Verfügbarkeit: Tubular heat exchangers

Tubular heat exchangers: for chemical engineers

Gespeichert in:

Bibliographische Detailangaben
1. Verfasser:	Cartaxo, Samuel Jorge Marques (VerfasserIn)
Format:	Buch
Sprache:	English
Veröffentlicht:	Berlin ; Boston De Gruyter 2022
Schriftenreihe:	De Gruyter graduate
Schlagworte:	Rohrwärmeaustauscher TB: Textbook Technische Chemie Wärmeaustauscher Wärmetechnik Wärmeübertrager
Online-Zugang:	https://www.degruyter.com/isbn/9783110585735 Inhaltsverzeichnis
Beschreibung:	XXVI, 337 Seiten Illustrationen, Diagramme 24 cm x 17 cm
ISBN:	3110585731 9783110585735

Internformat

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Datensatz im Suchindex

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adam_text	CONTENTS ACKNOWLEDGMENTS - VII DISCLAIMER ---- IX PREFACE - XI CONVERSION FACTORS - XIX PHYSICAL CONSTANTS - XXI NOMENCLATURE ---- XXIII 1 1.1 1.1.1 1.1.2 1.1.3 1.1.4 1.2 1.3 1.3.1 1.3.2 1.3.3 AN OVERVIEW OF THE EQUIPMENT - 1 PROCESS APPLICABILITY ---- 2 TYPES OF HAIRPINS - 3 PRIMARY CONCERNS ---- 5 WHERE TO USE A DOUBLE-PIPE EXCHANGER? - 5 ABOUT THE OPTIMAL DESIGN ---- 7 THE DOUBLE-PIPE EXCHANGER IS ACTUALLY A HAIRPIN! - 10 PIPES AND TUBES ---- 13 IS THERE A DIFFERENCE? ---- 13 PRACTICAL IMPLICATIONS OF PIPE AND TUBE DISTINCTION - 14 COMMERCIAL DIAMETERS AND LENGTHS - 14 2 2.1 2.2 2.3 2.3.1 2.3.2 2.3.3 2.4 2.4.1 2.4.2 2.5 2.5.1 2.5.2 2.5.3 2.5.4 2.5.5 HEAT EXCHANGER DESIGN EQUATIONS - 17 HEAT LOAD - 17 THE DESIGN EQUATION ---- 20 THE OVERALL HEAT TRANSFER COEFFICIENT - 21 DESIGN AND CLEAN OVERALL HEAT TRANSFER COEFFICIENTS - 24 RELATIVELY SMALL WALL THERMAL RESISTANCE - 25 CONTROLLING FLUID ---- 25 BASIC HEAT EXCHANGER DIFFERENTIAL EQUATIONS - 28 PARALLEL FLOW ---- 29 COUNTERFLOW ---- 31 LOG MEAN TEMPERATURE DIFFERENCE - 32 PARALLEL FLOW DOUBLE-PIPE HEAT EXCHANGER - 33 COUNTERFLOW DOUBLE-PIPE HEAT EXCHANGER - 35 THE RESTRICTIONS ON THE OVERALL HEAT TRANSFER COEFFICIENT - 36 LMTD AND FLUID FLOW ARRANGEMENT ---- 37 SPECIAL CASES OF LMTD ---- 39 XIV - - CONTENTS 2.5.6 2.5.7 2.5.8 2.5.9 2.6 2.6.1 2.6.2 THE PHYSICAL MEANING OF LMTD ---- 39 DO WE NEED LMTD NOWADAYS? ---- 39 AREA SIZING USING THE DESCRIPTIVE DIFFERENTIAL EQUATIONS ---- 40 PARALLEL FLOW OR COUNTERFLOW: WHAT IS THE DIFFERENCE? ---- 41 EXIT TEMPERATURES OF FLUIDS ---- 43 COUNTERFLOW ---- 43 PARALLEL FLOW ---- 45 PROBLEMS ---- 52 3 3.1 3.1.1 3.1.2 3.2 3.2.1 3.2.2 3.3 3.3.1 3.3.2 3.3.3 WALL TEMPERATURES ---- 57 COLD FLUID IN THE INNER PIPE ---- 58 NEGLIGIBLE CONDUCTIVE RESISTANCE ---- 59 THIN TUBE WALL ---- 59 HOT FLUID IN THE INNER PIPE ---- 60 NEGLIGIBLE CONDUCTIVE RESISTANCE ---- 61 THIN TUBE WALL ---- 61 GENERAL FORM OF WALL TEMPERATURE EQUATIONS ---- 61 SIGNIFICANT CONDUCTIVE AND CONVECTIVE RESISTANCES ---- 61 NEGLIGIBLE CONDUCTIVE WALL RESISTANCE -----62 THIN TUBE WALL ---- 62 PROBLEMS ---- 64 4 4.1 4.1.1 4.2 4.3 4.4 4.4.1 4.5 4.5.1 4.5.2 4.5.3 4.5.4 4.5.5 4.6 4.6.1 4.6.2 4.6.3 HEAT TRANSFER COEFFICIENTS ---- 67 METHODS OF ESTIMATION ---- 67 TYPES OF CORRELATIONS ---- 68 USING CORRELATIONS -----69 FLOW REGIMES ---- 70 EFFECTS OF FLUID FLOW DEVELOPMENT ---- 71 FULLY DEVELOPED LAMINAR FLOW IN PIPES ---- 72 HEAT TRANSFER COEFFICIENTS FOR CIRCULAR PIPES ---- 73 LAMINAR FLOW ---- 73 TURBULENT FLOW ---- 77 TRANSITION FLOW ---- 92 HEAT TRANSFER COEFFICIENTS FOR WATER ---- 94 LIQUID METALS ---- 95 HEAT TRANSFER COEFFICIENTS FOR THE ANNULUS ---- 100 ANNULUS EQUIVALENT DIAMETER ---- 101 PETUKHOV-ROIZEN CORRECTOR ---- 101 GNIELINSKI ANNULUS EQUATION ---- 102 PROBLEMS ---- 104 CONTENTS - - XV 5 5.1 5.1.1 5.1.2 5.1.3 5.1.4 5.2 5.3 5.3.1 5.3.2 5.4 5.4.1 5.4.2 5.4.3 5.4.4 5.5 PRESSURE DROP ---- 107 FRICTION FACTOR IN CIRCULAR TUBES ---- 108 ISOTHERMAL LAMINAR FLOW ---- 109 ISOTHERMAL TURBULENT FLOW ---- 109 ALL FLOW REGIMES ---- 110 EFFECT OF VARIABLE PHYSICAL PROPERTIES ---- 112 PRESSURE DROP CALCULATION WITH THE 2-K METHOD ---- 112 INNER TUBE PRESSURE DROP ---- 113 DISTRIBUTED PRESSURE DROP ---- 114 LOCALIZED PRESSURE DROP ---- 114 ANNULUS PRESSURE DROP ---- 118 DISTRIBUTED PRESSURE DROP ---- 119 LOCALIZED PRESSURE DROP ---- 119 ANNULUS WITH BONNET-TYPE RETURN ---- 121 ANNULUS WITH STRAIGHT-PIPE RETURN ---- 123 ALLOWABLE PRESSURE DROP ---- 125 PROBLEMS ---- 127 6 6.1 6.1.1 6.1.2 6.1.3 6.2 6.2.1 6.2.2 SERIES-PARALLEL ARRANGEMENTS---- 131 MEAN TEMPERATURE DIFFERENCE ---- 133 HOT FLUID IN SERIES AND COLD FLUID IN PARALLEL ---- 134 COLD FLUID IN SERIES AND HOT FLUID IN PARALLEL ---- 135 CHOICE OF THE FLUID DIVISION ---- 136 PRESSURE DROP CALCULATION ---- 137 TUBE PRESSURE DROP ---- 137 ANNULUS PRESSURE DROP ---- 137 PROBLEMS ---- 140 7 7.1 7.2 7.2.1 7.2.2 7.2.3 7.2.4 7.3 7.4 7.4.1 7.4.2 7.5 7.5.1 HEAT EXCHANGER DESIGN ---- 143 FLUID ALLOCATION ---- 143 DESIGN MARGIN ---- 144 OVER-DESIGN ---- 145 OVER-SURFACE ---- 146 FOULING OVER-SURFACE ---- 146 DESIGN MARGIN RANGES ---- 146 PHYSICAL PROPERTIES OF CHEMICAL COMPONENTS - 147 SIZING ---- 148 THE DESIGN VARIABLES ---- 148 SIZING OUTLINE ---- 149 RATING ---- 170 RATING OUTLINE ---- 171 XVI CONTENTS 7.6 THE DATA SHEET ---- 172 PROBLEMS ---- 192 8 MULTI-TUBE HEAT EXCHANGERS---- 195 8.1 TUBE COUNT ---- 195 8.2 DESIGN METHOD ---- 196 8.2.1 CROSS-FLOW AREA ---- 196 8.2.2 SHELL EQUIVALENT DIAMETER ---- 196 PROBLEMS ---- 204 9 FINNED TUBE HEAT EXCHANGERS - 207 9.1 FINS COUNT ---- 208 9.2 DESIGN METHOD ---- 209 9.2.1 CROSS-FLOW AREA ---- 209 9.2.2 SHELL EQUIVALENT DIAMETER ----- 210 9.3 FIN EFFICIENCY ---- 210 9.4 WEIGHTED FIN EFFICIENCY ----- 210 9.5 OVERALL HEAT TRANSFER COEFFICIENT - 211 9.6 FINNED WALL TEMPERATURES ----- 214 PROBLEMS ---- 228 APPENDIX A HEAT EXCHANGER SPECIFICATIONS - 233 A. L PIPING DATA (DN, NB, NPS)---- 233 A. 2 B.W.G.: BIRMINGHAM WIRE GAUGE ---- 239 A.3 HEAT TRANSFER TUBE DATA (B.W.G) ---- 241 A.4 FINNED AND MULTI-TUBE HAIRPIN DESIGN DATA ---- 244 APPENDIX 8 PROPERTIES OF MATERIALS - 249 B. L ABSOLUTE ROUGHNESS OF MATERIALS ---- 249 B. 2 THERMAL CONDUCTIVITY OF SELECTED MATERIALS ---- 250 APPENDIX C PHYSICAL PROPERTIES OF CHEMICAL COMPONENTS - 253 C. L INDEX ---- 253 C. 2 SELECTED GASES: PART A ---- 258 C.3 SELECTED GASES: PART B ---- 262 C.4 SELECTED VAPORS: PART A ----- 267 C.5 SELECTED VAPORS: PART B ----- 272 C.6 SELECTED VAPORS: PART C ----- 277 C.7 SELECTED VAPORS: PART D ----- 283 C.8 SELECTED VAPORS: PART E ----- 288 C.9 SELECTED LIQUIDS: PART A ----- 293 C.10 SELECTED LIQUIDS: PART B ----- 298 CONTENTS - XVII C.LL SELECTED LIQUIDS: PART C ---- 303 C.12 SELECTED LIQUIDS: PART D ---- 308 C.13 SELECTED LIQUIDS: PART E ----- 313 REFERENCES ---- 319 LIST OF GASES ---- 325 LIST OF VAPORS ---- 327 LIST OF LIQUIDS ---- 329 KEYWORD INDEX ---- 331
adam_txt	CONTENTS ACKNOWLEDGMENTS - VII DISCLAIMER ---- IX PREFACE - XI CONVERSION FACTORS - XIX PHYSICAL CONSTANTS - XXI NOMENCLATURE ---- XXIII 1 1.1 1.1.1 1.1.2 1.1.3 1.1.4 1.2 1.3 1.3.1 1.3.2 1.3.3 AN OVERVIEW OF THE EQUIPMENT - 1 PROCESS APPLICABILITY ---- 2 TYPES OF HAIRPINS - 3 PRIMARY CONCERNS ---- 5 WHERE TO USE A DOUBLE-PIPE EXCHANGER? - 5 ABOUT THE OPTIMAL DESIGN ---- 7 THE DOUBLE-PIPE EXCHANGER IS ACTUALLY A HAIRPIN! - 10 PIPES AND TUBES ---- 13 IS THERE A DIFFERENCE? ---- 13 PRACTICAL IMPLICATIONS OF PIPE AND TUBE DISTINCTION - 14 COMMERCIAL DIAMETERS AND LENGTHS - 14 2 2.1 2.2 2.3 2.3.1 2.3.2 2.3.3 2.4 2.4.1 2.4.2 2.5 2.5.1 2.5.2 2.5.3 2.5.4 2.5.5 HEAT EXCHANGER DESIGN EQUATIONS - 17 HEAT LOAD - 17 THE DESIGN EQUATION ---- 20 THE OVERALL HEAT TRANSFER COEFFICIENT - 21 " DESIGN " AND " CLEAN " OVERALL HEAT TRANSFER COEFFICIENTS - 24 RELATIVELY SMALL WALL THERMAL RESISTANCE - 25 CONTROLLING FLUID ---- 25 BASIC HEAT EXCHANGER DIFFERENTIAL EQUATIONS - 28 PARALLEL FLOW ---- 29 COUNTERFLOW ---- 31 LOG MEAN TEMPERATURE DIFFERENCE - 32 PARALLEL FLOW DOUBLE-PIPE HEAT EXCHANGER - 33 COUNTERFLOW DOUBLE-PIPE HEAT EXCHANGER - 35 THE RESTRICTIONS ON THE OVERALL HEAT TRANSFER COEFFICIENT - 36 LMTD AND FLUID FLOW ARRANGEMENT ---- 37 SPECIAL CASES OF LMTD ---- 39 XIV - - CONTENTS 2.5.6 2.5.7 2.5.8 2.5.9 2.6 2.6.1 2.6.2 THE PHYSICAL MEANING OF LMTD ---- 39 DO WE NEED LMTD NOWADAYS? ---- 39 AREA SIZING USING THE DESCRIPTIVE DIFFERENTIAL EQUATIONS ---- 40 PARALLEL FLOW OR COUNTERFLOW: WHAT IS THE DIFFERENCE? ---- 41 EXIT TEMPERATURES OF FLUIDS ---- 43 COUNTERFLOW ---- 43 PARALLEL FLOW ---- 45 PROBLEMS ---- 52 3 3.1 3.1.1 3.1.2 3.2 3.2.1 3.2.2 3.3 3.3.1 3.3.2 3.3.3 WALL TEMPERATURES ---- 57 COLD FLUID IN THE INNER PIPE ---- 58 NEGLIGIBLE CONDUCTIVE RESISTANCE ---- 59 THIN TUBE WALL ---- 59 HOT FLUID IN THE INNER PIPE ---- 60 NEGLIGIBLE CONDUCTIVE RESISTANCE ---- 61 THIN TUBE WALL ---- 61 GENERAL FORM OF WALL TEMPERATURE EQUATIONS ---- 61 SIGNIFICANT CONDUCTIVE AND CONVECTIVE RESISTANCES ---- 61 NEGLIGIBLE CONDUCTIVE WALL RESISTANCE -----62 THIN TUBE WALL ---- 62 PROBLEMS ---- 64 4 4.1 4.1.1 4.2 4.3 4.4 4.4.1 4.5 4.5.1 4.5.2 4.5.3 4.5.4 4.5.5 4.6 4.6.1 4.6.2 4.6.3 HEAT TRANSFER COEFFICIENTS ---- 67 METHODS OF ESTIMATION ---- 67 TYPES OF CORRELATIONS ---- 68 USING CORRELATIONS -----69 FLOW REGIMES ---- 70 EFFECTS OF FLUID FLOW DEVELOPMENT ---- 71 FULLY DEVELOPED LAMINAR FLOW IN PIPES ---- 72 HEAT TRANSFER COEFFICIENTS FOR CIRCULAR PIPES ---- 73 LAMINAR FLOW ---- 73 TURBULENT FLOW ---- 77 TRANSITION FLOW ---- 92 HEAT TRANSFER COEFFICIENTS FOR WATER ---- 94 LIQUID METALS ---- 95 HEAT TRANSFER COEFFICIENTS FOR THE ANNULUS ---- 100 ANNULUS EQUIVALENT DIAMETER ---- 101 PETUKHOV-ROIZEN CORRECTOR ---- 101 GNIELINSKI ANNULUS EQUATION ---- 102 PROBLEMS ---- 104 CONTENTS - - XV 5 5.1 5.1.1 5.1.2 5.1.3 5.1.4 5.2 5.3 5.3.1 5.3.2 5.4 5.4.1 5.4.2 5.4.3 5.4.4 5.5 PRESSURE DROP ---- 107 FRICTION FACTOR IN CIRCULAR TUBES ---- 108 ISOTHERMAL LAMINAR FLOW ---- 109 ISOTHERMAL TURBULENT FLOW ---- 109 ALL FLOW REGIMES ---- 110 EFFECT OF VARIABLE PHYSICAL PROPERTIES ---- 112 PRESSURE DROP CALCULATION WITH THE 2-K METHOD ---- 112 INNER TUBE PRESSURE DROP ---- 113 DISTRIBUTED PRESSURE DROP ---- 114 LOCALIZED PRESSURE DROP ---- 114 ANNULUS PRESSURE DROP ---- 118 DISTRIBUTED PRESSURE DROP ---- 119 LOCALIZED PRESSURE DROP ---- 119 ANNULUS WITH BONNET-TYPE RETURN ---- 121 ANNULUS WITH STRAIGHT-PIPE RETURN ---- 123 ALLOWABLE PRESSURE DROP ---- 125 PROBLEMS ---- 127 6 6.1 6.1.1 6.1.2 6.1.3 6.2 6.2.1 6.2.2 SERIES-PARALLEL ARRANGEMENTS---- 131 MEAN TEMPERATURE DIFFERENCE ---- 133 HOT FLUID IN SERIES AND COLD FLUID IN PARALLEL ---- 134 COLD FLUID IN SERIES AND HOT FLUID IN PARALLEL ---- 135 CHOICE OF THE FLUID DIVISION ---- 136 PRESSURE DROP CALCULATION ---- 137 TUBE PRESSURE DROP ---- 137 ANNULUS PRESSURE DROP ---- 137 PROBLEMS ---- 140 7 7.1 7.2 7.2.1 7.2.2 7.2.3 7.2.4 7.3 7.4 7.4.1 7.4.2 7.5 7.5.1 HEAT EXCHANGER DESIGN ---- 143 FLUID ALLOCATION ---- 143 DESIGN MARGIN ---- 144 OVER-DESIGN ---- 145 OVER-SURFACE ---- 146 FOULING OVER-SURFACE ---- 146 DESIGN MARGIN RANGES ---- 146 PHYSICAL PROPERTIES OF CHEMICAL COMPONENTS - 147 SIZING ---- 148 THE DESIGN VARIABLES ---- 148 SIZING OUTLINE ---- 149 RATING ---- 170 RATING OUTLINE ---- 171 XVI CONTENTS 7.6 THE DATA SHEET ---- 172 PROBLEMS ---- 192 8 MULTI-TUBE HEAT EXCHANGERS---- 195 8.1 TUBE COUNT ---- 195 8.2 DESIGN METHOD ---- 196 8.2.1 CROSS-FLOW AREA ---- 196 8.2.2 SHELL EQUIVALENT DIAMETER ---- 196 PROBLEMS ---- 204 9 FINNED TUBE HEAT EXCHANGERS - 207 9.1 FINS COUNT ---- 208 9.2 DESIGN METHOD ---- 209 9.2.1 CROSS-FLOW AREA ---- 209 9.2.2 SHELL EQUIVALENT DIAMETER ----- 210 9.3 FIN EFFICIENCY ---- 210 9.4 WEIGHTED FIN EFFICIENCY ----- 210 9.5 OVERALL HEAT TRANSFER COEFFICIENT - 211 9.6 FINNED WALL TEMPERATURES ----- 214 PROBLEMS ---- 228 APPENDIX A HEAT EXCHANGER SPECIFICATIONS - 233 A. L PIPING DATA (DN, NB, NPS)---- 233 A. 2 B.W.G.: BIRMINGHAM WIRE GAUGE ---- 239 A.3 HEAT TRANSFER TUBE DATA (B.W.G) ---- 241 A.4 FINNED AND MULTI-TUBE HAIRPIN DESIGN DATA ---- 244 APPENDIX 8 PROPERTIES OF MATERIALS - 249 B. L ABSOLUTE ROUGHNESS OF MATERIALS ---- 249 B. 2 THERMAL CONDUCTIVITY OF SELECTED MATERIALS ---- 250 APPENDIX C PHYSICAL PROPERTIES OF CHEMICAL COMPONENTS - 253 C. L INDEX ---- 253 C. 2 SELECTED GASES: PART A ---- 258 C.3 SELECTED GASES: PART B ---- 262 C.4 SELECTED VAPORS: PART A ----- 267 C.5 SELECTED VAPORS: PART B ----- 272 C.6 SELECTED VAPORS: PART C ----- 277 C.7 SELECTED VAPORS: PART D ----- 283 C.8 SELECTED VAPORS: PART E ----- 288 C.9 SELECTED LIQUIDS: PART A ----- 293 C.10 SELECTED LIQUIDS: PART B ----- 298 CONTENTS - XVII C.LL SELECTED LIQUIDS: PART C ---- 303 C.12 SELECTED LIQUIDS: PART D ---- 308 C.13 SELECTED LIQUIDS: PART E ----- 313 REFERENCES ---- 319 LIST OF GASES ---- 325 LIST OF VAPORS ---- 327 LIST OF LIQUIDS ---- 329 KEYWORD INDEX ---- 331
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author	Cartaxo, Samuel Jorge Marques
author_GND	(DE-588)1266200886
author_facet	Cartaxo, Samuel Jorge Marques
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author_sort	Cartaxo, Samuel Jorge Marques
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building	Verbundindex
bvnumber	BV047943742
classification_rvk	VN 7320
ctrlnum	(OCoLC)1319624347 (DE-599)DNB1244540560
discipline	Chemie / Pharmazie
discipline_str_mv	Chemie / Pharmazie
format	Book
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illustrated	Illustrated
index_date	2024-07-03T19:35:49Z
indexdate	2024-07-10T09:25:53Z
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isbn	3110585731 9783110585735
language	English
oai_aleph_id	oai:aleph.bib-bvb.de:BVB01-033325188
oclc_num	1319624347
open_access_boolean
owner	DE-29T DE-83
owner_facet	DE-29T DE-83
physical	XXVI, 337 Seiten Illustrationen, Diagramme 24 cm x 17 cm
publishDate	2022
publishDateSearch	2022
publishDateSort	2022
publisher	De Gruyter
record_format	marc
series2	De Gruyter graduate
spelling	Cartaxo, Samuel Jorge Marques Verfasser (DE-588)1266200886 aut Tubular heat exchangers for chemical engineers Samuel Jorge Marques Cartaxo Berlin ; Boston De Gruyter 2022 XXVI, 337 Seiten Illustrationen, Diagramme 24 cm x 17 cm txt rdacontent n rdamedia nc rdacarrier De Gruyter graduate Rohrwärmeaustauscher (DE-588)4178380-3 gnd rswk-swf TB: Textbook Technische Chemie Wärmeaustauscher Wärmetechnik Wärmeübertrager Rohrwärmeaustauscher (DE-588)4178380-3 s DE-604 Walter de Gruyter GmbH & Co. KG (DE-588)10095502-2 pbl Erscheint auch als Online-Ausgabe, PDF 978-3-11-058587-2 Erscheint auch als Online-Ausgabe, EPUB 978-3-11-058591-9 X:MVB https://www.degruyter.com/isbn/9783110585735 DNB Datenaustausch application/pdf http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=033325188&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA Inhaltsverzeichnis 1\p vlb 20211028 DE-101 https://d-nb.info/provenance/plan#vlb
spellingShingle	Cartaxo, Samuel Jorge Marques Tubular heat exchangers for chemical engineers Rohrwärmeaustauscher (DE-588)4178380-3 gnd
subject_GND	(DE-588)4178380-3
title	Tubular heat exchangers for chemical engineers
title_auth	Tubular heat exchangers for chemical engineers
title_exact_search	Tubular heat exchangers for chemical engineers
title_exact_search_txtP	Tubular heat exchangers for chemical engineers
title_full	Tubular heat exchangers for chemical engineers Samuel Jorge Marques Cartaxo
title_fullStr	Tubular heat exchangers for chemical engineers Samuel Jorge Marques Cartaxo
title_full_unstemmed	Tubular heat exchangers for chemical engineers Samuel Jorge Marques Cartaxo
title_short	Tubular heat exchangers
title_sort	tubular heat exchangers for chemical engineers
title_sub	for chemical engineers
topic	Rohrwärmeaustauscher (DE-588)4178380-3 gnd
topic_facet	Rohrwärmeaustauscher
url	https://www.degruyter.com/isbn/9783110585735 http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=033325188&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA
work_keys_str_mv	AT cartaxosamueljorgemarques tubularheatexchangersforchemicalengineers AT walterdegruytergmbhcokg tubularheatexchangersforchemicalengineers

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