# Performance evaluation of multi-stage open-loop impedance pump

- V. C. C. Lee
^{1}Email author, - Y. A. Abakr
^{2}and - K. C. Woo
^{2}

**12**:11

**DOI: **10.1186/s40712-017-0079-1

© The Author(s). 2017

**Received: **9 January 2017

**Accepted: **1 March 2017

**Published: **15 March 2017

## Abstract

### Background

Impedance pump is a simple valveless pumping mechanism, which transports fluid through the mismatch of impedance in the system. Mismatch in impedance occurs when an asymmetrical periodic excitation is exerted on the elastic tube. Periodic asymmetrical excitation will then produce a unidirectional flow. Considering a multi-stage system with a single and constant power source, it is well expected that there would be pumping limitation to which the enhancement can reach.

### Methods

A multi-stage open-loop impedance pump is developed in the current work. The current work experimentally analyzes and evaluates the pumping performance of a multi-stage open-loop impedance pump, with emphasis on the flow rates induced and pumping limitation. Analyses of flow rates, pressure head and excitation frequencies are performed in its non-dimensional form.

### Results

Taking a single-stage system as benchmark, enhancement of 35 and 33.3% is shown in the flow rate and pressure head respectively for a two-stage system. Enhancement of 110 and 60% is shown in flow rate and pressure head of a three-stage system in comparison to the single-stage system. For four-stage system, however, only 27 and 46.7% increments are demonstrated in the flow rate and pressure head, respectively.

### Conclusions

The implementation of multi-stage system with single constant power input is demonstrated to be limited only to the three-stage system where the declined pumping performance is exhibited in a four-stage system.

### Keywords

Valveless Multi-stage Impedance pump Performance evaluation Limitation## Background

Impedance pump is a simple pumping mechanism, which transports liquid through the mismatch of impedance in the system. It is very simple in design and offers a promising new technique for producing and enhancing flow rates for both macro- and micro-scale devices (Avrahami and Gharib 2008; Rinderknecht et al. 2005).

Impedance pump is a type of valveless pump which does not require vanes or blades to operate. In addition, it offers a low-noise and low-energy alternatives to current pumping system (Lee et al. 2011). A typical open-loop impedance pump consists of an elastic tube, connected to rigid tubing, where the rigid section is connected to a reservoir. Excitation at a single location (not in the middle) of the fluid-filled elastic tube will result in unidirectional flow. This is due to the mismatch in impedance in the elastic tube. Such pumping mechanism has shown to be highly sensitive towards the impedance in the tube, the location, and excitation frequency (Avrahami and Gharib 2008; Lee et al. 2015; Manopoulus et al. 2006; Hickerson 2005; Timmermann and Ottesen 2009).

The first demonstration of valveless impedance pumping was performed by Gerhart Liebau in 1954, using an elastic tube connected to reservoirs at different heights (Liebau 1954, 1955). Following Liebau’s work in 1954, there have been several works studying the underlying physics of the system, be it numerical or experimental. The major contributions include Hickerson in 2005, Loumes in 2007, Rosenfeld in 2010, Meier in 2011, and Lee in 2014. All these works show significant milestones in the advancement of impedance pump, emphasizing on the exploration and application of impedance pump in different domains. To date, three designs of flow rate enhancement impedance pumping system were reported.

Loumes introduced a concept on multi-layer bio-inspired impedance pump. Flow output and inner wall motion are found to be highest at the resonant frequency. Excitation force needed to produce a significant flow was demonstrated to be relatively smaller than a single-layer pump. Having said, with the similar excitation force, a larger flow rate can be induced. This design is operating at a single-stage system configuration. In 2010, Rosenfeld’s studied on the effects of sequential excitations on a single elastic tube and showed promising results where increase in flow rates was observed (Rosenfeld and Avrahami 2010). Similarly, Lee worked on a two-stage system, integrated from two single-stage systems (Lee et al. 2013, 2014), and also showed an enhancement in the flow rates. However, Rosenfield’s design showed higher complexities, where synchronizations of locations and excitation frequencies are prerequisites for an efficient pumping. Lee’s design, on the other hand, is much simpler as the operating conditions are similar to a single-stage system. Locations and excitation frequencies for pumping are shown to be unaffected by the multi-stage configuration. The interim reservoir in between stages has also showed to be a valuable part of the system, serving as the driving mechanism in flow rate enhancement (Lee and Chong 2016).

While enhancement in flow rates is shown possible, there lies a question to which the enhancement can sustain under single and constant power source. The current work analyzes and evaluates the pumping performance of such a multi-stage open-loop impedance pump, with emphasis on the flow rates induced and pumping limitation.

## Methods

- (i)
A conventional single-stage system

- (ii)
A two-stage system

- (iii)
A three-stage system, and

- (iv)
A four-stage system

*x*

_{ i }will be used to denote the instantaneous location of the mechanism while

*L*

_{ i }represents the total length of the elastic tube. Subscript,

*i*, of 1–4 will be used to represent four different tubes. All four excitation mechanism is fixed at tube location \( \raisebox{1ex}{${x}_i$}\!\left/ \!\raisebox{-1ex}{${L}_i$}\right. \) = 0.1. Detailed experimental methods and materials are available in Ref (Lee et al. 2014). Water is used as the working fluid in all experiments.

*α*), as expressed in Eq. (1)

*Q*) are normalized against the highest induced flow rate in a single-stage system for better illustration of the enhancement (Eq. 2). Pressure head (

*H*) is normalized with respect to the initial pressure head at height of 250 mm (Eq. 3).

*c*, as shown in Eq. 4,

*c*, as a function of the tube and fluid properties, the resonant frequency hence becomes

where

*r* is the radius of the tube

*ρ* is the water density

*ω* is the excitation frequency

*μ* is the coefficient of liquid viscosity

*E* is Young’s modulus of the elastic tube, and

*h* is the thickness of the tube

Resonant frequency is theoretically calculated to be 4.8 Hz using Eq. (5). Hence, a range of frequencies around the resonant frequency will be experimented to obtain the excitation frequency nearest to the resonance.

## Results and discussion

Pumping performance of a multi-stage open-loop impedance pump was analyzed and evaluated. This section consists of five subsections. First four subsections discuss on the pumping performance of each stages. The fifth subsection discusses the performance analyses and evaluation of a multi-stage system.

### A single-stage system

^{−1}at the Womersley number of 79.7 which corresponds to frequency of 4.5 Hz. This point of interest will serve as the benchmark pumping rate for comparison with the multi-stage systems of two-stage, three-stage, and four-stage systems. As shown in Fig. 2, the highest pumping rate occurs at the Womersley number of 79.9 (4.5 Hz), marking this number to be the resonance condition which is predicted theoretically to be 4.8 Hz with a difference of 6.3% due to the physical limitation of the actuators. Due to the instrumental limitation of hardware, the actuator was unable to work with frequency of 4.8 Hz. Hence, frequency interval of 0.5 is used instead. Frequency for efficient resonant pumping was located to be at 4.5 Hz. A plot of flow rate against pressure head (

*Q*−

*H*diagram) is shown in Fig. 4, indicating the flow development in a single-stage system.

The relation between *Q* and *H* is portrayed as a sinus-like curve. *Q* is normalized such that the maximum achievable flow rate is denoted as 1 while *H* is normalized with respect to the initial pressure head at water level of 250 mm in the reservoir. *Q*
_{1} is the flow rate observed in the left reservoir, shown to be the source reservoir while *Q*
_{2} is the flow rate observed in the right reservoir, the deliverable reservoir. *Q*
_{1} shows a negative flow rate indicating a decrement in the pressure head while *Q*
_{2} shows a positive flow rate indicating an increment in the pressure head. This shows that the transportation of water occurred in a unidirectional from left to right. The highest flow rate in the decreasing reservoir, *Q*
_{1}, is observed to be at the pressure head of 0.25 while for the increasing reservoir, *Q*
_{2}, is observed to be at 0.5; indicating the pumping work in the decreasing reservoir is higher than the increasing reservoir. This phenomenon is due to the impedance difference along the tube. At the compression location, \( \raisebox{1ex}{${x}_i$}\!\left/ \!\raisebox{-1ex}{${L}_i$}\right. \) of 0.1, the impedance at the right end tube is smaller as compared to the left end tube. Therefore, the water would tend to move towards the region with lesser impedance. As the water flow through the tube, pressure gradient between both reservoirs changes as well, creating a higher pressure in the right reservoir. With higher pressure in the right reservoir, the forces required to overcome the fluid inertia in the reservoir hence increases, thus required longer time to reach a higher pressure head.

### A two-stage system

*Q*−

*H*diagram of a two-stage system is plotted and shown in Fig. 5.

*Q*

_{1}represents the flow rate measured in the left reservoir,

*Q*

_{2}is the flow rate in the middle reservoir, and

*Q*

_{3}is the flow rate measured in the right reservoir. The flow rates are normalized based on the highest flow rate found in a single-stage system that serves as benchmark of 1.0. In Fig. 5, the main transportation work is observed to be from the left reservoir to the right reservoir. It is shown such that

*Q*

_{1}is in the negative direction showing water flowing out of the reservoir while

*Q*

_{3}is in the positive direction indicating water flowing in.

*Q*

_{2}on the other hand is shown to be oscillating at the initial level with pressure head of ±0.1 and flow rate of ±0.8. This shows that with a two-stage system, the middle reservoir serves as a transportation medium between the two end reservoirs. Similar phenomenon is also shown numerically in Ref (Lee and Chong 2016). The highest flow rate for

*Q*

_{1}and

*Q*

_{3}is observed to be at pressure head of 0.3 with flow rates of −1.5 and 1.35, respectively. The maximum pressure head of ±0.8 is shown where the flow rate reaches zero reading, giving a total pressure head of 1.6.

### A three-stage system

*Q*

_{1}, is observed to increase drastically to the maximum flow rate at pressure head of −0.16, where gradient is shown to be extremely steep. The flow rate is then gradually decreases to −0.64 with very small gradient and stops at the maximum pressure head of −0.8. Similarly, for flow rate in the second reservoir,

*Q*

_{2}stops at pressure head of −0.8, the formation to the maximum flow rate is however different such that the flow rate is observed to gradually increase to maximum at a pressure head of −0.64. Drastic drop is then observed from −0.64 to −0.8. Based on the figure, both

*Q*

_{1}and

*Q*

_{2}are shown to have negative flow rates indicating them as the source reservoirs for the system.

Flow rate in the third reservoir, *Q*
_{3}, is observed to have positive flow indicating water flowing into the reservoir. The maximum flow rate is observed at pressure head of 0.16; the flow rate is then shown to decrease and stop at pressure head of 0.48. Based on the curve, flow rate in the third reservoir is observed to be minimal. Looking into *Q*
_{4}, high positive flow rate is observed to reach a maximum of 2.1 at pressure head of 0.16. Flow rate is then observed to decrease gradually until pressure head of 1.12. Based on the curves, it is observed that the main deliverable pumping work is from *Q*
_{1} and *Q*
_{2} to the last two reservoirs where flow rates are shown to be very high. Deliverable rates are observed to have double increment of 1.1 than the single-stage system. Normalized increment of 0.7 is observed between the two- and three-stage systems.pt?>

### A four-stage system

*Q*−

*H*diagram for a four-stage system. Based on the figure, it is shown that the source of water transportation is from

*Q*

_{1}and

*Q*

_{2}. The main source is shown to be

*Q*

_{1}, while

*Q*

_{2}is shown to be the secondary source similar to the three-stage system. The curve trend is however different such that

*Q*

_{1}reduces more drastically as compared to the three-stage system; maximum flow rate is observed to be at the similar pressure head of −0.16.

*Q*

_{2}is observed to have similar trend for both three- and four-stage system where the maximum flow rate is observed to be at −0.48. Flow rate at the intermediate reservoir,

*Q*

_{3}, is observed to oscillate around the initial pressure head, similar to the curve shown for two-stage system as shown in Fig. 5.

*Q*
_{4} and *Q*
_{5} are observed to be the deliverable reservoir where positive flow rates are shown in Fig. 7. *Q*
_{4} shows minimal flow rate and stops at pressure head of 0.48, similar to the curve shown in the three-stage system. *Q*
_{5} on the other hand shows a higher flow rate as compared to *Q*
_{4}. *Q*
_{5} represents the final deliverable flow rate for a four-stage system and based on the flow rate shown; *Q*
_{5} is obviously lower than the three-stage system, indicating that for a multi-stage open-loop impedance pump, the maximum number of stages that can be implemented with notable and significant enhancement is only limited to three-stages. It should be noted that this limitation is subjected only to a single and constant power source.

### Performance analysis and evaluation

Performance of different stages in multi-stage open-loop impedance pump as function for pressure heads and flow rates was compared and analyzed. The performance was compared non-dimensionally where the pressure head is with respect to the initial pressure head at water level of 250 mm and the flow rate is with respect to the maximum flow rate induced (7.64 L min^{−1}) in a conventional single-stage system. Performance of a single-stage system was made the benchmark of comparison where the highest flow rate achieved is normalized to the number of 1. The pressure head on the other hand was observed to reach the highest increment of normalized value 0.6 giving a total pressure head difference of 1.2. The *Q* − *H* diagram of a single-stage system charting the performance of single-stage system is shown in Fig. 4.

Extensive experiments were performed for the two-stage impedance pump on the complex parameters governing its performance. A maximum pressure head of 0.8 was obtained giving a total pressure head difference of 1.6; this indicates an improvement of 33.3% on the achievable pressure head difference. The highest flow rate of 1.35 was induced in the two-stage system, showing an improvement of over 35% on the instantaneous flow rate in the system. Water was however observed to be oscillating at its initial water level in the interim level for a two-stage system. The interim reservoir also shown to be the transportation and driving mechanism for flow rate enhancement (Lee and Chong 2016).

Percentage differences comparison of maximum achievable head and flow of different stages of impedance pump

Stage (s) | Pressure head (%) | Flow rate (%) |
---|---|---|

1 | Benchmark | Benchmark |

2 | 33.3 | 35 |

3 | 60 | 110 |

4 | 46.7 | 27 |

Figure 7 shows the *Q* − *H* diagram of a four-stage system. A maximum pressure head of 0.96 with a total pressure head difference of 1.76 and maximum flow rate of 1.27. Comparing with the previous trend of performance of multi-stage system, the four-stage system had obviously decreases in its performance. A performance increment of 46.7 and 27% was observed in the pressure head and flow rate respectively as compared to a single-stage system. Improvement of 10% in pressure head was shown comparing with two-stage system; it was however shown a decrease of 5.9% comparing flow rate in four- and two-stage system. A complete decrease in performance was observed when comparing with the three-stage system where a percentage decrement of 8.3 and 39.5% was observed for the pressure head and flow rate, respectively.

*Q*−

*H*performance with respect to number of stages is presented in Fig. 8.

## Conclusions

For a multi-stage system drawing power from a single constant power source, it is well expected that there would be a limitation to which the enhancement can reach. Analysis and evaluation on the pumping performance of such a multi-stage system are conducted in the current work to study the highest possible enhancement with the increase of stages, as well as the system’s limitation. All studies are conducted using only a single power source of 720 W. A single-stage system was made the benchmark of multi-stage system here, where a normalized flow rate of 1 and normalized pressure head of 0.6 are established. With the increase in the number of stages, an improvement in the performance is observed. Enhancement of 35 and 33.3% is shown in the flow rate and pressure head respectively for a two-stage system. Enhancement of 110 and 60% is shown in flow rate and pressure head of a three-stage system in comparison to the single-stage system. For four-stage system, however, only 27 and 46.7% increments are demonstrated in the flow rate and pressure head, respectively. The implementation of multi-stage system with single constant power input is demonstrated to be limited only to the three-stage system where the declined pumping performance is exhibited in a four-stage system.

## Declarations

### Acknowledgements

The authors would like to thank the Ministry of Science, Technology and Innovation of Malaysia for providing the financial support in this project; Faculty of Engineering and Science (Curtin University Sarawak) and Faculty of Engineering (University of Nottingham Malaysia Campus) for providing the facilities and equipment for conducting this research.

### Authors’ contributions

VCC conducted the experimental work, and contributed the major part of the paper. YA and KC participated in the analysis and evaluation of experimental data. All authors read and approved the final manuscript.

### Competing interests

The authors declare that they have no competing interests.

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## Authors’ Affiliations

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