Device dictionary

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Reference ID	String
0	Model
1	Model- References the type of field Device, usually an advertised mode number, that is unique to a single manufacturer.
2	SVI
3	Manufacturer
4	Manufacturer Identification Code- References a specific manufacturer, which is usually a company name, that is responsible for the manufacture of this Field Device.
5	Masoneilan
6	Num resp preams
7	Number of Request Preambles- Number of Preambles required from the Host request by the Field Device.
8	Universal cmd rev
9	Universal Revision- Revision of the Universal Device Description, that the Field Device conforms to.
10	Transmit cmd rev
11	Field Device Revision- Revision of the Field Device Specific Device Description, that the Field Device conforms to.
12	Software rev
13	Field Device Software Revision- This revision corresponds to the software or firmware, that is embedded in the Field Device.
14	Hardware rev
15	Hardware Revision- Revision that corresponds to the electronics hardware of the Field Device.
16	Physicl signl code
17	Physical Signaling Code- The Physical Signaling Code describes the type of Physical Layer that has been implemented in the hardware that is responsible for the HART Communication port.
18	Device flags
19	Field Device Flags- Describes special features of the Field Device that affect the Data Link Layer.
20	Device id
21	Field Device Identification- Uniquely identifies the Field Device when combined with the Manufacturer Identification and Device Type. Therefore, this variable cannot be modified by the Host user.
22	Poll addr
23	Polling Address- Address used by the Host to identify a Field Device, and changeable by the User to control the Multidrop Mode.
24	Tag
25	Tag- Text that is associated with the Field Device installation. This text can be used by the user in any way. A recommended use is as a unique label to a plant that correlates to a Field Device label: a plant drawing, or on a Control System. This variable is also used as a type of data link layer address handle.
26	Message
27	Message- Text that is associated with the Field Device. This text can be used by the user in any way. There is no recommended use.
28	Descriptor
29	Descriptor- Text that is associated with the Field Device.This text can be used by the user in any way. There is no specific recommended use.
30	Date
31	Date- Gregorian calendar date that is stored in the Field Device. This date can be used by the user in any way. There is no specific recommended use. Enter MM/DD/YY
32	Final asmbly num
33	Final Assembly Number- Number that is used for identification purposes, and is associated with the overall Field Device.
34	.3f
35	s
36	8.3f
37	indicate the actual valve position in % with closed 0 % and open 100 %
38	valve pos
39	.1f
40	unit for valve position
41	position unit
42	indicate the actual actuator pressure
43	act pres
44	The act. pressure reported by the SVI can be in psi, bar or kPa
45	pressure unit
46	process variable
47	process var.
48	Unit for the process variable (PV) if the controller mode is selected.
49	PV unit
50	°C
51	°F
52	psi
53	bar
54	mbar
55	kPa
56	CF/min
57	Cubic Feet per minute
58	gal/min
59	l/min
60	m3/h
61	gal/s
62	l/s
63	CF/s
64	Cubic Feet per second
65	m3/s
66	SCF/min
67	standard Cubic Feet per minute
68	CF/h
69	Cubic Feet per hour
70	m3/min
71	gal/h
72	l/h
73	gal
74	l
75	m3
76	bbl
77	CF
78	Cubic Feet
79	ft
80	m
81	in
82	cm
83	mm
84	min
85	h
86	day
87	gr/s
88	gr/min
89	gr/h
90	kg/s
91	kg/min
92	kg/h
93	kg/day
94	lb/s
95	lb/min
96	lb/h
97	lb/day
98	mV
99	V
100	mA
101	Ohm
102	Hz
103	%
104	controller setpoint
105	remote SP
106	Unit for the controller setpoint (SP) if the controller mode is selected.
107	SP unit
108	Input signal and current loop in mA
109	inp sig
110	6.2f
111	input signal and current loop in percent
112	.2f
113	7d
114	valve pos
115	inpt
116	input signal and current loop in mA
117	analog
118	Hot key menu
119	Offline Config.
120	NORMAL MODE
121	MANUAL MODE
122	CONFIG MODE
123	CALIBRATE MODE
124	DIAGNOSTIC MODE
125	FAILSAFE MODE
126	EXAMINE
127	read identifier
128	positioner config.
129	positioner calibr.
130	diagnostic data
131	read status
132	Clear all the status coming from communication or device errors
133	clear Status
134	positioner PID
135	error limits
136	switches position
137	controller config.
138	controller calibr.
139	controller PID
140	controller param.
141	Limits how fast the output can change. It is expressed as the percent of full output range per second. Value must be between 1%/s and 100.0%/s .
142	Controller output
143	controller SP mode
144	check SVI
145	Manual valve setpoint in %.
146	change pos <->
147	TO MANUAL MODE
148	MANUAL MODE MENU
149	MANUAL MODE -->
150	NORMAL MODE -->
151	CONFIG MENU
152
153	Change tag, descriptor, message etc...reported by the SVI.
154	tag
155	Change options in config menu reported by the SVI like valve characterization , button lock , bumpless transfer and other options
156	options
157	Change setup in config menu reported by the SVI like actuator ATO or ATC, direct or reverse instrument, failsafe mode ...
158	setup
159	Access to controller functions.Change setpoint startup, units for process variable (PV) and setpoint (SP) , direct or reverse action, etc...
160	controller
161	CALIBRATE MENU
162	Selects the range sub dialog where the user can enter the upper and lower scale values for the input signal.The values typically are 4 and 20 mA but may be any values between 3.8 and 22 mA(Range signal).This dialog also allows automatic calibration of the position sensor (Stops limit)
163	range
164	The user can set tuning PID coefficients, run auto tune function and set output to I/P
165	tuning
166	To calibrate the signals, you will need a method of setting and changing the input signal.To calibrate the pressure, you will need a method of setting and changing the pressure in the actuator.
167	signals calibrate
168	DIAGNOSTIC MENU
169	Perform valve signature and valve fonctional analysis.
170	perform standard
171	Displays CONTINUOUS DIAGNOSTIC DATA including number of full strokes the valve has made,the number of cycles (direction changes),the time the valve has spent open, the time the valve has been closed and the time the valve has spent throttling near the seat. Displays the DIAGNOSTIC TEST RESULT DATA: after the standard diagnostics are completed the data: friction,spring range, supply pressure and response time open and closed are displays.
172	read diagnostic
173	Reset continuous diagnostic data (stroke count,cycle count, time open, time closed and time near closed ) to 0.The previous data are lost and must be recorded to be used later.
174	reset continuous
175	CONTROLLER
176	Display controller parameters like : setpoint (SP) , process variable (PV) , controller output(OUT-C) and valve position(POS).
177	controller view
178	To change the controller setpoint :remote(R-SP) , local (L-SP)or manual mode (M-SP).
179	mode and setpoint
180	To set tuning PID coefficients for controller mode
181	PID setting
182	Additional parameters for controller mode configuration.
183	Display the alarm message for the controller mode. If ABSOLUTE alarms are selected and the process variable is not between the low and high alarm limit, an alarm message will be displayed. If DEVIATION alarms are set and the difference between the setpoint and the process variable is not between the low and high alarm limit, an alarm message will be displayed.
184	alarms view
185	This function perform a master reset to the device, causing it to go through its startup routine and re-initializing all of its operating parameters from non volatile memory.
186	SVI RESET
187	special return to normal
188	stop procedure
189	return to manual
190	device busy
191	wrong mode
192	command not implemented
193	Manual valve setpoint in %. Value mut be between -5.0% and +105.0% .
194	man pos
195	Manual valve setpoint in mA.
196	set valve pos in mA
197	svi mode can be normal,manual,calibrate, configuration,diagnostic or failsafe.
198	mode
199	1d
200	SVI configuration information and actuator acting.
201	air to close
202	OFF=ATO ON=ATC
203	double acting
204	OFF=single acting (ON=double reserved for future use)
205	reverse instr
206	OFF=direct acting instrument ON=reverse acting instrument option hw reverse must be configured
207	fail high
208	OFF=fail low ON=fail high
209	OFF=controller off ON=controller on
210	bumpless
211	ON=bumpless transfer activation selected returning from manual to normal operating mode is deferred until the input signal matches the current valve position.
212	hw reverse
213	ON=hardware reverse OFF=software reverse
214	Status for low/upper limits and tight shutoff.
215	limits
216	LOWER LIMIT
217	Status for low/upper limits: OFF=not set / ON=set
218	UPPER LIMIT
219	TIGHT_SHUTOFF
220	Status for tight shutoff: OFF=not set / ON=set
221	cam used in the SVI:relationship between flow capacity (Cv) and percentage opening of the valve.Several cams are available:linear, =%50 , =%30 , quick opening coeff 50 , custom.
222	cam
223	cam used in the SVI:relationship between flow capacity (Cv) and percentage opening of the valve.Several cams are available:linear/=%50/=%30/quick opening coeff 50/custom.
224	define lock level for SVI buttons to avoid unintended modifications.
225	buttons
226	Level 3
227	Define lock level :no restriction
228	Level 2
229	Define lock level :lock out local calibrate and config menu
230	Level 1
231	Define lock level :lock out local manual menu
232	Level 0
233	Define lock level :lock out all buttons
234	This option determines whether the controller setpoint will be in local ,local only , remote or last mode on start up.
235	SP
236	PV_LOCAL_ONLY
237	0=local or remote 1=local only
238	PV_STARTUP_REMOTE
239	0=startup remote 1=startup local
240	PV_STARTUP_LAST
241	0=use flag above 1=start up last mode
242	SP_LOCAL_ONLY
243	SP_STARTUP_REMOTE
244	0=startup remote, 1=startup local
245	SP_STARTUP_LAST
246	0= local or remote, 1=start up last mode
247	LC_DIRECT
248	0=direct, 1=reverse
249	LC_RATIO_CONTROL
250	This option determines whether the controller setpoint will be in local ,local only , remote or last mode on start up.
251	SP startup mode
252	PC mode
253	In ratio control, the setpoint and process variable may be in different engineering units or on different scales. The relationship between the setpoint in process variable units and the raw setpoint is given by: SP(in PV)=ratio gain * SP + ratio bias.
254	Ratio control
255	ratio
256	The controller may be direct action ( its output increases when the process variable is greater than the setpoint) or reverse action (its output decreases then the process variable is greater than the setpoint).
257	controller action
258	action
259	Threshold for tight shutoff: when selected, if the input signal would position the valve below the tight shutoff value, full supply or atmosphere pressure is supplied to the actuator to close the valve with full seating force. Value between -1% and 20%.
260	Tight Shutoff
261	5.2f
262	The SVI allows the user to establish software limit stops.The control functions will NOT allow the valve position to be lower than the lower position limit.However this option DOES NOT PROVIDE MECHANICAL STOPS for the valve.During a electrical or air failure the valve will go to the fail safe position without regard to the software limit stops.The manual position full closed or full open will similary ignore limit stops.
263	Lower Limit
264	The SVI allows the user to establish software limit stops. The control functions will NOT allow the valve position to be above than the upper position limit.However this option DOES NOT PROVIDE MECHANICAL STOPS for the valve.During a electrical or air failure the valve will go to the fail safe position without regard to the software limit stops.The manual position full closed or full open will similary ignore limit stops.
265	Upper Limit
266	Choice of different languages is displayed on the SVI LCD.
267	language
268	English
269	Possibility of different languages display on the SVI LCD
270	French
271	The controller can process the setpoint and the process variable data every 0.15 s to 10.0 s. For fast processes, a rate of 0.2 s would be a reasonable value and for slow processes 2 s would be common.
272	controller rate
273	3.1f
274	When power is applied to the SVI, this parameter determines the setpoint value if the startup mode is local.
275	initial local SP
276	Value corresponding to the maximun error (in % opening ) between the setpoint and the valve position allowed, before setting a status flag or putting the valve in fail safe mode regards the selection of associated variables Time 1 and Time 2. Value must be between 0.5% and 100.0% .
277	pos error band
278	4.2f
279	Value of valve position below which the user considers the valve as being near closed position.Used in continuous diagnostic calculations. Must be between 0 and 20%.
280	valve near closed
281	time before set the flag : valve error position this time must be >= 1 s and below 327 s.
282	time 1
283	.0f
284	4.0f
285	time before to put the valve in failsafe mode this time must be >= 2 s and below 327 s and in any case greater than Time 1 However to inhibit failsave mode set -1 s.
286	time 2
287	time before setting the flag : pressure error if the pressure is not correct.
288	press fault limit
289	Low input signal for valve closed (direct acting) or low input signal for valve open (reverse acting). Must be between 3.5 mA and 14 mA.
290	low signal
291	high input signal for valve open (direct acting) or high input signal for valve open (reverse acting). Must be between 8 mA et 22 mA.
292	high signal
293	low pressure value for scaling the pressure sensor.
294	low press value
295	high pressure value for scaling the pressure sensor. Must be between 18 and 150 psi or 1.24 and 10.4 bar or 124 and 1040 kpa.
296	high press value
297	5.1f
298	4.1f
299	9.1f
300	units for input signal.
301	Input sig Unit
302	Engineering value for the process variable that corresponds to 4.0 mA and 20.0 mA. The SVI use these values to convert the auxiliary input to engineering units.
303	low PV value
304	8.2f
305	upper PV value
306	Engineering value for the process variable that corresponds to 4.0 mA. The SVI use these values to convert the auxiliary input to engineering units.
307	low SP value
308	Engineering value for the process variable that corresponds to 20.0 mA. The SVI use these values to convert the auxiliary input to engineering units.
309	upper SP value
310	Proportional gain P is the ratio of proportional action (part of controller output) to error.Value between 10 and 1000.
311	P
312	4d
313	Integal time or reset time, is the time constant of integral control.Value between 0 and 1000.
314	I
315	Derivative time or rate time is the time constant Typical range is 8 to 16 of derivative control.Value between 0 and 5000.
316	D
317	ms
318	Derivative gain is a parameter of derivative control. Value between 0 and 100.
319	Kd
320	Beta is nonlinear gain factor, ranging from -8 to 9. When beta is 0, the controller gain is linear. Otherwise the gain is a function of error. The larger the beta, the smaller the gain for small error. Typical beta value for a valve position controller is 7 or 8.
321	Beta
322	The setpoint is constrained to be between the low and high limits. Both local and remote setpoints are limited. The limits are entered in the same engineering units as the process variable. SP low limit must be lower than SP upper limit.
323	SP low limit
324	The setpoint is constrained to be between the low and high limits. Both local and remote setpoints are limited. The limits are entered in the same engineering units as the process variable. SP upper limit must be upper than SP low limit.
325	SP upper limit
326	Define the high alarm for the controller mode. Alarm are absolute or deviation. The alarm limits are entered in the same units as the process variable .
327	Low alarm limit
328	Define the high alarm for the controller mode. Alarm are absolute or deviation. The alarm limits are entered in the same units as the process variable .
329	Upper alarm limit
330	%/s
331	Only applies to P or PD control. It is the process controller output at a typical operating steady state. If the controller outputs range from 30 to 50 % at normal operation, the manual reset bias should be set at 40% in order to minimize steady state error. Value between 0 and 90% .
332	Manu. reset bias
333	2d
334
335	Select
336	SP tracking
337	When the controller is changed from manual mode to local mode, the setpoint is set to equal the current process variable. In that case the process will not be upset by the change from manual to local.
338	Freeze output
339	If the process variable read is not a valid reading, the controller output will not be changed.
340	Derivative mode
341	Determines whether a change in process variable or a change in error (setpoint - process variable) will cause derivative action. OFF=PV ON=error.
342	Alarm type
343	OFF=absolute ON=deviation
344	When the difference between the setpoint and the process variable is less than the dead zone, the controller will take no action to change the output.Must be between 0 and 20%.
345	Dead zone
346	In ratio control, the setpoint and process variable may be in different engineering units or on different scales. The relationship between the setpoint in process variable units and the raw setpoint is given by: SP(in PV unit)=ratio gain * SP + ratio bias.
347	Ratio gain
348	Ratio bias
349	Read the controller mode: manual , local or remote.
350	LCMode
351	Read the current loop controller (LC) mode: manual , local or remote.
352	LC current mode
353	local PV
354	local SP
355	Value for open stop adjustment.This value must be between 80%-100%.For some valves the open position stop exceeds the nominal travel of the valve.By entering a value, the position calibration can be adjusted to nominal travel .
356	open stop adj
357
358	Proportional gain in %.Common values are 50 for small valves up to 4000 for large valves.Must be between 0 and 5000.
359	Integral time or reset time in 1/10 s. Higher values of I cause less integral action, however a value of 0 gives no integral action .Common values are 10 to 200. Values between 0 and 1000.
360	(1/10s)
361	Derivative time or rate time in milli_seconds.Common values are 10 to 100. Values between 0 and 200.
362	Coefficient added to P when the valve is exhausting and compensates the variation in filling and exhausting speed. Can be positive or negative value range between -3000 to +3000.
363	Padj
364	Nonlinear gain factor.When beta is 0,the proportional gain is linear,otherwise the gain P is a function of error. The larger the beta,the smaller the gain for small error. Typical beta value is 7 or 8.Beta is ranging from -8 to +9.
365	Coefficient to increase the valve response for some applications.A value of 0 gives no Damping and 9 gives maximum damping of valve motion.
366	Damping
367	The response of the valve is different when the valve is nearly closed than when nearly open.This coefficient allows the user to make adjustments to try to equalize the valve response.Normal value is 6 and this value is ranging from 0 to 9.
368	Pos.Comp.
369	When the valve position is within the setpoint +/- the dead zone and, no additional position control is performed. This value is normally 0%.Used to avoid limit cycling for high friction valves.Range 0 to 1%.
370	Dead zone
371	Set constant current on the I/P.(2750 optimal value) to adjust the pneumatic block.
372	Output
373	Total number of valve strokes.
374	total travel
375	strokes
376	Time in hours for valve closed.
377	time closed
378	Time in hours for valve open.
379	time open
380	Time in hours for valve near closed.
381	time near closed
382	Number of cycles (direction changes).
383	nbr cycles
384	Friction.This value is given from the standard diagnostic calculations.
385	friction
386	Low spring value.This value is given from the standard diagnostic calculations.
387	low spring range
388	High spring value.This value is given from the standard diagnostic calculations.
389	upper spring range
390	low pressure value in the valve actuator.This value is given from the standard diagnostic calculations.
391	lower pressure
392	Upper pressure value in the valve actuator.This value is given from the standard diagnostic calculations.
393	upper pressure
394	Fastest time to open the valve on the full stroke .This value is given from the standard diagnostic calculations.
395	strok. time open
396	Fastest time to close the valve on the full stroke. This value is given from the standard diagnostic calculations.
397	strok. time close
398	Status from limit switches.
399	limit switches
400	SWITCH 1
401	OFF=open ON=closed
402	SWITCH 2
403	A speed between 1 and 10 must be entered.This determines the speed at which the valve will travel during the pressure vs. position test.A speed of 1 or 2 is appropriate for 1 to 3 inch valves,3 to 4 for 6 to 8 inch valves and higher speeds for larger valves.
404	Speed
405	bFaultCode1
406	Reports Device Errors
407	Position Error
408	Pressure Error 1
409	Pressure Error 2
410	I/P Out Voltage Error
411	Position Sensor Error
412	Pressure Sensor Error
413	Current Sensor Error
414	Reference Voltage Error
415	bFaultCode2
416	Reports Device Errors
417	Position Limit Change
418	Self Check Failure
419	Hart Error
420	Software Error
421	Reset Occurred
422	Switch to I/P
423	Data Overrun
424	Find Stop limits Failed
425	bFaultCode3
426	Circuit Temperature Error
427	EEPROM Write Failed
428	Position Sensor Error Latch
429	Pressure Sensor Error Latch
430	Reference Voltage Error Latch
431	Circuit Temperature Error Latch
432	Watchdog Timeout
433	Signal Calibration Failed
434	bFaultCode4
435	Reserved for future use
436	reserved
437
438	mA value of the auxillary signal
439	fSig2
440	A/D value of the auxillary signal
441	nSig2
442	pts
443	A/D value of the primary signal
444	nSig
445	A/D value of the position sensor.
446	nPos
447	A/D value of the pressure sensor
448	nPres
449	output value of the process controller
450	nOutput
451	current value send on the pneumatic block.
452	I/P
453	Internal SVI temperature in °C.
454	temperature
455	X define signal input in % and Y define position valve in % The mini and maxi values are respectively 0.0% and 100.0% The custom curve must have at least one pair. A coordinate (100.0%,100.0%) indicate the end of the curve.
456	X1
457	Y1
458	X2
459	Y2
460	X3
461	Y3
462	X4
463	Y4
464	X5
465	Y5
466	X6
467	Y6
468	X7
469	Y7
470	X8
471	Y8
472	X9
473	Y9
474	X10
475	Y10
476	REMOTE MODE ALARM
477	REMOTE MODE
478	LOCAL MODE ALARM
479	LOCAL MODE
480	MANUAL MODE ALARM
481	MANUAL MODE
482	Low value for primary signal calibration. Must be between 3.5mA and 8.0mA .
483	primary signal
484	high value for primary signal calibration. Must be between 12.0mA and 20.0mA .
485	Low value for pressure sensor calibration. Must be between 0 and 9psi / 0 and 0.6bar / 0 and 60kPa .
486	pressure
487	High value for pressure sensor calibration. Must be between 10 and 120psi / 0.7 and 8.0bar / 70 and 800kPa .
488	Low value for secondary signal calibration. Must be between 3.5mA and 8.0mA .
489	secondary signal
490	high value for secondary signal calibration. Must be between 12.0mA and 20.0mA .
491	FMU860
492	DT
493	DVC
494	FCX
495	AS800
496	340T
497	340C
498	344
499	Siemens Micro K
500	SITRANS L
501	SIPAN PH
502	SITRANS P
503	75SMT
504	UNIDELTA
505	8320
506	SX5100
507	TSV175
508	DMU
509	3780
510	BM70
511	8u
512	Procedure aborted TRY AGAIN.
513	Position Error
514	Pressure Error (type 1)
515	Pressure Error (type 2)
516	I/P Out Voltage Error
517	Position Sensor Error
518	Pressure Sensor Error
519	Current Sensor Error
520	Référence Voltage Error
521	Position calibration end points have changed
522	Self Check Failure
523	Hart Error
524	SVI Software Error
525	Reset Occurred
526	Switched to I/P mode
527	Data Overrun
528	Find Stop limits Failed
529	Circuit Temperature Error
530	EEPROM Write Failed
531	Position Sensor Error Latch
532	Pressure Sensor Error Latch
533	Référence Voltage Error Latch
534	Circuit Temperature Error Latch
535	Watchdog Timeout
536	Signal Calibration Failed
537	no fault code
538	PLEASE WAIT...
539	Clear Fault Codes NOT Completed
540	Clear Fault Codes Completed
541	Controller output = %{0}%/s
542	Manual setpoint:
543	setpoint;full open;full closed
544	Valve Position :
545	Going to MANUAL MODE prevents the valve from responding to the controller! Are you sure you want to go to MANUAL ?
546	WAIT ...
547	RETURN TO NORMAL MODE ?
548	NO;YES
549	WAIT WORK IN PROGRESS
550	Bumpless is set. Change the current loop to match the corresponding valve position ONLY IF NECESSARY.
551	Pos =%{0} % current =%{2} mA loop or %{1} %
552	Press ABORT key to abort the process
553	tag
554	descriptor
555	message
556	final assembly number
557	date
558	polling address
559	Record values ? Press: OK for YES ABORT for NO
560	custom cam used
561	no change;linear;equal(50);equal(30);quick open;custom
562	quick open cam used
563	no change;linear;equal%(50);equal%(30);quick_open;custom
564	equal%(30) cam used
565	equal%(50) cam used
566	no change;linear;equal%(50);equal%(30);quick_open;custom;
567	linear cam used
568	NEW CAM CHARACTERIZATION ?
569	Input your 9 XY pairs of points between ( 0.0%, 0.0%) and (100.0%,100.0%)
570	X[%{i}]
571	Y[%{i}]
572	Invalid segment X%{a} , X%{i} Slope too low .
573	Invalid segment X%{a} , X %{i} Slope change too high
574	Invalid segment X%{a} , X %{i} Slope change too much
575	CHANGE BAD SEGMENT(S) ?
576	YES; NO
577	Limits
578	Lower limit value
579	Upper limit value
580	Tight shut off value
581	Pressure units
582	Display language
583	Buttons:lock level
584	Valve near closed
585	I/P selection is not possible.
586	Double acting selection is not possible.
587	Please see documentation for reverse mode before selecting this mode.
588	Issue a Reset when return to Manual mode to ACTIVATE controller mode.
589	Position error band
590	Time1
591	Time2
592	Time 2 must be greater than Time 1.
593	Pressure Time
594	Controller mode not set.
595	setpoint:local only
596	no change;startup local;startup remote;startup last mode;local only
597	setpoint:startup last mode
598	setpoint:startup local
599	setpoint:startup remote
600	action:reverse
601	no change;direct;reverse
602	action:direct
603	PV unit
604	remote SP unit
605	Ratio control is ON.
606	Ratio control: YES
607	no change;NO;YES
608	Ratio control: NO
609	initial local SP %{0}
610	spinit
611	controller rate
612	make your choice:
613	range signals;find stop limits
614	low signal
615	high signal
616	Low and high signals must differ by at least 5mA.
617	supply pressure
618	high PV value
619	low SP value
620	high SP value
621	This command will stroke the valve and should NOT be performed with the process running.
622	Change open stop adjustment ?
623	open stop adjustment
624	WAIT WORK IN PROGRESS
625	Find stop limits executed
626	PID coefficients;auto tune;bias
627	P =%{0}% I =%{1}(1/10s) D =%{2}ms Padj =%{3}%
628	Beta =%{4} Damping =%{5} Compens. pos.=%{6} Dead zone =%{7}%
629	P (%)
630	I (1/10s)
631	D (ms)
632	Padj (%)
633	Beta
634	Damping
635	Compensation
636	Dead zone (%)
637	This procedure strokes the valve and should not be run with the valve in service and the process running.
638	WAIT AUTO TUNE IN PROGRESS
639	Press ABORT key to abort the process
640	AUTO TUNE CORRECTLY EXECUTED
641	The found Bias is not in the required range self-tuning is canceled. Ajust the BIAS.
642	Self-tuning for air fill direction fails. Check supply pressure or pneumatic block.
643	Self-tuning for air exhausting direction fails.Check the pneumatic block.
644	set the I/P value:
645	primary signal;secondary signal;pressure;view signals;reset to factory
646	Enter the low signal value:
647	Set the input current to: %[.2f]{0}mA and press OK
648	Enter the high signal value:
649	Set the input current to: %[.2f]{0}mA and press OK
650	primary signal: %{0} mA
651	Enter the low secondary signal value:
652	Set the secondary input current to: %[.2f]{0}mA and press OK
653	Enter the high secondary signal value:
654	secondary signal: %{0} mA
655	Enter the low pressure signal value:
656	Set the pressure to: %[.2f]{0}%{1} and press OK
657	Enter the high pressure signal value:
658	pressure: %{0} %{1}
659	primary signal: %[.2f]{0} mA secondary signal: %[.2f]{1} mA pressure: %[.2f]{2} %{3}
660	This procedure strokes the valve and should not be run with the valve in service and the process running.
661	Remove software limit stops to be able to perform standard diagnostic
662	Valve Speed
663	WAIT STANDARD DIAGNOSTIC IN PROGRESS
664	STANDARD DIAGNOSTIC EXECUTED
665	Continuous data;Result std diagn
666	Total travel= %{0}strokes Time closed= %{1}h Time open= %{2}h
667	Time near closed= %{3}h Nbre Cycles= %{4}
668	Following values are not meaningful if standard diagnostic has not been run.
669	friction = %{0}%{7} low spring range= %{1}%{7} upper spring range= %{2}%{7}
670	lower pressure= %{3}%{7} upper pressure= %{4}%{7}
671	stroking time to open: %[.1f]{t1}s stroking time to close: %[.1f]{t2}s
672	After resetting , the current values will be lost. Press ABORT if you need these values.
673	RESET CONTINUOUS DATA CORRECTLY EXECUTED
674	%{6} PV =%{1} %{4} R-SP =%{2} %{5} =%[.1f]{t1} %{4} OUT-C=%{3} % POS =%{0} %
675	%{6} PV =%{1} %{4} R-SP =%{2} %{5} OUT-C=%{3} % POS =%{0} %
676	%{6} PV =%{1} %{4} L-SP =%[.1f]{t1} %{4} OUT-C=%{3} % POS =%{0} % R-SP =%[.1f]{t2} %{4}
677	%{6} PV =%{1} %{2} M-SP =%{3} % POS =%{0} % R-SP =%[.1f]{t2} %{2}
678	make your choice:
679	SP value;SP mode
680	setpoint:Remote SP
681	no change;Remote SP;SP Local;Manual
682	setpoint:Local SP
683	no change;Remote SP;Local SP;Manual
684	no change;Local SP;Manual
685	setpoint:Manual
686	setpoint:Manual
687	Local SP
688	P =%{0}% I =%{1}(s) D =%{2}ms Kd =%{3} Beta =%{4}
689	Ratio Gain
690	Ratio Bias
691	The Ratio Gain and Bias compute setpoint out of range of process variable.
692	Ratio scaling exceeds capabilities of the SVI.
693	SP Low Limit
694	SP High Limit
695	Set point Low Limit must be less than Hight Limit.
696	Low Alarm Limit
697	High Alarm Limit
698	Output Rate Limit in %/s:
699	a
700	Maximum value allowed is: %[4.1f]{fK}%/s using controller rate : %{0}s
701	Manual Reset Bias
702	Select
703	ALARM TYPE: DEVIATION PV =%{0} %{1} SP =%[.1f]{t2} %{1} HIGH ALARM
704	ALARM TYPE: DEVIATION PV =%{0} %{1} SP =%[.1f]{t2} %{1} LOW ALARM
705	ALARM TYPE: DEVIATION PV =%{0} %{1} SP =%[.1f]{t2} %{1} NO ALARM
706	ALARM TYPE: ABSOLUTE PV =%{0} %{1} SP =%[.1f]{t1} %{1} HIGH ALARM
707	ALARM TYPE: ABSOLUTE PV =%{0} %{1} SP =%[.1f]{t1} %{1} LOW ALARM
708	ALARM TYPE: ABSOLUTE PV =%{0} %{1} SP =%[.1f]{t1} %{1} NO ALARM
709	A reset may cause the valve to move ! Perform RESET ???
710	Reset on SVI NOT correctly executed
711	Reset on SVI correctly executed
712	interrupt procedure in progress
713	interrupt procedure DONE
714	lower limit value= %{0}%
715	upper limit value= %{1}%
716	tight shutoff value= %{2}%
717	CAM: LINEAR
718	CAM: EQUAL % 50
719	CAM: EQUAL % 30
720	CAM: QUICK_OPEN
721	CAM: CUSTOM
722	STARTUP : LOCAL ONLY
723	STARTUP : LAST MODE
724	STARTUP : LOCAL
725	STARTUP : REMOTE
726	Ratio control : ON
727	Ratio control : OFF
728	Action : REVERSE
729	Action : DIRECT
730	LOCAL SP mode
731	REMOTE SP mode
732	MANUAL SP mode
Reference ID	String