1. Introduction Application of β-glucan

4. Conclusion

High Pressure Homogenizer (HPH, Nano Disperser, ILSHIN AUTOCLAVE)

In the HPH process, the pressure and the number of passes increases makeviscosity and molecular weight decrease without any acid/alkali solution (GreenChemistry).

The FT-IR spectra indicated no obvious modification of chemical structure ofpolymer before and after HPH treatment.

HPH has been shown to be a valid tool to reduce molecular weight of naturalpolymer (polysaccharides structure).

Facile depolymerization process of β-glucan

Using High Pressure Homogenizer

Jun Hee Choa, Taeyoung Kima, Yun Hye Yeona, Hyun Hyo Kima

aDepartment of Research & Development, ILSHINAUTOCLAVE CO. #835 Taplipdong, Yuseonggu, Daejeon 305-510, Korea

2. Experimental

ExperimentalLarge Molecular Weight

5 %(w/v) β-glucan Solution

3. Results & Discussion

Shear Force Cavitation

Entanglement and stretch

Smaller FragmentHigh Molecular Weight

PolymerDepolymerization

Process Method Advantage Disadvantage

Physical

(Radiation)

Ultrasonic • No Waste (Acid/Alkali), No-residues• Long Time Process

• Process Noise

E-beam, γ-Ray • No Waste (Acid/Alkali), No-residues• Dangerous Process

• High Cost

Chemical

Acidic hydrolysis

• High Solubility

• High Efficiency of Depolymerization

• Acid waste water

• Complex Process

Phosphorylation

Sulfation

• Enhancement of Solubility and

Functionality• Low Efficiency

BiologicalEnzymatic hydrolysis

• Selective Decomposition

• High Efficiency of Depolymerization

• High Cost

• Inefficiency

Problems

High Viscosity

&

Large Molecular

Weight

Method of Depolymerization

Plunger

Fluid inlet

Fluid outlet

Hydraulic motive cylinderPlunger seal

Alternatingmotion

High pressure Intensifier

Nozzle Chamber

• Shear Force

• Cavitation

• Impact Force

Inlet

High Pressure Pump

Pressure Gauge

Nozzle Chamber

High Energy

Outlet

Inlet Shear & Cavitation Zone

Impact Zone Outlet

Inlet

Pressure (bar) 500 1000 1500 2000 2500

Fluid velocity (m/sec) 313 442 542 626 700

Inlet

Outlet

Outlet

Impact Zone

Shear & Cavitation Zone

Shear & Cavitation Zone

Impact Zone

Fluid Velocity (Sound Speed: 340 m/s)

Low Molecular Weight

5 %(w/v) β-glucan Solution

- Natural Polymer: β-glucan

- Solvent: D.I Water

- Nano Disperser: NLM 100

Operating Pressure (bar) 200 – 1500

Max. Flow Rate (ml/min) 100

Pump System Motor Driven

Dimension (mm) 300*450*300

Weight (kg) 30

Viscosity(5 %(w/v) β-glucan) Molecular Weight FT-IR Spectrum

• HPH treatment produces significant changes in the viscosity and molecular weight of the β-glucan solution.

• As the pressure and the number of pass increases, the polymer solution shows a significant decrease of viscosity and molecular weight.

• High Depolymerization Effect, Short Process Time

and No Waste Water (Green Chemistry)

- β-glucan structure

Cosmetic Food Drug

TextileDrug Delivery System

Environment

UV-Vis

XRD

Characterization

- Viscometer

- Gel Chromatograph

- FT-IR

- UV-Vis

- XRD

• The intensity characteristics of the

peaks tend to decrease with

increasing numbers of passes under

high pressure homogenization.

• A decrease in crystallinity occurs

due to the destruction of the crystal

structure of chitosan as a result of

the cleavage of the glycosyl bonds

200 250 300 350 400 450

Ab

so

rba

nc

e

Wavelength (nm)

5 Passes

3 Passes

1 Pass

0 Pass

1500 bar

5 10 15 20 25 30 35 40

Inte

ns

ity

(a

rb.u

nit

)

2 Theta (degree)

0 Pass

1 Pass

3 Passes

5 Passes