Refolding and characterization of a yeast dehydrodolichyl diphosphate synthase overexpressed in Escherichia coli.

Dehydrodolichyl diphosphate synthase (DDPPs) catalyzes the sequential condensation of isopentenyl diphosphate with farnesyl diphosphate to synthesize long-chain dehydrodolichyl diphosphate, which serves as a precursor of glycosyl carrier in glycoprotein biosynthesis in eukaryotes. To perform kinetic and structural studies of DDPPs, we have expressed yeast DDPPs using Escherichia coli as the host cell. Thioredoxin and His tag were utilized to increase the solubility of the recombinant protein and facilitate its purification using Ni-nitrilotriacetic acid (NTA) column. The protein was overexpressed in E. coli but mostly existed in pellet in the absence of detergent. The low quantity of soluble DDPPs was purified using Ni-NTA, Mono Q anion-exchange, and size-column chromatographies. The protein in the pellet was solubilized with 7 M urea and purified using Ni-NTA under denaturing condition. The protein refolding was achieved via the stepwise dialysis to remove the denaturant in the presence of 6 mM beta-mercaptoethanol. Detergent n-octyl-beta-d-glucopyranoside and Triton X-100 increased the solubility of the DDPPs so that refolding can be performed at higher protein concentration. Alternatively, on-column refolding was carried out in a single step to obtain the active protein in large quantities. beta-Mercaptoethanol and Triton were both required in this quick refolding process. The kinetic studies indicated that the soluble and refolded DDPPs have comparable activities (k(cat) = 2 x 10(-4) s(-1)). Unlike its bacterial homologue, undecaprenyl diphosphate synthase, yeast DDPPs activity was not enhanced by Triton.     

Refolding and purification of Zymomonas mobilis levansucrase produced as inclusion bodies in fed-batch culture of recombinant Escherichia coli

Zymomonas mobilis levansucrase was overproduced by the fed-batch culture of recombinant Escherichia coli harboring a novel expression system that is constitutively expressed by the promoter from the Rahnella aquatilis levansucrase gene. Most of the levansucrase was produced as inclusion bodies in the bacterial cytoplasm, accounting for approximately 20% of the total cellular protein. Refolding after complete denaturation by high concentrations of urea or guanidine hydrochloride was not successful, resulting in large amounts of insoluble aggregates. During the development of the refolding method, it was found that direct solubilization of the inclusion bodies with Triton X-100 reactivated the enzyme, with a considerable refolding efficiency. About 65% of inclusion body levansucrase was refolded into active levansucrase in the renaturation buffer containing 4% (v/v) Triton X-100. The in vitro refolded enzyme was purified to 95% purity by single-step DEAE-Sepharose ion exchange chromatography. Triton X-100 was removed by this ion exchange chromatography.     

Refolding and Characterization of a Yeast Dehydrodolichyl Diphosphate Synthase Overexpressed in Escherichia coli

Dehydrodolichyl diphosphate synthase (DDPPs) catalyzes the sequential condensation of isopentenyl diphosphate with farnesyl diphosphate to synthesize long-chain dehydrodolichyl diphosphate, which serves as a precursor of glycosyl carrier in glycoprotein biosynthesis in eukaryotes. To perform kinetic and structural studies of DDPPs, we have expressed yeast DDPPs using Escherichia coli as the host cell. Thioredoxin and His tag were utilized to increase the solubility of the recombinant protein and facilitate its purification using Ni-nitrilotriacetic acid (NTA) column. The protein was overexpressed in E. coli but mostly existed in pellet in the absence of detergent. The low quantity of soluble DDPPs was purified using Ni-NTA, Mono Q anion-exchange, and size-column chromatographies. The protein in the pellet was solubilized with 7 M urea and purified using Ni-NTA under denaturing condition. The protein refolding was achieved via the stepwise dialysis to remove the denaturant in the presence of 6 mM β-mercaptoethanol. Detergent n-octyl-β- -glucopyranoside and Triton X-100 increased the solubility of the DDPPs so that refolding can be performed at higher protein concentration. Alternatively, on-column refolding was carried out in a single step to obtain the active protein in large quantities. β-Mercaptoethanol and Triton were both required in this quick refolding process. The kinetic studies indicated that the soluble and refolded DDPPs have comparable activities (k_cat = 2 × 10⁻⁴ s⁻¹). Unlike its bacterial homologue, undecaprenyl diphosphate synthase, yeast DDPPs activity was not enhanced by Triton.     

Refolding and Purification of Zymomonas mobilis Levansucrase Produced as Inclusion Bodies in Fed-Batch Culture of Recombinant Escherichia coli

Zymomonas mobilis levansucrase was overproduced by the fed-batch culture of recombinant Escherichia coli harboring a novel expression system that is constitutively expressed by the promoter from the Rahnella aquatilis levansucrase gene. Most of the levansucrase was produced as inclusion bodies in the bacterial cytoplasm, accounting for approximately 20% of the total cellular protein. Refolding after complete denaturation by high concentrations of urea or guanidine hydrochloride was not successful, resulting in large amounts of insoluble aggregates. During the development of the refolding method, it was found that direct solubilization of the inclusion bodies with Triton X-100 reactivated the enzyme, with a considerable refolding efficiency. About 65% of inclusion body levansucrase was refolded into active levansucrase in the renaturation buffer containing 4% (v/v) Triton X-100. The in vitro refolded enzyme was purified to 95% purity by single-step DEAE–Sepharose ion exchange chromatography. Triton X-100 was removed by this ion exchange chromatography.     

Effects of solutes on solubilization and refolding of proteins from inclusion bodies with high hydrostatic pressure

High hydrostatic pressure (HHP)-mediated solubilization and refolding of five inclusion bodies (IBs) produced from bacteria, three gram-negative binding proteins (GNBP1, GNBP2, and GNBP3) from Drosophila, and two phosphatases from human were investigated in combination of a redox-shuffling agent (2 mM DTT and 6 mM GSSG) and various additives. HHP (200 MPa) combined with the redox-shuffling agent resulted in solubilization yields of approximately 42%-58% from 1 mg/mL of IBs. Addition of urea (1 and 2 M), 2.5 M glycerol, L-arginine (0.5 M), Tween 20 (0.1 mM), or Triton X-100 (0.5 mM) significantly enhanced the solubilization yield for all proteins. However, urea, glycerol, and nonionic surfactants populated more soluble oligomeric species than monomeric species, whereas arginine dominantly induced functional monomeric species (approximately 70%-100%) to achieve refolding yields of approximately 55%-78% from IBs (1 mg/mL). Our results suggest that the combination of HHP with arginine is most effective in enhancing the refolding yield by preventing aggregation of partially folded intermediates populated during the refolding. Using the refolded proteins, the binding specificity of GNBP2 and GNBP3 was newly identified the same as with that of GNBP1, and the enzymatic activities of the two phosphatases facilitates their further characterization.     

Purification of cytochrome b6 A tightly bound protein in chloroplast membranes

Purification of cytochrome b₆ was pursued to further develop rational technology for purification, proof of purity, and study of properties of membrane proteins. Cytochrome b₆ was purified—the first time from any source—from spinach chloroplast membranes; yield of pure cytochrome b₆ was 30% of that found in ethanol-extracted particles. The three-step procedure (pH 8) employed: (I) extraction in Triton X-100-4 M (optionally 2 M) urea, (II) chromatography in a Bio-Gel A-1.5m Column (Triton X-100-4 M urea). Without this step, subsequent electrophoresis failed. (III) Preparative disc gel electrophoresis.

Properties of cytochrome b₆: Cytochrome b₆ migrated in undenatured form as a single band in disc electrophoresis (pH 8, 7 or 8.9). None of the limited, accepted properties of the cytochrome in particles was altered by the purification procedure: Reduced b₆ has absorption maxima (22 °C) at 434, 536, and 563 nm; at −199 °C the a absorption region shows two peaks of equal intensity at 561 and 557 nm. Cytochrome b₆ is reduced by dithionite (not by ascorbate) and is autoxidizable. The prosthetic group of b₆ is protohaemin and is fully extractable by acid-acetone. No non-haem iron is present. The millimolar extinction coefficient of reduced b₆ (563–600nm) per mole of haem is 21. The protein equivalent weight is 40000 g per mole of haem. Cytochrome b₄ is an intrinsically aggregatable molecule. The reduced cytochrome does not react with CO except when Triton X-100 is present.     

Inclusion body purification and protein refolding using microfiltration and size exclusion chromatography

The presence of inclusion body impurities can affect the refolding yield of recombinant proteins, thus there is a need to purify inclusion bodies prior to refolding. We have compared centrifugation and membrane filtration for the washing and recovery of inclusion bodies of recombinant hen egg white lysozyme (rHEWL). It was found that the most significant purification occurred during the removal of cell debris. Moderate improvements in purity were subsequently obtained by washing using EDTA, moderate urea solutions and Triton X-100. Centrifugation between each wash step gave a purer product with a higher rHEWL yield. With microfiltration, use of a 0.45 micron membrane gave higher solvent fluxes, purer inclusion bodies and greater protein yield as compared with a 0.1 micron membrane. Significant flux decline was observed for both membranes. Second, we studied the refolding of rHEWL. Refolding from an initial concentration of 1.5 mg ml-1, by 100-fold batch dilution gave a 43% recovery of specific activity. Purified inclusion bodies gave rise to higher refolding yields, and negligible activity was observed after refolding partially purified material. Refolding rHEWL with a size exclusion chromatography based process gave rise to a refolding yield of 35% that corresponded to a 20-fold dilution.     

Immobilized beta-cyclodextrin polymer coupled to agarose gel properly refolding recombinant Staphylococcus aureus elongation factor-G in combination with detergent micelle

A novel artificial chaperone system using a combination of interactions between the unfolded protein, a detergent and a chromatographic column packed with immobilized beta-cyclodextrin (beta-CD) polymer coupled to an agarose gel, was introduced to refold recombinant Staphylococcus aureus elongation factor-G (EF-G). Pre-mixing of 10% Triton X-100 and unfolded EF-G at 24 mg/ml followed by a 20-fold dilution into refolding buffer led to successful capturing of EF-G by Triton X-100 resulting in formation of a detergent-protein complex at 1.2mg/ml of final protein concentration. The complex was subsequently applied to the immobilized beta-CD polymer column resulting in correct refolding of EF-G at a concentration of 530 microg/ml with 99% mass recovery. Detergent concentrations above critical micelle concentration were required for efficient capturing of EF-G at high protein concentration. Other detergents with hydrophile-lipophile-Balance values similar to that of Triton X-100 (Triton N-101, Noindet P40 (NP40), and Berol 185) also produced similar result. Soluble polymerized beta-CD was more efficient than the monomer to remove the detergent from the protein complex in a batch system. Immobilized beta-CD polymer column further improved the capability of detergent removal and was able to prevent aggregation that occurred with the addition of soluble beta-CD polymer at high protein concentration in the batch system. The mechanism for this system-assisted refolding was tentatively interpreted: the released protein could correctly refold in an enclosed hydrophilic environment provided by the integration of matrix and beta-CD polymer, and thus avoided aggregation during detergent removal.     

Comparative study of enzyme activity and stability of bovine and human plasmins in electrophoretic reagents, beta-mercaptoethanol, DTT, SDS, Triton X-100, and urea

Effects of common electrophoretic reagents, reducing agents (beta-mercaptoethanol [BME] and DTT), denaturants (SDS and urea), and non-ionic detergent (Triton X-100), on the activity and stability of bovine plasmin (b-pln) and human plasmin (h-pln) were compared. In the presence of 0.1% SDS (w/v), all reagents completely inhibited two plns, whereas SDS (1%) and urea (1 M) denatured plns recovered their activities after removal of SDS by treatment of 2.5% Triton X-100 (v/v). However, reducing agents (0.1 M of BME and DTT) treated plns did not restore their activities. Based on a fibrin zymogram gel, five (from b-pln) and four (from h-pln) active fragments were resolved. Two plns exhibited unusual stability in concentrated SDS and Triton X-100 (final 10%) and urea (final 6 M) solutions. Two bands, heavy chain-2 (HC-2) and cleaved heavy chain-2 (CHC-2), of b-pln were completely inhibited in 0.5% SDS or 3 M urea, whereas no significant difference was found in h-pln. Interestingly, 50 kDa (cleaved heavy chain-1, CHC-1) of b-pln and two fragments, 26 kDa (light chain, LC) and 29 kDa (microplasmin, MP), of h-pln were increased by SDS in a concentration dependent manner. We also found that the inhibition of SDS against both plns was reversible.     

融合牛肠激酶轻链EKL包涵体蛋白的复性纯化

大肠杆菌高密度发酵表达肠激酶轻链融合蛋白DsbA-rEKL,主要以包涵体形式存在。包涵体经4mol/L尿素和0.5%TritonX-100洗涤,以6mol/L盐酸胍、100mmol/LDTT溶解,在胱氨酸存在下,以脉冲加样方式复性。融合蛋白复性在6mmol/L胱氨酸存在下、脉冲加量0.03mg/mL和复性终蛋白浓度0.3mg/mL为最佳复性方案。复性的融合蛋白加2mmol/LCaCL2后快速自切。经IDA-Sepharose及Q-Sepharose纯化,rEKL纯度可达95%以上,可高效酶切重组瑞特普酶融合蛋白Trx-rPA。实现了大规模生产rEKL,每升发酵液经复性及纯化后,可得rEKL60mg/L以上,使以融合蛋白表达rPA等药用蛋白成为现实。     

Computer Simulation and Additive-Based Refolding Process of Cysteine-Rich Proteins: VEGF-A as a Model

Refolding of cysteine-rich protein for establishing native conformation and a biologically active form is the most challenging step in recombinant protein synthesis. In this study, expressed vascular endothelial growth factor-A (VEGF-A), as a cysteine-rich protein, in a prokaryotic expression cell was refolded based on computer simulation technique and multiple chemical additive-based buffers to recover its biologically active form. For this purpose, cloned and expressed VEGF-A in Escherichia coli BL21 (DE3) was purified and dialyzed by a basic buffer containing nine diverse chemical additives. In parallel with the evaluations of the applied additives, professional computer simulation software was also used. The activity of refolded protein was evaluated in differentiation of mesenchymal stem cells (MSCs) to the endothelial cells (ECs). The results showed that dialyzing the produced recombinant VEGF-A in chemical additive-based buffers containing cysteine, 1, 4-dithiothreitol (DTT), arginine, and Triton X-100 led to efficient VEGF-A refolding. The results of flowcytometry analysis indicated that CD31 and CD144 as the specific ECs markers in VEGF-A treated MSCs were 31 and 73%, respectively. Protein refolding method using chemical additive-based buffers containing cysteine, DTT, arginine and Triton X-100 was the best accessible technique for refolding cysteine-rich recombinant VEGF-A.     

Tenacious binding of lipids to vimentin during its isolation and purification from Ehrlich ascites tumor cells

Vimentin enriched in cytoskeletal frameworks by Triton X-100 extraction of Ehrlich ascites tumor cells and purified from a low ionic strength extract of the cell residues by (NH4)2SO4 precipitation and DEAE-Sepharose and ssDNA-cellulose chromatography in the presence of 6 M urea was highly contaminated with lipids. Thin-layer chromatography of a chloroform-methanol extract of the purified protein revealed, besides small amounts of phospholipids, the presence of large quantities of neutral lipids.     

Chloroplast cytochrome b-6. Molecular composition as a lipoprotein.

Disc electrophoretically homogeneous spinach-chloroplast cytochrome b-6 was found to be a lipoprotein whose redox potential was essentially unchanged during isolation. These results further support the hypothesis of Triton X-100/4 M urea, pH 8, as a useful extracting medium for membrane lipoproteins. Cytochrome b-6 was found to have a heme equivalent dry weight of 1 mol of heme per 60000 g. Of this, 20000 g was lipid-extractable. The molecular weight was 60000 with a partial specific volume of 0.84 ml/g. The protein portion of the molecule (40000) consisted of 1 polypeptide chain of 20000 daltons, 1 of 9600 daltons and 2 of 6600 daltons. A simple lipid composition (relative to the original membrane) was found consisting of 7 mol of chlorophyll a and 6 mol of cardiolipin per mol of cytochrome; these two lipids thus account for about 75-80% of the lipid content. An unidentified minor neutral lipid and minor polar lipid were also detected. At pH 7.0 in the presence of 0.5% Triton X-100, E'-o was -0.080 V, and in the absence of Triton X-100, E'-o was -0.120 V. At pH 8 in 0.5% Triton X-100, E'-o was -0.084 V, thus indicating that the redox potential is independent of pH in the region 7-8. The redox reaction proceeded via a one-electron-transfer.     

Improving purification of recombinant human interferon gamma expressed in Escherichia coli; effect of removal of impurity on the process yield

Process development and optimization studies were performed in order to improve the purification process of (rhIFN-gamma). The objective was to generate material with higher purity and quantity. An in-process control screening was developed to obtain the optimal condition for column chromatographic purification by measuring LPS, nucleic acids, rhIFN- gamma, monomer and its covalent dimers. A new resin screening method was applied to select optimal resin for each of the chromatographic columns. The resulting process used Butyl and Q-Sepharose, refolding and SP-Sepharose for purification of IFN-gamma. Effects of different process conditions such as cell lysis, removal of impurity and oxygen concentration were evaluated. Removal of impurities was evaluated by washing of inclusion bodies with 1% Triton X-100 and 3M urea and different chromatography steps. The results reveal that Triton removed about 43% of the LPS but urea had no effect on removal of nucleic acids and LPS. Further analysis show that removal of impurities by column chromatography decreases aggregation and increases the process yield. Oxygen concentration was identified as parameter that could have a significant impact on covalent dimers formation, as an unacceptable pharmaceutical form of rhIFN-gamma. On the basis of small-scale studies, optimum operating conditions were chosen and the purification process was successfully scaled-up to a pilot scale process with step yield and product quality that were better than previous reports.     

Sensitivity and variability of the Bradford protein assay in the presence of detergents

The effects of Triton X-100, sodium dodecyl sulfate (SDS), and urea on the response of Coomassie blue G to 16 different proteins and peptides of Mr 1140 to 146,000 were studied to assess the significance of protein conformation and of ionic and nonionic interactions for the dye response to individual proteins. Triton X-100 at a final concentration of 0.008% (v/v) increased the sensitivity of the Bradford assay toward all proteins of Mr 5700 or higher by an average 33%. Increases ranged from +11% with myelin basic protein to +128% with aprotinin. The relative range of absorbance of proteins and deviations from bovine serum albumin decreased by approximately 25%. Triton X-100 appears to facilitate nonionic interactions of the dye with proteins of limited capacity for ionic binding. Conformation of proteins also seemed to be of some significance because the chaotropic agent urea (0.16 M final concentration) increased sensitivity of the assay by 14%. Sensitivity of the assay was lowered by SDS (0.004% final concentration, w/v) by an average 75% from that of the control assay. The results indicate that the incorporation of low concentrations of a nonionic detergent may be useful in improving sensitivity and variability of the Bradford assay.     

Mechanisms of membrane protein insertion into liposomes during reconstitution procedures involving the use of detergents. 2. Incorporation of the light-driven proton pump bacteriorhodopsin

A method has been developed for identifying the step in a detergent-mediated reconstitution procedure at which an integral membrane protein can be associated with phospholipids to give functional proteoliposomes. Large liposomes prepared by reverse-phase evaporation were treated with various amounts of the detergents Triton X-100, octyl glucoside, or sodium cholate as described in the preceding paper [Paternostre, M.-T., Roux, M., & Rigaud, J. L. (1988) Biochemistry (preceding paper in this issue)]. At each step of the solubilization process, we added bacteriorhodopsin, the light-driven proton pump from Halobacterium halobium. The protein-phospholipid detergent mixtures were then subjected to SM2 Bio-Beads treatments to remove the detergent, and the resulting vesicles were analyzed with respect to protein insertion and orientation in the membrane by freeze-fracture electron microscopy, sucrose density gradients, and proton pumping measurements. The nature of the detergent used for reconstitution proved to be important for determining the mechanism of protein insertion. With sodium cholate, proteoliposomes were formed only from ternary phospholipid-protein-detergent micelles. With octyl glucoside, besides proteoliposome formation from ternary mixed micelles, direct incorporation of bacteriorhodopsin into preformed liposomes destabilized by saturating levels of this detergent was observed and gave proteoliposomes with optimal proton pumping activity. With Triton X-100, protein insertion into destabilized liposomes was also observed but involved a transfer of the protein initially present in phospholipid-Triton X-100-protein micelles into Triton X-100 saturated liposomes. Our results further demonstrated that protein orientation in the resulting proteoliposomes was critically dependent upon the mechanism by which the protein was incorporated.     

Limited proteolysis of the pyruvate dehydrogenase multienzyme complex of Escherichia coli.

The hydrogenase from Paracoccus denitrificans, which is an intrinsic membrane protein, has been solubilised from membranes by Triton X-100. The partial specific volume of the solubilised protein has been determined using sucrose density gradient centrifugation in H2O and 2H2O. The values of the specific volumes of hydrogenase, measured in the presence or absence of Triton X-100, are 0.73 and 0.74 ml . g-1, respectively, indicating that hydrogenase binds much less than one micelle of Triton X-100. The sedimentation coefficient of hydrogenase is increased from 10.4 S to 15.9 S on removal of detergent. The Stokes' radius of hydrogenase, determined by gel filtration on Sepharose 6B, is 5.5 nm in the presence of Triton X-100 compared to 6.7 nm in the absence of detergent. The apparent molecular weight therefore increases from 242,500 to 466,000 on removal of detergent. In the presence of urea and sodium dodecylsulphate, the hydrogenase has an apparent molecular weight of 63,000. The enzyme therefore behaves as a non-covalently linked tetramer in the presence of Triton X-100. Removal of Triton X-100 results in association of tetramers to form octamers.     

Immobilized Triton X-100-assisted refolding of Green Fluorescent Protein-Tobacco Etch Virus protease fusion protein using β-cyclodextrin as the eluent

A new protein refolding technique based on the use of the non-charged detergent Triton X-100 immobilized to the cross-linked agarose gel Sepharose High Performance has been developed. The new solid phase was used in combination with soluble β-cyclodextrin (β-CD) to refold recombinant Green Fluorescent Protein fused to Tobacco Etch Virus protease (GFPTEVP) expressed as inclusion bodies in E. coli. Previous attempts to refold recombinant GFPTEVP by dilution had failed. In the new procedure a column packed with Triton X-100-coupled Sepharose High Performance was used to capture unfolded GFPTEVP followed by elution using an increasing β-CD concentration gradient. The yield of properly refolded GFPTEVP was 46% at a protein concentration of 380 μg/ml. In contrast, dilution refolding of GFPTEVP at 200 μg/ml refolding buffer resulted in only 4.7% of native protein.     

Renaturation of cobra venom phospholipase A2 expressed from a synthetic gene in Escherichia coli.

Cobra venom (Naja naja naja) phospholipase A2 (PLA2) contains 14 cysteines in the form of 7 disulfide bonds amongst its 119 amino acids. A gene encoding the PLA2 was synthesized and inserted into a bacterial expression vector containing the phage lambda pL promoter. In order to obtain protein without the initiating methionine at the N-terminus, a Factor Xa site was engineered upstream from the PLA2 gene. Upon heat-induction of the cells transformed with the expression plasmid, the protein is produced as insoluble inclusion bodies. The enzyme was partially purified by washing the inclusion bodies with Triton X-100 and urea. The expressed protein was first denatured with 8 M guanidine-HCl and 10 mM DTT. After digestion with Factor Xa, formation of disulfide bonds and refolding into the fully active form was carried out in the presence of cysteine and Ca2+. The renatured recombinant protein was purified by Affi-gel blue column chromatography. The purified recombinant enzyme had the same specific activity as the native enzyme when assayed on a variety of substrates and cross-reacted with antisera prepared against the native enzyme. This is the first report of the expression of a recombinant PLA2 from any venom.     

A cytoskeleton-associated plasma membrane heparan sulfate proteoglycan in Schwann cells

Schwann cells cocultured with sensory neurons in a serum-free medium accumulate a single species of radiolabeled heparan sulfate proteoglycan (HS-PG) during incubation in medium containing 35SO4. This HS-PG was poorly extracted from cultures by solutions containing 1% Triton X-100 in low salt buffer or by solutions containing 1 M KCl, 4 M urea plus dithiothreitol, 1 mM Tris-HCl, 5 mM EDTA, or 100 micrograms/ml of heparin. The HS-PG was efficiently extracted, however, by 1% Triton X-100 in the presence of 1 M KCl or by 1% deoxycholate. These treatments solubilize both cell membranes and the Schwann cell cytoskeleton. In intact cells the HS-PG was digested by trypsin, indicating it was at least partially exposed on the cell surface. When solubilized HS-PG was applied to a column of octyl-sepharose CL-4B, more than 90% was retained by the column, but was quantitatively eluted by a solution containing 1% Triton X-100. In addition, the solubilized HS-PG could be incorporated into artificial phospholipid vesicles. These results indicate the HS-PG is an integral plasma membrane protein. The inability of low ionic strength solutions containing Triton X-100 to solubilize the HS-PG suggested it was bound to an additional structure. To determine whether the HS-PG was associated with the cytoskeleton we isolated cytoskeletons by detergent lysis of cells and centrifugation. The major protein components of isolated cytoskeletons were spectrin (Mr 225,000), vimentin (Mr 58,000), and actin (Mr 45,000). When 35SO4-labeled cells were used to prepare cytoskeletons approximately 80% of the total HS-PG was recovered in the cytoskeleton fraction. These results suggest the HS-PG is an externally exposed integral plasma membrane protein that is anchored to the Schwann cell cytoskeleton.