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Understanding Heat Exchanger Reading 03a The ARAMCO Std.

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My <strong>Reading</strong> on <strong>Heat</strong> <strong>Exchanger</strong><br />

<strong>Reading</strong> 03- <strong>The</strong> <strong>ARAMCO</strong> <strong>Std</strong>.<br />

Part 1 of 2<br />

for my Aramco AOC’s QM31 Exam Preparations<br />

27 th May 2018<br />

http://satorp.com/<br />

Charlie Chong/ Fion Zhang


闭 门 练 功<br />

Charlie Chong/ Fion Zhang


闭 门 练 功<br />

Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Zhang<br />

Fion Zhang at Shanghai<br />

Damuqiao 大 木 桥 路<br />

27 th May 2018


Charlie Chong/ Fion Zhang<br />

http://greekhouseoffonts.com/


<strong>The</strong> Magical Book of <strong>Heat</strong> <strong>Exchanger</strong> <strong>Reading</strong><br />

Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Zhang


有<br />

书<br />

真<br />

幸<br />

福<br />

无 事 小 神 仙<br />

Charlie Chong/ Fion Zhang


Parts:<br />

1. API660/ ISO 16812:2007<br />

Shell-and-tube <strong>Heat</strong> <strong>Exchanger</strong>s<br />

2. Materials System Specification<br />

32-SAMSS-007<br />

Manufacture of Shell and Tube <strong>Heat</strong> <strong>Exchanger</strong>s<br />

Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Zhang<br />

American Petroleum Institute API 600 <strong>Std</strong>.


Part 1:<br />

Shell-and-tube <strong>Heat</strong> <strong>Exchanger</strong>s<br />

ANSI/API STANDARD 660<br />

EIGHTH EDITION, AUGUST 2007<br />

ISO 16812:2007 (Identical), Petroleum, petrochemical<br />

and natural gas industries-Shell-and-tube <strong>Heat</strong><br />

<strong>Exchanger</strong>s<br />

Charlie Chong/ Fion Zhang


Contents<br />

1. Scope<br />

2. Normative references<br />

3. Terms and definitions<br />

4. General<br />

5. Proposals<br />

6. Drawings and other required<br />

7. Design<br />

8. Materials<br />

9. Fabrication<br />

10. Inspection and testing<br />

11. Preparation for shipment<br />

12. Supplemental requirements<br />

Annex A (informative) Recommended practices<br />

Annex B (informative) Shell-and-tube heat exchanger checklist<br />

Annex C (informative) Shell-and-tube heat exchanger data sheets<br />

Annex 0 (informative) Responsibility data sheet<br />

Charlie Chong/ Fion Zhang


Foreword<br />

ISO (the International Organization for Standardization) is a worldwide<br />

federation of national standards bodies (ISO member bodies). <strong>The</strong> work of<br />

preparing International Standards is normally carried out through ISO<br />

technical committees. Each member body interested in a subject for which a<br />

technical committee has been established has the right to be represented on<br />

that committee.<br />

International organizations, governmental and non-governmental, in liaison<br />

with ISO, also take part in the work. ISO collaborates closely with the<br />

International Electrotechnical Commission (IEC) on all matters of<br />

electrotechnical standardization. International Standards are drafted in<br />

accordance with the rules given in the ISO/IEC Directives, Part 2.<br />

<strong>The</strong> main task of technical committees is to prepare International Standards.<br />

Draft International Standards adopted by the technical committees are<br />

circulated to the member bodies for voting. Publication as an International<br />

Standard requires approval by at least 75 % of the member bodies casting a<br />

vote.<br />

Charlie Chong/ Fion Zhang


Attention is drawn to the possibility that some of the elements of this<br />

document may be the subject of patent rights. ISO shall not be held<br />

responsible for identifying any or all such patent rights.<br />

ISO 16812 was prepared by Technical Committee ISO/TC 67, Materials,<br />

equipment and offshore structures for petroleum, petrochemical and natural<br />

gas industries, Subcommittee SC 6, Processing equipment and systems. This<br />

second edition cancels and replaces the first edition (ISO 16812:2002), which<br />

has been technically revised.<br />

Charlie Chong/ Fion Zhang


ISO collaborates closely with the<br />

International Electrotechnical<br />

Commission (IEC) on all matters<br />

of electrotechnical<br />

standardization. International<br />

Standards are drafted in<br />

accordance with the rules given<br />

in the ISO/IEC Directives, Part 2.<br />

Charlie Chong/ Fion Zhang


ISO Publication as an International<br />

Standard requires approval by at<br />

least 75 % of the member bodies<br />

casting a vote.<br />

Charlie Chong/ Fion Zhang


Introduction<br />

Users of this International Standard should be aware that further or differing<br />

requirements may be needed for individual applications. This International<br />

Standard is not intended to inhibit a vendor from offering, or the purchaser<br />

from accepting, alternative equipment or engineering solutions for the<br />

individual application. This may be particularly applicable where there is<br />

innovative or developing technology. Where an alternative is offered, the<br />

vendor should identify any variations from this International Standard and<br />

provide details.<br />

Annex A provides some optional recommended practices.<br />

A bullet (•) at the beginning of a clause or sub-clause indicates a requirement<br />

for the purchaser to make a decision or provide information (see checklist in<br />

Annex B).<br />

In this International Standard, where practical, US Customary (USC) units are<br />

included in parentheses for information.<br />

Charlie Chong/ Fion Zhang


A bullet (•)<br />

at the beginning of a clause or<br />

sub-clause indicates a<br />

requirement for the purchaser to<br />

make a decision or provide<br />

information (see checklist in<br />

Annex B).<br />

Charlie Chong/ Fion Zhang


A bullet (•)<br />

at the beginning of a clause or sub-clause indicates a requirement for the<br />

purchaser to make a decision or provide information (see checklist in Annex B).<br />

Charlie Chong/ Fion Zhang


In this International Standard, where practical, US Customary (USC) units are<br />

included in parentheses for information.<br />

Charlie Chong/ Fion Zhang


Petroleum, petrochemical and natural gas industries - Shelland-tube<br />

heat exchangers<br />

1 Scope<br />

This International Standard specifies requirements and gives<br />

recommendations for the:<br />

1. mechanical design,<br />

2. material selection,<br />

3. fabrication, inspection, testing and<br />

4. preparation for shipment of shell-and-tube heat exchangers for the<br />

petroleum, petrochemical and natural gas industries.<br />

This International Standard is applicable to the following types of shell-andtube<br />

heat exchangers:<br />

• heaters, condensers, coolers and reboilers.<br />

This International Standard is not applicable to vacuum-operated steam<br />

surface condensers and feed-water heaters.<br />

Charlie Chong/ Fion Zhang


Vacuum-operated Steam Surface Condensers<br />

Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Zhang<br />

Vacuum<br />

operated<br />

Steam<br />

Surface<br />

Condensers


Power Plant- Vacuumoperated<br />

Steam Surface<br />

Condensers<br />

Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Zhang


2 Normative references<br />

<strong>The</strong> following referenced documents are indispensable for the application of<br />

this document. For dated references, only the edition cited applies. For<br />

undated references, the latest edition of the referenced document (including<br />

any amendments) applies.<br />

• ISO 15156 (all parts) (NACE MR0175), Petroleum and natural gas<br />

industries- Materials for use in H 2 S-containing environments in oil and<br />

gas production<br />

• ASME B 16.5, Pipe Flanges and Flanged Fittings<br />

• ASME B 16.11, Forged Fittings, Socket-Welding and Threaded<br />

• ASME B 1.20.1, Pipe Threads, General Purpose (Inch)<br />

• EJMA, Standards of the Expansion Joint Manufacturers Association<br />

• NACE MR0103 -Materials Resistant to Sulfide Stress Cracking in<br />

Corrosive Petroleum Refining Environments<br />

• TEMA Standards Set, 8th Edition, Standards of the Tubular <strong>Exchanger</strong><br />

Manufacturers Association<br />

Normative : of or relating to a norm, especially an assumed norm regarded<br />

as the standard of correctness in behavior, speech, writing, etc. ( 规 范 的 ; 标 准 的 )<br />

Charlie Chong/ Fion Zhang


<strong>The</strong> following NACE referenced documents are indispensable for the<br />

application of this document.<br />

• ISO 15156 (all parts) (NACE MR0175), Petroleum and natural gas industries- Materials for<br />

use in H2S-containing environments in oil and gas production<br />

• NACE MR0103 -Materials Resistant to Sulfide Stress Cracking in Corrosive Petroleum<br />

Refining Environments<br />

Charlie Chong/ Fion Zhang


3 Terms and definitions<br />

For the purposes of this document, the following terms and definitions apply.<br />

3.1<br />

annular distributor<br />

additional chamber incorporated into a shell side nozzle to more evenly<br />

distribute shell side fluids entering or exiting the tube bundle<br />

Charlie Chong/ Fion Zhang


Annular Distributor<br />

Charlie Chong/ Fion Zhang


3.2<br />

category A welded joint<br />

longitudinal welded joint within the main shell, communicating chambers,<br />

nozzles or transitions in diameter; or any welded joint within a sphere or<br />

within a formed or flat head; or circumferential welded joint connecting<br />

hemispherical heads to main shells, to transitions in diameters or to<br />

communicating chambers<br />

3.3<br />

category B welded joint<br />

circumferential welded joint within the main shell, communicating chambers,<br />

nozzles or transitions in diameter, including joints between the transitions and<br />

a cylinder at either the large or small end; or circumferential welded<br />

joint connecting formed heads, other than hemispherical, to main shells, to<br />

transitions in diameter, to nozzles or to communicating chambers<br />

Charlie Chong/ Fion Zhang


Cat “B” includes most circumferential<br />

welded joints including formed heads (other<br />

than hemispherical) to main shells welds.<br />

FIG. UW-3 ILLUSTRATION OF WELDED JOINT LOCATIONS<br />

TYPICAL OF CATEGORIES A, B, C, and D<br />

Charlie Chong/ Fion Zhang<br />

ASME VIII-UW-03


Cat “A” includes all longitudinal welds and<br />

critical circumferential welds such as<br />

hemispherical head to shell welds.<br />

FIG. UW-3 ILLUSTRATION OF WELDED JOINT LOCATIONS<br />

TYPICAL OF CATEGORIES A, B, C, and D<br />

Charlie Chong/ Fion Zhang<br />

ASME VIII-UW-03


• Cat “A” includes all longitudinal welds and critical<br />

circumferential welds such as hemispherical head to shell<br />

welds.<br />

• Cat “B” includes most circumferential welded joints including<br />

formed heads (other than hemispherical) to main shells welds.<br />

• Cat “C” includes welded joints connecting: . flanges to<br />

nozzles or shell components. one side plate to another in a<br />

flat-sided vessel.<br />

• Cat “D” includes welded joints connecting nozzles to shells,<br />

heads or flat-sided vessels.<br />

Fion Zhang/ Charlie Chong<br />

ASME VIII-UW-03


• Cat “A” includes all longitudinal welds and critical circumferential welds<br />

such as hemispherical head to shell welds.<br />

• Cat “B” includes most circumferential welded joints including formed heads<br />

(other than hemispherical) to main shells welds<br />

Cat A<br />

Charlie Chong/ Fion Zhang<br />

Cat B<br />

Except<br />

Hemispherical Head<br />

ASME VIII-UW-03


Exercise:<br />

Charlie Chong/ Fion Zhang


Exercise:<br />

D<br />

C<br />

D<br />

?<br />

D<br />

C<br />

?<br />

B<br />

B<br />

D<br />

A<br />

A<br />

D<br />

D<br />

Charlie Chong/ Fion Zhang


Exercise:<br />

D<br />

C<br />

D<br />

?<br />

D<br />

C<br />

?<br />

B<br />

B<br />

D<br />

A<br />

A<br />

D<br />

D<br />

Charlie Chong/ Fion Zhang


Exercise:<br />

Charlie Chong/ Fion Zhang


Why Hemispherical Head fall under Cat “A” and<br />

What is RT1 and RT2?<br />

ASME Pressure Vessel Joint Efficiencies<br />

<strong>The</strong> ASME Pressure Vessel Joint Efficiencies article provides you with information about pressure vessel joint efficiency<br />

requirements and their connection with radiography testing.<br />

You may know Pressure Vessel Joint Efficiencies are linked to the radiography testing grades and there is a concession for full<br />

radiography testing as per the UW-11(a) (5) (b) clause which it is a little bit confusing.<br />

This article provides you the ASME pressure vessel joint efficiencies requirements and guidelines for the above clause.<br />

Based on the ASME Code requirement, manufacturers have to mark the type of RT i.e. RT1, RT2, RT3 and RT4 in the pressure<br />

vessel name plate and state the same in Pressure Vessel Data Report.<br />

We have seen many professionals, from inspectors to quality control engineers who are confused between RT1 and RT2,<br />

specifically when they see ASME Pressure Vessel Joint Efficiencies for both RT1 and RT2 is the same and equal to 1(E=1).<br />

<strong>The</strong>y say both RT1 and RT2 are categorized in the “Full Radiography” part in UW-11 clause ...<br />

So why are some joints in RT2 radiographed in spots?<br />

We are making spot radiography, but it is categorized in full radiography!!!<br />

So in this "ASME Pressure Vessel Joint Efficiencies" article we want to answer this question in very simple way, but before this,<br />

we need review joint categories and summarize them as below:<br />

Category A:<br />

All longitudinal welds in shell and nozzles<br />

All welds in heads, Hemispheric-head to shell weld joint<br />

Category B:<br />

All circumferential welds in shell and nozzles<br />

Head to shell joint (other than Hemispheric.)<br />

Category C and D are flange welds and nozzle attachment welds respectively<br />

Charlie Chong/ Fion Zhang<br />

http://www.inspection-for-industry.com/asme-pressure-vessel-joint-efficiencies.html


Do you know why? Why ASME considered the stringent rule for<br />

Category “A” weld than Category “B” weld?<br />

Longitudinal welds (Category A) are more critical than Circumferential welds (Category B) because they are under double stress.<br />

This the reason why in different part of ASME code we have stringent rules in category A joint compared to category B joint.<br />

See the following Fig. for joint categories:<br />

Now let's get back to the ASME Pressure Vessel Joint Efficiencies subject, to remove the above confusion about RT1 and RT2.<br />

We need to know:<br />

Charlie Chong/ Fion Zhang<br />

http://www.inspection-for-industry.com/asme-pressure-vessel-joint-efficiencies.html


When and where is there a code requirement for full radiography?<br />

Item 1: All butt welds in vessels used to contain a lethal substance (UW-11(a)).Lethal substances have specific definitions in<br />

ASME Code in UW-2 and it is the responsibility of the end user to determine if they ordered a vessel that contains lethal<br />

substances.<br />

Item 2: All butt welds in vessels in which the nominal thickness exceeds specified values (UW-11(a). You can find these values in<br />

subsection C, in UCS-57, UNF-57, etc. For example, this value for P-No.1 in UCS-57 is 1 ¼ inch.<br />

Item 3: All butt welds in an unfired steam boiler with design pressure > 50 psi (UW-11(a)).<br />

Item 4: All category A and D butt welds in vessel when “Full Radiography” optionally selected from table UW-12(column (a) in this<br />

table is selected); and categories B and C which intersect Category A shall meet the spot radiography requirement (UW-11(a) (5)<br />

(b)).<br />

<strong>The</strong> point is this: items 1, 2 and 3 are similar, but item 4 is completely different. In items 1, 2 and 3 it is mandated by code; to do<br />

full radiography in all butt welds in vessel so it means it is mandatory for designer to select column (a) in UW-12 table.<br />

But in item 4, there is no mandating rule. A manufacturer with its own decision has chosen to use column (a) in table UW-12 for<br />

full radiography.<br />

So here there is a concession or bonus to manufacturers for categories B and C.<br />

Charlie Chong/ Fion Zhang<br />

http://www.inspection-for-industry.com/asme-pressure-vessel-joint-efficiencies.html


What is concept behind this concession or bonus in pressure vessel RT2?<br />

If you review item 1, 2 and 3 one more time, you will see that the pressure vessel RT tests are related to the type of welds and<br />

services.<br />

You can see the pressure vessels in these items are critical from a safety point of view, one contains a lethal substance, the other one<br />

has a high thickness, which implicates high pressure, and the last one is an unfired steam boiler. But item 4 has no criticality like the<br />

other items have.<br />

But you should note all 4 items have been categorized in full radiography clause( U-11(a)), so to differentiate item 1, 2 and 3 from item<br />

4, the RT symbols are used in Code (UG-116).<br />

RT 1: Items 1, 2 and 3, (E=1), All butt welds-full length radiography<br />

RT 2: Item 4 (E=1), Category A and D butt welds full length radiography and category B and C butt welds spot Radiography<br />

RT 3: (E=0.85), Spot radiography butt welds<br />

RT 4: (E=0.7), Partial / No radiography<br />

You need to consider the hemispherical head joint to shell as category A, but ellipsoidal and torispherical head joint to shell as<br />

category B;<br />

Do you know why? Why ASME considered the stringent rule for pressure<br />

vessel RT test in hemispherical head joint?<br />

It is because this joint is more critical, because the thickness obtained from the formula for hemispherical head approximately would<br />

be half of the shell thickness; It means if the shell thickness is 1 inch, the hemispherical head thickness would be 0.5 inch.<br />

For more detail, you may review the Pressure Vessel Heads http://www.inspection-for-industry.com/pressure-vessel-heads.html<br />

article.<br />

Charlie Chong/ Fion Zhang<br />

http://www.inspection-for-industry.com/asme-pressure-vessel-joint-efficiencies.html


Do you know why? Why ASME considered the stringent rule for<br />

Category “A” weld than Category “B” weld?<br />

Longitudinal welds (Category A) are more critical than Circumferential welds (Category B) because they are under double stress.<br />

This the reason why in different part of ASME code we have stringent rules in category A joint compared to category B joint.<br />

Weld Types:<br />

Here is some clarification about the different type of welds that have specific definitions in ASME Code SEC VIII DIV 1 and related<br />

to the pressure vessel RT test.<br />

<strong>The</strong> concept is to define the different types and then introduce some restriction for using them.<br />

For example, a Type 1 weld is defined as a full penetration weld, typically double welded and Type 2 is welds with backing strips.<br />

So when you go to service restriction for a vessel containing a lethal substance, you see there is a restriction there that says all<br />

category A joints shall be weld Type 1 and Category B and C shall be type 1 or type 2.<br />

You should take this point in to account, which is this: the same joint category with different weld types have different joint<br />

efficiencies.<br />

Summary of weld types:<br />

Type 1: Full penetration welds (Typically Double welded)<br />

Type 2: Welds with backing strip<br />

Type 3: Single welded partial penetration welds<br />

Type 4, 5 and 6: Various Lap welds (rarely used)<br />

Charlie Chong/ Fion Zhang<br />

http://www.inspection-for-industry.com/asme-pressure-vessel-joint-efficiencies.html


Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Zhang


UW-11 RADIOGRAPHIC AND ULTRASONIC<br />

EXAMINATION<br />

(a) Full Radiography. <strong>The</strong> following welded joints<br />

shall be examined radiographically for their full<br />

length in the manner prescribed in UW-51:<br />

1. (1) all butt welds in the shell and heads of vessels<br />

used to contain lethal substances [see UW-2(a)];<br />

2. (2) all butt welds in the shell and heads of vessels in<br />

which the nominal thickness [see (g) below] at the<br />

welded joint exceeds 11/2 in. (38 mm), or exceeds the<br />

lesser thicknesses prescribed in UCS-57, UNF-57,<br />

UHA-33, UCL-35, or UCL-36 for the materials covered<br />

therein, or as otherwise prescribed in UHT-57, ULW-<br />

51, ULW-52(d), ULW-54, or ULT-57;<br />

3. (3) all butt welds in the shell and heads of unfired<br />

steam boilers having design pressures<br />

(-a) exceeding 50 psi (350 kPa) [see UW-2(c)];<br />

(-b) not exceeding 50 psi (350 kPa) [see UW-2(c)]<br />

but with nominal thickness at the welded joint<br />

exceeding the thickness specified in (2) above;<br />

4. (4) all butt welds in nozzles, communicating chambers,<br />

etc., with the nominal thickness at the welded joint that<br />

exceeds the thickness in (2) above or attached to the<br />

shell or heads of vessels under (1), (2), or (3) above<br />

that are required to be fully radiographed; however,<br />

except as required by UHT-57(a), Categories B and C<br />

butt welds in nozzles and communicating chambers<br />

that neither exceed NPS 10 (DN 250) nor 11/8 in. (29<br />

mm) wall thickness do not require any radiographic<br />

examination;<br />

Charlie Chong/ Fion Zhang


UW-11(a) Full Radiography. <strong>The</strong> following<br />

welded joints shall be examined<br />

radiographically for their full length in the<br />

manner prescribed in UW-51:<br />

(5) all Category A and D butt welds in the<br />

shell and heads of vessels where the design<br />

of the joint or part is based on a joint<br />

efficiency permitted by UW-12(a), in<br />

which case:<br />

(-a) Category A and B welds connecting the<br />

shell or heads of vessels shall be of Type<br />

No. (1) or Type No. (2) of Table UW-12;<br />

(-b) Category B or C butt welds [but not including<br />

those in nozzles and communicating chambers except as<br />

required in (4) above] which intersect the Category<br />

A butt welds in the shell or heads of<br />

vessels or connect seamless vessel shell<br />

or heads shall, as a minimum, meet the<br />

requirements for spot radiography in<br />

accordance with UW-52. Spot radiographs<br />

required by this paragraph shall not be<br />

used to satisfy the spot radiography rules<br />

as applied to any other weld increment.<br />

Charlie Chong/ Fion Zhang


Table UW-12<br />

Maximum ALLowabLe Joint Efficiencies for Arc and Gas Welded Joints<br />

Degree of Radiographic<br />

Examination<br />

(a) Full (b) Spot (c)<br />

Type No. Joint Description Limitations Joint Category [Note (1)] [Note (2)] None<br />

[1) Butt joints as attained by double welding or by None A, B, C & D 1.00 0.85 0.70<br />

other means which will obtain the same<br />

quality of deposited weld metal on the inside<br />

and outside weld surfaces to agree with the<br />

requirements of UW 35. Welds using metal<br />

backing strips which remain in place are<br />

excluded.<br />

(2) Single welded butt joint with backing strip (a) None except as in (b) below A, B, C & D 0.90 0.80 0.65<br />

other than those included under (1) (b)Circumferential butt joints with one plate offset; see A, B & C 0.90 0.80 0.65<br />

UW 13(b)[4) and Figure UW 13.1, sketch [i)<br />

[3) Single welded buttjointwithoutuse ofbacking Circumferential butt joints only, not over% in. [16 mm) A, B & C NA NA 0.60<br />

strip<br />

thick and not over 24 in. [600 mm) outside diameter<br />

(4) Double full fillet lap joint (a) Longitudinal joints not over % in. (10 mm) thick A NA NA 0.55<br />

(b) Circumferential joints not over % in. (16 mm) thick B & C [Note (3)] NA NA 0.55<br />

(5) Single full fillet lap joints with plug welds (a) Circumferential joints [Note (4)] for attachment of heads B NA NA 0.50<br />

conforming to UW 17<br />

not over 24 in. (600 mm) outside diameter to shells not<br />

over "/ 2 in. [13 mm) thick<br />

(b) Circumferential joints for the attachment to shells of c NA NA 0.50<br />

jackets not over % in. [16 mm) in nominal thickness<br />

where the distance from the center of the plug weld to the<br />

edge of the plate is not less than 1 1 h times the diameter of<br />

the hole for the plug.<br />

(6) Single full fillet lap joints without plug welds (a) For the attachment of heads convex to pressure to shells A&B NA NA 0.45<br />

not over % in. (16 mm) required thickness, only with use<br />

of fillet weld on inside of shell; or<br />

(b) for attachment of heads having pressure on either side, A&B NA NA 0.45<br />

to shells not over 24 in. [600 mm) inside diameter and<br />

not over % in. [ 6 mm) required thickness with fillet weld<br />

on outside of head flange only<br />

(7) Corner joints, full penetration, partial As limited by Figure UW 13.2 and Figure UW 16.1 C & D [Note (5)] NA NA NA<br />

penetration, and/ or fillet welded<br />

(8) Angle joints Design Eer U 2 (g) for Category B and C joints B, C & D NA NA NA<br />

GENERAL NOTES:<br />

(a} <strong>The</strong> single factor shown for each combination of joint category and degree of radiographic examination replaces both the stress reduction factor and the joint efficiency<br />

factor considerations previously used in this Division.<br />

(b) E" 1.0 for butt joints in compression.<br />

Charlie Chong/ Fion Zhang


115<br />

Table UW-12<br />

Maximum Allowable Joint Efficiencies for Arc and Gas Welded Joints<br />

Degree of Radiographic<br />

Examination<br />

Type No. Joint Description Limitations Joint Category<br />

(a) Full<br />

[Note (1)]<br />

(b) Spot<br />

[Note (2)]<br />

None A, B, C & D 1.00 0.85 0.70<br />

(1) Butt joints as attained by double welding or by<br />

other means which will obtain the same<br />

quality of deposited weld metal on the inside<br />

and outside weld surfaces to agree with the<br />

requirements of UW 35. Welds using metal<br />

backing strips which remain in place are<br />

excluded.<br />

(2) Single welded butt joint with backing strip<br />

other than those included under (1)<br />

(3) Single welded butt joint without use of backing<br />

strip<br />

(a) None except as in (b) below A, B, C & D 0.90 0.80 0.65<br />

(b)Circumferential butt joints with one plate offset; see<br />

UW 13(b)(4) and Figure UW 13.1, sketch (i)<br />

A, B & C 0.90 0.80 0.65<br />

Circumferential butt joints only, not over 5 / 8 in. (16 mm)<br />

A, B & C NA NA 0.60<br />

thick and not over 24 in. (600 mm) outside diameter<br />

(4) Double full fillet lap joint (a) Longitudinal joints not over 3 / 8 in. (10 mm) thick A NA NA 0.55<br />

(b) Circumferential joints not over 5 / 8 in. (16 mm) thick B & C [Note (3)] NA NA 0.55<br />

(5) Single full fillet lap joints with plug welds<br />

conforming to UW 17<br />

(a) Circumferential joints [Note (4)] for attachment of heads<br />

not over 24 in. (600 mm) outside diameter to shells not<br />

over 1 / 2 in. (13 mm) thick<br />

(b) Circumferential joints for the attachment to shells of<br />

jackets not over 5 / 8 in. (16 mm) in nominal thickness<br />

where the distance from the center of the plug weld to the<br />

edge of the plate is not less than 1 1 / 2 times the diameter of<br />

the hole for the plug.<br />

(c)<br />

None<br />

B NA NA 0.50<br />

C NA NA 0.50<br />

(6) Single full fillet lap joints without plug welds (a) For the attachment of heads convex to pressure to shells<br />

A & B NA NA 0.45<br />

not over 5 / 8 in. (16 mm) required thickness, only with use<br />

of fillet weld on inside of shell; or<br />

(b) for attachment of heads having pressure on either side,<br />

A & B NA NA 0.45<br />

to shells not over 24 in. (600 mm) inside diameter and<br />

not over 1 / 4 in. (6 mm) required thickness with fillet weld<br />

on outside of head flange only<br />

(7) Corner joints, full penetration, partial<br />

As limited by Figure UW 13.2 and Figure UW 16.1 C&D[Note (5)] NA NA NA<br />

penetration, and/or fillet welded<br />

(8) Angle joints Design per U 2(g) for Category B and C joints B, C & D NA NA NA<br />

GENERAL NOTES:<br />

(a) <strong>The</strong> single factor shown for each combination of joint category and degree of radiographic examination replaces both the stress reduction factor and the joint efficiency<br />

factor considerations previously used in this Division.<br />

(b) E = 1.0 for butt joints in compression.<br />

2013 SECTION VIII - DIVISION 1 UW-13


UW-11 RADIOGRAPHIC AND ULTRASONIC EXAMINATION<br />

(a) Full Radiography. <strong>The</strong> following welded joints shall be examined radiographically for their<br />

full length in the manner prescribed in UW-51:<br />

1. (1) all butt welds in the shell and heads of vessels used to contain lethal substances [see UW-2(a)];<br />

2. (2) all butt welds in the shell and heads of vessels in which the nominal thickness [see (g) below] at the welded joint exceeds<br />

11/2 in. (38 mm), or exceeds the lesser thicknesses prescribed in UCS-57, UNF-57, UHA-33, UCL-35, or UCL-36 for the<br />

materials covered therein, or as otherwise prescribed in UHT-57, ULW-51, ULW-52(d), ULW-54, or ULT-57;<br />

3. (3) all butt welds in the shell and heads of unfired steam boilers having design pressures<br />

(-a) exceeding 50 psi (350 kPa) [see UW-2(c)];<br />

(-b) not exceeding 50 psi (350 kPa) [see UW-2(c)]<br />

but with nominal thickness at the welded joint exceeding the thickness specified in (2) above;<br />

4. (4) all butt welds in nozzles, communicating chambers, etc., with the nominal thickness at the welded joint that exceeds the<br />

thickness in (2) above or attached to the shell or heads of vessels under (1), (2), or (3) above that are required to be fully<br />

radiographed; however, except as required by UHT-57(a), Categories B and C butt welds in nozzles and communicating<br />

chambers that neither exceed NPS 10 (DN 250) nor 11/8 in. (29 mm) wall thickness do not require any radiographic<br />

examination;<br />

5. (5) all Category A and D butt welds in the shell and heads of vessels where the design of the joint or part is based on a joint<br />

efficiency permitted by UW-12(a), in which case:<br />

(-a) Category A and B welds connecting the shell or heads of vessels shall be of Type No. (1) or Type No. (2) of Table UW-12;<br />

(-b) Category B or C butt welds [but not including those in nozzles and communicating chambers except as required in (4)<br />

above] which intersect the Category A butt welds in the shell or heads of vessels or connect seamless vessel shell or heads<br />

shall, as a minimum, meet the requirements for spot radiography in accordance with UW-52. Spot radiographs required by this<br />

paragraph shall not be used to satisfy the spot radiography rules as applied to any other weld increment.<br />

6. (6) all butt welds joined by electrogas welding with any single pass greater than 11/2 in. (38 mm) and all butt welds joined by<br />

electroslag welding;<br />

7. (7) ultrasonic examination in accordance with UW-53 may be substituted for radiography for the final closure seam of a<br />

pressure vessel if the construction of the vessel does not permit interpretable radiographs in accordance with Code<br />

requirements. <strong>The</strong> absence of suitable radiographic equipment shall not be justification for such substitution.<br />

8. (8) exemptions from radiographic examination for certain welds in nozzles and communicating chambers as described in (2),<br />

(4), and (5) above take precedence over the radiographic requirements of Subsection C of this Division.<br />

Charlie Chong/ Fion Zhang


(b) Spot Radiography. Except when spot radiography is required for Category B or C butt welds by (a)(5)(-b) above, butt<br />

welded joints made in accordance with Type No. (1) or (2) of Table UW-12 which are not required to be fully radiographed by (a)<br />

above, may be examined by spot radiography. Spot radiography shall be in accordance with UW-52. If spot radiography is<br />

specified for the entire vessel, radiographic examination is not required of Category B and C butt welds in nozzles and<br />

communicating chambers that exceed neither NPS 10 (DN 250) nor 11/8 in. (29 mm) wall thickness.<br />

NOTE: This requirement specifies spot radiography for butt welds of Type No. (1) or No. (2) that are used in a vessel, but does<br />

not preclude the use of fillet and/or corner welds permitted by other paragraphs, such as for nozzle and manhole attachments,<br />

welded stays, flat heads, etc., which need not be spot radiographed.<br />

(c) No Radiography. Except as required in (a) above, no radiographic examination of welded joints is required when the<br />

vessel or vessel part is designed for external pressure only, or when the joint design complies with UW-12(c).<br />

Charlie Chong/ Fion Zhang


UG-116 REQUIRED MARKING<br />

(e) When radiographic or ultrasonic examination has been performed on a vessel in accordance<br />

with UW-11, marking shall be applied under the Certification Mark as follows:<br />

1. “RT 1” when all pressure‐retaining butt welds, other than Category B and C butt welds<br />

associated with nozzles and communicating chambers that neither exceed NPS 10 (DN 250)<br />

nor 11/8 in. (29 mm) wall thickness [except as required by UHT-57(a)], satisfy the full<br />

radiography requirements of UW-11(a) for their full length; full radiography of the above<br />

exempted Category B and C butt welds, if performed, may be recorded on the<br />

Manufacturer’s Data Report; or<br />

2. “RT 2” when the complete vessel satisfies the requirements of UW-11(a)(5) and when the<br />

spot radiography requirements of UW-11(a)(5)(-b) have been applied; or<br />

3. “RT 3” when the complete vessel satisfies the spot radiography requirements of UW-11(b);<br />

or<br />

4. “RT 4” when only part of the complete vessel has satisfied the radiographic requirements of<br />

UW-11(a) or where none of the markings “RT 1,” “RT 2,” or “RT 3” are applicable.<br />

<strong>The</strong> extent of radiography and the applicable joint efficiencies shall be noted on the<br />

Manufacturer’s Data Report.<br />

Charlie Chong/ Fion Zhang


Vessel<br />

for a specified service that may<br />

Radiography<br />

include alternative operating conditions<br />

UW-11<br />

UW-51<br />

RT1: Full Radiography<br />

mandatory by code<br />

based on Service,<br />

thickness, toxicity<br />

UW-11(a)1,2,3,4<br />

Extent of<br />

radiography to be<br />

selected as<br />

permitted by code<br />

for conveniences or for desired<br />

joint efficiency factor<br />

UW-51<br />

UW-52<br />

Charlie Chong/ Fion Zhang<br />

RT2: Full<br />

radiography<br />

complying to<br />

UW-11(a) 5<br />

RT3: Spot<br />

radiography<br />

complying to<br />

UW-11(b)<br />

RT4: No<br />

radiography<br />

complying to<br />

UW-11(c)


3.4<br />

communicating chamber<br />

heat-exchanger appurtenance that intersects the shell or heads of the heat<br />

exchanger and forms an integral part of the pressure-containing envelope<br />

EXAMPLES Sump, annular distributor.<br />

Communicating<br />

Chamber<br />

Charlie Chong/ Fion Zhang


3.5<br />

effective surface<br />

outside surface area of the tubes that contributes to heat transfer<br />

3.6<br />

full-penetration weld<br />

welded joint that results in weld metal through the entire thickness of the<br />

components being joined<br />

3.7<br />

heat-exchanger unit<br />

one or more heat exchangers for a specified service that may include<br />

alternative operating conditions<br />

Charlie Chong/ Fion Zhang


3.8<br />

hydrogen service<br />

service that contains hydrogen at a partial pressure exceeding 700 kPa (100<br />

psi) absolute<br />

700 kPa?<br />

Charlie Chong/ Fion Zhang


Hydrogen Service<br />

service that contains<br />

hydrogen at a partial<br />

pressure exceeding 700<br />

kPa (100 psi) absolute<br />

0.7MPa?<br />

Charlie Chong/ Fion Zhang


3.9<br />

item number<br />

purchaser's identification number for a heat-exchanger unit<br />

3.10<br />

nubbin<br />

projection on the flange gasket surface, positioned at the centre of the gasket,<br />

used to concentrate the bolt load<br />

on the gasket<br />

3.11<br />

pressure design code<br />

recognized pressure vessel standard specified or agreed by the purchaser<br />

Charlie Chong/ Fion Zhang


Nubbin<br />

projection on the flange gasket surface, positioned at the centre of the gasket,<br />

used to concentrate the bolt load<br />

Charlie Chong/ Fion Zhang


Nubbin<br />

projection on the flange gasket surface, positioned at the centre of the gasket,<br />

used to concentrate the bolt load<br />

Nubbin<br />

projection on the flange<br />

gasket surface,<br />

positioned at the centre<br />

of the gasket, used to<br />

concentrate the bolt load<br />

Charlie Chong/ Fion Zhang


Nubbin<br />

Double-jacketed gaskets are probably the most commonly used style of gaskets in heat exchanger applications. <strong>The</strong>y are available in virtually any material<br />

that is commercially available in 26-gauge sheet. <strong>The</strong>y are also extensively used in standard flanges where the service is not critical. Since most doublejacketed<br />

gaskets are custom made, there is virtually no limit to size, shape or configuration in which these gaskets can be made.<br />

In some cases nubbins are provided on heat exchanger designs to provide an intermediate seal. This nubbin is normally 1/64" high by 1/8" wide. Experience<br />

has indicated, however, that there is little advantage to this particular design. <strong>The</strong> primary seal is still dependent on the inner lap of the gasket doing the<br />

brute work and the secondary seal, when applicable, would be provided by the outer lap.<br />

Nubbin<br />

projection on the flange<br />

gasket surface,<br />

positioned at the centre<br />

of the gasket, used to<br />

concentrate the bolt load<br />

Charlie Chong/ Fion Zhang


3.12<br />

seal-welded<br />

tube-to-tubesheet joint weld of unspecified strength applied between the<br />

tubes and tubesheets for the sole purpose of reducing the potential for<br />

leakage<br />

3.13<br />

strength-welded<br />

tube-to-tubesheet joint welded so that the design strength is equal to, or<br />

greater than, the axial tube strength specified by the pressure design code<br />

Charlie Chong/ Fion Zhang


4 General<br />

• 4.1 <strong>The</strong> pressure design code shall be specified or agreed by the purchaser.<br />

Pressure components shall comply with the pressure design code and the<br />

supplemental requirements given in this International Standard.<br />

4.2 <strong>Heat</strong>-exchanger construction shall conform to TEMA (8th edition), Class R,<br />

unless another TEMA class is specified.<br />

• 4.3 <strong>The</strong> vendor shall comply with the applicable local regulations specified<br />

by the purchaser.<br />

4.4 Annex A includes some recommended mechanical and design details for<br />

information.<br />

4.5 Annex B provides a checklist that can be used by the purchaser to ensure<br />

that bulletted items in this International Standard are addressed.<br />

4.6 Annex C provides examples of data sheets.<br />

4. 7 Annex D includes a recommended division of responsibility for<br />

completing the data sheet.<br />

Charlie Chong/ Fion Zhang


TEMA<br />

(Mechanical Design)<br />

<strong>Heat</strong>-exchanger construction<br />

shall conform to TEMA (8th<br />

edition), Class R, unless<br />

another TEMA class is<br />

specified.<br />

Charlie Chong/ Fion Zhang<br />

http://www.tema.org/


5 Proposals<br />

5.1 <strong>The</strong> vendor's proposal shall include, for each heat exchanger unit,<br />

completed data sheets such as those given in Annex C or, if a data sheet is<br />

included in the inquiry, a statement indicating complete compliance with that<br />

data sheet.<br />

5.2 Designs that are not fully defined by the nomenclature in TEMA (8th<br />

edition), Section 1, shall be accompanied by sketches that are sufficient to<br />

describe the details of construction.<br />

5.3 If an annular distributor is provided, the vendor shall define the type of<br />

construction proposed.<br />

5.4 <strong>The</strong> vendor shall determine the need for, and if required, include<br />

expansion joints based on all conditions supplied by the purchaser. <strong>The</strong><br />

vendor shall state the type of construction proposed.<br />

5.5 <strong>The</strong> proposal shall include a detailed description of all exceptions to the<br />

requirements of the purchaser's inquiry.<br />

Charlie Chong/ Fion Zhang


5.6 For stacked heat exchangers, the vendor shall supply the following<br />

components unless otherwise specified by the purchaser:<br />

a. bolts, nuts and gaskets for interconnecting nozzles;<br />

b. shims and bolting for interconnecting supports.<br />

5. 7 <strong>The</strong> vendor shall provide a separate quotation for the following items<br />

unless otherwise specified by the purchaser:<br />

a. a test component consisting of a test ring and gland, in accordance with<br />

TEMA (8th edition), Figure E-4.13-2 or equivalent, for each heat<br />

exchanger or group of similar heat exchangers with floating heads;<br />

b. one spare set of gaskets per heat-exchanger unit.<br />

Charlie Chong/ Fion Zhang


Stacked <strong>Heat</strong> <strong>Exchanger</strong>s,<br />

the vendor shall supply the following components unless otherwise specified by the purchaser:<br />

a. bolts, nuts and gaskets for interconnecting nozzles;<br />

b. shims and bolting for interconnecting supports.<br />

Charlie Chong/ Fion Zhang


TEMA- FIGURE E-4.13-2<br />

Test Ring<br />

Floating Tubesheet<br />

Shell Flange- Rear Head End<br />

Packing<br />

Packing Gland<br />

Gaskket<br />

Charlie Chong/ Fion Zhang


Stacked <strong>Heat</strong> <strong>Exchanger</strong>s<br />

Charlie Chong/ Fion Zhang


Stacked <strong>Heat</strong> <strong>Exchanger</strong>s<br />

Charlie Chong/ Fion Zhang


Stacked <strong>Heat</strong> <strong>Exchanger</strong>s<br />

Charlie Chong/ Fion Zhang


Stacked <strong>Heat</strong> <strong>Exchanger</strong>s<br />

Charlie Chong/ Fion Zhang


Stacked <strong>Heat</strong> <strong>Exchanger</strong>s<br />

Charlie Chong/ Fion Zhang


Break<br />

20180528-1043hrs<br />

Charlie Chong/ Fion Zhang


Break<br />

20180528-1043hrs<br />

Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Zhang<br />

20180531 May


有 书 真 幸 福 , 无 事 小 神 仙<br />

Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Zhang


Charlie Chong/ Fion Fion Zhang Zhang

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