Sidney C Gasoto1, Bertoldo Schneider1, João A P Setti2. 1. Graduate Program in Electrical and Computer Engineering, Federal Technologic University of Paraná, Curitiba, Paraná, Brazil. 2. Graduate Program in Biomedical Engineering, Federal Technologic University of Paraná, Curitiba, Paraná, Brazil.
Abstract
Peristaltic pumps are used in healthcare for their ability to aseptically displace various fluids, including medium-density gels and suspended solids. However, they have the undesirable characteristic of pulsing at their output. Three-dimensional printing is becoming a reality in tissue engineering, and it generally uses syringes to extrude hydrogels. One of the problems to be solved is the microdosing of biomaterials or bioinks when it is necessary to print large volumes. The use of peristaltic pumps in bioprinting is desirable as it does not limit the volume to the contents of a syringe while achieving dosage control. A peristaltic pump was designed and implemented to avoid pulsation errors and microliter dosing while allowing a large amount of fluid displacement. Two pumps with equal displacement were built. The first uses the conventional profile and is the baseline for comparisons, while the second presents the profile studied and proposed. The concepts demonstrated by Bernoulli were used, fixing the height of a column of water, while the two pumps provide flow to the system asynchronously, allowing the reading of pressure as a function of the speed variation created by the pulsation of each pump. An approximately 100 times reduction in pulsation was observed during fluid displacement with the variance reduced from 2.64 to 0.025 s2. The two pumps were also installed on a modified Ultimaker FDM 3D printer, and a standard for comparison was printed using a water-based hydrogel, corn starch, and corn-derived triglyceride, showing that the proposed pump improves the deposition quality of the material. Three-dimensional prints, tubes 20 mm in diameter by 8 mm in height and 0.7 mm in wall width, were also produced. Videos obtained show that the first pump was not able to print more than 4 mm in height, while the second prints the model with high quality and without deficiency. The results show that the new pump profile is able to provide a sufficiently constant volume for three-dimensional printing with excellent deposition control, building a simple object but difficult to obtain for a common peristaltic pump.
Peristaltic pumps are used in healthcare for their ability to aseptically displace various fluids, including medium-density gels and suspended solids. However, they have the undesirable characteristic of pulsing at their output. Three-dimensional printing is becoming a reality in tissue engineering, and it generally uses syringes to extrude hydrogels. One of the problems to be solved is the microdosing of biomaterials or bioinks when it is necessary to print large volumes. The use of peristaltic pumps in bioprinting is desirable as it does not limit the volume to the contents of a syringe while achieving dosage control. A peristaltic pump was designed and implemented to avoid pulsation errors and microliter dosing while allowing a large amount of fluid displacement. Two pumps with equal displacement were built. The first uses the conventional profile and is the baseline for comparisons, while the second presents the profile studied and proposed. The concepts demonstrated by Bernoulli were used, fixing the height of a column of water, while the two pumps provide flow to the system asynchronously, allowing the reading of pressure as a function of the speed variation created by the pulsation of each pump. An approximately 100 times reduction in pulsation was observed during fluid displacement with the variance reduced from 2.64 to 0.025 s2. The two pumps were also installed on a modified Ultimaker FDM 3D printer, and a standard for comparison was printed using a water-based hydrogel, corn starch, and corn-derived triglyceride, showing that the proposed pump improves the deposition quality of the material. Three-dimensional prints, tubes 20 mm in diameter by 8 mm in height and 0.7 mm in wall width, were also produced. Videos obtained show that the first pump was not able to print more than 4 mm in height, while the second prints the model with high quality and without deficiency. The results show that the new pump profile is able to provide a sufficiently constant volume for three-dimensional printing with excellent deposition control, building a simple object but difficult to obtain for a common peristaltic pump.
Peristaltic pumps have excellent metering,
sealing, asepsis, and
easy maintenance characteristics. They do not require valves, and
their mechanism has a long lifespan.[1] It
can displace small suspended solids and low- and medium-density gels.
They do not interact with mechanical parts and lubrication systems.
These characteristics are beneficial for devices that promote the
displacement of biomaterials for deposition in three dimensions, known
as 3D bioprinters and other devices used in tissue engineering. In
addition, the peristaltic pump has the potential to supply material
derived from a reservoir, which can recharge during printing. The
system allows printing large-volume objects;[2] it also can retract the product, which optimizes printing, removing
excess and dripping during movements without biomaterial deposition.
Bociaga et al.[2] showed that printers that
use syringes for extrusion of biomaterials have reduced printing quality
when the reservoir (syringe) assumes dimensions greater than 100 mL,
which prevents the printing of whole organs, such as a liver, kidney,
or heart. It also raises a crucial issue: the deposition of cells
at the bottom of the reservoir by decantation. This problem can be
solved with biomaterials agitation but is difficult to implement in
syringe-type reservoirs. Bociaga et al.[2] presented the development of a 3D bioprinting system based on a
peristaltic pump and tested two hydrogels with different compositions.
This shows that the peristaltic pump has great importance in these
devices, but it does not address the problem of pump pulsation.The term “peristaltic” refers to a tube’s
radial contraction and relaxation due to mechanical action or stimulus,
moving along its length, forming a wave.[3,4]This
pump is suitable for low- and medium-viscosity biomaterials,
such as air, liquids, gels, or suspensions, consisting of a liquid
phase and a small dispersed solid phase. It is not indicated when
the biomaterial consists of living cells if the occlusion is total.
The tube suitable for a peristaltic pump applied in healthcare is
silicone due to its asepsis characteristic.[1]The housing is constructed so that the tube is inserted and
withdrawn
from the inner cylinder, forming an arc, and thus, the rollers restart
the process. When a roller loses its action in the tube, it tends
to expand, promoting the back-flow of the contained material, causing
pulsation at the outlet.The search for off-the-shelf peristaltic
pumps provided many results,
not shown here, with several manufacturers claiming that their pumps
have low pulsation but without measuring this claim. In addition,
they do not disclose their projects, making it impossible to evaluate
and purchase a pump considered suitable for bioprinting.Peristalsis
is an effect found in most living things[5,6] and is widely
used for pumping products. New publications show constant
innovations in this type of pump. This work presents some of these
publications. The objective is to evaluate the concepts and solutions
of pulsation at the pump outlet, aiming at the extrusion of biomaterials
in 3D printers. In some patents of peristaltic pumps found in this
research, the authors claim to have low or no pulsation. This section
will show these patents.Lambert and Joergensen[1] showed a low-pulsation
peristaltic pump system, Figure , with two lines of six rollers each offset by 30°,
accommodating two interconnected tubes in the pump input and output
by “Y” elements. Thus, the pulsation of one of the paths
combines with the pulsation of the other, smoothing the pulses. However,
it uses a lot of rollers and two tubes. This technique doubles the
volume displaced per revolution and implies that the motor must work
at a very low speed to displace low amounts of biomaterial, desirable
in bioprinters, in addition to decreasing the resolution on the volume
control, the same problem with having large syringes when using small
exit holes, as discussed by Bociaga et al.[2]
Figure 1
Lambert
and Joergensen’s pump. Two lines of six rollers
each are shown offset by 30°.
Lambert
and Joergensen’s pump. Two lines of six rollers
each are shown offset by 30°.Usually industries do not comment on their projects and do not
disclose their secrets. However, Cole-Parmer (https://www.coleparmer.com/tech-article/reducing-pulsation-peristaltic-pumping) explained four methods to smooth pulsation at the output of their
pumps. Almost all of these methods were studied in the patents presented,
except the use of a pressure accumulator, called by them an air damper,
as this method implies maintaining pressure in the output line through
this accumulator, which makes it challenging to interrupt the flow
in a controlled manner, which is unwanted in bioprinting.In
US patent 3,726,613,[7] the author
uses a cam-controlled pusher synchronized with the drive, Figure . Rollers, or pistons,
act on the wall of a flexible tube to compress at a location downstream
of the elements, thus smoothing out pulsations in the flow of a fluid
carried by the peristaltic pump. This element is gently removed during
roller movement, reducing pulsation. It is a problematic construction
device. It involves various moving components and exact sizing of
the lever and cam. The fluid displacement caused by the pusher must
be identical and synchronized with the displacement caused by the
roller without obstructing the product outlet.
Figure 2
Casimir’s pump.
Pusher (1) displaces an equal volume as
the roller (2).
Casimir’s pump.
Pusher (1) displaces an equal volume as
the roller (2).It is possible to increase the
flow accuracy of a peristaltic pump
using multiple channels or tubes.[8] In his
patent, US 4,673,344, the author described a pump with several spring
cassettes split and pressed against a set of elongated rollers, Figure . These are mounted
on a shaft, spaced evenly and circularly. Each cassette has a cam
mounted on its side, which contacts the rollers and gradually relieves
spring pressure on the installed tubes. The author states that these
cams can be adjusted and replaced. This design makes it possible to
adjust the flow rate and pulsation for different pipe diameters. The
author also claims that it is possible to replace cassettes and tubes
while the pump is running.
Figure 3
Allington’s pump. Multiple channels with
several spring
cassettes.
Allington’s pump. Multiple channels with
several spring
cassettes.In US patent 5,620,313,[9] the author
described a peristaltic pump composed of 4 tubes arranged parallel
to each other and between the rotor axis, Figure , in the form of an endless thread. The rotor
compresses at least two distinct points, forming a volume inside the
tube between each occlusion point that moves as a function of rotor
rotation. The pump works with the effect of a linear peristaltic pump
with the compression zone advancing along each tube from one end to
the other, displacing the product along the tube. The author does
not state how the contact between the rotor and the tubes occurs in
the patent description. It is believed that there is friction between
these elements, which would cause the tube to wear out rapidly. However,
the displacement is continuous and sinusoidal, which minimizes pulsation
if added to the output.
Figure 4
Fockenberg’s pump. Four tubes are arranged
parallel to each
other and between the rotor axis. Radial (a) and axial (b) views.
Fockenberg’s pump. Four tubes are arranged
parallel to each
other and between the rotor axis. Radial (a) and axial (b) views.Another device[10] that
eliminates the
sudden entry and exit of rollers on the peristaltic pump tube, minimizing
the volumetric pulse of its exit, has a rotor with three rollers and
a spring system to push in the direction of occlusion of the tubes, Figure . However, a cam
drives the rollers and moves them away from the tube continuously
and gradually, providing a linear ramp. The system is divided into
three sectors of 120°. Sectors S1 and S3 have a ramp that linearly
presses the tubes, while in sector S2, the tube is pressed continuously,
providing the occlusion and, therefore, the displacement of the fluid
contained in the tube. This method does not eliminate the pulsation.
It just distributes it, thus creating a nonlinear displacement of
the fluid. Segment constriction causes nonlinearity in a pump cycle
at the beginning of sector two and releases after the end of the same
sector. This causes expansion of the tube and suction of the volume
at the outlet.
Figure 5
Pringle’s pump. Cam drives the rollers and moves
them away
from the tube continuously and gradually, providing a linear ramp.
System is divided into three sectors of 120°, S1, S2, and S3.
Pringle’s pump. Cam drives the rollers and moves
them away
from the tube continuously and gradually, providing a linear ramp.
System is divided into three sectors of 120°, S1, S2, and S3.In US patent 2005/0084402 A1,[11] a device
similar to that proposed by Pringle[10] was
shown, Figure , basically
differentiating the spring actuation system as it uses three rollers
and a housing profile that resembles a cam divided into sectors, which
either presses or does not press the pump tube. The authors argue
that removing all of the pulsation from the pump is impossible. Even
so, they guarantee that their design can linearize the dosage for
one rotation of the rotor, making the occlusion area the same length
as the release area of the tube, that is, 120°.
Figure 6
Vanek’s pump uses
three rollers and a housing profile that
resembles a cam divided into sectors, which either presses or does
not press the pump tube.
Vanek’s pump uses
three rollers and a housing profile that
resembles a cam divided into sectors, which either presses or does
not press the pump tube.Two patents, US 8,079,836
B2 and JP 2007-298034 A,[12,13] presented a slight
variation of the presented models with four rollers, Figure , and also defended
the initial and final ramp in the occlusion region pulse smoothing.
Figure 7
Gao and
Oude’s pump. Slight variation of the presented models
with four rollers: (a) Gao’s pump and (b) Oude’s pump.
Gao and
Oude’s pump. Slight variation of the presented models
with four rollers: (a) Gao’s pump and (b) Oude’s pump.Patent US 2006/0245964 A1[14] differs
from the others. It includes a delayed occlusion relief of 120°
from the pump outlet, Figure . When one roller relieves the tube, the other presses it,
compensating for the effect of negative fluid displacement eliminating
pulsation. The patent presents a variety of designs that try to cover
as many pump models as possible, always with the same purpose of relieving
occlusion lag at a certain distance depending on the number of rollers.
It is the best solution found during the search. The patent remains
valid, and reproduction for commercialization is not allowed.
Figure 8
Koslov et al.’s
pumps. Delayed occlusion relief of 120°
from the pump outlet. Two designs (a and b) are shown.
Koslov et al.’s
pumps. Delayed occlusion relief of 120°
from the pump outlet. Two designs (a and b) are shown.The device is defended in EP 3 017 836 A1[15] in which the pipeline is placed in a cavity with four zones, Figure . The first zone
is arranged so that a roller causes between 0 and 100% occlusion during
movement. The second and third zones allow the roller to maintain
total occlusion during travel. The fourth zone is constructed so that
the roller gradually decreases occlusion during its movement. The
length of each zone is less than the length of the arc between the
two neighboring latching elements. The sum of the lengths of the second
and third zones is equal to the distance of the bow between the two
adjacent latching elements.
Figure 9
Tsoukalis’s pump. Variation of the inner
diameter of the
tube: pump profile house (a) and tube profile(b).
Tsoukalis’s pump. Variation of the inner
diameter of the
tube: pump profile house (a) and tube profile(b).The cross-section of the tube is variable. In the second zone,
the cross-section is larger than that in the third zone by an amount
that leads to an increase in volume equal to that displaced in the
fourth zone at the moment of disengagement from the pipe roll.[15] At first glance, the pump is the same as the
others studied. However, the characteristic variation of the inner
diameter of the tube sets it apart. It corrects the displaced volume,
eliminates fluid back-flow, and ensures adequate dosage, but it is
not easy to manufacture. The patent remains valid, and reproduction
for commercialization is not allowed.To facilitate understanding, Table summarizes the patents
and characteristics of interest
to this research.
Table 1
Summary of Patents
author
general characteristics
Lambert and Joergensen[1]
easy to build, pulses are minimized
but not eliminated
von Casimir[7]
eliminates pulses
but difficult to build
Allington and Hull[8]
minimizes
pulses a lot but difficult to build, volume is multiplied
by the number of tubes
Fockenberg[9]
minimizes pulses,
difficult to build, volume is multiplied
by the number of tubes, friction can shorten tube life
Pringle[10]
distributes pulses linearly but difficult to build,
lots of
moving elements, does not eliminate pulses
Vanek[11]
low pulse, easy build
Gao
and Williams, Oude[12,13]
easy to build but does not eliminate pulses
Koslov et al.[14]
easy to build, eliminates
pulses completely
Tsoukalis[15]
eliminates pulses
completely
McIntyre
et al.[16] evaluated the pulsation
of a peristaltic pump through simulation and compared the results
with a pump obtained by additive manufacturing. It applies pulsation
measurement techniques with pressure sensors using standard valves
for flow control to adjust the flow at the pump outlet. His work is
rich in detail and demonstrates the simulated trials of two- and three-roller
pumps. The flow control valve used is simple and does not contain
the necessary resources to keep the flow constant since, in this type
of valve, when the pressure increases the flow also increases.The elements used to dispense products on the printing base in
bioprinters are like the needles used in healthcare but without the
bevel, diagonal cut that provides better perforation capacity. They
use the same Gauge (Ga) codes, color patterns, and beveled needle
diameters (https://darwin-microfluidics.com/blogs/tools/syringe-needle-gauge-table). Each researcher must choose the appropriate model for their impression,
hydrogel type, and viscosity.For a satisfactory result, the
ideal is that the outer diameter
of the needle is equal to or greater than the width of the desired
printed stroke, that is, a 0.4 mm needle will make a stroke up to
0.4 mm wide, while the height is defined by the distance from the
needle tip to the previous layer. For the trace to have the desired
height and width profile, a continuous material flow must be provided
and defined by the printing speed and the displacement of the pump.
A line 0.5 mm wide by 0.3 mm high and 1 mm long will have a volume
of 0.15 mm3 of material, or 0.15 μL. Therefore, for
the print speed of 600 mm/min, the material flow should be
90 mm3/min. The best print results were obtained
when the maximum height was limited to 75% of the width. In this way,
it is possible to calculate the flow required for each needle model
and printing speed.
Materials and Methods
When one wants
to deposit small amounts of material, as is the
case with 3D bioprinting, any difference in the dosed volume can represent
an unwanted form of printing, causing a lack or excess of biomaterial.
Bioprinters need the biomaterial deposited during printing to be supplied
continuously in a uniform volume. Pulses cause media to supply failures
that affect printing. The pulsation occurs due to the material reflux
in the expansion region. When the roll is removed, the rolling volume
is shifted back into the tube.[4] For each
complete revolution of the rotor, there will be several back-flow
pulses equal to the number of rollers, and the frequency (in Hertz)
is given by the number of rollers multiplied by the rotor speed (in
rpm), given by eq The volumetric
flow, defined as the volume
of a fluid that crosses a specific area per unit time for peristaltic
pumps,[17] is given in cm3/min
bywhere d is the inner
diameter
(in cm) of the flexible tube, N is the rotational
speed (in rpm), and r (in cm) is the radius of the
chamber, measured from the center of the rotor shaft to the center
of the roller that presses the tube.The volumetric flow rate
can be expressed in terms of the parametric
factors of the peristaltic pump. From eq , it can be stated that for a given size of the flexible
tube in the peristaltic pump, the flow depends not only on the speed
of rotation but also on the radius of rotation.[17]Determining the ideal flow for a peristaltic pump
applied to a
bioprinter depends on several factors, from the viscosity of the biomaterial,
the desired wall width, and the speed at which you want to print,
not being an easy task. The authors decided on a flow rate that they
believe is sufficient for most low-viscosity fluids and gels and reasonable
printing speed, ranging from 52.947 μL/min to 1,058.947 mL/min.It has been proposed to manufacture two pumps containing characteristics
of those studied, including overlapping some of them. The first pump
(pump A) has the characteristics of the pump proposed by Oude.[13] However, it is intended to be the baseline with
only three rolls. As seen in Figure , the cavity circumference was divided into 12 sections
of 30° each. During the rotating movement of the rotor, the rollers
are moved simultaneously. When the rotation is clockwise, the 3rd
roller moves over the 10th section (S10) and the tube clearing movement
occurs in the form of a ramp created by the arc region in this section.
On the other hand, the other rollers keep it pressed, moving the biomaterial
toward the exit and continuing the movement. The third roll presses
the tube again in the first section (S1), also in the form of a ramp
created by the arc in this region, forming a volume between rolls
3 and 1, which is continuously displaced while the rotor rotates.
Figure 10
Profile
of the first pump produced. When the rotation is clockwise,
the 3rd roller moves over the 10th section (S10) and the pipe cleaning
movement occurs in the form of a ramp created by the arc region in
this section. On the other hand, the other rollers keep it pressed,
moving the biomaterial toward the exit and continuing the movement.
Third roller again presses the tube in the first section (S1), also
in the form of a ramp created by the arc in this region, forming a
volume between rollers 3 and 1, which is continuously displaced while
the rotor turns.
Profile
of the first pump produced. When the rotation is clockwise,
the 3rd roller moves over the 10th section (S10) and the pipe cleaning
movement occurs in the form of a ramp created by the arc region in
this section. On the other hand, the other rollers keep it pressed,
moving the biomaterial toward the exit and continuing the movement.
Third roller again presses the tube in the first section (S1), also
in the form of a ramp created by the arc in this region, forming a
volume between rollers 3 and 1, which is continuously displaced while
the rotor turns.The second pump (pump
B) was built using the concepts found in
Koslov, Hagen, and Koslov.[14] However, ramps
were made in sections S1, S4, S6, and S10 and the pipe deviation along
section S5, Figure .
Figure 11
Profile of the second pump produced. Different pump times. (a)
At T0, roll 1 is in total occlusion, roll 2 is at the beginning of
occlusion, while roll 3 is at the beginning of release. (b) At T1,
roll 1 is wholly occluded, roll 2 at the end of the ramp is already
occluded, and roll 3 at the end of the ramp is entirely unobstructed.
Profile of the second pump produced. Different pump times. (a)
At T0, roll 1 is in total occlusion, roll 2 is at the beginning of
occlusion, while roll 3 is at the beginning of release. (b) At T1,
roll 1 is wholly occluded, roll 2 at the end of the ramp is already
occluded, and roll 3 at the end of the ramp is entirely unobstructed.Removal of the roller from the S10 section causes
an increase in
the volume of the tube. However, as the volume of the material moved
between two rollers is constant, this causes the material to retract,
causing the pulsation to appear at the product outlet. Removing the
previous roller, section 4, before closing the roller in section 1
causes more material to be introduced into the tube, creating a larger
volume between the two rollers between sections 1 and 9. When clogging
the tube in section 2, the release of the roller at S10 begins simultaneously
with the reintroduction of the roller into section S6 in a linear
fashion, correcting the expansion movement of the tube on the roller
at S10, since the roller at S6 presses the tube in the same proportion
as it is withdrawn at S10.For the pump displacement analysis,
the following data are applied
in eq The drive settings are set
toThe 3D print configure
file
in the 3D printer extrusion adjustment variable is set to 37.3359.inner diameter of the tube d = 1 mm
= 0.1 cmnumber of rotor rotations N = 1roll center radius r = 1.7167 cmThe pumps were manufactured in a CNC with an aluminum body, the
rotor in Poly-Oxy-Methylene (POM). The rollers are steel bearings
with external and internal diameters of 9 mm and 5 mm, respectively.
Each bearing has a width of 3 mm, and to allow compression of the
tube, two bearings side by side were used. The pumps are driven by
Nema 17, 4.5 kgf/cm stepper motors, controlled by the 3D printer board
used for the experiment.
Pump Pulse Test
The two pumps were
built and mounted
side by side with the outputs connected in parallel and driven one
at a time. The inlets were also joined in parallel and connected to
a fluid reservoir. A dye was used to facilitate the observation of
fluid displacement within the clear tube.The displaced fluid
was brought to a pressure sensor through a tube approximately 1.0 m
above the pressure sensor, positioned vertically, opened, and installed
inside a fluid collection system that takes it back to the reservoir.
The height was adjusted to 10 kPa above the local atmospheric
pressure, as indicated by the sensor when the pipe was filled with
water at room temperature, and the pumps were turned off. According
to the International System of Units (SI), 10 kPa is the pressure
of 101.95 cm of the water column at 4 °C applied to a
surface. This method guarantees a constant pressure in the system
since when pumped the liquid exits through the upper end of the vertical
tube, keeping the volume constant and, therefore, the pressure constant.Figure shows
the circuit of the system.
Figure 12
Assembly for pump pulsation tests. (a) Piping
schematic. (b) Photo
of the assembled system. (c) Detailed photo showing the pumps, sensor,
and reservoir.
Assembly for pump pulsation tests. (a) Piping
schematic. (b) Photo
of the assembled system. (c) Detailed photo showing the pumps, sensor,
and reservoir.The proposed test concept, which
defines that the system pressure
is constant if the flow is constant, can be expressed aswhere P is the pressure,
γ is the specific weight of the water contained in the vertical
pipe, v is the velocity of the flow generated by
the pump, g is the gravity acceleration, and Z is the height at which the water column is raised.The flow is reversed when the roller unlocks the tube, and the
velocity changes too, resulting in less pressure and allowing the
pulsation to be observed with the sensor used. In Figure b and 12c the assembly details are shown. The proposed test allows the verification
of small flow variations due to the sensor’s sensitivity. The
pressure sensor module for Arduino using BMP280 (https://www.bosch-sensortec.com/media/boschsensortec/downloads/datasheets/bst-bmp280-ds001.pdf) can measure pressures between 30 and 110 kPa with a 175 Hz
sampling rate and 0.000 16 kPa resolution. This sensor
is used to measure variations in atmospheric pressure and indicates
the absolute atmospheric pressure at sea level. The experiment reads
the local atmospheric pressure and subtracts this value from the measurements
obtained, resulting in the relative value of the water column in the
sensor.The sensor module does not have a pipe connection. A
metallic tube
was installed over it with an adequate diameter for installing flexible
tubes. A flexible membrane consisting of a PVC film was used over
the sensor to prevent it from coming into contact with the liquids
and provided a good seal.An Arduino Nano module was programmed
with the necessary routine
to read the sensor and send the data to the PC via USB serial. A Python
application was built on the PC to read the data and save it, from
which the graphs in Figure were extracted. The motors were driven by a module containing
the necessary electronics for operation. Two complete turns were commanded
for each motor. The reading corresponds to the signal generated by
the sensor during motor revolutions. The initial pressure of 10 kPa
is due to the tube being filled with water. Therefore, there is constant
pressure before starting the motors.
Figure 13
Graph obtained by reading the pressure
sensor: (a) pump A and (b)
pump B.
Graph obtained by reading the pressure
sensor: (a) pump A and (b)
pump B.
Printing with Pumps
The use of peristaltic pumps in
a 3D printing system for biomaterials requires regular dosing along
the path of the rollers. Two pumps were installed to replace the extrusion
head of an Ultimaker 3D printer built by the author. The body of a
5 mL syringe was used as a reservoir for the product to be deposited
on the glass platform covered with a thin layer of white PVC self-adhesive
film, allowing for contrast during filming and photos. The piping
between the reservoir and the pump was a silicone tube with an external
diameter of 4 mm and an internal diameter of 1 mm. The pump tube was
silicone with outside and inside diameters of 4 and 1 mm, respectively.
The rest of the tubing was rigid and transparent, ending in a Luer
Lock fitting, ensuring better sealing and fixing, where a 22 Ga needle
without bevel was placed. The material used for printing was a hydrogel
composed of 200 mL of water, 10 g of corn starch, and 5 mL of triglyceride
derived from corn. The mixture was heated to boiling. Blue food coloring
was used to obtain better contrast in the photos and videos. The mixture
was homogenized and cooled to room temperature before use. Two cameras
filmed the tests. One pointed at the printing base and the other at
the pumps. All of the photos, video, gcode used for printing, and
the data file obtained can be found on GitHub (https://github.com/sidneygasoto/Peristaltic-pump-3D-print/).The videos were edited to reduce the time and file size and accelerated
three times. The Repetier-Host (https://www.repetier.com/) app was used to control the 3D printer. Figures and 15 show the results of material deposition with peristaltic
pumps A and B, respectively.
Figure 14
Printing with pump A. Images were taken from
the video of pump
A at the moment when the roller starts releasing the tube due to the
start of the ramp ((a) time 00:00:33:19) and at the end of the ramp
((b) time 00:00:38:27). It is possible to observe that until the beginning
of the ramp the trace is consistent. Rectangle in a surrounds the
region, and along the ramp, the stroke loses its width until complete
absence, surrounded by the rectangle in b. Circles indicate the roll
positions at the beginning and end of the print failure.
Figure 15
Printing with pump B. Images taken from the video of pump B at
the moment when the ramp starts to release the tube (a) and at the
end of the ramp (b). Rectangles that enclose the print regions in
a and b show the regularity of the stroke width during the roll exit
ramp over the tube. Circles in a and b indicate the timing between
the last and the second to last rolls. (c) It is possible to see a
slight decrease in the thickness of the line.
Printing with pump A. Images were taken from
the video of pump
A at the moment when the roller starts releasing the tube due to the
start of the ramp ((a) time 00:00:33:19) and at the end of the ramp
((b) time 00:00:38:27). It is possible to observe that until the beginning
of the ramp the trace is consistent. Rectangle in a surrounds the
region, and along the ramp, the stroke loses its width until complete
absence, surrounded by the rectangle in b. Circles indicate the roll
positions at the beginning and end of the print failure.Printing with pump B. Images taken from the video of pump B at
the moment when the ramp starts to release the tube (a) and at the
end of the ramp (b). Rectangles that enclose the print regions in
a and b show the regularity of the stroke width during the roll exit
ramp over the tube. Circles in a and b indicate the timing between
the last and the second to last rolls. (c) It is possible to see a
slight decrease in the thickness of the line.It is possible to observe the printing faults and the variation
of the stroke width for pump A, while in pump B, no faults are observed;
only a slight decrease in the stroke width is observed, seen in more
detail in Figure .
Figure 16
Photo of prints; In (a) Pump A, there is a lack of material in
some places; In (b) Pump B, it is possible to see a slight decrease
in the line thickness.
Photo of prints; In (a) Pump A, there is a lack of material in
some places; In (b) Pump B, it is possible to see a slight decrease
in the line thickness.
Results and Discussion
In the graph of Figure it is possible to see that the pressure peaks for each roller
unclog the tube and return to occlusion. Table shows the statistical calculations obtained
from the sensor reading presented in the .xlsx file.
Table 2
Results of Statistical Calculations
Obtained by Sampling
pump A pressure (kPa)
pump B pressure (kPa)
maximum
10.264
10.144
minimum
9.629
10.056
medians
10.225
10.137
standard
deviation
0.164
0.0159
variations (s2)
2.68
0.025
A gcode has been edited to print a line whose
length requires more
than one turn of the pump impeller, allowing checking the rollers
passing through the areas causing the failure.Equation was used
to determine the pump’s displacement to obtain the necessary
volume of product to be deposited during the impressions. Pump displacement
is a parameter used to configure the printer and defines the number
of pulses in the stepper motor for each mm3 of product.The gcode (https://github.com/sidneygasoto/files/standardpattern.ngc) (line 12) defines that the printer should print from the current
location (X = 65.00 and Y = 15.00,
defined in the previous line) to X = 65.00 and Y = 150 0.00, that is, a straight line with a length of
135 mm in the Y direction, depositing 18.9 mm3 of material during the path at a speed of 500 mm/s,
0.14 mm3/min, which gives us an approximate height
of 0.2 mm in the line when using the 22 Ga needle (∼0.7 mm
in diameter).The same code was used to print on both pumps
and can be seen in
the Pump1-pattern.mp4 and Pump2-pattern.mp4 files found on GitHub
(https://github.com/sidneygasoto/Peristaltic-pump-3D-printvideos). Figure shows
a photo of the prints obtained and the lack of material can be observed
during the printing with Pump A, while with Pump B, no such failure
is observed, only slight variations in the width of the trace.A gcode (https://github.com/sidneygasoto/files/circle.ngc) was edited
to print a 3D model; a tube of 20 mm in diameter and 8 mm in height,
a single wall of approximately 0.7 mm in thickness, since a 22 Ga
needle (∼0.7 mm in diameter) was used. The same code was used
to print using the two pumps, the exact product extrusion parameters,
and the same hydrogel, and care was taken regarding the ambient temperature,
printer leveling, and any other variables that could interfere with
the experiment and can be seen in the videos Pump1-printing.mp4 and
Pump2-printing.mp4 found on GitHub (https://github.com/sidneygasoto/Peristaltic-pump-3D-print), represented in Figure . From pump A, Figure a, one can observe the irregularity of the biomaterial
deposition, creating a nonuniform face and collapsing after approximately
10–20 layers of 0.2 mm. Conversely, Figure b shows the print with pump B. It is observed
that the variation in the width of the stroke, obtained in the experiment
of printing the strokes, did not represent significant failures in
the layered printing since there was no lack of sufficient material
to interrupt the printing of the wall.
Figure 17
Photo of 3D prints:
(a) 3D print 1 and (b) 3D print 2. Best results
from five prints of each model. Irregularity of the deposition of
the biomaterial can be observed (a), creating a face, not uniform.
(b) Regular faces and near-perfect printing are obtained.
Photo of 3D prints:
(a) 3D print 1 and (b) 3D print 2. Best results
from five prints of each model. Irregularity of the deposition of
the biomaterial can be observed (a), creating a face, not uniform.
(b) Regular faces and near-perfect printing are obtained.Notably, a literature search revealed only one method to
investigate
the pulsation of peristaltic pumps, which motivated the authors to
apply the concepts found in Bernoulli’s equation, eq , presented in this research, and
to propose the method used for the use of both the sensor and the
water column technique to maintain constant pressure during the experiment.
The results obtained demonstrate consistency with those presented
by the authors, showing the pulses at the time of removal of the rollers,
proving the effect of flow reversal for pump A, while for pump B,
a reduction in these pulses was attained, and the profile pump B allows
the use of these for microdosing. During 3D printing with a higher
viscosity biomaterial, pump B had displacement variation during the
revolution. However, it still allowed an excellent result in the printed
form, which suggests that it can be used for this purpose. The silicone
tube was proposed because it is an inert material and consolidated
use in the medical environment as a biocompatible product. However,
it proved unsuitable for measuring high-viscosity materials as it
expands when pressure is increased. To avoid this effect, further
research with other materials for the tube is suggested, especially
tubes with reinforced walls. Future work also suggests printing more
complex 3D models, dimensional lifting of the printed models, and
exhaustive tests with different biocompounds to obtain a list of printable
biomaterials using a peristaltic pump and needle system for controlled
and precise control deposition.
Conclusion
Pulsation
in peristaltic pumps can lead to wrong dosages due to
the back-flow of product displaced from tube expansion when the element
producing the occlusion is removed. The analysis of several pump models
proposed in articles and patents showed that some models that can
eliminate pulsation and therefore dosing errors. The work evaluated
some models of pumps and submitted them to flow tests, obtaining the
volume variation as a function of the pulsation. The use of a manometer
and a set of vertical tubes was proposed to obtain constant pressure
and compare two pumps built for this purpose. The first pump was built
with ramps at the inlet and outlet of the rollers, which served as
a benchmark, which resulted in a pressure variation of 2.68 s2. On the other hand, the second pump, built with the concepts
and optimizations of a studied model, produced a variance of 0.025
s2. The pumps were installed on an Ultimaker 3D printer,
and print images were obtained. It is possible to observe the absence
of material caused by the removal of the roller over the tube in pump
A, while in pump B, this phenomenon did not occur, showing that the
pulsation was reduced. Thus, it is evident that it is possible to
use peristaltic pumps to pump fluids in 3D bioprinters and other devices
that require precise dosages. Pump B shows a reduction in the width
of the trace, indicating that there was less deposition of the biomaterial.
This effect was not relevant in the three-dimensional printing with
the proposed biomaterial, maintaining the expected quality and uniformity.
However, the author suggests the use of a silicone tube with thicker
or reinforced walls, which prevents the tube from expanding at higher
pressures, which occurs when the biomaterial has a higher density
or the outlet diameter is small, the printing of more complex 3D models,
dimensional lifting of the printed models, and exhaustive tests with
different biomaterials.
Authors: Shashank Acharya; Wenjun Kou; Sourav Halder; Dustin A Carlson; Peter J Kahrilas; John E Pandolfino; Neelesh A Patankar Journal: J Biomech Eng Date: 2021-07-01 Impact factor: 1.899