12-10 Pump Performance Curves in Simulations_Final

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Evaluate Sulzer Pumps in Your ProcesThrough aspenONE® ExchangeStephanie Quind t, Sulzer

Br ian Kurowski , AspenTech

December 10, 2015

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© 2015 Aspen Technology, Inc. All rights reserved.

Today’s Presenters 

Stephanie Quindt

Senior Applications Specialist

Brian Kurowski

Product Manager

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© 2015 Aspen Technology, Inc. All rights reserved.

© 2015 Aspen Technology, Inc. All rights reserved.

• What is aspenONE Exchange

• Benefits of Using Sulzer Select

• Demo of Sulzer Select

• Questions

Today’s Agenda 

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© 2015 Aspen Technology, Inc. All rights reserved.

© 2015 Aspen Technology, Inc. All rights reserved.

What is aspenONE Exchange

Flowsheets (1500+)

 – Complete Process Flowsheets

 – User Models

 – Extensions

Tools

 – Sulzer Select

 – PUMP-FLO

Literature

 – HTFS Research Network Documents

 – Process Manuals

Knowledge Base (300

 – Tech Tips

Training (100+)

 – Computer Based Training (

 – Videos

 – Documentation

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 Aspen Exchange is an on-line application

If you doan Aspen

 Account,

support p

for one

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35%

20% 40% 60% 80% 100%

Time

Conception 

Specification 

PurchaseManufacturing

Testing & Insta

Traditional

Project

StrategicRelationship

Project

Process Stages

0%

Creating Value - Compressed Schedule

Project Execution Time

Majority of the opportunity for compression of the project execution time lies in the fronMaking the right initial selections saves time, money and engineering hours.

7/23/2019 12-10 Pump Performance Curves in Simulations_Final

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Initial Selections

(Q, H, ɳ) 

50,000 ft.

Optimization

(Pump Model)

5,000 ft.

Wha

IteraChan

Value of Equipment Based Modeling – During FEED

Sulzer Select in aspenONE Exchange will meet your needs at a

7/23/2019 12-10 Pump Performance Curves in Simulations_Final

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Selecting the Right Equipment for the Service

 API Pump Offerings

for

Hydrocarbon

Processing

Industry Applications

Involve your Rotating Equipment Experts

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Selecting the Right Equipment (API Vs ANSI)

Flow = 225 USGPM, Diff Head = 160 ft., Liquid – Water

ANSI B73.1 API 610

Pump CPT 22-1B (3x1.5x10) (O) 2x3x8 – 1 - OHH

ɳ   64% 66%Motor 20 HP 20 HP

Price 7K 45K

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Optimization (Selecting the Correct Model)

Between Bearing Double Suction Pumps are typically specified for booster se

Flow = 2,738 USGPM and Diff Head = 273 ft.

BBS 10x14x18K-1

Eff = 80 %

NPSHr = 13.8 ft

Motor Rating = 300 HP

OHH 8x10x2

Eff = 79 %

NPSHr = 18.5

Motor Rating

319 K USD 223 K U

30% saving using

Sulzer Select in

aspenONE

Exchange

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Sulzer Presentation 2015

Optimization (Utilizing system flexibility For NPSH)

Vertically Suspended Pumps are usual choice where NPSHa is limited

Flow = 168.0 USGPM and Diff Head = 1674.0 ft.

SJD-12EHC 4 stg

Eff = 68.33 %

NPSHr = 6.49 ft

Motor Rating = 15 HP

ZF 100-50

Eff = 58%

NPSHr = 1

Motor Rat

163 K USD

98 K USD

40% saving using

Sulzer Select in

aspenONE

Exchange 

NPSHa =

NPSHa = 2.45Ft

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Sulzer Presentation 2015

Sulzer’s Sales Program Brochure 

Sulzer’s Sales Program:http://www.sulzer.com/en/-

/media/Documents/ProductsAnd

ps_and_Systems/General/Broch

gram_E00543.pdf  

 Additional Resources:http://www.sulzer.com/en/Products-and-

Services/Pumps-and-Systems 

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Software Demo

Sulzer Select

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Webinar SummaryPump Performance Curves in Simulations

•  Accelerate pump selection to sho

build time

• Evaluate heat exchanger fouling e

process

• Reduce utilities by finding optimu

built plant design•  Analyze safety scenarios using eq

flow and pressure

• Improve detail of existing simulati

including equipment data

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Visit the Aspen HYSYS Rwww.aspentech.com/aspen-h

Q&A

Stephanie Quindtstephanie.quindt@

Brian Kurowski

brian.kurowski@as

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 AspenTech is ranked as a top

innovative growth company

Thank You