提高精馏和精馏装置接触装置的能效和生物乙醇的净化程度

Y. Bulii, O. Obodovych
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引用次数: 0

摘要

通过增加液体在塔架上与蒸汽接触的停留时间,研究了浓缩塔、浓缩塔和啤酒蒸馏塔的能量效率、轻馏分分离过程中乙醇的纯化程度以及啤酒蒸馏过程的效率。提出了一种控制接触段和溢流段流体保留循环而不与相邻塔板混合的精馏技术。为了实现该方法,实验柱上装有同轴排列的鳞片盘,排除了流体运动的线性。每个托盘的溢流孔由与驱动机构相关联的活动阀按照控制器程序交替开启和关闭。将托盘的横截面改变为45- 50%,可以立即降低蒸汽率,并使溢出的液体通过溢流孔和刻度间隙。由于这个时间,溢出从5秒减少到2秒。研究表明,将啤酒在塔架上的停留时间延长至12秒,可使啤酒蒸馏液中的酒精浓度比标准柱提高28%。鳞片的同轴排列消除了形成停滞区和燃烧啤酒悬浮颗粒的可能性。蒸馏过程中加热蒸汽的具体消耗量不超过16公斤/分升的啤酒无水酒精。在分离轻馏分的过程中,液体在托盘上停留20秒,醛类、高醇类杂醇油和甲醇的提取率平均增长了30%,轻杂质和中间杂质的多重浓度增加了32%。蒸馏过程的加热蒸汽消耗量降至14 kg/dl。为了提高接触装置的效率,建议延长液体在托盘上的停留时间,直到接近相平衡状态,并向相邻的托盘提供不混合的液体溢出,使用具有共电流和交变截面完全补偿的托盘。
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INCREASING ENERGY EFFICIENCY OF CONTACT DEVICES OF THE DISTILLATION AND RECTIFICATION PLANTS AND DEGREE OF BIOETHANOL PURIFICATION
The aim of the work was a study the energy efficiency of the heads and fusels concentrating column and beer still, the degree of purification of ethanol in the process of the separation of light fraction and the efficiency of the process of а beer distillation by increasing residence time of the liquid on the trays for contact with the vapor. The technology of rectification with controlled cycles of fluid retention on the stages of the contact and its overflow without mixing to the adjacent trays is proposed. For implementing the method the experimental column was equipped with scaly trays with coaxial arrangement of scales, which excluded the linearity of the fluid motion. The overflow holes of each tray is alternately opened and closed by movable valves associated with the driving mechanism in accordance with the controller program. Change the cross-section of the trays at 45-50 % resulted in an immediate reduction of rate of vapor and provided the spilled liquid through the overflow hole and the gap of scales. Due to this time the overflow was reduced from 5 to 2 seconds. It was studied that the increasing of the residence time of the beer on the trays to 12 seconds can increase the concentration of alcohol in beer distillate by 28 % in comparison with the standard columns. The coaxial arrangement of scales eliminates the possibility of formation of stagnant zones and burning of suspended particles of a beer. Specific consumption of heating steam to the process distillation not exceed 16 kg/dl of absolute alcohol of a beer. In the process of the separation of light fractions with the fluid retention on trays to 20 seсonds a degree of extraction of aldehydes, higher alcohols of fusel oils and methyl alcohol grew on average by 30 %, the multiplicity of concentration of light and intermediate impurities increased by 32 %. The consumption of heating steam for the distillation process was reduced to 14 kg/dl of absolute alcohol. To increase the efficiency of contact devices, it is advisable to prolong the residence time of the liquid on the trays until close to the equilibrium state of phases, and to provide overflow of liquid without mixing to the adjacent trays, to use trays with full compensation of co-current and alternating cross-section.
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