Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
5447095 | Energy Procedia | 2016 | 12 Pages |
Abstract
Conventional jaggery making with a pan furnace consumes all bagasse for evaporation of water. Hot spots during boiling of juice causes caramelization of sugar. It gives dark brown colour to jaggery, which has low market value. Chemicals like lime, phosphoric acid and hydros powder are used as clarificant to enhance colour of jaggery. Traces of these chemicals in jaggery are harmful to human health. Freeze pre-concentration of sugarcane juice from 20ÌBrix to 40ÌBrix using a reversible heat pump saves bagasse during initial 63% water removal. Water is removed in the form of ice. It requires 335kJ/kg heat removal, which is equivalent to 15% of heat addition during evaporation. Recycling of saved bagasse in field improves the yield of sugarcane. Juice is exposed to -5ÌC during pre-concentration. It reduces inversion of sucrose and expected to improve the quality of jaggery by reduced exposure time to high temperature. Simple cycle analysis for FPCS of juice shows that COPc is 18 with R22 as refrigerant at -8ÌC evaporator and 3ÌC condenser temperature. Overall system COPc is expected, to be in the range of 9 to 12 after accounting for losses like cycling of thermal mass and heat gain from ambient. Power required for 1.5 TR FPCS is 0.5 to 0.6 kWe, which is about 0.1 INR/kg of jaggery produced. Payback period for FPCS is one year. Sugar inclusion in ice is estimated using empirical correlations for flow of solution over flat surface and it is 19.1ÌBrix. Energy consumption, sugar loss and cost of system are estimated. Ways of reducing sugar loss are investigated along with repercussion on energy consumption and system cost. Further experimental investigations on sugar inclusion in ice, which forms inside the tube needs to be experimentally tested.
Related Topics
Physical Sciences and Engineering
Energy
Energy (General)
Authors
Milind V. Rane, Dinesh B. Uphade,