customer - new mexico state university
TRANSCRIPT
—›
—›
—›
—›
CUSTOMER
REFERENCE
PROJECT
SERVICE OF UNIT
MODEL
SURFACE PER UNIT NO. OF UNITS:
QUOTATION NO. :
DATE :
CONNECTED IN :
:
:
:
:
:
:
COLD SIDE HOT SIDE
CONSTRUCTION OF SINGLE UNIT
CONNECTIONSCOLD SIDE
pos. pos.
HOT SIDE
type type
FLUID CIRCULATED
TOTAL FLUID ENTERING
volume
mass
FLUID TYPE
DENSITY
SPECIFIC HEAT
THERMAL CONDUCTIVITY
DYNAMIC VISCOSITY
LATENT HEAT
TEMPERATURE IN / SAT.
TEMPERATURE OUT
OPERATING PRESSURE
NO. OF PASSES / PLATE ARR.
PRESSURE DROP
EXCESS SURFACE / FOULING
HEAT EXCHANGED
LMTD / U-VALUE
DESIGN PRESSURE
TEST PRESSURE
DESIGN TEMPERATURE
PLATE MATERIAL
NO. OF PLATES
PLATE THICKNESS (mm)
FRONT/REAR MATERIAL:
GASKET MATERIAL:
GASKET TYPE:
TIE RODS:
SHROUD:
empty / flooded (H20)
CODE REQUIREMENTS:
NOTES:
Tap Water
30.0 gpm
14,908.4 lb/h
Liquid
61.96
0.999
0.364
0.664
Gas
35.0
170.0
1 / 1 x 7 SH
1.60 PSI
in A 2" Male NPT 316LSS
out B 2" Male NPT 316LSS
Steam
4.8 gpm
2,218.5 lb/h
Liquid
57.13
1.031
0.394
0.18
Gas
0.17
0.553
0.018
0.014
906.8
305.6
305.6
1 / 1 x 7 SW
7.18 PSI
in C 2" Male NPT 316LSS
out D 2" Male NPT 316LSS
2.40 /
2,011,714.0
195.4 / 631.28
150.0
195.0
305.6
AISI 316L
15
0.50
Carbon Steel
EPDM
Mechanically Fixed
Zinc Plated
Aluminum
276 | 284
.45 / .45
New Mexico State University
Brewery Research Facility
Water Heater
SX13-350-15
16.7 ft²
LMH-16-29144
24-Mar-2016
Single
PERFORMANCE OF UNIT
The unit is designed under balanced pressure conditions.
lb/ft³
Btu/lb·°F
Btu/h·ft·°F
cP
Btu/lb
°F
°F
PSI
FLOODED VOLUME (gal)
Btu/h
°F / Btu/ft²·h·°F
PSI
PSI
°F
weight (lb):
TSS Version: FULL 31.2.0 - I -BP
Plate Heat Exchanger
DA
CB
31
.0
Pre
ssu
re P
late
28
.73
14.0
5.0
23
.25
5.31
A,D
B,C
1.95 min.2.07 nom.
1.0 typ
19.13
2.0
0.3
8
4.63
4.63
11
.5
1.5
2.88
(2) Ø.563
3.25
1.5
NOTES: Dimensions shown in InchesTOLERANCE: Nozzle centerline & face: ±0.125" Frame foundation & bolt hole locations: ±0.25"
ConnectionsFluid Port Size Type MaterialHot (in) C 2 Male NPT 316LSSHot (out) D 2 Male NPT 316LSSCold (in) A 2 Male NPT 316LSSCold (out) B 2 Male NPT 316LSS
Nozzle Arrangement
Job No. -101Part No. SX13-350-15 Rev. 0Made Mar 24, 2016 By Lindsey HallCheck Mar 24, 2016 By Lindsey Hall
Construction Frame Size 350Plate Arr't 1 x 7 SH 1 x 7 SWNo. of Plates 15Plate Mtl. 316L SS / 0.5 mmMax No. of Plates 30Gasket Mtl. EPDM - Clip
Design ConditionsHot Cold
Design Pres. (PSIG) 150 150Test Pres. (PSIG) 195 195Design Temp. (F) 305.6 305.6Min. Temp. (F) 32 32Weight Dry/Filled (lb) 276 284
Version: FULL 31.2.0 Model: Sigma X13
—›
—›
—›
—›
CUSTOMER
REFERENCE
PROJECT
SERVICE OF UNIT
MODEL
SURFACE PER UNIT NO. OF UNITS:
QUOTATION NO. :
DATE :
CONNECTED IN :
:
:
:
:
:
:
COLD SIDE HOT SIDE
CONSTRUCTION OF SINGLE UNIT
CONNECTIONSCOLD SIDE
pos. pos.
HOT SIDE
type type
FLUID CIRCULATED
TOTAL FLUID ENTERING
volume
mass
FLUID TYPE
DENSITY
SPECIFIC HEAT
THERMAL CONDUCTIVITY
DYNAMIC VISCOSITY
LATENT HEAT
TEMPERATURE IN / SAT.
TEMPERATURE OUT
OPERATING PRESSURE
NO. OF PASSES / PLATE ARR.
PRESSURE DROP
EXCESS SURFACE / FOULING
HEAT EXCHANGED
LMTD / U-VALUE
DESIGN PRESSURE
TEST PRESSURE
DESIGN TEMPERATURE
PLATE MATERIAL
NO. OF PLATES
PLATE THICKNESS (mm)
FRONT/REAR MATERIAL:
GASKET MATERIAL:
GASKET TYPE:
TIE RODS:
SHROUD:
empty / flooded (H20)
CODE REQUIREMENTS:
NOTES:
Tap Water
30.0 gpm
14,762.1 lb/h
Liquid
61.35
0.999
0.378
0.461
Gas
90.0
193.0
1 / 1 x 7 SH
1.51 PSI
in A 2" Male NPT 316LSS
out B 2" Male NPT 316LSS
Steam
3.6 gpm
1,676.3 lb/h
Liquid
57.13
1.031
0.394
0.18
Gas
0.17
0.553
0.018
0.014
906.8
305.6
305.6
1 / 1 x 7 SW
4.31 PSI
in C 2" Male NPT 316LSS
out D 2" Male NPT 316LSS
17.60 /
1,520,000.0
158.6 / 674.89
150.0
195.0
305.6
AISI 316L
15
0.50
Carbon Steel
EPDM
Mechanically Fixed
Zinc Plated
Aluminum
276 | 284
.45 / .45
New Mexico State University
Brewery Research Facility
Summer Conditions
Water Heater
SX13-350-15
16.7 ft²
LMH-16-29144
24-Mar-2016
Single
PERFORMANCE OF UNIT
The unit is designed under balanced pressure conditions.
lb/ft³
Btu/lb·°F
Btu/h·ft·°F
cP
Btu/lb
°F
°F
PSI
FLOODED VOLUME (gal)
Btu/h
°F / Btu/ft²·h·°F
PSI
PSI
°F
weight (lb):
TSS Version: FULL 31.2.0 - I -BP
Plate Heat Exchanger