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METHOD FOR DRYING HIGH-MOISTURE DISPERSE MATERIALS AND DEVICE FOR ITS IMPLEMENTATION
专利权人:
Federalnoe gosudarstvennoe byudzhetnoe obrazovatelnoe uchrezhdenie vysshego obrazovaniya "Voronezhskij gosudarstvennyj universitet inzhenernykh tekhnologij" (FGBOU VO "VGUIT")
发明人:
Drannikov Aleksej Viktorovich (RU),Дранников Алексей Викторович (RU),Shevtsov Aleksandr Anatolevich (RU),Шевцов Александр Анатольевич (RU),Kostina Evgeniya Vasilevna (RU),Костина Евгения Васильевна (R
申请号:
RU2017140289
公开号:
RU0002674610C1
申请日:
2017.11.21
申请国别(地区):
RU
年份:
2018
代理人:
摘要:
FIELD: technological processes; food industry.SUBSTANCE: invention relates to the food and feed industry and can be used for drying, for example, materials such as beet pulp, apple and grape pomaces, etc. Method involves a 2-stage drying. At the first stage, the initial material is pre-dried with superheated steam of the atmospheric pressure of the material in a pulsed vibrating layer at a temperature of 130...140 °C, and on the second stage – drying in a fluidized bed with superheated steam of reduced pressure at a pressure of 20...30 kPa and a temperature of 90...100 °C. Exhaust superheated steam of atmospheric pressure with a temperature of 110...115 °C is divided into two streams. One steam stream is sent to overheat to a temperature of 130...140 °C with heating steam with a temperature of 160...170 °C, then return to the first stage. Second steam stream in an amount equal to the amount of moisture evaporated at the first stage from the material, is supplied to superheat the reduced pressure to a temperature of 90...100 °C. Exhaust superheated steam of reduced pressure with a temperature of 70...75 °C is also divided into two streams. One steam stream is sent to overheat to a temperature of 90...100 °C with exhaust superheated steam at atmospheric pressure, then return to the second stage. Second steam stream in an amount equal to the amount of moisture evaporated from the material in the second stage is used to create a reduced pressure of 20...30 kPa during condensation in countercurrent steam flow with cold water having a temperature of 10...15 °C. Device consists of chamber for drying with superheated steam of atmospheric pressure (1) and chamber for drying with superheated steam of reduced pressure (2), which are hermetic, connected in series with sluice gates (3, 4 and 5) and arranged in a vertical plane. Each drying chamber contains inside sloping perforated grid (6 and 8) and is equipped with inlet pipes (9 and 11) and outlet (10 and 12) of superheated s
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中国工程科技知识中心
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