NUMERICAL SIMULATION OF GAS-LIQUID PHASE FLOW FIELD IN STIRRED REACTOR BASED ON OILY SLUDGE
-
摘要: 采用安东帕流变仪对不同温度下含油污泥的流变性质进行测量,并通过拟合幂律方程得到相关流变参数。基于其流变特性,以空气-含油污泥为介质采用数值模拟方法研究了含油污泥温度以及反应器结构对气液两相流场、局部气含率分布以及通气搅拌功率的影响。结果表明:随着含油污泥温度升高,搅拌桨对液相扰动范围趋广,气含率分布趋于分散,气液两相混合程度愈加均匀,通气搅拌功率下降明显;对比4种不同反应器结构,双层桨分散性能最佳,液相平均流速最高,速度均匀度指数最低,在通气搅拌功率适宜的情况下其混合性能最佳。Abstract: The rheological properties of oily sludge at different temperatures were measured by Anton Paar rheometer, and the relevant rheological parameters were obtained by fitting the power-law equation. Based on the rheological characteristics of oily sludge, the effects of oily sludge temperature and reactor structure on gas-liquid phase flow field, local gas holdup distribution and stirring power were studied by numerical simulation with air-oily sludge as the medium. The results showed that with the increase of the temperature of oily sludge, the disturbance range of the stirring paddle to the liquid phase tended to be wider, the distribution of gas holdup tended to be dispersed, the mixing degree of gas and liquid two phases became more uniform, and the aeration stirring power decreased significantly; among the four different reactor structures, the double-layer impeller had the best dispersion performance, the highest average liquid flow rate and lowest velocity uniformity index. Its mixing performance was the best with an appropriate aeration stirring power.
-
Key words:
- oily sludge /
- rheology /
- CFD simulation /
- stir
-
[1] DU M M,LI J L,WANG F F,et al.The sludge-based adsorbent from oily sludge and sawdust: preparation and optimization[J].Environmental Technology,2021,42(20):3164-3177. [2] 白冬锐,张涛,詹雨雨,等.含油污泥处理技术进展[J].环境工程,2020,38(8):207-212. [3] 罗飞,贺利乐.生物法降解含油污泥反应器流场及工作参数研究[J].中国环境科学,2022,42(4):1754-1761. [4] 王飞飞,杨鹏辉,鱼涛,等.含油污泥催化热解工艺的优化及热解产物分析[J].环境工程,2019,37(9):171-176,204. [5] 梁宏宝,张全娟,陈洪涛,等.含油污泥联合处理技术的应用现状与展望[J].环境工程技术学报,2020,10(1):118-125. [6] 杨鹏辉,魏君,屈撑囤.延长油田含油污泥真空热解研究[J].环境工程,2015,33(10):101-103. [7] 王万福,张鸿涛,邓皓,等. 利用油泥热解残渣制备新型采油废水吸附剂的方法: CN102294217A[P]. 2011-12-28. [8] 仝坤,张哲娜,孙静文,等.一种油泥处理装置:CN210287095U[P]. 2020-04-10. [9] 王凯,虞军.搅拌设备[M].北京:化学工业出版社,2003. [10] 李挺,贾卓泰,张庆华,等.几种单层桨搅拌槽内宏观混合特性的比较[J].化工学报,2019,70(1):32-38. [11] 刘作华,周毅林,熊黠,等.逆流桨强化搅拌槽内流体混沌混合及流场结构失稳研究[J].化工学报,2022,73(1):222-231. [12] 张敏,田代幸宽,酒井谦二.自吸式曝气搅拌装置用于高温好氧消化系统的供氧性能研究[J].环境工程,2020,38(8):8-12. [13] 方玉建,张敏,孙先朋,等.机械搅拌槽内非牛顿流体内流特性研究[J].机械工程学报,2021,57(20):244-253. [14] 曹秀芹,柴莲莲,徐国庆,等.基于猪粪流变特性的厌氧消化反应器内的数值模拟[J].环境工程学报,2020,14(2):498-505. [15] 郭晓攀.非牛顿流体气液两相流的实验研究与数值模拟[D].上海:华东理工大学, 2015. [16] 杨娟,张庆华,杨超,等.不同组合桨搅拌槽内非牛顿流体的微观混合特性[J].过程工程学报,2019,19(5):865-871. [17] 巩志强,褚志炜,隽永龙,等.含油污泥气化特性[J].中国石油大学学报(自然科学版),2022,46(3):188-194. [18] WU B X.CFD simulation of gas and non-Newtonian fluid two-phase flow in anaerobic digesters[J].Water Research,2010,44(13):3861-3874. [19] WU B X.CFD investigation of turbulence models for mechanical agitation of non-Newtonian fluids in anaerobic digesters[J].Water Research, 2011,45(5):2082-2094. [20] SCARGIALI F,D’ORAZIO A,GRISAFI F,et al.Modelling and simulation of gas-liquid hydrodynamics in mechanically stirred tanks[J].Chemical Engineering Research & Design,2007,85(A5):637-646. [21] KHOPKAR A R,TANGUY P A.CFD simulation of gas-liquid flows in stirred vessel equipped with dual rushton turbines: influence of parallel, merging and diverging flow configurations[J].Chemical Engineering Science, 2008,63(14):3810-3820. [22] WU H,PATTERSON G K.Laser-Doppler measurements of turbulent-flow parameters in a stirred mixer[J].Chemical Engineering Science, 1989,44(10):2207-2221. [23] 朱嘉卉.含油污泥的理化特性研究与分析[D].杭州:浙江大学,2014. [24] 杨洁,刘天璐,宋慧波,等.微乳液法降低含油污泥黏度[J].化工学报,2016,67(7):2963-2969. [25] 张金强,刘仁鑫,杨卫平.基于CFD的堆肥反应器通气搅拌结构优化设计[J].农机化研究,2020,42(5):243-249. [26] 程群群,陈迁乔,戚莉,等.不同温度下空气-聚醚多元醇的搅拌特性[J].化工进展,2011,30(11):2376-2381. [27] 曹秀芹,徐国庆,袁海光,等.污泥厌氧消化反应器CFD数值模拟研究进展[J].环境工程学报,2018,12(11):3005-3019.
点击查看大图
计量
- 文章访问数: 142
- HTML全文浏览量: 33
- PDF下载量: 2
- 被引次数: 0