The MEGATRON® MT-MM stands out due to the following advantageous qualities compared with conventional emulsifying methods.
Low mechanical and thermal load of the product: Due to the fact that the drop formation is not primarily based on high shear forces or bounce effects a very gentle processing of the product is possible. At the membrane emulsifying process, the thermal and mechanical loads having an effect on products are lower than at conventional emulsifying methods around orders of magnitude.
Double emulsions: The production of double emulsions is without problems possible by the gentle emulsifying process.
High concentration of contents: By the system of it is possible to produce emulsions with up to approx. 50 % ratio of the disperse phase in one step – defined and reproducible. The emulsions arising in this process show also spatially very constant distributions of concentration.
Low energy consumption: Due to the proportionally low energy which is necessary to receive a certain emulsifying result is also the energy consumption and with that the energy costs related to a produced output much lower.
Small droplet sizes: Since the membrane pores show only a diameter of 1 – 2 μm, it is possible to produce very small droplets. Depending on speed droplets also can be produced due to the special drop formation mechanism in the sub micron area.
Narrow droplet size distributions: Because of the special drop formation mechanism very narrow droplet size distributions can be reached. It is also possible at certain applications and process parameters to produce monodisperse emulsions practically.
Controllability: The system MEGATRON® MT-MM works after the inline principle. Desired throughputs and droplet size distributions can reproducibly be well controlled.
Principal of process
A MEGATRON® MT-MM machine consists in principle from a cylindrical working chamber in which one a membrane is installed coaxially over a shaft. The working chamber has two product inlets, one for the disperse (inner) phase and one for the continuous (outer) phase. The disperse phase streams axially into the inside of and will be dispersed into the continuous phase while flowing through the pores of the membrane. The drop detachment is additionaly supported by the fast rotation. The drop formation or its size distribution depends on the process parameters: Speed, pore diameter of the membrane, viscosity of the continuous phase and the shear gap. The formed drops are taken away continuously by the outer phase.
|Approx. 5 – 40 l/h of liquid phase
|Max. working pressure
|6 bar(g) for continuous phase / 20 bar(g) for dispersed phase
|All wetted parts are made of SS 316L, electro-polished / All wetted O-rings are made of EPDM (other materials are available on request)
|High frequency motor, 4.0 kW, 10 000 rpm, 3 x 400 V, 167 Hz, IP 55, Design B3 / B5 / Suitable for operation with frequency inverter (must be operated with a frequency inverter)
|By frequency inverter, Type RECO® 34 / 4.0 integrated in the stainless steel housing
|Type: MMK 1-56 DW, horizontal design, with heating / cooling jacket, with double mechanical seal, product inlet G ½”, product outlet G ½”, material 316 L; electropolished, dosing connection
|Type MMG 55 / 2, material: stainless steel 316L
|Double mechanical seal
|Sealant pressure system
|Pressure vessel with volume 3 l with cooling coil, analogue manometer and analogue thermometer
|Pump with frequency converter for continuous phase
|Pump unit with gear pump head and magnetic coupling, flow rate up to approx. 40 l/h, controlled by frequency converter through touch screen panel
|Gas flow meter
|To control the gas flow / Gas flow: up to approx. 40 l / h
|Touch screen panel 6.4” TFT color / Network; 10 / 100 Mbit / USB- and RS232-Connection / Windows CE Core / Protection class: front IP 65 / back IP 20