US 5,322,841 AGrant

Method for Producing Neutral Glucans for Pharmaceutical Applications

Issue Date:1994-06-21

•28 Claims

•2 Drawing Sheets

Abstract

A method for producing soluble preparations of neutral glucan polymers is disclosed. The method involves treating whole glucan particles with a unique sequence or acid and alkaline treatments to produce soluble glucan. The soluble glucan can be purified to obtain a physiologically acceptable solution of neutral glucan molecules. A soluble neutral glucan preparation is obtained which forms a clear solution at a neutral pH and is equilibrated in a pharmaceutically acceptable carrier.

Metadata

Assignee

Alpha-Beta Technology, Inc.

Inventors

Spiros Jamas
D. Davidson Easson, Jr.
Gary R. Ostroff

Application Information

Application Number:US 9705473

Filing Date:1992-11-02

Priority Date:1989-09-08

Art Unit:181

Classifications

IPC:

A61K 31715

Field of Search:

435514536101;255;256;942541.1;114;121;123;124

Patent Drawings (2 sheets)

Description

BACKGROUND

Glucans are generally described as polymers of glucose and are derived from yeast, bacteria, fungi and plants. Glucans containing a .beta.(1-3)-linked glucopyranose backbone have long been known to have biological activity, specifically they have been shown to activate the immune system.

Neutral .beta.(1-3) glucan polymers are limited in their utility in parenteral pharmaceutical applications, however, because they are not readily soluble in physiological media. DiLuzio, U.S. Pat. No. 4,739,046 and Williams et al., U.S. Pat. No. 4,761,402. The primary reason for the inherent insolubility of .beta.(1-3) glucans is their tendency to form tightly associated triple-helical fibrils which resist hydration. For this reason, attempts to develop soluble .beta.(1-3) glucans depend on chemical substitution with charged groups, such as phosphate (U.S. Pat. Nos. 4,739,046; 4,761,402), amine (U.S. Pat. No. 4,707,471) or other functional groups (e.g., sulphate) which change the native conformation of the glucan molecules and may affect their biological and pharmacokinetic properties.

SUMMARY OF THE INVENTION

The present invention relates to a method for producing soluble glucan (also referred to as PGG) preparations. In the present method, insoluble glucans are processed through a unique sequence of acid and alkaline treatments to produce soluble glucan. The soluble glucan is then purified at an alkaline pH and below a critical concentration, to obtain a soluble glucan preparation appropriate for parenteral (e.g., intravenous, intraperitoneal, subcutaneous, intramuscular), topic, oral or intranasal administration to humans and animals. Soluble glucan produced by the present method can be maintained in a clear solution when neutralized to pH 7 and equilibrated in a pharmaceutically acceptable carrier. Glucan produced by the present method is a safe, potent immune system enhancer when administered to an individual. Safe and efficacious preparations of soluble glucan polymers of the present invention can be used in therapeutic and/or prophylactic treatment regimens of humans and animals to enhance their immune response.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1 is a graph showing the dose-dependent inhibitory effect on monocyte injestion of Zymosan by soluble, modified glucan derived from S. cerevisiae R4 compared to yeast extract (YE) glucan

FIG. 2 is a graph showing the change in peripheral total and differential white blood cell (WBC) counts in mice after a single, intravenous dose of PGG (5 mg/mouse).

FIG. 3 is a graph showing peripheral total and differential white blood cell (WBC) counts in mice after multiple dose subcutaneous administration of PGG (5 mg/mouse/day.times.4 days).

FIG. 4 is a graph showing the efficacy of the PGG glucans in an E. coli sepsis model in mice.

DETAILED DESCRIPTION OF INVENTION

The soluble glucan preparations of this invention are prepared from insoluble glucan particles. Soluble glucan is also referred to herein as PGG (poly-(1-6)-.beta.-D-glucopyranosyl-(1-3)-.beta.-D-glucopyranose). Preferably, insoluble glucans derived from yeast organisms are employed. Manners et al., Biol. J., 135:19-30, (1973). Glucan particles which are particularly useful as starting materials in the present invention are whole glucan particles described by Jamas et al., in U.S. Pat. Nos. 4,810,646, 4,992,540, 5,082,936 and 5,028,703, the teaching of all are hereby incorporated herein by reference. The source of the whole glucan particles can be the broad spectrum of glucan-containing fungal organisms which contain .beta.-glucans in their cell walls. Whole glucan particles obtained from the strain Saccharomyces cerevisiae R4 (NRRL Y-15903) described by Jamas et al. in U.S. Pat. No. 5,028,703 are particularly useful. the structurally modified glucans hereinafter referred to as "modified glucans" derived from S. cerevisiae R4 are potent immune system activators, as described in Jamas et al. in co-pending U.S. application Ser. No. 07/404,765, filed concurrently herewith, the teachings of which are hereby incorporated herein by reference.

The whole glucan particles utilized in this present invention can be in the form of a dried powder, as described by Jamas et al., in U.S. Pat. Nos. 4,810,646, 4,992,540, 5,082,936 and 5,028,703. For the purpose of this present invention it is not necessary to conduct the final organic extraction and wash steps described by Jamas et al.

In the present process, whole glucan particles are suspended in an acid solution under conditions sufficient to dissolve the acid-soluble glucan portion. For most glucans, an acid solution having a pH of from about 1 to about 5 and a temperature of from about 20.degree. to about 100.degree. C. is sufficient. Preferably, the acid used is an organic acid capable of dissolving the acid-soluble glucan portion. Acetic acid, at concentrations of from about 0.1 to about 5M or formic acid at concentrations of from about 50% to 98% (w/v) are useful for this purpose. The treatment is preferably carried out at about 90.degree. C. The treatment time may vary from about 1 hour to about 20 hours depending on the acid concentration, temperature and source of whole glucan particles. For example, modified glucans having more .beta.(1-6) branching than naturally-occurring, or wild-type glucans, require more stringent conditions, i.e., longer exposure times and higher temperatures. This acid-treatment step can be repeated under similar or variable conditions. In one embodiment of the present method, modified whole glucan particles from the strain, S. cerevisiae R4, which have a higher level of .beta.(1-6) branching than naturally-occuring glucans, are used, and treatment is carried out twice: first with 0.5M acetic acid at 90.degree. C. for 3 hours and second with 0.5M acetic acid at 90.degree. C. for 20 hours.

The acid-insoluble glucan particles are then separated from the solution by an appropriate separation technique, for example, by centrifugation or filtration. The pH of the resulting slurry is adjusted with an alkaline compound such as sodium hydroxide, to a pH of about 7 to about 14. The slurry is then resuspended in hot alkali having a concentration and temperature sufficient to solubilize the glucan polymers. Alkaline compounds which can be used in this step include alkali-metal or alkali-earth metal hydroxides, such as sodium hydroxide or potassium hydroxide, having a concentration of from about 0.1 to about 10N. This step can be conducted at a temperature of from about 4.degree. C. to about 121.degree. C., preferably from about 20.degree. C. to about 100.degree. C. In one embodiment of the process, the conditions utilized are a 1N solution of sodium hydroxide at a temperature of about 80.degree.-100.degree. C. and a contact time of approximately 1-2 hours. The resulting mixture contains solubilized glucan molecules and particulate glucan residue and generally has a dark brown color due to oxidation of contaminating proteins and sugars. The particulate residue is removed from the mixture by an appropriate separation technique, e.g., centrifugation and/or filtration.

The resulting solution contains soluble glucan molecules. This solution can, optionally, be concentrated to effect a 5 to 10 fold concentration of the retentate soluble glucan fraction to obtain a soluble glucan concentration in the range of about 1 to 5 mg/ml. This step can be carried out by an appropriate concentration technique, for example, by ultrafiltration, utilizing membranes with nominal molecular weight levels (NMWL) or cut-offs in the range of about 1,000 to 100,000 daltons. A membrane cut-off of about 10,000 daltons is particularly useful for this step.

The concentrated fraction obtained after this step is enriched in the soluble, biologically active glucan PGG. To obtain a pharmacologically acceptable solution, the glucan concentrate is further purified, for example, by diafiltration. In one embodiment of the present method, diafiltration is carried out using approximately 10 volumes of alkali in the range of about 0.2 to 0.4N. The preferred concentration of the soluble glucan after this step is from about 2 to about 5 mg/ml. The pH of the solution is adjusted in the range of about 7-9 with an acid, such as hydrochloric acid. Traces of proteinaceous material which may be present can be removed by contacting the resulting solution with a positively charged medium such as DEAE-cellulose, QAE-cellulose or Q-Sepharose. Proteinaceous material is detrimental to the quality of the glucan product, may produce a discoloration of the solution and aids in the formation of gel networks, thus limiting the solubility of the neutral glucan polymers. A clear solution is obtained after this step.

The highly purified, clear glucan solution can be further purified, for example, by diafiltration, using a pharmaceutically acceptable medium (e.g., sterile water for injection, phosphate-buffered saline (PBS), isotonic saline, dextrose) suitable for parenteral administration. The preferred membrane for this diafiltration step has a nominal molecular weight cut-off of about 10,000 daltons. The final concentration of the glucan solution is adjusted in the range of about 0.5 to 5 mg/ml. In accordance with pharmaceutical manufacturing standards for parenteral products, the solution can be terminally sterilized by filtration through a 0.22 .mu.m filter. The soluble glucan preparation obtained by this process is sterile, non-antigenic, and essentially pyrogen-free, and can be stored at room temperature for extended periods of time without degradation.

For purposes of the present invention, the term "soluble" as used herein to describe glucans obtained by the present process, means a visually clear solution can be formed in an aqueous medium such as water, PBS, isotonic saline, or a dextrose solution having a neutral pH (e.g., about pH 5 to about 7.5), at room temperature (about 20.degree.-25.degree. C.) and at a concentration of up to about 10 mg/ml. The term "aqueous medium" refers to water and water-rich phases, particularly to pharmaceutically acceptable aqueous liquids, including PBS, saline and dextrose solutions.

A critical advantage of this method is that precipitation, drying or reconstitution of the soluble glucan polymer is not required at any point in the process. The resulting solution is substantially free of protein contamination, is non-antigenic, non-pyrogenic and is pharmaceutically acceptable for parenteral administration to animals and humans. However, if desired, the soluble glucan can be dried by an appropriate drying method, such as lyophilization, and stored in dry form. The dried glucan can be reconstituted prior to use by adding an alkali solution such as about 0.1-0.4N NaOH and reprocessed starting from the step immediately following the organic acid contact steps described above.

The soluble glucans produced by the method of this invention are branched polymers of glucose, referred to as PGG, containing .beta.(1-3) and .beta.(1-6) linkages in varying ratios depending on the organism and processing conditions employed. The PGG glucan preparations contain neutral glucans, which have not been modified by substitution with functional (e.g., charged) groups or other covalent attachments. The biological activity of PGG glucan can be controlled by varying the average molecular weight and the ratio of .beta.(1-6) to .beta.(1-3) linkages of the glucan molecules, as described by Jamas et al. in U.S. Pat. Nos. 4,810,646, 4,992,540, 5,082,936 and 5,028,703. The average molecular weight of soluble glucans produced by the present method is generally from about 10,000 to about 500,000 daltons, preferably from about 30,000 to about 50,000.

The present soluble glucan preparations can be used as safe, effective, therapeutic and/or prophylactic agents, either alone or as adjuvants, to enhance the immune response in humans and animals. Soluble glucans produced by the present method enhance or prime the immune system so that the immune response is quicker and more pronounced. The present soluble glucan composition can be used to prevent or treat infectious diseases in malnourished patients, patients undergoing surgery, patients undergoing chemotherapy or radiotherapy, HIV-infected patients and the elderly, all of whom may have weakened immune systems. Methods of treating immunocompromised patients with glucans are described in detail in co-pending U.S. application Ser. No. 07/404,765 by Jamas et al. filed concurrently herewith.

The present composition is generally administered to an animal or a human in an amount sufficient to produce immune system enhancement. The preparation can be administered parenterally by injection, e.g., subcutaneously, intravenously, intramuscularly, intraperitoneally, topically, orally or intranasaly. The soluble glucans can be administered as a clear solution having a concentration of from about 1 mg/ml to about 5 mg/ml. The solvent can be a physiologically acceptable aqueous medium, such as water, saline, PBS or a 5% dextrose solution. The amount necessary to induce immune system enhancement will vary on an individual basis and be based at least in part on consideration of the individual's size, the severity of the symptoms and the results sought.

PGG is a non-toxic, non-antigenic glucan preparation which enhances or primes the body's natural defense against infection, particularly for patients with normal or decreased immunologic function, so that the normal immune response is faster and more pronounced. Parenteral administration of PGG mimics the natural physiologic response to an infectious challenge by enhancing the balanced, endogenous release of cytokines in appropriate quantities and proportions. PGG can be used for the prevention and treatment of infections caused by a broad spectrum of bacterial, fungal, viral and protozoan pathogens. The prophylactic administration of PGG to a person undergoing surgery, either preoperatively, intraoperatively and/or post-operatively, will reduce the incidence and severity of post-operative infections in both normal and high-risk patients. For example, in patients undergoing surgical procedures that are classified as contaminated or potentially contaminated (e.g., gastrointestinal surgery, hysterectomy, cesarean section, transurethal prostatectomy) and in patients in whom infection at the operative site would present a serious risk (e.g., prosthetic arthroplasty, cardiovascular surgery), concurrent initial therapy with an appropriate antibacterial agent and the present PGG preparation will reduce the incidence and severity of infectious complications.

In patients who are immunosuppressed, not only by disease (e.g., cancer, AIDS) but by courses of chemotherapy and/or radiotherapy, the prophylactic administration of PGG will reduce the incidence of infections caused by a broad spectrum of opportunistic pathogens including many unusual bacteria, fungi and viruses. Therapy using PGG has demonstrated a significant radioprotective effect with its ability to enhance and prolong macrophage function and regeneration and, as a result enhance resistance to microbial invasion and infection.

In high risk patients (e.g., over age 65, diabetics, patients having cancer, malnutrition, renal disease, emphysema, dehydration, restricted mobility, etc.) hospitalization frequently is associated with a high incidence of serious nosocomial infection. Treatment with PGG glucan may be started empirically before catheterization, use of respirators, drainage tubes, intensive care units, prolonged hospitalizations, etc. to help prevent the infections that are commonly associated with these procedures. Concurrent therapy with antimicrobial agents and the PGG is indicated for the treatment of chronic, severe, refractory, complex and difficult to treat infections.

Glucan produced by the present method enhances the non-specific defenses of mammalian mononuclear cells and significantly increases their ability to respond to an infectious challenge. The unique property of glucan-macrophage activation is that it does not result in increased body temperatures (i.e., fever) as has been reported with many non-specific stimulants of host defenses. This critical advantage of glucan may lie in the natural profile of responses it mediates in white blood cells. A unique mechanism of glucan activity in vitro is that pre-treatment of normal human leukocytes with PGG appears to prime the mononuclear cells to release elevated levels of monokines (TNF, GM-CSF, M-CSF, IL-6) upon subsequent stimulation with endotoxin or other infectious agents. This is considered highly advantageous since the monokines are not released systemically until exposure to the infectious agent. Thus, the present invention provides a soluble glucan which can be parenterally, topically, intranasaly, or orally administered to an animal or human to enhance the immune system, and a method for producing the soluble glucan.

The invention is further illustrated by the following Examples.

EXAMPLES

Example 1

Preparation of PGG from Dried Whole Glucan Particles

Whole glucan particles were prepared from dried Baker's Yeast (Universal Foods, WI) according to the procedure of Jamas et al., U.S. Pat. No. 4,810,646. 100 grams of the resulting dried whole glucan particles were resuspended in 3 liters of 90% formic acid and stirred at room temperature for 1 hour. The mixture was then heated to 80.degree. C. and stirred until a sudden drop in viscosity was observed. At this point, 9 liters of ethanol were added to the mixture resulting in formation of a precipitate, which was collected by centrifugation. The precipitate was then dissolved in 0.4M sodium hydroxide (NaOH) and the solution was centrifuged to remove undissolved particulates. The supernatant was concentrated by ultrafiltration using an Immersible-Cx-30 Ultrafilter (Millipore Corp., Bedford, Mass.) with a 30,000 dalton nominal molecular weight limit (NMWL) cut off. The retentate fraction was then diafiltered with ten volumes of water using the same equipment. The resulting solution was concentrated and equilibrated in sterile isotonic saline by diafiltration. The final yield of this fraction (>30,000 daltons) was 1.9 grams.

To produce a 10,000-30,000 fraction, the filtrate from the first ultrafiltration was concentrated by ultrafiltration through a 10,000 dalton membrane using an Immersible-CX-10 Ultrafilter (Millipore Corp.). The concentrated retentate fraction was then diafiltered with ten volumes of water, followed by equilibration in sterile isotonic saline. The final yield of this fraction was 2.7 grams.

Example 2

Production of PGG from Saccharomyces cerevisiae R4

Saccharomyces cerevisiae R4 (NRRL Y-15903) was cultured in 60 liters of a defined growth medium (4.45 g/l KH.sub.2 PO.sub.4, 3.0 g/L (NH.sub.4).sub.2 SO.sub.4, 1.1 g/l MgSO.sub.4.7H.sub.2 O, 1.8 g/l Lysine-HCl, 0.9 g/l Tyrosine, 0.012 g/l Adenine, 0.012 g/l Uracil, 5.0 g/l casamino acids, 0.45 g/l Histidine and 4.0 g/l Glucose) in a MPP-80 Mobile Pilot Plant Fermenter (New Brunswick Scientific, N.J.). When the culture reached an optical density (OD, 600 nm) of 30 the fermentation was stopped by adjusting the pH to 12 with 5M sodium hydroxide. The total cell yield was approximately 1.8 kg dry cell weight. The cells were harvested by centrifugation using a Westfalia Nozzle Bowl Separator (Model SKOG-205, Centrico, N.J.) and were washed with water. The concentrated cell suspension was transferred to a stainless steel stirred vessel and resuspended in 10 liters of 1M sodium hydroxide and stirred for 20 hours at 25.degree. C. The mixture was then heated to 90.degree. C. and stirred for an additional 1 hour. The insoluble particles were collected by centrifugation and washed with water. The concentrated slurry was resuspended to a volume of 10 liters in 1M sodium hydroxide and stirred at 90.degree. C. for 3 hours. This extraction step was repeated at 90.degree. C. for 1 hour. The insolubles were collected by centrifugation and washed with water. The concentrated slurry was then resuspended in 10 liters of water, the pH was adjusted to 4.5 with hydrochloric acid and stirred at 90.degree. C. for 1 hour, followed by centrifugation and washing. The concentrated slurry was then resuspended in 5 liters of 0.5M acetic acid and stirred at 90.degree. C. for 3 hours. The insolubles were collected by centrifugation. The yield of glucan particles at this step was 2.8 kg net weight.

An aliquot of 100 grams of the insoluble glucan particles was then resuspended in 500 ml of 0.5M acetic acid and was extracted at 90.degree. C. for 20 hours. The suspension was then neutralized to pH 7 with sodium hydroxide, and the insoluble glucan particles were collected by centrifugation. The glucans were resuspended in 200 ml of 1M sodium hydroxide and heated to 90.degree. C. for 1 hour to solubilize the glucan. The mixture was cooled and centrifuged to remove particulate debris. The supernatent solution was diluted to 0.4M sodium hydroxide with water and was filtered through a 0.5 .mu.m polypropylene depth filter. The resulting solution was concentrated four-fold by ultrafiltration through a 10,000 dalton NMWL membrane using a Minitan HRTF System (Millipore Corp.).

The retentate fraction was then diafiltered with ten volumes of 0.4M sodium hydroxide using the same equipment. The solution was diluted to obtain a 2 mg/ml glucan solution in 0.225M sodium hydroxide. The solution was adjusted to pH 9 with hydrochloric acid and diafiltered against sterile, isotonic saline using the Minitan System. The solution was then filtered through a 0.22 .mu.m sterilizing filter. This procedure gave 1.1 grams of sterile PGG glucan with a weight average molecular weight of 225,000 daltons.

Example 3

Affinity of Modified Glucans for the Monotype .beta.-glucan Receptor

The ability of glucan molecules to be recognized and bound to the .beta.-glucan receptor of monocytes is critical for their biological activity. Modified whole glucans derived from the mutant strain R4 (WGP-R4) demonstrated an increased affinity for the glucan receptor of monocytes when compare to naturally occurring glucans from Baker's yeast. Janusz et al., J. of Immunol., 137:3270-3276 (1986).

Water-soluble modified glucan (PGG) was prepared from WGP-R4 according to the procedure outlined in Example 2.

Human monocytes were incubated with various concentrations of the PGG for 15 minutes, washed to remove unbound glucan and then incubated with Zymosan for 30 minutes. After fixing and staining the monolayers, the percentage of monocytes ingesting Zymosan was determined. The affinity of glucan preparations for the .beta.-glucan receptor by was measured according to their ability to competitively occupy the receptor thus inhibiting the uptake of Zymosan by monocytes. Samples were compared by taking the concentration of glucan required to obtain 50% inhibition of Zymosan ingestion.

The significantly enhanced affinity of the soluble PGG glucan derived from WGP-R4 to the receptor is evident by the low concentration required to obtain a 50% inhibition of Zymosan ingestion. The results, presented in FIG. 1, demonstrate that the PGG glucan, designated WGP-R4, binds to the monocyte .beta.-glucan receptor with a much higher affinity (0.1 .mu.g/ml) than soluble glucan from Baker's yeast extract (3.5 .mu.g/ml), (YE glucan) representing a 35-fold increase in activity.

Example 4

Effect of PGG Molecular Weight on Macrophage Phagocytosis

Two molecular weight fractions of PGG from Saccharomyces cerevisiae R4 were prepared according to the procedure outlined in Example 2. The PGG preparations were then assayed for their affinity to the monocyte .beta.-glucan receptor by measuring inhibition of Zymosan phagocytosis as described in Example 3. The results, shown in Table 1 demonstrate that the molecular weight of the PGG preparations affects their affinity for the .beta.-glucan receptor, and therefore is expected to affect their in vivo immunologic activity.

Example 5

In Vivo Activity of PGG Glucans

The effect of in vivo administration of modified glucans on peripheral white blood cell (WBC) counts was characterized in mice. PGG preparations of the modified glucan from strain R4 were prepared according to the procedure outlined in Example 2 and administered intravenously (IV) and subcutaneously (SC) to male CD-1 mice. Total and differential cell counts were monitored at regular time intervals.

A profound increase in the total WBC count was observed particularly following single-dose IV administration of PGG. FIGS. 2 and 3 summarize the results, which show rapid (<6 hours) amplification of total WBC counts with, the most pronounced increase (12.times. and 6.times.) occurring in the monocyte and granulocyte counts, respectively. This is consistent with in vitro data suggesting the presence of a high affinity .beta.-glucan receptor present on human monocytes. The multiple-dose SC regimen (FIG. 3) elicited an increase in total WBC beginning at 48 hours and peaking at 144 hours after initiation of therapy. The increase in total counts was consistent with an increase in the peripheral monocyte population over this time period. The average monocyte count increased from 320/mm.sup.3 at zero hours to approximately 8,000/mm.sup.3 at 144 hours, representing at 24-fold increase.

Example 6

Infection Model

A sepsis model was developed in mice to characterize the efficacy of modified PGG glucans in protecting an immunologically intact host against serious infections, such as those which commonly occur following abdominal surgery. PGG derived from WGP-R4 was prepared according to the procedure outlined in Example 2.

The model used intraperitoneal challenge of mice with an 0.1 ml suspension of E. coli strain TVDL-rat (approximately 10.sup.8 CFU/ml) 24 hours following IV administration of PGG by single bolus injection using transthoracic cardiac puncture. Mice were returned to their cages and maintained on food and water ad libitum. A control group of 10 mice were injected with 0.1 ml sterile saline at the time of the PGG administration. Mortality rates for the treatment groups and saline control group were recorded at 48 hours after challenge. The results, shown in FIG. 4, demonstrated that PGG obtained from the modified glucan, WGP-R4, significantly reduced mortality, as compared to the saline control group (p<0.05) at doses as low as 0.01 mg/mouse (0.5 mg/kg body weight).

Equivalents

Those skilled in the art will recognize, or be able to ascertain, using no more than routine experimentation, many equivalents to the specific embodiments of the invention described specifically herein. Such equivalents are intended to be encompassed in the scope of the following claims.

Claims

We claim:

1. A process for producing purified neutral aqueous soluble .beta.(1-3) glucan having immuno-stimulating properties, comprising the steps of: a) contacting a suspension of aqueous insoluble .beta.(1-3) glucan with an organic acid under conditions sufficient to solubilize said glucan thereby forming an acid-soluble and acid-insoluble glucan mixture; b) contacting the acid-soluble portion of the glucan with an alkali solution under conditions sufficient to dissolve the alkali-soluble glucan; c) separating alkali-insoluble particulates from the solution of step (c); d) neutralizing the alkali-soluble glucan of step (c); and e) isolating an aqueous-soluble .beta.(1-3) glucan by size fractionation to produce a purified aqueous soluble .beta.(1-3) glucan that is suitable for parenteral administration.

2. A process of claim 1 wherein step (a) is performed at a temperature of about 20.degree. C. to about 100.degree. C. for a period of about 1 to about 20 hours.

3. A process of claim 1 wherein the alkali solution is 1N sodium hydroxide.

4. A process of claim 1 wherein step (b) is performed at a temperature of from about 4.degree. C. to about 121.degree. C. and for a period of about 1 to 3 hours.

5. A process of claim 1 further comprising contacting the solution obtained after step (d) with DEAE-cellulose, Q-Sepharose or QAE-cellulose.

6. Aqueous soluble .beta.(1-3) glucan produced by the method of claim 1.

7. A process of claim 1, wherein the aqueous insoluble .beta.(1-3)-glucan is derived from whole yeast glucan particles.

8. An aqueous soluble .beta.(1-3) glucan produced by the method of claim 1 having an increased avidity for the beta-glucan receptor compared to naturally occurring beta-glucans and which is substantially free of protein and essentially pyrogen free.

9. A process of claim 1 wherein the organic acid used in step (a) has a concentration of from about 0.1 to about 5M and a pH of from about 1 to about 5.

10. A process of claim 9 wherein the organic acid is acetic acid or formic acid.

11. A process of claim 1, wherein the alkali solution of step (b) is a solution of an alkali-metal or alkali earth-metal hydroxide having a pH of about 7 to about 14.

12. A process of claim 11, wherein the alkali solution of step (b) is a solution of an alkali-metal or alkali earth-metal hydroxide having a concentration of from about 0.1 to about 10.0N.

13. A process of claim 1, further comprising purifying the aqueous soluble .beta.(1-3) glucan by diafiltration with an alkali solution having a pH of about 7 to about 14.

14. A process of claim 13, wherein the diafiltration is performed with an alkali solution having a concentration of about 0.2 to about 0.4N.

15. A process of claim 1 further comprising purifying the aqueous soluble .beta.(1-3) glucan by size fractionation or diafiltration with a pharmaceutically acceptable medium.

16. A process of claim 15 wherein the pharmaceutically acceptable medium is selected from the group consisting of water, phosphate-buffered saline, isotonic saline and dextrose.

17. A process of claim 1 wherein the aqueous insoluble .beta.(1-3) glucan is derived from yeast.

18. A process of claim 17, wherein the yeast is a strain of Saccharomyces cerevisiae.

19. A process of claim 18, wherein the strain of Saccharomyces cerevisiae is strain R4 (NRRL accession number Y-15903).

20. A solution comprising purified soluble .beta.(1-3) glucan produced by the method of claim 1 and a pharmaceutically acceptable medium.

21. A solution of claim 20 containing from about 0.5 to about 10 mg/ml soluble .beta.(1-3) glucan in a pharmaceutically acceptable medium.

22. A solution of claim 21 wherein the pharmaceutically acceptable medium is selected from the group consisting of water, phosphate-buffered saline, isotonic saline and dextrose.

23. A process for producing a solution containing purified neutral aqueous soluble .beta.(1-3) glucans having immunostimulating properties, comprising the steps of: a) contacting a suspension of aqueous insoluble .beta.(1-3) glucan with an organic acid under conditions sufficient to solubilize said glucan thereby forming an acid-soluble and acid-insoluble glucan mixture; b) contacting the acid-soluble portion of the glucan with an alkali solution under conditions sufficient to dissolve the alkali-soluble glucan; c) separating alkali-insoluble particulates from the solution of step (b); d) neutralizing the alkali-soluble glucan of step (c); e) isolating an aqueous-soluble .beta.1-3 glucan by size fractionation to produce a purified glucan; and f) formulating the purified .beta.(1-3) glucans with a pharmaceutically acceptable medium to produce a solution which is suitable for parenteral administration.

24. A process of claim 23 wherein the aqueous insoluble .beta.(1-3) glucan is derived from yeast.

25. A process for producing purified neutral aqueous soluble yeast .beta.(1-3) glucan having immunostimulating properties, comprising the steps of: a) contacting a suspension of aqueous insoluble .beta.(1-3) glucan derived from yeast with an organic acid under conditions sufficient to solubilize said glucan thereby forming an acid-soluble and acid-insoluble glucan mixture; b) contacting the acid-soluble portion of the glucan with an alkali solution under conditions sufficient to dissolve the alkali-soluble glucan; c) separating alkali-insoluble particulates from the solution of step (b); d) neutralizing the alkali-soluble glucan of step (c); and e) isolating an aqueous soluble yeast .beta.(1-3) glucan by size fractionation to produce a purified neutral aqueous soluble .beta.(1-3) glucan that is suitable for parenteral administration.

26. Aqueous soluble yeast .beta.(1-3) glucan produced by the method of claim 25.

27. A process for producing a solution containing purified neutral aqueous soluble yeast .beta.(1-3) glucan having immunostimulating properties, comprising the steps of: a) contacting a suspension of aqueous insoluble .beta.(1-3) glucan derived from yeast with an organic acid under conditions sufficient to solubilize said glucan thereby forming an acid-soluble and acid-insoluble glucan mixture; b) contacting the acid-soluble portion of the glucan with an alkali solution under conditions sufficient to dissolve the alkali-soluble glucan; c) separating alkali-insoluble particulates from the solution of step (b); d) neutralizing the alkali-soluble glucan of step (c); e) isolating an aqueous soluble .beta.(1-3) glucan by size fractionation to produce a purified aqueous soluble glucan; and f) formulating the purified aqueous soluble yeast .beta.(1-3) glucan of step (e) with a pharmaceutically acceptable medium to produce a solution which is suitable for parenteral administration.

28. A solution comprising purified aqueous soluble yeast .beta.(1-3) glucan produced by the method of claim 27 and a pharmaceutically accepted medium.

Patent Citations (13)

Patent	Date	Inventor
US4138479	1979-02-01	Truscheit et al.
US4237266	1980-12-01	Sugiura et al.
US4739046	1988-04-01	DiLuzio et al.
US4761402	1988-08-01	Williams et al.
US4810646	1989-03-01	Jamas et al.
US5032401	1991-07-01	Jamas et al.
US5057503	1991-10-01	Czop et al.
EPX463540A1	1991-06-01
JPX55-071701	1980-08-01
JPX56-076401	1981-09-01
JPX59-045301	1984-06-01
JPX59-210901	1985-04-01
GBX2076418A	1980-05-01

Non-Patent Literature (16)

Manners et al., Biochem. J. (1973), vol. 135, pp. 19-30.
Shiota et al., J. Biochem. (1985), vol. 98, pp. 1301-1307.
Konopski et al., "Phagocytosis of .beta.-1,3-D-Glucan-Derivatized Microbeads by Mouse Peritoneal Macrophages Involves Three Different Receptors," Scand. J. Immunol. 33: 297-306 (1991).
Julia B. Reiskind and J. T. Mullins, "Molecular Architecture of the Hyphal wall of Achlya ambisexualis Raper. II. Ultrastructural Analyses and a Proposed Modell," Can. J. Microbiol. 27: 1100-1105 (1981).
Miyazaki et al., "Structural Examination of Antitumour, Water-Soluble Glucans from Grifora umbellata By Use of Four Types of Glucanase," Carbohydrate Research 65: 235-243 (1978).
G. H. Fleet and D. J. Manners, "Isolation and Composition of an Alkali-Soluble Glucan from the Cell Walls of Saccharomyces cerevisiae," Journal of General Microbiology 94: 180-192 (1976).
Latge' et al., "Composition Chimique et Ultrastructure des parois des corps hyphaux et des azygospores de Conidiobolus obscurus," Can. J. Microbiol. 30: 1507-1521 (1984).
Hara et al., "A Branched (1-3)-.beta.-D-Glucan From a Water Extact of Dictyophora indusiata FISCH," Carbohydrate Research 145: 237-246 (1986).
R. Goldman, "Induction of a .beta.-1,3-D-glucan receptor in P388D1 cells treated with retinoic acid or 1,25-dihydroxyvitamin D.sub.3," Immunology 63: 319-324 (1988).
Sherwood et al., "Soluble Glucan and Lymphokine-Activated Killer (LAK) Cells in the Therapy of Experimental Hepatic Metastases," Chemical Abstracts 108: 179752v (1988).
Janusz, M. J. et al., J. Immunol. 137: 3270-3276 (Nov. 15, 1986).
Manners, D. J. et al., Biochem. J. 135: 19-30 )1973).
Williams, D. L. et al., Chemical Abstracts 109: 66566q (1988).
Fleet, G. H. et al., Chemical Abstracts 85: 89819z (1976).
Bacon, J. et al., Biochem. J. 114: 557-567 (1969).
International Search Report for PCT/US90/05041 which claims priority to the subject application.

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