THERAPEUTIC CHOLESTEROL GALLSTONE DISSOLUTION METHOD

Abstract: A method and apparatus are disclosed for treating a patient having cholesterol calculi which involves infusing into the biliary tract of said patient a C5-C6 ester, ether or ketone having a boiling point in the range of 80 DEG -140 DEG C or a mixture thereof in an amount and at a flow rate effective to at least partially dissolve said calculi rapidly. The invention also encompasses dissolving cholesterol calculi by exposing such calculi to contact with effective quantities of those solvent compounds. The apparatus includes a high flow rate catheter pumping system for infusing a gallstone dissolution solvent into the gallbladder of a patient and aspirating the gallstone dissolution solvent from the gallbladder, and a unit measure container of the solvent. The preferred esters, ethers and ketones are n-propyl acetate, isopropyl acetate, ethyl propionate, ethyl isobutyrate, cyclopentanone, 3-pentanone and methyl t-amyl ether. Contact flow rates are sufficiently high to insure fluid turbulence in the biliary tract region surrounding the calculi.

Description: THERAPEUTIC CHOLESTEROL GALLSTONE DISSOLUTION METHOD CROSS-REFERENCE TO RELATED APPLICATION The application is a continuation-in-part of application Serial No. 07/341,900, filed April 24, 1989. BACKGROUND OF THE INVENTION 1. Field of the Invention: The invention herein relates to medical treatments of cholesterol calculi (particularly gallstones) by contact dissolution with organic solvents. More particularly it relates to therapeutic methods using low viscosity non-toxic pumpable solvents. 2. Background of the Prior Art; The contact dissolution of cholesterol gallstones by organic solvents in human patients is a well recognized medical procedure and may be favored over surgical procedures to remove gallstones in patients at increased risk of surgery; see, for instance, U.S. Patent No. 4,205,086. The dissolution procedures normally involve infusion of the solvent into the biliary tract (including the gallbladder and the bile ducts) by means of a T-tube, nasobiliary tube, percutaneous transhepatic catheter or cholecystostomy tube by use of a constant infusion pump or by gravity or by manual repeated installation and withdrawal using a syringe; see Palmer, et al.. Gut. 27. 2, 196 (1986) . Often the stones fragment during the dissolution procedure, which advantageously increases the rate of dissolution. A number of different types of solvents have been used or suggested for the dissolution procedure. These include organic solvents such as diethyl ether, chloroform or d-limonene as well as aqueous micellar solutions of bile salts. The aforementioned U.S. Patent No. 4,205,086 also lists a large number of useful liquid fatty acids and the alcohol esters thereof. A further solvent which has received substantial attention is monooctanoin, mentioned in U.S. Patent No. 4,755,167 and several articles, such as Thistle, et al., Gastroenteroloqy, 78. 5, 1016 (1980). More recently methyl t-butyl ether (MTBE) has been used as a cholesterol gallstone solvent; see, e.g., Allen, et al., Gastroenteroloqy. 88. 1, 122 (1985); Thistle, et al., U.S. Patent No. 4,758,596; and Thistle, et al., N. Enql. J. Med.. 320. 633 (1989). While all of these materials have shown some efficacy in in vivo and/or in vitro tests, all have some undesirable side effects or physical properties. Monooctanoin, for instance, has a relatively high viscosity and dissolves gallstones very slowly. MTBE was selected by Thistle,, et al., because its boiling point is above body temperature. However, if MTBE escapes from the gallbladder into the small intestine, it causes signs of systemic toxicity (sedation) , pain, nausea, and by endoscopy, damage to the epithelium of the small intestine. Entry of MTBE into the blood stream causes hemolysis, and one case of renal failure (reversible) has been reported. MTBE also has a relatively low boiling point (55'C), not far above ordinary body temperature, which poses some volatility problems in use because of its low flash point and strong, unpleasant odor. Those materials such as diethyl ether which have boiling points below body temperature are hazardous for clinical use because of rapid volatilization and marked increase in volume in use. Recently there has been developed a novel infusion pump which produces a high flow rate at low pressure. This pump has been described and claimed in U.S. Patent No. 4,902,276, issued February 20, 1990, and U.S. Patent Application Ser. No. 07/482,194 (February 20, 1990) by S. Zakko (the "Zakko pump"). While this pump has proved very effective for gallstone dissolution, its satisfactory performance depends on being used with relatively low viscosity solvents. It would therefore be advantageous to have a therapeutic procedure available in which cholesterol gallstones could be easily, safely and rapidly dissolved by a solvent which would be effective for dissolution of cholesterol gallstones, easy and safe to handle for medical personnel and capable of being used in the most effective equipment such as the Zakko pump. BRIEF SUMMARY OF THE INVENTION In one aspect, the invention herein is a method for treating a patient having cholesterol calculi, particularly gallstones, which comprises infusing into the biliary tract of said patient a C5-C6 ester, ether or ketone having a boiling point in the range of 80 β -140 β C or a mixture thereof in an amount and at a flow rate effective to at least partially dissolve said calculi rapidly. In another aspect, the invention herein is a method for dissolving cholesterol calculi (particularly gallstones) which comprises contacting said calculi with a C5-C6 ester, ether or ketone having a boiling point in the range of 80 β -140 , C or a mixture thereof in an amount and at a flow rate effective to at least partially dissolve said calculi rapidly. Particularly preferred among the C5-C6 esters, ethers and ketones are those selected from the group consisting of n-propyl acetate, isopropyl acetate, ethyl propionate, ethyl isobutyrate, cyclopentanone, 3-pentanone and methyl t-amyl ether (methyl 1,1-dimethylpropyl ether). These have all been found to produce rapid dissolution of cholesterol gallstones (at a rate generally comparable to that of MTBE) without problems of volatility or excessive viscosity. BRIEF DESCRIPTION OF THE DRAWINGS The advantages of this invention may be better understood by referring to the following description taken in conjunction with the accompanying drawings in which: Figure 1 depicts an embodiment of the invention using peristaltic pumps. Figure 2 depicts an embodiment of the catheter of the invention. Figure 3 depicts an embodiment of the reservoir of the invention containing a unit volume of solvent. Figure 4 depicts an embodiment of the tubing of the invention. Figure 5 depicts an embodiment of a kit containing the disposable portions of the invention. DETAILED DESCRIPTION AND PREFERRED EMBODIMENTS The efficacy of the methods of this invention can be best understood by consideration of the characteristics of cholesterol calculi and the claimed class of solvents useful in the invention. As used herein, the term ■■ cholesterol calculi" means those concretions which generally develop in hollow organs or ducts within humans and animals and which contain at least about 40% cholesterol. Well known common cholesterol calculi are cholesterol biliary duct stones and gallstones. Also, the term "biliary tract" will be recognized to encompass both the gallbladder and the bile ducts. Consideration of the usual equations used to describe dissolution of a sphere by a fluid under turbulent conditions indicates that not only equilibrium solubility but also viscosity is important. This is because viscosity influences the diffusion of cholesterol in the unstirred layer immediately surrounding the stone (according to the Stokes-Einstein relationship) . In addition, low viscosity is important since catheters used for this purpose must have a small bore (usually less than 8 French) , with a high flow-low pressure pumping system such as that of the Zakko Pump. The pressure needed to obtain a given flow varies inversely as the 4th power of the radius, and directly with the viscosity of the fluid being pumped. Thus for a small bore tube, the lower the viscosity, the greater is the solvent flow for a given pressure. There are two additional requirements for a satisfactory solvent. It must be relatively non-toxic in several aspects. First, the solvent must not damage the gallbladder mucosa significantly during a several hour exposure of the mucosa to the anhydrous solvent. Second, the solvent must not damage the mucosa of the biliary duct system or the small intestine if the solvent leaks out of the gallbladder. The solvent should cause little hemolysis if mixed with blood, should not cause release of toxic cytokines such as platelet activating factor, and should not be toxic if it escapes into the peritoneal cavity. In addition, the solvent should have a pleasant odor so that if absorbed it does not induce nausea. Further, the solvent should be rapidly metabolized by digestive enzymes if it escapes into the gastrointestinal tract, and the resultant digestive products should be known to be safe. Lastly, there are safety considerations in handling the solvent. If spilled, it should not cause danger to exposed employees. It should be a non-explosive and have a relatively high flash point. It should have a stable shelf life and not form peroxides or other explosive by-products. Viscosity is known to vary directly with the number of carbon atoms in a molecule. It varies inversely approximately exponentially with temperature. Boiling point and flash point also vary directly with the total number of carbon atoms, but the relationship is not as simple. Cholesterol solubility in solvents can be predicted to some extent by solubility parameter considerations. The determination of solvents suitable for effective contact dissolution of cholesterol gallstones thus involves multiple considerations. In addition, there are solute considerations. Cholesterol gallstones are composed of cholesterol monohydrate (and other insoluble salts) ; see Whiting, et al., Clin. Sci.. 68. 589 (1985). If gallstones are stored in the dry state, the water may evaporate so that the cholesterol monohydrate becomes anhydrous cholesterol. Therefore testing of solvents is best done on freshly harvested human gallstones which have been kept wet. Based on these considerations, our research has led to the discovery that effective solvents are those having 5-6 carbon atoms per molecule and being selected from the group consisting of ethers, esters and ketones with a boiling point in the range of 80"-140 , C and mixtures thereof. We have also discovered that within this class those compounds which are particularly preferred solvents, due to their most closely meeting the desirable criteria discussed above, are n-propyl acetate, isopropyl acetate, ethyl propionate, ethyl isobutyrate, cyclopentanone, 3-pentanone and methyl t-amyl ether (methyl 1,1-dimethylpropyl ether) . All of these are known compounds and need not be defined further here; their physical and chemical properties are well described in the chemical literature. Their efficacy and the techniques of the present invention may be seen from the following data. In the tests described in Table I below, fresh human faceted cholesterol gallstones (kept in distilled water) were dissolved in vitro and the times were recorded for the total dissolution, using a model gallbladder at a high flow rate achieved by a metering pump. "High flow rate" as used herein will mean rates of flow in the range which can be anticipated to result in fluid turbulence for the solvent in the region of the biliary tract surrounding the calculi (gallstones) . While "high" rates will vary according to solvent type and viscosity and with individual patients, it will be expected that appropriate flow rates will be at least about 20 ml/min, preferably at least about 100 ml/min, and more preferably at least about 150 ml/min. For comparison purposes a parallel test with MTBE is also shown. The second column shows the weight of stone treated, of which 90% by weight can be considered to be cholesterol. TABLE I Boiling Stone Dissolution Point, Weight, Time, Rate, Solvent β C mα min. mσ/min. n-propyl acetate 102 150 10 14 isopropyl acetate 89 147 14 9 ethyl propionate 99 140 10 13 ethyl isobutyrate 112 132 15 8 eye1opentanone 131 125 10 11 3-pentanone 101 142 9 14 methyl t-amyl ether 85 131 8 15 methyl t-butyl etherr 55 175 8 20 It will be evident from these data that the C5-C6 ether, ester and ketone solvents of this invention are essentially similar to the known MTBE in their ability to rapidly dissolve cholesterol gallstones, while yet having substantially higher boiling points than MTBE and thus substantially less potential for problems with volatility. Toxicological considerations indicate that the first six solvents have a low order of toxicity, although only limited information is available on cyclopentanone. The toxicity of methyl t-amyl ether has not been studied, but should be similar to that of MTBE; see Savolainen, et al., Arch. Toxicol.. 57, 285 (1985). In another series of experiments, the effectiveness of propyl acetate, isopropyl acetate, ethyl propionate and ethyl isobutyrate esters versus MTBE in dissolving cholesterol gallstones was determined in vitro. For this study stones from five cholecystectomy patients were matched. All stones were visually judged to be primarily cholesterol. The mean stone weight for the test sets (five stones each) ranged from 79-340 mg. The test protocol utilized a 30 ml polyethylene bag as a model gallbladder. One stone was dissolved at a time. For each stone a reservoir containing 150 ml of solvent was used. Flow to the bag was maintained at 180 ml/min. A closed loop pumping system was employed to deliver the solvent to the experimental stone within the polyethylene bag. A Medical Disposables International subclavian catheter (#1900115A) was used to deliver and withdraw the solvent and monitor pressure which controlled the pump. This catheter consisted of two 18 gage lumens and a single 16 gage lumen. The larger lumens were used to aspirate and infuse the solvent and the smaller lumen was used to monitor pressure within the model gallbladder. The termination of each lumen was a single port. The feed back from the pressure transducer was used to control the pumps to delivery 180 ml/min within a predetermined intralumen pressure. A flow of 180 ml/min was used to assure high turbulence and obtain optimum dissolution rates due to high rates of mass transfer. Complete dissolution was defined as the disappearance of all debris in the model gallbladder. The data are summarized in Table II. TABLE II Mean Time Overall Rate min. mg/min. Ethyl Propionate 14 12.22 MTBE 19 7.69 Isopropyl Acetate 26 5.48 Ethyl Isobutyrate 33 4.55 Propyl Acetate 35 4.45 This comparison shows the esters tested to be substantially equivalent to MTBE. The variation in rates is well within experimental expectations, since great differences exist from stone to stone for each solvent and the surface area per unit volume increases as the stone diameter (weight) decreases for similar materials and for similar geometries. It is also expected that the chemical differences from stone to stone may cause one solvent to perform appreciably different than the next. Metabolic considerations indicate that the esters (n-propyl acetate, isopropyl acetate, ethyl propionate and ethyl isobutyrate) are likely to be hydrolyzed by digestive esterases and quickly converted to the corresponding alkanol and aliphatic acid (which will ionize) . The hydrolysis products — ethanol, n-prσpanol and isopropanol and the acetate, propionate and butyrate ions — all have a low degree of toxicity. The ketones will be reduced in the liver to the equivalent alcohols, which are generally non-toxic. We believe that it is likely that a mixture the solvents will have less toxicity (expressed per unit volume of solvent) than any of the solvents alone because each of the solvents undergoes a different metabolic pathway. Any suitable technique of infusion of the described solvents into a patient in the method of this invention can be used; normally the one chosen will be as that described in the prior art for other solvents, , including monooctanoin and MTBE. The solvents are normally used in undiluted liquid form, but if desired may also be used as part of mixtures with inert liquid carriers. Since dissolution is a contact phenomenon it will be recognized that dilution in such mixtures will normally slow the rate of dissolution and extend the time needed to achieve the desired degree of gallstone dissolution. Another aspect of the invention is the in vivo dissolution of gallstones using the C5-C6 ester, ether and ketone class of solvents provided herein as the solvent in a high flow rate pumping system, in particular a continuous pumping system controlled by gallbladder pressure feedback and employing a delivery system consisting of a catheter, a continuous flow pumping system, a controller and a tubing set; see aforesaid U.S. Patent Application No. 07/482,194, filed February 20, 1990, to S. Zakko, incorporated herein by reference. In general, the system shown in that application and see Figure 1 herein, is capable of operating continuously at a high flow rate to produce continuous turbulence in the gallbladder while assuring that the intra-luminal gallbladder pressure does not exceed the critical leakage pressure, thereby preventing solvent from entering the intestine through the cystic and common bile ducts. Such a pumping system, in combination with the low viscosity solvent provided herein, has the capability of emptying the gallbladder many times faster than the rate of normal gallbladder contraction, to prevent solvent from emptying into the intestine should such a gallbladder contraction occur during perfusion. The system is however designed to permit internal pressure transients due to patient coughing, laughing, movement and the like without interrupting the solvent flow. The system will accept flow calibrations of both infusion and aspiration pumps and operate those pumps at substantially equal flow rates to minimize the control modulation and maximize the overall flow rate. The controller of the system can, for example, accept, upon command, flow rate, set pressure, lower pressure limit, upper pressure limit and alarm conditions and permit the operation at flow rates of the solvent from close to zero to 250 ml/min, with normal perfusion occurring at flow rates preferably above about 150 ml/min. As previously mentioned, the present solvents, due to their low viscosities, are intrinsically efficient in contact dissolution due to enhanced mass transfer performance; furthermore, the high flow rates and attendant turbulence permitted by the low viscosity will enhance the dissolution effect. The pump infuses solvent into the gallbladder of the patient through a catheter, shown in Figure 2, and more fully in the aforesaid U.S. Patent Application Serial No. 07/482,194. The catheter is constructed to permit the aspiration and infusion of the disclosed low viscosity class of esters, ethers and ketones at flow rates up to 250 ml/min while requiring no more than an 8 french catheter size. Such a catheter includes an infusion lumen, an aspiration lumen and a pressure sensing lumen to permit the continuous remote monitoring of intra-gallbladder pressure with a column of physiological saline. The catheter also includes a retention device to secure the catheter within the gallbladder intra- and post- operatively. The catheter 76 is supplied with solvent by a tubing set and reservoir which are provided as a disposable kit, as discussed below. The tubing, catheter and reservoir are constructed of materials compatible with the selected solvent. The tubing must be strong enough to be used in a peristaltic pump in which solvent is being infused or aspirated at flow rates up to 250 ml/min. and yet not limit flow or permit elastic deformation under positive or negative pressure which would adversely reduce the frequency response of the pump to control gallbladder pressure. Additionally, the reservoir allows for the gravity separation of bile and solvent, thereby permitting aspirated solvent to be reinfused. In more detail, the pumping system portrayed in Figure 1 comprises a peristaltic infusion pump 14 and a peristaltic aspiration pump 18. These pumps are driven by separate, reversible DC motors which are controlled by a programmable controller 90. The infusion pump draws the solvent from reservoir 10 by means of conduit 12 and discharges the solvent into infusion lumen 54 of catheter 76. The aspiration pump draws the solvent from the gallbladder by means of the aspiration lumen 50 of catheter 76 and conduit 25 and discharges it to reservoir 10. The pressure in the gallbladder is sensed by transducer 24 by means of a static liquid column 27. The analog pressure signal is converted to a digital signal by an analog to digital converter 94 and supplied to the micro-processor 96 through bus 98. In the normal operation mode, the microprocessor 96, responding to a pressure signal from transducer 24, operates the infusion pump 14 at the desired flow rate. The aspiration pump is driven at varying speeds when the pressure is above or below the desired pressure, and at a constant speed when the pressure is in the vicinity of the desired pressure, to keep the gallbladder pressure within the upper and lower pressure limits. Further, should the pressure remain above (as may occur with the beginning of a gallbladder contraction) or below the upper and lower pressure limits in excess of empirically determined delays, or above or below the upper and lower pressure alarms, for the associated delays, the controller causes the system to enter into an alarm mode in which both pumps operate in the aspiration direction at maximum flow rate to remove the low viscosity solvent. The catheter, shown in Figure 2, includes three fluid lumens 50, 52, 54 and a pigtail retention device 75. As shown in Figure 2, a separate lumen 70 in provided for the pigtail retention. The aspiration lumen 50 is made larger than the infusion lumen 54 to provide for the fact that the pressure drop in the aspiration mode is limited to the difference between atmospheric pressure and the solvent's vapor pressure. Additionally, under aspiration, the lumen tends to collapse, further reducing flow. In the infusion mode, the pressure within the infusion lumen can exceed 6 atmospheres; the catheter is constructed of a material which can endure this type of pressure. The pressure sensing lumen 52 need only be .020 inch in diameter to obtain excellent response. The ports 71 to the aspiration lumen 50 and the ports (not shown) to the infusion lumen 54 direct flow of the low viscosity solvent perpendicular to the plane of the pigtail. Each lumen 50, 52 and 54 terminates in a plurality of ports, each having a cross-sectional area less than the respective lumen with which it is in communication. This size ratio is desirable to reduce the possibility of lumen blockage. Each lumen terminates at the proximal end of the catheter in one of a series of polarized luer fittings 80, 82, 84, 86 for connection to the system tubing. Referring to Fig. 3, the solvent is preferably prepackaged in a disposable gravity-separation reservoir 10 containing a unit measure of the solvent 102, and special features enabling use in the continuous, high flow rate, Zakko pumping system. The reservoir 10 has a total volume larger than the volume of solvent 102 contained, for example 200 ml of solvent in a 250 ml container. The reservoir 10 includes an integral intake tube 104 and an integral return tube 114. One end 108 of the intake tube 104 terminates below the solvent-air meniscus 106, while the other end 110 of the intake tube 104 is constructed to mate only with the tubing from the infusion pump. Similarly, one end 112 of the return tube 114 extends further into the reservoir 10 than does the intake t be 104 in order to expel the solvent/bile mixture removed from t patient closer to the bottom of the reservoir 10. This is done to prevent the aspiration of waste bile by the intake tube 104. The other end 116 of the return tube 11 ■* : is also constructed with a connector which permits it to mate only with the tubing from the aspiration pump. Referring also to Figure 4, the tubing assemblies 12, 25 comprise the peristaltic tubing 128, 146 for the infusion and aspiration pumps respectively, catheter tubing 120, 152 for fluid flow between the peristaltic tubing 128, 146 and the catheter connectors 80, 82 and reservoir tubing 132, 142 for fluid flow between the peristaltic tubing 128, 146 and the reservoir intake 110 and return tubes 114. The tubing assemblies 12, 25 are specific for use with the infusion pump 14 and the aspiration pump 18, respectively. One end 134 of the reservoir tubing 132 terminates in a connector which will only mate with the connector 110 on the integral intake tube 104 from the reservoir 10. Similarly, one end 140 of the reservoir tubing 142 terminates in a connector which will only mate with the connector 116 on the integral return tube 114 from the reservoir 10. The other end 130, 144 of the reservoir tubing 132, 142 has a connector which will mate with the peristaltic tubing 128, 146 respectively. The catheter tubing 120, 152 also have connectors at one and 124, 150 which connect to the peristaltic tubing 128, 146 respectively. The other ends 122, 154 of the catheter tubing are constructed to mate only with the respective connectors on the catheter 80, 82. For example, the reservoir tubing may be constructed of .125" i.d./.210" o.d. polyethylene while the peristaltic pump tubing may be 5/16" i.d./7/16" o.d. "Tygothane" tubing. It is also possible to construct each tubing as a single unit. Additionally the pressure sensing lumen 52 communicates with the pressure transducer 24 through a pressure tube 27. Pressure tube 27 has a fitting 156 at one end for connection to the transducer 24 and a fitting at the other end 160 which permits its connection only to the proper catheter connector 84. Additionally, since transducer assemblies typically have a filling/aspiration port to permit their being filled with physiological saline, an additional tube 164 is needed with a fitting 162 for connection to the filling port of the transducer 163 and a fitting 166 for connection to a three-way syringe valve 165. The tubing 119 discussed is disposable and is typically replaced each time the reservoir 10 in replaced. Referring to Figure 5, the tubing 119, reservoir 10 and solvent 106 are most conveniently provided as a single unit kit 180 in a tray 182. The catheter 76 may be included in the kit or may be supplied separately since although the catheter 76 is disposable, typically only one catheter is used in one procedure with a single patient, while the reservoir 10 and the tubing 119 will be replaced several times in a procedure. The catheter 76, tubing 119 and reservoir 10 are provided pre- sterilized. As suggested by dashed line the unit measure of solvent or an additional unit measure of solvent may be supplied in an additional container, to be emptied into the reservoir at the point of use. It will be understood by those skilled in the art that there are numerous other embodiments which are not described above but which are clearly within the scope and spirit of the invention. The description above is therefore intended to be exemplary only and the scope of the invention is to be limited solely by the appended claims. We claim:

Claims: CLAIMS 1. A method for dissolving cholesterol calculi which comprises contacting said calculi with a solvent comprising a C5-C6 ester, ether or ketone having a boiling point in the range of 80°-140 β C or a mixture thereof in an amount and at a flow rate effective to at least partially dissolve said calculi rapidly. 2. A method as in Claim 1 wherein said ester, ether or ketone is n-propyl acetate, isopropyl acetate, ethyl propionate, ethyl isobutyrate, cyclopentanone, 3-pentanone or methyl t-amyl ether. 3. A method as in Claim 1 wherein said solvent is used in an undiluted form. 4. . A method as in Claim 1 wherein said solvent is used in a form in which it is mixed with and diluted by an inert carrier liquid. 5. A method as in Claim 1 wherein said contacting comprises pumping said solvent past said calculi. 6. A method as in Claim 5 wherein said pumping is conducted at a high solvent flow rate. 7. A method as in Claim 6 wherein said pumping is conducted at a high solvent flow rate at low pressure. 8. A method as in Claim 6 wherein said high solvent flow rate is on the order of at least 20 ml/min. 9. A method as in Claim 8 wherein said high solvent flow rate is on the order of at least 100 ml/min. 10. A method as in Claim 9 wherein said high solvent flow rate is on the order of at least 150 ml/min. 11. A method as in Claim 6 wherein said pumping is conducted with a constant circulation pump. 12. A method as in Claim 2 wherein said ester is n-propyl acetate. 13. A method as in Claim 2 wherein said ester is isopropyl acetate. 14. A method as in Claim 2 wherein said ester is ethyl propionate. 15. A method as in Claim 2 wherein said ester is ethyl isobutyrate. 16. A method as in Claim 1 wherein the rate of dissolution of said calculi is on the order of at least 8 mg/min. 17. A method as in Claim 16 wherein the rate of dissolution of said calculi is on the order of 8-14 mg/min. 18. A method for treating a patient having cholesterol calculi in the biliary tract which comprises infusing into the biliary tract of said patient a solvent comprising a Cs-C 6 ester, ether or ketone having a boiling point in the range of 80 β -140''C or a mixture thereof in an amount and at a flow rate effective to at least partially dissolve said calculi rapidly. 19. A method as in Claim 18 wherein said ester, ether or ketone is n-propyl acetate, isopropyl acetate, ethyl propionate, ethyl isobutyrate, cyclopentanone, 3-pentanone or methyl t-amyl ether. 20. A method as in Claim 18 wherein said infusion comprises pumping said solvent through said patient's biliary tract. 21. A method of gallstone dissolution using a high flow rate catheter pumping system for infusing a gallstone dissolution solvent into the gallbladder of a patient, and aspirating the gallstone dissolution solvent from the gallbladder characterized in which the solvent comprises a C 5 -C6 ester, ether or ketone having a boiling point in the range of 80°-l40 * 'C or a mixture thereof in an amount characterized in that said infusing and aspirating is at a flow rate effective to at least partially dissolve said calculi rapidly. 22. A method as is Claim 21 wherein said flow is continuous and at a rate sufficient to cause sustained turbulence within the gallbladder. 23. A method as in Claim 22 wherein said solvent is infused at a rate about 150 ml/min. 24. A container product for use with a gallstone dissolution apparatus including a high flow rate catheter pumping system for infusing a gallstone dissolution solvent into the gallbladder of a patient, and aspirating the gallstone dissolution solvent from the gallbladder, said container product comprising a unit measure of a solvent comprising C 5 -C ester, ether or ketone having a boiling point in the range of 80°-140 β C or a mixture thereof. 25. A product as in Claim 24 wherein said unit measure of solvent is packaged in a disposable kit including a disposable reservoir for holding the solvent, said reservoir including an inlet line constructed to be connected with an inlet line of said high flow rate pumping system to supply solvent to said i system. 26. A product as in Claim 25 wherein said solvent is ! prepackaged within said reservoir. 27. A product as in Claim 25 wherein said kit includes a ! disposable tubing set constructed to connect said reservoir with said high flow rate pumping system. . 28. A product as in Claim 27 wherein said high flow rate pumping system is a continuous flow system which includes peristaltic infusion and aspiration pumps and said tubing 1 includes sections of peristaltic tubing for said aspiration and infusion pumps and sections of connecting tubing connecting 3 said peristaltic tubing with said reservoir and a catheter. 29. A product as in Claim 25 wherein said disposable 2 reservoir includes a return line for connection with an outlet of said high flow rate pumping system to receive said solvent 4 and bile aspirated from said system and the volume of said reservoir being greater than the volume of pre-filled solvent 6 supplied to permit accumulation of bile and debris. 30. A product as in Claim 25 wherein said high flow rate pumping system with which said kit is to be used includes a control means responsive to intra gallbladder pressure for controlling the high flow rate pumping and said disposable tubing set includes a length of tubing for connecting a respective lumen of the catheter used with said system to said control means. 31. A product as in Claim 25 wherein said unit measure is of the order of 200 ml of said solvent. 32. A gallstone dissolution apparatus including a high flow rate catheter pumping system for infusing a gallstone dissolution solvent into the gallbladder of a patient, and aspirating the gallstone dissolution solvent from the gallbladder, characterized in that the solvent comprises a C5-C6 ; ester, ether or ketone having a boiling point in the range of 80"-140"'C or a mixture thereof in an amount and at a flow rate ! effective to at least partially dissolve said calculi rapidly. 33. Apparatus as in Claim 32 wherein said high flow rate ! catheter pumping system is a continuous flow system capable of simultaneous infusion and aspiration, said high flow rate _ catheter pumping system further including a reservoir for providing said solvent infused into and for receiving said > solvent aspirated from said gallbladder. 34. Apparatus as in Claim 33 wherein said reservoir » comprises a disposable unit package pre-filled with said solvent, the total volume of said reservoir is greater than the 1 volume of pre-filled solvent supplied to permit the accumulation of bile and debris and said reservoir is 5 constructed to enable separation of bile and debris from the solvent aspirated from the gallbladder.

Inventors: HOFMANN ALAN F, SCHTEINGART CLAUDIO D, HOFMANN, ALAN, F., SCHTEINGART, CLAUDIO, D.
Applicants: UNIV CALIFORNIA, THE REGENTS OF THE UNIVERSITY OF CALIFORNIA
Application year: 1990
Main classification: A61K31
IPC codes: A61B17, A61K31, A61M1, A61M37, A61P1, A61P3