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    DIN EN ISO 16812-2007 Petroleum petrochemical and natural gas industries - Shell-and-tube heat exchangers (ISO 16812 2007) English version EN ISO 16812 2007《石油、石化和天然气工业 管壳式热交换器》.pdf

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    DIN EN ISO 16812-2007 Petroleum petrochemical and natural gas industries - Shell-and-tube heat exchangers (ISO 16812 2007) English version EN ISO 16812 2007《石油、石化和天然气工业 管壳式热交换器》.pdf

    1、Juni 2007DEUTSCHE NORM Normenausschuss Erdl- und Erdgasgewinnung (NG) im DINNormenausschuss Maschinenbau (NAM) im DINPreisgruppe 17DIN Deutsches Institut fr Normung e.V. Jede Art der Vervielfltigung, auch auszugsweise, nur mit Genehmigung des DIN Deutsches Institut fr Normung e.V., Berlin, gestattet

    2、.ICS 27.060.30; 75.180.20!,wz#“9848700www.din.deDDIN EN ISO 16812Erdl-, petrochemische und Erdgasindustrie Rohrbndelwrmetauscher (ISO 16812:2007);Englische Fassung EN ISO 16812:2007Petroleum, petrochemical and natural gas industries Shell-and-tube heat exchangers (ISO 16812:2007);English version EN

    3、ISO 16812:2007Industries du ptrole, de la ptrochimie et du gaz naturel changeurs de chaleur faisceaux (ISO 16812:2007);Version anglaise EN ISO 16812:2007Alleinverkauf der Normen durch Beuth Verlag GmbH, 10772 BerlinErsatz frDIN EN ISO 16812:2005-07www.beuth.deGesamtumfang 49 SeitenDIN EN ISO 16812:2

    4、007-06 2 Nationales Vorwort Diese Europische Norm wurde vom Technischen Komitee CEN/TC 12 Materialien, Ausrstungen und Offshore-Bauwerke fr die Erdl-, petrochemische und Erdgasindustrie“ (Sekretariat: Frankreich) erstellt. Es handelt sich dabei um die unvernderte bernahme von ISO 16812:2006, erarbei

    5、tet von ISO/TC 67 Materials, equipment and offshore structures for petroleum, petrochemical and natural gas industries“, Subkomitee SC 6 Processing equipment and systems“. Fr Deutschland waren bei der Erstellung dieser Europischen Norm der Normenausschuss Erdl- und Erdgasgewinnung (NG) beteiligt sow

    6、ie der Normenausschuss Maschinenbau (NAM), der fr Deutschland im SC 6 aktiv mitarbeitet. Diese Europische Norm enthlt unter Bercksichtigung des DIN-Prsidialbeschlusses 13/1983 nur die englische Originalfassung der ISO-Norm. nderungen Gegenber DIN EN ISO 16812:2005-07 wurden folgende nderungen vorgen

    7、ommen: a) Der Abschnitt 3 Begriffe und Definitionen wurde gekrzt; b) im Abschnitt 4 Allgemeines wurden Querverweise auf die Anhnge aufgenommen; c) im Abschnitt 5 Anfragen wurde eine Neugliederung der Verantwortlichkeiten des Kufers und des Verkufers aufgenommen; d) im Abschnitt 7 Konstruktion wurden

    8、 die zulssigen Dicken fr plattierte Werkstoffe gendert sowie die Anforderungen an Dichtungen erweitert; e) im Abschnitt 9 Herstellung wurden die Werte fr die Wanddickenminderungen bei den Rohrverbindern gendert; f) die in Anhang C aufgefhrte Checkliste fr die Wrmetauscher wurde inhaltlich gendert; g

    9、) der in Anhang D wiedergegebene Umfang der Datenbltter fr die Verantwortlichkeiten der Vertragspartner wurde reduziert. Frhere Ausgaben DIN EN ISO 16812: 2005-07 EUROPEAN STANDARD NORME EUROPENNE EUROPISCHE NORM EN ISO 16812 February 2007 ICS 75.180.20; 27.060.30 Supersedes EN ISO 16812:2003English

    10、 Version Petroleum, petrochemical and natural gas industries Shell-and-tube heat exchangers (ISO 16812:2007) Industries du ptrole, de la ptrochimie et du gaz naturel changeurs de chaleur faisceaux (ISO 16812:2007) Erdl-, petrochemische und Erdgasindustrie Rohrbdelwrmetauscher (ISO 16812:2007) This E

    11、uropean Standard was approved by CEN on 3 February 2007. CEN members are bound to comply with the CEN/CENELEC Internal Regulations which stipulate the conditions for giving this European Standard the status of a national standard without any alteration. Up-to-date lists and bibliographical reference

    12、s concerning such national standards may be obtained on application to the CEN Management Centre or to any CEN member. This European Standard exists in three official versions (English, French, German). A version in any other language made by translation under the responsibility of a CEN member into

    13、 its own language and notified to the CEN Management Centre has the same status as the official versions. CEN members are the national standards bodies of Austria, Belgium, Bulgaria, Cyprus, Czech Republic, Denmark, Estonia, Finland, France, Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia,

    14、 Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal, Romania, Slovakia, Slovenia, Spain, Sweden, Switzerland and United Kingdom. EUROPEAN COMMITTEE FOR STANDARDIZATION COMIT EUROPEN DE NORMALISATION EUROPISCHES KOMITEE FR NORMUNG Management Centre: rue de Stassart, 36 B-1050 Brussel

    15、s 2007 CEN All rights of exploitation in any form and by any means reserved worldwide for CEN national Members. Ref. No. EN ISO 16812:2007: EEN ISO 16812:2007 (E) 2 Contents Page Foreword4 Endorsement notice .4 Introduction .5 1 Scope 6 2 Normative references 6 3 Terms and definitions .6 4 General8

    16、5 Proposals8 6 Drawings and other required data .9 6.1 Outline drawings and other supporting data9 6.2 Information required after outline drawings are reviewed . 10 6.3 Reports and records. 11 7 Design 12 7.1 Design temperature 12 7.2 Cladding for corrosion allowance. 12 7.3 Shell supports. 12 7.4 S

    17、tationary head. 13 7.5 Floating head. 13 7.6 Tube bundle. 14 7.7 Nozzles and other connections. 17 7.8 Flanged external girth joints 18 7.9 Expansion joints . 18 7.10 Gaskets 19 7.11 Handling devices 20 7.12 Hydrogen service 20 8 Materials 20 8.1 General. 20 8.2 Gaskets 21 8.3 Tubes . 21 9 Fabricati

    18、on. 21 9.1 Shells . 21 9.2 Pass-partition plates 21 9.3 Connection junctions . 22 9.4 Tubes . 22 9.5 Welding 22 9.6 Heat treatment. 22 9.7 Dimensional tolerances . 23 9.8 Gasket contact surfaces other than nozzle-flange facings 23 9.9 Tube holes. 24 9.10 Tube-to-tubesheet joints 24 9.11 Assembly. 25

    19、 10 Inspection and testing 25 10.1 Quality assurance. 25 10.2 Quality control. 25 EN ISO 16812:2007 (E) 3 Page 10.3 Pressure testing 27 10.4 Nameplates and stampings27 11 Preparation for shipment28 11.1 Protection.28 11.2 Identification 28 12 Supplemental requirements .28 12.1 General .28 12.2 Desig

    20、n.29 12.3 Examination .29 Annex A (informative) Recommended practices .31 Annex B (informative) Shell-and-tube heat exchanger checklist.33 Annex C (informative) Shell-and-tube heat exchanger data sheets 34 Annex D (informative) Responsibility data sheet 45 Bibliography47 EN ISO 16812:2007 (E) 4 Fore

    21、word This document (EN ISO 16812:2007) has been prepared by Technical Committee ISO/TC 67 “Materials, equipment and offshore structures for petroleum and natural gas industries“ in collaboration with Technical Committee CEN/TC 12 “Materials, equipment and offshore structures for petroleum, petrochem

    22、ical and natural gas industries“, the secretariat of which is held by AFNOR. This European Standard shall be given the status of a national standard, either by publication of an identical text or by endorsement, at the latest by August 2007, and conflicting national standards shall be withdrawn at t

    23、he latest by August 2007. This document supersedes EN ISO 16812:2003. According to the CEN/CENELEC Internal Regulations, the national standards organizations of the following countries are bound to implement this European Standard: Austria, Belgium, Bulgaria, Cyprus, Czech Republic, Denmark, Estonia

    24、, Finland, France, Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal, Romania, Slovakia, Slovenia, Spain, Sweden, Switzerland and United Kingdom. Endorsement notice The text of ISO 16812:2007 has been approved by CEN as EN

    25、ISO 16812:2007 without any modifications. EN ISO 16812:2007 (E) 5 Introduction Users of this International Standard should be aware that further or differing requirements may be needed for individual applications. This International Standard is not intended to inhibit a vendor from offering, or the

    26、purchaser from accepting, alternative equipment or engineering solutions for the individual application. This may be particularly applicable where there is innovative or developing technology. Where an alternative is offered, the vendor should identify any variations from this International Standard

    27、 and provide details. Annex A provides some optional recommended practices. A bullet (z) at the beginning of a clause or subclause indicates a requirement for the purchaser to make a decision or provide information (see checklist in Annex B). In this International Standard, where practical, US Custo

    28、mary (USC) units are included in parentheses for information. EN ISO 16812:2007 (E) 6 1 Scope This International Standard specifies requirements and gives recommendations for the mechanical design, material selection, fabrication, inspection, testing and preparation for shipment of shell-and-tube he

    29、at exchangers for the petroleum, petrochemical and natural gas industries. This International Standard is applicable to the following types of shell-and-tube heat exchangers: heaters, condensers, coolers and reboilers. This International Standard is not applicable to vacuum-operated steam surface co

    30、ndensers and feed-water heaters. 2 Normative references The following referenced documents are indispensable for the application of this document. For dated references, only the edition cited applies. For undated references, the latest edition of the referenced document (including any amendments) ap

    31、plies. ISO 15156 (all parts), Petroleum and natural gas industries Materials for use in H2S-containing environments in oil and gas production ASME B 16.51), Pipe Flanges and Flanged Fittings ASME B 16.11, Forged Fittings, Socket-Welding and Threaded ASME B 1.20.1, Pipe Threads, General Purpose (Inch

    32、) EJMA2), Standards of the Expansion Joint Manufacturers Association NACE MR01033), Materials Resistant to Sulfide Stress Cracking in Corrosive Petroleum Refining Environments TEMA Standards Set4), 8thEdition, Standards of the Tubular Exchanger Manufacturers Association 3 Terms and definitions For t

    33、he purposes of this document, the following terms and definitions apply. 3.1 annular distributor additional chamber incorporated into a shell side nozzle to more evenly distribute shell side fluids entering or exiting the tube bundle 3.2 category A welded joint longitudinal welded joint within the m

    34、ain shell, communicating chambers, nozzles or transitions in diameter; or any welded joint within a sphere or within a formed or flat head; or circumferential welded joint connecting hemispherical heads to main shells, to transitions in diameters or to communicating chambers 1) ASME International, 3

    35、 Park Avenue, New York, NY 10016-5990, USA. 2) Expansion Joint Manufacturers Association, 25 North Broadway, Tarrytown, NY 10591, USA. 3) NACE International, P.O. Box 218340, Houston, TX 77218-8340, USA. 4) Tubular Exchanger Manufacturers Association, 25 North Broadway, Tarrytown, NY 10591, USA. EN

    36、ISO 16812:2007 (E) 7 3.3 category B welded joint circumferential welded joint within the main shell, communicating chambers, nozzles or transitions in diameter, including joints between the transitions and a cylinder at either the large or small end; or circumferential welded joint connecting formed

    37、 heads, other than hemispherical, to main shells, to transitions in diameter, to nozzles or to communicating chambers 3.4 communicating chamber heat-exchanger appurtenance that intersects the shell or heads of the heat exchanger and forms an integral part of the pressure-containing envelope EXAMPLES

    38、 Sump, annular distributor. 3.5 effective surface outside surface area of the tubes that contributes to heat transfer 3.6 full-penetration weld welded joint that results in weld metal through the entire thickness of the components being joined 3.7 heat-exchanger unit one or more heat exchangers for

    39、a specified service that may include alternative operating conditions 3.8 hydrogen service service that contains hydrogen at a partial pressure exceeding 700 kPa (100 psi) absolute 3.9 item number purchasers identification number for a heat-exchanger unit 3.10 nubbin projection on the flange gasket

    40、surface, positioned at the centre of the gasket, used to concentrate the bolt load on the gasket 3.11 pressure design code recognized pressure vessel standard specified or agreed by the purchaser EXAMPLES ASME Section VIII, EN 13445. 3.12 seal-welded tube-to-tubesheet joint weld of unspecified stren

    41、gth applied between the tubes and tubesheets for the sole purpose of reducing the potential for leakage 3.13 strength-welded tube-to-tubesheet joint welded so that the design strength is equal to, or greater than, the axial tube strength specified by the pressure design code EN ISO 16812:2007 (E) 8

    42、4 General z 4.1 The pressure design code shall be specified or agreed by the purchaser. Pressure components shall comply with the pressure design code and the supplemental requirements given in this International Standard. 4.2 Heat-exchanger construction shall conform to TEMA (8thedition), Class R,

    43、unless another TEMA class is specified. z 4.3 The vendor shall comply with the applicable local regulations specified by the purchaser. 4.4 Annex A includes some recommended mechanical and design details for information. 4.5 Annex B provides a checklist that can be used by the purchaser to ensure th

    44、at bulletted items in this International Standard are addressed. 4.6 Annex C provides examples of data sheets. 4.7 Annex D includes a recommended division of responsibility for completing the data sheet. 5 Proposals 5.1 The vendors proposal shall include, for each heat exchanger unit, completed data

    45、 sheets such as those given in Annex C or, if a data sheet is included in the inquiry, a statement indicating complete compliance with that data sheet. 5.2 Designs that are not fully defined by the nomenclature in TEMA (8thedition), Section 1, shall be accompanied by sketches that are sufficient to

    46、describe the details of construction. 5.3 If an annular distributor is provided, the vendor shall define the type of construction proposed. 5.4 The vendor shall determine the need for, and if required, include expansion joints based on all conditions supplied by the purchaser. The vendor shall state

    47、 the type of construction proposed. 5.5 The proposal shall include a detailed description of all exceptions to the requirements of the purchasers inquiry. 5.6 For stacked heat exchangers, the vendor shall supply the following components unless otherwise specified by the purchaser: a) bolts, nuts and

    48、 gaskets for interconnecting nozzles; b) shims and bolting for interconnecting supports. 5.7 The vendor shall provide a separate quotation for the following items unless otherwise specified by the purchaser: a) a test component consisting of a test ring and gland, in accordance with TEMA (8thedition

    49、), Figure E-4.13-2 or equivalent, for each heat exchanger or group of similar heat exchangers with floating heads; b) one spare set of gaskets per heat-exchanger unit. EN ISO 16812:2007 (E) 9 6 Drawings and other required data 6.1 Outline drawings and other supporting data 6.1.1 The vendor shall submit, for review by the purchaser, outline drawings for each heat exchanger unit. The drawings shall include the following information: a) service, item number, project name and location, purchasers order number


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