Optimal designing of cracking tower for waste tires based on heat and mass transfer model （Ⅰ）Model development

LIU Baoqing; JIANG Jialing

您当前的位置：

首页 >

文章列表页 >

Optimal designing of cracking tower for waste tires based on heat and mass transfer model （Ⅰ）Model development

更新时间：2025-12-10

- Optimal designing of cracking tower for waste tires based on heat and mass transfer model （Ⅰ）Model development
- CIESC Journal Issue 7, Pages: 1525-1531(2006)
- 作者机构：
  
  浙江大学化学工程与生物工程学系,浙江,杭州,310027
- 作者简介：
- 基金信息：
- DOI：
  CLC：
- Online First：25 July 2006，
  
  Published：25 July 2006
- 稿件说明：
移动端阅览
LIU Baoqing, JIANG Jialing. Optimal designing of cracking tower for waste tires based on heat and mass transfer model （Ⅰ）Model development[J]. CIESC Journal, 2006, (7): 1525-1531.
DOI：

LIU Baoqing, JIANG Jialing. Optimal designing of cracking tower for waste tires based on heat and mass transfer model （Ⅰ）Model development[J]. CIESC Journal, 2006, (7): 1525-1531. DOI：

摘要

新型立式多层圆盘结构裂解塔是一种传导加热型单元设备，能把无钢丝废轮胎裂解为炭黑、燃料油和可燃气产品.在料环假设、松散介质假设、物性假设基础上，研究了空心加热盘上轮胎料块的传质模型，给出了料环高度、盘面积料量、停留时间、有效覆盖率以及临界处理量等参数的计算公式.应用颗粒传热扩散理论及橡胶裂解动力学方程，建立了新型裂解塔加热盘面和轮胎料块间的传热模型，得到了裂解塔内每道料环出料温度及橡胶残余率的迭代计算公式，并从理论上给出了裂解塔的最大处理量.应用该模型对3000 t8226;a-1裂解塔进行了理论计算，所得结果与实验数据吻合较好.

Abstract

A new vertical cracking tower with multiple hollow disks was developed

which could pyrolyze waste tires into carbon black

liquid oil and fuel gas.Based on the assumptions of annular granular heap

constant angle of repose and uniform physical properties

a mass transfer model in the cracking tower for waste tires was presented.The equations for calculating several important parameters

such as height and volume of each granular heap

retention time

effective covering ratio

critical capacity were provided along with the new mass transfer model.According to the penetration model of particle heat transfer and kinetic model of tire pyrolysis

the exit temperature and rubber remnant content in granular heaps were effectively predicted by a straightforward stepwise calculation procedure

and the maximum pyrolysis capacity was predicted as well.The theoretical results predicted with the heat and mass transfer model were in satisfactory agreement with experimental data from a 3000 t8226;a-1 pilot-plant.

关键词

Keywords

references

Views

190

下载量

CSCD

Alert me when the article has been cited

提交

Tools

Publicity Resources

Airside heat and mass transfer characteristics of split fin-and-tube heat exchangers under dehumidifying conditions

Coupled processes of chemical reaction, heat and mass transfer in non-thermal equilibrium porous medium

Liquid-liquid mass transfer performance of jet external loop reactor

Transfer study of Cu(Ⅱ) through hollow fiber renewal liquid membrane with LIX984N as carrier

Observation on Marangoni convection induced by desorption in falling soap film

Related Author

MA Xiaokui

DING Guoliang

ZHANG Yuanming

LI Mingchun

TIAN Yanwen

ZHAI Yuchun

XIA Rong’an

LIU Zhichang

Related Institution

上海交通大学制冷与低温工程研究所

东北大学冶金物理化学所

中国石油大学（北京）重质油国家重点实验室

北京化工大学化工资源有效利用国家重点实验室

厦门大学化学化工学院

⁰