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L-tert-leucine is mainly produced by chemical synthesis, enzymatic catalysis, and fermentation. Among them, enzymatic methods are the most widely used in industry due to high optical purity, environmental friendliness and low cost.

1. Chemical Synthesis Methods

(1) Strecker Reaction + Chiral Resolution

  • Raw materials: pivalaldehyde, NaCN, ammonia
  • Process:
    1. Strecker reaction to form racemic DL‑tert‑leucine
    2. chiral resolution using chiral acids (tartaric acid, dibenzoyl tartaric acid)
    3. purification to obtain L‑tert‑leucine
  • Disadvantages: low yield (<50%), highly toxic cyanide, heavy waste, high cost

(2) Asymmetric Strecker / Silylcyanation

  • Uses chiral auxiliaries (L-phenylglycinol) and chiral catalysts
  • Can directly obtain chiral products without resolution
  • Disadvantages: expensive catalysts, complex systems, high environmental pressure

(3) Asymmetric Hydrogenation of Keto Acids

  • Substrate: trimethylpyruvic acid
  • Catalysts: chiral Rh/Ru complexes (BINAP, DuPhos)
  • Disadvantages: high pressure, heavy metal residues, expensive ligands

2. Enzymatic Catalysis (Industrial Mainstream)

(1) Reductive Amination by Leucine Dehydrogenase (LeuDH)

  • Substrate: trimethylpyruvic acid + ammonia
  • Enzyme: L-leucine dehydrogenase (LeuDH)
  • Coenzyme regeneration: coupled with formate dehydrogenase (FDH) or glucose dehydrogenase (GDH)
  • Advantages:
    • ee >99%, conversion rate 95–98%
    • mild conditions, atmospheric pressure, no heavy metals
    • low cost with whole-cell biocatalysis
  • This is the dominant industrial route worldwide.

(2) Transaminase Method

  • Substrate: trimethylpyruvic acid with amino donors (L-alanine, L-glutamate)
  • No coenzyme needed, single-enzyme system
  • Limitations: substrate inhibition, moderate conversion

(3) Multi-enzyme Coupling System

  • Combined use of hydroxy acid dehydrogenase and LeuDH
  • High substrate concentration, low inhibition, self-sufficient coenzyme cycle

3. Fermentation Method (Under Development)

  • Uses engineered strains: Escherichia coli, Corynebacterium glutamicum, etc.
  • Constructs biosynthetic pathways for direct fermentation from glucose
  • Current status: low titer, long cycle, difficult purification
  • Future trend: promising for ultra-low-cost production via synthetic biology

4. Comparison of Production Methods

Method Advantages Disadvantages Optical Purity Industrial Status
Chemical Resolution Low raw material cost, mature Low yield, toxic, polluting ~98% Gradually phased out
Asymmetric Chemistry Good stereoselectivity Expensive catalysts, heavy metals 95–98% Small-scale only
LeuDH Enzymatic Method High ee, green, scalable Enzyme stability required >99% Mainstream
Transaminase Method No coenzyme needed Substrate inhibition 98–99% Pilot scale
Fermentation Ultra-low raw material cost Low titer, long cycle >99% R&D stage

5. Typical Industrial Process (Enzymatic Route)

  1. Preparation of trimethylpyruvic acid solution
  2. Whole-cell biocatalysis (engineered LeuDH + FDH strain)
  3. Cell removal and filtration
  4. Decolorization, concentration and pH adjustment
  5. Crystallization, centrifugation and drying
  6. Final product: L‑tert‑leucine (ee >99%)

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