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International Journal of Research in Engineering and Science (IJRES)
ISSN (Online): 2320-9364, ISSN (Print): 2320-9356
www.ijres.org Volume 3 Issue 5 ǁ May. 2015 ǁ PP.51-56
www.ijres.org 51 | Page
Modeling and Analysis of peritoneal dialysis piping set
XI Chuan-long1
, WU Jian-min2
, LIU fei3
YANG Jin-ye4
1
(College of Mechanical Engineering, Shanghai University of Engineering Science, Shanghai, china)
2
(College of Mechanical Engineering, Shanghai University of Engineering Science, Shanghai, china)
3
(College of Mechanical Engineering, Shanghai University of Engineering Science, Shanghai, china)
4
(College of Mechanical Engineering, Shanghai University of Engineering Science, Shanghai, china)
Abstract: With the number of end-stage renal disease (ESRD) patient population continues to increase.
However ESRD patients rely on renal replacement therapy (renal transplantation and dialysis) to maintain a
normal life. Design of a peritoneal dialysis tubing set, using three-dimensional design software SolidWorks; and
dialysis the tubing set in SolidWorks flow simulation.
Key words: peritoneal dialysis; peritoneal dialysis pipingset
I. Introduction
Chronickidney diseasehasbecome one of themajor diseases thatthreatenpublichealth.End-stage renal
disease(ESRD) is the end stage of chronic kidney disease, refers to irreversible renal function decline in patients
rely on renal replacement therapy (renal transplantation and dialysis) to maintain a normal life pathological state
needs[1]
.Dialysis can be divided into manual (continuous ambulatory peritoneal dialysis, CAPD) and automated
peritoneal dialysis (automated peritoneal dialysis, APD)[2]
。The traditionalperitoneal dialysis used to use
gravity,and automated peritoneal dialysis machine uses a peristaltic pump and other external power mode. As
one of the core components of peritoneal dialysis machine.It is particularly important for the design of dialysis
tubing set.HuYue-ming and other domestic scholars proposed treatment of renal failure smart peritoneal dialysis
system[3]
;Wang Hui put forward the design of automated peritoneal dialysis machine[4]
.The scholarsfocus onthe
design of automated peritoneal dialysis machine, but less research on peritoneal dialysis tubing set.Design a
dialysis tubing setbyusing three-dimensional softwareSolidWorks,and using SolidWorks flow simulation to
simulation dialysate on pipingset in process of dialysate from heating interface topatient interface, and analysis
the pressure drop, flow velocity distribution of dialysate.
II. Design piping set
The main function of tub set are follows: Firstly, delivery the dialysateto the patient's abdominal cavity,
then the dialysate is kept in cavity for some time;Secondly, the dialysis machine exhaust the dialysate through
the piping set from the abdominal cavity. Specific peritoneal dialysis usually go through four processes: heating
dialysate into the abdominal cavity; exhaust the waste dialysate out of the cavity ; pumping dialysate from
supplement bag interface to the heating interface; pumping dialysate into the heating interface from the last bag
interface. In this paper, based on the above four processes design a piping set.
Modeling and Analysis of peritoneal dialysis piping set
www.ijres.org 52 | Page
1.Patient interface valve 2.Waste dialysate interface valve 3.supplement interface valve 4.Last bag
interface valve 5.Heating interface valve 6.7.10.reversingvalve 8.9.A power pump valve 11.12.B
power pump valve
Figure 1Pipeline group two-dimensional map
The process of dialysate from heated interface to the patient interface can be de divided as following two
sub-processes. DA, DBrepresent the pump which is connected with the piping set inFigure 2 (a) and Figure 2(b).
The action of DA, DB aspirate and feed operation, respectively, using the left and right arrows indicate;Each
process two pumps simultaneously and independently of each other;In Figure 2 (a) a solid line indicates the
pumps A aspirate dialysate, the dashed line represents the operation of pump B feed liquid;So in Figure2 (b) the
solid line representsthe pump A feed dialysate, the dashed line represents the pump B aspirate dialysate;when
dialysate flow in the piping set, the valves which dialysate flow through the pipeline open.
(a)the sub-process of DA aspirate, DB feed
(b)the sub-process ofDA feed, DB aspirate
Figure 2 Dialysate from the heating process interface to patient interface
According to the peritoneal dialysis four dialysis process using SolidWorks software to build a
three-dimensional model of peritoneal dialysis piping set, and it is shown in Figure 3.with three layers to
Modeling and Analysis of peritoneal dialysis piping set
www.ijres.org 53 | Page
optimize the structure ofPipeline group(the different treatment process piping design in hierarchical framework),
it makes the pipeline group reduced volume, easy to carry.
Figure 3 three-dimensional model of peritoneal dialysis pipingset
III. simulation
According to the requirements of peritoneal dialysis, automated peritoneal dialysis begin to work when in
the dialysate heat at 37 ℃, then dialysate flow as certain rate to patients interface.As the actual dialysis process
has a variety of modes, so the project simulate the tidal peritoneal dialysismodel. simulation the transient
movement of dialysate as Figure 2(a) and 2(b).This article assumes heated dialysate flow in constant rate
topatient interface through the pipeline group. The purpose of the simulation is to simulate a real dialysis
process, intend to explore the feasibility of the pipeline group and get dialysate flow process in the pipeline
group pressure, velocity and flow trajectories distribution.When SolidWorks flow simulation create a new
project,You can use the wizard, and set the simulation parametersin accordance with Table 1 below.When you
have finished setting the basic parameters in Table 1, after setting the boundary conditions:(1)by reference [2]
tidal patterns,Inlet boundary conditions can be obtained:150~250ml/min(Thatis 2500~4200mm3
/s)and the
model is set200ml/min。(2)Outlet boundary condition:Ambient pressure is standard atmospheric pressure (using
Standard atmospheric pressureas value of abdominalcavity ).
Table 1Basic Settings simulation project
Item name Setting Options
Configuration name Create new:Dialysis tubing set simplified model
Unit system NMM(mm-g-s)temperature(celsius)
Analysis type
TickInternal[exclude cavities without flow
condition]
Physical features Tick gravity,Setting 9.81m/s2
Database of fluid Choose liquid-water
Flow characteristic Setting laminar and turbulent
Wall condition
Default wall thermal condition List, select
adiabatic wall
Roughness valve 0 micrometer
Initial condition The initial temperature was set to 37 ℃
Result & geometry resolution Setting results accuracy of 3
Modeling and Analysis of peritoneal dialysis piping set
www.ijres.org 54 | Page
IV. Simulation Results and Analysis
Now we analysis the sub-processes of dialysate from the heating interfaceto patient interface. And we are
concerned about the pressure distribution, velocity distribution and the section of velocity distribution in patient
interface.
4.1 Pressure distribution
Peritoneal dialysis pressure field distribution is shown in Figure 4.From Figure 4(a) we can learn about
pressure range very little. the pressure drop is 0.0034 atm in the process of Figure 2(a) . Figure 4(b) is the
sub-process-heating interface to patient interface, and pressure drop is 0.0059 atm. Figure 4a and Figure 4b
shows that the pipingset to the dialysate pressure drop is very small. The pressure did not fluctuate severely
during dialysis.
(a)the sub-process of DA aspirate, DB feed
(b) The sub-process of DA feed, DB aspirate Figure 4 two sub-process pressures distribution
4.2Velocity vector field
The simulation in Fig. 5a and 5b corresponds to the FIG. 2a and 2b .they are the velocity vector field
distribution of the two sub-processes. As can be seen from Figure 5 the overall dialysate flow is relatively flat,
and the speedis concentrated in 287 ~ 96mm/s. Dialysate flow rate of loss among every unit length of the
process is the same, and dialysate flow path of Figure 2(a) is longer than to Figure 2(b), so the maximum flow
rate of the dialysate in Figure 5(b) is larger than Figure 5(a).Figure 6 is a cross-section of dialysis fluid velocity
vector field shot into the patient interface, Figure 6(a) corresponds with 2(a) process. It shows patient interface
velocity vector screenshot, while Figure 6(b) simulates 2(b) process speed vector screenshots. From Figure 6(a)
and
Modeling and Analysis of peritoneal dialysis piping set
www.ijres.org 55 | Page
Figure 6(b)we know that the flow rate of the patient interface is concentrated in384~96mm/s.
(a)DA aspiration, DB sub-process liquid feed
(b)the sub-process ofDA feed, DB aspirate Figure 5 two sub-process velocity vector field distribution
(a)the sub-process of DA aspirate, DB feed
(b)the sub-process ofDA feed, DB aspirate Figure 6 two sub process velocity vector-sectional view of the patient
interface
Modeling and Analysis of peritoneal dialysis piping set
www.ijres.org 56 | Page
V. Conclusion
(1) Using SolidWorks completes piping set design and takes fluid simulations to test our design. Through
simulation we can get the fluid in the piping group pressure, velocity and fluid trajectory that can help us to
improve the design level.
(2) Pressure distribution is shown in Figure 4 and Figure 6 speed vector shows that dialysate flow to the patient
interface from the heating interface. During dialysis process piping group pressure drop is small and
dialysate achieves lower speed, making a more gentle pace flow into the abdominal cavity.
(3) In this paper, using Solid Works to simulate the a peritoneal dialysis process, there are also some drawbacks.
For example there are some deficiencies in the simulation medium by water instead of the dialysate.
References
[1] Liu Rongzhi Comparison of three peritoneal dialysis catheter complications and efficacy[D]. guang zhou: Southern Medical
University, 2013
[2] Allen R. Nissen son, Richard N. Fine. Handbook of dialysis therapy [M].Taiwan: Elsevier Taiwan Inc, 2011
[3] Hu Yueming, Yuan Peng, Wu Xinsheng. Intelligent Peritoneal Dialysis System for the Treatment of Renal Failure [J].Journal of
Biomedical Engineering, 2005, 22(6):1249~1252
[4] Wang Hui, He Jian-zhong, Zhao Man-man. Design of automated peritoneal dialysis machine [J].information technology, 2014,
(4):121~124

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Modeling and Analysis of peritoneal dialysis piping set

  • 1. International Journal of Research in Engineering and Science (IJRES) ISSN (Online): 2320-9364, ISSN (Print): 2320-9356 www.ijres.org Volume 3 Issue 5 ǁ May. 2015 ǁ PP.51-56 www.ijres.org 51 | Page Modeling and Analysis of peritoneal dialysis piping set XI Chuan-long1 , WU Jian-min2 , LIU fei3 YANG Jin-ye4 1 (College of Mechanical Engineering, Shanghai University of Engineering Science, Shanghai, china) 2 (College of Mechanical Engineering, Shanghai University of Engineering Science, Shanghai, china) 3 (College of Mechanical Engineering, Shanghai University of Engineering Science, Shanghai, china) 4 (College of Mechanical Engineering, Shanghai University of Engineering Science, Shanghai, china) Abstract: With the number of end-stage renal disease (ESRD) patient population continues to increase. However ESRD patients rely on renal replacement therapy (renal transplantation and dialysis) to maintain a normal life. Design of a peritoneal dialysis tubing set, using three-dimensional design software SolidWorks; and dialysis the tubing set in SolidWorks flow simulation. Key words: peritoneal dialysis; peritoneal dialysis pipingset I. Introduction Chronickidney diseasehasbecome one of themajor diseases thatthreatenpublichealth.End-stage renal disease(ESRD) is the end stage of chronic kidney disease, refers to irreversible renal function decline in patients rely on renal replacement therapy (renal transplantation and dialysis) to maintain a normal life pathological state needs[1] .Dialysis can be divided into manual (continuous ambulatory peritoneal dialysis, CAPD) and automated peritoneal dialysis (automated peritoneal dialysis, APD)[2] 。The traditionalperitoneal dialysis used to use gravity,and automated peritoneal dialysis machine uses a peristaltic pump and other external power mode. As one of the core components of peritoneal dialysis machine.It is particularly important for the design of dialysis tubing set.HuYue-ming and other domestic scholars proposed treatment of renal failure smart peritoneal dialysis system[3] ;Wang Hui put forward the design of automated peritoneal dialysis machine[4] .The scholarsfocus onthe design of automated peritoneal dialysis machine, but less research on peritoneal dialysis tubing set.Design a dialysis tubing setbyusing three-dimensional softwareSolidWorks,and using SolidWorks flow simulation to simulation dialysate on pipingset in process of dialysate from heating interface topatient interface, and analysis the pressure drop, flow velocity distribution of dialysate. II. Design piping set The main function of tub set are follows: Firstly, delivery the dialysateto the patient's abdominal cavity, then the dialysate is kept in cavity for some time;Secondly, the dialysis machine exhaust the dialysate through the piping set from the abdominal cavity. Specific peritoneal dialysis usually go through four processes: heating dialysate into the abdominal cavity; exhaust the waste dialysate out of the cavity ; pumping dialysate from supplement bag interface to the heating interface; pumping dialysate into the heating interface from the last bag interface. In this paper, based on the above four processes design a piping set.
  • 2. Modeling and Analysis of peritoneal dialysis piping set www.ijres.org 52 | Page 1.Patient interface valve 2.Waste dialysate interface valve 3.supplement interface valve 4.Last bag interface valve 5.Heating interface valve 6.7.10.reversingvalve 8.9.A power pump valve 11.12.B power pump valve Figure 1Pipeline group two-dimensional map The process of dialysate from heated interface to the patient interface can be de divided as following two sub-processes. DA, DBrepresent the pump which is connected with the piping set inFigure 2 (a) and Figure 2(b). The action of DA, DB aspirate and feed operation, respectively, using the left and right arrows indicate;Each process two pumps simultaneously and independently of each other;In Figure 2 (a) a solid line indicates the pumps A aspirate dialysate, the dashed line represents the operation of pump B feed liquid;So in Figure2 (b) the solid line representsthe pump A feed dialysate, the dashed line represents the pump B aspirate dialysate;when dialysate flow in the piping set, the valves which dialysate flow through the pipeline open. (a)the sub-process of DA aspirate, DB feed (b)the sub-process ofDA feed, DB aspirate Figure 2 Dialysate from the heating process interface to patient interface According to the peritoneal dialysis four dialysis process using SolidWorks software to build a three-dimensional model of peritoneal dialysis piping set, and it is shown in Figure 3.with three layers to
  • 3. Modeling and Analysis of peritoneal dialysis piping set www.ijres.org 53 | Page optimize the structure ofPipeline group(the different treatment process piping design in hierarchical framework), it makes the pipeline group reduced volume, easy to carry. Figure 3 three-dimensional model of peritoneal dialysis pipingset III. simulation According to the requirements of peritoneal dialysis, automated peritoneal dialysis begin to work when in the dialysate heat at 37 ℃, then dialysate flow as certain rate to patients interface.As the actual dialysis process has a variety of modes, so the project simulate the tidal peritoneal dialysismodel. simulation the transient movement of dialysate as Figure 2(a) and 2(b).This article assumes heated dialysate flow in constant rate topatient interface through the pipeline group. The purpose of the simulation is to simulate a real dialysis process, intend to explore the feasibility of the pipeline group and get dialysate flow process in the pipeline group pressure, velocity and flow trajectories distribution.When SolidWorks flow simulation create a new project,You can use the wizard, and set the simulation parametersin accordance with Table 1 below.When you have finished setting the basic parameters in Table 1, after setting the boundary conditions:(1)by reference [2] tidal patterns,Inlet boundary conditions can be obtained:150~250ml/min(Thatis 2500~4200mm3 /s)and the model is set200ml/min。(2)Outlet boundary condition:Ambient pressure is standard atmospheric pressure (using Standard atmospheric pressureas value of abdominalcavity ). Table 1Basic Settings simulation project Item name Setting Options Configuration name Create new:Dialysis tubing set simplified model Unit system NMM(mm-g-s)temperature(celsius) Analysis type TickInternal[exclude cavities without flow condition] Physical features Tick gravity,Setting 9.81m/s2 Database of fluid Choose liquid-water Flow characteristic Setting laminar and turbulent Wall condition Default wall thermal condition List, select adiabatic wall Roughness valve 0 micrometer Initial condition The initial temperature was set to 37 ℃ Result & geometry resolution Setting results accuracy of 3
  • 4. Modeling and Analysis of peritoneal dialysis piping set www.ijres.org 54 | Page IV. Simulation Results and Analysis Now we analysis the sub-processes of dialysate from the heating interfaceto patient interface. And we are concerned about the pressure distribution, velocity distribution and the section of velocity distribution in patient interface. 4.1 Pressure distribution Peritoneal dialysis pressure field distribution is shown in Figure 4.From Figure 4(a) we can learn about pressure range very little. the pressure drop is 0.0034 atm in the process of Figure 2(a) . Figure 4(b) is the sub-process-heating interface to patient interface, and pressure drop is 0.0059 atm. Figure 4a and Figure 4b shows that the pipingset to the dialysate pressure drop is very small. The pressure did not fluctuate severely during dialysis. (a)the sub-process of DA aspirate, DB feed (b) The sub-process of DA feed, DB aspirate Figure 4 two sub-process pressures distribution 4.2Velocity vector field The simulation in Fig. 5a and 5b corresponds to the FIG. 2a and 2b .they are the velocity vector field distribution of the two sub-processes. As can be seen from Figure 5 the overall dialysate flow is relatively flat, and the speedis concentrated in 287 ~ 96mm/s. Dialysate flow rate of loss among every unit length of the process is the same, and dialysate flow path of Figure 2(a) is longer than to Figure 2(b), so the maximum flow rate of the dialysate in Figure 5(b) is larger than Figure 5(a).Figure 6 is a cross-section of dialysis fluid velocity vector field shot into the patient interface, Figure 6(a) corresponds with 2(a) process. It shows patient interface velocity vector screenshot, while Figure 6(b) simulates 2(b) process speed vector screenshots. From Figure 6(a) and
  • 5. Modeling and Analysis of peritoneal dialysis piping set www.ijres.org 55 | Page Figure 6(b)we know that the flow rate of the patient interface is concentrated in384~96mm/s. (a)DA aspiration, DB sub-process liquid feed (b)the sub-process ofDA feed, DB aspirate Figure 5 two sub-process velocity vector field distribution (a)the sub-process of DA aspirate, DB feed (b)the sub-process ofDA feed, DB aspirate Figure 6 two sub process velocity vector-sectional view of the patient interface
  • 6. Modeling and Analysis of peritoneal dialysis piping set www.ijres.org 56 | Page V. Conclusion (1) Using SolidWorks completes piping set design and takes fluid simulations to test our design. Through simulation we can get the fluid in the piping group pressure, velocity and fluid trajectory that can help us to improve the design level. (2) Pressure distribution is shown in Figure 4 and Figure 6 speed vector shows that dialysate flow to the patient interface from the heating interface. During dialysis process piping group pressure drop is small and dialysate achieves lower speed, making a more gentle pace flow into the abdominal cavity. (3) In this paper, using Solid Works to simulate the a peritoneal dialysis process, there are also some drawbacks. For example there are some deficiencies in the simulation medium by water instead of the dialysate. References [1] Liu Rongzhi Comparison of three peritoneal dialysis catheter complications and efficacy[D]. guang zhou: Southern Medical University, 2013 [2] Allen R. Nissen son, Richard N. Fine. Handbook of dialysis therapy [M].Taiwan: Elsevier Taiwan Inc, 2011 [3] Hu Yueming, Yuan Peng, Wu Xinsheng. Intelligent Peritoneal Dialysis System for the Treatment of Renal Failure [J].Journal of Biomedical Engineering, 2005, 22(6):1249~1252 [4] Wang Hui, He Jian-zhong, Zhao Man-man. Design of automated peritoneal dialysis machine [J].information technology, 2014, (4):121~124