Basic Info.
Composition
Molasses Fermentation
Processing Material
Agronomic Products
Material
Stainless Steel 304 316
Working Pressure
ATM., Negative Pressure, Positive Pressure
Solvent
Methanol, Ethanol, Acetone and Other Organic Solve
Production Capacity (L/H)
50L/H~2000L/H
Transport Package
Standard Wooden Packing
Origin
Zhejiang, China (Mainland)
Product Description
Bioethanol Production Equipment by Sucrose Fermentation1. Sterilization of equipment and cleaning of piping2. Activation and culture of yeast3. Fermentation of sugar and ethanol fermentation4. Operation of the distillation column 1. Standard Technical Parameter List Of Kettle TowerType | HT-200 | HT-300 | HT-400 | HT-500 | HT-600 | HT-800 |
Tower Diameter (mm) | 200 | 300 | 400 | 500 | 600 | 800 |
Tower Height (mm) | 6000 | 7000 | 7000 | 7000 | 7500 | 7500 |
Tower Volume (m3) | 640 | 1220 | 1450 | 2300 | 2500 | 3200 |
Production Capacity (kg/h) | 45~50 | 90~100 | 150~160 | 280~300 | 420~440 | 600~620 |
Heating Area (m2) | 6.0 | 8.0 | 14 | 18 | 24 | 32 |
Condensation Cooling Area (m2) | 10+2 | 15+3 | 20+5 | 36+5 | 50+8 | 70+10 |
Packing Form | Stainless steel corrugated packing |
Outline size (m) | Long | 2.3 | 2.5 | 2.6 | 3.0 | 3.5 | 4.2 |
Wide | 0.7 | 0.8 | 1.0 | 1.2 | 1.4 | 1.8 |
High | 7.3 | 7.5 | 9 | 9 | 10 | 14 |
Equilibrium data of alcohol-water phase
Temperature | Liquid fraction | Vapour phase fraction |
| X | X | Y | Y |
C | ETOH | WATER | ETOH | WATER |
100 | 0 | 1 | 0 | 1 |
95.5 | 0.019 | 0.981 | 0.17 | 0.83 |
89 | 0.0721 | 0.9279 | 0.3891 | 0.6109 |
86.7 | 0.0966 | 0.9034 | 0.4375 | 0.5625 |
85.3 | 0.1238 | 0.8762 | 0.4704 | 0.5296 |
84.1 | 0.1661 | 0.8339 | 0.5089 | 0.4911 |
82.7 | 0.2337 | 0.7663 | 0.5445 | 0.4555 |
82.3 | 0.2608 | 0.7392 | 0.558 | 0.442 |
81.5 | 0.3273 | 0.6727 | 0.5926 | 0.4074 |
80.7 | 0.3965 | 0.6035 | 0.6122 | 0.3878 |
79.8 | 0.5079 | 0.4921 | 0.6564 | 0.3436 |
79.7 | 0.5198 | 0.4802 | 0.6599 | 0.3401 |
79.3 | 0.5732 | 0.4268 | 0.6841 | 0.3159 |
78.74 | 0.6763 | 0.3237 | 0.7385 | 0.2615 |
78.41 | 0.7472 | 0.2528 | 0.7815 | 0.2185 |
78.15 | 0.8943 | 0.1057 | 0.8943 | 0.1057 |
78 | 0.932 | 0.068 | 0.9212 | 0.0788 |
77.8 | 0.9673 | 0.0327 | 0.9423 | 0.0577 |
77.5 | 1 | 0 | 1 | 0 |
Alcohol Phase Equilibrium Diagram:2,Structure and properties This equipment by the heater, Evaporator, tower body, condensers, cooling, separator, such as flow meter, composition, major equipment and accessories are made of austenitic stainless steel material, and polished contact surfaces and pickling solution purification process, in line with GMP requirements 3,device characteristics energy saving:Because discharge residue at the bottom as the first of the preheater of heat and evaporation heat energy of steam as a second warm-up for the second time, making full use of energy. Meanwhile, the evaporation of steam full cooling and cooling water consumption significantly reduced, two comprehensive, than the average 50 less energy for distillation column.4,Working principle of the device It is use column heater to alcohol heating, alcohol heating evaporation temperature, steam by tower packing to condensation, by condensation liquid part return to tower, tower steam and return exchange, alcohol steam continue to, other and return Exchange per cent evaporator,, by flowmeter, qualified alcohol. 5,Equipment installation and debuggingistillation process for the installation of the total figure, the piping, valves, connectors and instrumentation accessories, factory assembled in front of the factory, users only need to press the order of the connections to the correct assembly.B,Installation should be appropriate for the device at run time, load, assembly equipment should be vertical, horizontal, grounding, bearing right.C,After the installation is complete, use hydraulic pressure to leak check, pressure, and leaks are found fastened in a timely manner. D,Cleaning equipment : surface in contact with the solution, should be thoroughly washed. E,Test Run : test material with water evaporation.6,operation specification6.1 Preparatory work before the machine:6.1.1 Check Device connection points before sealing, valves, meters are working properly, whether the pipeline, for leaks6.1.2 Check the heater, room is clean;6.1.3 Check opening and closing of the valve is in the proper location, you can review and correct the rear uses6.2 operate machine 6.2.1 Starting electric heating system, heat - Conducting oil reaches 120 C open the Import and Export of heat - pipe valves, starting at the same time heat conduction oil pump; 6.2.2 Open the valve and material conveying pump feed, to see when the liquid evaporation Chamber, vision, that is, turn off the feed valve condenser emptying always. 6.2.3 Tower kettle temperature to 105ºC, the top of the tower temperature 91ºC, pipeline condensation, close recovery alcohol pipeline valve, open return pipeline valve, condensation all return to tower, ten minutes about, in sampling detection alcohol concentration, alcohol concentration 65, open recovery pipeline valve, recovery directly into working capital. Master the reflux ratio at the same time, to keep the recovery of alcohol. 6.2.4 When tower temperature rose to 80ºC , open recirculating cooling water systems, hydraulic stability in 0.25~0.35mpa ; condensate temperature at 80ºC.6.3 Normal operationAdjust the feed valve opening, control of liquid surface is maintained at a certain height, so that evaporation and diluted amount of alcohol added, dynamic equilibrium of the residual emissions will;6.4 96°of alcohol recovery operations6.4.1 Other, tower kettle temperature to 87ºC, the top of the tower temperature 77ºC, pipeline condensation, close recovery alcohol pipeline valve, open return pipeline valve, condensation all return to tower, ten minutes about, in sampling detection alcohol concentration, alcohol concentration 96°, open recovery pipeline valve, recovery into cooling and to qualified alcohol barrel. Master the reflux ratio at the same time, to keep the recovery of alcohol.6.5 stop6.5.1 Turn off the supply of materials;
6.5.2 Turn off the heating system, stop the supply of heat sources ;
6.5.3 losed loop cooling water system.7,Maintenance and repair of equipment A,If the device is running in the process of evaporation recovery decreased, check whether the heating pipe scaling, leaks, adequacy of water supply, heat supply meets the conditions, wet dial is correct B,outages have to clean the surface of contact solution, turn off all valves and contact with the outside world C,The week in a row, the application of clear water about 15 minutes of cooking, in case the heater tube scaling. If a longer period of time does not run, to thoroughly clean the device. Prevents adhesion surface residue. D,the device runs for ten days to inspect the junction of fasteners and fastening. Always keep the equipment clean.8.special version A,Equipment in work, all the electrical equipment must be explosion - proof, no open flames jobs, smoking is prohibited in the workshop, the prohibition of wearing nail the sole officer to enter and good ventilation, fire extinguishers, fully furnished. B.Equipment maintenance charged operation. Equipment leaks work is prohibited. Distillation Operation
Distillation as the name suggests, is from a fermented mash of alcohol extracted.requirement:With minimal resource consumption of steam, cooling water, minimizing alcohol net, and try to do it does not run on wine, does not run under WINE.Existing distillation processes:----Distillation of single towerLeverage a single tower, by two distillation process for manufacturing alcohol.Distillation is the role of ethanol for the first time isolated from fermented beer, and excludes lees. Distillation is the concentration of ethanol and again ruled out impurities.Fermented beer pumps - mash feed heater pool after entering the cold and mash of alcohol waste liquid heat exchangers, heat into the tower from the top of the tower, and the bottom of the tower with heat conduction oil stove heated by heating oil, so that the base of the tower temperature of l05-108ºC, the top temperature of 92-95ºC, the top of the tower about 50% of the capacity of alcohol vapor cooling directly into the tank.Distillation again:After heating, the tundish alcohol into the tower from the top of the tower, the tower at the bottom of the heat conduction oil stove heated by heating oil, the base of the tower temperature of 105-107 ºC, central tower temperature of 92 ºCor so, alcohol vapor from the top of the tower into the first Xiling Seal engravers' Society.Wine without condensing the steam into the second condenser, the first and second condenser flow of condensate all, concentrations up to 96vv of alcohol condensed liquid impurities in the second condenser more, you can no longer flow into the tower, as a secondary alcohol sales, or into the fermentation and distillation of fermented. No CO2 gas condensation and low boiling point impurities, from the exhaust tube to the atmosphere. Production of alcohol in liquid phase out under the condensate return line, finished cooler, wine coolers, their quality requirements back into the wine library. Steam distillation of ethanol wastewater water, the discharge tube to the tower.
Address:
Unit 3, Building 21, 4th District, Xiawang Village, Yiwu City, Jinhua, Zhejiang, China
Business Type:
Manufacturer/Factory, Trading Company
Business Range:
Industrial Equipment & Components, Manufacturing & Processing Machinery
Management System Certification:
ISO 9001, ISO 9000
Company Introduction:
Our company offers variety of products which can meetyour multifarious demands. We adhere to the management principles of " Qualityfirst, customer first and credit-based" Since theestablishment of the company and always do our best to satisfy potential needsof our customers. Our company is sincerely willing to cooperate withenterprises from all over the world in order to realize a win-win situationsince the trend of economic globalization has developed with anirresistible force.