| |
Franken |
|
| |
Phase Seperators |
|
| |
Liquid / Liquid Phase Separation |
|
| |
|
|
| |
|
|
| |
|
|
| |
|
|
| |
|
|
| |
Why Phase Separators?
Phase separators remove droplets with diameters >0.1µm from liquid/ liquid dispensions. The resulting improvement in the purity of liquid recovered from both dispersed and continuous phases increases product quality and reduces the need for downstream treatment. FRANKEN Phase separators thus increase profits significantly as the investments and operating costs are low. |
|
| |
|
|
| |
Phase Separators ('Separators') : FRANKEN designed separators guarantee a very high performance because of application of state-of-the-art design rules based on empirically verified CFD design models and use of the proprietary range of high performance internals. |
|
| |
|
|
| |
Design philosophy : Droplete- droplet coalescence on microfibre, wire mesh and profile surfaces allows large droplets ( d> 1,000 µm) to form quickly and efficiently. As these droplets flow through the phase separator vessel, density differences cause them to migrate to the liquid interface under the influence of gravity.
Since coalescence is a mechanical separation process, it cannot remove the dissolved liquids.
|
|
| |
|
|
| |
Perfect Separation :
FRANKEN phase separators are designed for optimal coalescence in separating organic or aqueous droplets.To design each separator the major parameters are
1. Droplet size distribution at the inlet
2. Wetting behavior of the two liquids
3. Interfacial tension. |
|
| |
|
|
| |
Separation task defines the phase separation procedure : |
|
| |
Droplet Size defines the type of SEPERATOR |
|
| |
PT phase Separator
Fine droplets >0.1µm |
MPT phase Separator
medium droplets >10µm |
PTG phase Separator
coarse droplets >50µm |
| Coalescence process - Droplet formation and separation |
In Microfibre beds
Flow guides the fine droplets to the micrifibers
Droplet-droplet coalescence (collection of droplets) at the fiber cross points
Displacements of coarse droplets (d >1,000µm) at the fiber bed |
At profile surfaces
Density difference guides the droplets to the profile surfaces
Droplet-droplet coalescence at the profile surfaces
Displacements of coarse droplets ( d > 1,000µm) at certain profile areas |
At the interface
Coarse droplets shift to the interface under gravity
Droplet- droplet coalescence at the interface |
|
|
| |
|
|
| |
Process Conditions : |
|
| |
| |
Units |
PT |
MPT |
PTG |
| Density difference |
Kg/m3 |
>10 |
>50 |
>150 |
| Viscosity of continuous phase |
Mpas |
<500 |
<20 |
<5 |
| Viscosity of dispersed phase |
Mpas |
<500 |
<1,000 |
<2,000 |
| Interfacial tension( no surfactants) |
mN/m |
>2 |
>2 |
>2 |
| Maximum concentration of dispersed phase |
vol% |
<10 |
Any |
Any |
| Differential pressure (clean/ maximum) |
bar g |
<0.05/1.5 |
<0.02 |
<0.02 |
| Solid particles |
µm |
<5 |
<25 |
|
|
|
| |
|
|
| |
Application : |
|
| |
| PT Phase separator |
MPT Phase separator |
PTG Phase separator |
Product treatment
- water from silicone oil
- water from polycarbonate |
Biodiesel
- Glycerine from methyl ester
- Fatty acid from glycerine water |
Process enhancement
- Water from cumene
- Raffinate from methyl pyridine |
Process enhancement
- Rh solution from aldehyde
- extractant from Cs solution
- benzene fron hydrochloric acid |
Hydrocarbons from waste water Process enhancement
- Caustic soda from vinyl chloride
- Silicone oil from hydrochloric acid |
Capacity Enhancement
- Reservoir water from crude oil
- MCB/DCM from waste water
- Hydrocarbon from water |
|
|
| |
|
|
| |
Benefits :
• Very high separation efficiency
• Separation down to solubility limit
• Low pressure drop (<50 mbar)
• Wide selection of material
• Low operating costs
• Low maintenance
• Customized engineering and manufacture |
|
| |
|
|
| |
Focus on the Environment :
• Our technologies contribute to ecological sustainability and lower energy use.
• Modular and extensible design helps to make phase separaters future- proof.
• At the end of there operating lives, the internals can be refurbished or recycled.
|
|
| |
|
|
| |
 |
|
 |
| For laboratory and pilot plant scale testing, we are able to manufacture phase Separation elements of smallest dimensions for subsequent scale-up (e.g. Ø 50 mm) |
|
|
| |
|
|
| |
Referance Installations |
|
| |
| |
 |
|
 |
|
| |
2x 4-stage ion-exchange system for the purification of Biodiesel;
Capacity: 20 MMgy
Locations:
Europe: Austria, Germany, Netherlands,
USA : Arkansas, California, Missouri, Texas |
|
PT phase separator for the separation of watery phase from RME;
Capacity: 25 m³/h; 35 MMgy
Locations:
Europe: Austria, Germany, Great Britain |
|
| |
|
|
|
|
| |
 |
|
 |
|
| |
MPT phase separator for the separation of glycerine from methyl ester;
Capacity: 17,5 m³/h (4,600 gal/h),
Separation efficiency: all droplets > 25 µm
Locations:
Asia: India, Malaysia, Singapore Australia, USA
Europe: France, Germany, Great Britain, Spain |
|
PT phase separator for the separation of glycerine water from methyl ester;
Capacity: 52 m³/h; 80 MMgy
Locations:
Australia
Europe: Austria, Germany, Great Britain |
|
|
|
| |
|
|
| |
|
|
| |
| |
Designed & Manufactured By
Franken Filtertechnik KG
Max – Planck – Strasse 7
50354 Huerth
Germany
Tel +49 (0) 2233 9744-0
Fax +49 (0) 2233 97440-40
Web : www.frankenfilter.com
Email : info@frankenfilter.com |
|
Represented in INDIA by
SPEC Engineers & Consultants Pvt. Ltd.
2/86, WHS, Kirti Nagar
New Delhi – 110015
India
Tel +91 11 4142 0206 , 2541 3597
Fax +91 11 2519 3715
Web: www.specengineers.com
Email: info@specengineers.com |
|
|
| |
|
|
| |
|
|