Technical Analysis: Application of 317LMN Stainless Steel in Palm Oil Fractionation II Units

创建于06.11

Technical Analysis: Application of 317LMN Stainless Steel in Palm Oil Fractionation II Units

Abstract
This paper examines the strategic implementation of 317LMN (UNS S31726) austenitic stainless steel in palm oil fractionation II units. Through comparative analysis with conventional 304L/316L alloys, we demonstrate how 317LMN’s superior corrosion resistance and mechanical properties resolve chronic equipment failures while delivering 34% lower lifecycle costs. Data from field deployments confirm 8–10-year service intervals without corrosion-related downtime.
1,Critical Function of Fractionation II Units in Palm Oil Production
Fractionation II constitutes the core refining stage where crude palm oil (CPO) undergoes thermal separation into distinct triglyceride fractions:
  • Input:
CPO with 3–5% FFA (free fatty acids), 0.1–0.3% chloride contaminants
  • Process:
Multi-stage crystallization at 50–55°C → Heating to 220–260°C → Vacuum distillation
  • Output:
    • Olein (24°C melting point): Liquid frying oils
    • Stearin (44°C+ melting point): Solid fats for cosmetics/confectionery
Operational Significance:
  • Determines final product functionality (melting profile, oxidative stability)
  • Processes 95% of global palm oil output (2024: 78 million tonnes)
  • Energy intensity: 85–110 kWh/tonne, making equipment reliability critical

2. Process-Specific Challenges for Construction Materials

2.1. Corrosion Mechanisms in Fractionation II

Threat Source
Impact on Materials
Critical Zones
Free Fatty Acids
Uniform thinning (0.5–2 mm/year)
Evaporators, reboilers
Chlorides
(50–500 ppm)
Pitting/crevice corrosion
Condenser tubes, weld joints
Thermal Cycling
Stress corrosion cracking (SCC)
Flange connections, pump volutes

2.2. Key Material Requirements:

  • Temperature Resistance: Sustained 260°C + thermal shocks
  • Corrosion Resistance: PREN ≥ 30 for Cl⁻ > 200 ppm environments
  • Mechanical Integrity: Yield strength > 200 MPa at 260°C

3. Limitations of 304L/316L in Service

3.1. Documented Failure Modes:

  • 304L (PREN=19):
    • Severe pitting in condensers (Cl⁻ > 100 ppm)
    • SCC cracks in flange necks after 12–18 months
  • 316L (PREN=26):
    • Organic acid corrosion > 0.8 mm/year at 220°C
    • Weld decay requiring post-weld heat treatment

3.2. Operational Costs of Conventional Alloys:

Failure Mode
Downtime Frequency
Cost Impact (Per Incident)
Heat exchanger leaks
Every 2–3 years
$120k (repair) + $400k (production loss)
Pump replacement
Annually
$65k (part) + $200k (cleanup)
Product contamination
--
$2M+ (recall/penalties)

4. 317LMN: Performance Advantages & Economic Rationale

4.1. Material Science Superiority:

  • Enhanced PREN (≥36): Mo (4.5%) + N (0.15%) synergy
  • Critical Pitting Temperature: 55°C vs. 25°C for 316L
  • SCC Threshold: 90°C in 25% NaCl vs. 60°C for 316L

4.2. Field Performance Data (Malaysian Plant, 2021–2024):

Parameter
316L
317LMN
Improvement
Corrosion rate
0.45 mm/year
0.03 mm/year
15X
Maintenance interval
3 years
8+ years
167%
Total cost/10-years
$3.2M
$1.8M
44% savings

5. Metallurgical Profile of 317LMN

5.1. Composition (ASTM A312):

Element
Range (wt%)
Function
Cr
18.0–20.0
Passive film stability
Ni
13.5–17.5
Austenite phase retention
Mo
4.0–5.0
Chloride resistance
N
0.10–0.20
Strength boost, pit healing

5.2. Mechanical Properties at 260°C:

Property
317LMN
316L
Advantage
Yield Strength
248 MPa
172 MPa
+44%
Creep Resistance
120 MPa
85 MPa
+41%
Elongation
42%
35%
+20%

6. Kherlyn’s Integrated Supply Solution for 317LMN Systems

6.1. End-to-End Quality Control:

  • Raw Material Stage:
    • VOD refining (Vacuum Oxygen Decarburization) achieving:
      • O ≤ 30 ppm | S ≤ 0.003% | N=0.15±0.02%
    • ASTM A1063-compliant slab ultrasonic testing
  • Manufacturing Process:
    • PQF® (Premium Quality Forging) for seamless pipes (OD 12–24")
    • Solution annealing: 1120°C ±10°C, WQ < 60 sec
    • Electrolytic polishing (Ra ≤ 0.8 μm)

6.2. Third-Party Verified Compliance:

  • ITP (Inspection Test Plan):
    • Stage 1: PMI (Positive Material Identification) – Full spectrometer check
    • Stage 2: ASTM A262 Practice E – Intergranular corrosion test
    • Stage 3: Hydrotest at 1.5X design pressure
  • Certifications:
    • ASME B31.3 Process Piping
    • PED 2014/68/EU Annex I
    • Halal/Kosher material compliance

6.3. Prefabricated Piping Package Advantages:

Component
Kherlyn’s Solution
Industry Standard
Pipes
OD tolerance ±0.2%, WT +15%/-10%
±0.5%, WT ±12.5%
Fittings
CNC-machined from forged blanks
Cast/pressed
Flanges
RT (Radiographic Testing) on all welds
Spot RT
Delivery Cycle
12 weeks (ex-works)
18–24 weeks
Conclusion
The adoption of 317LMN stainless steel in palm oil fractionation II units resolves the fundamental conflict between corrosion resistance and high-temperature strength. Kherlyn’s vertically integrated supply model—combining precision metallurgy, digital traceability, and third-party validated quality—reduces lifecycle costs by 34% while eliminating food contamination risks. As global palm oil capacity expands toward 95 million tonnes by 2028, 317LMN represents the new benchmark for sustainable refining infrastructure.

Contact
Leave your information and we will contact you.

Copyright ©️ 2022, NetEase Zhuyou(and its affiliates as applicable). All Rights Reserved.

Company

Collections

About

Follow us

Team&Conditions

Work With Us

Featured Products

News

LinkedIn

All products

Shop

Facebook

Twitter