINK
3. Refer to figure 14. Install the replacement relief
valve with the arrow positioned so that the controller
output will be as noted in step 1 when the process is
shut down.
Changing Action
Proportional−Only to a Differential Gap
Controller
A proportional−only controller may be changed to a
differential gap controller, or vice versa, by changing
the position of the proportional tubing and inverting
the proportional band assembly.
(KEY 39)
CONNECTING
LINK (KEY 16)
Changing Reset Valve
1. Disconnect the appropriate tubing and remove
the reset restriction valve assembly (key 256,
figure 22) by removing the screw (key 22, not
shown) from the back of the case. Install the desired
replacement assembly.
2. Connect the tubing, check all connections for
leaks and perform the appropriate calibration
procedures.
1. Note the controller output pressure (zero or
supply) when the process is shut down.
2. Remove the differential relief valve assembly.
1. Isolate the controller or transmitter from process,
control, and supply pressure. Vent any trapped
pressure from the controller or transmitter before
proceeding with the following steps.
2. Disconnect the proportional tubing (key 25,
figure 16) from the mounting base (key 57, figure 23
or 24) and reinstall it in the other connection in the
mounting base.
3. Do not invert the reversing block unless also
changing the controller action from direct to reverse
(or vice versa).
4. Invert the proportional band assembly (refer to
figure 18):
a. Turn the proportional band adjustment knob
(key 73) to 10.
b. Unscrew the spring adjustor (key 65),
removing the bias spring (key 70) and washers
(key 64) with it.
27
Page 28
Instruction Manual
C1 Controllers and Transmitters
PROPORTIONAL BAND ADJUSTMENT KNOB
CANTILEVER SPRING
SPRING ADJUSTOR
GE34725−A
E1067
c. Unclip the lock spring (key 72). Remove the
indicator scale (key 69) and proportional band
adjustment knob (key 73).
d. Remove the gain adjustment bar (key 63). Flip
it over so it attaches to the opposite side of the
cantilever spring (key 8), as shown in figure 16,
and screw it back down.
e. Flip over the indicator scale (key 69); install it
and the proportional band adjustment knob
(key 73) as a unit. Snap in the lock spring
(key 72).
f. Tighten down the spring adjustor (key 65) with
the bias spring (key 70) and washers (key 64)
until it stops against the gain adjustment bar
(key 63).
g. Turn the proportional band adjustment knob to
the 10 setting. If it cannot be turned to the 10
setting loosen the spring adjustor (key 63).
5. Check all connections for leaks with a
soap−and−water solution. Perform the appropriate
calibration procedure.
(KEY 73)
LOCK SPRING
(KEY 72)
(KEY 8)
BIAS SPRING
(KEY 70)
WASHER
(KEY 64)
(KEY 65)
Figure 18. Proportional Band Assembly
September 2009
MACHINE SCREW
(KEY 56)
INDICATOR SCALE
(KEY 69)
MACHINE SCREW
(KEY 74)
GAIN ADJUSTMENT BAR
(KEY 63)
and 19 for key number locations unless otherwise
directed.
1. Isolate the controller or transmitter from process,
control, and supply pressure. Vent any trapped
pressure from the controller or transmitter before
proceeding with this procedure.
2. As shown in figure 15, locate the new tubing,
proportional band assembly, and reversing block
positions for the desired action.
3. Locate the two bellows (key 52), the proportional
band assembly (see figure 15), and the reversing
block (key 37).
4. Disconnect the tubing (refer to figure 15):
a. For a proportional−only controller or for a
transmitter, disconnect the proportional tubing
(key 25) from the mounting base and reconnect
them on the opposite side.
b. For a proportional−plus−reset controller,
disconnect the proportional tubing (key 27) and
reset tubing (key 27) from the mounting base and
reconnect them on the opposite side.
5. Invert the proportional band assembly (refer to
figure 18):
Reverse to Direct Action
Use the numbered steps below to change from
reverse action (increasing process pressure
produces decreasing output pressure) to direct
action (increasing process pressure produces
increasing output pressure), or vice versa. Changing
the action is accomplished by reversing the positions
of the reversing block, proportional band assembly,
and bellows tubing(s). Refer to figures 15, 16, 18,
28
a. Turn the proportional band adjustment knob
(key 73) to 10.
b. Unscrew the spring adjustor (key 65),
removing the bias spring (key 70) and washers
(key 64) with it.
c. Unclip the lock spring (key 72). Remove the
indicator scale (key 69) and proportional band
adjustment knob (key 73).
Page 29
Instruction Manual
September 2009
OUTER FLEXURE
(KEY 68)
MACHINE SCREW
(KEY 51)
MACHINE SCREW
(KEY 51)
BEAM
(KEY 39)
GE34726−B
E1068
Figure 19. Beam/Cantilever Spring Assembly
d. Remove the gain adjustment bar (key 63). Flip
it over so it attaches to the opposite side of the
cantilever spring (key 8) as shown in figure 15
and re−attach.
e. Flip over the indicator scale (key 69, figure
18); install it and the proportional ban knob (key
73) as a unit. Snap in the lock spring (key 72).
f. Tighten down the spring adjustor (key 65) with
the bias spring (key 70) and washers (key 64)
until it stops against the gain adjustment bar
(key 63).
g. Turn the proportional band adjustment knob to
the 10 setting. If it cannot be turned, loosen the
spring adjustor (key 65).
6. Change the reversing block assembly (figure 15
or 16, key 37):
a. Remove the sealing screw (key 49, figure 23
or 24). Inspect the O−ring (key 77 located in the
recessed area under the sealing screw head.
Replace the O−ring if necessary.
b. Remove the reversing block screw (key 50,
figure 23 or 24) and reversing block assembly
(key 37). Inspect the O−rings (key 77) located in
the recessed area under the reversing block
screw head and between the reversing block
assembly and the calibration adjuster (key 36).
Replace these O−rings if necessary.
C1 Controllers and Transmitters
BELLOWS SPACER
(KEY 34)
c. Position the reversing block assembly, with an
O−ring, on the calibration adjuster (key 36) so
that the nozzle is on the opposite side of the
beam (key 39) from which it was removed.
Position the reversing block hole in the calibration
adjuster. Install the reversing block screw (key
50) with an O−ring (key 77).
d. Install the sealing screw (key 49) with an
O−ring in the hole previously covered by the
reversing block assembly.
7. Check all connections for leaks with a
soap−and−water solution. Perform the appropriate
calibration procedures.
Relay Replacement
Key numbers used in this procedure are shown in
figure 21 or 22 except where indicated.
1. Shut off the supply pressure and process
pressure line(s) to the controller or transmitter.
2. Disconnect the tubing (key 24) from the relay.
3. Unscrew the output or supply pressure gauge
(key 2).
4. To remove the relay assembly, unscrew two
Phillips−head machine screws (key 29, not shown)
located behind the relay on the back of the case.
5. Remove the relay gasket (key 19, figure 21).
6. A new relay can be installed as a replacement. If
a new relay is being installed, continue with the next
step.
INNER FLEXURE
(KEY 67)
CANTILEVER SPRING
(KEY 8)
29
Page 30
Instruction Manual
C1 Controllers and Transmitters
7. Attach the replacement relay and new relay
gasket with machine screws inserted through the
back of the case. Reinstall the output or supply
gauge.
8. Connect the tubing, and check all connections for
leaks. Perform the appropriate calibration
procedures.
Changing Output Signal Range
Use the following information and subsequent
procedures when changing the output signal range
of the controller or transmitter. Use the following
procedure:
D For a controller or transmitter, use this
procedure to change from a 0.2 to 1.0 bar (3 to 15
psig) to a 0.4 to 2.0 bar (6 to 30 psig) output signal
range or vice versa.
D For a differential gap controller, use this
procedure to change from a 0 and 1.4 bar (0 and 20
psig) to a 0 and 2.4 bar (0 and 35 psig) output signal
range or vice versa.
D When changing the supply pressure source to
a new range, refer to table 5 for supply pressure
requirements for the output signal range selected.
Also, make appropriate changes to the nameplate of
the controller or transmitter, reflecting the new range
selections. Refer to figure 23 or 24 for key number
locations unless otherwise directed.
1. Shut off the supply pressure and process lines to
the controller or transmitter.
2. Disconnect the tubing from the mounting base
(key 57) and calibration adjuster (key 36).
Disconnect the tubing that connects the pressure
block (key 10, figure 21 or 22) to the Bourdon tube
or bellows assembly (key 5 or 52), at the pressure
block end.
September 2009
O−RING
(KEY 77)
A6281−1 / IL
Figure 20. Bellows Screw Detail
Note
The bellows screws (key 53) have an
O−ring (key 77, figure 20) installed
beneath the bellows screw head.
Remove the O−ring and obtain a
replacement when re−assembling the
bellows.
6. Unscrew the spring adjustor (key 65). Unclip the
lock spring (key 72, figure 18) and remove the
indicator scale (key 69) and the proportional band
adjustment knob (key 73).
7. Compress the bellows (key 52) so that the end of
the bellows, beam (key 39), and cantilever spring
(key 8) can be removed from the mounting base
(key 57).
8. Unscrew the bellows (key 52) from the
bellows/cantilever assembly.
9. Remove the cantilever spring from the spacer
(key 34).
a. Remove the beam machine screws (figure 19,
step 4).
b. Remove the cantilever machine screws
(figure 19, step 3).
3. Unscrew the machine screws (key 41, figure 21
or 22), and remove the subassembly from the case.
4. If the controller or transmitter uses a Bourdon
tube sensing element disconnect the Bourdon tube
from the beam (key 39) by removing the screw
(key 56). Be careful to avoid losing the bearing
(key 31). Unscrew the machine screws (key 55)
and remove the washers and Bourdon tube (keys 45
and 5).
5. Unscrew the bellows screws (key 53) from each
end of the mounting base (key 57).
30
c. Remove the inner flexure (figure 19, step 1)
and install it on the new cantilever.
10. Install the new cantilever spring (key 8) and
reconnect the beam (key 39) to the bellows spacer
(key 34) in reverse sequence of steps 9a. and 9b.
and reattach the bellows to the beam/cantilever
assembly.
11. Compress the bellows and install them into the
mounting base (key 57). Align the cantilever spring
with the gain adjustment bar (key 63). Install the
indicator scale (key 69) and the proportional band
Page 31
Instruction Manual
September 2009
adjustment knob (key 73) as a unit. Snap the lock
spring (key 72) onto the indicator scale.
12. Install the spring adjustor (key 65, figure 18)
with washers (key 64, figure 18) on either side of the
bias spring (key 70, figure 18). Tighten down the
spring adjustor until it stops against the gain
adjustment bar (key 63).
13. Turn the proportional band adjustment knob
to 10. If it cannot be turned to 10 loosen the spring
adjustor (key 65).
14. Secure the bellows (key 52) with the bellows
screws (key 53), making sure that the nozzle
(key 54) is centered on the flapper (key 40).
15. Unscrew the supply and output gauges
(figure 21 or 22, key 2) and install new gauges with
correct ranges.
16. Replace the subassembly in the case and
secure with machine screws (figure 21 or 22,
key 41). Re−install the Bourdon tube if it was
removed; refer to the Replacing the Bourdon Tube
section. Reconnect all tubing.
17. Check all tubing connections and the bellows
machine screws for leaks; tighten as necessary.
Perform the appropriate calibration procedures.
C1 Controllers and Transmitters
WARNING
Neither Emerson, Emerson Process
Management, nor any of their affiliated
entities assumes responsibility for the
selection, use, or maintenance of any
product. Responsibility for the
selection, use, and maintenance of any
product remains with the purchaser
and end−user.
Keys 71K, 71L, and 71M may also be
necessary for repair of C1B and C1D
controllers. Refer to the Common Parts
section for part numbers.
Parts Ordering
Whenever corresponding with your Emerson
Process Management sales office about this
equipment, mention the serial number of the unit.
The serial number can be found on the nameplate
(key 22, figure 21). When ordering replacement
parts, also state the complete 11−character part
number of each part required as found in the
following parts list.
WARNING
Use only genuine Fisher replacement
parts. Components that are not
supplied by Emerson Process
Management should not, under any
circumstances, be used in any Fisher
instrument. Use of components not
supplied by Emerson Process
Management may void your warranty,
might adversely affect the
performance of the instrument, and
could cause personal injury or
property damage.
Standard TemperatureRC100X00L12
High TemperatureRC100X00H12
Relay Replacement Kits
Kit includes keys 19 and 29, the replacement relay, and
2 Machine Screws
Standard TemperatureRRELAYX0L22
High TemperatureRRELAYX0H22
Case Assembly Seal Kit
Kit includes 3 Manifold Seals, 1 Manifold Cover,
and 10 Mounting ScrewsRC100X00012
Parts List
Common Parts (Figures 21, 22, 23,
and 24)
KeyDescriptionPart Number
Note
Part numbers are shown for recommended
spares only. For part numbers not shown,
contact your Emerson Process Management
sales office.
1Case and Cover Assembly, aluminum
31
Page 32
Instruction Manual
C1 Controllers and Transmitters
KeyDescriptionPart Number
Note
Key 2 is used as both a supply gauge and an
output gauge on units without a process
pressure gauge. A quantity of 2 is required
for these units. On units with a process
pressure gauge (key 106), key 2 is used for
the output gauge. A quantity of 1 is required
for these units.
Use key 3 for supply pressure indication
when a process pressure gauge is installed.
Key 3 installs on the supply pressure
regulator.
0−2.0 kg/cm2 and 0−30 psig11B8577X042
0−4.0 kg/cm2 and 0−60 psig11B8577X052
SST
0−2.0 kg/cm2 and 0−30 psig11B8583X032
0−4.0 kg/cm2 and 0−60 psig11B8583X052
Triple scale
Brass/Plastic
0−2.0 bar, 0−0.2 MPa, and 0−30 psig11B8577X012
0−4.0 bar, 0−0.4 MPa, and 0−60 psig11B8577X022
SST
0−2.0 kg/cm2 and 0−30 psig11B8583X012
0−4.0 kg/cm2 and 0−60 psig11B8583X022
2* Output Pressure Gauge, w/process pressure
gauge (1/8−inch connecting stem), Brass/Plastic
Triple scale
0−2.0 bar, 0−0.2 MPa, and 0−30 psig11B8577X012
0−4.0 bar, 0−0.4 MPa, and 0−60 psig11B8577X022
3* Supply Pressure Gauge, w/process pressure
gauge (1/4−inch connecting stem), Brass/Plastic
Triple scale
0−2.0 bar, 0−0.2 MPa, and 0−30 psig11B8579X022
0−4.0 bar, 0−0.4 MPa, and 0−60 psig11B8579X032
Note
Controllers with bellows sensing element
use only the 2.0 bar, 0 to 0.2 MPa, and 0 to 0
to 30 psig triple scale brass and stainless
steel process pressure gauges. Differential
pressure controllers do not use a process
pressure gauge.
4*Process Pressure Indicator Gauge (use only when specified)
Triple scale
Stainless steel
0−2.0 bar, 0−0.2 MPa, and 0−30 psig11B8584X022
0−20 bar, 0−2.0 MPa, and 0−300 psig11B8584X012
0−69 bar, 0−6.9 MPa, and 0−1000 psig11B8584X032
(30−0−30 inches wc) compound1L3780000A2
0−250 mbar (0−100 inches wc) positive1L3788000A2
0−0.35 mbar (0−5 psig) positive and for
0−350 mbar (0−10 inches Hg) vacuum1L3781000A2
0−0.5 bar (0−7.5 psig) positive1L3789000A2
0−0.7 bar (0−10 psig) positive1L3782000A2
0−1.0 bar (0−15 psig) positive, 0−1.0 bar
(0−30 inches Hg) vacuum, and 500−0−500 mbar
(15−0−7.5 psig) compound1L3783000A2
0−1.4 bar (0−20 psig) positive1L3784000A2
0−2.0 bar (0−30 psig) positive and 1.0−0−1.0 bar
(30−0−15 psig) compound1L3785000A2
Stainless steel,
0−1.0 bar (0−15 psig) positive, 0−1.0 bar
(0−30 inches Hg) vacuum, and 500−0−500 mbar
(15−0−7.5 psig) compound1L3786000A2
0−2.0 bar (0−30 psig) positive, 1.0−0−1.0 bar
(30−0−15 psig) compound1L3787000A2
*Recommended spare parts
1. This part is included in the Controller Repair Kit.
3. If ordering the bellows (key 71) to change the range of a gauge pressure
controller, also order the appropriate bellows spring (key 80). Also order
keys 101, 102, and 103 if you do not have them.
35
Page 36
Instruction Manual
C1 Controllers and Transmitters
SPRING−OUT CLEANING WIRE
RELAY ASSEMBLY
NOTES:
ARROW DOWN—RELIEVES ON DECREASING OUTPUT (OUTPUT @ SUPPLY DURING SHUTDOWN)
1
2
ARROW UP—RELIEVES ON INCREASING OUTPUT (OUTPUT @ ZERO DURING SHUTDOWN)
KEYS 80, 81, AND 82 ARE NOT SHOWN
GE31718−A
E1072
PROPORTIONAL-PLUS-RESET CONTROLLER WITH DIFFERENTIAL
Std Temp, chloroprene (2 req’d)1D397003012
High Temp, silicone (2 req’d)1N873604142
76* Nozzle O−Ring
Std Temp, nitrile1E222606992
High Temp, fluorocarbon1N838706382
(4)
, steel pl
(4)
bellows sensing instruments only1L379641012
(1)
, 18−8 SST (2 req’d)
(1)
(1)
,
KeyDescriptionPart Number
Note
A total of 5 O−rings (key 77) are used. 1
O−ring is used under the sealing screw (key
49), 1 O−ring is used under the reversing
block screw (key 50), 1 O−ring is used
between the reversing block ass’y (key 52)
and the calibration adjuster (key 36), and 1
O−ring is used in the recessed area under the
head of each of the bellows screws (key 53).
77* O−Ring,
Std Temp, nitrile (5 req’d)1D687506992
High Temp, fluorocarbon (5 req’d)1N430406382
Note
Keys 78 through 82 are used for
Proportional−Plus−Reset controllers only.
1. This part is included in the Controller Repair Kit.
3. If ordering the bellows (key 71) to change the range of a gauge pressure
controller, also order the appropriate bellows spring (key 104). Also order
keys 101, 102, and 103 if you do not have them.
4. This part is part of the bellows assembly, key 71.
Page 37
Instruction Manual
September 2009
A
A
C1 Controllers and Transmitters
C
C
B
B
A
A
NOTE:
KEYS 33 AND 74 ARE NOT SHOWN
GE26600−A
E1073
Figure 23. Controller Subassembly with Bourdon Tube Sensing Element
5/16 UNC X 1 inch
5/16 UNC X 1−1/2 inches
5/16 UNC X 2 inches
216Hex Nut, steel pl (specify quantity req’d)
For filter regulator mounting on
1051, 1052 and 1061
All other types and mountings
220Mounting Bracket, steel pl (not shown)
For casing mounting and casing−mounted filter
regulator on 1051 and 1052
221Lockwasher, steel pl (specify quantity req’d)
39
Page 40
Instruction Manual
C1 Controllers and Transmitters
KeyDescription
222Cap Screw, steel pl (specify quantity req’d)
5/16 UNC X 3/4 inch
5/16 UNC X 1 inch
5/16 UNC X 1−1/8 inches
5/16 UNC X 1−1/4 inches
5/16 UNC X 1−3/4 inches
5/16 UNC X 2−1/2 inches
3/8 UNF X 1−1/8 inches
1051 and 1052 size 40 (2 req’d)
1061 sizes 30, 80 and 100 (2 req’d)
243Street Elbow, pl galvanized malleable iron (not shown)
For mounting on 470, 472, 480, 513, 656,
657, 667, panel, pipe stand, 1051, 1052 and 1061
w/nipple−mounted filter regulator
244Pipe Nipple, pl galvanized steel (not shown)
For mounting on 470, 472, 480, 513, 656,
657, panel, pipe stand, 1051, 1052 and 1061
w/nipple−mounted filter regulator
250Clamp, Steel
For pipe stand mounting (2 req’d)
251Bracket Assembly, steel
For panel or wall mounting (2 req’d)
252Cap Screw, steel pl
For panel or wall mounting (4 req’d)
Note
Specify quantity of fittings.
Connector, Brass
1/4 NPT X 1/4 O.D. tubing
1/4 NPT X 3/8 O.D. tubing
Elbow, Brass
1/4 NPT X 1/4 O.D. tubing
1/4 NPT X 3/8 O.D. tubing
Fisher is a mark owned by one of the companies in the Emerson Process Management business division of Emerson Electric Co. Emerson
Process Management, Emerson, and the Emerson logo are trademarks and service marks of Emerson Electric Co. All other marks are the property
of their respective owners. This product may be covered under pending patent applications.
The contents of this publication are presented for informational purposes only, and while every effort has been made to ensure their accuracy, they
are not to be construed as warranties or guarantees, express or implied, regarding the products or services described herein or their use or
applicability. All sales are governed by our terms and conditions, which are available upon request. We reserve the right to modify or improve the
designs or specifications of such products at any time without notice. Neither Emerson, Emerson Process Management, nor any of their affiliated
entities assumes responsibility for the selection, use or maintenance of any product. Responsibility for proper selection, use, and maintenance of
any product remains solely with the purchaser and end−user.
Emerson Process Management
Marshalltown, Iowa 50158 USA
Sorocaba, 18087 Brazil
Chatham, Kent ME4 4QZ UK
Dubai, United Arab Emirates
Singapore 128461 Singapore
www.Fisher.com
40
EFisher Controls International LLC 2008, 2009; All Rights Reserved
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