Identification of yeast and bacteria involved in the mezcal fermentation of Agave salmiana.

AIMS: To identify the yeast and bacteria present in the mezcal fermentation from Agave salmiana. METHODS AND RESULTS: The restriction and sequence analysis of the amplified region, between 18S and 28S rDNA and 16S rDNA genes, were used for the identification of yeast and bacteria, respectively. Eleven different micro-organisms were identified in the mezcal fermentation. Three of them were the following yeast: Clavispora lusitaniae, Pichia fermentans and Kluyveromyces marxianus. The bacteria found were Zymomonas mobilis subsp. mobilis and Zymomonas mobilis subsp. pomaceae, Weissella cibaria, Weissella paramesenteroides, Lactobacillus pontis, Lactobacillus kefiri, Lactobacillus plantarum and Lactobacillus farraginis. CONCLUSIONS: The phylogenetic analysis of 16S rDNA and ITS sequences showed that microbial diversity present in mezcal is dominated by bacteria, mainly lactic acid bacteria species and Zymomonas mobilis. Pichia fermentans and K. marxianus could be micro-organisms with high potential for the production of some volatile compounds in mezcal. SIGNIFICANCE AND IMPACT OF THE STUDY: We identified the community of bacteria and yeast present in mezcal fermentation from Agave salmiana.

Evidence for the presence of an alternative glucose transport system in Clostridium beijerinckii NCIMB 8052 and the solvent-hyperproducing mutant BA101.

The effects of substrate analogs and energy inhibitors on glucose uptake and phosphorylation by Clostridium beijerinckii provide evidence for the operation of two uptake systems: a previously characterized phosphoenolpyruvate-dependent phosphotransferase system (PTS) and a non-PTS system probably energized by the transmembrane proton gradient. In both wild-type C. beijerinckii NCIMB 8052 and the butanol-hyperproducing mutant BA101, PTS activity declined at the end of exponential growth, while glucokinase activity increased in the later stages of fermentation. The non-PTS uptake system, together with enhanced glucokinase activity, may provide an explanation for the ability of the mutant to utilize glucose more effectively during fermentation despite the fact that it is partially defective in PTS activity.

Continuous butanol fermentation and feed starch retrogradation: butanol fermentation sustainability using Clostridium beijerinckii BA101.

Use of starch solution as feed for butanol bioconversion processes employing Clostridium beijerinckii BA101 may have added economic advantage over the use of glucose. Acetone butanol ethanol (ABE) was produced from 30 gL(-1) starch solution using a continuous process. The bioreactor was fed at a dilution rate of 0.02 h(-1) and starch solution/feed volume (3 L) was replaced every 72 h. The continuous reactor fed with cornstarch solution (feed temperature 19 degrees C) produced approximately 6.0 gL(-1) total ABE. Increasing the feed storage temperature to 37 degrees C improved ABE production to 7.2 gL(-1) suggesting that retrogradation was occurring more rapidly at 19 degrees C. In both these cases the fermentation drifted toward acid production after approximately 260 h, consistent with the retrogradation of starch overtime. The use of soluble starch, which is less prone to retrogradation, resulted in the production of 9.9 gL(-1) ABE at 37 degrees C feed storage temperature, as compared to 7.2 gL(-1) ABE when cornstarch was used. It should be noted that gelatinized starch retrogradation takes place after sterilization and prior to use of the feed medium, and does not occur during long-term storage of the raw corn material in the months leading up to processing. The degree of hydrolysis of gelatinized starch decreased from 68.8 to 56.2% in 3 days when stored at 37 degrees C. Soluble starch which does not retrograde demonstrated no change in the degree of hydrolysis.

Acetone butanol ethanol (ABE) production from concentrated substrate: reduction in substrate inhibition by fed-batch technique and product inhibition by gas stripping.

Acetone butanol ethanol (ABE) was produced in an integrated fed-batch fermentation-gas stripping product-recovery system using Clostridium beijerinckii BA101, with H(2) and CO(2) as the carrier gases. This technique was applied in order to eliminate the substrate and product inhibition that normally restricts ABE production and sugar utilization to less than 20 g l(-1) and 60 g l(-1), respectively. In the integrated fed-batch fermentation and product recovery system, solvent productivities were improved to 400% of the control batch fermentation productivities. In a control batch reactor, the culture used 45.4 g glucose l(-1) and produced 17.6 g total solvents l(-1) (yield 0.39 g g(-1), productivity 0.29 g l(-1) h(-1)). Using the integrated fermentation-gas stripping product-recovery system with CO(2) and H(2) as carrier gases, we carried out fed-batch fermentation experiments and measured various characteristics of the fermentation, including ABE production, selectivity, yield and productivity. The fed-batch reactor was operated for 201 h. At the end of the fermentation, an unusually high concentration of total acids (8.5 g l(-1)) was observed. A total of 500 g glucose was used to produce 232.8 g solvents (77.7 g acetone, 151.7 g butanol, 3.4 g ethanol) in 1 l culture broth. The average solvent yield and productivity were 0.47 g g(-1) and 1.16 g l(-1) h(-1), respectively.

Production of butanol from starch-based waste packing peanuts and agricultural waste.

We examined the fermentation of starch-based packing peanuts and agricultural wastes as a source of fermentable carbohydrates using Clostridium beijerinckii BA101. Using semidefined P2 medium containing packing peanuts and agricultural wastes, instead of glucose as a carbohydrate source, we measured characteristics of the fermentation including solvent production, productivity, and yield. With starch as substrate (control), the culture produced 24.7 g l(-1) acetone-butanol-ethanol (ABE), while with packing peanuts it produced 21.7 g l(-1) total ABE with a productivity of 0.20 g l(-1) h(-1) and a solvent (ABE) yield of 0.37. Cell growth in starch, packing peanuts, and agricultural wastes medium was different, possibly due to the different nature of these substrates. Using model agricultural waste, 20.3g l(-1) ABE was produced; when using actual waste, 14.8 g l(-1) ABE was produced. The use of inexpensive substrates will increase the economic viability of the conversion of biomass to butanol, and can provide new markets for these waste streams.

Molecular characterization and utilization of the CAK1 filamentous viruslike particle derived from Clostridium beijerinckii.

An examination of the replication origin and stability determinant associated with the CAK1 filamentous viruslike particle recovered from Clostridium beijerinckii NCIMB 6444 was carried out. Seven deletion derivatives, pCKE, pCEP1, pDT5, pCKP, pDTH102, pYL102E and pYL102, were constructed and transformed into C. beijerinckii NCIMB 8052. The successful transformation of pCKE, pDT5, pCKP, pDTH102, pYL102E and pYL102 into C. beijerinckii 8052, together with the corresponding recovery of single-stranded DNA from Escherichia coli indicated that the double- and single-stranded replication origins are located on a 0.4-kb CAK1 DNA fragment. Sequence analysis of the putative 0.4-kb replication origin region of CAK1 reveals a nick site containing 22 base pairs that has homology with plasmids pC194 and pUB110 and suggests the presence of a 2.0-kb DNA region involved in stability. The putative Rep protein of CAK1 contains three conserved motifs and three essential residues of the catalytic site in agreement with Rep proteins associated with the pC194 family. The utility of the developed CAK1-derived phagemid designated pYL102E was evaluated by using it to examine heterologous expression of: (1) the manA gene derived from Thermoanaerobacterium polysaccharolyticum in E. coli and C. beijerinckii NCIMB 8052 and (2) the sol operon derived from Clostridium acetobutylicum DSM 792 in C. beijerinckii SA-2.

Glucose uptake in Clostridium beijerinckii NCIMB 8052 and the solvent-hyperproducing mutant BA101.

Glucose uptake and accumulation by Clostridium beijerinckii BA101, a butanol hyperproducing mutant, were examined during various stages of growth. Glucose uptake in C. beijerinckii BA101 was repressed 20% by 2-deoxyglucose and 25% by mannose, while glucose uptake in C. beijerinckii 8052 was repressed 52 and 28% by these sugars, respectively. We confirmed the presence of a phosphoenolpyruvate (PEP)-dependent phosphotransferase system (PTS) associated with cell extracts of C. beijerinckii BA101 by glucose phosphorylation by PEP. The PTS activity associated with C. beijerinckii BA101 was 50% of that observed for C. beijerinckii 8052. C. beijerinckii BA101 also demonstrated lower PTS activity for fructose and glucitol. Glucose phosphorylation by cell extracts derived from both C. beijerinckii BA101 and 8052 was also dependent on the presence of ATP, a finding consistent with the presence of glucokinase activity in C. beijerinckii extracts. ATP-dependent glucose phosphorylation was predominant during the solventogenic stage, when PEP-dependent glucose phosphorylation was dramatically repressed. A nearly twofold-greater ATP-dependent phosphorylation rate was observed for solventogenic stage C. beijerinckii BA101 than for solventogenic stage C. beijerinckii 8052. These results suggest that C. beijerinckii BA101 is defective in PTS activity and that C. beijerinckii BA101 compensates for this defect with enhanced glucokinase activity, resulting in an ability to transport and utilize glucose during the solventogenic stage.

Soy molasses as fermentation substrate for production of butanol using Clostridium beijerinckii BA101.

Spray-dried soy molasses (SDSM) contains the sugars dextrose, sucrose, fructose, pinitol, raffinose, verbascose, melibiose, and stachyose. Of the 746 g kg(-1) total sugars in SDSM, 434 g kg(-1) is fermentable using Clostridium beijerinckii BA101. SDSM was used to produce acetone, butanol, and ethanol (ABE) by C. beijerinckii BA101 in batch cultures. Using 80 g l(-1) SDSM, 10.7 g l(-1) ABE was produced in P2 medium. Higher concentrations of SDSM resulted in poor solvent production due to the presence of excessive salt and inhibitory components. C. beijerinckii BA101 in SDSM at 80 g l(-1) concentration produced 22.8 g l(-1) ABE when supplemented with 25.3 g l(-1) glucose. SDSM contains 57.4 g kg(-1) mineral ash and 2% tri-calcium phosphate. Tri-calcium phosphate up to 43.1 g l(-1) was not inhibitory and at a tri-calcium phosphate concentration of 28.8 g l(-1), the culture produced more solvents (30.1 g l(-1)) than the control experiment (23.8 g l(-1)). In contrast, sodium chloride was a strong inhibitor of C. beijerinckii BA101 cell growth. At a concentration of 10 g l(-1) sodium chloride, a maximum cell concentration of 0.6 g l(-1) was achieved compared to 1.7 g l(-1) in the control experiment. The effects of two salts on specific growth rate constant (mu) and specific rate of ABE production (nu) for C. beijerinckii BA101 were examined.

Recent advances in ABE fermentation: hyper-butanol producing Clostridium beijerinckii BA101.

This is an overview of the mutant strain Clostridium beijerinckii BA101 which produces solvents (acetone-butanol-ethanol, ABE) at elevated levels. This organism expresses high levels of amylases when grown on starch. C. beijerinckii BA101 hydrolyzes starch effectively and produces solvent in the concentration range of 27-29 g x l(-1). C. beijerinckii BA101 has been characterized for both substrate and butanol inhibition. Supplementing the fermentation medium (MP2) with sodium acetate enhances solvent production to 33 g x l(-1). The results of studies utilizing commercial fermentation medium and pilot plant-scale reactors are consistent with the results using small-scale reactors. Pervaporation, a technique to recover solvents, has been applied to fed-batch reactors containing C. beijerinckii BA101, and solvent production as high as 165 g x l(-1) has been achieved. Immobilization of C. beijerinckii BA101 by adsorption and use in a continuous reactor resulted in reactor productivity of 15.8 g x l(-1) x h(-1). Recent economic studies employing C. beijerinckii BA101 suggested that butanol can be produced at US$0.20-0.25 x lb(-1) by employing batch fermentation and distillative recovery. Application of new technologies such as pervaporation, fed-batch culture, and immobilized cell reactors is expected to further reduce these prices.

ABE production from corn: a recent economic evaluation.

This article details an economic assessment of butanol production from corn using the newly developed hyper-butanol-producing strain of Clostridium beijerinckii BA101. Butanol is produced in batch reactors and recovered by distillation. For a plant with 153,000 metric tons of acetone, butanol, and ethanol (ABE) production capacity, the production equipment cost and total working capital cost is US$33.47x10(6) and US$110.46x10(6), respectively. Based on a corn price (C(p)) of US$79.23 x ton(-1) (US$2.01 x bushel(-1)), an ABE yield of 0.42 (g ABE/g glucose) butanol price is projected to be US$0.34 x kg(-1). An improved yield of 0.50 will reduce this price to US$0.29 x kg(-1). Assumptions, such as by-product credit for gases and complete conversion of corn steep liquor (CSL) to fermentation by-products, have been taken into consideration. An increased price of corn to US$197.10 x ton(-1) would result in a butanol price of US$0.47 x kg(-1). A grass-rooted plant would result in a butanol price of US$0.73 x kg(-1) (C(p) US$79.23 x ton(-1)). In a worst case scenario, the price of butanol would increase to US$1.07 x kg(-1) (C(p) 197.10 x ton(-1) for a grass-rooted plant and assuming no credit for gases). This is based on the assumption that corn price would not increase to more than US$197.10 x ton(-1).

Butanol production using Clostridium beijerinckii BA101 hyper-butanol producing mutant strain and recovery by pervaporation.

Clostridium beijerinckii BA101 (mutant strain) and C. beijerinckii 8052 (wild type) were compared for substrate and butanol inhibition. The wild-type strain is more strongly inhibited by added butanol than is the mutant strain. Acetone and butanol were removed from a fed-batch reactor inoculated with C. beijerinckii BA101 by pervaporation using a silicone membrane. In the batch reactor, C. beijerinckii BA101 produced 25.3 g/L of total solvents, whereas in the fermentation-recovery experiment it produced 165.1 g/L of total solvents. Solvent productivity increased from 0.35 (batch reactor) to 0.98 g/L.h (fed-batch reactor). The fed-batch reactor was fed with 500 g/L of glucose-based P2 medium. Acetone selectivities ranged from 2 to 10 whereas butanol selectivities ranged from 7 to 19. Total flux varied from 26 to 31 g/m2.h.

Production of acetone butanol ethanol (ABE) by a hyper-producing mutant strain of Clostridium beijerinckii BA101 and recovery by pervaporation.

A silicone membrane was used to study butanol separation from model butanol solutions and fermentation broth. Depending upon the butanol feed concentration in the model solution and pervaporation conditions, butanol selectivities of 20.88-68.32 and flux values of 158.7-215.4 g m(-)(2) h(-)(1) were achieved. Higher flux values (400 g m(-)(2) h(-)(1)) were obtained at higher butanol concentrations using air as sweep gas. In an integrated process of butanol fermentation-recovery, solvent productivities were improved to 200% of the control batch fermentation productivities. In a batch reactor the hyper-butanol-producing mutant strain C. beijerinckii BA101 utilized 57.3 g/L glucose and produced 24.2 g/L total solvents, while in the integrated process it produced 51.5 g/L (culture volume) total solvents. Concentrated glucose medium was also fermented. The C. beijerinckii BA101 mutant strain was not negatively affected by the pervaporative conditions. In the integrated experiment, acids were not produced. With the active fermentation broth, butanol selectivity was reduced by a factor of 2-3. However, the membrane flux was not affected by the active fermentation broth. The butanol permeate concentration ranged from 26.4 to 95.4 g/L, depending upon butanol concentration in the fermentation broth. Since the permeate of most membranes contains acetone, butanol, and ethanol (and small concentrations of acids), it is suggested that distillation be used for further purification.

Effect of acetate on molecular and physiological aspects of Clostridium beijerinckii NCIMB 8052 solvent production and strain degeneration.

The addition of sodium acetate to chemically defined MP2 medium was found to increase and stabilize solvent production and also increase glucose utilization by Clostridium beijerinckii NCIMB 8052. RNA and enzyme analyses indicated that coenzyme A (CoA) transferase was highly expressed and has higher activity in C. beijerinckii NCIMB 8052 grown in MP2 medium containing added sodium acetate than in the microorganism grown without sodium acetate. RNA analysis suggested the existence of a sol operon and confirmed the presence of a ptb-buk operon in C. beijerinckii NCIMB 8052. In addition to CoA transferase, C. beijerinckii NCIMB 8052 grown in MP2 medium containing added acetate demonstrated higher acetate kinase- and butyrate kinase-specific activity than when the culture was grown in MP2 medium containing no added acetate. Southern blot analysis with chromosomal DNA isolated from solventogenic and degenerated C. beijerinckii NCIMB 8052 indicated that C. beijerinckii NCIMB 8052 strain degeneration does not involve loss of the CoA transferase genes. The addition of acetate to MP2 medium may induce the expression of the sol operon, which ensures solvent production and prevents strain degeneration in C. beijerinckii NCIMB 8052.

Enhanced Butanol Production by Clostridium beijerinckii BA101 Grown in Semidefined P2 Medium Containing 6 Percent Maltodextrin or Glucose.

Dramatically elevated levels of butanol and acetone resulted in higher butanol and total solvent yields for hyperamylolytic Clostridium beijerinckii BA101 relative to the NCIMB 8052 parent strain grown in semidefined P2 medium containing either 6% glucose or STAR-DRI 5 maltodextrin. C. beijerinckii BA101 consistently produced on the order of 19 g of butanol per liter in 20-liter batch fermentations. This represents a greater than 100% increase in butanol concentration by the BA101 strain compared to the parent NCIMB 8052 strain. The kinetics of butanol production over time also indicate a more rapid rate of butanol production by BA101 in semidefined P2 medium containing glucose or maltodextrin. The lower levels of butyric and acetic acids produced over the course of the fermentation carried out by BA101 are consistent with an enhanced capacity for uptake and recycling of these acids. C. beijerinckii BA101 appears to more completely utilize carbohydrate compared to the 8052 strain. Carbon balance following fermentation by C. beijerinckii 8052 and BA101 indicates that sufficient carbon is available for the twofold increase in butanol concentration observed during BA101 fermentations. C. beijerinckii BA101 also has superior solvent production capacity during continuous culture fermentation in P2 medium containing 6% glucose. Volumetric solvent yields of 0.78 and 1.74 g/liter/h for BA101 and 0.34 and 1.17 g/liter/h for NCIMB 8052 were obtained at dilution rates of 0.05 and 0.20 h(sup-1), respectively. No drift towards acid synthesis (strain degeneration) was observed for up to 200 h (d = 0.05 h(sup-1)) and 100 h (d = 0.20 h(sup-1)).

Factors involved in the transformation of previously non-transformable Clostridium perfringens type B.

The pre-shock incubation of cells plus DNA and the methylation state of plasmid DNA were found to play a role in the electroporation-based transformation of Clostridium perfringens 3626B. Following pre-shock incubation, the highest number of C. perfringens 3626B transformants was obtained when plasmid pGK201 was both dam+ dcm+ modified, while no transformants were obtained when pGK201 was not methylated or only dcm methylated. This is consistent with the observation that plasmid pGK201 was protected against digestion by C. perfringens 3626B cell-associated nucleases for up to 3 min when methylated by both methylases. C. perfringens 3626B was successfully transformed only within a narrow cell recovery rate window. The ermAM gene associated with pGK201 and pAK102 was found to integrate into the chromosome of C. perfringens strain 13A and 3626B.

Transcriptional analysis of the Clostridium cellulovorans endoglucanase gene, engB.

An endoglucanase gene, which was shown to be identical to the previously sequenced engB gene [Attwood et al. (1993) Abstr. Ann. Meet. Am. Soc. Microbiol.], was isolated from a Clostridium cellulovorans genomic library. Because of the lack of transcriptional information concerning engB we examined its expression in C. cellulovorans and in the heterologous hosts Escherichia coli and C. acetobutylicum following transformation of engB. Northern analysis suggested that both E. coli and C. acetobutylicum produced several transcripts of various sizes. C. cellulovarans produced a single transcript of 1600 bp with the relative amount of engB mRNA from cellulose-grown cells being much greater than that from cellobiose-grown cells. Primer extensions showed that engB was transcribed from a single transcription initiation site in C. cellulovorans preceded by sequences similar to promoter sequences found in Gram-positive bacteria. Primer extensions from both E. coli and C. acetobutylicum strains containing the engB gene showed multiple transcription initiation sites, none of which corresponded to the site determined in C. cellulovorans. We conclude that transcriptional control of the engB gene is less stringent in heterologous backgrounds and postulate that expression of the engB gene in C. cellulovorans is increased in the presence of cellulose.

Heterologous expression of endo-beta-1,4-D-glucanase from Clostridium cellulovorans in Clostridium acetobutylicum ATCC 824 following transformation of the engB gene.

Heterologous expression of the Clostridium cellulovorans engB gene by Clostridium acetobutylicum BKW-1 was detected as zones of hydrolysis on carboxymethyl cellulose (CMC) Trypticase glucose yeast plates stained with Congo red. The extracellular cellulase preparation from C. acetobutylicum BKW-1 has a specific activity towards CMC which is more than fourfold that present in C. acetobutylicum ATCC 824. Western blot (immunoblot) analysis using the C. cellulovorans anti-EngB primary antibody demonstrated that an additional 44-kDa protein band was present in the supernatant derived from C. acetobutylicum BKW-1 but was not present in ATCC 824 or ATCC 824(pMTL500E).

Construction and characterization of a phage-plasmid hybrid (phagemid), pCAK1, containing the replicative form of viruslike particle CAK1 isolated from Clostridium acetobutylicum NCIB 6444.

A bacteriophage-plasmid hybrid (phagemid) designated pCAK1 was constructed by ligating 5-kbp Escherichia coli plasmid pAK102 (AprEmr) and the 6.6-kbp HaeIII-linearized replicative form of the CAK1 viruslike particle from Clostridium acetobutylicum NCIB 6444. Phagemid pCAK1 (11.6 kbp) replicated via the ColE1 replication origin derived from pAK102 in E. coli. Single-stranded DNA (ssDNA) molecules complexed with protein in a manner which protected ssDNA from nucleases were recovered from the supernatant of E. coli DH11S transformants containing pCAK1 in the absence of cell lysis. This suggests that the viral-strand DNA synthesis replication origin of CAK1 and associated gene expression are functional in E. coli DH11S. The single-stranded form of pCAK1 isolated from E. coli supernatant was transformed into E. coli DH5 alpha' or DH11S by electroporation. Isolation of ampicillin-resistant E. coli transformants following transformation suggests that the complementary-strand DNA synthesis replication origin of CAK1 is also functional in E. coli. The coat proteins associated with ssDNA of pCAK1 demonstrated sensitivity to proteinase K and various solvents (i.e., phenol and chloroform), similar to the results obtained previously with CAK1. Following phagemid construction in E. coli, pCAK1 was transformed into C. acetobutylicum ATCC 824 and C. perfringens 13 by intact cell electroporation. Restriction enzyme analysis of pCAK1 isolated from erythromycin-resistant transformants of both C. acetobutylicum and C. perfringens suggested that it was identical to that present in E. coli transformants.

Isolation and characterization of Clostridium acetobutylicum mutants with enhanced amylolytic activity.

Clostridium acetobutylicum mutants BA 101 (hyperamylolytic) and BA 105 (catabolite depressed) were isolated by using N-methyl-N'-nitro-N-nitrosoguanidine together with selective enrichment on the glucose analog 2-deoxyglucose. Amylolytic enzyme production by C. acetobutylicum BA 101 was 1.8- and 2.5-fold higher than that of the ATCC 824 strain grown in starch and glucose, respectively. C. acetobutylicum BA 105 produced 6.5-fold more amylolytic activity on glucose relative to that of the wild-type strain. The addition of glucose at time zero to starch-based P2 medium reduced the total amylolytic activities of C. acetobutylicum BA 101 and BA 105 by 82 and 25%, respectively, as compared with the activities of the same strains grown on starch alone. Localization studies demonstrated that the amylolytic activities of C. acetobutylicum BA 101 and BA 105 were primarily extracellular on all carbohydrates tested.

Isolation and characterization of a filamentous viruslike particle from Clostridium acetobutylicum NCIB 6444.

A single-stranded 6.6-kb DNA molecule complexed with protein was recovered from the supernatant of Clostridium acetobutylicum NCIB 6444. Electron microscopic examination of the DNA-protein complex revealed the presence of a filamentous viruslike particle, which was designated CAK1. The possible double-stranded plasmidlike replicative form and the single-stranded prophage were also recovered from the cell culture following alkaline lysis. CAK1 was released from the C. acetobutylicum cell culture in the absence of cell lysis. Polyethylene glycol-NaCl coprecipitation of the DNA-protein complex revealed the presence of single-stranded DNA complexed with protein in a manner rendering the DNA resistant to Bal 31 exonuclease. Proteinase treatment of CsCl density gradient-purified CAK1 resulted in recovery of DNase-sensitive single-stranded DNA. Tricine-sodium dodecyl sulfate-polyacrylamide gel electrophoresis of CAK1 demonstrated the presence of a 5-kDa major coat protein. Hybridization data indicated that the single-stranded DNA from CAK1 has homology with the M13 phage of Escherichia coli. An examination of various physical properties of CAK1 suggests that it is similar to the filamentous phage recovered from gram-negative microorganisms. Although infectivity or inducibility of CAK1 could not be demonstrated, to our knowledge this represents the first report of a nonlytic filamentous viruslike particle containing single-stranded DNA being recovered from a gram-positive bacterium.