01 · Heat exchangers · With AMI Exchangers, UK

Shell-and-tube heat exchangers, designed to TEMA and ASME.

Custom exchangers and like-for-like replacements for refineries, gas plants, power stations and marine duty. Designed and built in Hartlepool by AMI Exchangers, supplied and supported in the GCC by Petromarsh.

1–1,000+ m²Heat transfer area
R · C · BTEMA classes
10 stepsEnquiry to start-up
TEMA AES · 2 tube passes · cutawayShell side, hotTube side, cooling

Tap a part to see what it does. The red line is the hot shell-side fluid, the blue line is the cooling fluid inside the tubes.

The basics

What a shell-and-tube exchanger is, and how it works.

Two fluids at different temperatures pass each other without mixing. One runs inside a bundle of tubes, the other flows around the tubes inside a pressure shell. Heat moves through the tube walls from the hot fluid to the cold one.

TUBE SIDE

Inside the tubes

Usually the dirtier, more corrosive or higher-pressure fluid, such as seawater or cooling water. Tubes are easier to clean and cheaper to make in special alloys than the whole shell.

SHELL SIDE

Around the tubes

The fluid enters the shell and is steered back and forth across the bundle by baffles. This cross-flow raises turbulence and heat transfer, and the baffles also support the tubes against vibration.

PASSES

One, two or more passes

A pass partition in the channel sends the tube-side fluid down the shell and back again. More passes give higher velocity and better heat transfer, at the cost of more pressure drop.

Why plants choose shell-and-tube

  • Handles high pressure and high temperature that plate units cannot
  • Can be built in almost any metal, from carbon steel to titanium
  • Removable bundles allow cleaning and re-tubing on site
  • Robust, well understood and covered by TEMA, ASME and API codes

When another type is better

  • Clean, low-pressure liquids with a close temperature approach: a plate exchanger is smaller and cheaper
  • No cooling water on site: an air cooler (line 02)
  • Very large duty with tight plot space: compare against compact designs
Types

Build a TEMA type in three letters.

Every shell-and-tube exchanger is named by three letters from the TEMA standard: the front head, the shell, and the rear head. Pick one of each to see what you get, or start from a common type.

Front head

Shell

Rear head

Common types:
AES
Floating head, removable bundle
A
Channel with removable cover. Tubes can be cleaned without disturbing the piping.
E
One-pass shell. The most common shell.
S
Floating head with a split backing ring. The refinery workhorse.

The standard refinery exchanger. The bundle can be pulled for cleaning on both sides, and the floating head handles large temperature differences.

RRefinery class

The heaviest construction, for petroleum and related process duty. Larger corrosion allowances and thicker tubes.

CCommercial class

General process and commercial duty, where conditions are moderate.

BChemical class

Chemical process service, often with stainless or alloy materials.

Materials

Matched to the fluid, not to a catalogue.

Material choice decides how long an exchanger lasts. In the Gulf the usual enemies are seawater, chlorides, hydrogen sulphide and high ambient temperatures.

PartCarbon steelStainless and duplexSpecial alloys
Shell and channelPressure plate and pipeSA-516 Gr 70 · SA-106 Gr B304L, 316L, duplex 2205SA-240 · SA-312Clad plate for corrosive dutyexplosion-bonded cladding
TubesSeamless or weldedSA-179 · SA-214304L, 316L, duplex, super duplexSA-213 · SA-249 · SA-789Titanium, copper-nickel 90/10 and 70/30, admiralty brassSB-338 · SB-111
TubesheetsForgings or plateSA-266 · SA-105 · SA-516Stainless forgingsSA-182Clad tubesheets, naval brass for marineSB-171
GasketsSpiral wound, double-jacketed or solid metal, chosen for pressure, temperature and fluidASME B16.20
Seawater coolingTitanium, copper-nickel or super duplex tubes
Sour gas (H₂S)Materials to NACE MR0175 / ISO 15156
Hot chloridesDuplex or super duplex instead of 316L
Clean hydrocarbonsCarbon steel, the lowest cost
Standards

The codes we design, build and test to.

The datasheet names the code. We follow it, plus your company specification where one applies.

MechanicalTEMA, 10th edition

Construction classes R, C and B, the three-letter type names, tolerances and clearances.

Pressure designASME VIII Div. 1

Pressure vessel design rules for shell, channel and nozzles.

Oil and gasAPI 660 / ISO 16812

Extra requirements for shell-and-tube exchangers in petroleum, petrochemical and gas plants.

Europe and UKPED 2014/68/EU · EN 13445

CE marking for Europe. UKCA under the Pressure Equipment (Safety) Regulations 2016 for the UK.

Materials and weldingASME II · ASME IX

Material specifications, and qualified welding procedures and welders.

InspectionASME V · EN 10204 3.1

Non-destructive testing methods, and certified mill certificates for every pressure part.

Sour serviceNACE MR0175 / ISO 15156

Material limits for equipment exposed to hydrogen sulphide.

FlangesASME B16.5 · B16.47

Nozzle flange ratings and dimensions, matched to your piping class.

Client specsAramco SAMSS · ADNOC · DEP

Company specifications, such as Saudi Aramco 32-SAMSS-007, applied on top of the codes.

How an order runs

From your enquiry to start-up, in ten steps.

Your engineers red-line our drawings, you approve the design twice before production starts, and you can witness the tests. Tap a step to see what happens and which documents you receive.

From AMI Exchangers, Hartlepool

Built in the UK, working in the Gulf.

AMI Exchangers has completed more than 25,000 projects for power, marine, chemical and oil and gas clients. Petromarsh is their exclusive representative in the GCC.

Request a quote

Send us the datasheet, or just the duty.

If you have a TEMA datasheet, send it. If you do not, the items on the right are enough for us to size the exchanger and reply with a proposal.

  • Duty and service, with both fluids named
  • Flow rates on each side
  • Inlet and outlet temperatures
  • Design pressure and temperature
  • Allowed pressure drop
  • Fouling factors, if known
  • Preferred materials and design code
  • Site, delivery date and Incoterms
  • For a replacement: the old nameplate and drawing
  • Nozzle sizes and orientation