Emerson 1808 Series Relief Valve Or Backpressure Regulators Data Sheet

: Emerson Emerson-1808-Series-Relief-Valve-Or-Backpressure-Regulators-Data-Sheet-680887 emerson-1808-series-relief-valve-or-backpressure-regulators-data-sheet-680887 emerson pdf

Open the PDF directly: View PDF .
Page Count: 8

Download
Open PDF In Browser	View PDF

Bulletin 71.4:1808
July 2010

Types 1808 and 1808A Pilot-Operated Relief
Valves or Backpressure Regulators

W3507

W3716

Type 1808

Type 1808A

Figure 1. Types 1808 and 1808A Pilot-Operated Relief Valves or Backpressure Regulators

Introduction

Features

The Type 1808 globe-style and the Type 1808A
angle-style, pilot-operated relief valves or backpressure
regulators are economical, compact devices used in
gas or liquid service to maintain pressure on oil and gas
separators, and in pressure relief applications in gas
distribution systems. The Types 1808 and 1808A are
available with either a Type 6358 or 6358B pilot. The
Type 6358 pilot is used in gas or liquid backpressure
applications throughout the oil and gas production
industry. This pilot offers a low bleed construction so
it only bleeds when it is repositioning the main valve.
Pressure relief applications in the oil and gas industry
are typically handled by the Type 6358B pilot. This pilot
has a bleed restriction to reduce the buildup pressure
required to reach wide-open flow. These units control
pressures from 3 to 125 psig (0,21 to 8,6 bar), and the
set pressure is varied to individual requirements by
the adjusting screw on the pilot. On gas service, the
pilot exhaust can be piped into the downstream piping
or vented to atmosphere. On liquid service, the pilot
exhaust should be piped into the downstream piping or
to a safe location.

  •  Simple, Reliable Design—Units have fewer
  parts for reliable service and minimum spare
  parts inventory.
  •  Compact and Lightweight—Less than 12-inches 	
  (305 mm) tall and weighs 25 pounds (11 kg) or 	
  less, these units are easily transported and installed	
  where space is limited.
  •  Simplified, Convenient Installation in Any 	
  Position—Pressure connection in diaphragm 	
  casings and factory-piped pilot tubing mean 		
  no upstream control line is required on standard 	
  installations. There are no mounting restrictions to 	
  limit service.

www.fisherregulators.com

www.fisherregulators.com

D100163X012

  •  Versatility in Both Liquid and Gas Service—	
  Pilot exhaust port and standard tapped pilot spring 	
  case (Figure 2) both come with removable vent for 	
  remote piping when necessary. The standard 	  	
tapped pilot spring case comes complete with a 	  	
gasketed closing cap that permits pressure loading for
  remote pneumatic adjustment of the set pressure.

Bulletin 71.4:1808
Specifications
Available Configurations
	
See Table 1
Body Size and End Connection Style
	
2 NPT
Maximum Relief (Inlet) Pressure(1)
	
150 psig (10,3 bar) including buildup
Set Pressure Range
	
See Table 2
Differential Pressures
	
Maximum: 125 psig (8,6 bar)
	
Minimum: 5 psig (0,34 bar)
Type 6358 Pilot Bleed
	
Bleeds only when repositioning the main valve
Type 6358B Pilot Bleed
	
Continuously bleeds while inlet pressure is above 		
	
set pressure
Flow and Sizing Coefficients
	
See Table 3
Main Valve Flow Capacities
	
See Tables 4 and 5 and Capacity Information section
Pressure Registration
	
Internal (standard) or External (optional)
Pilot Tubing and Connections
	
1/4 NPT with or without P590 Series filter
Temperature Capabilities(1)
	
-20° to 180°F (-29° to 82°C)
Construction Materials
	
Main Valve
	
Type 1808 Body: Cast iron or WCC Steel
	
Type 1808A Body: Cast iron
	
Diaphram Plates and Diaphragm Casings:
	
Zinc-plated steel
	
Diaphragm: Neoprene (CR), Nitrile (NBR)

Construction Materials (continued)		
	
O-Rings: Nitrile (NBR)
	
Gaskets: Nitrile (NBR)
	
Back-up Rings: Polytetrafluoroethylene (PTFE)
	
Spring: Zinc-plated steel (standard)
	
Valve Plug Guide: Stainless steel
	
	
	
	
	
	
	
	
	
	
	
	
	
	

6358 Series Pilots
Body: Aluminum or CF8M Stainless steel
Spring Case: Aluminum or Stainless steel
Body Plug: Aluminum or Stainless steel
Valve Plug: Nitrile (NBR) or thermoplastic
plug with stainless steel stem
Spring: Zinc-plated steel
Diaphragm: Nitrile (NBR) or Fluorocarbon (FKM)
Spring Seat: Zinc-plated steel	
Stem Guide: Stainless steel
Adjusting Screw: Zinc-plated steel
O-Rings: Nitrile (NBR) or Fluorocarbon (FKM)
Closing Cap: Plastic or Stainless steel
Connector Cap: Stainless steel

	
	
	
	
	

Mounting Parts
Tubing: Stainless steel
Fittings: Steel or Stainless steel
Pipe Tees: Galvanized steel
Pipe Nipples: Malleable Iron, Galvanized Steel, 	
and Stainless Steel

Options
	
•  Upstream control line construction
	
•  Pressure gauge (0 to 160 psig/0 to 11,0 bar/
	  0 to 1,1 MPa)
	
•  P590 Series Pilot Supply Filter
Approximate Weights
	
Type 1808: 22 pounds (10 kg)
	
Type 1808A: 25 pounds (11 kg)

1. The pressure or temperature limits in this Bulletin and any applicable standard or code limitations should not be exceeded.

  •  Quick Disassembly—With the removal of just two
  nuts, the upper and lower casings lift away, exposing	
the trim and leaving the main valve body in the line.
  •  Optional Upstream Registration for Reduced 	
  Buildup—For gas service with the Type 6358B 	
  pilot, upstream control line construction is available 	
  to provide wide-open relief flow capacity with less 	
  buildup regardless of set pressure.
  •  Self-Draining Body—The Type 1808A angle-body
  design has increased capacity and provides 	 	

2

 

complete process fluid drainage from body cavity 	
during shut-down period or before disassembly of
the main valve.

Specifications
The Specifications section gives some general
specifications for the 1808 Series Pilot-Operated Relief
Valves or Backpressure Regulators. The nameplates
give detailed information for a particular regulator as it
comes from the factory.

	

Bulletin 71.4:1808
upper portion
of valve plug
to exhaust
port

upper portion
of valve plug

diaphragm
assembly

hollow
passage
in valve
plug stem

lower portion
of valve plug

hollow
passage
in valve
plug stem

lower portion
of valve plug

diaphragm
assembly

to exhaust
port

to main valve
diaphragm

to main valve
diaphragm

FIXED RESTRICTION

restriction plug

TYPE 6358B RELIEF SERVICE

TYPE 6358 BACKPRESSURE SERVICE
pilot exhaust

pilot

control spring
spring
diaphragm

valve plug
INLET PRESSURE
atmospheric pressure
Outlet/exhaust Pressure
loading pressure
E0075

main valve

Figure 2. Type 1808 with 6358 Series Operational Schematic

Principle of Operation

Pilots

Refer to Figure 2. A pressure relief valve is a control
device that opens to relieve fluid to atmosphere during
an overpressure occurrence. A backpressure regulator
is a control device that maintains a constant upstream
pressure throughout a given flow range. It functions
the same as a relief valve in that it opens on increasing
upstream pressure. The Type 1808 or 1808A cannot
be used as an ASME safety relief valve.

A 6358 Series pilot is typically used with one of several
different main valves in a pressure relief or backpressure
application. This pilot is usually used in gas service. It
has an easily-installed valve plug that can be removed
without removing the valve plug stem guide.

3

Bulletin 71.4:1808
Table 1. Available Configurations
TYPE
1808
1808A

PILOT

DESCRIPTION

6358

Globe-style body for backpressure applications

6358B

Globe-style body for relief applications

6358

Angle-style body for backpressure applications

6358B

Angle-style body for relief applications

Table 2. Types 6358 and 6358B Set Pressure Ranges, Pressure Ratings, and Pilot Spring Information
Set Pressure Ranges,
psig (bar)
3 to 18 (0,21 to 1,2)
15 to 40 (1,0 to 2,8)
35 to 125 (2,4 to 8,6)

Part Number

Color

PILOT spring Information
Wire Diameter, Inches (mm)

1B986027212
1e392527022
1k748527202

Green
Yellow
Red

0.120 (3,05)
0.148 (3,76)
0.192 (4,88)

Free Length, Inches (mm)
2.12 (54,0)
2.00 (51,0)
2.19 (55,6)

Table 3. Flow and Sizing Coefficients
TYPE

FLOW COEFFICIENTS
(WIDE-OPEN)

C1

Km

Cg

Cv

1808

1410

40.1

35.2

0.79

1808A

1800

51.4

35.0

0.76

IEC SIZING COEFFICIENTS
XT
0.78

FL
0.89
0.87

FD
0.50

Table 4. Capacities(1)(2) for the Type 1808 Using Standard Internal Control Line and a Type 6358 or 6358B Pilot with High-Gain Restriction
Relief
Pressure
Setting,
Psig (bar)

 

Capacity in Thousands of Scfh (Nm3/h) Of 0.6 specific gravity Natural Gas
Pressure Buildup In Psig (bar) Over Relief Pressure Setting
2 (0,14)

6 (0,41)

10 (0,69)

15 (1,0)

20 (1,4)

25 (1,7)

30 (2,1)

5
12
20
30
40

(0,34)
(0,83)
(1,4)
(2,1)
(2,8)

32
41
56
67
85

(0,9)
(1,1)
(1,5)
(1,8)
(2,3)

46
55
73
89
105

(1,2)
(1,5)
(2,0)
(2,4)
(2,8)

50
65
80
99
120

(1,3)
(1,7)
(2,1)
(2,7)
(3,2)

61
74
89
108
127

(1,6)
(2,0)
(2,4)
(2,9)
(3,4)

70
84
99
117
136

(1,9)
(2,3)
(2,7)
(3,1)
(3,6)

80
93
108
127
145

(2,1)
(2,5)
(2,9)
(3,4)
(3,9)

89
102
117
136
154

(2,4)
(2,7)
(3,1)
(3,6)
(4,1)

50
60
70
80

(3,5)
(4,1)
(4,8)
(5,5)

94 (2,5)
----------

120
135
150
161

(3,2)
(3,6)
(4,0)
(4,3)

137
152
168
180

(3,7)
(4,1)
(4,5)
(4,8)

145
163
181
200

(3,9)
(4,4)
(4,8)
(5,4)

154
172
190
201

(4,1)
(4,6)
(5,1)
(5,4)

163
181
200
218

(4,4)
(4,8)
(5,4)
(5,8)

172
190
209
227

(4,6)
(5,1)
(5,6)
(6,1)

90
100
110
125

(6,2)
(6,9)
(7,6)
(8,6)

-------------

170
183
197
201

(4,6)
(4,9)
(5,3)
(5,4)

192
209
223
241

(5,1)
(5,6)
(6,0)
(6,5)

213
231
246
267

(5,7)
(6,2)
(6,6)
(7,2)

227
245
263
284

(6,1)
(6,6)
(7,0)
(7,6)

236
254
272
298

(6,3)
(6,8)
(7,3)
(8,0)

245 (6,6)
263 (7,0)
281 (7,5)
----

  Shaded areas indicate capacities with main valve wide-open.
1. Capacities based on 0 psig (0 bar) outlet pressure. If outlet pressure is not 0 psig (0 bar), shaded capacities may be recalculated using the wide-open Cg and the desired pressure drop.
2. For Type 1808A capacities, multiply the capacities in this table by 1.27.

Relief Valve
As long as the inlet pressure is below the set pressure,
the pilot control spring keeps the pilot valve plug
closed. Inlet pressure passes through the pilot
restriction and registers as loading pressure on top of
the diaphragm. Force from the main spring, in addition
to inlet pressure bleeding through the pilot restriction,
provide downward loading pressure to keep the main
valve closed.
When the inlet pressure rises above the set pressure,
the pressure on the pilot diaphragm overcomes the
pilot control spring and opens the pilot valve plug. The

4

pilot then exhausts the loading pressure from the top
of the main valve diaphragm. The pilot continuously
exhausts gas when the inlet pressure is above the set
pressure. The inlet pressure unbalance overcomes
the main spring force and opens the main valve.
As the inlet pressure drops, the pilot control spring
begins to close the pilot valve plug and the exhaust
slows. This causes the inlet pressure to build in the
main valve diaphragm casing, allowing the control spring
to close the main valve. Once the main valve is closed,
the pilot valve plug closes and the exhaust stops.

Bulletin 71.4:1808
Table 5. Capacities for the Type 1808 Using Optional External Control Line and Type 6358B Pilot with High-Gain Restriction
Set Pressure
Range, Psig (bar)

Buildup over
set pressure to
begin opening
main valve(2),
Psig (bar)

3 to 18
(0,21 to 1,2)

3
5
10
15

(0,21)
(0,35)
(0,69)
(1,0)

0.9
0.7
0.7
0.7

15 to 40
(1,0 to 2,8)

15
20
30
40

(1,0)
(1,4)
(2,1)
(2,8)

40
50
60
70

(2,8)
(3,5)
(4,1)
(4,8)

80
90
100
110
125

(5,5)
(6,2)
(6,9)
(7,6)
(8,6)

35 to 125
(2,4 to 8,6)

1.
2.
3.
4.

Set Pressure(1),
Psig (bar)

Buildup over
set pressure
to fully open
main valve(3),
psig (bar)

(0,06)
(0,05)
(0,05)
(0,05)

6.0
4.0
1.2
1.0

Pressure drop
below set
pressure to
reseat pilot,
psig (bar)

CApacities of 0.6
specific gravity
natural gas(4),
scfh (Nm3/h)

(0,41)
(0,28)
(0,08)
(0,07)

37 000
37 000
42 000
52 000

(992)
(992)
(1126)
(1394)

0.8 (0,05)

1.1 (0,07)

53 000
63 000
82 000
101 000

(1420)
(1688)
(2198)
(2707)

1.4 (0,09)

1.9 (0,13)

102 000
121 000
139 000
157 000

(2734)
(3243)
(3725)
(4208)

2.2 (0,15)

176 000
194 000
213 000
231 000
258 000

(4717)
(5199)
(5708)
(6191)
(6914)

1.0 (0,07)

1.6 (0,11)

Set pressure is defined as the pressure at which the pilot exhaust starts to bubble (discharge).
Crack pressure is the inlet pressure at which the main valve starts audible flow.
Inlet pressure buildup over the set pressure to achieve wide-open capacity.
Capacities with inlet piping equal to body size and without outlet piping.

Backpressure Regulator
As long as inlet pressure remains below setpoint, the
pilot spring keeps the pilot valve plug closed. Inlet
pressure passes through the upper port around the
upper portion of the valve plug then through the hollow
passage in that valve plug. Force from the main spring,
along with inlet pressure bleeding through the pilot,
provide downward loading pressure to keep the main
valve closed.
When inlet pressure rises above the set pressure,
pressure on the pilot diaphragm overcomes the control
spring to close the upper port and stroke the valve plug
to open the lower port. The pilot then exhausts loading
pressure from the top of the main valve diaphragm.
The pilot exhausts only while repositioning the main
valve. The inlet pressure unbalance overcomes the
spring force and opens the main valve.
As the inlet pressure drops, the pilot control spring
begins to close the pilot valve plug and the exhaust
slows. This causes the inlet pressure to build in the
main valve diaphragm casing, allowing the control spring
to close the main valve. Once the main valve is closed,
the pilot valve plug closes and the exhaust stops.

Installation
Types 1808 and 1808A relief valves or backpressure
regulators may be installed in any position as long as
the flow through the main valve corresponds with the
flow arrow on the main valve body (Type 1808) or runs
in through the bottom connection and out through the
side connection (Type 1808A).

An upstream control line is not required because of
the integral pilot supply tubing; however, for a more
accurate relief valve or backpressure regulator, this
tubing may be disconnected for upstream registration,
and the main valve diaphragm casing tapping plugged.
For liquid service, the pilot exhaust should be piped
to the downstream line or to a safe location. For gas
service, the pilot must be piped to a safe area because,
in enclosed conditions such as inside installations,
exhausting gas can accumulate causing a danger
of explosion. A vent line or stack must be located to
avoid venting gas near buildings, air intakes, or other
hazardous locations, and the line or stack opening must
be protected against anything that might clog it. The
thrust effect of a venting relief valve must be considered
when designing relief valve outlet piping and anchoring.

Capacity Information
Gases
Tables 4 and 5 give relief capacities at selected
set pressures for the Type 1808 backpressure
regulator or relief valve. Flows are in thousands of
scfh (60°F and 14.7 psia) and thousands of Nm³/h
(0°C and 1,01325 bar) of 0.6 specific gravity natural
gas. To determine equivalent capacities for air,
propane, butane, or nitrogen, multiply the Table 4 or 5
capacity by the following appropriate conversion factor:
0.775 for air, 0.625 for propane, 0.548 for butane, or
0.789 for nitrogen. For gases of other specific gravities,
multiply the given capacity by 0.775, and divide by
the square root of the appropriate specific gravity. If
capacity is desired for the Type 1808A, multiply by 1.27.
5

Bulletin 71.4:1808

5.31
(135)

5.94
(151)

11.44
(291)

2.19
(57)

3.19
(81)

2.94
(75)

3.19
(81)

11.81
(300)

3.19
(81)

6.13
(156)

inches
(mm)

TYPE 1808A

TYPE 1808

1808

9.88
DIAMETER
(251)
10.88
(276)

COMMON DIMENSIONS
FOR BOTH TYPES

Figure 3. Dimensions

  1.  To determine capacities at set pressures or 	
    buildups not given in Tables 4 and 5, use one 	
    of the following formulas, and convert according
    to the factors in the preceding paragraph
    if necessary:
Q = (P1 + buildup)abs Cg

   (P1 + buildup)abs
   C1	
   ΔP	

520
GT

Liquids

  2.  For pressure drops lower than critical (absolute 	
    outlet pressure greater than one-half of absolute 	
    inlet pressure), use the following formula:
Q=

ΔP
3417
520
C (P + buildup)abs SIN
C1 (P1+ buildup)abs
GT g 1

where,
   Q	
   G	
   T	
	
   Cg	

6

= absolute inlet pressure
= P1 + Patm + buildup
= P1 + 14.7 + buildup
= Cg/Cv (See Table 3)
= pressure drop across the valve in psig

Deg.

= flow capacity in scfh
= specific gravity of gas
= absolute temperature of gas at inlet in °Rankine
(°Rankine = °F + 460)
= sizing coefficient from Table 3

To determine relief capacities in U.S. gallons per
minute, use the Catalog 10 liquid sizing procedures
in conjunction with the appropriate liquid sizing
coefficient (Cv) and recovery coefficient (Km) from the
Specifications section. Then, if capacity is desired in
Nm3/h, multiply U.S. gallons per minute by 0.2271.

Ordering Information
Refer to the Specifications section on page 2. Fill
out the order guide on page 7, carefully review the
description of each specification. Always specify the
type numbers of other desired equipment as well as
the main valve and pilot.

Bulletin 71.4:1808
Ordering Guide
Type (Select One)
    1808 (globe body)***
    1808A (angle body)**
Body Material (Select One)
    Cast iron***
    WCC Steel (Type 1808 only)*
Pilot (Select One)
    Type 6358 (for backpressure application)***
    Type 6358B (for relief application)***

Gauge (Optional)
    Yes
Pilot Supply Filter (Optional)
    Yes
Main Valve Parts Kit (Optional)
    Yes, please send one parts kit to match this order.
Pilot Parts Kit (Optional)
    Yes, please send one parts kit to match this order.

Set Pressure Range (Select One)
    3 to 18 psig (0,21 to 1,2 bar), Green***
    15 to 40 psig (1,0 to 2,8 bar), Yellow***
    35 to 125 psig (2,4 to 8,6 bar), Red***
O-Ring Material (Select One)
    Nitrile (NBR)***
    Fluorocarbon (FKM)**
Tubing and Fittings (Select One)
    Stainless steel tubing and steel fittings***
    Stainless steel tubing and stainless steel fittings***
Upstream Control Line Construction (Optional)
    Yes

Specification Worksheet
  Application:
  Specific Use
  Line Size
  Gas Type and Specific Gravity
  Gas Temperature
  Relief Valve Size:
  Brand of upstream regulator?
  Orifice size of the upstream regulator?
  Wide-open coefficient of the upstream regulator?

Regulators Quick Order Guide
***
**
*

Readily Available for Shipment
Allow Additional Time for Shipment
Special Order, Constructed from Non-Stocked Parts.
Consult your local Sales Office for Availability.

  Pressure:
  Maximum Inlet Pressure (P1max)
  Minimum Inlet Pressure (P1min)
  Downstream Pressure Setting(s) (P2)
  Maximum Flow (Qmax)
  Performance Required:
  Accuracy Requirements?
  Need for Extremely Fast Response?
  Other Requirements:

Availability of the product being ordered is determined by the component with the
longest shipping time for the requested construction.

7

Bulletin 71.4:1808

Industrial Regulators

Natural Gas Technologies

TESCOM

Emerson Process Management
Regulator Technologies, Inc.

Emerson Process Management
Regulator Technologies, Inc.

Emerson Process Management
Tescom Corporation

USA - Headquarters
McKinney, Texas 75069-1872 USA
Tel: 1-800-558-5853
Outside U.S. 1-972-548-3574

USA - Headquarters
McKinney, Texas 75069-1872 USA
Tel: 1-800-558-5853
Outside U.S. 1-972-548-3574

USA - Headquarters
Elk River, Minnesota 55330-2445 USA
Tel: 1-763-241-3238

Asia-Pacific
Shanghai, China 201206
Tel: +86 21 2892 9000

Asia-Pacific
Singapore, Singapore 128461
Tel: +65 6777 8211

Europe
Bologna, Italy 40013
Tel: +39 051 4190611

Europe
Bologna, Italy 40013
Tel: +39 051 4190611
Gallardon, France 28320
Tel: +33 (0)2 37 33 47 00

Middle East and Africa
Dubai, United Arab Emirates
Tel: +971 4811 8100

Europe
Selmsdorf, Germany 23923
Tel: +49 (0) 38823 31 0

For further information visit www.fisherregulators.com
The Emerson logo is a trademark and service mark of Emerson Electric Co. All other marks are the property of their prospective owners. Fisher is a mark owned by Fisher Controls, Inc., a
business of Emerson Process Management.
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. We reserve the right to modify or improve the designs or specifications of such
products at any time without notice.
Emerson Process Management does not assume responsibility for the selection, use or maintenance of any product. Responsibility for proper selection, use and maintenance of any Emerson
Process Management product remains solely with the purchaser.

©Emerson Process Management Regulator Technologies, Inc., 1978, 2010; All Rights Reserved



---

Source Exif Data:

File Type                       : PDF
File Type Extension             : pdf
MIME Type                       : application/pdf
PDF Version                     : 1.4
Linearized                      : Yes
Encryption                      : Standard V2.3 (128-bit)
User Access                     : Print
Tagged PDF                      : Yes
XMP Toolkit                     : Adobe XMP Core 4.1-c037 46.282696, Mon Apr 02 2007 18:36:42
Create Date                     : 2010:07:06 23:48:07+08:00
Metadata Date                   : 2010:07:06 23:48:11+08:00
Modify Date                     : 2010:07:06 23:48:11+08:00
Creator Tool                    : Adobe InDesign CS3 (5.0.4)
Thumbnail Format                : JPEG
Thumbnail Width                 : 256
Thumbnail Height                : 256
Thumbnail Image                 : (Binary data 11484 bytes, use -b option to extract)
Instance ID                     : uuid:a9f9e016-8009-4b25-988c-60614f9a9ee7
Document ID                     : adobe:docid:indd:3371a667-f92f-11de-a8a2-afcf1ae1e3d0
Rendition Class                 : proof:pdf
Derived From Instance ID        : 3371a666-f92f-11de-a8a2-afcf1ae1e3d0
Derived From Document ID        : adobe:docid:indd:3371a665-f92f-11de-a8a2-afcf1ae1e3d0
Manifest Link Form              : ReferenceStream, ReferenceStream, ReferenceStream, ReferenceStream, ReferenceStream, ReferenceStream, ReferenceStream, ReferenceStream, ReferenceStream
Manifest Placed X Resolution    : 72.00, 300.00, 300.00, 72.00, 72.00, 72.00, 72.00, 72.00, 72.00
Manifest Placed Y Resolution    : 72.00, 300.00, 300.00, 72.00, 72.00, 72.00, 72.00, 72.00, 72.00
Manifest Placed Resolution Unit : Inches, Inches, Inches, Inches, Inches, Inches, Inches, Inches, Inches
Manifest Reference Instance ID  : uuid:f8cb9cde-23c5-11da-bf8f-000a95badf96, uuid:7CA185730A7EDF11A3D4D8C08CDC58CA, uuid:215A92F70A7EDF11AC14CA3AE1AD47F2, uuid:111bd73d-add3-4d8e-9cf6-4aa44cbd778b, uuid:85ea6bee-25e9-40f3-a963-f53429020609, uuid:85ea6bee-25e9-40f3-a963-f53429020609, uuid:111bd73d-add3-4d8e-9cf6-4aa44cbd778b, uuid:001f1581-6df6-4a1f-af34-1f8c75fdaec8, uuid:f8cb9cde-23c5-11da-bf8f-000a95badf96
Manifest Reference Document ID  : uuid:E928E74DCF8ADD11B90DF7725639CDFB, uuid:EF28E74DCF8ADD11B90DF7725639CDFB, uuid:1B2F99E1D2ACDD11AB03FAFE7874E2B3, uuid:192F99E1D2ACDD11AB03FAFE7874E2B3, uuid:192F99E1D2ACDD11AB03FAFE7874E2B3, uuid:1B2F99E1D2ACDD11AB03FAFE7874E2B3, uuid:293E381A8089DD118544C08236248DC5
Format                          : application/pdf
Producer                        : Adobe PDF Library 8.0
Trapped                         : False
Page Count                      : 8
Creator                         : Adobe InDesign CS3 (5.0.4)

EXIF Metadata provided by EXIF.tools