Microfluidics systems promise tremendous improvements in quality, rapidity and cost outlay, as compared with macroscopic systems, when chemical mixing and reaction processes are being carried out, since the reaction and dwell times in the fluid paths of microfluidics systems are very short and only very small substance quantities are used and processed with high accuracy and in a reproducible way. So that, especially in industrial production, the quantity, throughput and productivity requirements can be satisfied, the fluid paths (mixing or reaction branches) have to be connected in parallel, where appropriate in large numbers (numbering-up).
Depending on the application, the parallel connection may be such that in each case a plurality of identical microducts are formed and connected in parallel in microfluidics components, for example a mixer or reactor, or such that entire microfluidics components or systems composed of microfluidics components are multiply connected in parallel. By means of suitable microengineering methods (for example, etching methods, LIGA technology or micromechanics), the parallel fluid paths can be produced identically with high precision, so that in each case the same process conditions, such as pressure, temperature, mass throughflow, etc., should prevail in all the parallel-connected fluid paths and therefore in each case the same products can be obtained from all the parallel mixing or reaction branches and be merged without losses of quality. This also presupposes, however, that all the parallel-connected mixing or reaction branches are supplied with the same volume flows of starting materials. The problem arises here that microfluidics systems are inclined to operationally induced variations in the effective throughflow resistance due to blockages of the fluid paths. Thus, for example, reaction products may stick as solids to the duct walls (fouling), thus increasing the pressure drop across the reaction branch, and then come loose again, with the result that the pressure drop decreases abruptly. This behavior may occur cyclically and to a different extent or at different times for each reaction branch. Whereas in macroscopic systems, for example, the mass throughflow can readily be measured, virtually fault-free, and be delivered to a throughflow control, this is not possible at a justifiable outlay for the individual fluid paths in the case of parallelized microfluidics systems.
US 2005/0232387 A1 discloses a microfluidics system for mixing two starting materials, in which two injection pumps convey the starting materials through two supply ducts into a mixing or reaction duct. Furthermore, US 2005/0232387 A1 discloses a valve circuit for the continuous conveyance of the respective starting material and for filling the respective injection pump, consisting here of two individual injectors, the valve circuit being designed, in a first valve position, to connect one of the two injectors to an intake line for the respective starting material, in a second valve position to shut off said injector and, in a third valve position, to connect it to the supply duct and to the other injector located on the latter.
EP 0 299 658 A2 discloses a system for mixing at least starting materials, in which two injection pumps driven synchronously by means of a common drive suck in the starting materials from reservoirs via valve arrangements and subsequently convey them through two supply ducts into a mixing unit.
DE 20 2005 007 485 U1 discloses an arrangement for the metering of fluids by means of injection pumps and of valves, assigned to these, for changing over between fluid uptake and fluid discharge.
In this case, a plurality of the injection pumps may be operated in parallel via a single drive.
DE 103 41 110 A1 discloses a mixing and metering section which is formed by microengineering on a chip and which is filled with the starting materials via valves by an injection pump.
The object on which the invention is based is, in a microfluidics system, to supply all the parallel-connected mixing or reaction branches with the same volume flows of starting materials and at the same time to equalize the initial volume flow from one and the same starting material.
The object is achieved, according to the invention, by means of the microfluidics system specified in claim 1.
Claim 2 specifies an advantageous design of the microfluidics system according to the invention.
The subject of the invention is therefore a microfluidics system for mixing at least two starting materials,
An injection pump is provided in each case per starting material for each mixing or reaction branch, these injection pumps being driven in common, as is known, for example, for double injection pumps. In the first valve position, the injection pumps are filled simultaneously with the respective starting material by suction intake. In the second valve position, the sucked-in starting materials are brought to a predetermined pressure. In this case, the individual injection pumps are connected fluidically to one another, so that the same pressure prevails in all the injection pumps. In the third valve position, the starting materials are distributed to the parallel mixing or reaction branches, each injection pump supplying in each case a reaction or mixing branch and being decoupled fluidically in each case from the other injection pumps. Since all the injection pumps are driven in common, the volume flows in all the parallel mixing or reaction branches are identical, even when these have different throughflow resistances.
In order to achieve a continuous supply of the mixing or reaction branches, in a way known per se, for each injection pump, a further injection pump operating complementarily to this may be provided, the two injection pumps alternately sucking in the starting material and supplying it to the reaction branch.
For a further explanation of the invention, reference is made below to the figures of the drawing in which, in particular,
The valve circuits 91, 92, 93 are in each case designed, in a first valve position, for connecting the injection pumps 811 . . . 83n to the respective intake line 71, 72, 73 for sucking in the starting material 1, 2, 3 from the reservoir, in a second valve position for shutting off the injection pumps 811 . . . 83n, so that an operating pressure can be built up in the injection pumps 811 . . . 83n, and, in a third valve position, for connecting the injection pumps 811 . . . 83n to the supply ducts 511 . . . 53n assigned in each case, in order to press the starting material 1, 2, 3 into the respective supply ducts 511 . . . 53n. The injection pumps 811 . . . 83n in each case connected to each valve circuit 91, 92, 93 have a common drive 101, 102, 103 and are driven in parallel.
As indicated in
Number | Date | Country | Kind |
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10 2007 028 116.3 | Jun 2007 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP2008/057616 | 6/17/2008 | WO | 00 | 1/8/2010 |