Integrated Furfural Extraction Process Coimbatore in Zimbabwe
- Use: Cooking Oil
- Type:Cooking Oil Processing Equipment
- Production Capacity: 50~140 TPD
- Power: 79.12 kw
- Dimension(L*W*H): up to specs
- Voltage: 110V220V/380V
- Core Components: PLC, Hot Selling Guangzhou Small 6Yl-100 Screw Oil Pres
- Market: Zimbabwe
Process design, kinetics, and techno-economic assessment of
Process: furfural extraction, reaction (chromite free catalyst) & purification. • Net co-production of 2-methyltetrahydrofuran, the green solvent used. • A Langmuir-Hinshelwood kinetic model with 2 active sites (metal–acid) is developed. • Low H 2 O concentrations compete for sites with furfural but without side-reactions. •
The sustainable production of furfural investigated in this study has significantly catered to most of the challenges in traditional industrial route in terms of capacity as well as environmental compatibility. The steady state process flow diagram of the integrated dual step furfural production mediated by aqueous LTTM media is exhibited in
Furfural production from biomass residues: Current
A furfural yield of 52.3% was achieved when the system is coupled with continuous supercritical carbon dioxide extraction at a flow rate of 3.77 g/min and temperature of 423 K, significantly higher than the system without supercritical carbon dioxide extraction, i.e. furfural yield of 28.8%.
This study aims to propose a new process design, simulation, and techno-economic analysis of an integrated process plant that produces glucose and furfural from palm oil empty fruit bunches (EFB). In this work, an Aspen Plus-based simulation has been established to develop a process flow diagram of co-production of glucose and furfural along with the mass and energy balances. The plant’s
Techno-economic assessment of hybrid extraction
tigation on the furfural purification process involved the use of a combined integrated and intensified tech- nique, which showed a decrease in the total annual
Furfural is an important fuel precursor which can be converted to hydrocarbon fuels and fuel intermediates. In this work, the production of furfural by dehydration of process-relevant pentose rich corn stover hydrolyzate using a biphasic batch reaction system has been investigated. Methyl isobutyl ketone (MIBK) and toluene have been used to extract furfural and enhance overall furfural yield
Techno-economic assessment of hybrid extraction
Butyl chloride was found to be the most suitable solvent for the hybrid extraction/distillation process of furfural production. The proposed hybrid sequence was more favorable than the traditional distillation process when the methanol fraction of the feed stream was
In this study, furfural production in a two-stage system was investigated using Eucalyptus wood residues (pinchips) as raw material. Firstly, an autohydrolysis treatment at 170 °C was performed for 40 min to solubilise xylosaccharides from biomass. In a second stage with sulphuric acid, furfural production was evaluated at different temperatures (170–240 °C) and reaction times (2.5–30
Integrated Production and Separation of Furfural Using an
An integrated platform for furfural production and separation from xylans using an acidic aqueous biphasic system (AcABS) is described here. The AcABS is composed of the ionic liquid (IL) tributyltetradecylphosphonium chloride ([P444(14)]Cl) and hydrochloric acid (HCl), the latter acting both as a catalyst and phase-forming agent. Furfural is produced in the AcABS biphasic regime under
Furfural is a versatile platform and multipurpose chemical that can be produced with no carbon efficiency loss from pentose sugars present in prehydrolysate streams. Existing processes for the production of furfural are typically energy-intensive with limitations to recover value-added molecules and byproducts such as lignin and acetic acid. In this work, we demonstrate a novel integrated
