TC34 1x2x6-2VSL LIN,LAR,LNG
UsedSpecifications
Description
TC34 1x2x6-2VSL LIN,LAR,LNG
ACD Nikkiso TC34 submersible cryogenic pump, model 59435-1 1x2x6-2VSL, previously operated in LIN, LAR, and LNG service. This unit is rated for 70 GPM at 204 PSIG discharge pressure with a 25 HP motor designed for continuous duty operation in controlled environments. The pump operates at 5950 RPM on 460V, 3-phase power drawing 32 amps.
Technical Specifications
Service: LIN,LAR,LNG
Capacity: 70 Gallons Per Minute (GPM)
HP: 25 Designed for continuous duty operation in controlled environments
Feet: 3.7
Suction Pressure: 10 PSIG
Discharge Pressure: 204 PSIG
Max Suction Pressure: 50 PSIG
RPM: 5950
Phase: 3
Voltage: 460
Amps: 32
Type: Submersible
Service Factor 1.00
Code: H
Design: B
Insulation: F
Max Ambient in Celsius: 0
Inspection, shipping & payment
Terms set by Gas Equipment 4 Sale.
Price on Request
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Seller
Gas Equipment 4 Sale
Waxahachie, TX, United States
Business and location confirmed by Metal Mountain.
Questions buyers ask
What flow and head is this rated for, and at what NPSH?
This pump is rated for 70 GPM at 204 PSIG discharge pressure with a suction pressure of 10 PSIG (maximum suction pressure 50 PSIG). The listing does not specify NPSH required or available—ask the seller for the pump curve showing flow, head, and NPSH characteristics at the 5950 RPM operating speed. Submersible cryogenic pumps typically have low NPSH requirements due to their installation below liquid level, but the actual value depends on impeller design and operating point.
What service has it been in, and what were the running hours?
This unit previously operated in LIN (liquid nitrogen), LAR (liquid argon), and LNG (liquid natural gas) service. The listing does not provide total running hours or service history—ask the seller for operating logs, maintenance records, and whether it was in continuous or intermittent duty.
What should I inspect on a used pump before buying?
Inspect motor windings for moisture intrusion or insulation breakdown (particularly critical given the 0°C maximum ambient rating and cryogenic service), check shaft runout and bearing condition, and examine all seals for deterioration or leakage history. Verify the impeller for erosion or cavitation damage, confirm the discharge head is compatible with your system requirements, and request witness testing at operating temperature if possible. On units that handled LNG, check for any documentation of thermal cycling history and pressure testing to code.
General guidance for this type of equipment. Ask about this specific unit in your inquiry — the seller answers directly.