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CONTROL METHOD FOR PROCESSES OF DRYING AND STORAGE OF PLANT MATERIALS WITH INCREASED CONTENT OF FATTY ACIDS

机译:脂肪酸含量增加的植物材料干燥存储过程的控制方法

摘要

FIELD: heating, drying.;SUBSTANCE: invention relates to automation of technological processes of drying and storage of crops, especially oil-bearing-crops. The method comprises drying oscillating in the temperature regime of plant materials in gravitationally moving layer of shaft dryer consisting of alternating in series zones of heating and cooling; processing of raw materials with antioxidant and feeding it to the silo storage with periodic active ventilation; supply of exhaust air after heating zones for preheating of plant materials; the discharge of the resulting steam-air mixture of the exhaust air after zones of cooling, preheating of plant materials and active ventilation in a cyclone for removal of suspended particulate matter comprised in it, followed by cooling and dehumidifying in the evaporator and heating first in the condenser of the heat pump and then in the heater; feeding of the prepared in a heat pump conditioned air to the zones of heating and cooling to form a closed loop, and stabilization of hydrothermal characteristics of the raw materials during drying and storage with impact on the flow rate, temperature and moisture content of the conditioned air supplied to the zones of heating and cooling of the dryer, and the flow rate of antioxidant depending on the flow rate of the dried plant raw material the novelty is the fact that after each heating zone mixing of plant raw material with an antioxidant is carried out, and for obtaining conditioned air the steam ejector heat pump is used, comprising a steam generator with electric heating elements and the safety valve, the ejector, the evaporator, the cold-receiver, the heat-exchanger-wasteheat exchanger, the condenser, the thermal expansion valve, the condensate collector working in a closed thermodynamic cycle; in the cold-receiver of the steam ejector heat pump the steam-air mixture is cooled to the dew point temperature and its dehumidification is carried out by condensation of moisture contained in it on the cooling surface of the cold-receiver in the form of droplet liquid; the resulting conditioned air from the cold-receiver is discharged in three flows: one is directed to the cooling zones of the dryer, the second for the active ventilation, and the third in series to the heat-exchanger-wasteheat exchanger, the condenser of steam ejector heat pump, the heaters and then to the heating zones of the dryer; in the steam generator working steam is obtained and fed in two flows, one of which is directed to heaters for additional heating the conditioned air prior to supply to the heating zones of the dryer, and the other - to the ejector nozzle, creating vacuum in the evaporator with lower temperature of the coolant boiling, which is used as water; the mixture of the coolant steams and working steam after ejector is fed to the condenser for heating the conditioned air prior to the heaters; one part of the condensate formed in the condenser is fed into the evaporator to replenish the loss of water and its another part to the heat-exchanger-wasteheat exchanger and further with the condensate formed in the cold-receiver and the heaters is first discharged into the collector of condensate, and then into the steam generator to form a closed loop; according to the current values of humidity of plant raw materials in the zones of heating the flow rate of the antioxidant is determined at the steps of mixing; according to the amount of water steam in the steam-air mixture after drying and silos the ejection coefficient of steam ejector heat pump is determined with the impact on the ratio of the working steam flow supplied to the ejector nozzle, and the ejected coolant steam from the evaporator by varying the flow rate of the working steam, and the productivity of the steam generator is determined based on the influence on power efficiency of its electric heating elements, depending on the working steam pressure supplied to the ejector.;EFFECT: invention enables to provide stabilization of quality of plant raw materials with increased content of fatty acids.;1 dwg
机译:技术领域:本发明涉及农作物,特别是含油作物的干燥和储存的工艺过程的自动化。该方法包括:在竖井干燥机的重力运动层中,在植物材料的温度范围内进行干燥振荡,该干燥运动由交替的加热和冷却串联区域组成;用抗氧化剂加工原料,并通过定期主动通风将其喂入料仓中;在加热区后供应废气以预热植物材料;在冷却,植物材料预热和在旋风分离器中进行主动通风以去除其中所含的悬浮颗粒物之后,将产生的废气的蒸汽-空气混合物排出,然后在蒸发器中进行冷却和除湿,然后在热泵的冷凝器,然后在加热器中;在热泵中将调制后的空气送入加热和冷却区域以形成闭环,并在干燥和存储过程中稳定原料的水热特性,这会影响调节后的流量,温度和水分含量提供给干燥机的加热和冷却区域的空气,以及抗氧化剂的流量取决于干燥的植物原料的流量,新颖性是这样的事实,即在每个加热区域之后进行植物原料和抗氧化剂的混合为了获得调节后的空气,使用了蒸汽喷射器热泵,该蒸汽喷射器包括带有电加热元件和安全阀的蒸汽发生器,喷射器,蒸发器,冷接收器,热交换器-废热热交换器,冷凝器,热力膨胀阀,冷凝水收集器以封闭的热力学周期工作;在蒸汽喷射器热泵的冷接收器中,蒸汽-空气混合物被冷却到露点温度,并且通过将其中包含的水分凝结成液滴形式在冷接收器的冷却表面上进行除湿液体;来自冷接收器的调节空气以三股形式排出:一股被引导至干燥机的冷却区,第二股被引导用于主动通风,第三股被串联至热交换器-废热热交换器,即冷凝器。蒸汽喷射器热泵,然后将加热器加热到干燥机的加热区;在蒸汽发生器中,获得工作蒸汽并将其分两股进料,其中一股被引导到加热器,以便在供应给干燥机的加热区域之前,对调节过的空气进行附加加热,另一股-进入喷射器喷嘴,从而产生真空。冷却液沸腾温度较低的蒸发器,用作水;将喷射器之后的冷却剂蒸汽和工作蒸汽的混合物送入冷凝器,以在加热器之前加热调节后的空气;冷凝器中形成的一部分冷凝水被送入蒸发器以补充水的损失,另一部分冷凝水进入热交换器-废热热交换器,冷凝器中形成的冷凝水又将加热器首先排放到冷凝器中。冷凝水的收集器,然后进入蒸汽发生器,形成一个闭环;根据加热区域内植物原料的当前湿度值,在混合步骤中确定抗氧化剂的流量。根据干燥和筒仓干燥后蒸汽-空气混合物中的水蒸汽量,确定蒸汽喷射器热泵的喷射系数,并影响供应到喷射器喷嘴的工作蒸汽流量和从中排出的冷却剂蒸汽的比率。通过改变工作蒸汽的流量来蒸发蒸发器,并根据供应给喷射器的工作蒸汽压力,基于对其电加热元件的功率效率的影响来确定蒸汽发生器的生产率。通过增加脂肪酸的含量来稳定植物原料的质量。; 1 dwg

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