This application is a National Stage Entry entitled to and hereby claiming priority under 35 U.S.C. §§ 365 and 371 to corresponding PCT Application No. PCT/GB2016/053888, filed Dec. 9, 2016 entitled “A Dialysis Machine”, which in turn claims priority to G.B. Patent Application No.: 1523104.6, filed Dec. 30, 2015, entitled the same. The disclosures of the above applications are incorporated herein by reference in their entireties.
The present invention relates to a dialysis machine.
Dialysis is a treatment which replaces the renal function of removing excess fluid and waste products, such as potassium and urea, from blood. The treatment is either employed when renal function has deteriorated to an extent that uremic syndrome becomes a threat to the body's physiology (acute renal failure) or, when a longstanding renal condition impairs the performance of the kidneys (chronic renal failure).
There are two major types of dialysis, namely hemodialysis and peritoneal dialysis. In peritoneal dialysis treatment, a dialysate solution is run through a tube into the peritoneal cavity. The fluid is left in the cavity for a period of time in order to absorb the waste products, and is subsequently removed through the tube for disposal. It is common for patients in the early stages of treatment for a longstanding renal condition to be treated by peritoneal dialysis before progressing to hemodialysis at a later stage. In hemodialysis, the patient's blood is removed from the body by an arterial line and treated by a dialysis machine before being returned to the patient's body by a venous line. The machine passes the blood through a dialyser containing tubes formed from a semi-permeable membrane. On the exterior of the semi-permeable membrane is a dialysate solution. The semi-permeable membrane filters the waste products and excess fluid from the blood into the dialysate solution. The membrane allows the waste and a controlled volume of fluid to permeate into the dialysate solution whilst preventing the loss of larger more desirable molecules, like blood cells and certain proteins and polypeptides.
The action of dialysis across the membrane is achieved primarily by diffusion (the migration of molecules by random motion from a region of higher concentration to a region of lower concentration). Fluid removal (otherwise known as ultrafiltration) is achieved by altering the hydrostatic pressure of the dialysate solution side of the membrane, causing free water to move across the membrane along the pressure gradient. The correction of uremic acidosis of the blood is achieved by use of a bicarbonate buffer. The bicarbonate buffer also allows the correction of the blood bicarbonate level. The dialysate solution consists of a sterilized solution of mineral ions. These ions are contained within an acid buffer which is mixed with the purified water and bicarbonate base prior to delivery to the dialyser.
In use, the dialysate solution may be passed through the dialyser once before being discarded to ensure that the composition of the dialysate solution remains constant. However, this requires up to 120 litres of dialysate solution for each dialysis session. Alternatively, a closed loop fluid path dialysis machine may be used so as to reduce the amount dialysate solution required for a single session down to 6 to 10 litres. The reduced amount of dialysate solution required can be provided in a pre-mixed supply thus removing the requirement to connect the hemodialysis machine to a permanent source of purified water, for example water purified by reverse osmosis from a mains supply. The composition of recirculated dialysate solution needs to be tightly controlled to keep the patient's blood at an optimal composition.
Monitoring of the dialysate solution can be done by a range of means such as temperature and conductivity sensing as well as other methods. Typically, such measurements are taken with respect to an absolute reference point which may result in slight errors or uncertainties in the measurements due to minor differences between the material/solution used to record the absolute reference point and the material/solution used in the dialysis machine.
The present invention seeks to provide an improved hemodialysis machine.
A first aspect of the invention provides a hemodialysis machine comprising a fluid pathway for delivering a dialysate solution, wherein the fluid pathway comprises a pre-dialysis pathway and a post-dialysis pathway, a dialyser for dialysing patient's blood using the dialysate solution, the dialyser connected between the pre-dialysis pathway and the post-dialysis pathway, a first sensor system configured to sense a characteristic of the dialysate solution at a first location on the pre-dialysis pathway, a second sensor system configured to sense a characteristic of the dialysate solution at a second location on the post-dialysis pathway and a control system configured to make a comparative analysis of the measurements taken by the first sensor and the second sensor for monitoring the composition of the dialysate solution.
Advantageously, this arrangement can be used to measure the concentrations of dialysate, acid, sodium bicarbonate and water in their respective flow paths via comparative measurements without reliance on an absolute reference point. Additionally, this machine is also able to determine if there is a blood leak in any of the flow paths.
Preferably, the hemodialysis machine comprises a removable, mountable cartridge, wherein the cartridge defines the fluid pathway.
Provision of a cartridge as a consumable component, in combination with filtration of dialysate solution, allows for the hemodialysis machine to be optimised for convenient transportation with the patient. This is advantageous as typically a patient is required to be treated either at a medical facility or at home due to the large size of conventional hemodialysis machines. A smaller machine, similar to the size of a conventional desktop computer, would permit a patient to self-dialyse at any convenient location.
Where the machine is provided with a cartridge, the first sensor system preferably comprises a first sensor cell located on the cartridge and the second sensor system comprises a second sensor cell located on the cartridge.
Advantageously, providing the sensor cells on the removable cartridge.
The cartridge may comprise a dialyser outlet and the first sensor cell is located immediately upstream of said dialyser outlet.
The cartridge may comprise a dialyser inlet and the second sensor cell is located immediately downstream of said dialyser inlet.
Advantageously, this ensures that the dialysate is analysed at similar points along the flow path regardless of direction of flow of the dialysate. The first and second sensor systems may sense a characteristic of the dialysate solution by passing light through the solution. Alternatively, the first and second sensor systems may sense a characteristic of the dialysate solution by passing ultrasound through the solution.
The cartridge may comprise a cartridge drain outlet and a third sensor cell is located immediately upstream of the cartridge outlet port.
Advantageously, this enables the system to analyse the constituents of the dialysate when the machine is put into bypass mode so as to bypass the sensor cells. This can then be used as reference measurements for each component.
The cartridge may comprise a water inlet port and a fourth sensor cell located immediately downstream of the water inlet port.
Advantageously, this enables the RO water to be analysed when it enters the cartridge. This measurement can then be used as a comparison for the water in the dialysate and can, for example, be used to determine the efficiency of any water treatment/regeneration unit in the hemodialysis machine.
Each sensor cell preferably comprises a window formed in the cartridge.
Advantageously, this arrangement provides a more optically transparent region to reduce attenuation of a signal of a sensor.
The window may comprise a separate plastics material secured to the cartridge.
In that way, one may select the material for the window for each different type of sensor used.
The window may comprise a flexible membrane arranged to minimise unwanted reflections.
Advantageously, the flexible membrane is very thin and so results in greatly reduced attenuation of the sensor signal.
Where the hemodialysis machine comprises a platen and a door and wherein the cartridge is configured to be removably mountable between said platen and door, the door is capable of opening and closing relative to the platen so as to prevent any external light from entering the sensor cells.
Advantageously, this provides a simple way of blocking background light from entering the sensor cells.
Each sensor system may comprise a light source and a detector, wherein each detector is preferably located in the platen.
The light source may be located in the door or in the platen.
Each sensor system may comprise a reflective surface.
Advantageously, this enables reflective absorption spectroscopy to be utilised. This increases the flow path and hence the absorption which increases the overall sensitivity of the sensor. Multiple reflective surfaces in the system could further increase the sensitivity by further increasing the flow path through the fluid being measured.
The reflective surface is preferably provided on the door.
The hemodialysis machine may comprise an optical lever, preferably formed integrally with the cartridge.
At least one of the sensor cells may comprise a functional coating configured to react to the dialysate solution.
Advantageously, functional coatings can react with components of the dialysate solution, such as oxygen, in a measureable way, such as via fluorescence. This can enable the sensor systems to determine absolute quantities of components of the dialysate.
A particulate sensor configured to analyse the size distribution of particulate matter in the dialysate may be provided.
Advantageously, this enables the system to monitor whether there is a build of large particulate matter in the system which may cause blockages in the dialyser.
The hemodialysis machine may contain a fixed volume of dialysate solution.
The cartridge is disposable.
Advantageously, this enables the sensor cells to be disposed of after each use, ensuring that the sensor cells are clean for each session and reduces the need for cleaning processes to be carried out following each session. Furthermore, provision of a disposable cartridge permits the majority of the fluid components of the hemodialysis machine to be disposed of after each use, thus reducing the risk of contamination of infection occurring.
According to a second aspect of the invention, there is provided a cartridge for use in a hemodialysis machine, the cartridge defining a fluid pathway for delivering clean dialysate solution to a dialyser via a pre-dialysis pathway and for receiving used dialysate solution from the dialyser via a post dialysis pathway, the cartridge defining a sensor cell in the pre-dialysis pathway and a sensor cell in the post dialysis pathway.
Embodiments of the invention will now be described with reference to the accompanying drawings, in which:
In
The cartridge 30 has a platen side 31 and a door side 32. The platen side 31 engages the platen on the main body 2 of the machine 10, and the door side 32 engages the door 4 of the machine 10. The cartridge 30 is formed from an acrylic, such as SG-I0, which is moulded in two parts (the machine side and the patient side) before being bonded together. In this way a series of flow paths are formed in the cartridge 30 for carrying dialysate and its constituent parts of water, bicarbonate solution and acid solution. Both the platen side 31 and door side 32 are covered in a clear flexible membrane formed from, for example, DEHP-free PVC which is operable by pneumatic pressure applied to the membrane by a pneumatic compressor in the main body 2.
Referring to
The dialyser 12 has an inlet 20 for receiving clean dialysate solution and an outlet 22 for removing spent dialysate solution from the dialyser 12. The dialyser also has an inlet 24 for receiving untreated blood from the peristaltic pump 16 and an outlet 26 for returning processed blood to the patient. The dialyser 12 is typically provided in a substantially upright orientation, in use, with the patient's blood flowing longitudinally through the dialyser 12 from the blood inlet 24 to the blood outlet 26. The dialysate solution inlet 20 and dialysate solution outlet 22 are configured to be orientated substantially orthogonal to the blood inlet 24 and blood outlet 26, and to provide a counterflow. Dialysate solution is circulated through the hemodialysis machine 10 at a fluid flow rate in the region of 400 to 800 ml/min for approximately four hours.
The dialysis system defines a fluid circuit including a cartridge 30 as will now be described. The cartridge 30 is a consumable (i.e. disposable) component within the hemodialysis machine 10 described.
Referring to
A series of flow paths are formed in the cartridge 30 for carrying dialysate solution constituted from water, bicarbonate solution and acid solution. The flow paths are located between the sheet of material closing the machine side 31 of the cartridge 30 and a further sheet of the same material closing the patient side 32 of the cartridge 30.
In use, the variation of pressure applied to the flexible diaphragm of each pump chamber is controlled by conventional valving. A pressure source applies either a positive or negative pneumatic pressure to one side of the diaphragm of each pump chamber, as required, to pump fluid through the fluid paths in the cartridge 30, in a circuit defined by a plurality of valves.
The valves of the cartridge 30 are conventional diaphragm valves defined by respective openings in the cartridge 30 and closed by respective flexible diaphragms. Each valve is operable by applying a negative pressure to the diaphragm to open the valve and applying a positive pressure to the diaphragm to close the valve. The diaphragm of each valve is part of the single, common sheet of material applied to the machine side of the cartridge 30. The valves are opened and closed according to a flow control strategy, as will become apparent.
The machine side of the cartridge 30 abuts a pump driver (not shown) comprising a platen having a plurality of recessed surfaces, each recessed surface substantially corresponding in geometry and volume to a pump chamber defined in the cartridge 30. Each recessed surface has a fluid port connectable with a source of positive fluid pressure and, with a source of negative fluid pressure via a valve.
The positive and negative fluid pressure sources include a pressure pump and a vacuum pump respectively. When the valve is operated to allow fluid to flow into a recessed surface from the source of positive fluid pressure, the diaphragm moves into a corresponding pump chamber and any fluid, i.e. dialysate solution, therein is expelled from that pump chamber via the series of flow paths. When the valve is operated to allow fluid to flow out of a recessed surface to the source of negative fluid pressure, the diaphragm is moved away from a pump chamber and into the corresponding recessed surface to permit fluid to be drawn into that pump chamber via the series of flow paths. The surface of the pump chambers and of the platen provide a positive stop for each diaphragm, to prevent overstretching thereof. The positive stop ensures that the volume of fluid drawn into and pumped from the pump chambers is accurately controlled and remains constant during the dialysis session.
The cartridge 30 has two main functions, preparation of dialysate solution and flow balance. Each function is performed by a separate part of the cartridge 30 as illustrated in
The cartridge 30 is further provided with a plurality of connections to and from the cartridge 30. A first inlet port 38, from hereon referred to as the water inlet port, defined in the machine side of the cartridge 30 receives purified water from a purified water supply 31 such as a reverse osmosis (RO) water supply. A first outlet port 42, from hereon referred to as the water outlet port, defined in an edge of the cartridge 30 directs the purified water to a first dialysate solution constituent which, in the illustrated embodiment, is bicarbonate 46.
A second inlet port 50, from hereon referred to as the bicarbonate inlet port, defined in the same edge of the cartridge 30 as the water outlet port 42 receives purified water mixed with the bicarbonate 46.
A third inlet port 82, from hereon referred to as the acid inlet port, defined in the opposite edge of the cartridge 30 to the water outlet port 42 and bicarbonate inlet port 50 receives a second dialysate solution constituent which, in the illustrated embodiment, is acid 80 and enables the acid 80 to mix with the purified water mixed with bicarbonate 46.
A second outlet port 104, from hereon referred to as the clean dialysate solution outlet port, is defined in the same edge of the cartridge as the water outlet port 42 and the bicarbonate inlet port 50. The clean dialysate outlet port 104 directs clean dialysate solution to the dialyser 12. A fourth inlet port 106, from hereon referred to as the spent dialysate solution inlet port, is defined in the same edge of the cartridge 30 as the water outlet port 42, bicarbonate inlet port 50 and clean dialysate outlet port 104. The spent dialysate solution inlet port 106 receives spent dialysate solution from the dialyser 12.
A third outlet port 122, from hereon referred to as the drain port, is defined in the same edge of the cartridge as the acid inlet port 82. In the illustrated embodiment, the drain port 122 directs spent dialysate solution out of the cartridge 30.
Dialysate Preparation
Dialysate solution is prepared in the cartridge 30 by combining purified water with two dialysate constituents, namely a bicarbonate solution and an acid solution.
Purified water is admitted into the cartridge 30 from a purified water supply 31 via the water inlet port 38. The purified water passes through a channel 40 via a water inlet valve 41, when open, and exits the cartridge 30 at the water outlet port 42. The characteristics of the purified water is measured at water sensor cell 124, which in this embodiment, is located immediately upstream of the water inlet valve 41. By sensor cell, we mean a part configured to allow sensing of material contained therein or passing therethrough. The water sensor cell 124 is described in more detail below. However, it will be appreciated that the water sensor cell 124 may be positioned anywhere between the water inlet 38 and water outlet 42. Positioning the water sensor cell 124 proximate then the water outlet 42 enables the characteristics of the bicarbonate solution to be measured. If the bicarbonate solution is passed back through the bicarbonate cartridge 46 by closing bicarbonate mixing chamber valve 68. From here, the purified water is carried by a tube 44 through a bicarbonate cartridge 46 in a known manner to generate a purified water and bicarbonate solution. The purified water and bicarbonate solution is carried by a tube 48 and re-admitted into the cartridge 30 via the bicarbonate inlet port 50.
The temperature of the bicarbonate solution is measured at sensing port 52 and the bicarbonate solution pressure is measured at sensing port 54. The bicarbonate solution passes through a bicarbonate control valve 56, when open, before entering a bicarbonate solution reservoir 58 having an inlet and an outlet. The bicarbonate control valve 56 is closed when flow therethrough is not required.
A bicarbonate dosing pump chamber 60 having an inlet and an outlet receives the bicarbonate solution from the bicarbonate solution reservoir 58 through a bicarbonate dosing pump inlet valve 62. The bicarbonate dosing pump chamber 60 is closed by a diaphragm to define a bicarbonate dosing pump which, upon actuation of the diaphragm, pumps the bicarbonate solution from the bicarbonate dosing pump 60 to a first mixing pump chamber 66 (bicarbonate pump chamber). The bicarbonate dosing pump 60 has a bicarbonate dosing pump outlet valve 64 which is closed when the bicarbonate dosing pump inlet valve 62 is open. The bicarbonate dosing pump outlet valve 64 is opened to permit bicarbonate solution to be pumped to the bicarbonate pump chamber 66. When the bicarbonate dosing pump outlet valve 64 is open, the bicarbonate dosing pump inlet valve 62 is closed to prevent bicarbonate solution from being pumped back into the bicarbonate solution reservoir 58.
The bicarbonate pump chamber 66 having an inlet and an outlet receives the purified water and bicarbonate solution from the bicarbonate dosing pump 60 via a bicarbonate pump inlet valve 68. The bicarbonate pump inlet valve 68, when open, can also admit purified water into the bicarbonate pump chamber 66 from the water inlet port 38. The bicarbonate pump chamber 66 is closed by a diaphragm to define a pump which, upon actuation of the diaphragm, pumps the bicarbonate solution and purified water therein through a bicarbonate pump outlet valve 70 to a second mixing pump chamber 76 (acid pump).
When the bicarbonate pump inlet valve 68 is open, the bicarbonate pump outlet valve 70 and water outlet valve 41 are closed. When the bicarbonate pump outlet valve 70 is open, the bicarbonate pump inlet valve 68 is closed to prevent the bicarbonate and purified water solution from being pumped back into channel 40. From the bicarbonate pump outlet valve 70, the bicarbonate and purified water solution enters the acid pump chamber 76.
The acid pump chamber 76 having an inlet and an outlet receives the bicarbonate and purified water solution from the bicarbonate pump 66 via an acid pump inlet valve 78. The acid pump inlet valve 78, when open, can also admit an acid solution into the pump chamber 76. The acid pump chamber 76 is closed by a diaphragm to define a pump which, upon actuation of the diaphragm, pumps the acid solution, bicarbonate solution and purified water therein through an acid pump outlet valve 88 to the first flow balance pump chamber 100. When the acid pump inlet valve 78 is open, the acid pump outlet valve 88 is closed. When the acid pump outlet valve 88 is open, the acid pump inlet valve 78 is closed.
The acid solution is admitted into the cartridge 30 from a pre-determined supply of acid 80 via the acid solution inlet port 82. From the acid solution inlet port the acid solution passes through an acid dosing pump chamber 86 via an acid dosing pump inlet valve 84 and an acid dosing pump outlet valve 87. The acid dosing pump outlet valve 87 is closed when the acid dosing pump inlet valve 84 is open. The acid dosing pump inlet valve 84 is closed when the acid dosing pump outlet valve 87 is open.
The dialysate solution exits the acid pump chamber 76 via the acid pump outlet valve 88 and passes through a first dialysate solution sensor cell 130, described in more detail below, which is also known as a pre-flow balancer sensor cell. The sensor cell 130 is located upstream of both the first and second flow balance chambers 100, 108, i.e. prior to the separation of the single channel from the acid pump chamber 79 into two flow paths (one to each balance chamber).
Flow Balance
The flow balance function of the cartridge 30 provides first and second flow balance pump chambers 100, 108, each having two inlets and two outlets to define two independent flow paths therethrough. The first and second flow balance pump chambers 100, 108 are of approximately equal volume. Either the first or second flow balance pump chamber 100, 108 pumps dialysate solution to a dialyser 12 and the other of the first or second flow balance pump chambers 100, 108 pumps dialysate solution from the dialyser 12 to the drain port 122. After every approximately 20 strokes of the first and second flow balance pumps 100, 108, their function is reversed.
From this point onwards, dialysate solution will be referred to as either clean dialysate solution or spent dialysate solution. Clean dialysate solution is intended to mean dialysate solution that is either new dialysate solution or clean dialysate solution that has been treated to remove waste product therefrom. Spent dialysate solution is intended to mean dialysate solution that has passed through the dialyser 12 to remove waste fluids from a patients' blood into the dialysate solution.
Each of the first and second flow balance pump chambers 100, 108 are closed by a diaphragm to define respective pumps. The diaphragm is actuated away from a pump chamber by a negative pressure source to draw a volumetrically measured quantity of dialysate solution into the pump chamber. The diaphragm is actuated toward the pump chamber to pump the fluid therein out of an outlet.
The first flow balance pump chamber 100 has a clean dialysate solution inlet valve 98 for receiving clean dialysate solution from the acid pump 76 and a clean dialysate solution outlet valve 102 for pumping clean dialysate solution to the dialyser 12. The first flow balance pump chamber 100 also has a spent dialysate solution inlet valve 118 for receiving spent dialysate from the dialyser 12 and a spent dialysate solution outlet valve 120 for pumping the spent dialysate to drain via drain outlet port 122.
At any one time, only one of valves 98, 102, 118 or 120 will be open and the other three valves will be closed. The flow balance function, as described above, requires alternating the function of each flow balance pump approximately every 20 cycles. Therefore, when the first flow balance pump 100 is pumping clean dialysate solution to the dialyser 12, only valves 98 and 102 are in use and when the first flow balance pump 100 is pumping spent dialysate solution from the dialyser 12 to drain, only valves 118 and 120 will be in use.
The clean dialysate solution is pumped out of the first flow balance pump chamber 100 through the first flow balance pump clean dialysate solution outlet valve 102, upon closure of the first flow balance pump clean dialysate inlet valve 98, to the dialyser 12 via the dialyser outlet port 104. Prior to passing through the dialyser outlet point 104, the clean dialysate passes through a second dialysate sensor cell 136, also known as a pre-dialyser sensor cell, to characterise the clean dialysate solution. The second dialysate sensor cell 136 is located upstream, preferably immediately upstream, of said outlet point 104. A second clean dialysate sensor cell 136 is provided to corroborate the provided by measurements taken at the first dialysate sensor cell 130 and to ensure that no contamination of the clean dialysate solution has occurred in the flow balance chambers 100, 108.
Spent dialysate solution returns to the cartridge 30 from the dialyser 12 via the dialyser inlet port 106 and flows through a spent dialysate sensor cell 142, also known as a post-dialyser sensor cell. The spent dialysate sensor cell 142 is provided so as to characterise the spent dialysate when it returns to the cartridge 30, this enables the detection of contaminants such as blood which may be present in the dialysate solution after passing through the dialyser 12. Provision of two sensor cells 130, 136 allows a comparison to be made between two locations, i.e. pre and post the dialyser 12, rather than against absolute values.
The second flow balance pump chamber 108 has a spent dialysate solution inlet valve 110 for receiving spent dialysate solution from the dialyser 12 and a spent dialysate solution outlet valve 112 for pumping the spent dialysate solution to drain via drain outlet port 122. The second flow balance pump 108 also has a clean dialysate solution inlet valve 114 for receiving clean dialysate solution from the acid pump chamber 76 and a clean dialysate solution outlet valve 116 for pumping clean dialysate solution to the dialyser 12.
At any one time, only one of valves 110, 112, 114, 116 will be open and the other three valves will be closed. When the second flow balance pump 108 is pumping clean dialysate solution to the dialyser 12, only valves 114 and 116 will be in use and when the second flow balance pump 108 is pumping spent dialysate solution from the dialyser 12 to drain, only valves 114 and 116 will be in use.
In the illustrated example, the operation of the first and second flow balance pumps 100, 108 can be switched so that the first flow balance pump 100 is used to draw spent dialysate solution from the dialyser 12 and the second flow balance pump 108 is used to pump clean dialysate solution into the dialyser 12 as described below.
The clean dialysate solution is drawn into the second flow balance pump chamber 108 from the acid pump 76 via the second flow balance pump clean dialysate solution inlet valve 114 upon actuation of the diaphragm. The clean dialysate solution is then pumped from the second flow balance pump chamber 108 via the second flow balance pump clean dialysate solution outlet valve 116, upon closure of the clean dialysate solution inlet valve 114, to the dialyser 12.
Spent dialysate solution from the dialyser 12 is drawn into the first flow balance pump 100 via the second flow balance pump spent dialysate solution inlet valve 118. The spent dialysate solution is then pumped out of the first flow balance pump chamber 100 via the second flow balance pump spent dialysate solution outlet valve 120, upon closure of the spent dialysate solution inlet valve 118, to drain via drain outlet port 122. Prior to flowing to drain, the spent dialysate solution passes through drain sensor cell 148 located upstream, preferably immediately upstream, of the drain outlet 122. Using various combinations of the valves and pumps it is possible to flow the acid, bicarbonate solution, or purified water through the cartridge 30 without passing through the dialyser 12. Providing a single sensor proximate to the drain valve 122, preferably immediately upstream of said drain valve, then each component, or several of the components combined can be sensed prior to enabling the solution to flow to the dialyser 12. Alternatively, a separate sensor system could be provided for each of the components of the dialysate solution.
The system may be configured to run in a bypass mode periodically, such as hourly, where each of the components will be passed through the cartridge and characterised at 122 so as to check the reference measurements of the system so as to recalibrate the sensing system of the dialysis machine. This removes the dependence of the sensor systems of the machine 10 from dependence on absolute values.
The volume of fluid that is returned from the dialyser 12 is greater than the volume of fluid that is pumped to the dialyser via the first or second flow balance pump 100, 108. The first and second flow balance pumps have fixed volumes meaning that the excess fluid volume cannot be accommodated in the first or second flow balance pump. An ultrafiltration pump 200 is provided between the first and second flow balance pumps 100, 108 and has an inlet valve 202 and an outlet valve 204. The ultrafiltration pump 200 comprises a concave recess in the cartridge closed by a flexible diaphragm, the concave recess and the flexible diaphragm defining an ultrafiltration pump chamber.
In use, the inlet valve 202 of the ultrafiltration pump 200 is opened to allow the ultrafiltration pump 200 to draw in a pre-determined volume of spent dialysate solution. When the inlet valve 202 of the ultrafiltration pump 200 is open, the outlet valve 204 of the ultrafiltration pump 200 is closed. When the ultrafiltration pump 200 has received a volume of spent dialysate solution, the outlet valve 204 is opened and the spent dialysate solution in the ultrafiltration pump chamber is pumped through the outlet valve 204 to drain via the drain outlet port 122. When the outlet valve 204 of the ultrafiltration pump 200 is open, the inlet valve 202 of the ultrafiltration pump 200 is closed.
Regeneration
In
At the beginning of a dialysis session, the hemodialysis machine is primed with a known quantity of pre-mixed dialysate solution or purified water via flow input ports 170 or 174. The input port(s) 170, 174 for the pre-mixed dialysate solution and purified water are located at an elevation higher than the highest elevation of the hemodialysis machine.
If purified water is used to prime the hemodialysis machine, the purified water is circulated through the hemodialysis machine prior to connection to the patient to dose the purified water in a known manner by circulating the purified water through a dialysate regeneration device.
Instead of spent dialysate solution being pumped to drain via the drain outlet port 122,
In the illustrated embodiment, the dialysate regeneration device 154 comprises a material, such as sorbent, within a container that has a spent dialysate solution inlet 156 and a clean dialysate solution outlet 158. The spent dialysate solution is pumped through the sorbent to regenerate the spent dialysate solution in a known manner.
“Ultrafiltrate” is intended to mean the waste product which is removed from a patients blood into the dialysate solution during hemodialysis treatment.
The dialysate regeneration device 154 sets the proportion of the base constituent parts, i.e. acid and bicarbonate, in the dialysate solution after removal of ultrafiltrate from the dialysate solution. The clean dialysate solution, after regeneration, is of greater volume in the system than at the beginning of the dialysis session. The excess liquid in the system is removed via an overflow device 162 provided in a reservoir 160.
Sodium bicarbonate is a natural food source for biofilm which can cause bio-incompatibility and unacceptable errors in clean dialysate solution dosing and control. An endotoxin filter 176 is provided downstream of the reservoir 160 for removing biofilm flushed through the clean dialysate solution fluid circuit by the dialysate solution.
The clean dialysate solution having been filtered and potentially stored in the reservoir for a period of time is likely to be at a temperature below that of the human body. A heater 178 may be provided downstream of the endotoxin filter 176 for heating the clean dialysate solution to a temperature of about 37° C. before being passed through an air vent 180 to remove any bubbles from the clean dialysate solution.
The clean dialysate solution passes through the sensor cell 136 which analyses the ‘clean’ dialysate solution and compares the measurement with earlier measurements to determine the efficiency of the regeneration device by detecting the presence of any contaminants, such as urea, in the dialysate solution. This removes the need for any additional separate sensors.
The acid supply is replaced with a sodium chloride supply 186 for adjusting the clean dialysate solution on each pass of the dialysate solution through the cartridge 30 in accordance with a measurement taken in the sensor cell 136 and by the sensors 52, 54. The acid dosing pump 86 pumps sodium chloride to the acid pump 76 which in turn pumps homogenous, clean dialysate solution to the first flow balance pump 100. The flow balance pumps 100, 108 operate as described previously.
Dialysate Solution Recirculation
In situations where neither filtration equipment nor a continuous purified water supply are available, a single pre-mixed supply of clean dialysate solution 170 can be re-circulated through the hemodialysis machine. By re-circulating the dialysate solution at a comparatively slow speed, i.e. between 100 ml/min and 300 ml/min, configured to saturate the semi-permeable diaphragm of the dialyser 12 with dialysate solution, the dialysate solution remains viable for a number of cycles through the hemodialysis machine. A pre-mixed supply of dialysate solution 170 is provided in a vessel.
In one embodiment, the dialysate solution is circulated through the hemodialysis machine at 100 ml/min and saturates the semi-permeable membrane of the dialyser within one pass of dialysate solution through the hemodialysis machine. The vessel holds a volume of dialysate solution in the order of 60 litres with approximately 25 litres of dialysate solution being circulated through the hemodialysis machine in a single dialysis session.
In another embodiment, the dialysate solution is circulated through the hemodialysis machine at 200 to 300 ml/min and saturates the semi-permeable membrane of the dialyser after a number of passes of dialysate solution through the hemodialysis machine. The vessel holds a volume of pre-mixed dialysate solution in the order of 20 litres for approximately two hours. The dialysate solution is re-circulated through the hemodialysis machine a number of times.
Referring to
i) Connecting the drain port 122 to the clean dialysate inlet port 38;
ii) Disconnecting and blocking the acid inlet port 82;
iii) Connecting the water outlet port 42 to the bicarbonate inlet port 50;
iv) Priming the hemodialysis machine with pre-mixed clean dialysate solution and purified water;
v) Connecting the clean dialysate outlet port to the inlet of the dialyser;
vi) Connecting the outlet of the dialyser to the spent dialysate solution inlet port and,
v) Flowing dialysate solution through the hemodialysis machine 10 at a fluid flow rate configured to saturate the semi-permeable diaphragm of the dialyser 12.
The reservoir, as described with reference to
Structure of the Sensor Cells
Referring to
In the illustrated embodiment, both the platen and door sides of the sensor cell 124 include a window, e.g. an aperture, in the cartridge 30, that is covered in a clear flexible membrane. The sensor cell membrane may be formed from the same material as the membrane and may be formed from the same membrane that covers the flow chambers, although, in alternative arrangements, the membrane may be separate from the membrane and/or may be a different material thereto. The membrane of the sensor cells is able to be secured to the platen by use of a vacuum so as to provide a flat surface which works to provide a uniform transmission of the optical signal and minimises reflectance of the signal. Similarly, the membrane of the sensor cells is able to be secured to the door by use of a vacuum. Use of a different material for the platen and door sides of the sensor cells to the material used to produce the cartridge 30 reduces the amount of attenuation of the optical signal, which occurs when passing through the cartridge material.
The light for each of the sensor systems of the dialysis machine is provided from a single light source which is split off, e.g. by the use of optical fibres, to direct the optical signal to each of the sensor systems. This enables the light source, i.e. the emission spectra, of the light source for each sensor system to be identical. In alternative arrangements, the light source of each sensor system may be separate components, such as LEDs, which are able to produce a very reproducible emission spectra.
The detector 125 is in the form an optical spectrometer, located in the platen of the main body 2 of the dialysis machine 10, and the light source 126 is provided in the door 4 of the dialysis machine. The detector 125 and light source 126 are arranged so as to oppose each other and have a sensor cell 124 positioned therebetween, as is shown in
Additionally, providing sensors on both the clean dialysate and spent dialysate lines ensures that the system does not need to take regular background light readings as any background light that is present in the readings will simply be eliminated by virtue of the comparison when the readings are compared.
With reference to
The light frequency used may be ultra violet, visible light or near infrared. Instead of light absorption or reflectance, characteristics of the fluid may be determined from measuring its refractive index.
It will be appreciated that although the structure of the sensor systems of
In embodiments including refraction spectroscopy or ultrasonic sensing, the measurements recorded by the sensor cells may use the measurements taken by the temperature sensor 52 temperature readings further to increase the accuracy of the systems and account for changes in the refractive index or the speed of sound through a medium which occur due to changes in temperature.
The morphology of the cartridge may be modified so as further to increase the sensitivity of the sensor systems. A structure may be provided so as to collimate the light from the source, which can help to improve resolution. Alternatively, a structure, e.g a raised smooth, curved surface may be provided to amplify any changes in the signal produced by changes in the dialysate, e.g. an optical lever may be provided within the sensor cell.
In a further alternative arrangement, the window(s) of the sensor cell may be covered by a plastics material which is separate from and secured to, e.g. by welding, the cartridge.
It some embodiments, the system may have different pairs of sensors. i.e. transmission, reflectance, ultrasonic, and these could all be used to check against the others.
Each of the sensor cells may further be provided with a coating on at least one surface, where the coating is an active substance designed to emit a measurable characteristic upon interaction with a component of the dialysate solution. Such an active coating could be designed to fluoresce upon interaction with Oxygen, which would allow the sensor systems to monitor proper de-aeration of the dialysate solution.
The dialysis system may further be provided with a sensor for sensing any particulate matter present in the dialysate solution. For example an additional flow cell may be provided for such a measurement. In one embodiment, the sensing could be done using dynamic light scattering so as to sense the distribution of any particulate matter
In the embodiments described above, the sensor systems are configured to provide continuous measurement of the dialysate solution, this enables the system to provide immediate feedback if the dialysate solution is found to be contaminated, e.g. by urea or blood in the solution. However, the sensor may alternatively be configured periodically to sense the solutions.
Number | Date | Country | Kind |
---|---|---|---|
1523104 | Dec 2015 | GB | national |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/GB2016/053888 | 12/9/2016 | WO |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2017/115069 | 7/6/2017 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
2696173 | Thormod | Dec 1954 | A |
3338171 | Conklin et al. | Aug 1967 | A |
3468261 | Schmierer | Sep 1969 | A |
3605566 | Vetter | Sep 1971 | A |
3606592 | Madurski et al. | Sep 1971 | A |
3753493 | Mellor | Aug 1973 | A |
3774762 | Lichtenstein | Nov 1973 | A |
3807906 | Breit | Apr 1974 | A |
3921622 | Cole | Nov 1975 | A |
3972320 | Kalman | Aug 1976 | A |
4070725 | Austin et al. | Jan 1978 | A |
4142845 | Lepp et al. | Mar 1979 | A |
4161264 | Malmgren | Jul 1979 | A |
4205686 | Harris et al. | Jun 1980 | A |
4353990 | Manske et al. | Oct 1982 | A |
4366061 | Papanek et al. | Dec 1982 | A |
4368261 | Klose et al. | Jan 1983 | A |
4370983 | Lichtenstein | Feb 1983 | A |
4430048 | Fritsch | Feb 1984 | A |
4494912 | Pauliukonis | Jan 1985 | A |
D277991 | Becker | Mar 1985 | S |
4534755 | Calvert et al. | Aug 1985 | A |
4534756 | Nelson | Aug 1985 | A |
4546669 | Fischer et al. | Oct 1985 | A |
4564342 | Weber et al. | Jan 1986 | A |
4599165 | Chevallet | Jul 1986 | A |
4648869 | Bobo, Jr. | Mar 1987 | A |
4666598 | Heath et al. | May 1987 | A |
4710163 | Butterfield | Dec 1987 | A |
4771792 | Seale | Sep 1988 | A |
4828543 | Weiss et al. | May 1989 | A |
4897184 | Shouldice et al. | Jan 1990 | A |
D308249 | Buckley | May 1990 | S |
4969991 | Valadez | Nov 1990 | A |
5000664 | Lawless et al. | Mar 1991 | A |
5012197 | Seiffert et al. | Apr 1991 | A |
5032265 | Jha et al. | Jul 1991 | A |
5055198 | Shettigar | Oct 1991 | A |
5095910 | Powers | Mar 1992 | A |
5103211 | Daoud et al. | Apr 1992 | A |
5126831 | Nakagawara | Jun 1992 | A |
5232434 | Inagaki et al. | Aug 1993 | A |
5252213 | Ahmad et al. | Oct 1993 | A |
D341890 | Sievert et al. | Nov 1993 | S |
D344339 | Yoshikawa et al. | Feb 1994 | S |
5304349 | Polaschegg | Apr 1994 | A |
D347896 | Dickinson et al. | Jun 1994 | S |
D351470 | Scherer et al. | Oct 1994 | S |
5385540 | Abbott et al. | Jan 1995 | A |
5421823 | Kamen et al. | Jun 1995 | A |
5458468 | Ye et al. | Oct 1995 | A |
5476368 | Rabenau et al. | Dec 1995 | A |
5476792 | Ezrielev et al. | Dec 1995 | A |
D370979 | Pascale et al. | Jun 1996 | S |
5558347 | Nicholson | Sep 1996 | A |
5586872 | Skobelev et al. | Dec 1996 | A |
5586873 | Novak et al. | Dec 1996 | A |
5591344 | Kenley | Jan 1997 | A |
5643201 | Peabody et al. | Jul 1997 | A |
5650071 | Brugger et al. | Jul 1997 | A |
5653456 | Mough | Aug 1997 | A |
5658456 | Kenley et al. | Aug 1997 | A |
5665307 | Kirschner et al. | Sep 1997 | A |
5727550 | Montecalvo | Mar 1998 | A |
D395085 | Kenley et al. | Jun 1998 | S |
5788851 | Kenley et al. | Aug 1998 | A |
5807322 | Lindsey et al. | Sep 1998 | A |
5882300 | Malinouskas et al. | Mar 1999 | A |
5948247 | Gillerfalk et al. | Sep 1999 | A |
5957670 | Duncan et al. | Sep 1999 | A |
5995910 | Discenzo | Nov 1999 | A |
6077443 | Goldau | Jun 2000 | A |
6126831 | Goldau et al. | Oct 2000 | A |
6132378 | Marino | Oct 2000 | A |
6143181 | Falkvall et al. | Nov 2000 | A |
6153102 | Kenley et al. | Nov 2000 | A |
6216029 | Paltieli | Apr 2001 | B1 |
6218329 | Singh et al. | Apr 2001 | B1 |
6251279 | Peterson et al. | Jun 2001 | B1 |
6261065 | Nayak et al. | Jul 2001 | B1 |
6303036 | Collins et al. | Oct 2001 | B1 |
6382923 | Gray | May 2002 | B1 |
6514462 | Simons | Feb 2003 | B1 |
6558347 | Jhuboo et al. | May 2003 | B1 |
6582206 | Schluecker | Jun 2003 | B2 |
6626832 | Paltieli et al. | Sep 2003 | B1 |
6626878 | Leisner et al. | Sep 2003 | B1 |
6645176 | Christenson et al. | Nov 2003 | B1 |
6663829 | Kjellstrand | Dec 2003 | B1 |
6733476 | Christenson et al. | May 2004 | B2 |
6743204 | Christenson et al. | Jun 2004 | B2 |
6801646 | Pena et al. | Oct 2004 | B1 |
6814547 | Childers et al. | Nov 2004 | B2 |
6967002 | Edgson et al. | Nov 2005 | B1 |
7040142 | Burbank | May 2006 | B2 |
7107837 | Lauman et al. | Sep 2006 | B2 |
7153286 | Busby et al. | Dec 2006 | B2 |
7220358 | Schacht et al. | May 2007 | B2 |
7284964 | McDowell et al. | Oct 2007 | B2 |
7383721 | Parsons et al. | Jun 2008 | B2 |
7434312 | Christenson et al. | Oct 2008 | B2 |
7494590 | Felding et al. | Feb 2009 | B2 |
7604398 | Akers et al. | Oct 2009 | B1 |
7648627 | Beden et al. | Jan 2010 | B2 |
7857976 | Bissler et al. | Dec 2010 | B2 |
7874999 | Busby | Jan 2011 | B2 |
7896197 | Furey et al. | Mar 2011 | B2 |
D641882 | Hickey et al. | Jul 2011 | S |
8114043 | Muller | Feb 2012 | B2 |
8132388 | Nagy et al. | Mar 2012 | B2 |
8137184 | Ajiro et al. | Mar 2012 | B2 |
8137300 | Han et al. | Mar 2012 | B2 |
8167431 | DeCusatis et al. | May 2012 | B2 |
8187184 | Muller et al. | May 2012 | B2 |
8192388 | Hogard | Jun 2012 | B2 |
8197431 | Bennison | Jun 2012 | B2 |
8221320 | Bouton | Jul 2012 | B2 |
8348850 | Frinak et al. | Jan 2013 | B2 |
8360977 | Marttila et al. | Jan 2013 | B2 |
8529490 | Wariar et al. | Sep 2013 | B2 |
8535522 | Fulkerson et al. | Sep 2013 | B2 |
8535525 | Heyes et al. | Sep 2013 | B2 |
D693469 | Chung et al. | Nov 2013 | S |
8597505 | Fulkerson et al. | Dec 2013 | B2 |
D702842 | Hyde et al. | Apr 2014 | S |
8685244 | Heyes et al. | Apr 2014 | B2 |
8696571 | Marttila et al. | Apr 2014 | B2 |
8708908 | Bouton | Apr 2014 | B2 |
8708946 | Han et al. | Apr 2014 | B2 |
D705432 | Lura et al. | May 2014 | S |
8798908 | Bourdeaut | Aug 2014 | B2 |
8801646 | Han et al. | Aug 2014 | B2 |
D714454 | Amemiya et al. | Sep 2014 | S |
D714946 | Lura et al. | Oct 2014 | S |
8926544 | Hogard | Jan 2015 | B2 |
D724740 | Collins et al. | Mar 2015 | S |
8974394 | Frinak et al. | Mar 2015 | B2 |
9011334 | Bouton | Apr 2015 | B2 |
D735868 | Mareguddi et al. | Aug 2015 | S |
9220825 | Buckberry | Dec 2015 | B2 |
D781410 | Ritter et al. | Mar 2017 | S |
9744285 | Heyes et al. | Aug 2017 | B2 |
9833553 | Higgitt et al. | Dec 2017 | B2 |
10456516 | Heyes et al. | Oct 2019 | B2 |
D867597 | Bauer et al. | Nov 2019 | S |
10543305 | Buckberry et al. | Jan 2020 | B2 |
D879967 | Verguldi et al. | Mar 2020 | S |
D907211 | Spurling | Jan 2021 | S |
10881775 | Wallace | Jan 2021 | B2 |
10960120 | Wallace et al. | Mar 2021 | B2 |
D924410 | Mendoza et al. | Jul 2021 | S |
D938046 | Gupta et al. | Dec 2021 | S |
11365728 | Westenbrink | Jun 2022 | B2 |
20030217962 | Childers et al. | Nov 2003 | A1 |
20040195157 | Mullins et al. | Oct 2004 | A1 |
20040206703 | Bosetto et al. | Oct 2004 | A1 |
20040215129 | Edgson et al. | Oct 2004 | A1 |
20040223857 | Kline | Nov 2004 | A1 |
20050020961 | Burbank et al. | Jan 2005 | A1 |
20050205476 | Chevallet et al. | Sep 2005 | A1 |
20050209547 | Burbank et al. | Sep 2005 | A1 |
20050234384 | Westberg et al. | Oct 2005 | A1 |
20060121623 | He | Jun 2006 | A1 |
20070083193 | Werneth et al. | Apr 2007 | A1 |
20080006089 | Adnan et al. | Jan 2008 | A1 |
20080283096 | Scheringer et al. | Nov 2008 | A1 |
20090007642 | Busby et al. | Jan 2009 | A1 |
20090009290 | Kneip et al. | Jan 2009 | A1 |
20090012450 | Shah et al. | Jan 2009 | A1 |
20090012452 | Slepicka et al. | Jan 2009 | A1 |
20090012457 | Childers et al. | Jan 2009 | A1 |
20090101550 | Muller | Apr 2009 | A1 |
20090211975 | Brugger et al. | Aug 2009 | A1 |
20090230043 | Heyes et al. | Sep 2009 | A1 |
20100043694 | Patel | Feb 2010 | A1 |
20100045471 | Meyers | Feb 2010 | A1 |
20100089807 | Heyes et al. | Apr 2010 | A1 |
20100139254 | Sebestyen et al. | Jun 2010 | A1 |
20100263687 | Braun et al. | Oct 2010 | A1 |
20110009797 | Kelly et al. | Jan 2011 | A1 |
20110034850 | Jonsson | Feb 2011 | A1 |
20110132838 | Curtis et al. | Jun 2011 | A1 |
20110168614 | Pouchoulin et al. | Jul 2011 | A1 |
20120164022 | Muginstein et al. | Jun 2012 | A1 |
20120269907 | Coates | Oct 2012 | A1 |
20120276549 | Cunningham | Nov 2012 | A1 |
20120292237 | Heyes | Nov 2012 | A1 |
20120308431 | Kotsos et al. | Dec 2012 | A1 |
20130037465 | Heyes et al. | Feb 2013 | A1 |
20130056419 | Curtis | Mar 2013 | A1 |
20130153495 | Kelly et al. | Jun 2013 | A1 |
20130199998 | Kelly et al. | Aug 2013 | A1 |
20130274642 | Soykan | Oct 2013 | A1 |
20140224736 | Heide | Aug 2014 | A1 |
20140251885 | Heyes | Sep 2014 | A1 |
20140271106 | Alessandro et al. | Sep 2014 | A1 |
20140299544 | Wilt et al. | Oct 2014 | A1 |
20150027951 | Wallace et al. | Jan 2015 | A1 |
20150076053 | Higgitt et al. | Mar 2015 | A1 |
20150112119 | Buckberry | Apr 2015 | A1 |
20150129481 | Higgitt et al. | May 2015 | A1 |
20150238673 | Gerber et al. | Aug 2015 | A1 |
20150258263 | Hogard | Sep 2015 | A1 |
20150352269 | Gerber | Dec 2015 | A1 |
20150359954 | Gerber et al. | Dec 2015 | A1 |
20160045656 | Buckberry | Feb 2016 | A1 |
20160051743 | Buckberry | Feb 2016 | A1 |
20160058933 | Ballantyne | Mar 2016 | A1 |
20160076535 | Clifton et al. | Mar 2016 | A1 |
20160077644 | Ritter et al. | Mar 2016 | A1 |
20170056576 | Doyle et al. | Mar 2017 | A1 |
20170167983 | Klomp | Jun 2017 | A1 |
20170252498 | Heyes et al. | Sep 2017 | A1 |
20170296730 | Soto et al. | Oct 2017 | A1 |
20180133391 | Heyes et al. | May 2018 | A1 |
20180154059 | Heyes et al. | Jun 2018 | A1 |
20180193545 | Crnkovich et al. | Jul 2018 | A1 |
20180344915 | Wallace | Dec 2018 | A1 |
20190001042 | Buckberry | Jan 2019 | A1 |
20190015577 | Garrido et al. | Jan 2019 | A1 |
20190024654 | May et al. | Jan 2019 | A1 |
20190358381 | Westenbrink | Nov 2019 | A1 |
20190374698 | Buckberry et al. | Dec 2019 | A1 |
20190376504 | Westenbrink | Dec 2019 | A1 |
20190385434 | Yuds et al. | Dec 2019 | A1 |
20200030515 | Merchant | Jan 2020 | A1 |
20200075159 | Bardorz et al. | Mar 2020 | A1 |
20200268958 | Heyes et al. | Aug 2020 | A1 |
20200330671 | Buckberry et al. | Oct 2020 | A1 |
20210110920 | Heyes et al. | Apr 2021 | A1 |
20220001087 | Heyes et al. | Jan 2022 | A1 |
20220160943 | Buckberry et al. | May 2022 | A9 |
20220241480 | Fincham | Aug 2022 | A1 |
20220241573 | Fincham | Aug 2022 | A1 |
Number | Date | Country |
---|---|---|
81430 | Aug 1997 | CA |
10024447 | Nov 2001 | DE |
EU0043757640001 | Oct 2017 | EM |
EU0043757640002 | Oct 2017 | EM |
EU0079551250002 | Jun 2020 | EM |
0165751 | Dec 1985 | EP |
0754468 | Jan 1997 | EP |
2219703 | Aug 2010 | EP |
2955512 | Dec 2015 | EP |
2310136 | Dec 1976 | FR |
90079551250001 | May 2020 | GB |
90079551250002 | May 2020 | GB |
H04266740 | Sep 1992 | JP |
H06261872 | Sep 1994 | JP |
H07174659 | Jul 1995 | JP |
2000130334 | May 2000 | JP |
1645323 | Nov 2020 | JP |
WO 8101800 | Jul 1981 | WO |
WO-9100113 | Jan 1991 | WO |
WO-9116542 | Oct 1991 | WO |
WO 9506205 | Mar 1995 | WO |
WO 9525893 | Sep 1995 | WO |
WO-9625214 | Aug 1996 | WO |
WO-9710013 | Mar 1997 | WO |
WO-9728368 | Aug 1997 | WO |
WO-9929356 | Jun 1999 | WO |
WO 2000006217 | Feb 2000 | WO |
WO-0057935 | Oct 2000 | WO |
WO-02066833 | Aug 2002 | WO |
WO-02081917 | Oct 2002 | WO |
WO 2003101510 | Dec 2003 | WO |
WO-2005044339 | May 2005 | WO |
WO-2005080794 | Sep 2005 | WO |
2006120415 | Nov 2006 | WO |
WO 2006120417 | Nov 2006 | WO |
WO-2008100671 | Aug 2008 | WO |
WO-2008106191 | Sep 2008 | WO |
WO-2008135245 | Nov 2008 | WO |
WO-2009006489 | Jan 2009 | WO |
WO-2009024333 | Feb 2009 | WO |
WO-2009038834 | Mar 2009 | WO |
WO 2009061608 | May 2009 | WO |
WO-2009127624 | Oct 2009 | WO |
WO-2010089130 | Aug 2010 | WO |
WO-2010146343 | Dec 2010 | WO |
WO-2011027118 | Mar 2011 | WO |
WO-2011068885 | Jun 2011 | WO |
WO-2011105697 | Sep 2011 | WO |
WO-2011105698 | Sep 2011 | WO |
WO 2013057109 | Apr 2013 | WO |
WO-2013052680 | Apr 2013 | WO |
WO 2013110906 | Aug 2013 | WO |
WO 2013110919 | Aug 2013 | WO |
WO 2013114063 | Aug 2013 | WO |
WO-2013121162 | Aug 2013 | WO |
WO-2013121163 | Aug 2013 | WO |
WO 2014072195 | May 2014 | WO |
WO-2014082855 | Jun 2014 | WO |
2014155121 | Oct 2014 | WO |
WO 2015007596 | Jan 2015 | WO |
WO 2015022537 | Feb 2015 | WO |
WO 2016016870 | Feb 2016 | WO |
WO-2017137723 | Aug 2017 | WO |
WO-2018115816 | Jun 2018 | WO |
Entry |
---|
Huarui He, Mark A. Mortellaro, Marc J. P. Leiner, Robert J. Fraatz, and James K. Tusa Journal of the American Chemical Society 2003 125 (6), 1468-1469 DOI: 10.1021/ja0284761 (Year: 2003). |
International Search Report and Written Opinon issued for International Application No. PCT/GB2016/053888, dated Feb. 20, 2017. |
Kivi, Air Embolism, Healthline, Aug. 20, 2012, p. 1-5. |
Ergo-Express Motorized Dialysis Cart, Aug. 14, 2017, youtube.com [online], [site visited Jan. 9, 2022], Available from internet, URL: https://www.youtube.com/watch?v=j4rAXthOmbY (Year: 2017). |
Home Dialysis Tescon Aqua Tech, Aug. 1, 2020, youtube.com [online], [site visited Jan. 9, 2022], Available from internet, URL: https://www.youtube.com/watch?v=WLLPZoS_mz4 (Year: 2020). |
LH02028 Portable Hemodialysis Machine, date unknown, aliexpress.com [online], [site visited Jan. 4, 2022], Available from internet: https://www.aliexpress.eom/item/1005003324875329.html?randl_currency=USD&_randl shipto=US&src=google&aff_fcid=1003bab3b8db4e93b9ba88522a14cfc1-1641319351626-05232-UneMJZVf&aff fsk-UneMJZVf&aff_platform=aaf&sk=UneMJZVf&aff_trace_key= (Year: 2022). |
Medical Hemodialysis Machine, date unknown, aliexpress.com [online], [site visited Jan. 4, 2022], Available from internet: https://www.aliexpress.com/item/1005003445721549.html?_randl_currency=USD&_randl_shipto=US&src=google&aff_fcid=a524f3f9cd9b4976b6b47962f3439d62-1641319166409-02691-UneMJZVf&aff_fsk-UneMJZVf&aff platform-aaf&sk-UneMJZVf&aff_trace_key=a524f 3f9cd9b4976b6b47962f3439d62-1641319166409-02691-UneMJZVf&terminal_id=d0c2cca4b7664d 128cb4801 a9ef03ff2 (Year: 2022). |
Millenium HX Portable Dialysis Water System, Jul. 2, 2014, youtube.com [online], [site visited Jan. 10, 2022], Available from internet, URL: https://www.youtube.com/watch?v=IGEbPi2CDsw (Year: 2014). |
Portable home dialysis device, Nov. 2, 2017, med-technews.com [online], [site visited Jan. 4, 2022], Available from internet: https://www.med-technews.com/news/portable-home-dialysis-device-to-launch-next-year/ (Year: 2017). |
Number | Date | Country | |
---|---|---|---|
20200276372 A1 | Sep 2020 | US |