石油炼制与化工 ›› 2023, Vol. 54 ›› Issue (12): 135-142.

• 设备及防腐 • 上一篇    下一篇

渣油加氢空气冷却器NH4Cl结晶影响因素分析及沉积特性预测研究

顾友杰1,金浩哲2,张艺骞1,偶国富1   

  1. 1. 常州大学流动腐蚀与智能防控研究所
    2. 浙江理工大学流动腐蚀研究所
  • 收稿日期:2023-03-29 修回日期:2023-08-14 出版日期:2023-12-12 发布日期:2023-12-05
  • 通讯作者: 顾友杰 E-mail:higu2453@163.com
  • 基金资助:
    国家自然科学基金;国家自然科学基金;江苏省研究生科研与实践创新计划项目

ANALYSIS OF INFLUENCING FACTORS ON NH4Cl CRYSTALLIZATION AND PREDICTION OF DEPOSITIVE CHARACTERISTICS IN RESIDUAL OIL HYDROGENATION AIR COOLER

  • Received:2023-03-29 Revised:2023-08-14 Online:2023-12-12 Published:2023-12-05
  • Contact: You-Jie Gu E-mail:higu2453@163.com

摘要: 渣油加氢装置因原料劣化腐蚀性强,设备长期处于极端运行工况下,导致冷换设备铵盐腐蚀性风险大。以沸腾床渣油加氢系统空气冷却器(简称空冷器)为研究对象,采用NRTL-RK模型构建多组分体系下反应流出物系统化学离子-平衡模型,并通过工艺过程关联分析和数值模拟分析相结合的方式,对系统内铵盐结晶腐蚀风险进行评估。计算结果表明,空冷器存在NH4Cl腐蚀风险,结晶温度为169~187 ℃,且铵盐结晶速率随着温度降低不断增加,极限工况下为0.22 kg/h。空冷器对流换热模型通过组分运输方程和冷凝模型构建,数值模拟结果表明,随着流动的持续,最大的传质系数(1.52×10-4 m/s)和腐蚀速率(0.43 mm/a)出现在出口集合管底部。

关键词: 沸腾床渣油加氢, 空气冷却器, 铵盐结晶, 沉积预测, 风险评价

Abstract: With the depletion of crude oil resources, a large number of highly corrosive inferior crude oils are refined in China. Among them, ammonium salt corrosion risk of cold exchange equipment is high due to strong corrosiveness of raw material and long-term extreme operating conditions of equipment. In this paper, the air cooler of the fluidized bed residue hydrogenation system was taken as the research object, and NRTL-RK model was used to construct the chemical ion-equilibrium model of the reaction effluent system under the multi-component system. Through the process correlation analysis and numerical simulation analysis, the risk of ammonium salt crystallization corrosion in the system was evaluated. The process calculation results showed that there was corrosion risk of ammonium chloride in the air cooler of the system, the crystallization temperature was 169-187 ℃, and the crystallization rate of ammonium salt increased continuously with the decrease of temperature, the limit operating condition was 0.22 kg/h. The convection heat transfer model of air cooler was constructed by component transport equation and condensation model. The numerical simulation results showed that the maximum mass transfer coefficient (1.52×10-4 m/s) and corrosion rate (0.43 mm/a) occurred at the bottom of the outlet manifold.

Key words: hydrogenation of residue in boiling bed, air cooler, ammonium salt crystallization, sediment prediction, risk evaluation