API 660 Compliant ASME Section VIII Div. 1 Tube Bundle for Removable Installation in Shell & Tube Heat Exchangers

Place of Origin: CHINA
Brand Name: YUHONG
Certification: ASME VIII Div. 1, PED/97/23/CE, TEMA R, TEMA C, TEMA B
Model Number: HEAT EXCHANGER TUBE BUNDLE
Minimum Order Quantity: 1 SET
Price: Negotiable
Packaging Details: Wooden case/ Ply-Wooden Cases with Steel Frames
Delivery Time: 30 - 90 DAYS
Payment Terms: T/T,L/C
Supply Ability: 500 Tons/ Month
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Specifications
Highlight Features

API 660 Compliant Tube Bundle

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ASME Section VIII Div. 1 Heat Exchanger Tube Bundle

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Removable Installation Shell & Tube Heat Exchanger Bundle

Product Description
TUBEBUNDLE FOR API660 SHELL & TUBE HEAT EXCHANGER
ASME-Fabricated Tube Bundles for Refinery, Petrochemical, and Process Heating/Cooling Service

Yuhong Group Co., Ltd. manufactures shell & tube heat exchanger tube bundles in accordance with API 660 and TEMA Class R requirements. Our facility is qualified for ASME Section VIII Div. 1 pressure vessel construction, with NDE and heat treatment capabilities covering carbon steel, alloy steel, stainless steel, duplex, and nickel-base materials.

Product Overview

This tube bundle is the core heat transfer component of a shell & tube heat exchanger, designed for removable or fixed installation within a cylindrical shell. The bundle consists of a tubesheet at one or both ends, a predetermined number of tubes arranged in a specified layout pattern (triangular, square, or rotated square), baffle plates to direct shell-side flow and support the tubes, tie rods with spacers to secure the baffle stack, and optional impingement plate at the inlet nozzle.

Configurations include:
  • Fixed tubesheet - tubesheet welded or bolted to the shell; no differential thermal expansion accommodation; suitable for moderate temperature differences
  • Heat Exchanger tube - each tube, allowing free thermal expansion; fitted with floating head, no expansion joint; removable bundle
  • Floating head - one tubesheet fixed, the other free to move axially; accommodates large thermal differentials and permits full tube cleaning

Each bundle is engineered per the purchaser's process data sheet, with tube count, pass arrangement, baffle spacing, and material selection calculated to meet specified heat duty, pressure drop, and allowable tube vibration margin.

Component Materials and Standards

All materials are specified per ASME Section II and conform to API 660 supplementary requirements. Typical selections are listed below:

Component Standard Material Grades Applicable Specification
Tubes (smooth / low-finned) SA-179, SA-213 TP304L/316L, SA-789 UNS S31803, SB-338 Gr.2, SB-163 UNS N06600 ASTM/ASME tube specification
Tubesheet (fixed / floating) SA-266 Gr.2, SA-182 F304L/F316L, Clad plate (≥3 mm overlay) ASME SA-266 / SA-182 / clad per ASME VIII-1 UW-13
Baffles & Support Plates SA-516 Gr.70, SA-387 Gr.11/22 (Cr-Mo for high T) ASME SA-516 / SA-387
Tie Rods & Spacers SA-193 Gr.B7 / SA-194 Gr.2H, or alloy equivalent ASME SA-193 / SA-194
Impingement Plate Same or compatible with tube material Per exchanger nozzle location

Tube pitch, baffle thickness, and unsupported tube span are calculated per TEMA and API 660 vibration avoidance guidelines, with baffle spacing limited to maintain tube natural frequency above excitation frequencies.

Inspection and Testing Requirements

Each tube bundle is subject to the following inspection and test sequence. Additional NDE (RT, MT, PT, UT) is available per purchaser specification:

Test / Inspection Method Basis / Acceptance
Tube-to-tubesheet joint Expanded + seal welded or strength welded Per ASME VIII-1 App. A; leak test at 1.5× design pressure
Tube-side hydrotest Hydraulic pressure applied to tube pass(es) Hold per ASME UG-99; no pressure drop
Shell-side hydrotest (with test ring for removable bundles) Hydraulic pressure to shell side No visible leakage at joint; test ring bolted per API 660
Dimensional check Measured against approved fabrication drawing Tube pitch, baffle spacing, orientation, pass partition location
NDE - tubes (full length) Eddy current (ET) or internal rotary UT (IRUT) Per ASME Section V; acceptance per purchaser spec
NDE - tubesheet forging UT for lamination Per SA-388 / SA-435
Post-weld heat treatment (PWHT) Furnace or local, as required by thickness/material Per ASME VIII-1 UCS-56 / UHT-56

Fixed tubesheet bundles additionally require shell-side hydrotest with the shell assembled. For U-tube and floating head bundles, the test ring method is employed to verify joint integrity before installation.

Typical Service Applications
Industry Sector Process Unit Tube Bundle Service Conditions
Petroleum Refining Crude preheat trains, hydrotreaters, catalytic reformers 200-450°C; hydrogen/hydrocarbon; up to 20 MPa
Petrochemical Ethylene cracker quench coolers, recycle gas coolers High-temp hydrocarbon; cyclic operation
Chemical Processing Reactor effluent coolers, distillation reboilers, condensers Corrosive or fouling fluids; varying pressure
Oil & Gas Gas dehydration, amine regenerators, lean/rich heat exchangers Wet sour gas; CO₂/H₂S service
Power & Industrial Feedwater heaters, lubrication oil coolers, intercoolers Clean or moderate-fouling water/oil service

The API 660 tube bundle is specified for critical services where reliability, maintainability, and code compliance are mandatory.

Engineering Advantages and Customization
Reliability through traceability.

Every material component is mill-tested and traceable to ASME Section II. Welding procedures are qualified per ASME Section IX, with welders certified for each material group.

Thermal design flexibility.

Tube layout, baffle cut orientation, and pass arrangement are optimized using thermal-hydraulic calculations (e.g., HTRI) to match the required duty within allowable pressure drop limits. For fouling services, wider tube pitch and removable bundles are recommended.

Fabrication precision.

Tube holes are drilled and/or reamed to within tolerance per TEMA standards. Tube ends are expanded and optionally seal-welded to the tubesheet, with expansion depth and torque controlled to prevent tube thinning and ensure consistent joint strength.

Custom options available:
  • Low-finned tubes for increased surface area in gas-phase or viscous-fluid duty
  • Bimetallic tubes for corrosion resistance with cost-effective base material
  • NACE-compliant materials and PWHT for wet sour service
  • Critical service NDE (100% RT of tube-to-tubesheet welds, helium leak testing)
  • Replacement bundles dimensioned to match existing shells with no shell modification
Common Technical Questions
Q: How is tube-to-tubesheet joint tightness verified before bundle installation?
For removable bundles, a hydrostatic test ring with pressure connections is bolted to the tubesheet, and shell-side pressure is applied while the tube side is monitored. This method replicates service loading without requiring the full shell assembly.
Q: What limits the repairability of a tube bundle?
Tube plugging is generally permitted up to 10% of the total tube count without recalculating thermal performance. Beyond that, heat transfer duty degrades and flow distribution across the remaining tubes becomes uneven. Full re-tube or bundle replacement is the recommended course.
Q: Why is flow-induced vibration analysis required for API 660 bundles?
Vibration leads to tube fretting at baffle contact points, fatigue cracking at the tubesheet, and eventual tube failure. API 660 requires the manufacturer to evaluate tube natural frequency, fluid elastic instability, and vortex shedding. Mitigation measures include reduced baffle spacing, increased tube wall thickness, or alternate tube layout.
TEMA Shell and Tube Heat Exchanger Tube Bundle
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