Silicon Carbide Heat Exchanger Tubes for Drawing-Based Supply

Silicon carbide tubes transfer heat between tube-side and shell-side media. ADCERAX supports replacement-tube and OEM projects with 14 and 19 mm OD reference groups, material-route selection and drawing-based interface review.

Catalogue No. AT-THG-HRQ001
Material SSiC / RSiC
Heat-transfer role Tube-wall heat exchange for cooling, condensation and heat recovery
Fit and sealing Bore, wall and tube ends matched to the tube sheet and seals
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Drawing & Process Review

Silicon Carbide Tubes for Heat-Exchange Assemblies

Silicon carbide heat exchanger tubes are SiC ceramic tubes used as the heat-transfer components inside a tube bundle, a shell-and-tube exchanger or a custom heat-recovery assembly. Heat passes through the tube wall between the tube-side and shell-side media, and the tube wall also keeps the two media separated.

The tube itself is one component in that assembly. The SiC material route, the tube bore and wall, the tube ends, the tube sheet and the seals together form the media boundary, so each of these is defined on the component drawing rather than assumed from the material.

Dimensions of Silicon Carbide Heat Exchanger Tube

Calculation of sic heat exchanger tube area (㎡) and length with an outer dia of 14mm
Item No. Heat Exchanger Mold Quantities of Heat Exchanger L=3000mm L=2500mm L=2000mm L=1500mm L=1000mm
AT-THG-HRQ001 DN100 7 0.92 0.77 0.62 0.46 0.31
AT-THG-HRQ002 DN150 0.1 0.15 0.2 0.2 0.3 0.15
AT-THG-HRQ003 DN200 31 4.09 3.41 2.73 2.05 1.36
AT-THG-HRQ004 DN250 0.1 0.15 0.2 0.2 0.3 0.15
AT-THG-HRQ005 DN300 76 10.03 8.36 6.69 5.01 3.34
AT-THG-HRQ006 DN350 0.1 0.15 0.2 0.2 0.3 0.15
AT-THG-HRQ007 DN400 140 18.47 15.39 12.32 9.24 6.16
AT-THG-HRQ008 DN450 0.1 0.15 0.2 0.2 0.3 0.15
AT-THG-HRQ009 DN500 230 30.35 25.29 20.23 15.17 10.12
AT-THG-HRQ010 DN600 0.1 0.15 0.2 0.2 0.3 0.15
AT-THG-HRQ011 DN700 454 59.90  49.92 39.94 29.95 19.97
AT-THG-HRQ012 DN800 0.1 0.15 0.2 0.2 0.3 0.15
AT-THG-HRQ013 DN900 769 101.47 84.56 67.64 50.73 33.82
AT-THG-HRQ014 DN1000 0.1 0.15 0.2 0.2 0.3 0.15
AT-THG-HRQ015 DN1200 1393 183.80  153.17 122.53 91.90  61.27

 

Calculation of sic heat exchanger tube area (㎡) and length with an outer dia of 19mm
Item No. Heat Exchanger Mold Quantities of Heat Exchanger L=3000mm L=2500mm L=2000mm L=1500mm L=1000mm
AT-THG-HRQ0016 DN100 7 1.25  1.04  0.84  0.63  0.42 
AT-THG-HRQ0017 DN150 13 2.33  1.94  1.55  1.16  0.78 
AT-THG-HRQ0018 DN200 22 3.94  3.28  2.63  1.97  1.31 
AT-THG-HRQ0019 DN250 38 6.80  5.67  4.54  3.40  2.27 
AT-THG-HRQ0020 DN300 55 9.85  8.21  6.57  4.92  3.28 
AT-THG-HRQ0021 DN350 73 13.07  10.89  8.71  6.54  4.36 
AT-THG-HRQ0022 DN400 96 17.19  14.33  11.46  8.60  5.73 
AT-THG-HRQ0023 DN450 126 22.56  18.80  15.04  11.28  7.52 
AT-THG-HRQ0024 DN500 151 27.04  22.53  18.03  13.52  9.01 
AT-THG-HRQ0025 DN600 230 41.19  34.32  27.46  20.59  13.73 
AT-THG-HRQ0026 DN700 316 56.59  47.16  37.72  28.29  18.86 
AT-THG-HRQ0027 DN800 421 75.39  62.82  50.26  37.69  25.13 
AT-THG-HRQ0028 DN900 526 74.19  78.49  62.79  47.10  31.40 
AT-THG-HRQ0029 DN1000 649 116.22  96.85  77.48  58.11  38.74 
AT-THG-HRQ0030 DN1200 955 171.01  142.51  114.01  85.51  57.00 

 

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Silicon Carbide Material Performance by Route

The values below are material-level references from the ADCERAX silicon carbide grade data sheet, listed per manufacturing route with the condition at which they are stated. They support material selection. The tube specification itself comes from the component drawing, the surface condition, the operating media and the agreed tests.

Property Unit SSiC (AD-SIC-SS) RBSiC / SiSiC (AD-SIC-RB)
SiC content wt% ≥99 85 nominal
Residual free silicon wt% No silicon-infiltrated free phase 15 nominal
Bulk density g/cm³ 3.10 typical ≥3.02
Apparent open porosity vol% <0.1 ≤0.1
Flexural strength MPa 380 250 at 20 °C; 280 at 1200 °C
Compressive strength MPa ≥2600 Not stated
Young's modulus GPa 420 330 at 20 °C; 300 at 1200 °C
Poisson's ratio — 0.16 Not stated
Thermal conductivity W/(m·K) 100–120 at room temperature 45 at 1200 °C
Application-temperature ceiling °C 1600 1380

SSiC, RSiC and RBSiC: Which SiC Route for Your Tubes

All three routes are silicon carbide, but they differ in what fills the space between the SiC grains, and that difference is what decides media compatibility.

SSiC — pressureless-sintered silicon carbide
Dense, SiC ≥99 wt%, no silicon-infiltrated free phase, open porosity <0.1 vol%. The usual starting point for tubes that hold a media boundary. Dense is not gas-tight as a component — the tube, tube sheet and seals hold the leak rate.

RSiC — recrystallized silicon carbide
Porous. Useful where high temperature and thermal cycling matter more than a tight boundary, but process liquid can enter the pore structure. No numeric grade data exists for this route, so porosity, hot strength, permeability and acceptance are confirmed for the specific tube ordered.

RBSiC / SiSiC — reaction-bonded, silicon-infiltrated
Dense, with roughly 15 wt% nominal free silicon. That phase belongs in the compatibility review: media that attack silicon can attack the tube through it even where the SiC skeleton is unaffected.

NBSiC — nitride-bonded silicon carbide
Porous SiC skeleton with a silicon nitride bonding phase, around 12 vol% porosity. A furnace material, not a media boundary — not used as a gas-tight heat-exchange barrier without component-level permeation or leak-rate acceptance.

No single corrosion rate, permeability figure or service life covers all four routes, and a conclusion from one does not transfer to another. Send both-side media with concentration, temperature, solids and cleaning method, and the route is selected against that.

Failure Modes and Service Life of SiC Heat Exchanger Tubes

Silicon carbide tubes fail by cracking and interface problems, not by general thinning. Knowing the pattern changes what the replacement enquiry needs.

  • Thermal-shock cracking
    Cracks near an end or support after a temperature excursion point to ΔT and ramp rate. Tolerance depends on route, wall thickness, both-side heat transfer, supports, end restraint and pre-existing defects — there is no single allowable ΔT. Agree ramp rates and cycle acceptance for the specific tube where cycling is severe.
  • Mechanical and assembly-induced cracking
    Chips and cracks at ends and contact faces, traceable to point loading during handling, hard metal contact, misalignment at the tube sheet, seal over-compression or a restrained thermal expansion path. Support along the length; stay within the drawing's clamping load.
  • Erosion at high-velocity zones
    Material loss at entry points and high-velocity bends where flow carries solids, crystals or dust. Check these zones specifically; particle size, concentration, velocity and impact angle drive the rate.
  • Media attack through the structure
    In porous routes: process liquid entering the pore structure. In silicon-infiltrated routes: attack on the free silicon phase. Both are route-specific — see 06B. Discolouration or roughness change warrants inspection, not a log note.
  • Seal and interface leakage
    Often read as tube failure when the tube is intact. Confirm whether the leak path is through the ceramic or around it before ordering replacements.

Packaging Process for Silicon Carbide Heat Exchanger Tubes

Silicon Carbide Heat Exchanger Tubes are secured using reinforced wooden crating to protect the module during long-distance international transport. Each unit is wrapped with multi-layer moisture-barrier film and fixed onto a vibration-resistant wooden base to prevent structural stress. The exterior crate is further sealed and braced to ensure safe handling during loading, unloading, and maritime shipment.

ADCERAX® Packaging of Silicon Carbide Heat Exchanger Tubes

Where Silicon Carbide Heat Exchanger Tubes Are Used

These four duties cover most SiC tube enquiries. In each case the operating data listed is what the material route and the tube geometry are selected against.

  • Corrosive Chemical Cooling and Condensation

    Cooling and condensation duties where acids, halogen-containing media or oxidising compounds shorten the life of metal heat-transfer parts, and where the tube wall has to keep the two media apart. For the review, specify both fluids with their concentrations and impurities, the temperatures, the pressure condition on each side and whether condensation occurs, then the SiC route is selected against that chemistry rather than against acid service in general.

  • Acid Pickling and Metal Surface Treatment Lines

    Pickling and surface-treatment circuits, where tubes can see chloride-rich acids, suspended solids and continuous recirculation. The hard SiC surface helps against wall attack and erosion, but the useful review needs the acid blend, the working temperature, the flow velocity, the particle content and the cleaning cycle, because erosion at high-velocity zones is driven by the solids and the velocity rather than by the acid alone.

  • Flue-Gas Heat Recovery in Furnaces and Kilns

    Furnace and kiln heat-recovery duties with hot gas, dust, thermal cycling and corrosive condensates. Here the thermal cycle usually governs: specify the gas chemistry, where condensation occurs, the dust loading, the ramp rates and hold times, and the support and seal arrangement, since support spacing and end restraint decide how the tube carries a temperature gradient.

  • Waste-Acid Recovery and Environmental Process Equipment

    Waste-acid recovery, corrosive gas treatment and environmental process equipment, where heat has to be moved while the boundary between the two media holds. Specify the exposure on both sides, the expected fouling, the cleaning method and the media-boundary requirement. ADCERAX can review drawings or existing equipment interfaces for replacement, retrofit or new-equipment supply.

Operational Guidance for ADCERAX Silicon Carbide Heat Exchanger Tubes

Silicon carbide heat exchanger tubes are used in corrosive heat-exchange systems where chemical compatibility, thermal stability and abrasion resistance are critical to equipment reliability. Application suitability should be reviewed according to process media, temperature, pressure, flow velocity, particle content, cleaning method and sealing design.

  • At receipt

    1. Check drawing revision against what was ordered
    2. Confirm tube identity and quantity
    3. Measure key dimensions and inspect ends and sealing faces
    4. Keep inspection records with the batch

  • During assembly

    1. Support along the length; avoid point loading and hard metal contact
    2. Check alignment into tube-sheet holes and seal compression against the drawing
    3. Confirm the arrangement allows the thermal movement the design assumes — a restrained expansion path loads the ceramic

  • At start-up

    1. Follow the equipment owner's operating procedure
    2. Ramp rates, hold times and pressure limits belong to that procedure, not to a fixed SiC sequence

  • In service

    1. Track temperatures, pressure difference, flow and fouling
    2. Note leakage and any change in cleaning behaviour
    3. Base cleaning intervals on actual fouling rate, not a fixed calendar
    4. When a tube is removed, record the operating observation with it — that pairing is what makes the next replacement enquiry accurate

FAQ: Silicon Carbide Heat Exchanger Tube Selection

  1. Q: When should I choose silicon carbide heat exchanger tubes instead of metal tubes?
    A: When metal tubes corrode, pit, scale or contaminate the product in acid, halogen-containing or abrasive media, and the cost of unplanned replacement outweighs the higher component cost. The comparison is specific to your media and temperatures — send both-side chemistry and operating conditions and the review will say whether a SiC route fits.
  2. Q: Can SiC heat exchanger tubes be used with HF, HCl or mixed acids?
    A: Often yes, but it is reviewed case by case against the specific SiC route, concentration, temperature, pressure and cleaning method. The silicon-infiltrated route needs particular attention: its residual free silicon phase can be attacked where the SiC skeleton would not be.
  3. Q: What information is needed for a tube quotation?
    A: Send what you already have: a drawing, sketch, measured dimensions or photographs of the old part; the AT reference if one is relevant; replacement or OEM; quantity and whether a sample is needed first; the media, temperatures and pressure you know. ADCERAX will organise the review and tell you what is still needed.
  4. Q: How do tube size and wall thickness affect the exchanger?
    A: OD, bore, wall and length set the heat-transfer area, flow resistance and pressure drop, and the wall also carries the mechanical and thermal load. There is no single best wall thickness — it is balanced against thermal duty, pressure difference, support spacing and installation constraints. For a replacement tube, match the existing drawing rather than re-optimise.
  5. Q: Are SiC heat exchanger tubes suitable for flue-gas recovery?
    A: Yes, where hot gas, dust, thermal cycling and corrosive condensates are present. The review needs gas temperature and chemistry, where condensation occurs, dust loading, flow velocity, ramp rates and the seal and support arrangement — the thermal cycle and support spacing usually govern rather than the material.
  6. Q: How can a damaged old tube help identify a replacement?
    A: Record the overall tube, each end and the damaged area separately, and label which measurements come from intact surfaces and which from worn or chipped areas. That is what separates design dimensions from damage. An original drawing, or an intact tube from the same position, resolves it fastest.
  7. Q: How should replacement tubes from different installation positions be identified?
    A: Group them by installation position and drawing revision, give each group its own quantity, and keep each group's photographs and measurements together. Tubes from different positions often differ at the ends or in length even when the bodies look identical — a single mixed quantity is the most common cause of a wrong delivery.
Silicon carbide heat exchanger tube customization diagram showing length, diameters, wall thickness, and end machining details

Custom Silicon Carbide Heat Exchanger Tubes to Drawing

What can be varied
ADCERAX publishes 14 and 19 mm OD groups. Other diameters, lengths, end profiles and surface finishes are reviewed against the drawing. Achievable tolerance depends on the dimension and the length — it is not a single figure across the part.

Interface matching
For a replacement, the tube-sheet, support and sealing geometry is read from the existing equipment. For an OEM build it is agreed with the exchanger designer, including how much thermal movement the arrangement has to allow.

Supply programme
Replacement, OEM prototype, small batch or repeat order — each sets a different drawing revision, inspection scope and packaging. Freezing the revision is what lets a later order be supplied against the same approved specification without re-review.

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