大豆蛋白废水中乳清蛋白的泡沫分离实验

采用泡沫分离法回收大豆蛋白废水中蛋白,考察了pH值、气体的流速、进料浓度、液柱和泡沫层高度等因素对分离效果的影响.低进气速度、高泡沫层高度、适当的pH值以及低进料浓度有利于较好的分离.结果表明:当进料浓度为0.54 g/L、pH值为5、泡沫层与液池高度比4∶1,通气量为15.0 L/h 时,富集比可以达到3.25;当进料浓度为0.54 g/L、pH值为5、泡沫层与液池高度比3∶1,通气量为15.0 L/h,此时脱除率可以达到48.5%.     

固定酶法催化合成生物柴油Ⅰ.大孔树脂固定化脂肪酶的制备

研究了用于生物柴油酶催化的大孔树脂固定化脂肪酶的制备过程,考察和优化了脂肪酶固定化方法及条件。结果表明,采用大孔树脂D3520作载体,以载体涂布法固定化脂肪酶的最适固定化条件为:酶用量为酶∶树脂=0.16∶1(质量比),吸附时间1~3 h,pH值范围为9.0~9.4,固定化温度40℃。酶活力可达91.49 U/g,酶活回收率约为54%。     

响应面法优化泡沫分离明胶水溶液

利用响应面法对泡沫分离明胶水溶液条件进行优化,通过单因素实验和Box-Behnken实验设计原理,研究稀释倍数,温度,装液量和pH值4个因素对泡沫分离明胶蛋白回收率和富集比的影响。得出明胶蛋白泡沫分离的最佳条件为:稀释倍数7.01、温度33.66℃、装液量346.38mL、pH值3.52。此条件下明胶蛋白的回收率为75.81%,富集比为2.01,试验结果表明,泡沫分离法能够为明胶蛋白回收提供了一个有效的方法。     

消泡剂共存体系中泡沫分离蛋白质

在以牛血清白蛋白(BSA)为目标蛋白、聚环氧丙烷环氧乙烷甘油醚(PGE)为消泡剂的模拟体系中,考察了表面活性剂种类(非离子型Tween-20和离子型SDBS)、浓度、溶液pH及操作参数(气体流量、初始液池高度)对BSA分离效率的影响. 结果表明,2种活性剂均能改善模拟体系的泡沫性能,使泡沫分离. 后者作用更强并能促进BSA的吸附,因DBS-通过静电作用与带相反电荷的BSA结合形成疏水性更强的BSA-DBS复合物. pH通过影响BSA的电荷分布而影响其与SDBS的结合,进而影响对BSA的吸附,初始BSA浓度0.1 g/L, PGE 4 mg/L, SDBS 50 mg/L, pH为3.4时,约66%蛋白质浓缩在泡沫液中,富集比为5.34. 增加气速或初始液池高度可得到较高收率,但富集比减小.     

泡沫相部分水平泡沫分离塔强化分离牛血清蛋白的工艺研究

为了加强泡沫相排液,提高目的产物的富集比,设计了一种新型泡沫分离塔即泡沫相部分水平泡沫分离塔.以传统泡沫相垂直泡沫分离塔为对照塔,以牛血清蛋白(BSA)为体系,考察了表观气速、装液量、物料初始浓度和初始pH对牛血清蛋白(BSA)富集比和回收率的影响.结果表明泡沫相部分水平泡沫分离塔有效减小了泡沫相排液的阻力,提高了BS...     

响应面法优化产低温脂肪酶工程菌Cl02的发酵条件

目的采用响应面法优化产低温脂肪酶工程菌Cl02的发酵条件。方法通过单因素试验考察培养基中酵母氮源含量、pH值、甘油含量和甲醇含量对酶活的影响,确定产酶的主要影响条件,在此基础上,根据Box-Benheken中心组合试验设计原理,采用三因素三水平的响应面分析法,综合考察各因子对低温脂肪酶酶活的影响,建立低温脂肪酶酶活的二次回归模型。结果培养基中酵母氮源含量、pH值和甲醇含量对酶活的影响显著。最适产低温脂肪酶条件为:酵母氮源含量7.3 g/L、pH 6.0、甲醇含量9.1 g/L,在此条件下,低温脂肪酶酶活可达42.25 IU/ml,比优化前(28.0 IU/ml)提高了50.9%。结论利用响应面法优化的发酵条件可显著提高工程菌的产酶能力,为规模化生产低温脂肪酶奠定了基础。     

泡沫分离法回收水溶液中微量钼（Ⅵ）的研究

以十六烷基三甲基氯化铵（CTAC）为表面活性剂,采用自制的泡沫分离塔回收水溶液中的微量钼（Ⅵ）,考察了溶液pH、空气流量、表面活性剂质量浓度等对钼（Ⅵ）回收率和富集率的影响,并对该过程进行动力学分析。实验结果表明：随溶液pH增加,钼（Ⅵ）的富集率和回收率均先增加后减少;随CTAC浓度增加,钼（Ⅵ）的回收率增加而富集率减少;随空气流量增加,钼（Ⅵ）的富集率减少而回收率先增加后减少。在溶液pH为9、气体流量为 200 mL/min、表面活性剂质量浓度为0.30 g/L条件下,钼（Ⅵ）的回收率达到90%,富集倍数达到10倍。动力学分析表明,泡沫分离钼（Ⅵ）的过程是零级动力学过程,拟合方程为ρ=-0.288 8t+4.290 4,R2=0.993 8。     

麻黄强化泡沫分离甘草酸的工艺研究

为了提高泡沫分离甘草中甘草酸的分离效果,开发了甘草麻黄配伍泡沫分离工艺,并就麻黄对浸提液泡沫性能的影响进行了研究。结果表明,麻黄强化了甘草酸的提取,但降低了浸提液中甘草苷的浓度,使得浸提液的泡沫性能发生变化而影响泡沫分离甘草酸的分离效果。以甘草酸的富集比和回收率为评价指标,研究了温度、气体体积流量、甘草酸初始浓度和甘草麻黄质量配比对分离效果的影响。结果表明当温度为40℃、气体体积流量为100 m L×min~(-1)、甘草酸初始浓度为0.2 g×L~(-1)和甘草麻黄质量配比为5:3时,获得甘草酸的富集比和回收率分别为8.34和62.5%。与单独泡沫分离甘草中甘草酸相比,甘草酸的富集比提高了121.7%,而回收率并未明显降低。因此,麻黄的引入有效地提高了泡沫分离甘草酸的分离效果。     

甲醇对NS81006催化大豆油制备生物柴油的影响研究

游离脂肪酶催化法以其酶催化剂生产成本较低,反应速率较快的优点,成为生物柴油制备的新的关注方向.游离脂肪酶NS81006可以有效催化大豆油甲醇解制备乍物柴油,但其催化活性在反应后期下降,甲醇可能对NS81006催化活性及回用稳定性造成影响.研究了甲醇对NS81006酶活的影响以及不同甲醇添加策略对NS81006催化效果的影响.研究结果表明,反应体系中过多甲醇的存在对NS81006酶活产生负而影响;通过减少甲醇添加量和缩短甲醇与NS81006作用时间可有效降低酶活损失,提高NS81006回用稳定性;在优化策略下,NS81006连续使用6个批次,生物柴油得率保持90%以上.     

黏土吸附法固定化脂肪酶的初步研究

为研究天然黏土为载体固定化脂肪酶的可行性,采用羟基化、硅烷化处理,对黏土进行改性,并以此为载体吸附固定化脂肪酶,探讨黏土固定化脂肪酶的条件对酶活及蛋白吸附量的影响,优化固定化脂肪酶条件。研究结果表明:黏土经羟基化、硅烷化改性处理后能显著提高固定化酶活和蛋白固定量,其中硅烷化改性最优;载体固定脂肪酶最优条件为:加酶量50 mg/g,载体粒径180—250μm,pH值为4.0,固定化温度25℃,固定化时间2.0 h;与游离酶相比,固定化酶显示出更广的pH值适应性。黏土固定化脂肪酶重复使用10批次后,仍能保留76.85%的初始活力。以天然黏土为载体固定化脂肪酶,具有较好的实际可应用性及操作稳定性,在较低pH值条件下应用具有一定优势。     

间歇式泡沫分离法回收海水中硼的研究

采用间歇式泡沫分离法研究了海水中硼的回收工艺。主要考察了表面活性剂种类及用量、溶液pH、气体流量等因素对海水中硼的分离性能的影响。实验结果表明：十二烷基三甲基氯化铵（DTAC）、十四烷基三甲基氯化铵（TTAC）、十六烷基三甲基氯化铵（CTAC）以及十八烷基三甲基氯化铵（OTAC） 4种表面活性剂中CTAC对海水中硼的分离效果最好;随溶液pH的增加,硼的回收率和富集比均先增大后减小;随CTAC用量的增加,硼的回收率逐渐增大并趋于稳定,而富集比先增大后减小;随气体流量的增加,硼的回收率先增大后减小,而富集比则逐渐减小。在实验条件范围内,当CTAC质量浓度为0.2 g/L、溶液pH为9、气体流量为200 mL/min时,硼的回收率达到90%,富集比达到8。     

泡沫分离法分离纯化无患子皂苷的研究

采用泡沫分离法分离纯化无患子皂苷溶液,收集溢出分离柱的泡沫液,采用紫外分光光度计分别测定原液和泡沫液的皂苷含量,通过富集比、回收率以及纯度表征分离效果。结果表明:在进料浓度为 2.0 g/L、进料量为 150 mL、气速为 32 L/h、温度为 30 ℃、pH值为4.3条件下,富集比可达到2.153,收率与纯度分别达到 79.19 % 和 74.68 %。     

Purification and Concentration of the Total Saikosaponins Extracted from Radix Bupleuri using Foam Fractionation

The purpose of this study was to investigate the use of foam fractionation to recover saikosaponins. First, the solvent extraction method was applied for the extraction of saikosaponins from radix bupleuri using ethanol or deionized water. Then, the foam fractionation technique in batch mode was used for the recovery of the total saikosaponins from the extract. The effects of initial concentration, air flow rate, liquid loading volume, pH, and operating time on the process performance were investigated. The recovery percentage 77.2% and an enrichment ratio 3.68 of total saikosaponins with one-stage separation were obtained under the optimal conditions of initial saikosaponin concentration 0.18 mg/mL, air flow rate 50 mL/min, liquid loading volume 200 mL, pH 5.5, and operating time of 2 h. A two-stage foam fractionation technology was also designed, which was effective for improving both the recovery percentage and enrichment ratio simultaneously.     

Study on Riboflavin Recovery from Wastewater by a Batch Foam Separation Process

Abstract

A batch recovery of riboflavin via foam separation from industrial simulative wastewater was studied using a cationic surfactant, cetyltrimethyl ammonium bromide (CTAB). The experimental parameters examined were the surfactant concentration, air flow rate, pH, and foam height. Under optimal operating conditions obtained through an orthogonal experiment, the maximum enrichment ratio of 48.7 was achieved for riboflavin along with 99.3% removal efficiency. The optimal operating conditions had the concentration of CTAB at 0.3 g/L, air flow rate at 400 ml/min, foam height at 90 cm, and pH at 12. Therefore foam separation proved to be an effective method to recover the riboflavin in terms of the good enrichment and removal efficiency.     

Concentration of Proteins from Single Component Solution Using a Semibatch Foaming Process

ABSTRACT

A laboratory-scale foam separation system was employed to examine the enrichment and recovery of six proteins: sodium caseinate, β-casein, bovine serum albumin (BSA), β-lactoglobulin, plusmn;-Iactalbumin, and chymotrypsinogen A. In this report we present experimental data which demonstrate the effectiveness of the separation process in extracting proteins from single component solutions. In particular, we have examined the effects of: 1) the solution pH at a fixed air flow rate and initial protein concentration, 2) superficial air velocity at fixed values of pH and protein concentration, and 3) protein concentration at the optimum pH and at a given superficial air velocity. The maximum enrichment of BSA was obtained at its isoelectric point (pH 48), and for other proteins better enrichment was achieved at a pH higher than their isoelectric point. The lower the superficial velocity in the 079–02 cm/s range the higherthe enrichment for all the proteins except for plusmn;-lactalbumin and chymotrypsinogen A (for these proteins enrichment was insensitive to the superficial velocity). The higher enrichment was also obtained by foaming at a smaller initial protein concentration (in the 30–120 mg/L range).     

基于甘草配伍黄芩同时泡沫分离甘草酸和黄芩苷

为了同时分离甘草中有表面活性的甘草酸和黄芩中无表面活性的黄芩苷,开发了甘草配伍黄芩泡沫分离工艺。通过荧光光谱、紫外吸收光谱和红外吸收光谱分析表明,甘草酸与黄芩苷存在相互作用,并且甘草黄芩配伍强化了甘草酸和黄芩苷的提取。以甘草酸和黄芩苷的富集比和回收率为评价指标,当温度为40℃、气体体积流量为100 ml·min^-1、甘草酸初始浓度为0.2 g·L^-1、甘草黄芩质量比为3：1时,获得甘草酸的富集比和回收率分别为11.0和73.5%,黄芩苷的富集比和回收率分别为5.8和38.5%。通过甘草与黄芩配伍,利用泡沫分离获得黄芩中的黄芩苷。同时,与单独泡沫分离甘草中甘草酸相比,甘草酸的富集比提高了194.9%,回收率提高了23.3%。因此,甘草配伍黄芩能有效泡沫分离甘草酸和黄芩苷。     

泡沫分离法提取乙醇水体系中甲基橙

采用泡沫分离法对含甲基橙的乙醇水溶液进行了提取研究. 考察了乙醇体积分数、气体流量、pH、甲基橙浓度和表面活性剂浓度对提取效果的影响,并对泡沫分离乙醇-水体系中提取中药有效成分的可行性进行了探讨. 结果表明,以十六烷基三甲基溴化铵(CTAB)为表面活性剂,在乙醇体积分数25%的乙醇-水体系中,在pH 6.0、气速80 mL/min、甲基橙浓度35 mg/L及CTAB浓度80 mg/L的操作条件下,甲基橙的富集比为14.38,回收率在98.5%以上. 在一定范围内提高表面活性剂浓度或加入稳泡剂以削弱乙醇的消泡作用,从而将泡沫分离技术应用于乙醇-水体系中中药有效成分的提取是可能的.     

Study on Streptomycin Sulfate Recovery by Batch Foam Separation

The feasibility of foam separation as a technique was assessed for the recovery of streptomycin sulfate from the waste solution by using an anionic surfactant sodium dodecyl sulfate (SDS). The experimental parameters examined were SDS concentration, superficial gas velocity, initial pH, and liquid loading volume. The results showed that sodium dodecyl sulfate as the surfactant for foam separation had good foaming quality and could effectively concentrate streptomycin sulfate of the aqueous solution by technology of foam separation. The enrichment ratio and the recovery rate of streptomycin sulfate were 4.0 and 85%, respectively under the best operating conditions of sodium dodecyl sulfate concentration 0.4 g/L, superficial gas velocity 300 mL/min, liquid loading volume 300 mL and initial pH 6.0 when streptomycin sulfate concentration was 0.5 g/L.     

Protein Recovery from Sweet Potato Starch Wastewater by Foam Separation

In this study, an inclined foam separation column was designed to effectively recover protein from sweet potato starch wastewater. The effects of the influent protein concentration, pH, air flow rate, influent volume, foaming time, and inclined column angle on foam separation performance were assessed. The optimum foam separation conditions consisted of influent protein concentration 4.51 mg/mL, pH 4, air flow rate 0.15 mL/min, influent volume 500 mL, foaming time 100 min, and inclined column angle 30°. In these conditions, protein recovery percentage and enrichment ratios were 84.1% and 1.3, respectively. The biochemical oxygen demand (BOD₅) and chemical oxygen demand (COD_Cr) of the residual solution (620 and 950 mg/mL, respectively) were lower than those of the original (influent) solution.     

Separation of Tea Saponin by Two-Stage Continuous Foam Fractionation

A technology of two-stage continuous foam fractionation for tea saponin recovery was studied for increasing both the enrichment ratio and the recovery percentage. In the first stage, the effect of air flow rate, the initial pH, the feed flow rate, and the feed position were studied at a temperature of 60°C. The results showed that when the conditions of the first stage were at a temperature of 60°C, air flow rate 150 mL/min, pH 5.3, feed flow rate 1.92 mL/min, and feed position at the interface between the liquid phase and the foam phase, the enrichment ratio, and the recovery percentage of tea saponin were 4.02 and 56.4%, respectively, and the effluent solution was added to the second stage as the initial solution. When the conditions of the second stage were at a temperature of 30°C and an air flow rate of 300 mL/min, the recovery percentage of tea saponin reached 47.6%, and the foamate was added to the first stage as feed solution. The total recovery percentage of tea saponin reached 86.3% by the two-stage continuous foam fractionation.