Product-driven process design: from molecule to enterprise
Gespeichert in:
| Hauptverfasser: | , , |
|---|---|
| Format: | Buch |
| Sprache: | English |
| Veröffentlicht: |
Berlin
De Gruyter
[2023]
|
| Ausgabe: | 2nd edition |
| Schriftenreihe: | De Gruyter graduate
|
| Schlagworte: | |
| Online-Zugang: | https://www.degruyter.com/isbn/9783111014906 Inhaltsverzeichnis Inhaltsverzeichnis |
| Beschreibung: | XVII, 576 Seiten Illustrationen, Diagramme 24 cm, 983 g |
| ISBN: | 9783111014906 3111014908 |
Internformat
MARC
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| 100 | 1 | |a Zondervan, Edwin |e Verfasser |0 (DE-588)1205470999 |4 aut | |
| 245 | 1 | 0 | |a Product-driven process design |b from molecule to enterprise |c Edwin Zondervan, Cristhian Almeida-Rivera, and Kyle Vincent Camarda |
| 250 | |a 2nd edition | ||
| 264 | 1 | |a Berlin |b De Gruyter |c [2023] | |
| 264 | 4 | |c © 2023 | |
| 300 | |a XVII, 576 Seiten |b Illustrationen, Diagramme |c 24 cm, 983 g | ||
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| 653 | |a Product Technology | ||
| 653 | |a Process Engineering | ||
| 653 | |a Chemical Engineering | ||
| 653 | |a Industrial Chemistry | ||
| 653 | |a TB: Textbook | ||
| 653 | |a Produktdesign; Produktentwicklung; Technische Chemie; Verfahrenstechnik; Research and Development | ||
| 653 | |a Product Technology; Process Engineering; Chemical Engineering; Industrial Chemistry | ||
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Datensatz im Suchindex
| _version_ | 1806960712657928192 |
|---|---|
| adam_text |
CONTENTS
FOREWORD
-
VII
PART
I:
PRODUCT-CENTRED
DESIGN
1
1.1
1.2
1.3
INTRODUCTION
-
3
THE
CURRENT
SETTING
OF
THE
PROCESS
INDUSTRY
-
3
THE
DEVELOPMENT
OF
THE
PDPS
APPROACH
-
4
STRUCTURE
OF
THE
BOOK
-
5
2
2.1
2.1.1
2.1.2
2.1.3
2.1.4
2.2
2.2.1
2.2.2
2.3
2.3.1
2.3.2
2.3.3
2.4
2.5
2.5.1
2.5.2
2.5.3
2.5.4
2.6
2.7
PERFORMANCE
PRODUCTS
IN
A
CHALLENGING
ENVIRONMENT
-
9
A
CHALLENGING
ENVIRONMENT
FOR
THE
PROCESS
INDUSTRY
-
9
ENVIRONMENTAL
AND
ENERGY
CHALLENGES
-
9
CHANGES
IN
CONSUMER
NEEDS
AND
REQUIREMENTS
-
13
CHANGES
IN
THE
NETWORK
OF
RAW
MATERIALS
AND
THEIR
AVAILABILITY
-
16
TECHNOLOGICAL
AND
OPERATIONAL
CHANGES
-
18
PRODUCT-CENTERED
PROCESS
DESIGN
-
39
PRODUCT
LIFE
CYCLE
-
43
STRUCTURED
PRODUCTS
AND
FAST-MOVING
CONSUMER
GOODS
-
46
NEW
PRODUCT
DEVELOPMENT
-
48
STAGE-GATE
INNOVATION
PROCESS
-
49
MANAGEMENT
TOOLS
TO
SUPPORT
NPD
-
52
COMPETITIVE
ADVANTAGE
-
58
DESIGN
IS
NOT
A
TRIVIAL
TASK
-
60
CHALLENGES
OF
THE
FMCG
SECTOR
-
62
CHALLENGE
#1:
PRODUCT
PROFILE
IMPROVEMENT
BY
MICROSTRUCTURE
CREATION
-
64
CHALLENGE
#2:
PRODUCT
NATURALNESS
BY
MILD
PROCESSING
-
68
CHALLENGE
#3:
BENIGN
PRODUCTS
BY
IMPROVED
SUSTAINABILITY
PRACTICES
-
72
CHALLENGE
#4:
ON-SHELF
AVAILABILITY
BY
SUPPLY
CHAIN
OPTIMIZATION
-
74
A
NOVEL
APPROACH
FOR
PRODUCT
DESIGN
AND
PROCESS
SYNTHESIS
-
75
TAKE-AWAY
MESSAGE
-
76
3
A
STRUCTURED
APPROACH
FOR
PRODUCT-DRIVEN
PROCESS
DESIGN
OF
CONSUMER
PRODUCTS
-
86
3.1
3.2
INTRODUCTION
-
86
CONCEPTUAL
PROCESS
DESIGN
IN
THE
CONTEXT
OF
PROCESS
SYSTEMS
ENGINEERING
-
91
3.2.1
3.2.2
3.2.3
DEVELOPMENTS
IN
NEW
PROCESSES
AND
RETROFITS
-
92
INTERACTIONS
BETWEEN
PROCESS
DEVELOPMENT
AND
PROCESS
DESIGN
-
93
STRUCTURE
OF
THE
DESIGN
ACTIVITY
-
94
X
-
CONTENTS
3.2.4
LIFESPAN
PERFORMANCE
CRITERIA
-
95
3.3
PROCESS
SYNTHESIS
IN
THE
INDUSTRY
OF
CONSUMER
PRODUCTS
-
97
3.4
A
PRODUCT-DRIVEN
PROCESS
SYNTHESIS
APPROACH
-
99
3.4.1
GENERALITIES
-
99
3.4.2
STRUCTURE
OF
THE
METHODOLOGY
-
100
3.5
TAKE-AWAY
MESSAGE
-
108
4
FORMULATION
OF
DESIGN
PROBLEMS
AND
IDENTIFICATION
OF
CONSUMER
WANTS
-
114
4.1
INTRODUCTION
-
114
4.2
LEVEL
0:
FORMULATION
OF
THE
DESIGN
PROBLEM
-
114
4.3
LEVEL
1:
IDENTIFYING
CONSUMER
WANTS
-
118
4.3.1
THE
PERCEPTION
AND
CREATION
OF
VALUE
-
119
4.3.2
CONSUMER
FOCUS:
THE
CONSUMER
IS
KING
-
121
4.3.3
CONSUMER
WANTS
AND
NEEDS
AND
PRODUCT
SPECIFICATIONS
-
124
4.3.4
QUALITY
FUNCTION
SEPLOYMENT
-
127
4.3.5
THE
QFD
HOUSE
OF
QUALITY
-
129
4.3.6
BROC
DECISION
MAKING
METHOD
-
132
4.4
TAKE-AWAY
MESSAGE
-
136
5
PROJECT
MANAGEMENT
AND
REPORTING
-
139
5.1
PROJECT
MANAGEMENT
-
139
5.1.1
PROJECT
VERSUS
BUSINESS
AS
USUAL
-
139
5.1.2
TYPICAL
PHASES
OF
A
PROJECT
-
141
5.1.3
MANAGING
A
PROJECT
EFFECTIVELY
-
142
5.1.4
PRINCE2
METHODOLOGY
-
144
5.1.5
PRINCE2
PRINCIPLES
-
146
5.1.6
PRINCE2
THEMES
-
147
5.1.7
PRINCE2
PROCESSES
-
147
5.1.8
MAKING
A
PROJECT
SUCCESSFUL
-
148
5.2
REPORTING
-
150
5.2.1
PREPARATION
OF
WRITTEN
REPORTS
-
150
5.2.2
PREPARATION
OF
ORAL
PRESENTATIONS
-
155
5.2.3
WHAT
TO
INCLUDE
AND
WHAT
NOT
TO
INCLUDE
-
155
5.3
TAKE-AWAY
MESSAGE
-
157
6
PRODUCT
FUNCTION
AND
GENERATION
OF
IDEAS
-
158
6.1
LEVEL
2:
PRODUCT
FUNCTION
-
158
6.1.1
BUILDING
HOQ-2
-
161
6.1.2
GENERATION
OF
IDEAS
-
164
6.2
LEVEL
3:
INPUT-OUTPUT
-
170
6.2.1
ECONOMIC
EVALUATION
-
171
CONTENTS
-
XI
6.3
TAKE-AWAY
MESSAGE
-
174
7
7.1
7.2
7.3
7.3.1
7.3.2
7.3.3
7.3.4
7.3.5
7.3.6
7.4
7.5
7.6
7.7
7.8
BRAINSTORMING
TECHNIQUES
-
177
INTRODUCTION
-
177
THE
BASICS
OF
BRAINSTORMING
-
178
POPULAR
BRAINSTORMING
TECHNIQUES
-
178
MIND
MAPPING
-
178
SCAMPER
-
180
REVERSE
BRAINSTORMING
-
180
SWOT
ANALYSIS
-
181
TRIZ
-
182
OTHER
POPULAR
BRAINSTORMING
CONCEPTS
-
182
SETTING
UP
A
BRAINSTORMING
SESSION
-
182
CONDUCTING
THE
BRAINSTORMING
SESSION
-
183
EXAMPLE
OF
A
BRAINSTORMING
SESSION
-
185
TAKE-AWAY
MESSAGE
-
187
FURTHER
READING
-
187
8
8.1
8.2
8.3
NETWORK
OF
TASKS,
MECHANISMS
AND
OPERATIONAL
WINDOW
-
189
LEVEL
4:
FUNDAMENTAL
TASKS
AND
TASK
NETWORK
-
189
LEVEL
5:
MECHANISM
AND
OPERATIONAL
WINDOW
-
196
TAKE-AWAY
MESSAGE
-
205
9
9.1
9.1.1
9.1.2
9.2
EQUIPMENT
SELECTION
AND
DESIGN
-
207
LEVEL
7:
EQUIPMENT
SELECTION
AND
DESIGN
-
207
SELECTION
OF
OPERATING
UNITS
-
208
DESIGN
OF
OPERATING
UNITS
-
209
TAKE-AWAY
MESSAGE
-
251
10
10.1
10.2
10.2.1
10.2.2
10.3
MULTIPRODUCT
AND
MULTIPRODUCT-EQUIPMENT
INTEGRATION
-
255
LEVEL
6:
MULTIPRODUCT
INTEGRATION
-
255
LEVEL
8:
MULTIPRODUCT-EQUIPMENT
INTEGRATION
-
256
SUPPLY
CHAIN
MANAGEMENT
-
258
SUPPLY
CHAIN
MODELING
-
259
TAKE-AWAY
MESSAGE
-
262
11
11.1
11.2
11.3
11.4
MOLECULAR
PRODUCT
DESIGN
-
264
INTRODUCTION
AND
MOTIVATION
-
264
CAMD
METHODOLOGY
-
265
QUANTITATIVE
STRUCTURE-PROPERTY
RELATIONSHIPS
-
266
OPTIMIZATION
FORMULATIONS
FOR
CAMD
-
267
XII
-
CONTENTS
11.5
MATHEMATICAL
TECHNIQUES
FOR
THE
SOLUTION
OF
CAMD
OPTIMIZATION
PROBLEMS
-
269
11.6
EXAMPLE
-
270
11.6.1
INITIAL
STEPS
-
271
11.6.2
GENERATION
OF
QSPR
MODELS
-
272
11.6.3
PROBLEM
FORMULATION
-
273
11.6.4
EXAMPLE
RESULTS
-
275
11.7
TAKE-AWAY
MESSAGE
-
276
PART
II:
PROCESS
DESIGN
PRINCIPLES
12
PROCESS
SYNTHESIS
-
281
12.1
INTRODUCTORY
CONCEPTS
-
281
12.2
COLLECTION
OF
RELEVANT
INFORMATION
-
283
12.3
THE
HIERARCHY
OF
DECISIONS
-
286
12.4
DATA
STRUCTURES
FOR
THE
SPACE
OF
ALTERNATIVE
DESIGNS
-
291
12.5
EVALUATION
OF
ALTERNATIVE
DESIGNS
-
292
12.6
TAKE-AWAY
MESSAGE
-
294
12.7
FURTHER
READING
-
295
13
PROCESS
SIMULATION
-
296
13.1
PROCESS
SIMULATORS
-
296
13.2
MODULAR
AND
EQUATION-ORIENTED
MODES
-
296
13.3
ANALYSIS,
PROCESS
AND
SIMULATION
FLOWSHEETS
-
298
13.4
DEGREES
OF
FREEDOM
ANALYSIS
-
300
13.5
BIDIRECTIONAL
INFORMATION
AND
DESIGN
SPECS
-
300
13.6
RECYCLES
AND
TEAR
STREAMS
-
301
13.7
CONVERGENCE
ALGORITHMS
-
301
13.8
OPEN-LOOP
SIMULATION
OF
AN
AMMONIA
SYNTHESIS
PLANT
IN
UNISIM
-
303
13.8.1
BACKGROUND
-
303
13.8.2
UNISIM
DESIGN
SOLUTION
-
305
13.8.3
CREATING
A
NEW
UNIT
SET
-
306
13.8.4
BUILDING
THE
SIMULATION
-
307
13.8.5
DEFINING
REACTION
SETS
-
311
13.8.6
ENTERING
THE
SIMULATION
ENVIRONMENT
-
316
13.8.7
USING
THE
WORKBOOK
-
317
13.8.8
INSTALLING
THE
FEED
STREAMS
-
318
13.8.9
INSTALLING
UNIT
OPERATIONS
-
321
13.9
REVIEW
SIMULATION
RESULTS
-
333
13.10
SAVING
-
334
13.11
CLOSED-LOOP
SIMULATION
OF
AN
AMMONIA
SYNTHESIS
PLANT
IN
UNISIM
-
334
CONTENTS
-
-
XIII
13.11.1
13.11.2
13.12
13.12.1
13.12.2
13.12.3
13.13
13.13.1
13.13.2
13.14
REVIEW
OF
UNISIM
DESIGN
CONVERGENCE
METHODS
-
335
UNISIM
DESIGN
SOLUTION
-
337
ADD
RECYCLE
LOOP
TO
AMMONIA
SYNTHESIS
PROCESS
-
337
ADDING
A
TEE
-
337
ADDING
A
COMPRESSOR
-
338
ADDING
A
RECYCLE
-
339
OPTIMIZE
THE
PURGE
RATE
TO
DELIVER
DESIRED
PRODUCT
-
342
INSTALLING,
CONNECTING
AND
DEFINING
THE
ADJUST
-
343
ADJUSTING
THE
TARGET
VARIABLE
-
344
INVESTIGATE
THE
EFFECTS
OF
FLASH
FEED
TEMPERATURE
ON
PRODUCT
COMPOSITION
-
346
13.14.1
13.14.2
13.15
13.16
DEFINING
THE
KEY
VARIABLES
-
346
CREATING
THE
CASE
STUDY
-
349
TAKE-AWAY
MESSAGE
-
351
FURTHER
READING
-
352
14
14.1
14.2
14.2.1
14.2.2
14.2.3
14.3
14.4
14.4.1
14.4.2
14.4.3
14.4.4
14.5
14.5.1
14.5.2
14.5.3
14.6
14.6.1
14.6.2
14.7
14.7.1
14.7.2
14.8
14.9
14.10
14.11
REACTOR
DESIGN
-
353
ESSENCE
OF
REACTORS
-
353
IDEAL
REACTORS
-
353
BATCH
REACTORS
-
353
PLUG
FLOW
REACTOR
(PFR)
-
353
CONTINUOUSLY
STIRRED
TANK
REACTOR
(CSTR)
-
354
GENERAL
REACTOR
DESIGN
-
354
.
MIXING
IN
INDUSTRIAL
REACTORS
-
362
GAS
MIXING
-
362
LIQUID
MIXING
-
362
GAS-LIQUID
MIXING
-
364
SOLID-LIQUID
MIXING
-
365
TYPES
OF
REACTORS
-
366
VAPOR-LIQUID
REACTORS
-
366
CATALYTIC
PROCESSES
-
367
BIOREACTORS
-
369
HEATING
AND
COOLING
OF
REACTING
SYSTEMS
-
379
STIRRED
TANK
REACTORS
-
380
CATALYTIC
REACTORS
-
380
HEAT
EXCHANGERS
AS
REACTORS
-
381
HOMOGENEOUS
REACTIONS
-
381
HETEROGENEOUS
REACTIONS
-
381
SAFETY
CONSIDERATIONS
IN
REACTOR
DESIGN
-
382
CAPITAL
COST
OF
REACTORS
-
382
TAKE-AWAY
MESSAGE
-
383
FURTHER
READING
-
384
XIV
-
CONTENTS
15
BATCH
PROCESS
DESIGN
-
385
15.1
CONTINUOUS
VERSUS
BATCH-WISE
-
385
15.2
BATCH
SCHEDULING
-
386
15.3
BASICS
OF
BATCH
SCHEDULING
-
387
15.4
STATE-TASK
NETWORKS
-
391
15.5
MATHEMATICAL
FORMULATIONS
OF
SCHEDULING
PROBLEMS
-
392
15.6
EXAMPLE:
SCHEDULING
OF
AN
ICE
CREAM
FACTORY
-
394
15.7
IMPLEMENTATION
-
397
15.8
AIMMS
CODE
FOR
THE
SCHEDULING
MODEL
-
399
15.9
TAKE-AWAY
MESSAGE
-
402
15.10
FURTHER
READING
-
402
16
SEPARATION
TRAIN
DESIGN
-
404
16.1
SEPARATIONS
IN
PROCESS
DEVELOPMENT
-
404
16.2
ENERGY
AND
SEPARATIONS
-
404
16.3
SELECTION
OF
A
SUITABLE
SEPARATION
METHOD
-
405
16.4
THE
SEQUENCING
OF
SEPARATIONS
-
406
16.5
THE
SEQUENCING
OF
ORDINARY
DISTILLATION
COLUMNS
-
408
16.6
COMPLEX
COLUMN
CONFIGURATIONS
FOR
TERNARY
MIXTURES
-
410
16.7
ESTIMATING
THE
ANNUALIZED
COSTS
FOR
SEPARATION
SEQUENCES
-
412
16.8
DISTILLATION
COLUMN
DESIGN
WITH
A
PROCESS
SIMULATOR
-
414
16.8.1
SETTING
YOUR
SESSION
PREFERENCES
-
415
16.8.2
BUILDING
THE
SIMULATION
-
416
16.8.3
REVIEW
SIMULATION
RESULTS
-
428
16.9
TAKE-AWAY
MESSAGE
-
430
16.10
FURTHER
READING
-
430
17
PLANT-WIDE
CONTROL
-
431
17.1
PROCESS
CONTROL
-
431
17.2
INCENTIVES
FOR
PROCESS
CONTROL
-
431
17.3
IMPORTANCE
OF
MODELING
-
433
17.4
BLOCK
DIAGRAMS
-
433
17.5
CONTROL
SCHEMES
-
434
17.6
DYNAMIC
MODEL
DEVELOPMENT
AND
BEHAVIORAL
DIAGRAMS
-
435
17.7
LINEARIZATIONS
AND
LAPLACE
TRANSFORMS
-
438
17.8
BASIC
CONTROL
LOOPS
-
439
17.9
SENSORS
AND
VALVES
-
442
17.10
PROCESS
INTERLOCKS
-
443
17.11
PROCESS
CONTROL
OVER
THE
ENTIRE
PROCESS
-
444
17.12
TAKE-AWAY
MESSAGE
-
447
17.13
FURTHER
READING
-
448
CONTENTS
-
XV
18
HEAT
INTEGRATION
-
449
18.1
PINCH
ANALYSIS
-
449
18.2
MOTIVATION
FOR
HEAT
INTEGRATION
BY
PINCH
ANALYSIS
-
449
18.3
THE
PINCH
ANALYSIS
APPROACH
-
450
18.4
TAKE-AWAY
MESSAGE
-
462
18.5
FURTHER
READING
-
463
19
PROCESS
AND
PRODUCT
SAFETY
-
464
19.1
INTRODUCTION
-
464
19.2
RELEVANT
DEFINITIONS
-
464
19.3
INHERENTLY
SAFE
DESIGN
-
465
19.3.1
LEARNING
FROM
THE
PAST
-
467
19.4
HAZARDS
IN
CHEMICAL
INDUSTRY
-
469
19.5
SAFETY
OF
CONSUMER
PRODUCTS
-
471
19.5.1
MICROBIOLOGICAL
POISONING
-
472
19.5.2
FOOD
SAFETY
ACT
1990
-
476
19.5.3
MICROBIOLOGICAL
HAZARDS
-
476
19.5.4
HAZARDS
TO
PLANT
AND
PROCESSES
-
477
19.6
DESIGN
FOR
PROCESS
SAFETY
-
477
19.6.1
QRA
AND
LOPA
-
479
19.6.2
PROCESS
CONTROL
-
480
19.6.3
HAZARD
ANALYSIS
OF
CRITICAL
CONTROL
POINTS
(HACCP)
-
480
19.6.4
HYGIENE
-
481
19.6.5
ENGINEERING
FOR
FOOD
SAFETY
-
483
19.7
PROCESS
SAFETY
MANAGEMENT
FOR
PLANT
OPERATION
-
486
19.8
RISK-BASED
PROCESS
SAFETY
-
487
19.8.1
COMMITMENT
TO
PROCESS
SAFETY
-
488
19.8.2
UNDERSTAND
HAZARDS
AND
RISKS
-
490
19.8.3
RISK
MANAGEMENT
-
494
19.8.4
LEARN
FROM
EXPERIENCE
-
495
19.9
SAFETY
MODELING
APPROACHES
-
497
19.9.1
EQUIPMENT
SIZING
-
497
19.10
INDUSTRY
4.0
AND
OUTLOOK
-
502
19.11
TAKE-AWAY
MESSAGE
-
505
20
TECHNO-ECONOMICAL
EVALUATION
OF
PROJECTS
-
507
20.1
INTRODUCTION
-
507
20.2
TOTAL
CAPITAL
INVESTMENT
-
508
20.2.1
FIXED
CAPITAL
INVESTMENT
-
509
20.2.2
WORKING
CAPITAL
-
510
20.2.3
START-UP
COSTS
-
511
20.3
TOTAL
MANUFACTURING
COST
-
512
XVI
----
CONTENTS
20.3.1
PRODUCTION
COST:
DIRECT
PRODUCTION
COSTS
-
512
20.3.2
PRODUCTION
COST:
FIXED
CHARGES
-
512
20.3.3
PRODUCTION
COST:
PLANT
OVERHEAD
-
512
20.3.4
GENERAL
EXPENSES
-
514
20.4
REQUIRED
SELLING
PRICE
-
514
20.5
ESTIMATION
OF
FCI
-
514
20.5.1
FCI
BASED
ON
TURNOVER
RATIO
-
514
20.5.2
FCI
BASED
ON
INVESTMENT
PER
UNIT
OF
PRODUCTION
CAPACITY
-
515
20.5.3
FCI
BASED
ON
THE
SIX-TENTH
RULE
-
515
20.5.4
FCI
BASED
ON
STEP
COUNTING
-
515
20.5.5
FCI
BASED
ON
FACTORIAL
METHODS
-
516
20.6
ESTIMATION
OF
EQUIPMENT
COST
-
517
20.6.1
ECONOMY-OF-SCALE
EQUATION
-
517
20.6.2
EMPIRICAL
CORRELATIONS
-
518
20.6.3
COST
PER
UNIT
WEIGHT
ESTIMATION
-
519
20.7
PROJECT
FINANCIAL
ASSESSMENT
-
520
20.7.1
ECONOMIC
POTENTIAL
-
521
20.7.2
THE
GROSS
MARGIN
-
522
20.7.3
PAYBACK
PERIOD
-
522
20.7.4
RETURN
ON
INVESTMENT
-
523
20.7.5
DISCOUNTED
CASH
FLOW
ANALYSIS
-
523
20.8
MARKET
EFFECTS
-
525
20.9
COMPUTER
TOOLS
FOR
COST
ESTIMATING
-
526
20.10
TAKE-AWAY
MESSAGE
-
527
21
DESIGN
FOR
SUSTAINABILITY
-
529
21.1
TAKING
THE
LONG-TERM
VIEW
-
529
21.2
METRICS
FOR
SUSTAINABILITY
-
530
21.3
INCLUDING
SUSTAINABILITY
METRICS
WITHIN
THE
DESIGN
PROCESS
-
534
21.4
RETROFIT
FOR
IMPROVED
SUSTAINABILITY
-
535
21.5
TAKE-AWAY
MESSAGE
-
537
21.6
FURTHER
READING
-
537
22
OPTIMIZATION
-
539
22.1
CLASSIFICATION
OF
OPTIMIZATION
PROBLEMS
-
539
22.2
OBJECTIVES
AND
CONSTRAINTS
-
540
22.3
SPECIFIC
FORMULATIONS
FOR
PROCESS
DESIGN
AND
OPERATIONS
-
542
22.4
SOLUTION
ALGORITHMS
FOR
OPTIMIZATION
PROBLEMS
-
544
22.5
TAKE-AWAY
MESSAGE
-
548
22.6
FURTHER
READING
-
550
CONTENTS
-
XVII
INDEX
-
569
23
23.1
23.2
23.3
23.4
23.5
23.6
23.6.1
23.6.2
23.6.3
23.6.4
23.7
23.8
ENTERPRISE-WIDE
OPTIMIZATION
-
551
WHAT
IS
ENTERPRISE-WIDE
OPTIMIZATION?
-
551
FAST-MOVING
CONSUMER
GOOD
SUPPLY
CHAINS
-
551
SCHEDULING
-
552
PLANNING
-
554
MIXED-INTEGER
PROGRAMMING
-
554
OPTIMIZATION
CHALLENGES
-
558
THE
CHALLENGE
OF
FLEXIBILITY
-
559
THE
CHALLENGE
OF
SUSTAINABILITY
-
559
THE
CHALLENGE
OF
COMPLEXITY
-
562
PERSPECTIVES
-
562
TAKE-AWAY
MESSAGE
-
564
FURTHER
READING
-
564
A
APPENDIX
-
565 |
| adam_txt |
CONTENTS
FOREWORD
-
VII
PART
I:
PRODUCT-CENTRED
DESIGN
1
1.1
1.2
1.3
INTRODUCTION
-
3
THE
CURRENT
SETTING
OF
THE
PROCESS
INDUSTRY
-
3
THE
DEVELOPMENT
OF
THE
PDPS
APPROACH
-
4
STRUCTURE
OF
THE
BOOK
-
5
2
2.1
2.1.1
2.1.2
2.1.3
2.1.4
2.2
2.2.1
2.2.2
2.3
2.3.1
2.3.2
2.3.3
2.4
2.5
2.5.1
2.5.2
2.5.3
2.5.4
2.6
2.7
PERFORMANCE
PRODUCTS
IN
A
CHALLENGING
ENVIRONMENT
-
9
A
CHALLENGING
ENVIRONMENT
FOR
THE
PROCESS
INDUSTRY
-
9
ENVIRONMENTAL
AND
ENERGY
CHALLENGES
-
9
CHANGES
IN
CONSUMER
NEEDS
AND
REQUIREMENTS
-
13
CHANGES
IN
THE
NETWORK
OF
RAW
MATERIALS
AND
THEIR
AVAILABILITY
-
16
TECHNOLOGICAL
AND
OPERATIONAL
CHANGES
-
18
PRODUCT-CENTERED
PROCESS
DESIGN
-
39
PRODUCT
LIFE
CYCLE
-
43
STRUCTURED
PRODUCTS
AND
FAST-MOVING
CONSUMER
GOODS
-
46
NEW
PRODUCT
DEVELOPMENT
-
48
STAGE-GATE
INNOVATION
PROCESS
-
49
MANAGEMENT
TOOLS
TO
SUPPORT
NPD
-
52
COMPETITIVE
ADVANTAGE
-
58
DESIGN
IS
NOT
A
TRIVIAL
TASK
-
60
CHALLENGES
OF
THE
FMCG
SECTOR
-
62
CHALLENGE
#1:
PRODUCT
PROFILE
IMPROVEMENT
BY
MICROSTRUCTURE
CREATION
-
64
CHALLENGE
#2:
PRODUCT
NATURALNESS
BY
MILD
PROCESSING
-
68
CHALLENGE
#3:
BENIGN
PRODUCTS
BY
IMPROVED
SUSTAINABILITY
PRACTICES
-
72
CHALLENGE
#4:
ON-SHELF
AVAILABILITY
BY
SUPPLY
CHAIN
OPTIMIZATION
-
74
A
NOVEL
APPROACH
FOR
PRODUCT
DESIGN
AND
PROCESS
SYNTHESIS
-
75
TAKE-AWAY
MESSAGE
-
76
3
A
STRUCTURED
APPROACH
FOR
PRODUCT-DRIVEN
PROCESS
DESIGN
OF
CONSUMER
PRODUCTS
-
86
3.1
3.2
INTRODUCTION
-
86
CONCEPTUAL
PROCESS
DESIGN
IN
THE
CONTEXT
OF
PROCESS
SYSTEMS
ENGINEERING
-
91
3.2.1
3.2.2
3.2.3
DEVELOPMENTS
IN
NEW
PROCESSES
AND
RETROFITS
-
92
INTERACTIONS
BETWEEN
PROCESS
DEVELOPMENT
AND
PROCESS
DESIGN
-
93
STRUCTURE
OF
THE
DESIGN
ACTIVITY
-
94
X
-
CONTENTS
3.2.4
LIFESPAN
PERFORMANCE
CRITERIA
-
95
3.3
PROCESS
SYNTHESIS
IN
THE
INDUSTRY
OF
CONSUMER
PRODUCTS
-
97
3.4
A
PRODUCT-DRIVEN
PROCESS
SYNTHESIS
APPROACH
-
99
3.4.1
GENERALITIES
-
99
3.4.2
STRUCTURE
OF
THE
METHODOLOGY
-
100
3.5
TAKE-AWAY
MESSAGE
-
108
4
FORMULATION
OF
DESIGN
PROBLEMS
AND
IDENTIFICATION
OF
CONSUMER
WANTS
-
114
4.1
INTRODUCTION
-
114
4.2
LEVEL
0:
FORMULATION
OF
THE
DESIGN
PROBLEM
-
114
4.3
LEVEL
1:
IDENTIFYING
CONSUMER
WANTS
-
118
4.3.1
THE
PERCEPTION
AND
CREATION
OF
VALUE
-
119
4.3.2
CONSUMER
FOCUS:
THE
CONSUMER
IS
KING
-
121
4.3.3
CONSUMER
WANTS
AND
NEEDS
AND
PRODUCT
SPECIFICATIONS
-
124
4.3.4
QUALITY
FUNCTION
SEPLOYMENT
-
127
4.3.5
THE
QFD
HOUSE
OF
QUALITY
-
129
4.3.6
BROC
DECISION
MAKING
METHOD
-
132
4.4
TAKE-AWAY
MESSAGE
-
136
5
PROJECT
MANAGEMENT
AND
REPORTING
-
139
5.1
PROJECT
MANAGEMENT
-
139
5.1.1
PROJECT
VERSUS
BUSINESS
AS
USUAL
-
139
5.1.2
TYPICAL
PHASES
OF
A
PROJECT
-
141
5.1.3
MANAGING
A
PROJECT
EFFECTIVELY
-
142
5.1.4
PRINCE2
METHODOLOGY
-
144
5.1.5
PRINCE2
PRINCIPLES
-
146
5.1.6
PRINCE2
THEMES
-
147
5.1.7
PRINCE2
PROCESSES
-
147
5.1.8
MAKING
A
PROJECT
SUCCESSFUL
-
148
5.2
REPORTING
-
150
5.2.1
PREPARATION
OF
WRITTEN
REPORTS
-
150
5.2.2
PREPARATION
OF
ORAL
PRESENTATIONS
-
155
5.2.3
WHAT
TO
INCLUDE
AND
WHAT
NOT
TO
INCLUDE
-
155
5.3
TAKE-AWAY
MESSAGE
-
157
6
PRODUCT
FUNCTION
AND
GENERATION
OF
IDEAS
-
158
6.1
LEVEL
2:
PRODUCT
FUNCTION
-
158
6.1.1
BUILDING
HOQ-2
-
161
6.1.2
GENERATION
OF
IDEAS
-
164
6.2
LEVEL
3:
INPUT-OUTPUT
-
170
6.2.1
ECONOMIC
EVALUATION
-
171
CONTENTS
-
XI
6.3
TAKE-AWAY
MESSAGE
-
174
7
7.1
7.2
7.3
7.3.1
7.3.2
7.3.3
7.3.4
7.3.5
7.3.6
7.4
7.5
7.6
7.7
7.8
BRAINSTORMING
TECHNIQUES
-
177
INTRODUCTION
-
177
THE
BASICS
OF
BRAINSTORMING
-
178
POPULAR
BRAINSTORMING
TECHNIQUES
-
178
MIND
MAPPING
-
178
SCAMPER
-
180
REVERSE
BRAINSTORMING
-
180
SWOT
ANALYSIS
-
181
TRIZ
-
182
OTHER
POPULAR
BRAINSTORMING
CONCEPTS
-
182
SETTING
UP
A
BRAINSTORMING
SESSION
-
182
CONDUCTING
THE
BRAINSTORMING
SESSION
-
183
EXAMPLE
OF
A
BRAINSTORMING
SESSION
-
185
TAKE-AWAY
MESSAGE
-
187
FURTHER
READING
-
187
8
8.1
8.2
8.3
NETWORK
OF
TASKS,
MECHANISMS
AND
OPERATIONAL
WINDOW
-
189
LEVEL
4:
FUNDAMENTAL
TASKS
AND
TASK
NETWORK
-
189
LEVEL
5:
MECHANISM
AND
OPERATIONAL
WINDOW
-
196
TAKE-AWAY
MESSAGE
-
205
9
9.1
9.1.1
9.1.2
9.2
EQUIPMENT
SELECTION
AND
DESIGN
-
207
LEVEL
7:
EQUIPMENT
SELECTION
AND
DESIGN
-
207
SELECTION
OF
OPERATING
UNITS
-
208
DESIGN
OF
OPERATING
UNITS
-
209
TAKE-AWAY
MESSAGE
-
251
10
10.1
10.2
10.2.1
10.2.2
10.3
MULTIPRODUCT
AND
MULTIPRODUCT-EQUIPMENT
INTEGRATION
-
255
LEVEL
6:
MULTIPRODUCT
INTEGRATION
-
255
LEVEL
8:
MULTIPRODUCT-EQUIPMENT
INTEGRATION
-
256
SUPPLY
CHAIN
MANAGEMENT
-
258
SUPPLY
CHAIN
MODELING
-
259
TAKE-AWAY
MESSAGE
-
262
11
11.1
11.2
11.3
11.4
MOLECULAR
PRODUCT
DESIGN
-
264
INTRODUCTION
AND
MOTIVATION
-
264
CAMD
METHODOLOGY
-
265
QUANTITATIVE
STRUCTURE-PROPERTY
RELATIONSHIPS
-
266
OPTIMIZATION
FORMULATIONS
FOR
CAMD
-
267
XII
-
CONTENTS
11.5
MATHEMATICAL
TECHNIQUES
FOR
THE
SOLUTION
OF
CAMD
OPTIMIZATION
PROBLEMS
-
269
11.6
EXAMPLE
-
270
11.6.1
INITIAL
STEPS
-
271
11.6.2
GENERATION
OF
QSPR
MODELS
-
272
11.6.3
PROBLEM
FORMULATION
-
273
11.6.4
EXAMPLE
RESULTS
-
275
11.7
TAKE-AWAY
MESSAGE
-
276
PART
II:
PROCESS
DESIGN
PRINCIPLES
12
PROCESS
SYNTHESIS
-
281
12.1
INTRODUCTORY
CONCEPTS
-
281
12.2
COLLECTION
OF
RELEVANT
INFORMATION
-
283
12.3
THE
HIERARCHY
OF
DECISIONS
-
286
12.4
DATA
STRUCTURES
FOR
THE
SPACE
OF
ALTERNATIVE
DESIGNS
-
291
12.5
EVALUATION
OF
ALTERNATIVE
DESIGNS
-
292
12.6
TAKE-AWAY
MESSAGE
-
294
12.7
FURTHER
READING
-
295
13
PROCESS
SIMULATION
-
296
13.1
PROCESS
SIMULATORS
-
296
13.2
MODULAR
AND
EQUATION-ORIENTED
MODES
-
296
13.3
ANALYSIS,
PROCESS
AND
SIMULATION
FLOWSHEETS
-
298
13.4
DEGREES
OF
FREEDOM
ANALYSIS
-
300
13.5
BIDIRECTIONAL
INFORMATION
AND
DESIGN
SPECS
-
300
13.6
RECYCLES
AND
TEAR
STREAMS
-
301
13.7
CONVERGENCE
ALGORITHMS
-
301
13.8
OPEN-LOOP
SIMULATION
OF
AN
AMMONIA
SYNTHESIS
PLANT
IN
UNISIM
-
303
13.8.1
BACKGROUND
-
303
13.8.2
UNISIM
DESIGN
SOLUTION
-
305
13.8.3
CREATING
A
NEW
UNIT
SET
-
306
13.8.4
BUILDING
THE
SIMULATION
-
307
13.8.5
DEFINING
REACTION
SETS
-
311
13.8.6
ENTERING
THE
SIMULATION
ENVIRONMENT
-
316
13.8.7
USING
THE
WORKBOOK
-
317
13.8.8
INSTALLING
THE
FEED
STREAMS
-
318
13.8.9
INSTALLING
UNIT
OPERATIONS
-
321
13.9
REVIEW
SIMULATION
RESULTS
-
333
13.10
SAVING
-
334
13.11
CLOSED-LOOP
SIMULATION
OF
AN
AMMONIA
SYNTHESIS
PLANT
IN
UNISIM
-
334
CONTENTS
-
-
XIII
13.11.1
13.11.2
13.12
13.12.1
13.12.2
13.12.3
13.13
13.13.1
13.13.2
13.14
REVIEW
OF
UNISIM
DESIGN
CONVERGENCE
METHODS
-
335
UNISIM
DESIGN
SOLUTION
-
337
ADD
RECYCLE
LOOP
TO
AMMONIA
SYNTHESIS
PROCESS
-
337
ADDING
A
TEE
-
337
ADDING
A
COMPRESSOR
-
338
ADDING
A
RECYCLE
-
339
OPTIMIZE
THE
PURGE
RATE
TO
DELIVER
DESIRED
PRODUCT
-
342
INSTALLING,
CONNECTING
AND
DEFINING
THE
ADJUST
-
343
ADJUSTING
THE
TARGET
VARIABLE
-
344
INVESTIGATE
THE
EFFECTS
OF
FLASH
FEED
TEMPERATURE
ON
PRODUCT
COMPOSITION
-
346
13.14.1
13.14.2
13.15
13.16
DEFINING
THE
KEY
VARIABLES
-
346
CREATING
THE
CASE
STUDY
-
349
TAKE-AWAY
MESSAGE
-
351
FURTHER
READING
-
352
14
14.1
14.2
14.2.1
14.2.2
14.2.3
14.3
14.4
14.4.1
14.4.2
14.4.3
14.4.4
14.5
14.5.1
14.5.2
14.5.3
14.6
14.6.1
14.6.2
14.7
14.7.1
14.7.2
14.8
14.9
14.10
14.11
REACTOR
DESIGN
-
353
ESSENCE
OF
REACTORS
-
353
IDEAL
REACTORS
-
353
BATCH
REACTORS
-
353
PLUG
FLOW
REACTOR
(PFR)
-
353
CONTINUOUSLY
STIRRED
TANK
REACTOR
(CSTR)
-
354
GENERAL
REACTOR
DESIGN
-
354
.
MIXING
IN
INDUSTRIAL
REACTORS
-
362
GAS
MIXING
-
362
LIQUID
MIXING
-
362
GAS-LIQUID
MIXING
-
364
SOLID-LIQUID
MIXING
-
365
TYPES
OF
REACTORS
-
366
VAPOR-LIQUID
REACTORS
-
366
CATALYTIC
PROCESSES
-
367
BIOREACTORS
-
369
HEATING
AND
COOLING
OF
REACTING
SYSTEMS
-
379
STIRRED
TANK
REACTORS
-
380
CATALYTIC
REACTORS
-
380
HEAT
EXCHANGERS
AS
REACTORS
-
381
HOMOGENEOUS
REACTIONS
-
381
HETEROGENEOUS
REACTIONS
-
381
SAFETY
CONSIDERATIONS
IN
REACTOR
DESIGN
-
382
CAPITAL
COST
OF
REACTORS
-
382
TAKE-AWAY
MESSAGE
-
383
FURTHER
READING
-
384
XIV
-
CONTENTS
15
BATCH
PROCESS
DESIGN
-
385
15.1
CONTINUOUS
VERSUS
BATCH-WISE
-
385
15.2
BATCH
SCHEDULING
-
386
15.3
BASICS
OF
BATCH
SCHEDULING
-
387
15.4
STATE-TASK
NETWORKS
-
391
15.5
MATHEMATICAL
FORMULATIONS
OF
SCHEDULING
PROBLEMS
-
392
15.6
EXAMPLE:
SCHEDULING
OF
AN
ICE
CREAM
FACTORY
-
394
15.7
IMPLEMENTATION
-
397
15.8
AIMMS
CODE
FOR
THE
SCHEDULING
MODEL
-
399
15.9
TAKE-AWAY
MESSAGE
-
402
15.10
FURTHER
READING
-
402
16
SEPARATION
TRAIN
DESIGN
-
404
16.1
SEPARATIONS
IN
PROCESS
DEVELOPMENT
-
404
16.2
ENERGY
AND
SEPARATIONS
-
404
16.3
SELECTION
OF
A
SUITABLE
SEPARATION
METHOD
-
405
16.4
THE
SEQUENCING
OF
SEPARATIONS
-
406
16.5
THE
SEQUENCING
OF
ORDINARY
DISTILLATION
COLUMNS
-
408
16.6
COMPLEX
COLUMN
CONFIGURATIONS
FOR
TERNARY
MIXTURES
-
410
16.7
ESTIMATING
THE
ANNUALIZED
COSTS
FOR
SEPARATION
SEQUENCES
-
412
16.8
DISTILLATION
COLUMN
DESIGN
WITH
A
PROCESS
SIMULATOR
-
414
16.8.1
SETTING
YOUR
SESSION
PREFERENCES
-
415
16.8.2
BUILDING
THE
SIMULATION
-
416
16.8.3
REVIEW
SIMULATION
RESULTS
-
428
16.9
TAKE-AWAY
MESSAGE
-
430
16.10
FURTHER
READING
-
430
17
PLANT-WIDE
CONTROL
-
431
17.1
PROCESS
CONTROL
-
431
17.2
INCENTIVES
FOR
PROCESS
CONTROL
-
431
17.3
IMPORTANCE
OF
MODELING
-
433
17.4
BLOCK
DIAGRAMS
-
433
17.5
CONTROL
SCHEMES
-
434
17.6
DYNAMIC
MODEL
DEVELOPMENT
AND
BEHAVIORAL
DIAGRAMS
-
435
17.7
LINEARIZATIONS
AND
LAPLACE
TRANSFORMS
-
438
17.8
BASIC
CONTROL
LOOPS
-
439
17.9
SENSORS
AND
VALVES
-
442
17.10
PROCESS
INTERLOCKS
-
443
17.11
PROCESS
CONTROL
OVER
THE
ENTIRE
PROCESS
-
444
17.12
TAKE-AWAY
MESSAGE
-
447
17.13
FURTHER
READING
-
448
CONTENTS
-
XV
18
HEAT
INTEGRATION
-
449
18.1
PINCH
ANALYSIS
-
449
18.2
MOTIVATION
FOR
HEAT
INTEGRATION
BY
PINCH
ANALYSIS
-
449
18.3
THE
PINCH
ANALYSIS
APPROACH
-
450
18.4
TAKE-AWAY
MESSAGE
-
462
18.5
FURTHER
READING
-
463
19
PROCESS
AND
PRODUCT
SAFETY
-
464
19.1
INTRODUCTION
-
464
19.2
RELEVANT
DEFINITIONS
-
464
19.3
INHERENTLY
SAFE
DESIGN
-
465
19.3.1
LEARNING
FROM
THE
PAST
-
467
19.4
HAZARDS
IN
CHEMICAL
INDUSTRY
-
469
19.5
SAFETY
OF
CONSUMER
PRODUCTS
-
471
19.5.1
MICROBIOLOGICAL
POISONING
-
472
19.5.2
FOOD
SAFETY
ACT
1990
-
476
19.5.3
MICROBIOLOGICAL
HAZARDS
-
476
19.5.4
HAZARDS
TO
PLANT
AND
PROCESSES
-
477
19.6
DESIGN
FOR
PROCESS
SAFETY
-
477
19.6.1
QRA
AND
LOPA
-
479
19.6.2
PROCESS
CONTROL
-
480
19.6.3
HAZARD
ANALYSIS
OF
CRITICAL
CONTROL
POINTS
(HACCP)
-
480
19.6.4
HYGIENE
-
481
19.6.5
ENGINEERING
FOR
FOOD
SAFETY
-
483
19.7
PROCESS
SAFETY
MANAGEMENT
FOR
PLANT
OPERATION
-
486
19.8
RISK-BASED
PROCESS
SAFETY
-
487
19.8.1
COMMITMENT
TO
PROCESS
SAFETY
-
488
19.8.2
UNDERSTAND
HAZARDS
AND
RISKS
-
490
19.8.3
RISK
MANAGEMENT
-
494
19.8.4
LEARN
FROM
EXPERIENCE
-
495
19.9
SAFETY
MODELING
APPROACHES
-
497
19.9.1
EQUIPMENT
SIZING
-
497
19.10
INDUSTRY
4.0
AND
OUTLOOK
-
502
19.11
TAKE-AWAY
MESSAGE
-
505
20
TECHNO-ECONOMICAL
EVALUATION
OF
PROJECTS
-
507
20.1
INTRODUCTION
-
507
20.2
TOTAL
CAPITAL
INVESTMENT
-
508
20.2.1
FIXED
CAPITAL
INVESTMENT
-
509
20.2.2
WORKING
CAPITAL
-
510
20.2.3
START-UP
COSTS
-
511
20.3
TOTAL
MANUFACTURING
COST
-
512
XVI
----
CONTENTS
20.3.1
PRODUCTION
COST:
DIRECT
PRODUCTION
COSTS
-
512
20.3.2
PRODUCTION
COST:
FIXED
CHARGES
-
512
20.3.3
PRODUCTION
COST:
PLANT
OVERHEAD
-
512
20.3.4
GENERAL
EXPENSES
-
514
20.4
REQUIRED
SELLING
PRICE
-
514
20.5
ESTIMATION
OF
FCI
-
514
20.5.1
FCI
BASED
ON
TURNOVER
RATIO
-
514
20.5.2
FCI
BASED
ON
INVESTMENT
PER
UNIT
OF
PRODUCTION
CAPACITY
-
515
20.5.3
FCI
BASED
ON
THE
SIX-TENTH
RULE
-
515
20.5.4
FCI
BASED
ON
STEP
COUNTING
-
515
20.5.5
FCI
BASED
ON
FACTORIAL
METHODS
-
516
20.6
ESTIMATION
OF
EQUIPMENT
COST
-
517
20.6.1
ECONOMY-OF-SCALE
EQUATION
-
517
20.6.2
EMPIRICAL
CORRELATIONS
-
518
20.6.3
COST
PER
UNIT
WEIGHT
ESTIMATION
-
519
20.7
PROJECT
FINANCIAL
ASSESSMENT
-
520
20.7.1
ECONOMIC
POTENTIAL
-
521
20.7.2
THE
GROSS
MARGIN
-
522
20.7.3
PAYBACK
PERIOD
-
522
20.7.4
RETURN
ON
INVESTMENT
-
523
20.7.5
DISCOUNTED
CASH
FLOW
ANALYSIS
-
523
20.8
MARKET
EFFECTS
-
525
20.9
COMPUTER
TOOLS
FOR
COST
ESTIMATING
-
526
20.10
TAKE-AWAY
MESSAGE
-
527
21
DESIGN
FOR
SUSTAINABILITY
-
529
21.1
TAKING
THE
LONG-TERM
VIEW
-
529
21.2
METRICS
FOR
SUSTAINABILITY
-
530
21.3
INCLUDING
SUSTAINABILITY
METRICS
WITHIN
THE
DESIGN
PROCESS
-
534
21.4
RETROFIT
FOR
IMPROVED
SUSTAINABILITY
-
535
21.5
TAKE-AWAY
MESSAGE
-
537
21.6
FURTHER
READING
-
537
22
OPTIMIZATION
-
539
22.1
CLASSIFICATION
OF
OPTIMIZATION
PROBLEMS
-
539
22.2
OBJECTIVES
AND
CONSTRAINTS
-
540
22.3
SPECIFIC
FORMULATIONS
FOR
PROCESS
DESIGN
AND
OPERATIONS
-
542
22.4
SOLUTION
ALGORITHMS
FOR
OPTIMIZATION
PROBLEMS
-
544
22.5
TAKE-AWAY
MESSAGE
-
548
22.6
FURTHER
READING
-
550
CONTENTS
-
XVII
INDEX
-
569
23
23.1
23.2
23.3
23.4
23.5
23.6
23.6.1
23.6.2
23.6.3
23.6.4
23.7
23.8
ENTERPRISE-WIDE
OPTIMIZATION
-
551
WHAT
IS
ENTERPRISE-WIDE
OPTIMIZATION?
-
551
FAST-MOVING
CONSUMER
GOOD
SUPPLY
CHAINS
-
551
SCHEDULING
-
552
PLANNING
-
554
MIXED-INTEGER
PROGRAMMING
-
554
OPTIMIZATION
CHALLENGES
-
558
THE
CHALLENGE
OF
FLEXIBILITY
-
559
THE
CHALLENGE
OF
SUSTAINABILITY
-
559
THE
CHALLENGE
OF
COMPLEXITY
-
562
PERSPECTIVES
-
562
TAKE-AWAY
MESSAGE
-
564
FURTHER
READING
-
564
A
APPENDIX
-
565 |
| any_adam_object | 1 |
| any_adam_object_boolean | 1 |
| author | Zondervan, Edwin Almeida-Rivera, Cristhian Camarda, Kyle Vincent |
| author_GND | (DE-588)1205470999 (DE-588)1205471235 (DE-588)1205471332 |
| author_facet | Zondervan, Edwin Almeida-Rivera, Cristhian Camarda, Kyle Vincent |
| author_role | aut aut aut |
| author_sort | Zondervan, Edwin |
| author_variant | e z ez c a r car k v c kv kvc |
| building | Verbundindex |
| bvnumber | BV049434197 |
| classification_rvk | VC 6450 VN 7000 QR 525 |
| ctrlnum | (OCoLC)1378740288 (DE-599)DNB1287957870 |
| dewey-full | 660.28 |
| dewey-hundreds | 600 - Technology (Applied sciences) |
| dewey-ones | 660 - Chemical engineering |
| dewey-raw | 660.28 |
| dewey-search | 660.28 |
| dewey-sort | 3660.28 |
| dewey-tens | 660 - Chemical engineering |
| discipline | Chemie / Pharmazie Wirtschaftswissenschaften |
| discipline_str_mv | Chemie / Pharmazie Wirtschaftswissenschaften |
| edition | 2nd edition |
| format | Book |
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| id | DE-604.BV049434197 |
| illustrated | Illustrated |
| index_date | 2024-07-03T23:10:45Z |
| indexdate | 2024-08-10T01:07:02Z |
| institution | BVB |
| institution_GND | (DE-588)10095502-2 |
| isbn | 9783111014906 3111014908 |
| language | English |
| oai_aleph_id | oai:aleph.bib-bvb.de:BVB01-034780272 |
| oclc_num | 1378740288 |
| open_access_boolean | |
| owner | DE-860 DE-N2 |
| owner_facet | DE-860 DE-N2 |
| physical | XVII, 576 Seiten Illustrationen, Diagramme 24 cm, 983 g |
| publishDate | 2023 |
| publishDateSearch | 2023 |
| publishDateSort | 2023 |
| publisher | De Gruyter |
| record_format | marc |
| series2 | De Gruyter graduate |
| spelling | Zondervan, Edwin Verfasser (DE-588)1205470999 aut Product-driven process design from molecule to enterprise Edwin Zondervan, Cristhian Almeida-Rivera, and Kyle Vincent Camarda 2nd edition Berlin De Gruyter [2023] © 2023 XVII, 576 Seiten Illustrationen, Diagramme 24 cm, 983 g txt rdacontent n rdamedia nc rdacarrier De Gruyter graduate Bemessung (DE-588)4005461-5 gnd rswk-swf Chemische Verfahrenstechnik (DE-588)4069941-9 gnd rswk-swf Spezialchemikalie (DE-588)1112625623 gnd rswk-swf Arzneimittel (DE-588)4003115-9 gnd rswk-swf Herstellung (DE-588)4159653-5 gnd rswk-swf Prozessentwicklung Technik (DE-588)4278925-4 gnd rswk-swf Chemieanlage (DE-588)4121084-0 gnd rswk-swf Produktentwicklung (DE-588)4139402-1 gnd rswk-swf Produktdesign Produktentwicklung Technische Chemie Verfahrenstechnik Research and Development Product Technology Process Engineering Chemical Engineering Industrial Chemistry TB: Textbook Produktdesign; Produktentwicklung; Technische Chemie; Verfahrenstechnik; Research and Development Product Technology; Process Engineering; Chemical Engineering; Industrial Chemistry Spezialchemikalie (DE-588)1112625623 s Arzneimittel (DE-588)4003115-9 s Produktentwicklung (DE-588)4139402-1 s Herstellung (DE-588)4159653-5 s Chemische Verfahrenstechnik (DE-588)4069941-9 s Prozessentwicklung Technik (DE-588)4278925-4 s Chemieanlage (DE-588)4121084-0 s Bemessung (DE-588)4005461-5 s DE-604 Almeida-Rivera, Cristhian Verfasser (DE-588)1205471235 aut Camarda, Kyle Vincent Verfasser (DE-588)1205471332 aut Walter de Gruyter GmbH & Co. KG (DE-588)10095502-2 pbl Erscheint auch als Online-Ausgabe, ePub 9783111015699 (DE-604)BV049469248 Erscheint auch als Online-Ausgabe, ePDF Zondervan, Edwin Product-Driven Process Design 2nd, Revised and Extended Edition Berlin/Boston : De Gruyter, 2023 1 Online-Ressource, (XVII, 576 Seiten) : Illustrationen, Diagramme 978-3-11-101495-1 (DE-604)BV049469248 X:MVB https://www.degruyter.com/isbn/9783111014906 B:DE-101 application/pdf https://d-nb.info/1287957870/04 Inhaltsverzeichnis DNB Datenaustausch application/pdf http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=034780272&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA Inhaltsverzeichnis 1\p dnb 20231117 DE-101 https://d-nb.info/provenance/plan#dnb 2\p dnb 20231117 DE-101 https://d-nb.info/provenance/plan#dnb |
| spellingShingle | Zondervan, Edwin Almeida-Rivera, Cristhian Camarda, Kyle Vincent Product-driven process design from molecule to enterprise Bemessung (DE-588)4005461-5 gnd Chemische Verfahrenstechnik (DE-588)4069941-9 gnd Spezialchemikalie (DE-588)1112625623 gnd Arzneimittel (DE-588)4003115-9 gnd Herstellung (DE-588)4159653-5 gnd Prozessentwicklung Technik (DE-588)4278925-4 gnd Chemieanlage (DE-588)4121084-0 gnd Produktentwicklung (DE-588)4139402-1 gnd |
| subject_GND | (DE-588)4005461-5 (DE-588)4069941-9 (DE-588)1112625623 (DE-588)4003115-9 (DE-588)4159653-5 (DE-588)4278925-4 (DE-588)4121084-0 (DE-588)4139402-1 |
| title | Product-driven process design from molecule to enterprise |
| title_auth | Product-driven process design from molecule to enterprise |
| title_exact_search | Product-driven process design from molecule to enterprise |
| title_exact_search_txtP | Product-driven process design from molecule to enterprise |
| title_full | Product-driven process design from molecule to enterprise Edwin Zondervan, Cristhian Almeida-Rivera, and Kyle Vincent Camarda |
| title_fullStr | Product-driven process design from molecule to enterprise Edwin Zondervan, Cristhian Almeida-Rivera, and Kyle Vincent Camarda |
| title_full_unstemmed | Product-driven process design from molecule to enterprise Edwin Zondervan, Cristhian Almeida-Rivera, and Kyle Vincent Camarda |
| title_short | Product-driven process design |
| title_sort | product driven process design from molecule to enterprise |
| title_sub | from molecule to enterprise |
| topic | Bemessung (DE-588)4005461-5 gnd Chemische Verfahrenstechnik (DE-588)4069941-9 gnd Spezialchemikalie (DE-588)1112625623 gnd Arzneimittel (DE-588)4003115-9 gnd Herstellung (DE-588)4159653-5 gnd Prozessentwicklung Technik (DE-588)4278925-4 gnd Chemieanlage (DE-588)4121084-0 gnd Produktentwicklung (DE-588)4139402-1 gnd |
| topic_facet | Bemessung Chemische Verfahrenstechnik Spezialchemikalie Arzneimittel Herstellung Prozessentwicklung Technik Chemieanlage Produktentwicklung |
| url | https://www.degruyter.com/isbn/9783111014906 https://d-nb.info/1287957870/04 http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=034780272&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA |
| work_keys_str_mv | AT zondervanedwin productdrivenprocessdesignfrommoleculetoenterprise AT almeidariveracristhian productdrivenprocessdesignfrommoleculetoenterprise AT camardakylevincent productdrivenprocessdesignfrommoleculetoenterprise AT walterdegruytergmbhcokg productdrivenprocessdesignfrommoleculetoenterprise |
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