SPG Membrane Emulsification SPG Technology Co., Ltd. http://www.spg-techno.co.jp/ The characteristics of SPG membrane emulsification is shown in the diagram below compared with emulsification by a high pressure homogenizer. As it indicates, the SPG membrane emulsification yield uniform emulsion droplets in a wide range of size, which suggests monodispersion can be obtained. Thus, in consideration of production quantity in manufacturing, the membrane is able to obtain various sized droplets in emulsion at a constant rate of 90%. However, emulsification using the homogenizer will result in polydispersion due to several sized droplets exisiton in emulsion, which implies that it is impossible to maintain steady yield efficiency and productivity in manufacturing. For example, about 90% yield rate applies to the emulsion with average particle diameter of 0.8μm, however, producing 6μm emulsion droplets, the rate dropts to about 20% because of its wide distribution as shown in the following diagram②. ① SPG membrane Emulsion particle diameter distribution ② High-pressure homogenizer made by other company (excerpt from the catalog) 1/8 SPG Membrane Direct Emulsification Disperse phase solution and continuous phase solution are prepared in a container respectively. The disperse phase solution penetrate the SPG membrane producing uniform emulsion. The continuous phase requires a slight current. The size of emulsion droplet will be about three to four times bigger than that of the SPG pore . Syringe type Gas pressure type 8 8 1 1 2 2 3 5 3 5 4 4 6 6 7 7 1:S Syringe for disperse phase 2:Disperse phase (Soybean oil) 3:Vial Vial for continuous continuous phase 1:Disperse Disperse phase tank 2:Disperse phase (Soybean oil) 3:Container Container for continuous continuous phase 4:Continuous phase (contains an emulisifier) 5 : SPG membrane 6 : Stirring magnet 7:Stirrer 8:Pressure 8:Syringe pressure 4:Continuous phase (contains an emulisifier) 5:SPG membrane 6:Stirring magnet 7:Stirrer 8:Gas pressure Principal Disperse phase SPG current Continuous phase 2/8 SPG Membrane High Speed Emlsification Emlsification(Premix) mlsification(Premix) The disperse phase solution and continuous phase solution premixed roughly is penetrated to yield uniform emulsion droplets. The diameter of emulsion will be smaller than once or twice the size of the spg pore diameter. Syringe type Gas pressure type 8 8 1 4 1 4 2 2 3 3 5 5 6 6 7 7 1: Syringe、2: Dispers phase(Soybean oil) 3:Glass vial、4:Continuous phase (contains emulisifier) 5 : SPG membrane 6 : Stirring magnet 7:Stirrer 8:Preesure 1:、Tank 2:Dispers phase(Soybean oil) 3:Continuous phase Container 4:Continuous phase (contains an emulisifier) 5 : SPG membrane 6:Stirring magnet 7:Stirrer 8:Gas pressure ※ 6:Stirring magnet and 7:Stirrer may be used in case by case. Disperse phase Principal Continuous phase SPG 3/8 SPG Membrane Emulsification apparatus ●SPGmembrane emulsification appartus(small to smaller size) ●Membrane emulisification homogenizer and SPG filter kit(for wo, for ow) Second emulisification First emulisification ●SPG Membrane Emulsification Pumping Devices, etc SPG Memb. SPG Memb. 4/8 Example: how to start SPG membrane emulsification test First of all, the stability of emulsion needs to be confirmed by stirring for compsition of dispersion/continious phase. Adding Stirring Settled 1 2 1:Dispersion phase 2:Continuous phase disribution (contains surfactant) SPG pumping connector (disposable) 1 Dp 2 separated stablized Dispersion phase and Contineous phase disribution Recheck Dp Pressuring by syringe 1 SPG memb.emulsification (SPGchangable type) SPG filter kit (disposable) disribution Dp Gas pressure 1 2 2 disribution Dp 5/8 Searching for method method of emulsion mass production using SPG membrane For selecting the scale of SPG module, you will need to determine the process capacity per SPG unit length(emulsification speed for disperse phase and pressure force) based on the usage of bench scale. Also, SPG effective length for desire production condition (proccessing amount of dispersion phase, proccessing time) can be obtained by multipling SPG length times the number of SPG tube. Example Emulsive condition for dispherse phase using selected SPG pore size is examined by the SPG membrnae emulsification kit. SPG Internal Pressure Formula micro kit SPG effective length 1cm SPG High Speed Minikit SPG effective length 11cm Pressure gauge (Minute) regulator Gas pressure Tank for Continuous phase Disperse phase tank SPG module Continuous phase SPG module Stirrer Circulating pump Process Capacity ① Assuming: The SPG pore diameter 10μm Tank for Continuous SPG effective length 1cm phase Emulsification speed 10ml/(hours・cm) Yield condition ① Process amount of disperse phase =10ℓ, Time required for the process =4hours From the above condition, (Process amount of disperse phase =10ℓ)/(Emulsification speed10ml/time・cm)=1000hours・cm 1000hours・cm/( Time required for the process= 4hours)=250cm=25cm 25cm× 25cm×10tubes 10tubes Modules Modules 6/8 Photos for SPG Membrane Emulsification Equipment (MedMed-sized) sized) Disperse phase tank Continuous phase tank SPG module Disperse phase tank Continuous phase tank SPG module 7/8 2ℓ 6ℓ L250×7tubes 5ℓ 25ℓ L500×30tubes Basically, the structure of this model is the same as one of the SPG high speed minikit. SPG membrane emulsification Equipment (med-sized) SPG module with the several tubes Stirrer Controller panel Disperse phase tank Contineous phase tank Gas pressure Observation window SPG module Circulation pump Collecting Emulsion 8/8
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