GEA Heat Exchangers, Inc. PHE Division100 GEA DriveYork, PA 17406 USAPh: +717-268-6200Fax: +717-268-6162info.phe-systems.usa@gea.comWebsite: www.gea-phe.com/usa

Condenser

Customer / Project Project Created 7/11/2015 12:41 PM Selection ID NUK9E7Q8GUser name Alex Croitoru Print date 7/11/2015

Model: C15BW

Heat of rejection rate (kW) 23.0 Number of refrigerant circuits 1Log mean temp. diff. (C) 5.3 Nominal surface (m) 3.7Overall HTC (W/mK) 1,385 Dimensions 124W x 532H x 144DOversurface percent 19.2 Net weight (kg) 16.4Model size 5x20

Design Conditions Side A - Condensing Side B - LiquidRefrigerant R-134a

Ref. mass flow (kg/min) 7.1Condensing temp. (C) 40.0Condensing pressure (bar ga) 9.2Gas entering temp. (C) 60.0Subcooling (C) 6.0Fluid type Water

Fluid mass flow rate (kg/min) 66Entering fluid temp. (C) 32.0Leaving fluid temp. (C) 37.0Fluid flow rate (L/min) 66.4Fluid fouling factor (mK/W) 0.000018Model Parameters

Number of channels 29 30

Velocity (m/s) 0.4 0.2Pressure drop (kPa) 1.7 11.0Heat transfer coef. (W/mK) 1,778 9,167Internal volume (L) 4.311 4.460

GEA Heat Exchangers, Inc. PHE Division100 GEA DriveYork, PA 17406 USAPh: +717-268-6200Fax: +717-268-6162info.phe-systems.usa@gea.comWebsite: www.gea-phe.com/usa

Ratings at Varying Conditions

Percent difference -15% -7% 0% 7% 15%

Pressure drop (kPa) (Side A) 1.2 1.4 1.7 1.9 2.1Pressure drop (kPa) (Side B) 8.1 9.5 11.0 12.6 14.4Heat of rejection rate (kW) 19.5 21.3 23.0 24.7 26.5Fluid flow rate (L/min) (Side B) 56.4 61.4 66.4 71.4 76.3Fluid mass flow rate (kg/min) (Side B) 56 61 66 71 76Entering fluid temp. (C) (Side B) 32.0 32.0 32.0 32.0 32.0Leaving fluid temp. (C) (Side B) 37.0 37.0 37.0 37.0 37.0Oversurface percent 30.4 24.4 19.2 14.4 10.2

DisclaimerThis software and the generated calculations provided herein are estimates only and should be treated as such. GEA PHE Systems North America, Inc. always strives to givecomplete and accurate information, but cannot provide any guarantees. This software and its output are provided "as is" and any express or implied warranties, including, butnot limited to, the implied warranties of merchantability and fitness for a particular purpose are disclaimed. In no event shall GEA PHE Systems North America, Inc. be liablefor any direct, indirect, incidental, special, exemplary, or consequential damages (including, but not limited to, procurement of substitute goods or services; loss of use, data,or profits; or business interruption) however caused and on any theory of liability, whether in contract, strict liability, or tort (including negligence or otherwise) arising in anyway out of the use of this software, even if advised of the possibility of such damage.

Dimension Sheet Brazed Plate Heat Exchanger

Customer:

Project:

Model Nomenclature:

Selection ID:

Dimensions data

Technical data

Allowable Working Pressure and Temperature

Max pressure Circuit A

Circuit B

Max temperature

Min temperature

Standard construction materials

Braze Alloy

Connector

Plate

Code Approvals

Connections

Circuit A Circuit B

Position 1 Position 2 Position 3 Position 4 Standard

Optional

Height

Installation Notes:

Pipe in counter flow direction

Water Strainer (20-40 mesh) installation recommended

BPHE weight:

Dimensions are in inches [mm]reference only.

Volume:

Circuit A: Circuit B:

H

G

A

C

FDB

2 4

1 3

A:

B:

C:

D:

F:

G:

H:

NUK9E7Q8G

Project Created 7/11/2015 12:41 PMC15BW

4.88 (124.0)20.94 (531.9)2.88 (73.2)18.81 (477.8)5.51 (140.0)2.36 (59.9)5.67(144.0)

0.152 ft (4.311 L) 0.157 ft (4.460 L) 36.2 lb (16.4 kg)

1-3/8" IDS 7/8" IDS 1-3/8" IDS 1-3/8" IDS

Copper 99.9%304 Stainless Steel316L Stainless Steel

0.79 (20.0)1.58 (40.0)

450 psig (31.0 bar ga)450 psig (31.0 bar ga)

350.0 F (176.7 C)-320.0 F (-195.6 C)UL Listed, CRN pending

Optional: ASME (UM stamped), PED (CE)