基于动力学线性化的先进过程控制策略在蛋氨酸结晶中的应用

王志轩 ,  张玉玺 ,  朱英涛 ,  汤伟伟 ,  龚俊波

天津大学学报(自然科学与工程技术版) ›› 2026, Vol. 59 ›› Issue (10) : 1091 -1099.

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天津大学学报(自然科学与工程技术版) ›› 2026, Vol. 59 ›› Issue (10) : 1091 -1099. DOI: 10.11784/tdxbz202511011

基于动力学线性化的先进过程控制策略在蛋氨酸结晶中的应用

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Application of Advanced Process Control Strategy Based on Kinetic Linearization in Methionine Crystallization

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摘要

蛋氨酸在工业结晶过程中存在稳定性差、工况复杂以及产品易团聚等诸多问题,导致产品质量不稳定,生产系统很难持续高效运行.本文使用了导流筒-挡板型结晶器,配备完整的控制系统、循环系统以及分离系统.控制系统依托单回路和串级控制,并使用可靠的质量流量计、在线粒度分析仪等工业仪表,获得二次成核过程关键参数,实现对结晶过程变量的间接感知.进一步将结晶动力学各控制变量通过变换进行线性化处理,并引入先进过程控制策略,成功构建了适用性较强的多变量动力学混合控制体系.工业化应用后,人工调控频率在进料不稳定的工况下由初始的 8 次/h 降至 0 次/h,实现搅拌转速和母液采出的自动控制,D10、D50 和 D90 波动现象显著收敛.产品核心质量指标与市售产品相近,粒径分布由双峰现象趋向正态分布,产品堆积密度提高约 10%,显微形貌显示团聚情况得到有效抑制.先进过程控制策略的应用在强耦合与大时滞条件下仍具有较好的鲁棒性和可用性,能够大幅减少人工干预频次,实现蛋氨酸结晶产品质量的有效控制,显著提高蛋氨酸工业结晶过程的稳定性及产品一致性.

Abstract

Methionine crystallization faces numerous challenges in industrial crystallization processes,such as poor stability,complex operating conditions,and product agglomeration. These issues lead to unstable product quality and make it difficult to maintain sustained,efficient operation of the methionine production system. Herein,a draft tube-baffle crystallizer was employed,equipped with a complete control system,a circulation system,and a separation system. The control system used single-loop and cascade control strategies and incorporated reliable industrial instruments,such as mass flow meters and online particle size analyzers,to monitor key parameters of secondary nucleation,thereby enabling indirect observation of crystallization process variables. Furthermore,by transforming and linearizing the control variables of crystallization kinetics and introducing advanced process control strategies,a highly adaptable multivariable kinetic hybrid control system was successfully implemented. After industrial application,under conditions of unstable feed,the frequency of manual adjustments decreased from eight times per hour to zero,achieving automatic control of stirring speed and mother liquor discharge. Fluctuations in D10,D50,and D90 significantly converged,and the core quality indicators of the product became comparable to those of commercially available methionine. Additionally,the particle size distribution shifted from a bimodal pattern toward a normal distribution. The bulk density of the product increased by about 10%,and microscopic analysis revealed that agglomeration was effectively suppressed. Even under conditions of strong coupling and significant time delays,the advanced process control strategies proved robust and effective. This approach substantially decreases manual intervention,ensures precise control of methionine product quality,and markedly improves the stability and uniformity of the industrial methionine crystallization process.

关键词

蛋氨酸 / 工业结晶 / 过程控制 / 模型开发

Key words

methionine / industrial crystallization / process control / model development

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引用格式 ▾
王志轩,张玉玺,朱英涛,汤伟伟,龚俊波. 基于动力学线性化的先进过程控制策略在蛋氨酸结晶中的应用[J]. 天津大学学报(自然科学与工程技术版), 2026, 59(10): 1091-1099 DOI:10.11784/tdxbz202511011

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参考文献

[1]

龚俊波,孙 杰, 王静康. 面向智能制造的工业结晶研究进展[J]. 化工学报, 2018, 69(11): 4505-4517.

[2]

Gong Junbo, Sun Jie, Wang Jingkang. Research progress of industrial crystallization towards intelligent manufacturing[J]. CIESC Journal, 2018, 69(11): 4505-4517(in Chinese).

[3]

Ferguson S, Morris G, Hao H X, et al. In-situ monitoring and characterization of plug flow crystallizers[J]. Chemical Engineering Science, 2012, 77:105-111.

[4]

Braatz R D. Advanced control of crystallization processes[J]. Annual Reviews in Control, 2002, 26:87-99.

[5]

Rawlings J B, Sink C W, Miller S M. Control of crystallization processes[M]// Handbook of Industrial Crystallization. 2nd ed. Boston:Butterworth-Heinemann, 2002.

[6]

Worlitschek J, Mazzotti M. Model-based optimization of particle size distribution in batch-cooling crystallization of paracetamol[J]. Crystal Growth & Design, 2004, 4(5): 891-903.

[7]

Nagy Z K, Braatz R D. Advances and new directions in crystallization control[J]. Annual Review of Chemical and Biomolecular Engineering, 2012, 3:55-75.

[8]

Nagy Z K, Fevotte G, Kramer H, et al. Recent advances in the monitoring,modelling and control of crystallization systems[J]. Chemical Engineering Research and Design, 2013, 91(10): 1903-1922.

[9]

Mullin J W, Nývlt J. Programmed cooling of batch crystallizers[J]. Chemical Engineering Science, 1971, 26(3): 369-377.

[10]

Jones A G, Mullin J W. Programmed cooling crystallization of potassium sulphate solutions[J]. Chemical Engineering Science, 1974, 29(1): 105-118.

[11]

Tacsi K,Gyürkés M,Csontos I, et al. Polymorphic concentration control for crystallization using Raman and attenuated total reflectance ultraviolet visible spectroscopy[J]. Crystal Growth & Design, 2020, 20(1): 73-86.

[12]

Shikata F, Kimura S, Hattori Y, et al. Real-time monitoring of granule properties during high shear wet granulation by near-infrared spectroscopy with a chemometrics approach[J]. RSC Advances, 2017, 7(61): 38307-38317.

[13]

Howard K S, Nagy Z K, Saha B, et al. A process analytical technology based investigation of the polymorphic transformations during the antisolvent crystallization of sodium benzoate from IPA/water mixture[J]. Crystal Growth & Design, 2009, 9(9): 3964-3975.

[14]

Kadam S S, van der Windt E, Daudey P J, et al. A comparative study of ATR-FTIR and FT-NIR spectroscopy for in-situ concentration monitoring during batch cooling crystallization processes[J]. Crystal Growth & Design, 2010, 10(6): 2629-2640.

[15]

张 腾. 基于模拟与过程分析技术的结晶先进控制策略[D]. 天津:天津大学, 2020.

[16]

Zhang Teng. Study on Advanced Crystallization Control Strategy Based on Modeling and Process Analytical Technology[D]. Tianjin:Tianjin University, 2020(in Chinese).

[17]

Aamir E, Nagy Z K, Rielly C D, et al. Combined quadrature method of moments and method of characteristics approach for efficient solution of population balance models for dynamic modeling and crystal size distribution control of crystallization processes[J]. Industrial and Engineering Chemistry Research, 2009, 48(18): 8575-8584.

[18]

Mesbah A, Huesman A E M, Kramer H J M, et al. A comparison of nonlinear observers for output feedback model-based control of seeded batch crystallization processes[J]. Journal Process Control, 2011, 21(4): 652-666.

[19]

Mesbah A, Huesman A E M, Kramer H J M, et al. Real-time control of seeded batch crystallization processes[J]. AICHE Journal, 2011, 57(6): 1557-1569.

[20]

Ma C Y, Wang X Z. Simultaneous characterization of multiple properties of solid and liquid phases in crystallization processes using NIR[J]. Particuology, 2011, 9(6): 589-597.

[21]

Doki N, Seki H, Takano K, et al. Process control of seeded batch cooling crystallization of the metastable α-form glycine using an in-situ ATR-FTIR spectrometer and an in-situ FBRM particle counter[J]. Crystal Growth & Design, 2004, 4(5): 949-953.

[22]

Cote A, Zhou G, Stanik M. A novel crystallization methodology to ensure isolation of the most stable crystal form[J]. Organic Process Research & Development, 2009, 13(6): 1276-1283.

[23]

赵绍磊, 王耀国,张 腾, 等. 制药结晶中的先进控制[J]. 化工学报, 2020, 71(2): 459-474.

[24]

Zhao Shaolei, Wang Yaoguo, Zhang Teng, et al. Advanced control in pharmaceutical crystallization[J]. CIESC Journal, 2020, 71(2): 459-474(in Chinese).

[25]

Brkar M R A, Nagy Z K, Saleemi A N, et al. The impact of direct nucleation control on crystal size distribution in pharmaceutical crystallization processes[J]. Crystal Growth & Design, 2009, 9(3): 1378-1384.

[26]

Liu G J, Li J J, Deng S M. Applications of supercritical anti-solvent process in preparation of solid multicomponent systems[J]. Pharmaceutics, 2021, 13(4): 475.

[27]

Fujiwara M, Nagy Z K, Chew J W, et al. First-principles and direct design approaches for the control of pharmaceutical crystallization[J]. Journal of Process Control, 2005, 15(5): 493-504.

[28]

关国强,唐 凯,李 红, 等. 基于 ATR-UV 实时浓度检测的扑热息痛冷却结晶过程研究[J]. 化工学报, 2015, 66(9): 3580-3587.

[29]

Guan Guoqiang, Tang Kai, Li Hong, et al. Cooling crystallization of paracetamol in ethanol solution based on real-time ATR-UV measurement[J]. CIESC Journal, 2015, 66(9): 3580-3587(in Chinese).

[30]

Saleemi A N, Steele G, Pedge N I, et al. Enhancing crystalline properties of a cardiovascular active pharmaceutical ingredient using a process analytical technology based crystallization feedback control strategy[J]. International Journal of Pharmaceutics, 2012, 430(1/2): 56-64.

[31]

Nagy Z K, Fujiwara M, Braatz R D. Modelling and control of combined cooling and antisolvent crystallization processes[J]. Journal of Process Control, 2008, 18(9): 856-864.

[32]

Simon L L, Pataki H, Marosi G, et al. Assessment of recent process analytical technology(PAT)trends: A multiauthor review[J]. Organic Process Research & Development, 2015, 19(1): 3-62.

[33]

Ghadipasha N, Romagnoli J A, Tronci S, et al. A model-based approach for controlling particle size distribution in combined cooling-antisolvent crystallization processes[J]. Chemical Engineering Science, 2018, 190:260-272.

[34]

Aamir E, Rielly C D, Nagy Z K. Experimental evaluation of the targeted direct design of temperature trajectories for growth-dominated crystallization processes using an analytical crystal size distribution estimator[J]. Industrial & Engineering Chemistry Research, 2012, 51(51): 16677-16687.

[35]

许 秀. 科里奥利质量流量计原理及其应用[J]. 工业仪表与自动化装置, 2005(1): 52-58.

[36]

Xu Xiu. Coriolis mass flowmeter and its application[J]. Industrial Instrumentation & Automation Device, 2005(1): 52-58(in Chinese).

[37]

Imran A, Wolf E, Kramer H M. Contribution of crystalimpeller and crystal-crystal collisions to secondary nucleation[J]. Proceeding of European Congress of Chemical Engineering, 2007, 6:180-196.

[38]

Syamlal M, Obrien T J. Computer simulation of bubbles in a fluid bed[J]. AICHE Symposium Series, 1989, 85(270): 22-31.

[39]

Botsaris G D, Qian R Y, Barrett A. New insights into nucleation through chiral crystallization[J]. AICHE Journal, 1999, 45(1): 201-203.

[40]

Randolph A D, Larson M A. Transient and steady state size distributions in continuous mixed suspension crystallizers[J]. AICHE Journal, 1962, 8(5): 639-645.

基金资助

国家自然科学基金资助项目(22278300,22478284)

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