Integrated membrane process for pretreating and desolventizing hexane-soybean oil miscella–A pilot plant study

R Subramanian, N Muthuganesan, S Venu… - Journal of Membrane …, 2024 - Elsevier
R Subramanian, N Muthuganesan, S Venu, SK Gopika, UG Thummar, A Chakkaravarthi…
Journal of Membrane Science, 2024Elsevier
The study aimed to develop a membrane desolventizing technology for solvent recovery in
vegetable oil extraction. Pretreatment of crude miscella is a prerequisite for an organic
solvent nanofiltration (OSN) based desolventizing process. Solvent-resistant ultrafiltration
(SRUF) membrane employed in micelle-enhanced ultrafiltration (MEUF) of hexane-crude
soybean oil miscella displayed high phospholipids (PL) rejection (98.5%) and productivity
(∼ 28 L/m 2/h), accompanied with a moderate oil rejection (∼ 22%). The PL-rich retentate …
Abstract
The study aimed to develop a membrane desolventizing technology for solvent recovery in vegetable oil extraction. Pretreatment of crude miscella is a prerequisite for an organic solvent nanofiltration (OSN) based desolventizing process. Solvent-resistant ultrafiltration (SRUF) membrane employed in micelle-enhanced ultrafiltration (MEUF) of hexane-crude soybean oil miscella displayed high phospholipids (PL) rejection (98.5 %) and productivity (∼28 L/m2/h), accompanied with a moderate oil rejection (∼22 %). The PL-rich retentate fraction was alkali-treated to recover the oil in the stream (8.8 %). This complementary pretreatment approach met the quality requirements and maximized the yield of treated oil (>98 %) while reducing the chemicals in the process. A subsequent two-stage desolventizing of MEUF-treated miscella with solvent-resistant nanofiltration (SRNF) membrane reduced the oil-in-permeate to 1.37 %, achieving the set recycling criteria (<2 %). The results obtained from the pilot scale study (batch size 40 kg of crude miscella) revealed that the MEUF met the pretreatment requirements, and the subsequent OSN process recovered ∼63 % of hexane through a non-thermal route for recycling in the extraction process. The pilot-scale evaluation demonstrated the technical feasibility of the proposed membrane desolventizing process employing indigenous spiral-wound SRUF and SRNF membrane modules.
Elsevier
以上显示的是最相近的搜索结果。 查看全部搜索结果

Google学术搜索按钮

example.edu/paper.pdf
搜索
获取 PDF 文件
引用
References