Partition Efficiency of High-Pitch Locular Multilayer Coil for Countercurrent Chromatographic Separation of Proteins Using Small-Scale Cross-Axis Coil Planet Centrifuge and Application to Purification of Various Collagenases with Aqueous-Aqueous Polymer Phase Systems

Partition efficiency of the high-pitch locular multilayer coil was evaluated in countercurrent chromatographic (CCC) separation of proteins with an aqueous-aqueous polymer phase system using the small-scale cross-axis coil planet centrifuge (X-axis CPC) fabricated in our laboratory. The separation column was specially made by high-pitch (ca 5 cm) winding of 1.0 mm I.D., 2.0 mm O.D. locular tubing compressed at 2 cm intervals with a total capacity of 29.5 mL. The protein separation was performed using a set of stable proteins including cytochrome C, myoglobin, and lysozyme with the 12.5% (w/w) polyethylene glycol (PEG) 1000 and 12.5% (w/w) dibasic potassium phosphate system (pH 9.2) under 1000 rpm of column revolution. This high-pitch locular tubing yielded substantially increased stationary phase retention than the normal locular tubing for both lower and upper mobile phases. In order to demonstrate the capability of the high-pitch locular tubing, the purification of collagenase from the crude commercial sample was carried out using an aqueous-aqueous polymer phase system. Using the 16.0% (w/w) PEG 1000 - 6.3% (w/w) dibasic potassium phosphate - 6.3% (w/w) monobasic potassium phosphate system (pH 6.6), collagenase I, II, V and X derived from Clostridium hystolyticum were separated from other proteins and colored small molecular weight compounds present in the crude commercial sample, while collagenase N-2 and S-1 from Streptomyces parvulus subsp. citrinus were eluted with impurities at the solvent front with the upper phase. The collagenase from C. hystolyticum retained its enzymatic activity in the purified fractions. The overall results demonstrated that the high-pitch locular multilayer coil is effectively used for the CCC purification of bioactive compounds without loss of their enzymatic activities.     

New small-scale cross-axis coil planet centrifuge. Partition efficiency and application to purification of bullfrog ribonuclease

The new small-scale cross-axis coil planet centrifuge (X-axis CPC) previously designed and fabricated in our laboratory has a distinctive feature such that four separation columns of similar weight are mounted symmetrically around the rotary frame to achieve stable balancing of the centrifuge under a high revolution speed. In this column layout, neighboring columns must be rotated in the opposite direction if viewed from the center of the centrifuge to avoid twisting the interconnecting flow tubes. The effect of rotational direction of the columns on the partition efficiency was evaluated with separation of a set of test samples such as cytochrome c, myoglobin, and lysozyme using an aqueous-aqueous polymer phase system composed of 12.5% (w/w) polyethylene glycol (PEG) 1000 and 12.5% (w/w) dibasic potassium phosphate under 1000 rpm of column revolution. A series of experiments was performed using a set of two diagonally located columns (connected in series) each consisting of five coiled layers of 1 mm I.D. with a total capacity of 27.0 mL. Both right- and left-handed coils were tested each under the optimized conditions for choice of mobile phase and direction of the column rotation so that the satisfactory volume of the mobile phase was retained in the column by the aid of Archimedean screw effect. The results of these studies showed that one particular combination of handedness of the coil and direction of the rotation yielded the best peak resolution for each mobile phase. In order to demonstrate the capability of the apparatus, the purification of ribonuclease (RNase) from the extract of bullfrog egg, sialic acid binding lectin (cSBL), was carried out using both organic-aqueous and aqueous-aqueous polymer phase systems. When using the 16.0% (w/w) PEG 1000-6.3% (w/w) dibasic potassium phosphate-6.3% (w/w) monobasic potassium phosphate system, cSBL was successfully separated from other proteins present in the extract while commercial RNase A was eluted at near the solvent front by the lower phase mobile. The cSBL retained its native RNase activity. The overall results demonstrated that the present new small-scale X-axis CPC is useful for the purification of bioactive compounds without loss of their native activities.     

Protein separation with aqueous-aqueous polymer systems by two types of counter-current chromatographs.

Two different types of counter-current chromatographs, the cross-axis coil planet centrifuge (X-axis CPC) and horizontal flow-through coil planet centrifuge (horizontal CPC), were evaluated for protein separation with an aqueous-aqueous two-phase polymer system. The sample solution, containing 10-200 mg each of cytochrome c, myoglobin, ovalbumin and hemoglobin in 2 ml of each phase was eluted with the lower phase. In both instruments, the effects of the flow-rate, revolution speed, and parameter beta (helical diameters of the multilayer coil) on the protein separation were investigated. The best results were obtained from the X-axis CPC operated at 750 rpm and a flow-rate of 2.0 ml/min using a multilayer coil with a small helical diameter (beta = 0.25-0.60). Four protein samples were well resolved in less than 5 h.     

Rapid linear scale-up of a protein separation by centrifugal partition chromatography

The scaling up of the separation of two proteins with an aqueous two-phase system (ATPS) from 176 mg with a 500 ml laboratory scale centrifugal partition chromatography (CPC) column to 2.2g with a 6.25 litre pilot-scale column is presented. A model sample system of a mixture of lysozyme and myoglobin was chosen for this study using an ATPS system comprising 12.5% (w/w) PEG-1000:12.5% (w/w) K2HPO4. It was found that the maximum sample concentration possible without precipitation was 2.2mg/ml for each constituent. The optimisation of rotor speed, mobile phase flow rate and sample loading was performed on a laboratory-scale device. It was found that a centrifuge speed of 2000 rpm (224 'g'), 10 ml/min mobile phase flow rate with a 43 ml (10% of active column volume) sample volume gave optimum operating conditions. This was linearly scaled up to pilot scale by increasing mobile phase flow rate, fraction size and sample loading in the ratio of the system capacities (i.e. 12.5:1). Flow rate was therefore increased from 10 ml/min to 125 ml/min, fraction size from 10 ml to 125 ml and sample loading from 43 ml to 500 ml. Rotor speed however was reduced from 2000 rpm on the laboratory device to 1293 rpm on the pilot-scale device to maintain the same 224 'g' field in each chamber, as the pilot-scale CPC unit has a larger rotor radius than the laboratory one. Resolution increased from Rs=1.28 on the 500 ml rotor to Rs=1.88 on the 6.25 litre rotor, giving potential throughputs in batch mode of over 40 g/day.     

Effect of Coriolis force on counter-current chromatographic separation by centrifugal partition chromatography

The effect of Coriolis force on the counter-current chromatographic separation was studied using centrifugal partition chromatography (CPC) with four different two-phase solvent systems including n-hexane-acetonitrile (ACN); tert-butyl methyl ether (MtBE)-aqueous 0.1% trifluoroacetic acid (TFA) (1:1); MtBE-ACN-aqueous 0.1% TFA (2:2:3); and 12.5% (w/w) polyethylene glycol (PEG) 1000-12.5% (w/w) dibasic potassium phosphate. Each separation was performed by eluting either the upper phase in the ascending mode or the lower phase in the descending mode, each in clockwise (CW) and counterclockwise column rotation. Better partition efficiencies were attained by the CW rotation in both mobile phases in all the two-phase solvent systems examined. The mathematical analysis also revealed the Coriolis force works favorably under the CW column rotation for both mobile phases. The overall results demonstrated that the Coriolis force produces substantial effects on CPC separation in both organic-aqueous and aqueous-aqueous two-phase systems.     

Development and evaluation of a spiral tube column for counter-current chromatography

An improved type-J counter-current chromatography (CCC) planet centrifuge with two spiral tube columns (volume 2×15 mL, β value 0.3-0.7, tubing 0.8 mm id) was developed and evaluated for its retention ability of four typical different solvent systems including heptane-methanol (1:1, v/v) (A), hexane-ethyl acetate-methanol-water (1:1:1:1, v/v) (B), n-butanol-acetic acid-water (4:1:5, v/v) (C), PEG1000-K(2)HPO(4)-water (12.5:12.5:75, w/w) (D) under eight different operation modes. The results indicated that the spiral tube column could significantly increase the retention of four typical solvent systems compared with a traditional multilayer coil column with similar parameters (volume 35 mL, β value 0.3-0.7, tubing 0.8 mm id). The retention of stationary phase (S(f)) for the less polar system (A) and moderately polar solvent system (B) can be increased by about 10%, and for the polar system (C) and aqueous two-phase system (ATPS) (D) by 30-40%. The preliminary applications of this spiral tube column to the separation of small molecular compounds such as moderately polar theaflavins, polar anthocyanins and dipeptides were successful. Acceptable resolution can be obtained between cytochrome c and myoglobin, lysozyme and myoglobin when it was applied on protein separation; however, it still needs to be improved with regard to its column efficiency.     

Mixer-settler counter-current chromatography with multiple spiral disk assembly

A novel system for performing high-speed counter-current chromatography has been developed for separation of biopolymers using polymer phase systems. The spiral disk assembly consisting of eight units, each equipped with over 300 mixer-settler sets, was constructed and performance evaluated in terms of retention of the stationary phase and separation efficiency. A series of experiments was performed with a polymer phase system composed of polyethylene glycol 1000 (12.5%, w/w) and dibasic potassium phosphate (12.5%, w/w) using two stable protein samples of myoglobin and lysozyme at various experimental conditions of flow rates and revolution speeds. The best results were obtained with revolution speeds of 800-1000rpm at flow rates of 0.25-0.5ml/min where the partition efficiency of several 100 theoretical plates was achieved with over 50% stationary phase retention.     

Gram Quantity Separation of DNP (Dinitrophenyl) Amino Acids with Multi-Layer Coil Countercurrent Chromatography (CCC)

Abstract

The efforts have been successfully made to extend the preparative capability of the high-speed CCC scheme with a multi-layer large capacity coiled column. The apparatus is a table top model of a horizontal flow-through coil planet centrifuge which produces a synchronous planetary motion of the column holder. The separation column was prepared from a single piece of 70 m long, 2.6 mm i.d., PTFE tubing coiled around the spool-shaped holder to form multiple layers of the coil with a total capacity of about 400 ml. The performance of the apparatus was assessed with a standard set of DNP amino acid samples and a two-phase solvent system composed of chloroform, acetic acid and 0.1N HCl (2:2:1). Preparative capability of the method was evaluated in terms of the retention level of the stationary phase and peak resolution for various sample size ranging from 0.05g to 2g. The effects of sample volume, sample concentration and the choice of the sample diluent on the separation were studied. The results indicated that both the retention level and the peak resolution tend to decrease with the increase of the sample volume applied at a given concentration. For separation of 1 gram quantity, best results were obtained by applying the sample dissolved in a small volume (10 ml) consisting of equal amounts of the two phases. Overall results indicate that the present scheme is capable of efficient separation for gram quantity of samples in a short period of time. The preparative capability may be further increased by the use of a larger-diameter and/or longer coil.     

Solubility and binding properties of PEGylated lysozyme derivatives with increasing molecular weight on hydrophobic-interaction chromatographic resins

Dynamic binding capacities and resolution of PEGylated lysozyme derivatives with varying molecular weights of poly (ethylene) glycol (PEG) with 5 kDa, 10 kDa and 30 kDa for HIC resins and columns are presented. To find the optimal range for the operating conditions, solubility studies were performed by high-throughput analyses in a 96-well plate format, and optimal salt concentrations and pH values were determined. The solubility of PEG-proteins was strongly influenced by the length of the PEG moiety. Large differences in the solubilities of PEGylated lysozymes in two different salts, ammonium sulfate and sodium chloride were found. Solubility of PEGylated lysozyme derivatives in ammonium sulfate decreases with increased length of attached PEG chains. In sodium chloride all PEGylated lysozyme derivatives are fully soluble in a concentration range between 0.1 mg protein/ml and 10 mg protein/ml. The binding capacities for PEGylated lysozyme to HIC resins are dependent on the salt type and molecular weight of the PEG polymer. In both salt solutions, ammonium sulfate and sodium chloride, the highest binding capacity of the resin was found for 5 kDa PEGylated lysozyme. For both native lysozyme and 30 kDa mono-PEGylated lysozyme the binding capacities were lower. In separation experiments on a TSKgel Butyl-NPR hydrophobic-interaction column with ammonium sulfate as mobile phase, the elution order was: native lysozyme, 5 kDa mono-PEGylated lysozyme and oligo-PEGylated lysozyme. This elution order was found to be reversed when sodium chloride was used. Furthermore, the resolution of the three mono-PEGylated forms was not possible with this column and ammonium sulfate as mobile phase. In 4 M sodium chloride a resolution of all PEGylated lysozyme forms was achieved. A tentative explanation for these phenomena can be the increased solvation of the PEG polymers in sodium chloride which changes the usual attractive hydrophobic forces in ammonium sulfate to more repulsive hydration forces in this hydrotrophic salt.     

Rapid separation of polysaccharides using a novel spiral coil column by high‐speed countercurrent chromatography

The separation of polysaccharides is time consuming. We developed and optimized a type‐J counter‐current chromatography system with a novel tri‐rotor spiral coil column for the rapid separation of polysaccharides. The optimal composition of an aqueous PEG1000/K₂HPO₄/KH₂PO₄ system was found to be 14:16:14 w/w/w where the lower phase was the mobile phase. Optimal performance was achieved at a column rotational speed, temperature, and flow rate of 1200 rpm, 45°C, and 3.0 mL/min, respectively. The mobile phase was pumped from the inner terminal in a ‘‘head‐to‐tail’’ elution mode. Polysaccharide LCP‐1 (10.7 mg) was successfully obtained in high purity in one step from 50.0 mg of a crude polysaccharide extracted from the lychee fruit (Litchi chinensis) within 100 min. LCP‐1 possess a number‐average molecular weight and weight‐average molecular weight of 1.05 × 10⁵ and 1.59 × 10⁵ kDa, respectively. The monosaccharide composition consists of the molar ratio of glucose, galactose, and arabinose of 1.3:3.5:1.     

Large-Scale Preparative Counter-Current Chromatography with a Coil Planet Centrifuge

Abstract

Development of the large-scale preparative countercurrent chromatographic schemes has been continued by increasing the diameter of the separation column. A 0.55 cm i.d. FEP tube was coaxially coiled around the holder (7.5 cm, 10 cm or 15 cm in diameter) of a horizontal flow-through coil planet centrifuge (15 cm revolutional radius). Performance of each column was evaluated on the separation of dinitrophenyl amino acid samples with a two-phase solvent system composed of chloroform, acetic acid, and 0.1N hydrochloric acid (2:2:1) by using both aqueous and nonaqueous phases as the mobile phase. Experiments with the short preliminary columns (114 ml capacity) revealed that the hydrodynamic distribution of the two solvent phases was sensitively affected by the helical diameter of the column. However, by choosing the proper elution mode of the mobile phase, satisfactory results were obtained with the helical diameters of 7.5 cm and 15 cm at a high flow rate of 500 ml/h under a moderate revolutional speed of 300 rpm. With the long coiled columns (750 ml capacity), the preparative capability of the present scheme was successfully demonstrated on separations of the 1g-quantity sample mixture under optimized operational conditions. Overall results indicated that the sample-loading capacity of the present scheme can be further increased by the use of longer and/or larger-diameter columns.     

Stationary phase retention and preliminary application of a spiral disk assembly designed for high-speed counter-current chromatography

A spiral disk assembly composed of five single-channel units was designed for high-speed counter-current chromatography (HSCCC). The retention of different solvent systems ranging from moderately polar to polar organic-aqueous systems to aqueous two-phase systems (ATPs) was investigated under different elution modes. The results indicated that the spiral disk assembly can produce excellent retention of stationary phase for moderately polar organic-aqueous solvent systems, such as chloroform-methanol-water (4:3:2) and hexane-ethyl acetate-methanol-water (1:1:1:1) by pumping lower mobile phase from head (H) to tail (T), and upper mobile phase from tail (T) to head (H) even at a high flow-rate (8 mL/min, Sf>70%), regardless of whether the inlet is at the inner or outer terminal of the channel. This makes it possible for fast analysis of some small molecular compounds. This has been proved in the separation of mixtures of three flavones, including isorhamnetin, kaempferol, and quercetin. The spiral disk assembly can also provide satisfactory retention for polar to ATPS such as 1-butanol-acetic acid-water (4:1:5) (<3 mL/min, Sf>70%), 12.5% poly(ethylene glycol) (PEG) 1000-12.5% K2HPO4-75% water (< or =1 mL/min, Sf>70%) and 4% PEG 8000-5% Dextran T500-91% water (< or =0.5 mL/min, Sf>50%) by pumping lower mobile phase from inner terminal (I) to outer terminal (O), and upper mobile phase from outer terminal (O) to inner terminal (I) at a low flow-rate, while this is not possible with the multilayer coil column. Acceptable resolutions were achieved when it was used for the separation of peptides such as Leu-Tyr and Val-Tyr, and proteins including cytochrome c and myoglobin, lysozyme and myoglobin, and fresh chicken egg-white proteins.     

Evaluation of Analytical Countercurrent Chromatographs: High-Speed Countercurrent Chromatograph-4000 Vs. Analytical Toroidal Coil Centrifuge

Abstract

Performance of two countercurrent chromatographic models, high speed countercurrent chromatograph (HSCCC-4000) and analytical toroidal coil centrifuge (TCC), is evaluated in terms of theoretical plate number, resolution factor and separation time to assess their analytical capability. A series of experiments was conducted to investigate the effects of internal diameter and length of the coiled column, and flow rate of the mobile phase on the separation of indole auxins in two-phase solvent systems composed of n-hexane-ethyl acetate-methanol-water at different volume ratios. The three components of indole auxins were completely resolved in 16 min with a HSCCC system equipped with a multilayer coil of a 0.55 mm I.D. PTFE tube with theoretical plates ranging from 1290 to 829. Similar separation was achieved in 24 min with a TCC systems equipped with a 0.3 mm I.D. PTFE tube with theoretical plates ranging from 1811 to 969. It is concluded that both systems have comparable analytical capability at the present stage of development.     

Protein separation using toroidal columns by type-J synchronous counter-current chromatography towards preparative separation

Separation of large bioactive molecules such as proteins, DNAs and RNAs using aqueous two-phase systems (ATPSs) and liquid–liquid partition-based counter-current chromatography (CCC) can avoid risks of sample loss and denaturation, and greatly reduce processing time. We have constructed toroidal columns (length 26–140 m, column volume 51–280 ml, bore size 1.6 mm) suitable for mounting onto a commercially available preparative CCC apparatus. With the use of an ATPS containing 12.5% (w/w) PEG1000 and 12.5% (w/w) K₂HPO₄ and at a rotational speed of 800 rpm for the rotor of the CCC device, the lower phase (i.e. the phosphate-enriched phase) has been used as the mobile phase and a pair of proteins, myoglobin and lysozyme, as model proteins for demonstrating the separation capability of the CCC system. For a toroidal column with a length of 53.5m and a column volume of 107.5 ml, and operated for the Coriolis force parallel flow mode at 0.62 ml/min, protein sample loading (containing 2.2 mg/ml myoglobin and lysozyme, respectively) at 1.7% and 7.4% to the column volume led to peak resolution (with theoretical plate number TP and stationary phase retention S_f shown in the parenthesis) of R_s = 1.5 (N = 211 and N = 113 TP for myoglobin and lysozyme, respectively, and S_f = 45.0%), and R_s = 1.4 (218 and 152 TP, and S_f = 34.0%). However, further increase of the loading to 13% failed to separate the two proteins. Although proteins eluted at positions predictable from the distribution coefficients, they showed broader peaks when compared with small dipeptides under identical CCC operating conditions. This confirms that the molecular weight of the partitioned species is an important factor causing peak broadening on CCC chromatograms. These results paved the way for further scaling-up toroidal CCC columns for processing larger quantities of samples containing large biomolecules.     

Protein separation by open tubular capillary electrochromatography employing a capillary coated with phenylalanine functionalized tentacle-type polymer under both cathodic and anodic electroosmotic flows

The use of a phenylalanine (Phe) functionalized tentacle-type polymer coated capillary column for protein separation by open tubular capillary electrochromatography (OTCEC) was demonstrated in this work. The tentacle-type stationary phase was prepared from silanized fused-silica capillaries of 50 microm I.D. by glycidyl methacrylate graft polymerization and subsequent Phe functionalization. Due to the amphoteric functional groups of the Phe bonded on the tentacle-type polymer stationary phase, protein separation in the prepared column can be performed under both cathodic and anodic electroosmotic flow (EOF) by varying the pH values of the mobile phase. Model proteins including ribonuclease A (RNase A), myoglobin, transferrin, insulin were baseline separated under cathodic EOF with a mobile phase of pH 8.8. Comparison between the separation result of the four proteins under conditions of OTCEC and capillary zone electrophoresis indicates that the migration behavior of the four proteins in the prepared column was the result of the interplay of chromatographic retention and electrophoretic migration. Besides, three basic proteins including RNase A, cytochrome c (Cyt-c) and lysozyme (Lys) were fully resolved under anodic EOF with an acidic running buffer (pH 2.5). The elution order was the same as the isoelectric point values of the proteins (RNase A相似文献   

Large-scale preparative countercurrent chromatography for separation of polar compounds

Gram quantity separations of polar compounds (tryptophyl-leucine and valyl-tyrosine) have successfully been accomplished with the use of a horizontal coil planet centrifuge. Two columns of different length fluorinated ethylene propylene tubing but of same internal diameter (0.55 cm) were coaxially coiled around a holder 7.5 cm or 15 cm in diameter and used to assess the preparative capabilities of the apparatus in terms of stationary phase retention and sample peak resolution. Optimal operating conditions derived from preliminary studies with the short column were applied to a column 7 times in length and volume. Volume capacities were 114 ml and 750 ml respectively. A hydrophilic solvent system of n-butanol, acetic acid and water (4:1:5) was used with both the aqueous and non-aqueous phases being used as the mobile phase. Preliminary studies revealed that the hydrodynamic distribution of the two phases was independent of the helical diameter while peak resolution was sensitive to both helical diameter and rpm setting.     

Preparation of the monomers of gingerols and 6-shogaol by flash high speed counter-current chromatography

The flash high speed counter-current chromatographic (FHSCCC) separation of gingerols and 6-shogaol was performed on a HSCCC instrument equipped with a 1200-ml column (5 mm tubing i.d.) at a flow rate of 25 ml/min. The performance met the FHSCCC feature that the flow rate of mobile phase (ml) is equal to or greater than the square of the diameter of the column tubing (mm). The separation employed the upper phase of stationary phase of the n-hexane-ethyl acetate-methanol-water (3:2:2:3, v/v) as the stationary phase. A stepwise elution was performed by eluting with the lower phase of n-hexane-ethyl acetate-methanol-water (3:2:2:3, v/v) for first 90 min and the lower phase of the n-hexane-ethyl acetate-methanol-water (3:2:6:5, v/v) for the second 90 min. In each separation 5 g of the ethyl acetate extract of rhizomes of ginger was loaded, yielding 1.96 g of 6-gingerol (98.3%), 0.33 g of 8-gingerol (97.8%), 0.64 g of 6-shogaol (98.8%) and 0.57 g of 10-gingerol (98.2%). The separation can be expected to scale up to industrial separation.     

阴离子交换整体柱对蛋白质的分离与纯化

分别用乙二胺、二乙胺、三乙胺将自制的以甲基丙烯酸缩水甘油酯(GMA)为单体、乙二醇二甲基丙烯酸酯(EDMA)为交联剂的整体柱修饰为弱、强阴离子交换整体柱。考察了该整体柱的性能,选择出分离蛋白质(牛血清白蛋白、溶菌酶和谷胱甘肽)的最佳实验条件,并在最佳分离条件下考察了这些蛋白质在整体柱上的色谱行为和该整体柱对纤维素降解酶的分离纯化情况。实验结果表明,该整体柱性能良好,可以实现对纤维素降解酶的快速分离与纯化。同时,实验也证明采用梯度洗脱可以实现对某些蛋白质的分离纯化。     

Considerations of sample application and elution during size-exclusion chromatography-based protein refolding

A mechanism for size-exclusion chromatography-based protein refolding is described. The model considers the steps of loading the denatured protein onto a gel filtration column, and protein elution. The model predictions are compared with results of refolding lysozyme (10 and 20 mg/ml) using Superdex 75 HR. The main collapse in protein structure occurred immediately after loading, where the partition coefficient of unfolded lysozyme increased from 0.1 to 0.48 for the partially folded molecule. Use of a refolding buffer as the mobile phase resulted in complete refolding of lysozyme; this eluted at an elution volume of 15.6 ml with a final partition coefficient of 0.54. The model predicted the elution volume of refolded lysozyme at 19.3 ml.     

Cross-axis synchronous flow-through coil planet centrifuge (type XLL). I. Design of the apparatus and studies on retention of stationary phase

The fourth prototype holds a pair of column holders in the lateral position at 15 cm from the center of the rotary shaft horizontally mounted on the rotary frame at 7.6 cm from the central axis of the apparatus. Using short coils of 2.6 mm I.D. PTFE (polytetrafluoroethylene) tubing with 7.6 cm and 24 cm helical diameters, retention of the stationary phase was measured in ten pairs of two-phase solvent systems under various experimental conditions. Satisfactory retention was obtained by choosing proper combinations of three factors, i.e., the direction of planetary motion, head-tail elution mode, and inward-outward elution mode. The polar butanol solvent systems showed excellent retention from 65 to 80% in the 7.6 cm helical diameter left-handed coil.