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SELECTIVE ORGAN HYPOTHERMIA
METHOD AND APPARATUS
CROSS REFERENCE TO RELATED
This application is a continuation application of pending U.S. application Ser. No. 09/650,940, filed Aug. 30, 2000, titled "Selective Organ Hypothermia Method and Apparatus", which is a continuation of U.S. application Ser. No. 09/306,866, filed May 7, 1999, now U.S. Pat. No. 6,235,048, titled "Selective Organ Hypothermia Method and Apparatus", which is a divisional application of U.S. application Ser. No. 09/012,287, filed Jan. 23,1998, titled "Selective Organ Hypothermia Method and Apparatus", now U.S. Pat. No. 6,051,019.
STATEMENT REGARDING FEDERALLY
SPONSORED RESEARCH OR DEVELOPMENT
BACKGROUND OF THE INVENTION
1. Field of the Invention
The current invention relates to selective cooling, or hypothermia, of an organ, such as the brain, by cooling the blood flowing into the organ. This cooling can protect the tissue from injury caused by anoxia or trauma.
2. Background Information
Organs of the human body, such as the brain, kidney, and heart, are maintained at a constant temperature of approximately 37° C. Cooling of organs below 35° C. is known to provide cellular protection from anoxic damage caused by a disruption of blood supply, or by trauma. Cooling can also reduce swelling associated with these injuries.
Hypothermia is currently utilized in medicine and is sometimes performed to protect the brain from injury. Cooling of the brain is generally accomplished through whole body cooling to create a condition of total body hypothermia in the range of 20° to 30° C. This cooling is accomplished by immersing the patient in ice, by using cooling blankets, or by cooling the blood flowing externally through a cardiopulmonary bypass machine. U.S. Pat. No. 3,425,419 to Dato and U.S. Pat. No. 5,486,208 to Ginsburg disclose catheters for cooling the blood to create total body hypothermia However, they rely on circulating a cold fluid to produce cooling. This is unsuitable for selective organ hypothermia, because cooling of the entire catheter by the cold fluid on its way to the organ would ultimately result in non-selective, or total body, cooling.
Total body hypothermia to provide organ protection has a number of drawbacks. First, it creates cardiovascular problems, such as cardiac arrhythmias, reduced cardiac output, and increased systemic vascular resistance. These side effects can result in organ damage. These side effects are believed to be caused reflexively in response to the reduction in core body temperature. Second, total body hypothermia is difficult to administer. Immersing a patient in ice water clearly has its associated problems. Placement on cardiopulmonary bypass requires surgical intervention and specialists to operate the machine, and it is associated with a number of complications including bleeding and volume overload. Third, the time required to reduce the body temperature and the organ temperature is prolonged. Minimizing the time between injury and the onset of cooling has been shown to produce better clinical outcomes.
Some physicians have immersed the patient's head in ice to provide brain cooling. There are also cooling helmets, or
head gear, to perform the same. This approach suffers from the problems of slow cool down and poor temperature control due to the temperature gradient that must be established externally to internally. It has also been shown that
5 complications associated with total body cooling, such as arrhythmia and decreased cardiac output, can also be caused by cooling of the face and head only.
Selective organ hypothermia has been studied by Schwartz, et. al. Utilizing baboons, blood was circulated and
1° cooled externally from the body via the femoral artery and returned to the body through the carotid artery. This study showed that the brain could be selectively cooled to temperatures of 20° C. without reducing the temperature of the entire body. Subsequently, cardiovascular complications
15 associated total body hypothermia did not occur. However, external circulation of the blood for cooling is not a practical approach for the treatment of humans. The risks of infection, bleeding, and fluid imbalance are great. Also, at least two arterial vessels must be punctured and cannulated. Further,
20 percutaneous cannulation of the carotid artery is very difficult and potentially fatal, due to the associated arterial wall trauma. Also, this method could not be used to cool organs such as the kidneys, where the renal arteries cannot be directly cannulated percutaneously.
25 Selective organ hypothermia has also been attempted by perfusing the organ with a cold solution, such as saline or perflourocarbons. This is commonly done to protect the heart during heart surgery and is referred to as cardioplegia. This procedure has a number of drawbacks, including lim
30 ited time of administration due to excessive volume accumulation, cost and inconvenience of maintaining the perfusate, and lack of effectiveness due to temperature dilution from the blood. Temperature dilution by the blood is a particular problem in high blood flow organs such as the
35 brain. For cardioplegia, the blood flow to the heart is minimized, and therefore this effect is minimized.
Intravascular, selective organ hypothermia, created by cooling the blood flowing into the organ, is the ideal method.
4Q First, because only the target organ is cooled, complications associated with total body hypothermia are avoided. Second, because the blood is cooled intravascularly, or in situ, problems associated with external circulation of blood are eliminated. Third, only a single puncture and arterial vessel
45 cannulation is required, and it can be performed at an easily accessible artery such as the femoral, subclavian, or brachial. Fourth, cold perfusate solutions are not required, thus eliminating problems with excessive fluid accumulation. This also eliminates the time, cost, and handling issues
5Q associated with providing and maintaining cold perfusate solution. Fifth, rapid cooling can be achieved. Sixth, precise temperature control is possible.
Previous inventors have disclosed the circulation of a cold fluid to produce total body hypothermia, by placing a probe
55 into a major vessel of the body. This approach is entirely unfeasible when considering selective organ hypothermia, as will be demonstrated below.
The important factor related to catheter development for selective organ hypothermia is the small size of the typical
60 feeding artery, and the need to prevent a significant reduction in blood flow when the catheter is placed in the artery. A significant reduction in blood flow would result in ischemic organ damage. While the diameter of the major vessels of the body, such as the vena cava and aorta, are as
65 large as 15 to 20 mm., the diameter of the feeding artery of an organ is typically only 4.0 to 8.0 mm. Thus, a catheter residing in one of these arteries cannot be much larger than
2.0 to 3.0 mm. in outside diameter. It is not practical to construct a selective organ hypothermia catheter of this small size using the circulation of cold water or other fluid. Using the brain as an example, this point will be illustrated.
The brain typically has a blood flow rate of approximately 5 500 to 750 cc/min. Two carotid arteries feed this blood supply to the brain. The internal carotid is a small diameter artery that branches off of the common carotid near the angle of the jaw. To cool the brain, it is important to place some of the cooling portion of the catheter into the internal carotid 1° artery, so as to minimize cooling of the face via the external carotid, since face cooling can result in complications, as discussed above. It would be desirable to cool the blood in this artery down to 32° C, to achieve the desired cooling of the brain. To cool the blood in this artery by a 5C.° drop, :5 from 37° C. down to 32° C, requires between 100 and 150 watts of refrigeration power.
In order to reach the internal carotid artery from a femoral insertion point, an overall catheter length of approximately 100 cm. would be required. To avoid undue blockage of the 20 blood flow, the outside diameter of the catheter can not exceed approximately 2 mm. Assuming a coaxial construction, this limitation in diameter would dictate an internal supply tube of about 0.70 mm. diameter, with return flow being between the internal tube and the external tube. 25
A catheter based on the circulation of water or saline operates on the principle of transferring heat from the blood to raise the temperature of the water. Rather than absorbing heat by boiling at a constant temperature like a freon, water 3Q must warm up to absorb heat and produce cooling. Water flowing at the rate of 5.0 grams/sec, at an initial temperature of 0° C. and warming up to 5° C, can absorb 100 watts of heat. Thus, the outer surface of the heat transfer element could only be maintained at 5° C, instead of 0° C. This will 3J require the heat transfer element to have a surface area of approximately 1225 mm2. If a catheter of approximately 2.0 mm. diameter is assumed, the length of the heat transfer element would have to be approximately 20 cm.
In actuality, because of the overall length of the catheter, 40 the water would undoubtedly warm up before it reached the heat transfer element, and provision of 0° C. water at the heat transfer element would be impossible. Circulating a cold liquid would cause cooling along the catheter body and could result in non-specific or total body hypothermia. 45 Furthermore, to achieve this heat transfer rate, 5 grams/sec of water flow are required. To circulate water through a 100 cm. long, 0.70 mm. diameter supply tube at this rate produces a pressure drop of more than 3000 psi. This pressure exceeds the safety levels of many flexible medical grade 50 plastic catheters. Further, it is doubtful whether a water pump that can generate these pressures and flow rates can be placed in an operating room.
The selective organ cooling achieved by the present invention is accomplished by placing a cooling catheter into the feeding artery of the organ. The cooling catheter is based on the vaporization and expansion of a compressed and condensed refrigerant, such as freon. In the catheter, a shaft 60 or body section would carry the liquid refrigerant to a distal heat transfer element where vaporization, expansion, and cooling would occur. Cooling of the catheter tip to temperatures above minus 2° C. results in cooling of the blood flowing into the organ located distally of the catheter tip, and 65 subsequent cooling of the target organ. For example, the catheter could be placed into the internal carotid artery, to
cool the brain. The size and location of this artery places significant demands on the size and flexibility of the catheter. Specifically, the outside diameter of the catheter must be minimized, so that the catheter can fit into the artery without compromising blood flow. An appropriate catheter for this application would have a flexible body of 70 to 100 cm. in length and 2.0 to 3.0 mm. in outside diameter.
It is important for the catheter to be flexible in order to successfully navigate the arterial path, and this is especially true of the distal end of the catheter. So, the distal end of the catheter must have a flexible heat transfer element, which is composed of a material which conducts heat better than the remainder of the catheter. The catheter body material could be nylon or PBAX, and the heat transfer element could be made from nitinol, which would have approximately 70 to 100 times the thermal conductivity of the catheter body material, and which is also superelastic. Nitinol could also be treated to undergo a transition to another shape, such as a coil, once it is placed in the proper artery. Certain tip shapes could improve heat transfer as well as allow the long tip to reside in arteries of shorter length.
The heat transfer element would require sufficient surface area to absorb 100 to 150 watts of heat. This could be accomplished with a 2 mm. diameter heat transfer tube, 15 to 18 cm. in length, with a surface temperature of 0° C. Fins can be added to increase the surface area, or to maintain the desired surface area while shortening the length.
The cooling would be provided by the vaporization and expansion of a liquid refrigerant, such as a freon, across an expansion element, such as a capillary tube. For example, freon R12 boiling at 1 atmosphere and a flow rate of between 0.11 and 0.18 liter/sec could provide between approximately 100 and 150 watts of refrigeration power. Utilizing a liquid refrigerant allows the cooling to be focused at the heat transfer element, thereby eliminating cooling along the catheter body. Utilizing boiling heat transfer to the expanded fluid also lowers the fluid flow rate requirement to remove the necessary amount of heat from the blood. This is important because the required small diameter of the catheter would have higher pressure drops at higher flow rates.
The catheter would be built in a coaxial construction with a 0.70 mm. inner supply tube diameter and a 2.0 mm. outer return tube diameter. This limits the pressure drops of the freon along the catheter length, as well as minimizing the catheter size to facilitate carotid placement. The inner tube would carry the liquid freon to the tubular heat transfer element at the distal end of the catheter body. If a heat transfer element surface temperature of 0° C. is maintained, just above the freezing point of blood, then 940 mm2 of surface area in contact with the blood are required to lower the temperature of the blood by the specified 5° C. drop. This translates to a 2.0 mm. diameter heat transfer tube by 15 cm. in length. To generate 0° C. on the nitinol surface, the freon must boil at a temperature of minus 28° C. It is important to have boiling heat transfer, which has a higher heat transfer coefficient, to maintain the surface temperature at 0° C. There are several freons that can be controlled to boil at minus 28° C, such as a 50/50 mixture of pentafluoroethane and 1,1,1 trifiuoroethane or a 50/50 mixture of difluoromethane and pentafluoroethane. The 50/50 mixture of pentafluoroethane and 1,1,1 trifiuoroethane would require a flow rate of approximately 7.0 liters/min or 0.52 gram/sec to absorb 100 watts of heat. At this flow rate, the pressure drop along the inner tube is less than 7 psi in 100 cm. of length, and the pressure drop along the outer tube is less than 21 psi in 100 cm. of length.
The inner supply tube of the catheter would be connected to a condenser, fed by the high pressure side of a compressor,