Chemical Industry and Engineering Progress ›› 2019, Vol. 38 ›› Issue (05): 2112-2122.DOI: 10.16085/j.issn.1000-6613.2018-1643
• Chemical processes and equipment • Previous Articles Next Articles
Qingwen WEI(),Lidong ZHANG(),Qing WANG
Received:
2018-08-10
Revised:
2018-09-26
Online:
2019-05-05
Published:
2019-05-05
Contact:
Lidong ZHANG
通讯作者:
张立栋
作者简介:
<named-content content-type="corresp-name">韦庆文</named-content>(1991—),男,硕士研究生。E-mail:<email>2284131304@qq.com</email>。
基金资助:
CLC Number:
Qingwen WEI, Lidong ZHANG, Qing WANG. Perturbation and mixing enhancement of stirring internals installed in rotary retorts[J]. Chemical Industry and Engineering Progress, 2019, 38(05): 2112-2122.
韦庆文, 张立栋, 王擎. 回转干馏炉内扰流件的扰动及增混特性[J]. 化工进展, 2019, 38(05): 2112-2122.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2018-1643
参数 | 油页岩颗粒 (大颗粒) | 页岩灰颗粒 (小颗粒) |
---|---|---|
泊松比 | 0.25 | 0.25 |
剪切模量/Pa | 1×108 | 1×108 |
真实密度/kg·m-3 | 2200 | 2600 |
参数 | 油页岩颗粒 (大颗粒) | 页岩灰颗粒 (小颗粒) |
---|---|---|
泊松比 | 0.25 | 0.25 |
剪切模量/Pa | 1×108 | 1×108 |
真实密度/kg·m-3 | 2200 | 2600 |
参数 | 回转炉-颗粒 | 颗粒-颗粒 |
---|---|---|
恢复系数 | 0.1 | 0.5 |
静摩擦系数 | 0.9 | 0.6 |
滚动摩擦系数 | 0.05 | 0.05 |
参数 | 回转炉-颗粒 | 颗粒-颗粒 |
---|---|---|
恢复系数 | 0.1 | 0.5 |
静摩擦系数 | 0.9 | 0.6 |
滚动摩擦系数 | 0.05 | 0.05 |
参数 | 钢材 | 陶瓷 | 玻璃 |
---|---|---|---|
泊松比 | 0.3 | 0.23 | 0.27 |
剪切模量/Pa | 7.5×1010 | 2.4×1010 | 3.2×1010 |
密度/kg·m-3 | 7800 | 2800 | 2500 |
参数 | 钢材 | 陶瓷 | 玻璃 |
---|---|---|---|
泊松比 | 0.3 | 0.23 | 0.27 |
剪切模量/Pa | 7.5×1010 | 2.4×1010 | 3.2×1010 |
密度/kg·m-3 | 7800 | 2800 | 2500 |
参数 | 钢材-陶瓷 | 陶瓷-陶瓷 | 玻璃-陶瓷 |
---|---|---|---|
恢复系数 | 0.7 | 0.8 | 0.8 |
静摩擦系数 | 0.3 | 0.4 | 0.7 |
滚动摩擦系数 | 0.04 | 0.04 | 0.04 |
参数 | 钢材-陶瓷 | 陶瓷-陶瓷 | 玻璃-陶瓷 |
---|---|---|---|
恢复系数 | 0.7 | 0.8 | 0.8 |
静摩擦系数 | 0.3 | 0.4 | 0.7 |
滚动摩擦系数 | 0.04 | 0.04 | 0.04 |
干馏炉 | 实验值/mm | 模拟值/mm | 误差值/% |
---|---|---|---|
无绕流件 | 56.1 | 57.8 | 3.0 |
直板绕流件 | 66.3 | 65.2 | 1.7 |
前半圆绕流件 | 68.7 | 68.1 | 0.9 |
后半圆绕流件 | 67.7 | 66.2 | 2.2 |
圆柱绕流件 | 72.2 | 69.0 | 4.4 |
干馏炉 | 实验值/mm | 模拟值/mm | 误差值/% |
---|---|---|---|
无绕流件 | 56.1 | 57.8 | 3.0 |
直板绕流件 | 66.3 | 65.2 | 1.7 |
前半圆绕流件 | 68.7 | 68.1 | 0.9 |
后半圆绕流件 | 67.7 | 66.2 | 2.2 |
圆柱绕流件 | 72.2 | 69.0 | 4.4 |
回转干馏炉类型 | 时均M |
---|---|
无扰流件 | 0.290 |
圆柱扰流件 | 0.405 |
前半圆扰流件 | 0.412 |
后半圆扰流件 | 0.423 |
直板扰流件 | 0.395 |
回转干馏炉类型 | 时均M |
---|---|
无扰流件 | 0.290 |
圆柱扰流件 | 0.405 |
前半圆扰流件 | 0.412 |
后半圆扰流件 | 0.423 |
直板扰流件 | 0.395 |
回转干馏炉类型 | |
---|---|
圆柱扰流件 | 82.8° |
前半圆扰流件 | 78.9° |
后半圆扰流件 | 104.6° |
直板扰流件 | 55.8° |
回转干馏炉类型 | |
---|---|
圆柱扰流件 | 82.8° |
前半圆扰流件 | 78.9° |
后半圆扰流件 | 104.6° |
直板扰流件 | 55.8° |
干馏炉 | 时均总动能 /10-4J | 时均总势能 /10-3J | 时均总机械能 /10-3J | 机械能差 /10-3J |
---|---|---|---|---|
无扰流件 | 3.80 | -7.30 | -6.92 | 3.08 |
直板 | 5.89 | -5.01 | -4.42 | 5.58 |
前半圆 | 5.54 | -4.95 | -4.39 | 5.61 |
后半圆 | 5.71 | -4.36 | -3.79 | 6.21 |
圆柱 | 5.30 | -4.73 | -4.20 | 5.80 |
干馏炉 | 时均总动能 /10-4J | 时均总势能 /10-3J | 时均总机械能 /10-3J | 机械能差 /10-3J |
---|---|---|---|---|
无扰流件 | 3.80 | -7.30 | -6.92 | 3.08 |
直板 | 5.89 | -5.01 | -4.42 | 5.58 |
前半圆 | 5.54 | -4.95 | -4.39 | 5.61 |
后半圆 | 5.71 | -4.36 | -3.79 | 6.21 |
圆柱 | 5.30 | -4.73 | -4.20 | 5.80 |
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