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Fabrication Services — Vessel Fabrication

Columns and Towers

Tray-type and packed-type distillation, absorption, stripping, and fractionation columns — engineered from process simulation through hydrostatic test and fabricated to ASME Section VIII Division 1 & 2.

Overview

Tall vessels engineered for vapor-liquid mass transfer

A column or tower is a tall vertical pressure vessel that brings a rising vapor phase into intimate contact with a descending liquid phase, so components can transfer between the two based on differences in volatility, solubility, or reactivity. Distillation columns separate a liquid mixture by boiling point, using reboiler-generated vapor and condenser reflux. Absorption and stripping columns transfer a target component into or out of a liquid solvent — absorption pulls a component into the liquid, stripping drives it back out, often with heat or steam. Fractionation towers extend the same principle to multiple simultaneous product cuts, common in crude and gas processing trains.

Before a shell course is ever rolled, Fintelius runs process simulation and separation feasibility modeling against the feed composition, corrosivity, fouling tendency, and reaction chemistry — then sizes the shell, internals, and support structure to match.

  • Distillation, absorption, stripping & fractionation service, tray-type or packed-type internals
  • Debutanizer, depropanizer, demethanizer, condensate stabilizer & absorber/stripper configurations
  • Carbon steel, stainless steel (304/316), duplex & clad materials for corrosive service
  • Designed to ASME Section VIII Div. 1 & 2, API RP 520/521 relief sizing, NACE MR0175 for sour service
Process column — fractionation tower fabrication
How It Works

From process simulation to a hydrostatically tested tower

Every column follows the same disciplined path through the shop, whatever its internals or service.

1

Process Simulation & Sizing

Feed composition, corrosivity, fouling tendency, and separation duty are modeled to size the shell diameter, height, and internals.

2

Shell Rolling & Course Fabrication

Plate is rolled into shell courses and joined by longitudinal and circumferential welds to the design diameter and wall thickness.

3

Welding, NDE & PWHT

Welds are radiographed and ultrasonically tested; thick-walled sections undergo post-weld heat treatment to relieve residual stress.

4

Internals Installation

Trays, packing supports, distributors, and downcomers are installed and leveled to the process design.

5

Hydrostatic Testing & Dispatch

The complete vessel is hydrostatically tested, coated, and prepared for shipment — in sections for tall towers where required.

Column Types

Matched to the separation duty

DC

Distillation Column

Separates a liquid mixture into components by boiling point, using reboiler vapor and condenser reflux — the core unit operation of a fractionation train.

AS

Absorber & Stripper Column

Transfers a target component between a gas and liquid solvent — absorption towers for amine/glycol gas treating, strippers to regenerate the solvent.

FT

Fractionation Tower

Multi-product distillation with several side draws, producing a range of cuts simultaneously — debutanizers, depropanizers, and demethanizers.

Internals Technology

Trays or packing — chosen for the duty, not by default

Trays generally handle higher liquid loads and are easier to inspect; packing offers lower pressure drop and higher separation efficiency per unit of height.

01

Sieve Trays

Simple perforated plates — low cost, good capacity, but less turndown flexibility than valve trays.

02

Valve Trays

Moving caps open with vapor flow, giving better turndown and operating flexibility across varying loads.

03

Bubble Cap Trays

The most flexible turndown of any tray type, at higher cost and pressure drop — specified for legacy or highly variable-load service.

04

Structured Packing

Corrugated metal or plastic sheet packing — low pressure drop and high efficiency, favored in vacuum towers.

05

Random (Dumped) Packing

Raschig rings, Pall rings & Berl saddles — cheaper and more robust in fouling or corrosive service, at lower efficiency than structured packing.

06

Packing Supports & Redistributors

Support plates, hold-down grids, and liquid redistributors installed every several bed heights to prevent channeling.

Core Equipment & Mechanical Design

What a tall vertical vessel demands

Wind, seismic, and thermal loading make column mechanical design a discipline of its own.

01

Shell & Head Rolling

Plate rolling and forming to the design diameter, course length, and wall thickness set by pressure and corrosion allowance.

02

Skirt Support Design

Skirt and anchor bolt design engineered for combined dead load, wind, seismic, and thermal loading on tall towers.

03

Nozzle & Manway Fabrication

Feed, reflux, draw, vent, and instrumentation nozzles with reinforcement pads; manways for internal access.

04

Davits & Lifting Lugs

Maintenance-access hardware supporting tray and internals servicing without external crane dependency.

05

Wind & Seismic Load Analysis

Overturning moment and base shear analysis for tall vertical vessels, feeding directly into skirt and shell design.

06

Post-Weld Heat Treatment

Stress-relief heat treatment for thick-walled shell sections per code requirements.

07

Radiography & Ultrasonic NDE

Weld integrity verification across longitudinal and circumferential shell seams before hydrostatic test.

08

Hydrostatic Test Rigs

Full-vessel pressure testing to design specification prior to dispatch.

09

Insulation & Coating

Insulation for energy conservation, personnel protection, or freeze protection, plus protective coating systems.

Design Specifications

Capability at a glance

Column Types
Tray-type & packed-type; distillation, absorption, stripping & fractionation
Configurations
Debutanizer, depropanizer, demethanizer, absorber, stripper, condensate stabilizer
Governing Codes
ASME Section VIII Div. 1 & 2
Relief & Safety
Sized per API RP 520/521
Sour Service
NACE MR0175 / ISO 15156 compliant construction available
Materials
Carbon steel, stainless steel 304/316, duplex, clad materials
Tray Spacing
Typically 18–24 in., sized against flooding & capacity
Diameter Range
Small strippers under 0.5 m up to large fractionators over 6 m
Height Range
Compact skid columns up to tall distillation towers exceeding 60–90 m
Operating Pressure
Deep vacuum service up to high-pressure gas processing duty
Testing
Radiography, ultrasonic testing & full hydrostatic test
Delivery Format
Shop-fabricated, tested vessel — complete or in sections for tall towers
Applications

Where our columns and towers go to work

CD

Crude Distillation Units

Primary fractionation of crude oil into naphtha, kerosene, diesel, and gas oil cuts in refinery operations.

GP

Gas Processing

Amine absorption & regeneration towers and glycol dehydration columns removing acid gas and water vapor from produced gas.

PC

Petrochemical Fractionation

Debutanizer, depropanizer & demethanizer columns splitting NGL streams into individual product components.

CS

Condensate Stabilization

Stabilizer columns setting condensate vapor pressure to meet pipeline and storage specifications.

BF

Biofuel & Chemical Processing

Separation and purification columns for biofuel production and general chemical processing operations.

ES

Environmental Scrubbers

Absorption-based scrubbing towers for emissions control and environmental compliance.

Need a column or tower engineered for your separation duty?

Send us your feed composition, separation requirements, and site constraints for a fabrication proposal.

Request a Proposal