Inflection Point Engineering IPE-TM-300 Vessels

Metric Equivalents for Vessels & Trays

IPE-TM-300-01

1. Table of Contents

1. Table of Contents 1

2. Purpose 1

3. General 1

4. General Applications 1

4.1 Dual Dimensioning 1

4.2 Pipe, Nozzles and Manway Sizes 1

4.3 Typical Dimensions 2

5. Vessel Diameters 2

6. Vessel Dimensions Other Than Diameter 3

6.1 Vessel Length 3

6.2 Corrosion Allowance 3

6.3 Tray Dimensions 3

Attachment 1 – 301 Sample 4

Attachment 2 – 307 Item List 5

Attachment 3 – 307 Loading Page 6

2. Purpose

This procedure describes the Inflection Point Engineering dimensioning practice for vessels and trays for projects specified in metric units.

3. General

Generally, English units are used for process design calculations but frequently the customer requires the Schedule A to be specified in metric units.

The Vessel Section of the Basic Engineering Design Questionnaire (BEDQ) gives the customer the opportunity to provide dimensioning instructions to Inflection Point Engineering.

4. General Applications

Clearly identify English units when used (e.g., 18" OD).

4.1 Dual Dimensioning

Dual dimensioning is not a Inflection Point Engineering practice. However, if dual dimensioning is specifically required by the customer, list metric units as primary and English units as secondary contained in parenthesis (i.e., 300 mm (12 inches)).

4.2 Pipe, Nozzles and Manway Sizes

Use English units only without dual dimensioning for specifying pipe, nozzle and manway sizes. However, if the customer specifically requires metric dimensions for pipe and/or manways, use mm. Always specify holes and slots in pipes and distributors in mm regardless of the units chosen for the pipe sizes.

4.3 Typical Dimensions

Use mm for all dimensions with a note on each drawing and specification; i.e., "All dimensions are in mm unless specifically noted otherwise". Do not indicate the abbreviation as “mm” on drawings and/or specifications (e.g., specify 300; not 300 mm). The General Notes sheets of Project Specifications 301 and 307, and the Legend Note of the Piping & Instrument Diagram fulfill this requirement for most situations. Do not use centimeter or meter units.

For dimensions under one inch, round off to the closest mm except for 1/16 of an inch. Above one inch, round off to the closest 5 mm increment and for 12 inches and above, to the closest 10 mm. A few common equivalents are presented below:

EnglishMetric*
mm
EnglishMetric*
mm
EnglishMetric*
mm
1/16"
1/8"
3/16"
1/4"
5/16"
3/8"
1/2"
1.6
3
5
6
8
10
13
3/4"
1"
1-1/2"
2"
3"
4"
5"
19
25
40
50
75
100
125
6"
7"
8"
9"
10"
11"
12"
150
180
200
230
250
280
300

* Use closer equivalents when dimensions are critical. Note that chordal dimensions in trayed columns are excluded from these rounding rules.

5. Vessel Diameters

Use the practices described below for specifying the diameters of vessels when metric dimensions are required. Continuous Catalyst Regenerator (CCR) units are excluded from these rules.

6. Vessel Dimensions Other Than Diameter

6.1 Vessel Length

Round up overall tangent lengths of vessels and vessel skirt heights to the next higher 100 mm increment.

6.2 Corrosion Allowance

Specify corrosion allowance in mm as indicated in Section 4.3.

6.3 Tray Dimensions

Apply the following guidelines to metric tray dimensions.

Procedure Number Revised
IPE-TM-300-01 Rev 4 Page of 6

Attachment 1 – 301 Sample

Attachment 2 – 307 Item List

































































































Service: Service: Service: Service: Service: Service: Service: Service: Service: Service: Service: Service: Item Number: 200-V7Item Number: 200-V7Item Number: 200-V7Item Number: 200-V7Item Number: 200-V7Item Number: 200-V7
NotesNotes
ItemItemQuanQuanID ofID ofMaterialMaterialDescriptionDwg orDimensionsDimensionsDimensionsDimensionsTrayTrayTray(Sheet(Sheet
NoNoAssemAssemVesselVesselSht NoNoNoNo2&3)2&3)
1191914001400TP410TP410Sieve TraysSieve Trays519-201, 261, 261, 26
2111400014000TP410TP410Sieve TraysSieve Trays5201, 6, 261, 6, 261, 6, 26
W=100X=272X=272Below
311--TP410TP410TrapTrap3-22020
21-29
45522002200TP410TP410Sieve TraysSieve Trays5Odd2, 262, 262, 26
22-30
55522002200TP410TP410Sieve TraysSieve Trays5Even2x, 262x, 262x, 26
Below
62222002200TP410TP410TrapsTraps3-28030

Tray sections shall pass through a 24” ID vessel manway.

Attachment 3 – 307 Loading Page

Project

Service: DebutanizerService: DebutanizerService: DebutanizerItem Number: 200-V7Item Number: 200-V7
Tray DataTray Data
Tray Identification
(Tray Numbers)
Top
1-20
Bottom
21-30
Vessel ID, mm14002200
Operating Pressure, kg/cm2(g)10.3410.69
Operating Temperature, C72199
Structural Design Temperature, C
Fluid DescriptionHcbnHcbn
Foam Derating Factor1.001.00
Vapor -Flow Rate, kg/h3368876900
Density, kg/m326.11331.559
Liquid -Flow Rate, kg/h28005184230
Density, kg/m3501.106603.473
Viscosity, cP0.110.16
Surface Tension, dynes/cm5.67.6
Type of TraySieveSieve
For Sieve Trays
Weir Height, M, mm5065
Downcomer Clearance, N, mm4060
Total Number of Holes7501390
Hole Diameter, mm1313
Hole Area/Bubbling Area x 100
Tray spacing, S, mm (for exceptions see Project Specification 301 Vessels)600600
Notes
Tray Layout
Number of Passes12
A, mm215370
B, mm970535
C, mm215390
D, mm
E, mm
F, mm
G, mm