Open Access Article
Martin
Andersson‡
a,
Sofia
Johansson‡
a,
Henrik
Bergman
a,
Linhong
Xiao
b,
Lars
Behrendt
*b and
Maria
Tenje
*a
aDept. Materials Science and Engineering, Science for Life Laboratory, Uppsala University, Box 35, 751 03 Uppsala, Sweden. E-mail: maria.tenje@angstrom.uu.se
bDept. Organismal Biology, Science for Life Laboratory, Uppsala University, Norbyvägen 18 A, 752 36 Uppsala, Sweden. E-mail: lars.behrendt@scilifelab.uu.se
First published on 23rd March 2021
This work describes a programmable heat-stage compatible with in situ microscopy for the accurate provision of spatiotemporally defined temperatures to different microfluidic devices. The heat-stage comprises an array of integrated thin-film Joule heaters and resistance temperature detectors (RTDs). External programming of the heat-stage is provided by a custom software program connected to temperature controllers and heater–sensor pairs. Biologically relevant (20–40 °C) temperature profiles can be supplied to cells within microfluidic devices as spatial gradients (0.5–1.5 °C mm−1) or in a time-varying approach via e.g. step-wise or sinusoidally varying profiles with negligible temperature over-shoot. Demonstration of the device is achieved by exposing two strains of the coral symbiont Symbiodinium to different temperature profiles while monitoring their single-cell photophysiology via chlorophyll fluorometry. This revealed that photophysiological responses to temperature depended on the exposure duration, exposure magnitude and strain background. Moreover, thermal dose analysis suggested that cell acclimatisation occurs under longer temperature (6 h) exposures but not under shorter temperature exposures (15 min). As the thermal sensitivity of Symbiodinium mediates the thermal tolerance in corals, our versatile technology now provides unique possibilities to research this interdependency at single cell resolution. Our results also show the potential of this heat-stage for further applications in fields such as biotechnology and ecotoxicology.
The increasing frequency of warming events causes biological impacts across our planet and one ecosystem particularly afflicted by thermal stress is coral reefs, one of the most biodiverse and productive ecosystems. Corals gain >70% of their energy through a symbiotic relationship with photosynthetic microalgae from the genus Symbiodiniaceae (Dinoflagellata).2 Increasing temperatures can provoke coral ‘bleaching’, a process by which Symbiodinium disappears from the coral tissue through an essentially unknown mechanism. The frequency of these bleaching events has increased over the past decades and coral reefs are now facing near extinction due to the effects of global warming. The severity of bleaching is intimately linked to the thermal resilience of Symbiodinium, which has been intensively studied on the bulk level within and between species.3,4 Proposed strategies for mitigating coral bleaching include rearing coral stocks with enhanced stress tolerance via assisted evolution5,6 or experimental evolution of Symbiodinium cultivars.7 These strategies, however, seldom take into account the phenotypic heterogeneity among single cells of Symbiodinium, which could reveal genotypes with increased resistance towards environmental stress as found in, e.g., bacterial populations.8 Mapping the photosynthetic response of single-cells of Symbiodinium under thermal stress in vitro could therefore have immediate consequences for our understanding of coral thermal resilience in situ and could possibly provide new avenues for coral reef restoration.
Microfluidics has emerged as a key technology for characterizing phenotypic variations in populations of single cells under external perturbations. For example, microfluidic platforms are used to measure viability and Ca2+ flux of single mammalian cells,9 map real-time growth rates of single bacteria to monitor antibiotic susceptibility10 and determine phenotypes of single microalgal cells co-cultured with bacteria.11 Key to this success is the ability of microfluidic platforms to physically immobilize several thousands of single cells, often using hydrodynamic forces or mechanical features such as wells, pillars or channel restrictions at precisely defined locations12 and then deliver external physico-chemical stimuli to those same sites. Stimuli can be in the form of drugs or toxins delivered via integrated microfluidic channels or pressure delivered via integrated microelectromechanical actuators.13 Due to the small size of microfluidic channels, only minimal sample and reagent volumes are required, which reduces costs, shortens reaction times and enables biochemical studies where sample materials are scarce.
To reliably measure the effects of thermal stress on organisms within microfluidic systems, providing accurate temperatures is essential. One approach is to mount the microfluidic system inside a small incubator providing a well-defined and stable temperature.14–17 However, these systems often require long ramping times and offer limited possibilities to cycle temperatures or deliver well-defined gradients of temperatures across the microfluidic devices. For precise temperature control on-chip, miniaturised heaters are typically used, such as Joule heaters increasing the temperature through conversion of electrical energy to heat via resistive losses.18 Several microfluidic systems use this principle of operation via microstructured thin-film metal electrodes,19,20 screen printed electrodes21 or conductive liquids.22 However, these systems integrate the temperature control within the microfluidic device and are typically developed for a single application, meaning that their use in other areas is limited. Further, sterility requirements often limit them to single-use, which increases costs and reduces usability of these temperature control systems.
Here, we present a reusable modular temperature regulation system that can be combined with interchangeable microfluidic systems of various designs. By placing the microfluidic chip immediately on the temperature control stage via a thin film of immersion oil and using active liquid cooling, a powerful and versatile system with spatiotemporal temperature regulation is created. This represents a technological advancement over more rigid fixed-design systems where the temperature control and microfluidics device are combined. The facile chip mounting is achieved by providing a flat surface by using thin-film Joule heaters and RTDs, recessed into the top glass plate of the heat-stage. The temperature regulation system is capable of providing stable temperatures in the range of 20–40 °C to cells immobilized within microfluidic chips. Importantly, biologically relevant temperatures can be supplied to the cells in the form of spatial gradients or in a dynamic, time-varying fashion. In this study, the functionality of the temperature regulation system was demonstrated by combining it with a microfluidic device with an array of 16
500 individual microwells containing single cells of two strains of Symbiodinium. The photophysiological changes occurring in single cells under temperature perturbations were assessed via pulse amplitude modulated chlorophyll fluorometry (PAM) imaging. We suggest that this novel engineering approach provides a powerful and versatile platform for single cell investigations of photosynthetic stress resilience and heterogeneity under recreated spatiotemporal thermal exposure profiles.
Cooling of the heat-stage was achieved by flowing deionized water through a 120 μm deep and 12 mm wide channel embedded in the glass substrate of the heat-stage. The cooling channel was fabricated through wet etching and fusion bonding of two separate glass wafers. To find a suitable design of the cooling system, heat transfer was modelled using FEM in COMSOL to compare active and passive cooling. From this (data not shown), we concluded that active liquid cooling stretching several mm outside of the temperature control window provides the best performance. The resulting design is displayed in Fig. 1A and S5B.† Further, the cooling channel was deliberately placed between the objective and the Joule heaters to prevent heating of high-magnification objectives where immersion oil could act as a thermal bridge.
For cell experiments, the heat-stage was assembled with a PDMS–glass microfluidic chip. The microfluidic chip was assembled on top of the heat-stage by adding a drop of immersion oil in between the two devices. The three single-cell arrays of the microfluidic chip (each with 5500 microwells across an area of 1.53 mm × 5.80 mm) were aligned to the heaters under a stereo microscope (Fig. 1B and S5†). Scotch tape was added to secure the attachment of the chip.
The temperature-controlling unit (Fig. 1D) interfaces the heat-stage with the software. The unit delivers power to the heaters, transduces the signals from the RTDs and controls the feedback system. Temperatures were set by modifying the power levels supplied to the heaters via pulse-width-modulation. Here, each heater was connected to a supply voltage of 12 V in series with an NPN switching transistor, which was in turn connected to ground. The transistor was switched ON and OFF by the pulse-with-modulated signal from the microcontroller with a 12 bit resolution in a given duty cycle and, hence, the applied power across the heaters could be controlled with the same resolution. The RTDs were transduced by the temperature controller using RTD-to-digital converters with a resolution of up to 0.0534 °C. A detailed description of the hardware of the system is found in ESI† section 4.
Even though the preferred mode of operation for any application is automatic mode as this allows the operator to select temperatures rather than power levels, the inherent properties of the heat-stage are best characterized by running it in manual mode. For this evaluation, the power applied to the heaters was increased from 0 to a constant value of 300 mW at t = 0. The responses of the six heaters were analyzed to find steady-state temperatures, time constants and sensitivities for different flow rates of cooling liquid (Fig. S1†). The experiments were repeated with and without a reference chip attached to the heat-stage to mimic the effect of having a microfluidic device attached to the heat-stage and to evaluate the resulting heat transfer. The time constants, τ, which are found by modelling the response as a first order system, demonstrated a decrease with increasing flow rate and an increase as the reference chip was placed on the stage (ESI† section 2). Under normal operating conditions (with the chip attached and 60 μl min−1 cooling flow), τ was in the order of 150 s and reached a steady-state temperature of about 50 °C when applying 300 mW. The sensitivity, which is calculated as the applied power divided by the steady-state temperature, was largely independent of whether a chip was present on the stage or not (ESI† section 2). A higher sensitivity, as seen for low cooling liquid flow rates, requires a high resolution of the applied power to be able to fine-tune the desired temperatures. The 12 bit resolution, i.e. 4092 discrete power levels, facilitated in the temperature regulation system met this demand. For the lower sensitivity, seen for high cooling liquid flow rates, a higher maximum power is required to be able to achieve a fast response when operated in automatic mode. In this study, the maximum power was limited to 300 mW; however the same hardware would be able to operate at powers up to 2.4 W, a limit which is set by the switching transistors with a maximum allowed current of 200 mA at 12 V.
The resulting sensitivities and time constants have implications on the optimization of the P and I coefficients of the temperature controller. As the sensitivity is essentially independent of loading the stage with a chip, the P coefficient could be set as the same value for different chips. However, the sensitivity and hence the P coefficient are dependent on the cooling flow rate. Time constants depend on both the chip and flow rate, and therefore, the I coefficient has to be optimized for each given flow rate and chip size in this study. In future work, this could be implemented by using adaptive tunings, which are functions of both the measured flow rate and the mass of the chip.
For operation in automatic mode, the P and I coefficients of the controller were selected as a trade-off between rapid temperature change and avoiding any temperature overshoot. It should be noted that as the feedback loop runs continuously, the temperature of the stage will remain at the desired setting despite drift in the steady-state temperature of the heaters or changes in the environment, such as room temperature or placement of a microfluidic chip on the stage. Thermally responsive liquid crystal sheets were used to confirm the uniformity of the temperatures across the temperature control stage and only minor deviations were detected (Fig. S3†). In this work, we demonstrated temporal temperature profiles with step-wise increasing and oscillating profiles as well as a spatial linear temperature gradient across the area (Fig. 2). In addition, the versatility of the temperature regulation system makes it possible to produce a wide set of other spatiotemporally controlled temperatures, which are not described here.
500 microwells, which was subsequently attached to the heat-stage. During all thermal exposure experiments, cells were kept under complete darkness.
Thermal stress can affect the stability of photosystem constituents and repair processes,3 which can affect the cells' ability to photosynthesize. Previous experiments25 systematically tested the timing of thermal adaptation in Symbiodinium by growing cells at 25 °C, transferring them to 30 °C and subsequently measuring their Fv/Fm at different time intervals. This revealed that 6 h of incubation at 30 °C significantly enhanced the thermal tolerance of Symbiodinium (compared to 0 h of incubation) and that this thermal acclimation was associated with de novo synthesis of proteins. The time required for de novo synthesis of proteins (∼6 h) was thus considered a suitable duration of thermal acclimation in our experiments with Symbiodinium.
To quantify the effect of varying durations of temperature stress on Symbiodinium, three different temperature experiments were performed:
i) Short-term: single cells were exposed to a step-wise increase of +1 °C each with a duration of 15 min per step,
ii) Long-term: single cells were exposed to a step-wise increase of +1 °C each with a duration of 6 h per step
iii) Sinusoidal: single cells were exposed to a sinusoidal temperature profile with a period of 30 min and repeated several times.
Our a priori assumption for experiments i) and ii) was that cells exposed to short-term thermal stress (<6 h) would not be able to acclimate their photometabolism to elevated temperatures, whereas cells exposed to long-term thermal stress (>6 h) would have enough time to do so. Based on previous works,26–28 we also expected considerable heterogeneity among single cells of Symbiodinium in their ability to withstand thermal stress events.
Time-resolved temperature exposures were accomplished by running the temperature regulation system in automatic mode. During the start-up procedure, the adaptive functionality of the temperature controller was used where the P and I coefficients were reduced by a common factor to avoid any risk of temperature overshoot when setting a pre-conditioning state at 22 °C, which is the nominal cultivation temperature of Symbiodinium. After start-up, the P and I coefficients were set back to their optimized values, giving +1 °C step-increase in about 40 s with minimal overshoot (∼0.1 °C for each step-increase). It is noted that the noise level of the read-out from the RTDs increased for higher temperature, an effect that is attributed to thermal noise generated by some of the electrical components (Fig. S2†).
Long-term temperature exposures consistently caused more dramatic declines in Fv/Fm than short-term temperature exposures. For example, in CCMP2467 temperatures of +5 °C reduced Fv/Fm by 13% in short-term exposures and by 29% in long-term exposures. In CCMP421, a similar effect was observed, although less pronounced. Here, short-term exposures to +5 °C reduced Fv/Fm by 4.7%, whereas long-term exposures caused a reduction of 6.7%. These data suggest that prolonged thermal stress exposure decreases the ability of both Symbiodinium CCMP2467 and CCMP421 to effectively photosynthesize when compared to short-term thermal exposures. At first, these result seem to contradict our hypothesis on metabolic adaptation of the Symbiodinium strains but further analysis of the relationship between intensity and duration of thermal stress is given in section 2.5.
The observed variability in single-cell Fv/Fm between both strains of Symbiodinium was high, both during pre-stimulus conditions (i.e. 22 °C) and during elevated temperatures (Fig. 3). Measuring and tracking this variability over the entire experimental duration enabled the identification of single cells with Fv/Fm values that were two standard deviations (SD) above or below the population average as marked in red and blue, respectively (Fig. 3). Notably, cells with above average values of Fv/Fm consistently outperformed cells with below average values of Fv/Fm in their ability to withstand increasing thermal stress throughout experiments. These data highlight that populations of single cells contain variable phenotypes which differ in their ability to withstand temperature stress of varying durations. Such population characteristics go undiscovered in typical bulk approaches yet could be exploited to, e.g., select specific cells with desirable traits for the assisted evolution of Symbiodinium or other biotechnologically important unicellular microalgae.
Temperature gradients were produced with good linearity for slopes ranging from 0.1 °C mm−1 to 2.5 °C mm−1. The gradients used T = 24 °C as the set-point for the heater nearest the inlet of the cooling channel as shown in Fig. 5A. Regression analysis demonstrated linearity for 1.1 °C mm−1 (r2 = 0.99992) (Fig. S2†). For slopes ranging from 0.5 °C mm−1 and below, r2 decreased as the temperature differences approached the noise floor of the RTDs (Fig. S2†). At steep slopes, i.e. >1.5 °C mm−1, the linearity was reduced as the cooling channel was unable to remove a sufficient amount of excess heat closest to the inlet. To expand the range of possible linear temperature gradients realized by future users, the flow rate of the cooling liquid could be increased (thereby increasing the cooling at the low temperature side) or the set-point temperature at the low temperature side could be increased (thereby increasing the temperature differences between the cooling liquid and the heat-stage surface). Either approach would result in improved linearity also at slopes above 1.5 °C mm−1.
To qualitatively assess the photophysiological effects of a spatial thermal gradient, cells of Symbiodinium CCMP2467 were immobilized within microwells and assessed for their Fv/Fm. First, the cells were exposed to a homogeneous temperature of 25 °C (applied to all heaters for 20 min) and afterwards exposed to a linear temperature gradient (‘stimulus’) of 1.2 °C mm−1 for 6 h with a low temperature set-point of 25 °C. A temperature of 25 °C was chosen as a set point since previous experiments concluded that no severe effects on Fv/Fm were observed for temperatures lower than 25 °C (Fig. 3A and B). To visualize the temperature gradient, a thermally responsive liquid crystal sheet was placed on the stage (Fig. 5B and S3†) and the resulting color changes revealed a linear gradient across the active heating area. We attribute the small deviation from constant temperatures, along the lengths of the individual heaters and RTDs, to the laminar flow profile of the cooling liquid. Three zones were defined on the heat-stage along the thermal gradient (‘inlet’, ‘middle’ and ‘outlet’, referring to their position along the cooling channel) and the types of photophysiology of cells in these three temperature zones were compared (Fig. 5C and D). After 6 h of exposure to this thermal gradient, cells of Symbiodinium were assessed for their Fv/Fm, which revealed a 3.5% (inlet, n = 98), 12.7% (middle, n = 93) and 25.9% (outlet, n = 96) reduction in average Fv/Fm when compared to the average pre-stimulus Fv/Fm (n = 295, data from all heating arenas combined) (Fig. 5C). Histograms of Fv/Fm from before and after exposure to the temperature gradient (Fig. 5D) show a normal distribution that is progressively shifted towards lower average values of Fv/Fm the closer the cells are positioned to the outlet, i.e. the location of the highest temperature in the gradient. Together, this data supports that the heat-stage effectively delivers temperature gradients to immobilized cells of Symbiodinium and that it increased the throughput when operated in this mode. The reduction in Fv/Fm due to elevated temperature is, however, not directly comparable to the reduction that was achieved during short-term stepwise increases in temperature (Fig. 3A and B). We hypothesize that the stepwise increase in temperature causes different photophysiological responses than immediate exposure to single elevated temperature regimes.
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Single-cell data from short- and long-term temperature exposures (Fig. 3) and sinusoidal temperature exposures (Fig. 4) were analyzed to determine the thermal dose at which the photophysiology of Symbiodinium became substantially affected. In this study, cells were considered to be affected by temperature stress when their Fv/Fm decreased for the first time below 50% compared to pre-stimulus values (referred to as D50% or distress dose). The resulting D50% for stepwise increasing temperature profiles revealed that a majority of single cells from both Symbiodinium strains can withstand much higher accumulated thermal doses when these are applied for longer periods (here 6 h) rather than shorter periods (15 min) (Fig. 6A). This can be compared to the temperatures where Fv/Fm decreases below 50% of its initial value for the first time, which are lower for long-term exposures (CCMP2467 = 28 °C, CCMP421 = 33 °C) than short-term exposures (CCMP2467 = 31 °C, CCMP421 = 35 °C). A sustained feature of these measurements is that Symbiodinium strain CCMP421 is more resilient to temperature stimuli than CCMP2467, irrespective of whether the thermal stress is expressed in terms of temperature (Fig. 3) or thermal dose (Fig. 6A), or investigated in short-term (15 min) or long-term (6 h) experiments. To test whether the shape of a thermal exposure profile plays a role in determining the photophysiological effects in Symbiodinium, we designed sinusoidal temperature profiles to give the same thermal dose as those applied during short-term exposures. For both profiles, this enabled us to compare the relationship between accumulated thermal dose and specific temperatures for Symbiodinium CCMP2467 and revealed that cells on average withstood a higher thermal dose under short-term experiments than under sinusoidal experiments (Fig. 6B). We suggest that this observation is a result of the earlier exposure of cells to higher temperatures during sinusoidal experiments than during short-term experiments. Meanwhile, the spread in D50% is larger for the sinusoidal profile than for stepwise increasing temperature exposures. Together these data support that the application of temperature profiles with an identical thermal dose results in different photophysiological outcomes between the two strains of Symbiodinium.
:
11 HAc
:
11 HNO3
:
150 H2O) until the metal was etched through. This was followed by HF etching (49 wt%) to a depth of 120 μm. After stripping in acetone and Mo etch, the wafer was covered in a protective resist layer (S1813, Shipley, spin-cast at 6000 rpm). The fluid inlet and outlet were laser-cut using a pulse frequency of 10 kHz and a pulse peak power of 320 μW (AIO Go 4 mm, Östling marking systems, λ = 532 nm). The wafer was cleaned in acetone while sonicated in an ultrasonic bath.
Prior to bonding, the two glass wafers were cleaned using RCA-1 (1
:
1
:
5 NH4OH
:
H2O2
:
H2O) and activated for bonding using HNO3 (69 wt%) at 80 °C for 10 min, followed by rinsing in DI water. Directly after bonding by a light pressure, the wafer stack was thermally treated at 625 °C under ambient pressure for 6 h. A detailed protocol is provided in previous work.30
Next, thin-film electrodes were defined on the glass wafer stack. A flat top surface was achieved by recessing the electrodes into the glass. First, the solder pads were formed by UV lithography in an image-reversed resist layer (S1813, Shipley, spin cast at 6000 rpm) and trenches were wet etched in the glass using buffered HF (BOE 7
:
1, J.T. Baker). 2/400 nm Cr/Ni electrodes were defined by e-beam evaporation (PVD 75, Kurt J. Lesker Company) and lift-off in acetone. The electrode designs included the line electrodes of the Joule heaters and RTDs and were added using the same lithography process: UV patterning of an image-reversed resist layer (S1813, Shipley, spin cast at 6000 rpm), evaporation of 2/250/5 nm Cr/Ni/Au, and lift-off. Details are found in previous work.23 The electrodes were annealed at 430 °C for 30 min in an Ar environment (Micro TF-6, Koyo Lindberg) and the wafer was diced (DAD 361, Disco) into individual chips. The resistances of the thin-film Joule heaters and RTDs, assessed with a handheld multimeter, were 65–70 Ω and 60–65 Ω, respectively.
The electronic components were surface mounted onto the PCBs. Solder was dispensed using a 0.120 mm solder stencil and a screen printer (ProtoPrint S, LPKF). Components were placed using pick-and-place (ProtoPlace S, LPKF) and soldered using a soldering oven (Protoflow S, LPKF). Soldering was performed in two steps; first, the electrical components were soldered at 230 °C (SMD291AXT4, Chip Quik Inc), second, the thin-film Joule heaters and RTDs were soldered at 175 °C (SMDLTLFP10, Chip Quik Inc).
To connect the cooling flow, polyethylene tubing (ID 0.380 mm) containing an inner stainless steel tube support was mounted into the fluid interface. The tubing was then heated to 145 °C to form a seal and glue (Epo-tec 730, Epoxy Technology) was added to provide strain relief.
The heat-stage was finalized by attaching the PCB of the heat-stage to a 3D printed holder of microtiter plate format to provide a good fit in the microscope and to add the ability to align the microfluidic device (described below) with the heater array.
:
100 dilution, resulting in mid-exponentially growing cultures on the days of the experiments.
The heat-stage with the microfluidic chip was combined with an upright multi-color variable chlorophyll fluorescence imaging microscope (IMAG-RGB; Heinz Walz GmbH, Germany). A detailed description of the microscope system can be found elsewhere.31 Using the saturation-pulse-method, the maximum quantum yield of photosynthetic energy conversion in photosystem (PS) II, Fv/Fm = (Fm − F0)/Fm, was measured in single cells of Symbiodinium. Here Fv, Fm and F0 define the variable, maximal and minimal fluorescence of dark-adapted cells, respectively. Saturation pulses were provided by combining all three RGB (red-green-blue) light emitting diodes resulting in ‘white light’. For both Symbiodinium species, visualization with a 10× objective (Zeiss Fluar 10×/0.5) yielded fluorescence readouts with ∼500–1000 cells per field of view. No noticeable drift in XYZ was observed during experiments. Corrections of beam heterogeneities were made in ImagingWin based on acquired fluorescence images with a homogeneous fluorescence standard in conjunction with a built-in background normalization of subsequent experimental images. After experiments, light transmission images were combined with PAM image stacks within ImageJ32 and registered to avoid artefacts arising from XY shifts. Single cells were manually identified within the light transmission image, and the resulting mask used to quantify Fv/Fm from chlorophyll fluorescence images using an in-house ImageJ script. During all experiments, cells within microwells were perfused with fresh f/2 medium, equilibrated to room temperature, using a non-pulsatile flow of 400 μl h−1 using low-friction 25 ml glass syringes (Hamilton 1000 series, Hamilton Corp.) mounted onto a syringe pump (neMESYS, Cetoni). The flow rate of cooling liquid in the heat-stage was set by applying 40 mbar to a pressure driven pump (MFCS-EZ, Fluigent), which resulted in a flow of about 60 μl min−1.
Footnotes |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/d0lc01288b |
| ‡ M. Andersson and S. Johansson should be considered joint first author. |
| This journal is © The Royal Society of Chemistry 2021 |