Co-reporter:Yin-Ning Zhou and Zheng-Hong Luo
Polymer Chemistry 2013 vol. 4(Issue 1) pp:76-84
Publication Date(Web):29 Aug 2012
DOI:10.1039/C2PY20575K
In this work, we report an example of the facile synthesis of methyl methacrylate/tert-butyl acrylate (MMA/tBA) gradient copolymers (poly(MMA-grad-tBA) using the Cu(0) and conventional ATRP ligands as catalysts in DMF solvent at 25 °C. Semi-batch copper(0)-mediated living radical copolymerization technique (Cu(0)-mediated LRP) was used for achieving the chain gradient microstructure of the resulting copolymers. We also compared copolymerizations with two different ATRP ligands at ambient temperature allowing control over the molecular weight and polydispersity with a quarter of catalyst concentration versus a conventional ATRP in dipolar protic solvent (i.e. DMF), while the reaction temperature up to 80 °C in a non-polar medium (i.e. toluene) in order to reach the above polymerization efficiency. The addition of a small amount of reducing agent (i.e. hydrazine hydrate) into the reaction system allows the reaction proceeding in the oxygen tolerant system without losing control and decreasing total conversion such as using the reagents without deoxygenating.
Co-reporter:Jian-Jian Wang, Yin-Ning Zhou, Ping Wang and Zheng-Hong Luo
RSC Advances 2013 vol. 3(Issue 15) pp:5045-5055
Publication Date(Web):30 Jan 2013
DOI:10.1039/C3RA22682D
A series of fluorene-based rod–coil block copolymers with different lengths of fluorine-containing coil segments (poly[2,7-(9,9-dihexylfluorene)]-block-poly (2,2,3,3,4,4,4-heptafluorobutyl methacrylate), PF-b-PHFBMA) were well designed and successfully synthesized via atom transfer radical polymerization (ATRP). The thermal behavior, optical properties and surface properties of these rod–coil block copolymers were investigated. The thermal properties of the copolymers presented a good thermal stability, while the optical properties did not show a noticeable dependence on the lengths of the coil segments. In addition, they showed a high dependence on the self-assembly behavior in selective solvents. The surface properties were obviously influenced by the structure of the micelles formed in different selective solvents (i.e. THF, CHCl3 and C2F3Cl3). The incorporation of the fluorine-containing coil segments in the polyfluorene-based polymers yielded a low energy surface and various interesting surface morphologies, which gives the polymers many potential applications.
Co-reporter:Xiong-Fa Yang;Tao Zheng;Li-Ming Che
Journal of Applied Polymer Science 2013 Volume 128( Issue 6) pp:4302-4313
Publication Date(Web):
DOI:10.1002/app.38668
Abstract
The use of distributed parameter model is becoming a common approach for simulating liquid–solid flow in loop polymerization reactors. However, there are still several issues with it. One of them is the absence of modeling of distributed pressure, as no thermodynamic state-equation is incorporated into the model. In this work, inner pressure of the reactor was associated with temperature using a thermodynamic state-equation for high-pressure liquid. The thermodynamic state-equation was solved together with a dynamically distributed reactor model based on the mass, energy, and momentum conservation as well as polymerization kinetics to predict the dynamic trajectories of component concentration, temperature, pressure, and bulk mass velocity in the reactor. Industrial steady-state data were used for model validation. The application of the model was demonstrated by simulating the effect of recycle ratio on the above distributed reactor parameters. © 2012 Wiley Periodicals, Inc. J. Appl. Polym. Sci., 2013
Co-reporter:Lu Yu, Jing-Jing Qiu, Hua Cheng, Zheng-Hong Luo
Materials Chemistry and Physics 2013 Volume 138(2–3) pp:780-786
Publication Date(Web):15 March 2013
DOI:10.1016/j.matchemphys.2012.12.060
Gold nanoparticles “AuNPs” with improved stability against aggregation were prepared using a self-assembled ABC non-amphiphilic poly(dimethylsiloxane)-b-poly(methyl methacrylate)-b-poly(2,2,3,3,4,4,4-heptafluorobutylmethacrylate) (PDMS-b-PMMA-b-PHFBMA) triblock copolymer as a template. The polymer-stabilized AuNPs were characterized by UV–visible spectrophotometry and transmission electron microscopy (TEM). Depending on the self-assembled templates, the relatively monodispersed and stable AuNPs with an average diameter of 30 nm were obtained. Therefore the triblock copolymer was demonstrated to be an effective stabilizer for the synthesis of AuNPs. The PDMS-b-PMMA-b-PHFBMA copolymer used in the study contains siloxane and fluorinated segments and belongs to ABC non-amphiphilic triblock copolymers, which proves that the asymmetric ABC non-amphiphilic triblock copolymers can also self-assemble in a dilute solution to serve as a template, or “nanoreactors”. To the best of our knowledge, this work is the first example of facile preparation of metal nanoparticles using self-assembled ABC non-amphiphilic fluorosilicone triblock copolymer as a template. Our present work broadens the range of polymer templates that can be used to synthesize and stabilize metal nanoparticles from amphiphilic block polymers (or symmetric ABA non-amphiphilic block polymers) to asymmetric ABC non-amphiphilic block polymers. In addition, this work also broadens the application of fluorinated ABC triblock copolymers.Graphical abstractHighlights► The AuNPs are prepared using a self-assembled fluorosilicone copolymer template. ► The AuNPs are characterized by UV–visible spectrophotometry and TEM. ► The triblock copolymer is demonstrated to be an effective stabilizer for AuNPs. ► The self-assembled fluorosilicone copolymers can serve as nanoreactors. ► The first example for preparing AuNPs is via self-assembled copolymer template.
Co-reporter:Hong-Ming Zhou;Hua Cheng
Polymer Engineering & Science 2013 Volume 53( Issue 7) pp:1475-1486
Publication Date(Web):
DOI:10.1002/pen.23400
Abstract
The double-hydrophobic well-defined polydimethylsiloxane-block-poly(methyl methacrylate) (PDMS-b-PMMA) diblock copolymers were synthesized via atom transfer radical polymerization (ATRP). Their chemical compositions and the structure were investigated. The micellization behavior of the double-hydrophobic diblock copolymers with equal block length was thoroughly studied. The results showed that their self-assembly behavior was analogous to the star-like micelles. Furthermore, the effect of temperature on the aggregates was investigated to verify that the resulting copolymer (PDMS-b-PMMA) was to some extent temperature sensitive. Till date, there have been few reports on the utilization of nonamphiphilic block copolymers to synthesize and confine metal nanoparticles in aggregates. In this study, we explored the role of double-hydrophobic block copolymers as a mediator for organically dispersible silver nanoparticles (AgNPs) and it offered to be an effective stabilizer for preparing AgNPs. Besides, AgNPs generated in organic solvent is an important addition to the hitherto predominantly water-based processes for producing nanoparticles inside the polymer surfactant. POLYM. ENG. SCI., 2013. © 2012 Society of Plastics Engineers
Co-reporter:Jie Chen;Jin-Jin Li
Journal of Polymer Science Part A: Polymer Chemistry 2013 Volume 51( Issue 5) pp:1107-1117
Publication Date(Web):
DOI:10.1002/pola.26473
Abstract
In this work, fluorinated nonamphiphilic gradient copolymers of tert-butyl acrylate (tBA) and 2,2,3,3,4,4,4-heptafluorobutyl methacrylate (HFBMA) [poly(tBA-grad-HFBMA)] were first synthesized by semibatch atom transfer radical copolymerization of tBA and HFBMA. Their hydrolysis at acidic conditions led to amphiphilic poly(acrylic acid-grad-HFBMA). The chemical compositions and structures of these copolymers were characterized by proton nuclear magnetic resonance spectroscopy, Fourier transform infrared spectroscopy, and gel permeation chromatography. Their surface properties were evaluated with water contact angle measurement and x-ray photoelectron spectroscopy. The micellization behaviors of amphiphilic copolymer were also studied by transmission electron microscopy and dynamic light scattering. The results showed that the fluorinated and amphiphilic gradient copolymers could self-assemble in a dilute solution to form aggregates of morphologies. Furthermore, the effect of pH on the aggregates was investigated to verify that the resulting gradient copolymers were to some extent pH sensitive. © 2012 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem, 2013
Co-reporter:Xiaomin Chen, Jiu Dai, Zhenghong Luo
Particuology 2013 Volume 11(Issue 6) pp:703-714
Publication Date(Web):December 2013
DOI:10.1016/j.partic.2012.11.008
•Catalytic syngas dehydrogenation was controlled by dissociation–adsorption of O2.•A porous medium CFD model coupled with kinetics was used to simulate syngas dehydrogenation FBR.•Simulation results were in a reasonable agreement with experimental data.•Inlet gas temperature and composition affected hot spot temperature and H2 conversion.A comprehensive 2D computational fluid dynamics (CFD) model was developed to simulate the flow behavior and catalytic dehydrogenation reaction of syngas in a heterogenous fixed-bed reactor (FBR). The model combined the porous medium CFD model with a reaction kinetics model. To acquire an accurate reaction kinetics model, a comprehensive reaction mechanism was studied for the heterogeneous catalytic dehydrogenation reaction of syngas over a supported metal catalyst. Based on the reaction mechanism and a statistical test, a reliable kinetics model was proposed. The CFD model combined with the above kinetics model was validated with one set of experimental data. The CFD model was also used to predict key reaction variable distributions such as the temperature and the component concentrations in the reactor.
Co-reporter:Jin-Jin Li, Yin-Ning Zhou and Zheng-Hong Luo
Soft Matter 2012 vol. 8(Issue 43) pp:11051-11061
Publication Date(Web):05 Oct 2012
DOI:10.1039/C2SM26539G
A series of brush copolymers (i.e. poly(methyl methacrylate (MMA)-co-2-(2-bromoisobutyryloxy)ethyl methacrylate (BIEM)-graft-acrylic acid (AA))) having three backbone composition profiles, i.e. random, gradient and block, were synthesized via the combination of atom transfer radical polymerization (ATRP)/model-based semibatch ATRcoP and the “grafting from” method. These samples allowed us to systematically investigate the effects of the composition profile (including the grafting density corresponding to the composition profile) on the micelle formation and pH responsivity of the brush copolymers in solution. FTIR, 1H NMR and GPC were used to provide evidence for the formation of the well-defined brush copolymers. TEM, light transmittance and DLS were used to investigate the self-assembly and pH responsivity of the resulting copolymers. It was found that the micelles formed by these copolymers underwent a different conformational transition caused by the change from acidic to basic in the solution. These transitions were mainly influenced by pH and composition profile since the composition profile also had a strong effect on the acid-dissociation degree of the brush copolymer.
Co-reporter:Wei-Cheng Yan, Jiang Li, Zheng-Hong Luo
Powder Technology 2012 Volume 231() pp:77-87
Publication Date(Web):November 2012
DOI:10.1016/j.powtec.2012.07.047
An Eulerian–Eulerian two-fluid coupling the population balance model (PBM) is developed to describe the gas–solid two-phase flow in a multizone circulating polymerization reactor (MZCR). The polymerization kinetics is also incorporated into the coupled model by using a user-defined function (UDF). The model is first used to predict the entire field in the MZCR with considering the polydispersity of solid phase. Furthermore, the temperature field is obtained numerically with considering polymerization reaction, and the effect of inlet gas temperature on the temperature field is also investigated. Finally, the model is adopted to distinguish between the flow behaviors in a circulating fluidized bed reactor (CFBR) and a MZCR. The simulated results show that the flow behavior in the MZCR with polydisperse solid phase is different from that with uniform particle size and the inlet gas temperature has great effects on the temperature distribution. Moreover, the simulation results also show that the differences in between CFBR and MZCR are mainly embodied in the temperature distribution.A CFD-PBM model is developed to describe the gas–solid two-phase flow in a multizone circulating polymerization reactor (MZCR). The polymerization kinetics is also incorporated into the CFD-PBM model. The entire fields in the MZCR are obtained numerically. The model is also used to distinguish the flow behaviors in between a circulating fluidized bed reactor (CFB) and a MZCR.Highlights► We present a CFD-PBM model to describe the flow field in a polymerization MZCR. ► The CFD-PBM model incorporates propylene polymerization kinetics. ► The entire field in the MZCR with the solid PSD is predicted via the model. ► The model is used to distinguish between the flow behavior in MZCR and CFBR. ► The results show that the temperature field in a CFBR is different from that in a MZCR.
Co-reporter:Wei-Cheng Yan, Guo-Qiang Chen, and Zheng-Hong Luo
Industrial & Engineering Chemistry Research 2012 Volume 51(Issue 46) pp:15132
Publication Date(Web):October 31, 2012
DOI:10.1021/ie301923n
In this work, the CFD modeling approach, which is an old approach in chemical engineering, is extended to the propylene polymerization process in a multizone circulating reactor (MZCR) in order to design a new gas-barrier system in the MZCR from the fluid-dynamics viewpoint. First, the CFD modeling approach based on an Eulerian–Eulerian model, incorporating a kinetic theory of granular flow, is applied to describe the gas–solid flow in a polypropylene MZCR. Furthermore, the modeling approach is used to obtain important operation data of the gas-barrier inlet and to optimize the gas-barrier inlet configuration. Accordingly, the entire field in the MZCR with the optimal gas-barrier system above is predicted. The simulation results show that the four-way tangential gas-barrier configuration is suitable in the MZCR, which is the first use of a gas-barrier inlet that allows an optimal flow field in the MZCR. This article has reported an old approach in chemical engineering that has been applied to a new field for the purpose of designing a new gas barrier, which opens up a new research field in the olefin polymerization process.
Co-reporter:Ya-Qing Zhuang, Xi Gao, Ya-ping Zhu, Zheng-hong Luo
Powder Technology 2012 Volume 221() pp:419-430
Publication Date(Web):May 2012
DOI:10.1016/j.powtec.2012.01.041
A comprehensive two-dimensional (2D) reactor model has been developed to simulate the flow behavior in a fixed-bed reactor for preparing olefins from methanol. An exponent-function kinetic model based on a lumped-species reaction scheme has been incorporated to a commercial computational fluid dynamics (CFD) code Fluent by user defined functions for simulating the methanol to olefins (MTO) reaction. The approach and model have been validated with the actual data collected from open reports where the above kinetic model is adopted. Furthermore, the coke deposition and the component distributions during the MTO reaction over SAPO-34 have been simulated in the fixed bed reactor as a function of feed temperature (673–753 K), space velocity (57–113g ⋅ (gcat ⋅ h)− 1) and feed composition. In addition, the optimizational simulation has also been done. The simulation results show that the methanol conversion and the catalytic deactivation are closely related to each other and are obviously influenced by operation conditions studied in this work.A reactor model incorporating an exponent-function kinetic model based on a lumped-species reaction scheme has been developed to simulate the flow behavior in a fixed-bed reactor for preparing olefins from methanol. The coke deposition and the component distributions during the MTO reaction have been simulated. The optimizational simulation has also been done.Highlights► We present a CFD model to describe the flow in a MTO FBR. ► A MTO kinetic equation is incorporated. We test the CFD model. ► We predict the flow and MTO behaviors in the MTO FBR. ► We predict the effects of operating conditions on the MTO FBR.
Co-reporter:Cheng-Mei Guan;Pei-Ping Tang
Journal of Applied Polymer Science 2012 Volume 123( Issue 2) pp:1047-1055
Publication Date(Web):
DOI:10.1002/app.34570
Abstract
Well-defined polydimethylsiloxane-block-polystyrene (PDMS-b-PS) diblock copolymers were prepared by reversible addition-fragmentation chain transfer (RAFT) polymerization using a functional PDMS-macro RAFT agent. The RAFT polymerization kinetics was simulated by a mathematical model for the RAFT polymerization in a batch reactor based on the method of moments. The model described molecular weight, monomer conversion, and polydispersity index as a function of polymerization time. Good agreements in the polymerization kinetics were achieved for fitting the kinetic profiles with the developed model. In addition, the model was used to predict the effects of initiator concentration, chain transfer agent concentration, and monomer concentration on the RAFT polymerization kinetics. © 2011 Wiley Periodicals, Inc. J Appl Polym Sci, 2011
Co-reporter:Ji-Rong Wu;Guo-Qiao Lai;Hai-Jiang Yu
Journal of Applied Polymer Science 2012 Volume 124( Issue 5) pp:3821-3830
Publication Date(Web):
DOI:10.1002/app.35469
Abstract
Poly(γ-methacryloxypropyltrimethoxysilane) (PMPTS)-grafted silica hybrid nanoparticles were prepared by surface-initiated atom transfer radical polymerization (SI-ATRP). The resulting PMPTS-grafted silica hybrid nanoparticles were characterized using Fourier transform infrared spectroscopy (FTIRS), nuclear magnetic resonance (NMR), gel permeation chromatography (GPC), X-ray photoelectron spectroscopy (XPS), atomic force microscopy (AFM), scanning electron microscopy (SEM), static water contact angle (WCA) measurement, and thermogravimetric analysis (TGA). Combined FTIRS, NMR, XPS, SEM, and TGA studies confirmed that these hybrid nanoparticles were successfully prepared by surface-initiated ATRP. SEM and AFM studies revealed that the surfaces of the nanoparticles were rough at the nanoscale. In addition, the results of the static WCA measurements showed that the nanoparticles are of low surface energy and their surface energy reaches as low as 6.10 mN m−1. © 2011 Wiley Periodicals, Inc. J Appl Polym Sci, 2012
Co-reporter:Hua Cheng;Jin-Jin Li
Journal of Polymer Science Part A: Polymer Chemistry 2012 Volume 50( Issue 7) pp:1249-1253
Publication Date(Web):
DOI:10.1002/pola.25871
Co-reporter:Yin-Ning Zhou;Jin-Jin Li
Journal of Polymer Science Part A: Polymer Chemistry 2012 Volume 50( Issue 15) pp:3052-3066
Publication Date(Web):
DOI:10.1002/pola.26091
Abstract
Recent studies have demonstrated that gradient copolymers exhibit unique thermal properties. Although these properties can be determined by copolymer composition, other factors such as chain and sequence lengths and their distributions can also influence them. Accordingly, the synthesis of gradient copolymers requires simultaneously tailor-made chain structure and thermal properties. In this work, we carried out a systematic study on the preparation of poly(methyl methacrylate-grad-2-hydroxyethyl methacrylate) [poly(MMA-grad-HEMA)] with synchronously tailor-made chain composition distribution and glass transition temperature (Tg) through semibatch atom transfer radical polymerization. First, a comprehensive model for simultaneously predicting gradient copolymer microstructure and Tg was presented using the concept of pseudo-kinetic rate coefficients and Johnston equation. The model was validated by comparing simulation results with the classical reference data. Furthermore, the model was used to guide the experimental synthesis of the poly(MMA-grad-HEMA) gradient copolymers potentially as excellent damping material. The thermal properties of these gradient copolymer samples were evaluated. © 2012 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem, 2012
Co-reporter:Li-Hong Wei, Wei-Cheng Yan, Zheng-Hong Luo
Powder Technology 2011 Volume 214(Issue 1) pp:143-154
Publication Date(Web):25 November 2011
DOI:10.1016/j.powtec.2011.08.005
A Eulerian–Eulerian model incorporating the kinetic theory of granular flow is adopted to describe the gas–solid two-phase flows in a multizone circulating propylene polymerization reactor. Corresponding simulations are carried out in a commercial computational fluid dynamics (CFD) code Fluent. First, the model is validated by comparing simulation results with the experimental data. Entire fields in the reactor composed of a riser and a downer are also obtained numerically. Furthermore, the model is used to distinguish the flow behaviors in the riser and the downer. The effects of riser-outlet configuration and operation gas velocity on the flow behaviors in the reactor are also investigated numerically. The simulated results show that the flow behaviors in the riser of MZCR are different from those in the downer of MZCR. In addition, the simulation results also show that both the exit configuration of the riser and the operation gas velocity can significantly affect the flow behaviors in the MZCR.Graphical abstractHighlights► We present a CFD model to describe the flow in a multizone circulating propylene polymerization reactor. ► We incorporate the kinetic theory of granular flow into the CFD model. ► The model is validated by comparing simulation results with the experimental data. ► We distinguish the flow behaviors in the riser and the downer using the CFD model. ► We investigate the effects of riser-outlet configuration and operation gas velocity in the riser using the CFD model.
Co-reporter:Xi-Zhong Chen, De-Pan Shi, Xi Gao, Zheng-Hong Luo
Powder Technology 2011 Volume 205(1–3) pp:276-288
Publication Date(Web):10 January 2011
DOI:10.1016/j.powtec.2010.09.039
Co-reporter:Zu-Wei Zheng, De-Pan Shi, Pei-Lin Su, Zheng-Hong Luo, and Xiao-Jun Li
Industrial & Engineering Chemistry Research 2011 Volume 50(Issue 1) pp:322-331
Publication Date(Web):December 1, 2010
DOI:10.1021/ie101699b
In this work, we developed the steady-state and dynamic models for the commercial polypropylene process of Basell Spheripol technology, involving fundamental chemical engineering principles and advanced software tools, i.e., Polymers Plus and Aspen Dynamics. The models considered the important issues of physical property and thermodynamic model selection, catalyst characterization, and reactor model. Besides, a multisite catalyst with traditional Ziegler−Natta polymerization kinetics was introduced to describe the broad molecular weight distribution of the polymers produced in this polypropylene technology. Both the continuous stirred tank reactor model and the combined plug flow reactors model were proposed to simulate the reactors. Furthermore, we validated the models using industrial data and demonstrated application of the dynamic model to grade change, start up, and shut down at a certain emergent accident.
Co-reporter:Wei Wang;Zu-Wei Zheng
Journal of Applied Polymer Science 2011 Volume 119( Issue 1) pp:352-362
Publication Date(Web):
DOI:10.1002/app.32629
Abstract
A coupled-single-particle and Monte Carlo model was used to simulate propylene polymerization. To describe the effects of intraparticle transfer resistance on the polymerization kinetics, the polymeric multilayer model (PMLM) was applied. The reaction in each layer of the PMLM was described with the Monte Carlo method. The PMLM was solved together with the Monte Carlo model. Therefore, the model included the factors of the mass- and heat-transfer resistance as well as the stochastic collision nature of the polymerization catalyzed with single-site-type/multiple-site-type catalysts. The model presented results such as the polymerization dynamics, the physical diffusion effect, and the polymer molecular weight and its distribution. The simulation data were compared with the experimental/actual data and the simulation results from the uniform Monte Carlo model. The results showed that the model was more accurate and offered deeper insight into propylene polymerization within such a microscopic reaction–diffusion system. © 2010 Wiley Periodicals, Inc. J Appl Polym Sci, 2011
Co-reporter:Ke-Jian Lian;Chang-Qing Chen;Hui Liu;Ning-Xing Wang;Hai-Jiang Yu
Journal of Applied Polymer Science 2011 Volume 120( Issue 1) pp:156-164
Publication Date(Web):
DOI:10.1002/app.32682
Abstract
Well-defined poly(dimethylsiloxane)-block-poly(methyl methacrylate)-block-poly(2,2,3,3,4,4,4-heptafluorobutyl methacrylate) (PDMS-b-PMMA-b-PHFBMA) triblock copolymers were synthesized via atom transfer radical polymerization (ATRP). Surface microphase separation in the PDMS-b-PMMA-b-PHFBMA triblock copolymer films was investigated. The microstructure of the block copolymers was investigated by transmission electron microscopy (TEM) and atomic force microscopy (AFM). Surface composition was studied by X-ray photoelectron spectroscopy (XPS). The chemical composition at the surface was determined by the surface microphase separation in the PDMS-b-PMMA-b-PHFBMA triblock copolymer films. The increase of the PHFBMA content could strengthen the microphase separation behavior in the PDMS-b-PMMA-b-PHFBMA triblock copolymer films and reduce their surface tension. Comparison between the PDMS-b-PMMA-b-PHFBMA triblock copolymers and the PDMS-b-PHFBMA diblock copolymers showed that the introduction of the PMMA segments promote the fluorine segregation onto the surface and decrease the fluorine content in the copolymers with low surface energy. © 2010 Wiley Periodicals, Inc. J Appl Polym Sci, 2011
Co-reporter:Jing-Jing Qiu
Journal of Polymer Science Part A: Polymer Chemistry 2011 Volume 49( Issue 11) pp:2513-2519
Publication Date(Web):
DOI:10.1002/pola.24669
Co-reporter:Yin-Ning Zhou;Hua Cheng
Journal of Polymer Science Part A: Polymer Chemistry 2011 Volume 49( Issue 16) pp:3647-3657
Publication Date(Web):
DOI:10.1002/pola.24804
Abstract
This investigation reported the preparation of fluorinated and nonamphiphilic well-defined poly(styrene)-block-poly(2,2,3,3,4,4,4-heptafluorobutyl methacrylate) (PS-b-PHFBMA) diblock copolymers via atom transfer radical polymerization (ATRP). Their chemical composition, structure, and bulk morphology were thoroughly investigated. In addition, their self-assembly behavior in a dilute organic mixture solution was investigated. It was found that that the ATRP could be used to prepare the well-defined fluorinated and nonamphiphilic PS-b-PHFBMA diblock copolymers in a controlled manner. The results also showed that abundant morphologies including sphere, worm-like structure, and vesicle could be formed with different volume ratios of these two solvents, which proves that the nonamphiphilic fluorinated diblock copolymers can self-assemble in a dilute solution, and the aforementioned reason for self-assembly was also discussed preliminarily in this work. Finally, the effect of temperature on the aggregates was investigated to verify whether the self-assembly behavior was to some extent temperature sensitive. © 2011 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem, 2011
Co-reporter:Hai-Jiang Yu
Polymer Engineering & Science 2011 Volume 51( Issue 2) pp:218-224
Publication Date(Web):
DOI:10.1002/pen.21809
Abstract
Both silica/polystyrene (SiO2/PS) and silica/polystyrene-b-polymethacryloxypropyltrimethoxysilane (SiO2/PS-b-PMPTS) hybrid nanoparticles were synthesized via surface-initiated atom transfer radical polymerization (SI-ATRP) from SiO2 nanoparticles. The growths of all polymers via ATRP from the SiO2 surfaces were well controlled as demonstrated by the macromolecular characteristics of the grafted chains. Their wettabilities were measured and compared by water contact angle (WCA) and surface roughness. The results show that the nanoparticles possess hydrophobic surface properties. The static WCA of SiO2/PS-b-PMPTS hybrid nanoparticles is smaller than that of SiO2/PS hybrid nanoparticles, meanwhile, the surface roughness of SiO2/PS-b-PMPTS hybrid nanoparticles is yet slightly rougher than that of SiO2/PS hybrid nanoparticles, which shows that the combination and competition of surface chemistry and roughness of a solid material can finally determine its wettability. POLYM. ENG. SCI., 2011. © 2010 Society of Plastics Engineers
Co-reporter:Hai-Jiang Yu
Journal of Polymer Science Part A: Polymer Chemistry 2011 Volume 49( Issue 1) pp:174-183
Publication Date(Web):
DOI:10.1002/pola.24434
Abstract
A series of superhydrophobic poly(methacryloxypropyltrimethoxysilane, MPTS-b-2,-2,3,3,4,4,4-heptafluorobutyl methacrylate, HFBMA)-grafted silica hybrid nanoparticles (SiO2/PMPTS-b-PHFBMA) were prepared by two-step surface-initiated atom transfer radical polymerization (SI-ATRP). Under the adopted polymerization conditions in our previous work, the superhydrophobic property was found to depend on the SI-ATRP conditions of HFBMA. As a series of work, in this present study, the effects of polymerization conditions, such as the initiator concentration, the molar ratio of monomer and initiator, and the polymerization temperature on the SI-ATRP kinetics and the interrelation between the kinetics and the surface properties of the nanoparticles were investigated. The results showed that the SI-ATRP of HFBMA was well controlled. The results also showed that both the surface microphase separation and roughness of the hybrid nanoparticles could be strengthened with the increase of the molecular weight of polymer-grafted silica hybrid nanoparticles. © 2010 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem, 2010
Co-reporter:De-Pan Shi, Zheng-Hong Luo and An-Yi Guo
Industrial & Engineering Chemistry Research 2010 Volume 49(Issue 9) pp:4070
Publication Date(Web):April 5, 2010
DOI:10.1021/ie901424g
A three-dimensional computational fluid dynamics (CFD) model, using an Eulerian−Eulerian two-fluid model which incorporates the kinetic theory of granular flow, was developed to describe the gas−solid two-phase flow in fluidized-bed polymerization reactors. Corresponding simulations were carried out in a commercial CFD code Fluent. The entire flow field in the reactors was calculated by the model. The predicted pressure drop data were in agreement with the classical calculated data. In addition, the model was used to describe the solid holdup distributions, the bubble behaviors, and the solid velocity vectors in the free and agitated fluidized-bed polymerization reactors, respectively. The effects of the addition of an agitator on the gas−solid flow behaviors were preliminarily investigated via the model. The simulation results showed that the addition of an agitator can strengthen the fluidization efficiency and reduce the operation stability of the bed. However, the simulation results also showed that the total fluidization quality of the free fluidized bed was higher than that of the agitated fluidized bed at a superficial gas velocity of 0.5 m·s−1.
Co-reporter:Zheng-Hong Luo, Pei-Lin Su, and Wei Wu
Industrial & Engineering Chemistry Research 2010 Volume 49(Issue 22) pp:11232-11243
Publication Date(Web):October 5, 2010
DOI:10.1021/ie1003784
In industrial loop reactors for catalytic propylene polymerization, the reactor pressure can influence the polymerization rate, feed flow rate, and product properties, especially safe operation of the reactor. To predict the pressure change during polymerization and check the performance of pressure-relief devices in response to emergency accidents, a dynamic model was developed based on mass and energy balances as well as thermodynamics and kinetics. In this model, the pressure was related to the temperature by a state equation for high-pressure liquid. The pipeline equations of the reactors described by the conservation of mechanical energy were incorporated into the model to better predict the pressure. In addition to the pressure, the model can also predict other variables, such as temperature, slurry density, and solids holdup in the reactors. Dynamic data from an industrial plant were used for model validation. Furthermore, the application of the model was demonstrated by simulating several typical emergency accidents.
Co-reporter:Ya-Qing Zhuang, Xiang Ke, Xiao-Li Zhan, Zheng-Hong Luo
Powder Technology 2010 Volume 201(Issue 2) pp:146-152
Publication Date(Web):26 July 2010
DOI:10.1016/j.powtec.2010.03.017
Co-reporter:Xi Gao, De-Pan Shi, Xi-Zhong Chen, Zheng-Hong Luo
Powder Technology 2010 Volume 203(Issue 3) pp:574-590
Publication Date(Web):25 November 2010
DOI:10.1016/j.powtec.2010.06.025
A three-dimensional (3D) computational fluid dynamics (CFD) model, using an Eulerian–Eulerian two-fluid model which incorporates the kinetic theory of granular flow, the energy balance and heat transfer equations, was developed to describe the steady-state liquid–solid two-phase flow in a loop propylene polymerization reactor composing of loop and axial flow pump. The entire temperature field in the reactor was calculated by the model. The predicted pressure gradient data were found to agree well with the classical calculated data. Furthermore, the model was used to investigate the influences of the circulation flow velocity, the slurry concentration, the solid particle size and the cool water temperature on the temperature field in the reactor. The simulation results showed that the whole loop can be divided into four sections. In addition, the simulation results also showed that the continuous stirred-tank reactor (CSTR) assumption is invalid for the entire field in the loop reactor.
Co-reporter:De-Pan Shi, Zheng-Hong Luo, Zu-Wei Zheng
Powder Technology 2010 Volume 198(Issue 1) pp:135-143
Publication Date(Web):20 February 2010
DOI:10.1016/j.powtec.2009.11.002
Understanding hydrodynamics of tubular loop reactors is crucial in proper scale-up and design of these reactors. Computational fluid dynamics (CFD) models have shown promise in gaining this understanding. In this paper, a three-dimensional (3D) CFD model, using a Eulerian–Eulerian two-fluid model incorporating the kinetic theory of granular flow, was developed to describe the steady-state liquid–solid two-phase flow in a tubular loop propylene polymerization reactor composing of loop and axial flow pump. Corresponding simulations were carried out in the commercial CFD code Fluent. The entire flow field in the loop reactor was calculated by the model. The predicted pressure gradient data were found to agree well with the classical calculated data. Furthermore, the model was used to investigate the influences of the circulation flow velocity and the sold particle size on the solid hold-up. The simulation results showed that the solid hold-up has a relatively uniform distribution in the loop reactor at small particles in volume and high-circulation flow velocities.A three-dimensional CFD model, using a Eulerian–Eulerian two-fluid model incorporating the kinetic theory of granular flow, was developed to describe the steady-state liquid–solid two-phase flow in a tubular loop propylene polymerization reactor composing of loop and axial flow pump. The predicted pressure gradient data were found to agree well with the classical calculated data.
Co-reporter:Yin-ning Zhou, Cheng-mei Guan, Zheng-hong Luo
European Polymer Journal 2010 Volume 46(Issue 11) pp:2164-2173
Publication Date(Web):November 2010
DOI:10.1016/j.eurpolymj.2010.09.002
Well-defined poly(dimethylsiloxane)-b-poly(2,2,3,3,4,4,4-heptafluorobutylmethacryl-ate-b-poly(styrene) (PDMS-b-PHFBMA-b-PS) triblock copolymers were prepared by two-step reversible addition–fragmentation chain transfer (RAFT) polymerization. A comprehensive mathematical model for the two-step RAFT polymerization in a batch reactor was presented using the method of moments. The model described molecular weight, monomer conversion and polydispersity index as a function of polymerization time. Good agreements in the polymerization kinetics were achieved for fitting the kinetic profiles with the suggested model. In addition, the model was used to predict the effects of initiator concentration, chain transfer agent concentration and monomer concentration on the two-step RAFT polymerization kinetics. The simulated results showed that for the two-step RAFT polymerizations, the effects initiator concentration, chain transfer agent concentration and monomer concentration are identical and the influence degrees are different yet.
Co-reporter:Cheng-Mei Guan, Zheng-Hong Luo, Jing-Jing Qiu, Pei-Ping Tang
European Polymer Journal 2010 Volume 46(Issue 7) pp:1582-1593
Publication Date(Web):July 2010
DOI:10.1016/j.eurpolymj.2010.04.003
Well-defined poly(dimethylsiloxane)-b-poly(2,2,3,3,4,4,4-heptafluorobutyl methacrylate-b-poly(styrene) (PDMS-b-PHFBMA-b-PS) triblock copolymers were prepared by two-step reversible addition-fragmentation chain transfer (RAFT) polymerization. The two-step RAFT polymerization proceeded in a controlled manner as demonstrated by the macromolecular characteristics of the blocks and corresponding polymerization kinetic data. Furthermore, surface properties and morphologies of the polymers were investigated with static water contact angle (WCA) measurement, X-ray photoelectron spectroscopy (XPS), transmission electron microscopy (TEM) and atomic force microscopy (AFM) which showed low surface energy and microphase-separation surfaces.
Co-reporter:Zheng-Hong Luo;De-Pan Shi ;Yong Zhu
Journal of Applied Polymer Science 2010 Volume 115( Issue 5) pp:2962-2970
Publication Date(Web):
DOI:10.1002/app.31388
Abstract
In this study, the kinetics of propylene polymerization catalyzed with the fourth heterogeneous Ziegler-Natta catalyst is studied. More than one type of active site is present in the propylene polymerization based on an analysis of the GPC curves. A multiple active site kinetic model (MSmodel) is proposed by using Monte Carlo technique. Good agreements in the polymerization kinetics are achieved for fitting the kinetic profiles with the MSmodel. In addition, the MSmodel is used to describe the dynamic evolutions of the active sites and their effects on the propylene polymerization. The simulated results indicate that different types of active sites have different polymerization kinetics and the site type can affect the propylene polymerization kinetics. © 2009 Wiley Periodicals, Inc. J Appl Polym Sci, 2010
Co-reporter:Cheng-Mei Guan;Pei-Ping Tang
Journal of Applied Polymer Science 2010 Volume 116( Issue 6) pp:3283-3290
Publication Date(Web):
DOI:10.1002/app.31780
Abstract
Well-defined poly(dimethylsiloxane-b-styrene) diblock copolymers were prepared by reversible addition–fragmentation chain-transfer (RAFT) polymerization. Monohydroxyl-terminated polydimethylsiloxane was modified to form a functional polydimethylsiloxane/macro-RAFT agent, which was reacted with styrene to form the diblock copolymers. The chemical compositions and structures of the copolymers were characterized by proton nuclear magnetic resonance spectroscopy, Fourier transform infrared spectroscopy, and gel permeation chromatography. The surface properties and morphology of the copolymers were investigated with static water contact-angle measurements, X-ray photoelectron spectroscopy, transmission electron microscopy, and atomic force microscopy, which showed a low surface energy and microphase separation surfaces that were composed of hydrophobic domains from polydimethylsiloxane segments. © 2010 Wiley Periodicals, Inc. J Appl Polym Sci, 2010
Co-reporter:Zhenghong Luo;Hua Chen ;Wei Xu
Chinese Journal of Chemistry 2010 Volume 28( Issue 2) pp:303-308
Publication Date(Web):
DOI:10.1002/cjoc.201090071
Abstract
The design and synthesis of two aromatic amines with dendritic structures, i.e. 3,4,5-tribenzyloxyaniline (3,4,5-G1-NH2) and 2,5-dibenzyloxyaniline (2,5-G1-NH2), were conducted. A coupling reaction of three or two equivalents of benzyl bromide to one equivalent of methyl hydroxybenzoate generated methyl 3,4,5-tribenzyloxybenzoate (3,4,5-G1-COOCH3), methyl 2,5-dibenzyloxybenzoate (2,5-G1-COOCH3) and 2,6-dibenzyloxybenzoate (2,6-G1-COOCH3) in high yields. All G1-COOCH3 derivatives were studied by X-ray analysis. The results show that these dendrons have sufficient volume to be used as the fine ligands for certain catalysts. The amide intermediates (benzamide, G1-CONH2) were obtained by reaction between ammonia and G1-COOCH3. Interestingly, 2,6-dibenzyloxybenzamide (2,6-G1-CONH2) can not be prepared in the same condition, which may be due to the overlarge steric block. Sodium hypochlorite was an effective oxidant to generate methyl carbamates G1- NHCO2CH3.
Co-reporter:Zheng-Hong Luo;Shao-Hua Wen;De-Pan Shi ;Zu-Wei Zheng
Macromolecular Reaction Engineering 2010 Volume 4( Issue 2) pp:123-134
Publication Date(Web):
DOI:10.1002/mren.200900040
Co-reporter:Hai-Jiang Yu
Journal of Polymer Science Part A: Polymer Chemistry 2010 Volume 48( Issue 23) pp:5570-5580
Publication Date(Web):
DOI:10.1002/pola.24371
Abstract
Poly(siloxane-fluoroacrylate)-grafted silica hybrid nanoparticles were prepared by surface-initiated atom transfer radical polymerization (SI-ATRP). The silica nanoparticles with α-bromo-ester initiator group for copper-mediated ATRP were prepared by the self-assembled monolayers of (3-aminopropyl)triethoxysilane and 2-bromoisobutyrate bromide. Well-defined diblock copolymer brushes consisting of poly(methacryloxypropyltrimethoxysilane) and poly(2,2,3,3,4,4,4-heptafluorobutyl methacrylate) blocks were obtained by using initial homopolymer brushes as the macroinitiators for the SI-ATRP of the second monomer. Chemical compositions and structures of the nanoparticles were characterized by Fourier transform infrared spectroscopy, proton nuclear magnetic resonance spectroscopy, and gel permeation chromatography. Surface properties and morphology of the nanoparticles were investigated with X-ray photoelectron spectroscopy, scanning electron microscopy, atomic force microscopy, and water contact angle measurement. It is revealed that the surfaces of the nanocomposites are rough at the microscale and nanoscale. The formation reason of the superhydrophobic surfaces was also discussed in this work. © 2010 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem, 2010
Co-reporter:Zheng-Hong Luo;Xiao-Zi You;Hua-Rong Li
Korean Journal of Chemical Engineering 2010 Volume 27( Issue 1) pp:66-72
Publication Date(Web):2010 January
DOI:10.1007/s11814-009-0329-x
A kinetic model for the chlorination of glycerol with hydrochloric acid in the use of acetic acid as catalyst is presented in this study. The model is based on a comprehensive chlorination mechanism, taking the formation of 1,3-dichloro-2-propanol and 2,3-dichloro-1-propanol into account while ignoring the formation of any intermediate in the chlorination system. Simulations were carried out under different chlorination conditions to calculate the concentrations of the main chemical species in the reaction system. The validity of the model was examined via a comparison of the calculated data with the experimental data on the chlorination of glycerol with hydrochloric acid at 363–393 K. The results show the model is capable of describing the chlorination performance with good agreement with experimental data.
Co-reporter:Zheng-Hong Luo, Xiao-Zi You and Hua-Rong Li
Industrial & Engineering Chemistry Research 2009 Volume 48(Issue 1) pp:446
Publication Date(Web):November 17, 2008
DOI:10.1021/ie8011177
Direct preparation of 1,3-dichloro-2-propanol from glycerol is carried out in a batch reactor using acetic acid catalyst at 363−393 K. The analytical technique, gas chromatography, is employed in order to follow the time evolution of the reagents. The kinetic model of the process is developed. Furthermore, the model parameters of the process are also determined by data fitting. The results show that direct preparation follows the SN2 mechanism. A kinetic model corresponding to the mechanism is proposed in this work. The experimental results show that the kinetic model agrees well with the experiments.
Co-reporter:Zheng-Hong Luo, Xiao-Zi You and Jie Zhong
Industrial & Engineering Chemistry Research 2009 Volume 48(Issue 24) pp:10779
Publication Date(Web):November 9, 2009
DOI:10.1021/ie900933b
In the present study, a reactor design for the direct preparation of dichloropropanol (DCP) from glycerol (GLY) is presented. As an optimum design, a reactive distillation (RD) column in which the second chlorination of GLY occurs during the direct preparation of DCP from GLY has been introduced. Using a simple equilibrium mathematical model of RD, a pilot plant scale column is designed. Furthermore, the whole preparation process of DCP from GLY used the optimum RD column as the central unit is simulated by using an advanced software tool, namely ASPEN PLUS. The pilot plant realization of the whole preparation process is presented and its results are compared with the theoretical prediction. On the basis of the pilot plant data and simulated results, a new technology of DCP production has been designed.
Co-reporter:Zheng-Hong Luo;Hai-Jiang Yu ;Wei Zhang
Journal of Applied Polymer Science 2009 Volume 113( Issue 6) pp:4032-4041
Publication Date(Web):
DOI:10.1002/app.30486
Abstract
Microphase separation behavior on the surfaces of poly(dimethylsiloxane)-block-poly(2,2,3,3,4,4,4-heptafluorobutyl methacrylate) (PDMS-b-PHFBMA) diblock copolymer coatings was investigated. The PDMS-b-PHFBMA diblock copolymers were successfully synthesized via atom transfer radical polymerization (ATRP). The chemical structure of the copolymers was characterized by nuclear magnetic resonance and Fourier transform infrared spectroscopy. Surface composition was studied by X-ray photoelectron spectroscopy. Copolymer microstructure was investigated by atomic force microscopy. The microstructure observations show that well-organized phase-separated surfaces consist of hydrophobic domain from PDMS segments and more hydrophobic domain from PHFBMA segments in the copolymers. The increase in the PHFBMA content can strengthen the microphase separation behavior in the PDMS-b-PHFBMA diblock copolymers. And the increase in the annealing temperature can also strengthen the microphase separation behavior in the PDMS-b-PHFBMA diblock copolymers. Moreover, Flory-Huggins thermodynamic theory was preliminarily used to explain the microphase separation behavior in the PDMS-b-PHFBMA diblock copolymers.© 2009 Wiley Periodicals, Inc. J Appl Polym Sci, 2009
Co-reporter:Zheng-Hong Luo;Hai-Jiang Yu;Teng-Yun He
Journal of Applied Polymer Science 2008 Volume 108( Issue 2) pp:1201-1208
Publication Date(Web):
DOI:10.1002/app.27708
Abstract
The poly(dimethylsiloxane)-block-poly(ethyl methylacrylate) diblock copolymers (PDMS-b-PEMA) were synthesized by atom transfer radical polymerization (ATRP). The chemical structure of the copolymers was characterized by nuclear magnetic resonance (NMR) and Fourier transform infrared (FTIR) spectroscopy. Thermal behaviors were observed via differential scanning calorimetry (DSC). In the DSC curve, the resulting copolymers appear two glass transition temperatures (Tg's), one at −123°C corresponding to the PDMS block and the other at 65°C ascribed to the PEMA segment. Moreover, the copolymer microstructure was investigated by transmission electron microscopy (TEM). The results show that the diblock copolymers are microphase separated if the bulk contains enough PEMA segment. The surface properties of the PDMS-b-PEMA diblock copolymers were searched by contact angle. The PDMS-b-PEMA diblock copolymers are of low surface energy. The polymerization kinetics was also investigated, and the results show that the reaction proceeds in a living manner. © 2008 Wiley Periodicals, Inc. J Appl Polym Sci, 2008
Co-reporter:Zheng-Hong Luo;Wei Wang ;Pei-Lin Su
Journal of Applied Polymer Science 2008 Volume 110( Issue 6) pp:3360-3367
Publication Date(Web):
DOI:10.1002/app.28952
Abstract
In the present study, a model is established to describe the propylene polymerization kinetics catalyzed by the typical catalysts with single-/multi-active site type in a liquid phase stirred-tank reactor using the Monte Carlo simulation method, regardless of the mass and heat diffusion effects within the polymer particles. Many kinetic data, including polypropylene yield, concentration transformation of catalyst active sites, number–average molecular weight, etc., are obtained by the model. The simulated kinetic results are found to be in agreement with the reference ones obtained in a population balance model. Furthermore, the comparisons of the kinetic data between the polymerization catalyzed by the catalyst with single-active site type (typically silica-supported metallocene) and the catalyst with multi-active site type (typically MgCl2-supported Ziegler-Natta catalyst) have been studied using the model. Especially, the effects of hydrogen on the polymerization are studied using the model. The studied results show that the theory of catalyst active site can be used to explain the different propylene polymerization kinetics catalyzed by the typical catalyst with single-/multi-active site type. In addition, the role of hydrogen in the propylene polymerization needs to be emphasized. © 2008 Wiley Periodicals, Inc. J Appl Polym Sci, 2008
Co-reporter:Zhenghong Luo;Tengyun He;Haijiang Yu;Lizong Dai
Macromolecular Reaction Engineering 2008 Volume 2( Issue 5) pp:398-406
Publication Date(Web):
DOI:10.1002/mren.200800018
Co-reporter:Zheng-Hong Luo;Yi Zheng;Zhi-Kai Cao;Shao-Hua Wen
Polymer Engineering & Science 2007 Volume 47(Issue 10) pp:1643-1649
Publication Date(Web):12 SEP 2007
DOI:10.1002/pen.20848
The model of the molecular weight distribution (MWD) of polypropylene produced in a loop reactor is established. The simulated MWD data of the polymers produced in steady-state polymerizations agree with the actual data collected from certain plant. The simulated weight-average molecular weight data also agree with the plant data in start-up processes. Furthermore, the model can be used to simulate the influence of the operation parameters on the MWD of the polymers produced in the steady-state polymerizations as well as the dynamic polymerizations. The simulated results of the steady state polymerizations show the MWD width of polypropylene decreases with the increase of both the propylene flow and the hydrogen flow, but increases with the increase of the catalyst flow. We also find the weight fraction of the polymers with short chains increases with the increase of both the propylene flow and the hydrogen flow, meanwhile, a small shift of the MWD curve to long chains can also be found as the catalyst flow increases. In the dynamic polymerizations, simulations indicate the MWD width and the weight fraction of the polymers with long chains all decrease in both of the start-up process and the end-up process of the polymerizations. POLYM. ENG. SCI., 47:1643–1649, 2007. © 2007 Society of Plastics Engineers
Co-reporter:Zheng-hong Luo, Teng-yun He
Reactive and Functional Polymers (May 2008) Volume 68(Issue 5) pp:931-942
Publication Date(Web):May 2008
DOI:10.1016/j.reactfunctpolym.2008.01.004
Co-reporter:De-Pan Shi, Zheng-Hong Luo, Zu-Wei Zheng
Powder Technology (20 February 2010) Volume 198(Issue 1) pp:135-143
Publication Date(Web):20 February 2010
DOI:10.1016/j.powtec.2009.11.002
Understanding hydrodynamics of tubular loop reactors is crucial in proper scale-up and design of these reactors. Computational fluid dynamics (CFD) models have shown promise in gaining this understanding. In this paper, a three-dimensional (3D) CFD model, using a Eulerian–Eulerian two-fluid model incorporating the kinetic theory of granular flow, was developed to describe the steady-state liquid–solid two-phase flow in a tubular loop propylene polymerization reactor composing of loop and axial flow pump. Corresponding simulations were carried out in the commercial CFD code Fluent. The entire flow field in the loop reactor was calculated by the model. The predicted pressure gradient data were found to agree well with the classical calculated data. Furthermore, the model was used to investigate the influences of the circulation flow velocity and the sold particle size on the solid hold-up. The simulation results showed that the solid hold-up has a relatively uniform distribution in the loop reactor at small particles in volume and high-circulation flow velocities.A three-dimensional CFD model, using a Eulerian–Eulerian two-fluid model incorporating the kinetic theory of granular flow, was developed to describe the steady-state liquid–solid two-phase flow in a tubular loop propylene polymerization reactor composing of loop and axial flow pump. The predicted pressure gradient data were found to agree well with the classical calculated data.
Co-reporter:Wei-Cheng Yan, De-Pan Shi, Zheng-Hong Luo, Ying-Hua Lu
Chemical Engineering Science (15 September 2011) Volume 66(Issue 18) pp:4127-4137
Publication Date(Web):15 September 2011
DOI:10.1016/j.ces.2011.05.039
A three-dimensional (3D) computational fluid dynamics (CFD) model, using an Eulerian–Eulerian two-fluid model incorporating the kinetic theory of granular flow, is adopted to describe the steady-state liquid–solid two-phase flow under conditions employed in a tubular loop propylene polymerization reactor composed of loop and axial flow pump. The model is validated by comparing its simulation result with the classical calculated data as well as a set of data collected from certain pilot plant in China. The entire flow behaviors and the effects of guide vane on them in the reactor are also investigated numerically. Especially, the whole field in the loop reactor with the guide vane is obtained via the above model. The results show that a guide vane weakens the turbulent intensity, reduces the component of the rotating velocity, and contributes to the uniform distribution of the particles in the reactor. The second flow phenomenon is successfully predicted in the loop reactor with the guide vane.Graphical AbstractDownload high-res image (51KB)Download full-size imageHighlights► We present a 3D CFD model to describe the liquid-solid flow in a loop polymerization reactor. ► We distinguish the effect of guide vane in loop polymerization reactors by applying the CFD model. ► We find that a guide vane weakens the turbulent intensity and reduces the rotating velocity fraction. ► We also predict the second flow phenomenon in the loop reactor with the guide vane.
Co-reporter:Wei-Cheng Yan, Zheng-Hong Luo, An-Yi Guo
Chemical Engineering Science (1 November 2011) Volume 66(Issue 21) pp:5148-5163
Publication Date(Web):1 November 2011
DOI:10.1016/j.ces.2011.07.004
A computational fluid dynamics model, coupled with population balance model (CFD–PBM), was developed to describe the liquid–solid two-phase flow in a pilot-plant tubular loop propylene polymerization reactor. The model combines the advantage of CFD to calculate the entire flow field and that of PBM to calculate the particle size distribution (PSD). Particle growth, aggregation and breakage were taken into account to describe the evolution of the PSD. The model was first validated by comparing simulation results with the classical calculated data. Furthermore, four cases studies, involving particle aggregation, particle breakage, particle growth or involving particle growth, breakage and aggregation, were designed to identify the model. The entire flow behavior and PSD in the tubular loop reactor, i.e. PSD, solid holdup and liquid phase velocity distribution, were also obtained numerically. The results showed that the model is effective in describing the entire flow behavior and in tracking the evolution of the PSD.Graphical abstractDownload high-res image (109KB)Download full-size imageHighlights► We present a CFD–PBM model to describe the flow in a loop polymerization reactor. ► The model is validated by comparing simulation results with the classical data. ► Four cases studies are designed to identify the model. ► The model is effective in describing the entire flow and tracking the PSD evolution.
Co-reporter:Xi Gao, Ya-Ping Zhu, Zheng-hong Luo
Chemical Engineering Science (1 December 2011) Volume 66(Issue 23) pp:6028-6038
Publication Date(Web):1 December 2011
DOI:10.1016/j.ces.2011.08.031
A comprehensive two-dimensional heterogeneous reactor model was developed to simulate the flow behavior and catalytic coupling reaction of carbon monoxide (CO)–diethyl oxalate (DEO) in a fixed-bed reactor. The two-temperature porous medium model, which was revised from a one-temperature porous medium model, as well as one equation turbulent model, and exponent-function kinetic model was constructed for the turbulent velocity scale comparing with laminar flow and simulation of the catalytic coupling reaction. The simulation results were in good agreement with the actual data collected from certain pilot-plant fixed bed reactors in China. Based on the validated approach and models, the distributions of reaction parameters such as temperature and component concentrations in the reactor were analyzed. The simulations were then carried out to understand the effects of operating conditions on the reactor performance which showed that the conduction oil temperature in the reactor jacket and the CO concentration are the key impact factors for the reactor performance.Graphical AbstractDownload high-res image (181KB)Download full-size imageHighlights► We present a CFD model to describe the flow in a catalytic coupling FBR. ► The CFD model incorporates a two-temperature porous medium model. ► The model is validated by comparing simulation results with some actual data. ► The model is used to predict the effects of operating conditions on the FBR.