IPE-TM-300 Vessels
IPE-TM-300-01
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
This procedure describes the Inflection Point Engineering dimensioning practice for vessels and trays for projects specified in metric units.
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.
Clearly identify English units when used (e.g., 18" OD).
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)).
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.
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:
| English | Metric* mm | English | Metric* mm | English | Metric* 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.
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.
Round up overall tangent lengths of vessels and vessel skirt heights to the next higher 100 mm increment.
Specify corrosion allowance in mm as indicated in Section 4.3.
Apply the following guidelines to metric tray dimensions.
| Procedure Number Revised IPE-TM-300-01 Rev 4 Page of 6 |
|---|
| Service: | Service: | Service: | Service: | Service: | Service: | Service: | Service: | Service: | Service: | Service: | Service: | Item Number: 200-V7 | Item Number: 200-V7 | Item Number: 200-V7 | Item Number: 200-V7 | Item Number: 200-V7 | Item Number: 200-V7 | |
| Notes | Notes | |||||||||||||||||
| Item | Item | Quan | Quan | ID of | ID of | Material | Material | Description | Dwg or | Dimensions | Dimensions | Dimensions | Dimensions | Tray | Tray | Tray | (Sheet | (Sheet |
| No | No | Assem | Assem | Vessel | Vessel | Sht No | No | No | No | 2&3) | 2&3) | |||||||
| 1 | 19 | 19 | 1400 | 1400 | TP410 | TP410 | Sieve Trays | Sieve Trays | 5 | 19-20 | 1, 26 | 1, 26 | 1, 26 | |||||
| 2 | 1 | 1 | 14000 | 14000 | TP410 | TP410 | Sieve Trays | Sieve Trays | 5 | 20 | 1, 6, 26 | 1, 6, 26 | 1, 6, 26 | |||||
| W=100 | X=272 | X=272 | Below | |||||||||||||||
| 3 | 1 | 1 | - | - | TP410 | TP410 | Trap | Trap | 3-220 | 20 | ||||||||
| 21-29 | ||||||||||||||||||
| 4 | 5 | 5 | 2200 | 2200 | TP410 | TP410 | Sieve Trays | Sieve Trays | 5 | Odd | 2, 26 | 2, 26 | 2, 26 | |||||
| 22-30 | ||||||||||||||||||
| 5 | 5 | 5 | 2200 | 2200 | TP410 | TP410 | Sieve Trays | Sieve Trays | 5 | Even | 2x, 26 | 2x, 26 | 2x, 26 | |||||
| Below | ||||||||||||||||||
| 6 | 2 | 2 | 2200 | 2200 | TP410 | TP410 | Traps | Traps | 3-280 | 30 | ||||||||
Tray sections shall pass through a 24” ID vessel manway.
Project
| Service: Debutanizer | Service: Debutanizer | Service: Debutanizer | Item Number: 200-V7 | Item Number: 200-V7 |
|---|---|---|---|---|
| Tray Data | Tray Data | |||
| Tray Identification (Tray Numbers) | Top 1-20 | Bottom 21-30 | ||
| Vessel ID, mm | 1400 | 2200 | ||
| Operating Pressure, kg/cm2(g) | 10.34 | 10.69 | ||
| Operating Temperature, C | 72 | 199 | ||
| Structural Design Temperature, C | ||||
| Fluid Description | Hcbn | Hcbn | ||
| Foam Derating Factor | 1.00 | 1.00 | ||
| Vapor -Flow Rate, kg/h | 33688 | 76900 | ||
| Density, kg/m3 | 26.113 | 31.559 | ||
| Liquid -Flow Rate, kg/h | 28005 | 184230 | ||
| Density, kg/m3 | 501.106 | 603.473 | ||
| Viscosity, cP | 0.11 | 0.16 | ||
| Surface Tension, dynes/cm | 5.6 | 7.6 | ||
| Type of Tray | Sieve | Sieve | ||
| For Sieve Trays | ||||
| Weir Height, M, mm | 50 | 65 | ||
| Downcomer Clearance, N, mm | 40 | 60 | ||
| Total Number of Holes | 750 | 1390 | ||
| Hole Diameter, mm | 13 | 13 | ||
| Hole Area/Bubbling Area x 100 | ||||
| Tray spacing, S, mm (for exceptions see Project Specification 301 Vessels) | 600 | 600 | ||
| Notes | ||||
| Tray Layout | ||||
| Number of Passes | 1 | 2 | ||
| A, mm | 215 | 370 | ||
| B, mm | 970 | 535 | ||
| C, mm | 215 | 390 | ||
| D, mm | ||||
| E, mm | ||||
| F, mm | ||||
| G, mm |
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