Separation of Sesamin and Sesamolin by a Supercritical Fluid-Simulated Moving Bed

This work shows how the sesamin and sesamolin in sesame seed can be extracted, enriched and purified by the related technologies of supercritical carbon dioxide. Sesame oil is first obtained from the sesame seeds by supercritical carbon dioxide extraction (SFE);lignans in the oil are enriched and precipitated as the top product by supercritical fluid fractionation technology (SFF);the crude lignans are then separated by supercritical fluid-simulated moving bed chromatography (SF-SMB) to obtain pure sesamin and sesamolin. The simulated moving bed is a continuous chromatography;the use of supercritical carbon dioxide as the desorbent simplifies the downstream treatment. By experimental validation, this work also shows that replacing liquid by SF as the desorbent for the SMB automatically creates a gradient operation for the SMB and enlarges the separable range of the operating conditions. Both the design and operation of the SF-SMB are introduced in this paper. The application of SF-SMB to the separation of sesamin and sesamolin provides a novel example for demonstrating the diversity of SF and the potential applications for the production of natural products and the development of botanical drugs.

A Non-linear Non-ideal Model of Simulated Moving Bed Chromatography for Chiral Separations

A non-linear non-ideal model,taking into account non-linear competitive isotherms,axial disperison,film mass transfer,intraparticle diffusion,and port periodic switching,was developed to simulate the dynamics of simulated moving bed chromatography(SMBC),The model equations were solved by a new efficient numerical technique of orthogonal collocation on finite elements with periodical movement of conceantration vector,The simulated SMBC performance is in accordance with the experimental results reported in the literature for separation of 1,1''''''''-bi-2-naphtol enantiomers using SMBC,This model is useful for design,operation ,optimization and scale-up of non-linear SMBC for chiral separations with significant non-ideal effects,especially for high solute concentration and small intraparticle diffusion coefficient or large chiral stationary phase particle.

Numerical Simulation of Asynchronous Simulated Moving Bed Chromatography

Asynchronous simulated moving bed chromatography (ASMBC), known also as the 'VARICOL' process, is more efficient and flexible than the well-known and traditional simulated moving bed chromatography (SMBC). A detailed model of ASMBC, taking account of non-linear competitive isotherms, mass transfer parameters, and complex port switching schedule parameters, was developed to simulate the complex dynamics of ASMBC.The simulated performance is in close agreement with the experimental data of chiral separation reported in the literature. The simulation results show that ASMBC can achieve the performance similar to SMBC with fewer columns and can achieve better performance than SMBC with the same total column number. All design and operation parameters can be chosen correctly by numerical simulation. This detailed ASMBC model and the numerical technique are useful for design, operation, optimization and scale-up of ASMBC.

Purification of L-Lysine in Simulated Moving Bed and Fixed-Bed Chromatography

L-Lysine was produced by a microbial process utilizing a Corynebacterium glutamicum （ATCC 21799） strain. L-Lysine was purified from the cultivated medium by fixed-bed and simulated moving bed （SMB） chromatography. The separation conditions including pH, eluent concentration and Lys+ and Lys2+ adsorption isotherms were studied in batch adsorption. The column capacity, eluent flow rate and eluent concentration have been studied in fixed-bed chromatography. Maximum purification rate of lysine was obtained as 0.066 （g/（g·h）） （per gram resin and per hour） at an eluent flow rate of 10 （mL/min） in fixed-bed chromatography. The results obtained from SMB were 0.11 （g/（g·h）） for L-lysine purification rate and 96% for L-lysine recovery.

Mathematical modeling of salt-gradient ion-exchange simulated moving bed chromatography for protein separations

The salt-gradient operation mode used in ion-exchange simulated moving bed chromatography (SMBC) can improve the efficiency of protein separations. A detailed model that takes into account any kind of adsorption/ion-exchange equilibrium, salt gradient, size exclusion, mass transfer resistance, and port periodic switching mechanism, was developed to simulate the complex dynamics. The model predictions were verified by the experimental data on upward and downward gradients for protein separations reported in the literature. All design and operating parameters (number, configuration, length and diameter of columns, particle size, switching period, flow rates of feed, raffinate, desorbent and extract, protein concentrations in feed, different salt concentrations in desorbent and feed) can be chosen correctly by numerical simulation. This model can facilitate the design, operation, optimization, control and scale-up of salt-gradient ion-exchange SMBC for protein separations.

Continuous size fractionation of magnetic nanoparticles by using simulated moving bed chromatography

The size fractionation of magnetic nanoparticles is a technical problem,which until today can only be solved with great effort.Nevertheless,there is an important demand for nanoparticles with sharp size distributions,for example for medical technology or sensor technology.Using magnetic chromatography,we show a promising method for fractionation of magnetic nanoparticles with respect to their size and/or magnetic properties.This was achieved by passing magnetic nanoparticles through a packed bed of fine steel spheres with which they interact magnetically because single domain ferro-/ferrimagnetic nanoparticles show a spontaneous magnetization.Since the strength of this interaction is related to particle size,the principle is suitable for size fractionation.This concept was transferred into a continuous process in this work using a so-called simulated moving bed chromatography.Applying a suspension of magnetic nanoparticles within a size range from 20 to 120 nm,the process showed a separation sharpness of up to 0.52 with recovery rates of 100%.The continuous feed stream of magnetic nanoparticles could be fractionated with a space-time-yield of up to 5 mg/(L∙min).Due to the easy scalability of continuous chromatography,the process is a promising approach for the efficient fractionation of industrially relevant amounts of magnetic nanoparticles.

模拟移动床色谱分离技术研究进展

模拟移动床色谱(Simulated moving bed chromatography,SMBC)是一种新型分离手段,具有分离效果好、投资成本少以及适合连续性大规模生产等特点,近些年来备受关注,研究热度居高不下,在食品、化工和制药等行业均有广泛应用。SMBC由模拟移动床技术与色谱分离技术相结合产生,通过回顾色谱分离技术的起源,介绍模拟移动床色谱分离技术的原理及应用领域,列举模拟移动床色谱在高效分离淀粉糖、低聚糖、糖醇及有机酸等混合物的实际应用场景,为该技术的工业应用提供参考。

模拟移动床色谱技术及其应用

详细地介绍了一种现代化分离技术模拟移动床色谱技术的发展历史及其工作原理,同时介绍了模拟移动床色谱在石油化工、糖醇分离、手性化合物及其他方面的主要应用。

生产银杏黄酮的模拟移动床色谱工艺

Separation of Ginkgo flavonoids using simulated moving bed chromatography to replace the batch chromatography is discussed.The product of higher purity is obtained,and in this process,the yield of product increased and cost decreased.Furthermore,this process is very clean.

银杏内酯B的纯化

报道了具有生产规模的银杏内酯B(GB)纯化工艺。该工艺包括萃取、模拟移动床、结晶3个步骤。其核心是用模拟移动床色谱对银杏内酯B进行规模化精细分离。所得产品纯度w(GB)≥90%,收率≥70%,生产能力20g/h。生产1g银杏内酯B净消耗乙酸乙酯29L,乙醇50mL,甲醇40mL。产物用高效液相色谱、液质联用及核磁共振做了鉴定。

模拟移动床色谱分离替考拉宁条件研究

探讨了用模拟移动床色谱分离提纯替考拉宁的可行性 ,且优化出最佳分离条件为 ts=1 0min,υF=0 .0 8m L/min,υp=1 .5 m L/min,υD=0 .8m L/min,CF=8mg/m L。

顺序式模拟移动色谱纯化木糖醇母液

以木糖醇母液为原料,采用顺序式模拟移动色谱技术纯化木糖醇母液。在制备色谱研究的基础上,研究顺序式模拟移动床(SSMB)技术纯化木糖醇母液的最佳工艺参数。结果表明最佳工艺参数为:进料浓度60%,进料量为546.00 g/h,进水量为819.00 g/h,循环量382.2 m L。在此条件下木糖醇出口浓度为41.2%,纯度达到94.8%,收率达到90.6%,较木糖醇母液纯度提高31.12%,本研究为木糖醇母液产业化利用奠定了实践基础。

抗菌素替考拉宁模拟移动床色谱分离的中试研究

从单柱色谱理论出发,结合实验给出了替考拉宁用模拟移动床色谱进行中试分离的工艺条件,并对所得结果进行了分析。

基于浮点编码的遗传算法优化模拟移动床色谱分离木糖醇母液

开发了一种基于浮点编码遗传算法的模拟移动床色谱优化方法。该优化方法中将归一化的生产强度取最大值作为目标函数,同时将纯度的n次方作为罚函数。运算过程中浮点编码遗传算法的适度值由模拟移动床色谱的稳态模型求得。为了保证遗传算法每一代的个体均满足模拟移动床色谱本身的约束条件,算术杂交和完全非均匀变异被用作演化算子。采用该算法很容易得到模拟移动床色谱分离过程中非线性条件下的最优条件。这种优化算法被应用于木糖醇母液的模拟移动床色谱,结果表明当罚函数指数n值由小到大变化时,可以得到产品纯度由低到高的最优分离条件。进一步比较了当n值为20时的实验值与仿真值后发现,实验结果与仿真值相吻合,木糖和木糖醇的纯度分别达到99 51%和99 26%。

液相制备色谱的研究进展

介绍国内外制备色谱方面的概况,综述了模拟移动床色谱、高速逆流色谱和超临界流体色谱等3种典型的液相制备色谱的研究进展。

对二甲苯模拟移动床分离过程的模拟与优化

对国内外模拟移动床的研究状况及模拟移动床的设计方法进行了简短的综述,基于Aspen Chromatography软件,以对二甲苯模拟移动床吸附分离过程为研究对象,结合实际工况数据,采用模拟移动床SMB模型,对模拟移动床吸附分离过程进行设计与模拟,抽取液中对二甲苯的纯度高达99.98%,,收率高达98.08%,.考察了切换时间(t_s)、抽取液流量(Q_E)、进料量(Q_F)、吸附剂钝化以及管路死体积对吸附分离过程的影响.模拟结果表明:借助于Aspen Chromatography,采用SMB模型能较好地描述模拟移动床分离过程的真实情况,对模拟移动床分离过程的工艺设计、优化及操作具有重要的指导意义.

模拟移动色谱法纯化葡萄糖母液的技术研究

为重复利用葡萄糖母液,采用模拟移动色谱技术纯化葡萄糖母液。在单柱制备色谱研究的基础上,研究模拟移动床(SMB)技术与顺序式模拟移动床(SSMB)技术纯化葡萄糖母液的最佳工艺参数。结果表明:SSMB技术是纯化葡萄糖母液的较优技术,最佳工艺参数为进料浓度50%、柱温60℃、进料量为66.4kg·h-1,进水量为99.6 kg·h-1,在此条件下葡萄糖出口浓度为42.3%,纯度达到95.77%,收率达到91.23%,较葡萄糖母液提高14.43%。本研究为葡萄糖母液产业化利用奠定了基础。

模拟移动床色谱法分离纯化链甾醇

以羊毛脂中提取的链甾醇为原料,采用模拟移动床色谱法(SMBC)进行了分离纯化。以C18为固定相,甲醇为洗脱液,采用四区SMBC系统,每区有两根色谱柱(150 mm×10 mm×10μm),经过两次SMBC分离,得到高纯度链甾醇产品。以纯度、生产率和溶剂消耗量为指标,确定链甾醇在SMBC中的最佳分离条件为:切换时间6.4 min,四区流量分别为9.97,7.53,8.53和4.97 mL/min,进料流量1.00 mL/min(第一次SMBC分离);切换时间6.0 min,四区流量分别为9.95,7.98,8.53和6.62 mL/min,进料流量0.55 mL/min(第二次SMBC分离)。结果表明,以90.1%含量的链甾醇粗品为原料,在优化实验条件下,先除去吸附能力比链甾醇强的杂质,再除去吸附能力比链甾醇弱的杂质,得到高纯度(≥98.9%)的链甾醇产品,回收率为93.8%。

模拟移动床色谱在手性药物大规模拆分中的应用

模拟移动床色谱作为手性药物大规模拆分领域中的强有力工具 ,越来越受到人们的重视。该文介绍了模拟移动床色谱技术的发展情况及其工作原理 ,对描述模拟移动床色谱分离行为的理论模型和分离操作中操作参数的确定也作了介绍。