Purification, characterization, and fibrinogen cleavage sites of three fibrinolytic enzymes from the venom of Crotalus basiliscus basiliscus.

Three distinct fibrinolytic enzymes have been purified from the venom of Crotalus basiliscus basiliscus (the Mexican west coast rattlesnake). The high-performance liquid chromatography-based purification comprised the following steps: (a) hydrophobic interaction chromatography; (b) hydroxylapatite chromatography; (c) anion-exchange chromatography. Following hydrophobic interaction chromatography two fibrinolytic activity peaks were detected, Cbfib1 and Cbfib2. Cbfib2 was rendered homogeneous following hydroxylapatite chromatography. Upon hydroxylapatite chromatography Cbfib1 was shown to consist of two components, Cbfib1.1 and Cbfib1.2. Both Cbfib1.1 and Cbfib1.2 were purified to homogeneity using anion-exchange chromatography. SDS-polyacrylamide gel electrophoresis revealed that Cbfib1.1 and Cbfib1.2 had similar molecular weights (approximately 23,500), whereas Cbfib2 displayed a molecular weight of approximately 22,500. The enzymes do not appear to be glycosylated. Tryptic digests of all three enzymes, analyzed by high-performance reverse-phase chromatography, suggest that Cbfib1.1 and Cbfib1.2 are closely related and different from Cbfib2. The latter displayed more similarity with Cbfib1.2 than with Cbfib1.1. Specific fibrinolytic activity for all three enzymes was very similar, but general proteolytic activity varied substantially with Cbfib2 showing a 12-fold higher specific proteolytic activity when compared to Cbfib1.1 and Cbfib1.2. None of these enzymes exhibited hemorrhagic activity when injected (up to 100 micrograms) subcutaneously into mice. Cbfib1.1 and Cbfib1.2 action against fibrinogen was directed equally against both the A alpha- and B beta-chains. Against fibrin the rate of degradation of the alpha-chain was considerably higher than that of the beta-chain. Cbfib2 showed mainly alpha-fibrin(ogen)ase activity with limited activity on the beta-chain. Several fibrinogen cleavage sites on the A alpha-chain have been identified: Cbfib1.1 and Cbfib1.2 cleave at Lys413-Leu414, Ser505-Thr506, and Tyr560-Ser561. Cbfib2 cleaves mainly at Gly254-Ser255 and Pro516-Met517.     

Purification of carbonic anhydrase isoenzymes by high-performance affinity chromatography and hydrophobic interaction chromatography

Isoenzymes of carbonic anhydrase were purified by a combination of affinity chromatography and hydrophobic interaction chromatography. Immobilization of sulfonamides on an epoxy-activated support provided a stationary phase for affinity chromatography which was stable to hydrolysis by carbonic anhydrase. A first purification step allowed the isolation of enzymes directly from homogenates of human erythrocytes and rat stomach. Without any further preparation, except the addition of ammonium sulfate to the eluate from affinity chromatography, the isoenzymes could be separated by hydrophobic interaction chromatography with very high recovery of protein and retention of enzymatic activity.     

Chromatography of hydroxysteroid dehydrogenases

The structure-function study of hydroxysteroid dehydrogenases has stimulated the development of their chromatography, which in turn reveals more mechanisms of these enzumes. Due to the various membrane associations and mild hydrophobic nature of most of the enzymes studied up to now, hydrophobic interaction chromatography has played a crucial role in their purification, using media such as phenyl-Superose or Sepharose-PEG. At the same time, affinity chromatography, especially the dye-containing columns, proves very efficient for these dehydrogenases, as the latter utilizes adenylyl-containing cofactors. Elution by their specific ligand facilitates their purification. In this paper, the use of detergents in the purification of these enzymes is also reviewed. Hydroxysteroid dehydrogenase preparation is further improved by rapid purification which facilitates the elimination of protein microheterogeneity, caused in vitro by oxidation, reduction or partial proteolysis. This process was shown to increase the crystallizability of the enzymes [Lin et al., J. Cryst. Growth, 122 (1992) 242–245; Zhu et al., J. Mol. Biol., 234 (1993) 242–244]. The fast purification permitted a simpler procedure and better combination of various columns than conventional chromatography. This leads to even higher efficiency, yielding homogeneous and highly active preparations.     

Negative chromatography: Progress,applications and future perspectives

In negative chromatography, the impurities bind on the adsorbent, and the product is allowed to flow through the chromatographic column. Negative chromatography is an alternative to positive chromatography under certain circumstances and has been used to purify various biomolecules. For this review, a detailed survey of the performance of reported studies on negative chromatography was conducted. The applications of negative chromatography in the capture and intermediate purification steps for biomolecules (e.g., plasmid DNA, antibodies, enzymes, hemoglobin, virus particles and cells) are reviewed. The negative chromatographic adsorbents adsorb the impurities through surface charge, hydrophobic interaction at specific sites on the surface, hydrophobic interaction, hydrogen bonding and functional groups. Examples of applications of negative chromatography according to the type of chromatography matrix used are summarized and discussed. In addition, the effects of operating conditions (initial protein concentration, buffer ions, pH and salt concentration) are discussed, and the criteria for choosing negative or positive chromatography are summarized. The literature survey showed that there will be future limitations and challenges ahead in implementation of negative chromatography. Possible solutions to the limitations and challenges of negative chromatography and future trends for developing negative chromatography are discussed.     

Purification of human macrophage colony stimulating factor (CSF-1) from medium conditioned by pancreatic carcinoma cells

Colony Stimulating Factor-1 has been purified to apparent homogeneity from the serum-free medium conditioned by cultured human pancreatic carcinoma cells which had been induced with phorbol myristate acetate. The purification scheme consisted of sequential steps of batchwise adsorption to calcium phosphate gel, adsorption to lentil lectin-Sepharose, binding to immobilized antibodies, hydrophobic interaction chromatography, and reversed-phase high-performance liquid chromatography. The purified glycoprotein was found to have a subunit molecular weight corresponding to the smallest of four species (approximately 40,000, 33,000, 28,000 and 23,000) which were observed when less purified preparations were examined.     

Detection of two high molecular weight hydrophobic forms of the human estrogen receptor

The human estrogen receptor gene encodes a single protein of molecular weight 65,000 daltons. However, using a sensitive and rapid technique of high-performance hydrophobic interaction chromatography we have detected two distinct estrogen receptor species both of which are high molecular weight proteins (ca. 60A) as determined by high-performance size-exclusion chromatography. These are detected either in the presence or absence of sodium molybdate; rechromatography of individual isoform indicates that the two protein complexes have independent hydrophobic contact points. Consistent elution patterns of the two receptor species indicates they are formed selectively. We conclude that different post-translational modifications of the estrogen receptor protein could allow their specific interaction with non-receptor components resulting in the formation of two distinct high molecular weight complexes which would be rapidly resolved by high-performance hydrophobic interaction chromatography.     

Linear multidimensional liquid chromatography in the preparative scale purification of calmodulin from brain extract

Rapid preparative scale purification of calmodulin from crude bovine brain extract is achieved in a single chromatographic run by physically coupling two different liquid chromatography columns which employ different separation mechanisms. In this case columns packed with newly commercialized 40-microns silica-based hydrophobic interaction and 5-microns micron silica-based weak anion-exchange chromatography media were used. The only sample preparation required for conducting this purification procedure is the addition of salt to the crude brain supernatant to promote the initial binding of calmodulin to the hydrophobic interaction chromatography media. Chromatography carried out on such linear arrangements of columns has been referred to as linear multidimensional liquid chromatography.     

Calorimetry for studying the adsorption of proteins in hydrophobic interaction chromatography

Hydrophobic interaction chromatography is a very popular chromatography method for purification of proteins and plasmids in all scales from analytical to industrial manufacturing. Despite this frequent use, the complex interaction mechanism and the thermodynamic aspects of adsorption in hydrophobic interaction chromatography are still not well understood. Calorimetric methods such as isothermal titration calorimetry and flow calorimetry can help to gain a deeper understanding of the adsorption strength, the influence of salt type and temperature. They can be used to study conformational changes of proteins, which are often associated with the adsorption in hydrophobic interaction chromatography. This review offers a detailed introduction into the thermodynamic fundamentals of adsorption in hydrophobic interaction chromatography with a special focus on the potential applications of isothermal titration calorimetry and flow calorimetry for studying specific problems and relationships of the adsorption behavior of proteins and its various influencing factors. Models for characterizing conformational changes upon adsorption are presented together with methods for assessing this problem for different proteins and stationary phases. All of this knowledge can contribute greatly to forming a sound basis for method development, process optimization and finding modelling strategies in hydrophobic interaction chromatography.     

A simple and rapid purification of kallikrein from rat submandibular gland.

Rat submandibular kallikrein was isolated in an 87% yield by a very quick and simple procedure involving hydrophobic interaction chromatography. Furthermore, that purification method was superior to both aprotinin-affinity chromatography and immunoaffinity chromatography for the purification of rat submandibular kallikrein. The kallikrein purified by hydrophobic interaction chromatography consisted of a number of isoenzymes. The major component of Mr 38,000 seen on SDS-gel electrophoresis was found to be the glycosylated kallikrein, whereas the minor component of Mr 26,000 represented the non-glycosylated enzyme.     

Review: cyclodextrins and their interaction with amylolytic enzymes

This review is concerned with inhibition of amylases by cyclodextrins (cyclic maltooligosaccharides), the interaction that occurs between amylases and cyclodextrins and the application of cyclodextrin affinity chromatography in the purification of amylases. In many cases, amylases that are competitively inhibited by cyclodextrins can be purified by cyclodextrin affinity chromatography with the cyclodextrins interacting with the active site on such enzymes. Interestingly amylases that are not competitively inhibited by cyclodextrins may also be purified by cyclodextrin affinity chromatography. Therefore, cyclodextrin affinity chromatography can function in the purification of such amylolytic enzymes with the interaction occurring at a site removed from the active site. In such cases it appears that the cyclodextrin is interacting with an affinity site or binding site that is present on some amylolytic enzymes. It seems that certain similarities occur among the binding sites of such enzymes. Literature concerning amylases, and their subsequent purification using cyclodextrin affinity chromatography is reviewed and the fundamental basis of the interaction of the cyclodextrin with amylolytic enzymes is discussed here.     

Separation of various calmodulins, calmodulin tryptic fragments, and different homologous Ca2+-binding proteins by reversed-phase, hydrophobic interaction, and ion-exchange high-performance liquid chromatography techniques

Reversed-phase, hydrophobic interaction, and ion-exchange high-performance liquid chromatography techniques have been used to separate different Ca2+-binding proteins and their proteolytic fragments. An alkali-stable ion-exchange column permitted the baseline separation of calmodulin fragments which differed only by one to three charged amino acids. The new hydrophobic interaction chromatography system displayed a high-resolution power separating calmodulins from different sources and calmodulin fragments obtained by trypsin proteolysis. The properties and advantages of the different systems are discussed in detail.     

Purification of a -hydantoinase using a laboratory-scale Streamline phenyl column as the initial step

A -hydantoinase from Thermus sp. was overexpressed in Escherichia coli and purified to homogeneity for subsequent crystallization. The purification was performed with hydrophobic interaction chromatography as the capture step followed by anion-exchange chromatography and gel permeation chromatography as intermediate purification and polishing steps, respectively. The hydrophobic interaction step was done in fluidized bed mode in a laboratory-scale Streamline column made from conventional laboratory equipment. The whole purification protocol could be finished within one day. The purified enzyme crystallizes. The crystals are suitable for X-ray protein structure analysis and diffract to at least 2.3 Å resolution. Complete data sets have been measured up to 2.6 Å resolution. The X-ray structure is currently being solved.     

HPLC-based two-step purification of fibrinolytic enzymes from the venom of Agkistrodon contortrix contortrix and Agkistrodon piscivorus conanti

In investigations aimed at characterizing snake venom blood clot-dissolving enzymes, we have developed a rapid two-step high-performance chromatography method for the isolation of these fibrinolytic enzymes from the venoms of Agkistrodon contortrix contortrix and Agkistrodon piscivorus conanti. The first step consisted of hydrophobic interaction chromatography on a propyl-aspartamide column. Fractions containing the fibrinolytic activity were then concentrated and applied to a hydroxylapatite column. The resulting preparation, assessed for purity by reverse-phase chromatography and sodium dodecyl sulfate-polyacrylamide gel electrophoresis, was homogeneous. The molecular weight of both venom fibrinolytic enzymes was approximately 23,000 and amino acid analysis, immunological cross-reaction, cyanogen bromide, and tryptic digestion indicate a significant degree of structural similarity. However, the general proteolytic activity of the A. p. conanti venom enzyme was significantly lower than the corresponding activity of the A. c. contortrix venom, whereas their fibrinolytic activities were quite similar.     

Glycolytic enzymes of Trypanosoma brucei. Simultaneous purification, intraglycosomal concentrations and physical properties

We have developed a method for the simultaneous purification of hexokinase, glucosephosphate isomerase, phosphofructokinase, fructose-1,6-bisphosphate aldolase, triosephosphate isomerase, D-glyceraldehyde-phosphate dehydrogenase, phosphoglycerate kinase, glycerol-3-phosphate dehydrogenase and glycerol kinase from Trypanosoma brucei in yields varying over 8-55%. Crude glycosomes were prepared by differential centrifugation of cell homogenates. Subsequent hydrophobic interaction chromatography on phenyl-Sepharose resulted in six pools containing various mixtures of enzymes. These pools were processed via affinity chromatography (immobilized ATP), hydrophobic interaction chromatography (octyl-Sepharose) and ion-exchange chromatography (CM- and DEAE-cellulose) which resulted in the purification of all nine enzymes. The native enzyme and subunit molecular masses, as determined by gel filtration and gel electrophoresis under denaturing conditions, were compared with those of their homologous counterparts from other organisms. Trypanosomal hexokinase is a hexamer and differs in subunit composition from the mammalian enzymes (monomers) as well as in subunit size (51 kDa versus 96-100 kDa, respectively). Phosphofructokinase only differs in subunit size (51 kDa for T. brucei versus 80-90 kDa for mammals) but had identical subunit composition (tetrameric). The others all have the same subunit composition as their mammalian counterparts. Except for triosephosphate isomerase, all Trypanosoma enzymes have subunits which are 1-5 kDa larger in size. Together these nine enzymes contribute 3.3 +/- 1.6% to the total cellular protein of T. brucei and at least 90% to the total glycosomal protein. A comparison of calculated intraglycosomal concentrations of the enzymes with the glycosomal metabolite concentrations shows that in the case of aldolase, glyceraldehyde-phosphate dehydrogenase and phosphoglycerate kinase, the concentration of active sites is of the same order of magnitude as that of their reactants. A common feature of the glycosomal glycolytic enzymes (with the exception of glucosephosphate isomerase) is that they are highly basic proteins with pI values between 8.8 and 10.2, values which are 1-4 higher than in the case of their mammalian cytosolic counterparts and 3-6 higher than in the case of the various unicellular organisms. It is suggested that both the larger subunit size and the basic character of the T. brucei glycolytic proteins are involved in the routing of the enzymes from their site of biogenesis (the cytosol) towards their site of action (the glycosome).     

Tetanus toxoid purification: chromatographic procedures as an alternative to ammonium-sulphate precipitation

Given an existing demand to establish a process of tetanus vaccine production in a way that allows its complete validation and standardization, this paper focuses on tetanus toxoid purification step. More precisely, we were looking at a possibility to replace the widely used ammonium-sulphate precipitation by a chromatographic method. Based on the tetanus toxin's biochemical characteristics, we have decided to examine the possibility of tetanus toxoid purification by hydrophobic chromatography, and by chromatographic techniques based on interaction with immobilized metal ions, i.e. chelating chromatography and immobilized metal affinity chromatography. We used samples obtained from differently fragmented crude tetanus toxins by formaldehyde treatment (assigned as TTd-A and TTd-B) as starting material for tetanus toxoid purification. Obtained results imply that purification of tetanus toxoid by hydrophobic chromatography represents a good alternative to ammonium-sulphate precipitation. Tetanus toxoid preparations obtained by hydrophobic chromatography were similar to those obtained by ammonium-sulphate precipitation in respect to yield, purity and immunogenicity. In addition, their immunogenicity was similar to standard tetanus toxoid preparation (NIBSC, Potters Bar, UK). Furthermore, the characteristics of crude tetanus toxin preparations had the lowest impact on the final purification product when hydrophobic chromatography was the applied method of tetanus toxoid purification. On the other hand, purifications of tetanus toxoid by chelating chromatography or immobilized metal affinity chromatography generally resulted in a very low yield due to not satisfactory tetanus toxoid binding to the column, and immunogenicity of the obtained tetanus toxoid-containing preparations was poor.     

Purification of a phospholipase B inhibitor from Saccharomyces cerevisiae

The phospholipase B activity of plasma membrane vesicles from Saccharomyces cerevisiae is inhibited by the 100 000 X g supernatant of mechanically disrupted yeast cells. A 1850-fold purification of the inhibitor activity was achieved by gel filtration, ion exchange chromatography with DEAE-cellulose and hydrophobic interaction chromatography with Octyl-Sepharose. SDS-polyacrylamide gel electrophoresis of the purified inhibitor revealed two main bands with an apparent Mr of 60 000 and 26 500. The phospholipase B activity was strongly reduced but not completely blocked by this preparation, while the lysophospholipase and transacylase reactions, which are catalyzed by the same membrane-bound enzymes (Witt, W. et al. (1984) Biochim. Biophys. Acta 795, 108-116), were not affected.     

Hydrophobic interaction chromatography on octyl sepharose--an approach for one-step platform purification of cyclodextrin glucanotransferases

Cyclodextrin glucanotransferase (CGTase) from Bacillus circulans ATCC 21783 was concentrated by ultrafiltration and subsequently purified by hydrophobic interaction chromatography on Octyl Sepharose 4 fast flow. The matrix was able to bind selectively to the enzyme at a very low ammonium sulfate concentration of 0.67 M and enzyme desorption was performed by decreasing gradient of the salt. The overall recovery was 80% with 689-fold purity. CGTases derived from four soil isolates and Toruzyme, the commercial preparation of CGTase, also bound to Octyl Sepharose under similar conditions at 0.67 M and eluted at 0.55-0.5 M of ammonium sulfate. Octyl Sepharose chromatography can thus be used as a platform approach for purification of CGTases from various bacterial sources. Long stretches of sequence predominated by hydrophobic amino acids are reportedly present in the starch binding domains of CGTases. Starch binding experiments indicated the binding of the enzymes to the octyl matrix through these domains.     

Native purification of biomolecules with temperature-mediated hydrophobic modulation liquid chromatography

The high-resolution purification of native enzymes is impeded by the limitations in the mobile-phase choices required for conventional hydrophobic separations such as in reverse-phase chromatography. To avoid problems associated with varying the composition of the mobile phase, we developed a stationary phase with a hydrophobicity that can be modulated by slight variations in temperature to bind and elute biomolecules. This chromatographic matrix was tested on nucleotide analogs, amino acids, and protein samples. Visualization of the temperature-dependent hydrophobic interaction with the chromatographic matrix was performed with fluorescence microscopy of CY3-ATP. Amino acids adsorbed to the column according to their known hydrophobicities, confirming the hydrophobic nature of their interaction with the matrix. Biomolecules were separated by modulating the hydrophobicity of the column matrix with slight adjustments to the running temperature between 22 and 37 degrees C without changing the mobile phase. Freedom in the choice of a mobile phase for both the loading and the elution of samples provides great practical advantages by eliminating the need for buffer-exchange steps and allowing more native conditions for purifying delicate enzymes, such as myosin.     

Leucyl-tRNA and lysyl-tRNA synthetases, derived from the high-Mr complex of sheep liver, are hydrophobic proteins

The leucyl-tRNA and lysyl-tRNA synthetase components of the multienzyme complex from sheep liver were selectively dissociated by hydrophobic interaction chromatography on hexyl-agarose and purified to homogeneity. Conservation of activities during the purification required the presence of Triton X-100. The homogeneous enzymes corresponded to a monomer of Mr 129000 and a dimer of Mr 2 X 79000, respectively. Both were strongly adsorbed to the hydrophobic support phenyl-Sepharose, in conditions where the corresponding purified enzymes from yeast and Escherichia coli were not bound. Moreover, like the corresponding enzymes from yeast but unlike those of prokaryotic origin, the purified leucyl-tRNA and lysyl-tRNA synthetases derived from the complex displayed affinity for polyanionic supports. It is shown that proteolytic conversion of lysyl-tRNA synthetase to a fully active dimer of Mr 2 X 64000, leads to loss of both the hydrophobic and the polyanion-binding properties. These results support the view that each subunit of lysyl-tRNA synthetase is composed of a major catalytic domain, similar in size to the subunit of the prokaryotic enzyme, contiguous to a chain extension which carries both cationic charges and hydrophobic residues. The implications of these findings on the structural organization of the complex are discussed in relation to its other known properties.     

疏水相互作用层析分离重组人干扰素α2b

目的采用疏水相互作用层析分离重组人干扰素α2b,去除干扰素样品中的二聚体,得到高纯度的干扰素用于进一步的研究。方法首先采用阳离子交换层析纯化复性重组人干扰素α2b,去除了大部分的杂蛋白,然后采用疏水相互作用层析纯化重组人干扰素α2b,去除复性过程中产生的错误折叠体和二聚体,并考察盐浓度、pH值、流速和洗脱液中尿素对疏水相互作用层析纯化效果的影响。结果硫酸铵初始浓度1.2 mol/L、缓冲液pH值6.0、流速2.5 mL/min、洗脱液中添加尿素浓度为2 mol/L时疏水相互作用层析纯化效果最佳。最终得到的重组人干扰素α2b非还原型SDS-PAGE电泳均呈单一条带。结论确定了疏水层析纯化重组人干扰素α2b的最优条件,成功提取到具有高活性、高纯度的重组人干扰素α2b纯品。