12-10 pump performance curves in simulations_final
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7/23/2019 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
7/23/2019 12-10 Pump Performance Curves in Simulations_Final
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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
7/23/2019 12-10 Pump Performance Curves in Simulations_Final
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Aspen Exchange is an on-line application
If you doan Aspen
Account,
support p
for one
7/23/2019 12-10 Pump Performance Curves in Simulations_Final
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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
7/23/2019 12-10 Pump Performance Curves in Simulations_Final
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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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