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Appendix g, Aerco – AERCO BMK 2.0 LN Natural Gas 2008 User Manual

Page 99

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APPENDIX G

G-3

5)

T

H

IS

IS

A

T

Y

P

ICA

L INS

T

A

LLA

T

IO

N

DRA

W

ING.

LO

CA

L CODES

AND

AUT

HORIT

IES

SHOUL

D B

E

CONS

UL

T

E

D

.

CONV

E

N

IE

NT

F

LOOR DRA

IN. RE

LI

E

F

V

A

LV

E

S

H

OULD B

E

P

IP

E

D

V

E

R

T

ICA

LLY

T

O

A

HE

IGHT

1

8'

' A

B

O

V

E

F

LOOR.

FI

T

T

IN

G

S

TO

P

R

EV

ENT

IN

TE

RFE

R

ENCE

WI

TH

REM

O

VAL

O

F

BO

IL

ER

PANE

LS AN

D CO

VE

RS.

A

LL

PI

PI

NG

A

ND

E

LECT

RI

C

CONNECT

IONS (

S

E

RVICE

SWIT

CHES, CONDUIT

BOXES

) SHOU

LD

L

IKE

WISE B

E

6

" A

W

AY

F

R

OM

SIDE

PA

NEL

S

.

1)

F

O

R A

C

T

U

A

L

SIZ

E

S A

ND L

O

CAT

IO

N

S OF

PIPING A

ND OT

HER C

O

N

N

ECT

IO

N

S

T

O

THE

BO

IL

ER,

S

EE

DI

M

E

NSI

O

N

AL

DRA

WI

NG

(

AP-

A-

79

7)

.

3)

AL

L (

*)

IT

EM

S A

R

E I

NCL

UDE

D SE

PARA

T

E

LY

IN

S

H

IP

M

E

NT

FRO

M

F

A

CT

O

R

Y.

NO

T

ES:

2)

SHEL

L DRA

IN

VA

LV

E A

ND CO

NDE

NSAT

E

DRAI

N

T

R

AP

SHO

U

LD

B

E

A

RRANG

ED

TO

P

E

RM

IT

THE

FL

UI

DS

TO

D

R

AI

N F

R

EEL

Y

, BY

G

R

AVI

T

Y

, T

O

A

4)

L

O

CAT

E

WA

T

E

R INL

E

T

AND

OUT

LET

F

IT

T

INGS

(

i.e

. UN

IONS

, E

LB

O

W

S

, E

T

C.) A

M

INIMUM OF

6'

' F

R

OM B

OILE

R

N

O

R

T

H

VAL

E,

N

J 0

76

47

INT

E

RNA

TIO

NA

L

, INC.

APPD.

DW

N.

BY

SCALE

DATE

DATE

JK

NTS

1023

07

AERCO

SD-A-

674

T

E

M

P

E

R

AT

URE G

A

UGE

P&T

PRES

SURE

&

B

A

LA

NCING VAL

VE

IS

OL

A

T

ION V

A

LV

E

UN

IO

N

Y S

T

R

A

IN

ER

LE

G

E

N

D

B

E

NCHM

ARK

2

.0

M

IL

. B

T

U L

O

W

NO

x

GA

S

F

IRE

D B

OIL

E

R

3-

U

N

IT

INS

T

A

LLA

T

ION

(2

Z

E

RO

-S

ID

E

& 1

S

EPA

RAT

E

)

* C

O

NDE

NS

A

T

E

DR

A

IN T

RA

P

1-

1/

2"

NP

T

D

RA

IN CO

NN

.

BAC

KF

LO

W

P

R

E

VEN

T

ER

DI

A

P

HRA

G

M

T

Y

P

E

E

X

P

A

NS

IO

N

T

A

NK

LI

N

E

SI

Z

E

B

YPA

SS

SU

PP

LY

WA

TE

R

H

EAT

IN

G

SY

ST

EM

SU

PP

LY

PR

ESS

U

R

E

RE

DU

CI

N

G

F

IL

L VAL

VE

P&T

SY

ST

EM

PU

M

P

CH

E

C

K

VA

LV

E

(T

YP

.)

A

U

TOM

A

TIC

AI

R

VE

N

T

AI

R

SEP

AR

AT

O

R

G

AS

SU

PP

LY

H

EAT

IN

G

SY

ST

EM

RE

T

UR

N

* 2"

M

A

N

U

A

L

S

HUT

O

F

F

VA

LV

E

P&T

RE

LI

E

F

VA

LV

E (

T

YP.

)

REV

C

DO

WNST

REA

M

O

F

T

H

E

2"

M

A

NU

AL

SHUT

O

F

F

VA

LVE

TO

B

R

IN

G

THE

G

A

S

PRE

SSURE

DO

WN T

O

2

.0

PS

IG

.

6)

W

H

E

N

A

V

A

ILA

B

LE

GA

S

P

R

E

S

S

URE

IS

GRE

A

T

E

R T

H

A

N

2

.0 P

S

IG, A

L

O

CK

-U

P

S

T

Y

LE

RE

GULA

T

O

R

M

U

S

T

B

E

INS

T

A

LL

E

D

7)

A

GAS

REGUL

A

T

O

R IS

M

A

NDAT

O

R

Y

F

O

R T

H

E ST

AT

E

OF

M

ASS

ACHUS

ET

T

S

, REGARDL

ES

S OF

SU

PPL

Y

PRES

SURE.

S

EE DI

AG

RAM

1

AT

M

AXI

M

U

M

BT

U/

HR I

N

PUT

,

MA

IN

T

A

IN

MI

N

IMU

M N

A

TU

R

A

L

G

A

S

P

R

E

S

S

U

R

E

A

T

4.

0"

W

.C

.(

F

M

GA

S T

R

AIN)

/5

.0

" W.C.(

IRI GAS

T

R

A

IN)

;

MA

X

. GA

S

P

R

E

S

S

URE

=

2.

0

P

S

IG. (S

E

E

NOT

E

6)

D

R

IP T

R

AP

* 2

" M

A

N

U

A

L

S

HUT

O

F

F

VAL

VE

M

A

IN

T

A

IN

A R

E

G

U

LA

T

E

D

4.

0"

W

.C

. (

N

AT

. G

AS,

F

M

)/

5.

0"

W

.C

. (

N

AT

. G

AS,

IR

I)

G

AS PR

ESSU

R

E AT

MAX

B

T

U/

HR I

N

P

UT

G

AS SU

PPL

Y

(T

O

BO

IL

ER

)

(SEE N

O

T

E 7

)

Di

ag

ram 1

P&

T

DR

IP

T

R

A

P