| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 149463 | Chemical Engineering Journal | 2012 | 11 Pages |
Gas–liquid processing in microreactors remains mostly restricted to the laboratory scale due to the complexity and expenditure needed for an adequate numbering-up with a uniform flow distribution. Here, the numbering-up is presented for multi-phase (gas–liquid) flow in microreactor suitable for a production capacity of kg/h. Based on the barrier channels concept, the barrier-based micro/milli reactor (BMMR) is designed and fabricated to deliver flow non-uniformity of less than 10%. The BMMR consists of eight parallel channels all operated in the Taylor flow regime and with a liquid flow rate up to 150 mL/min. The quality of the flow distribution is reported by studying two aspects. The first aspect is the influence of different viscosities, surface tensions and flow rates. The second aspect is the influence of modularity by testing three different reaction channels type: (1) square channels fabricated in a stainless steel plate, (2) square channels fabricated in a glass plate, and (3) circular channels (capillaries) made of stainless steel. Additionally, the BMMR is compared to that of a single channel regard the slug and bubble lengths and bubble generation frequency. The results pave the ground for bringing multi-phase flow in microreactor one step closer for large scale production via numbering-up.
► Numbering-up gas–liquid flow in microreactor suitable for kg/h production capacity. ► Flow non-uniformity is studied using barrier-channels concept. ► Taylor flow with uniformity larger than 90% achieved in the parallel channels. ► Six fluids are studied with different viscosities, surface tensions and flow rates. ► Three channels type are studied square and circular in steel and square in glass.
