Abstract
Deep-sea sponges and their microbial symbionts transform various forms of carbon (C) and nitrogen (N) via several metabolic pathways, which, for a large part, are poorly quantified. Previous flux studies on the common deep-sea sponge Geodia barretti consistently revealed net consumption of dissolved organic carbon (DOC) and oxygen (O2) and net release of nitrate (). Here we present a biogeochemical metabolic network model that, for the first time, quantifies C and N fluxes within the sponge holobiont in a consistent manner, including many poorly constrained metabolic conversions. Using two datasets covering a range of individual G. barretti sizes (10–3,500 ml), we found that the variability in metabolic rates partially resulted from body size as O2 uptake allometrically scales with sponge volume. Our model analysis confirmed that dissolved organic matter (DOM), with an estimated C:N ratio of 7.7 ± 1.4, is the main energy source of G. barretti. DOM is primarily used for aerobic respiration, then for dissimilatory reduction to ammonium ( (DNRA), and, lastly, for denitrification. Dissolved organic carbon (DOC) production efficiencies (production/assimilation) were estimated as 24 ± 8% (larger individuals) and 31 ± 9% (smaller individuals), so most DOC was respired to carbon dioxide (CO2), which was released in a net ratio of 0.77–0.81 to O2 consumption. Internally produced from cellular excretion and DNRA fueled nitrification. Nitrification-associated chemoautotrophic production contributed 5.1–6.7 ± 3.0% to total sponge production. While overall metabolic patterns were rather independent of sponge size, (volume-)specific rates were lower in larger sponges compared to smaller individuals. Specific biomass production rates were 0.16% day–1 in smaller compared to 0.067% day–1 in larger G. barretti as expected for slow-growing deep-sea organisms. Collectively, our approach shows that metabolic modeling of hard-to-reach, deep-water sponges can be used to predict community-based biogeochemical fluxes and sponge production that will facilitate further investigations on the functional integration and the ecological significance of sponge aggregations in deep-sea ecosystems.
Introduction
Sponges are abundant and key ecosystem engineers of the deep sea that occur scattered on soft- and hard-bottomed surfaces and in multi- or mono-specific aggregations (). These so-called sponge grounds create complex habitats and thereby support high local biodiversity (; ; ). As deep-sea sponges process large amounts of water for filter feeding, they are implicated to have an important role in the biogeochemical cycling and benthic–pelagic coupling of carbon (C), nitrogen (N), and silicon (Si) (, ; ; ).
Deep-sea sponges efficiently filter (preferably nano- and pico-) plankton (; ; ) and, similar to their shallow counter parts (), consume dissolved organic carbon (DOC), constituting most of their diet (). The efficiency at which sponges process (e.g., assimilate, respire, release) organic and inorganic nutrients (e.g., C, N) is termed production efficiency, which is an important ecological and metabolic parameter to determine energy (re)cycling in organisms (also referred to as growth efficiency) (; ; ; ) and ecosystems (; ; ). Despite its potential relevance, the C and N production efficiency of deep-sea sponges and most other deep-sea benthos are largely unknown—especially in situ assessments of metabolic rates and conversions—because of the technical constraints of conducting (properly controlled) experiments in the deep sea. Recent advances in technology and accessibility of remotely operated vehicle have increased the ability to collect live deep-sea sponges for ex situ-controlled laboratory experiments (e.g., ; ; ,) and even in situ metabolic rate measurements (; ; ).
Geodia barretti (Porifera, Demospongiae) is one of the best studied deep-sea sponge species. In the North-Atlantic Ocean, along the continental shelf and in fjords, the massive, ball-shaped G. barretti can be present in large densities of up to 0.4–5 individuals per square meter, known as “Geodia grounds” (; ; ). It is considered to be a slow-growing sponge species that, if undisturbed, can reach a meter in diameter, although most specimens have a diameter of 20–30 cm (; ). Oxygen (O2) consumption by G. barretti individuals, combined with biomass estimates from video imaging, indicated that Geodia sponge grounds have high metabolic activity and C demand (ex situ, ; eddy correlation, ). To date, the metabolic C demands of G. barretti have been derived from O2 consumption measurements and a supposed respiratory quotient (RQ) for organic matter (OM) mineralization (O2:CO2). Despite the importance of RQ in estimating the C demand from O2 measurements, its value has never been empirically determined for G. barretti. The RQ values for G. barretti might deviate from values for canonical organic matter mineralization because of the various metabolic pathways conducted by the endosymbionts.
G. barretti is considered as a high microbial abundance (HMA) species, containing a dense and diverse community of microbial symbionts (∼1011 microbes per cubic centimeter) (; ). Microbial symbionts (i.e., the microbiome) and sponge host are a metabolically integrated functional unit, known as a “holobiont.” This, generally considered mutualistic, symbiosis is known to benefit in a variety of ways, which include nutrition, development, defense, and immunity (). In G. barretti, the microbiome is actively involved in the (re)cycling of C and N compounds and, therefore impacts the holobiont nutrition (; ; ). As for many sponge species, anaerobic and aerobic N-transforming processes occur in G. barretti, thereby expanding its metabolic capacity (; ). It has been hypothesized that G. barretti actively controls the oxygenation level of its tissue to maintain aerobic and anaerobic micro-environments that facilitate the co-existence of aerobic and anaerobic symbionts (). The nitrifying and denitrifying potential of the microbial populations within the tissue of G. barretti has been demonstrated by cutting sponges in small fragments (0.3–0.4 cm3) and incubating those pieces under labeled substrates (; ). However, N transformations within intact, pumping G. barretti individuals have yet to be resolved and quantified.
Two studies have examined the C, N, and O2 exchange rates of intact G. barretti individuals. studied larger specimens (∼1-L volume) using the “in–ex” methodology, i.e., sponge filtration rates are combined with the composition of inhalant and exhalant water to obtain release/uptake fluxes. used incubation flow chambers to quantify fluxes for smaller (∼100-ml volume) specimens. Both studies found that G. barretti effectively removed organic C and concluded that the observed organic matter consumption was sufficient to sustain the minimal metabolic needs. found a relatively higher net organic C intake compared to . This difference can be attributed to the smaller size of the individuals tested by , as volume-specific pumping rates may be related to sponge size (). Regarding N, intact G. barretti was found to release nitrate () rather than ammonium (), indicative of net nitrification (), yet the metabolic conversions of O2, C, and N within and exchanges among sponge and symbionts can be complex, and it is not straightforward to derive those from net fluxes obtained by the in–ex and chamber incubation techniques.
To integrate existing experimental metabolic flux data, we constructed a metabolic network model for the holobiont. Metabolic (or stoichiometric) network models are common tools to quantify and predict the intracellular metabolism of, for example, eukaryotic cells and microbes (; ) based on net resource (e.g., C, N) fluxes. Such models are underexplored to quantify sponge–symbiont metabolism, despite their potential to elucidate the intricacies of the sponge physiology and their ecological significance. To date, only one study that employs a genome-scale metabolic network model to reconstruct biochemical conversions in the sponge–symbiont system of the tropical sponge Amphimedon queenslandica exists (). In our study, we applied the metabolic network model to quantify internal and unconstrained C, N, and O2 fluxes of the common and abundant deep-sea G. barretti holobiont. To assess the size dependency of G. barretti metabolism, we compared and separately analyzed the metabolic datasets of and because they assessed different size classes. The size dependency of metabolism is particularly relevant when estimating the metabolic fluxes and metabolic demands of sponge grounds from video images. The outcome of the model advances the understanding on G. barretti metabolism and its potential role in biogeochemical cycling within the vast, benthic deep-sea ecosystems where it abounds.
Materials and Methods
Datasets
The experimental data of and were used to develop and constrain the metabolic network model for larger and smaller G. barretti, respectively, since they cover different size ranges. We refer to their publications (; ) for a full description of sponge collection, experimental procedures, data analyses, and data presentation and only briefly recap some relevant aspects here.
In short, maintained G. barretti individuals in ex situ (running seawater) conditions in the Institute of Marine Research aquarium facilities at Austevoll (Norway) and measured exchange fluxes using the “in–ex” method. The flow rates and O2 uptake of G. barretti were collected simultaneously in 2012 (n = 17, sponge volume = 150–3,500 ml) (Table 1). Dissolved inorganic N [DIN, consisting of , nitrite (, and ] exchange rates and bacterial cell removal were measured in 2011 (n = 53, sponge volume = 125–3,400 ml), and DIN exchange rates and total OC (TOC = DOC + POC) removal were measured in 2014 (n = 29, sponge volumes unknown) (Table 1). converted bacterial cell removal to bacterial C uptake using standard conversion factors and defined DOC uptake as TOC uptake minus bacterial C uptake (Table 1). measured exchange fluxes in G. barretti individuals (n = 12, sponge volume = 9–210 ml) (Table 1) using incubation flow chambers under ex situ (running seawater) conditions in aquarium facilities in Bergen (Norway) in 2017 (n = 9) and 2018 (n = 3). O2, DOC, and living POC (LPOC, consisting of bacteria and phytoplankton C) removal rates were calculated from changes in incubation water and used to calculate a C budget (Table 1; ). For both studies, the incubation water was collected from 160-m depth () and 200-m depth () from nearby fjords, thus representing deep water. This corresponds with the depth range of 200–300 m where G. barretti grounds are typically found ().
TABLE 1
| Dataset | Smaller—incubation chambers () | Larger—in–ex () |
| Volume (cm3) | 9–210 | 150–3,500 |
| C-content (mmol cm–3) | 4.1 | 3.2 |
| Fluxes (μmol cm–3 day–1) | Mean ± SD (n = 12) | Mean ± SD (n = 17 to n = 53) |
| Bacteria-C (r1) | 0.15 ± 0.15 | 0.30 ± 0.11 |
| Phytoplankton-C | 0.0010 ± 0.0013a | n.d. |
| Dissolved organic carbon, DOC (r11) | 25.7 ± 12.3b | 5.2 ± 2.1 |
| O2 (r12) | 11.2 ± 8.1 | 7.7 ± 5.8 |
| (r13) | −0.061 ± 0.47c | 0.0096 ± 0.0032 |
| (r14) | −0.95 ± 0.79c | −0.82 ± 0.53 |
| (r15) | −0.023 ± 0.046c | 0.018 ± 0.013 |
Experimental metabolic datasets of intact Geodia barretti sponges (; ) which were analyzed with the metabolic network model.
Positive fluxes indicate uptake, and negative fluxes indicate release. aPhytoplankton-C assimilation was not included in the model because of its small contribution to organic C uptake. bThe DOC range is larger than the range reported by to match the variation in O2 uptake rates. cDissolved inorganic N flux data are analyzed as part of this study.
DIN Exchange Rates From Incubation Chambers
Changes in DIN (, , and ) were also measured by , but as these data were not presented before, the procedures and the results are presented in this paper. DIN fluxes were determined as follows: duplicate samples for DIN (, , and ) were collected at t = 0, 1, 2, 3, and 4 h in 2017 and t = 0, 2, 4, 6, and 8 h in 2018 from the incubation chambers with acid-washed 100-ml polycarbonate syringes. The samples were subsequently filtered over sterile 0.2-μm polyethersulfone syringe filters (Whatman Puradisc), collected in 10-ml high-density polyethylene vials, and stored at −20°C until further analysis. Nutrients were analyzed in the laboratory with a QuAAtro Gas Segmented Continuous Flow Analyzer. Measurements were made simultaneously for (), , and combined with (). All measurements were calibrated with standards diluted in low-nutrient seawater. DIN exchange rates were calculated from a linear regression slope and incubation volume and corrected with changes in control (i.e., no sponge) incubations. Fluxes were normalized to sponge volume to obtain fluxes in μmol N cm–3 (sponge) day–1 (Table 1, Supplementary Figure 1).
Linear Inverse Modeling Concepts
Metabolic network models are a type of linear inverse modeling (LIM), which are based on mass balances under steady-state conditions. This implies that the internal changes of a substance due to chemical reactions are balanced by the inflow and outflow into a system and that the system can be solved by a set of linear equations (). The steady-state metabolic situation is justified by the rationale that chemical reactions take place on shorter timescales than transport (exchange) fluxes (). As detailed through subsequent sections, LIM of stoichiometric (metabolic) networks requires the following: (1) selection of relevant substances and (chemical) processes and conceptualization of the metabolic network, (2) stoichiometrically balancing of all chemical reactions and construction of mass balances for each substance, (3) constraining model solutions with actual flux measurements or fluxes derived from literature (although LIM can solve for or constrain missing flux data), and (4) mathematically solving the model, including variability and uncertainty analysis (; ; ).
Sponge Metabolic Network Model Concept
The metabolic network model integrates the C, N, and O2 metabolism of G. barretti and consists of both net holobiont metabolism and host versus symbiont-driven metabolism (Figure 1 and Table 2). In detail, sponges rely largely on heterotrophy as they filter the water column for LPOC, consisting predominantly of bacterioplankton in the deep sea (; Table 1) (r1), and consume dissolved organic matter (DOM) (r11). Sponges aerobically respire assimilated organic matter to obtain energy for basal metabolism (r1–r2). The metabolic waste of N is mineralized to (r1–r2). The assimilated organic matter that is not required for basal metabolism is allocated to biomass production (r10). The C (or N) balance for sponges applied in the network model is: assimilation = production + respiration (mineralization in case of N) (; ).
FIGURE 1
TABLE 2
| r | Description | Reactions | Coefficients and ranges (no units) |
| Aerobic consumption | |||
| 1 | Bacteria consumption | fp_N_bac = 0.2–0.8 RQ (O2:CO2) 1-1.16 () C:Nspo = 3.9–4.5 (measured) C:Nbac = 4–6 (; ) | |
| 2 | DOM consumption | fp_N_DOM = 0.2–0.8 C:NDOM = 6–11 RQ and C:Nspo as in equation 1 | |
| Microbial processes | |||
| Anaerobic consumption | |||
| 3 | Denitrification | + 0.5⋅fr_Cdenit⋅C:NDOM⋅φdenit⋅N2 | φdenit0.8 () fp_N_denit = 0.3–0.6 |
| 4 | DNRA | φDNRA0.56 () fp_N_DNRA = 0.3–0.6 | |
| Chemoautotrophy | |||
| 5 | oxidation | ||
| 6 | oxidation | ||
| 7 | Production from nitrification | ||
| 8 | Anammox | →N2 | |
| 9 | Production from anammox | Adjusted from | |
| (Biomass) Production (closure term) | |||
| 10 | Production | Spo→production | |
| Stoichiometric coupling | |||
| - | Production from nitrification | r7=Cfix_ao⋅N:Cspo⋅r5 + Cfixno⋅N:Cspo⋅r6 | Cfix_ao0.073 () range 0.04–0.11 Cfix_no0.022 (), range 0.01–0.03 |
| - | Production from anammox | r9=Cfix_am⋅N:Cspo⋅r8 | Cfix_am0.066 (), range 0.03–0.1 |
Reactions and coefficients involved in C, N, and O metabolism as implemented in the metabolic network model.
The details are explained in the Section “Sponge Metabolic Network Model Concept”. The consumption processes of bacteria (Bacw) [reaction (r) 1] and dissolved organic matter (r2–4) include the production of sponge biomass (Spo) with a source- and process-dependent production efficiency that is explicit for N (fp_Nbac in r1, fp_NDOM in r2, fp_Ndenit in r3, and fp_NDNRA in r4) and implicit for C. The fraction not used for production (1—production efficiency) is respired. The respired C fractions are fr_Cbac in r1, fr_CDOM in r2, fr_Cdenitin r3, and fr_CDNRAin r4 and are dependent on the stoichiometry (C:N) of the sponge (C:Nspo) relative to the source (C:Nbac and C:NDOM). The ratios of electron acceptor per C respired are RQ for O2 and φdenit and φDNRA for NO3 (r1-r4). Chemoautotrophic processes (r5–6, r8) include the production of sponge biomass (Spo) (r7, r9) with a stoichiometric coupling (C fixation efficiency) that is process dependent (Cfix_ao for r5–r7, Cfix_no for r6–r7, and Cfix_am for r8–r9). The reaction numbers (r) correspond to those in Figure 1.
Microbial symbionts expand the metabolic capacity of the sponge host by exploiting metabolic pathways additional to mere aerobic respiration, such as heterotrophy coupled to denitrification (r3) (; ) and dissimilatory reduction to (DNRA) (r4) in anoxic parts of the sponge. The latter process has not been measured, but the accompanying genes (napA, nrfA) were found in G. barretti (Gavriilidou, personal communication). The included chemoautotrophic processes are nitrification in oxic (r5, r6) and anaerobic oxidation (anammox) (r8) in anoxic parts of the sponge holobiont (; ). N2 fixation is not considered in the model since, at present, no genetic evidence exists for G. barretti (). All considered microbial processes yield production (growth) of symbionts, either via anaerobic heterotrophy (denitrification and DNRA) or chemoautotrophy (nitrification and anammox) (r7, r9; Table 2). The production of symbiont biomass is considered an integrative part of sponge holobiont production, as the sponge host can phagocyte and ingest (in an undetermined amount) microbial symbionts that may continuously grow within the sponge tissue, including chemoautotrophic bacteria. The process of assimilation by symbionts (for which genetic evidence exists; Gavriilidou, personal communication) is considered implicit in organic matter consumption (r1–r2), where it functions as an internal feedback loop (from to production). Because of the steady-state approach, production of sponge (holobiont) biomass is treated as a closure term (r10).
Finally, all remaining mass-balanced substances, i.e., DOM (r11), O2 (r12), (r13), (r14), (r15), CO2 (r16), and N2 (r17), have an exchange with the environment (Figure 1).
Reactions and Coefficients
All reactions are stoichiometrically coupled for N and C, with N as base and C derived from the stoichiometry of the substrates. For example, in reaction 2, assimilated DOM is converted to sponge (holobiont) biomass (“Spo”) with a N production efficiency (fp_N_DOM), while the remaining fraction is excreted as (1−fp_NDOM). The C production efficiency (fp_C_DOM) and the fraction that is respired to CO2 (fr_CDOM=1−fp_CDOM) depends on the stoichiometry (molar C:N ratio) of DOM and sponge biomass:fp_CDOM = fp_NDOM⋅ C:Nspo / C:NDOM (Table 2). Reactions 1, 3, and 4 have a similar structure as reaction 2 (Table 2). The measured (molar) stoichiometry of G. barretti biomass “Spo” (C:Nspo) is 4.2 ± 0.29 [n = 20 specimens collected by and ]. The C:N ratios of assimilated food sources (bacteria and DOM) are unconstrained, but experimental studies indicated that G. barretti preferentially assimilates N-rich DOM, with C:N ratios close to or below Redfield (C:N < 6.6) (; ). The C:N ratios of marine bacteria (C:Nbac) are typically 4 to 6, thus below the Redfield ratio (; ; ). The C:N ratios of seawater DOM (C:NDOM) are generally higher, with average C:N ratios of labile DOM of 10.7 (). The C production efficiencies of metazoans typically range from ∼20 to 30%, which would correspond to fp_NDOM of 32–48% on Redfield DOM (C:NDOM = 6.6). However, G. barretti might have a higher fp_N_DOM as heterotrophic symbionts can assimilate into organic N (; Gavriilidou pers. communication). The C production efficiency for denitrification (fp_Cdenit) is ∼25% (; ), and DNRA has a comparable production efficiency (fp_CDNRA)(; ). Depending on the stoichiometry of DOM, the N production efficiencies (fp_Ndenit) and (fp_NDNRA) are expected to range from 30 to 60%. The variability and uncertainty in C:N of the assimilated substrates and production efficiencies were considered in model solutions (Table 2, “Section Model Implementation and Solutions”).
Oxygen is used as electron acceptor in r1 and r2, and the respiratory quotient (RQ; O2 consumed to CO2 produced) depends on the elemental composition of the substrate and the fraction of substrate that is respired (Table 2 and Figure 1). RQ ranges from 1 for oxidation of glucose to 1.16 for complete mineralization of plankton Redfield OM (C:N = 6.6) to (; ). In anoxic parts of the sponge tissue, may be used as an electron acceptor and is reduced to N2 in denitrification (r3, Table 2) and to in DNRA (r4, Table 2). consumption per CO2 produced for Redfield OM in denitrification (φdenit) is 0.8 (r3; ; ). In DNRA, this ratio (φDNRA) is determined as 0.56 (r4; ). In the oxic compartments of the sponge holobiont, is oxidized to (r5) and is oxidized to (r6). oxidation in G. barretti is primarily conducted by archaea, while oxidizers are primarily Nitrospira bacteria (). The energy and the corresponding chemoautotrophic yields are higher for oxidation than for oxidation, with an average reported molar Cfix:Noxidized ratios of 0.073 for -oxidizing archaea () and 0.022 for -oxidizing bacteria (). These chemoautotrophic yields were used to constrain the production of sponge holobiont “Spo” (r7) as a function of r5 and r6 (Table 2 and Figure 1). In the anoxic compartments of the sponge holobiont, anammox takes place (), in which N2 is produced from and by anammox bacteria (r8). The growth and the energy yields of anammox bacteria are well studied; anammox bacteria fix inorganic C coupled to oxidation (r9), with ∼0.07 Cfix: oxidized (; ), which was used to constrain r9 as a function of r8 (Table 2 and Figure 1).
Model Constraints
The metabolic network model is generic and can be applied to any sponge volume, depending on data availability. Since two almost complete metabolic flux datasets were available for G. barretti that covered distinct volumes [9–210 ml () versus 150–3,500 ml ()] and are based on different methods, we quantified metabolism of “smaller” (from incubation chambers) and “larger” (by in–ex) G. barretti individuals separately (Table 1). This not only allowed us to evaluate the potential size dependence of metabolic activities but also provided an independent assessment of the eventual metabolic patterns inferred.
The measured metabolic exchange fluxes (μmol cm–3 day–1) were used to constrain the exchange fluxes of O2 (r12), (r13), (r14), and (r15) for smaller (incubation chambers) and larger (in–ex) specimens (Table 1). For external bacteria uptake (r1) and DOM uptake (r11), the measured bacteria C and DOC uptake fluxes combined with C:Nbac and C:NDOM constrained the model.
In addition, the model was constrained with 13 inequalities (soft constraints), of which 10 stated that all metabolic reactions (r1–r10) must be positive. Furthermore, two inequalities limited DOM consumption in denitrification and DNRA (r3, r4) to be lower than aerobic DOM consumption (r2). Lastly, the anammox rates (r8) were constrained to be limited to a maximum of 20% of denitrification rates (r3) (; ).
Model Implementation and Solutions
The metabolic network model of G. barretti was implemented and solved in the modeling environment R () with R-package LIM (). With 17 unknowns (reactions) and 16 knowns (eight mass balances and eight constraints), the model was almost even determined, resulting in small ranges of possible solutions for each reaction. The (small) ranges in reaction rates were assessed by Bayesian sampling of the solution space with 500 iterations using the function “xsample” (). This resulted in reaction rate values with standard deviations < 4% of average. The variation in reaction rates is mostly depending on model input parameters, which comprises reaction coefficients (e.g., C:NDOM and fp_N_DOM) (Table 2) and constraints (e.g., measured O2 uptake and release; Table 1). However, the linear setup allows only single-parameter values rather than ranges. Inclusion of uncertainty and variability in parameters was achieved by creating one million model input files with values that were randomly sampled from parameter ranges. The ranges for reaction coefficients are as explained in “Section “Reactions and Coefficients”” (Table 2), and the ranges for constraints are mean ± standard deviation (SD) for larger and smaller sponges (Table 1). Only ∼0.2–1.0% of parameter combinations resulted in a feasible model solution, corresponding to 10,088 and 2,228 feasible model solutions for smaller and larger sponges, respectively. The feasibility of parameters to produce successful results gives an indication on the likelihood of these parameter values. A successful input file is available in the Supporting Information. The R code to run the model is available at Zenodo (doi: 10.5281/zenodo.4139792). The model results from all feasible model solutions, and the likelihood of parameter values in smaller and larger sponges was analyzed for mean, SD, and min and max based on 5 and 95% confidence intervals (CI).
Results
Analysis of Measured Flux Data
DIN Exchange in Incubation Chambers
All G. barretti showed a net release of , corrected to control incubations in which concentrations remained constant (Supporting Figure 1), of, on average, 0.95 ± 0.79 μmol N cm–3 day–1 (mean ± SD, used throughout text, n = 12, Table 1). release was positively correlated to O2 consumption (r = 0.82, p < 0.01, n = 12). The and concentrations in the chambers did not significantly change (i.e., the regression slope was not significant) during incubations with sponges and neither in control incubations without sponges (Supporting Figure 1). Although the concentration changes were insignificant, we calculated control-corrected and fluxes to obtain feasible ranges for the metabolic network model analysis. The average (control-corrected) release and release rates by G. barretti in incubation chambers were 0.023 ± 0.069 and 0.061 ± 0.47 μmol N cm–3 day–1, respectively (n = 12, Table 1).
Size Relationships
The datasets of smaller G. barretti individuals (9–210 ml in incubation chambers) and larger G. barretti individuals (150–3,500 ml with in–ex) were analyzed together to explore for allometric relationships in data. A statistically significant allometric relationship was found between sponge volume and O2 consumption rates, although only 21% of the variation could be explained with this regression (Figure 2). The allometric equation for volume-specific O2 consumption rates (vOcr, μmol cm–3 day–1) as a function of volume (V, cm–3) for G. barretti is: vOcr = 25.5⋅V−0.23(p < 0.01, R2 = 0.21, n = 29, Figure 2). No temperature correction was needed since all data were collected at a similar temperature of 8–9°C. At overlapping sizes, O2 consumption rates are comparable between the two datasets (green circle, Figure 2). No allometric relations were found for DIN net exchange data (data not shown).
FIGURE 2
Model Results
The equalities (hard constraints) and inequalities (soft constraints) were internally consistent, as the model was able to resolve an internal metabolic flux network for smaller and larger G. barretti sponges (Table 3). As imposed with measured metabolic flux data (Table 1), almost all model-produced metabolic rates (μmol cm–3 day–1) were higher in smaller compared to larger specimens (Table 3), except the assimilation of bacteria (r1), which was higher in larger sponges (Tables 1, 3). However, the overall relative partitioning of internal C- and N-transforming processes was similar for smaller and larger sponge individuals (Figures 3, 4).
TABLE 3
| Smaller sponges—incubations | Larger sponges—in–ex | |||||||
| C/O2 | N | C/O2 | N | |||||
| Mean | SD | Mean | SD | Mean | SD | Mean | SD | |
| Fluxes (μmol cm–3 day–1) | ||||||||
| Bacteria assimilation (r1) | 0.15 | 0.090 | 0.031 | 0.019 | 0.30 | 0.064 | 0.062 | 0.015 |
| Dissolved organic matter (DOM) assimilation (r2) | 14.0 | 4.5 | 1.9 | 0.74 | 4.4 | 1.1 | 0.60 | 0.17 |
| Denitrification (r3) (DOC-) | 0.81 | 0.62 | 0.47 | 0.35 | 0.19 | 0.16 | 0.11 | 0.09 |
| DNRA (r4) (DOC-) | 4.5 | 2.7 | 1.9 | 1.1 | 1.5 | 0.90 | 0.62 | 0.39 |
| oxidation (r5) | 3.0 | 1.2 | 1.1 | 0.39 | ||||
| oxidation (r6) | 2.9 | 1.2 | 1.1 | 0.39 | ||||
| Production - nitrification (r7) | 0.28 | 0.13 | 0.067 | 0.032 | 0.10 | 0.043 | 0.025 | 0.010 |
| Anammox (r8) | 0.011 | 0.0094 | 0.0051 | 0.0050 | ||||
| Production (r10) | 6.5 | 2.9 | 1.5 | 0.68 | 1.7 | 0.59 | 0.40 | 0.14 |
| Total DOM uptake (r11) | 19.3 | 4.0 | 2.6 | 0.79 | 6.1 | 0.93 | 0.82 | 0.17 |
| Oxygen uptake (r12) | 15.8 | 2.5 | 6.1 | 1.0 | ||||
| exchange (r13) | 0.017 | 0.26 | 0.010 | 0.0019 | ||||
| release (r14) | −0.59 | 0.32 | −0.40 | 0.10 | ||||
| exchange (r15) | −0.022 | 0.027 | 0.019 | 0.0073 | ||||
| CO2 release (r16) | −12.9 | 2.1 | −4.7 | 0.83 | ||||
| N2 release (r17) | −0.49 | 0.37 | −0.12 | 0.10 | ||||
| Fractions and efficiencies (%) and ratios (-) | ||||||||
| Production efficiency on DOM | 31 | 9 | 55 | 14 | 24 | 8 | 42 | 12 |
| Production efficiency (total) | 31 | 14 | 57 | 12 | 24 | 8 | 45 | 11 |
| Fraction microbial production to total production | 28 | 16 | 28 | 16 | 32 | 16 | 32 | 16 |
| Fraction chemoautotrophy to total production | 5.1 | 3.0 | 5.1 | 3.0 | 6.7 | 2.9 | 6.7 | 2.9 |
| RQ | 1.23 | 0.065 | 1.30 | 0.055 | ||||
| Fraction denitrification to nitrification | 18 | 15 | 11 | 10 | ||||
| Fraction DNRA of nitrification | 58 | 21 | 50 | 20 | ||||
Metabolic network model results for smaller and larger Geodia barretti for C/O2 and N.
Release is indicated with a negative sign.
FIGURE 3

Model-calculated average C fluxes ± SD (μmol C cm–3 day–1) in smaller Geodia barretti specimens (top) and larger G. barretti specimens (bottom). G. barretti assimilates bacteria (r1_BacCupt) and mainly dissolved organic carbon (r11_tDOCupt), which is used for aerobic respiration (r2_DOCupt), denitrification (r3_denitDOCupt), and DNRA (r4_DNRA_DOCupt). Production processes are shown in green, where r10_totCprod is the total C (biomass) production by the holobiont. r16_CO2rel (blue) is the net CO2 release rate. The reaction numbers correspond to Figure 1 and Table 2.
FIGURE 4

Model-calculated metabolic aerobic (blue) and anaerobic (orange) nitrogen-transforming fluxes in smaller Geodia barretti individuals (left) and larger G. barretti individuals (right). The reaction numbers refer to Figure 2 and Table 2.
Sponge Host Metabolism
G. barretti metabolism was dominated by heterotrophy, with DOM as primary food source (Table 3 and Figure 3). DOM assimilation and aerobic respiration by the sponge (holobiont) (r2) were the main heterotrophic processes in G. barretti, independent of size (Table 3 and Figure 3). Because this process dominated sponge metabolism, it was also most sensitive to input parameters. Lower values of C:NDOM input range (Table 2) resulted in more feasible model solutions (Figure 5). Feasible C:NDOM values averaged 7.6 ± 1.4 in both smaller and larger sponges (Figure 5). Higher values of fp_N_DOM from the rather wide input range (20–80%, Table 2) resulted in more feasible model solutions in smaller sponges, while the opposite was found in larger sponges (Figure 5). The averages of feasible fp_N_DOM values were 58 ± 18% in smaller sponges compared to 41 ± 17% in larger sponges (Figures 5, 6). The corresponding average C production efficiency (fp_C_DOM) was 33 ± 12% in smaller sponges and 24 ± 11% in larger sponges (Figures 5, 6). The associated C (biomass) production rate was 4.8 ± 2.8 and 1.0 ± 0.55 μmol C cm–3 day–1 in smaller and larger sponges, respectively (Figures 3, 6). The majority of assimilated DOC, i.e., 67 ± 12% in smaller sponges and 76 ± 11% in larger sponges, was aerobically respired to CO2 (Figure 6).
FIGURE 5

Distribution of coefficients in reaction 2 [(DOM) assimilation and aerobic respiration] to produce feasible model solutions: stoichiometry (C:N) of DOM (left) and C (middle) and N (right) production efficiencies in smaller (top) and larger (bottom) Geodia barretti.
FIGURE 6

Schematic representation of internal C and N metabolism in Geodia barretti. Metabolic processes are indicated with solid arrows with reaction (r) numbers corresponding to those of Figure 2 and Table 2. Aerobic and anaerobic processes are separated in the blue and yellow part, respectively. Exchange fluxes are shown with dotted arrows. Model-calculated average metabolic rates in μmol C cm–3 day–1 or μmol N cm–3 day–1, shown adjacent to arrows, differ between smaller and larger G. barretti (right). The partition of dissolved organic matter to oxic and anoxic processes and to (C and N) sponge biomass production and respiration are shown with percentages. Dashed arrows indicate chemoautotrophic processes. Internal NH4+ excretion and re-assimilation, shown by the green arrow, is expected to take place but is not explicitly modeled. Bacteria uptake (r1) and NO2– (r15) and NH4+ (r13) exchange are not shown for simplicity.
Microbial N-Transforming Processes
Oxic N-transforming processes dominated over anoxic N-transforming processes necessary to create a net release (Table 3 and Figures 4, 6). The dominant microbial N-transforming processes were nitrification (r5–r6) and DNRA (r4) (Table 3, Figure 4). The nitrification rates in smaller sponges ranged from 1.1 to 5.1 μmol N cm–3 day–1 (5–95% confidence interval), with an average of 3.0 ± 1.2 μmol N cm–3 day–1 (Table 3 and Figures 4, 6). The nitrification rates in larger sponges ranged from 0.51 to 1.8 μmol N cm–3 day–1 (1.1 ± 0.39 μmol N cm–3 day–1; Table 3 and Figures 4, 6). Nitrification was responsible for 38 ± 14% of the O2 consumption, independent of sponge size. Nitrification (r5–r6) and DNRA (r4) are positively related: nitrification uses the produced substrate of DNRA ( and vice versa. The model results indicate that N cycling from coupled / conversion in DNRA and nitrification is 58 ± 21% of nitrification in smaller sponges and 50 ± 20% in larger sponges (Table 3 and Figure 6). The remaining part of comes from the mineralization of organic N (r1–r4) (Figure 6). The modeled DNRA and nitrification rates were sensitive to the imposed maximum ratio DNRA vs. aerobic respiration (r4 vs. r2) because more O2 is available to nitrification if OM is mineralized anaerobically (via DNRA) compared to aerobic mineralization (r2) (Supplementary Figure 2). Denitrification rates (r3) were consistently below DNRA rates (r4) in both sponges (Table 3 and Figure 4). The anammox rates, which were constrained to be below denitrification rates, were the lowest of all nitrogen-transforming rates (Table 3 and Figure 4). N2 loss via denitrification was 18 ± 15% of nitrification in smaller sponges and 11 ± 10% in larger sponges (Table 3 and Figures 4, 6). The N2 release rates were 0.49 ± 0.37 and 0.12 ± 0.10 μmol N cm–3 day–1 in smaller and larger sponges, respectively (Table 3 and Figure 6).
Microbial symbiont C (biomass) production was 1.6 ± 1.1 μmol C cm–3 day–1 in smaller sponges, from which 1.3 ± 0.98 μmol C cm–3 day–1 came from heterotrophy (denitrification, DNRA) and 0.28 ± 0.13 μmol C cm–3 day–1 came from chemoautotrophy (nitrification, anammox) (Figures 3, 6 and Table 3). In larger sponges, symbiont C (biomass) production was 0.53 ± 0.34 μmol C cm–3 day–1, from which 0.43 ± 0.30 μmol C cm–3 day–1 came from heterotrophy and 0.10 ± 0.043 μmol C cm–3 day–1 came from chemoautotrophy (Figures 3, 6 and Table 3).
Integrated Holobiont Metabolism and Net Exchange
Integrated G. baretti holobiont metabolism comprises biomass production rates and efficiencies of sponge and microbial symbionts. The holobiont production (r10) rates in smaller sponges were 6.5 ± 2.9 μmol C cm–3 day–1 and 1.5 ± 0.68 μmol N cm–3 day–1 (C:N = 4.2) (Table 3 and Figures 3, 6), with an estimated contribution of 28 ± 16% by nitrogen-transforming symbionts, comprising 5.1 ± 3.0% of total production from chemoautotrophy. The holobiont production (r10) in larger sponges was 1.7 ± 0.59 μmol C cm–3 day–1 and 0.40 ± 0.14 μmol N cm–3 day–1 (C:N = 4.2) (Table 3 and Figures 3, 6), with a contribution of 32 ± 16% by nitrogen-transforming symbionts, comprising 6.7 ± 2.9% of total production from chemoautotrophy. Overall production efficiencies for all assimilated OM, including bacterial uptake [production / assimilated OM, r10/(r11 + r1)], were 31 ± 14% for C and 57 ± 12% for N in smaller sponges compared to 24 ± 8% for C and 45 ± 11% for N in larger sponges (Table 3). The CO2 release rates were 13 ± 2.1 μmol C cm–3 day–1 in smaller G. barretti and 4.7 ± 0.83 μmol C cm–3 day–1 in larger G. barretti (Table 3 and Figures 3, 6). The overall RQ (O2: CO2) was 1.23 ± 0.065 in smaller G. barretti and 1.30 ± 0.056 in larger G. barretti (Table 3).
The model-calculated exchange rates of O2 and comprised a smaller range compared to the measured rates (compare Tables 1, 3) because not all combinations of flux measurements resulted in feasible model solutions. The average model-based release rates were lower compared to the averages of the measured rates because more feasible solutions were obtained at the low end of measured release rates (compare Tables 1, 3). Higher O2 uptake values from the measured range resulted in more feasible solutions in smaller sponges, while the opposite occurred in large sponges (compare Tables 1, 3).
Specific Rates
Specific rates (day–1) are derived from C-based reaction rates (μmol C cm–3 day–1) (Table 3) relative to C content (M, μmol cm–3; Table 1). The specific assimilation rates derived from total organic matter consumption (r1 + r11) were 4.7 10–3 and 2.0 × 10–3 day–1 for smaller and larger sponges, respectively (Table 4). Daily production rates (r10) were 1.6 × 10–3 (0.16%) and 0.67 × 10–3 (0.067%) day–1 for smaller and larger sponges, respectively (Table 4), indicative of allometric scaling.
TABLE 4
| Specific rates (day–1) | Smaller | Larger |
| Assimilation (r1 + r11) | 0.0047 | 0.0020 |
| Respiration (r16) | 0.0031 | 0.0015 |
| Production (r10) | 0.0016 | 0.00067 |
Model-based specific rates (day–1) for small and larger Geodia barretti.
These rates are derived from model results (μmol C cm–3 day–1) per carbon biomass (mmol cm–3 day–1).
Discussion
The aim of this study was to infer internal C and N metabolic conversions in a deep-sea sponge holobiont system. To this end, a metabolic network model integrating C and N metabolism of the sponge G. barretti and its microbial symbionts was developed. The presented model can serve as a valuable data analysis tool to quantify internal and intermediate routes in sponge metabolism given any metabolic dataset. In this study, we used two independent metabolic datasets to constrain internal G. barretti metabolism that encompassed a range of sponge volumes. The model results indicate that G. barretti has complex but flexible metabolism consisting of aerobic and anaerobic processes. The measured fluxes and model metabolic results suggest that specific metabolic rates decline with increasing G. barretti size, while the ratios between oxic and anoxic processes and between sponge host and microbial metabolism seem rather independent of size.
Organic Matter Assimilation by G. barretti
The measured DOC assimilation rates (
As the C and N production efficiencies for G. barretti and other deep-sea sponges were largely unknown, they were inferred by sensitivity analysis (Figure 5). Our estimated C production efficiency values of 24 ± 8% in larger individuals and 31 ± 14% in smaller individuals (Table 3 and Figures 3, 5, 6) are within the reported range of 20–30% for metazoans (
Most of the assimilated DOC (76 ± 8% in larger sponges and 69 ± 9% in smaller sponges) was respired to CO2 (Figures 3, 6). Model quantification of net CO2 release rate (respiration minus fixation) relative to O2 consumption allowed us to estimate an integrated RQ. The estimated RQ values (O2:CO2) were very similar between the two datasets, 1.25–1.30 ± 0.06 (Table 3; 0.77–0.80 for CO2:O2), a value in between complete mineralization of Redfield DOM to (1.16) and (1.43) (
Microbial Nitrogen-Transforming Processes
In contrast to most marine animals, several sponge species (in particular, HMA demosponges) release rather than (
All model-based internal N-transforming process rates were higher compared to previous estimates from isotope tracer incubations with G. barretti tissue fragments (volume 0.30–0.45 cm–3) (
Genes (napA, nrfA) involved in all steps of DNRA have been found in metagenomes of G. barretti (Gavriilidou, personal communication) and other deep-sea sponges (
Dark carbon fixation rates in G. barretti (or other Geodiidae spp.) associated with nitrification and anammox have not yet been experimentally quantified. The first model-based estimates of dark carbon fixation rates for G. barretti are presented here (Table 3 and Figure 3), acknowledging the different energy yields from each nitrogen-transforming process (e.g., oxidation, oxidation, anammox). CO2 fixation rates contributed only a small fraction of 5.1–6.5% of G. barretti production and ∼1.5% of total C assimilation. These contributions are very similar to the range of 0.2–2.1% fixation relative to assimilation for the deep-sea encrusting sponge Hymedesmia coriacea (
The model covers N-based metabolism but not sulfur-based metabolism because sulfur data were not available. Both genes for sulfate reduction (heterotrophy) and sulfur oxidation (chemoautotrophy) are found in G. barretti (
Size Dependency of Metabolism
Based on the metabolic datasets of
O2 consumption in G. barretti is directly linked to pumping since pumping supplies sponge tissue with O2 and G. barretti that reduce their pumping activity rapidly become anoxic (
The lower production efficiencies (24 ± 8% for C, 45 ± 11% for N; Table 3 and Figure 5) and production rates (0.067% day–1; Table 4) in larger G. barretti compared to smaller G. barretti (31 ± 14% for C, 57 ± 12% for N; Table 3 and Figure 5; 0.19% day–1, Table 4) fit with theoretical predictions that production efficiencies decrease with size (
Sponge (Biomass) Production
Production by the sponge holobiont is allocated to various processes, which are mainly growth, reproduction, and renewal. The magnitudes and portions of each flow are largely unquantified for Geodia (and other deep-sea sponges). Therefore, we did not go any further with our model beyond estimating production by the sponge holobiont. Our production rates for G. barretti of 0.16% day–1 in smaller sponges and 0.067% day–1 in larger sponges (Table 4) seem low compared to modeled estimates for deep-sea sponges (0.23% day–1;
Ecosystem Context Using Model Estimations
The metabolic activity of G. barretti influences local C and N cycling at the benthic boundary layer, given the enormous abundance of this species over the extensive deep-sea area of the boreal region, forming the so-called Geodia grounds (
Care must be taken, however, since, on a larger ecosystem scale, the average G. barretti biomass in the south-west Barents Sea region (i.e., Trømso Plateau, North Cap bank, and areas in between; approximately 125,000 km2) is ∼50 g WW m–2 (
Another important aspect of our model that can improve the ecological context of deep-sea sponges and sponge grounds is the size dependence on metabolic rates. Currently, benthic biomass estimations in deep-sea ecosystems, such as the Barents Sea, are largely based on trawl catch data (e.g.,
Statements
Data availability statement
The dataset of
Author contributions
AK developed the model, performed the data analyses and model analyses, prepared the figures, and wrote the manuscript. MB and JG designed and conducted the incubation experiments, performed nutrient analyses, and contributed to the writing of the manuscript. SV contributed to model conceptualization and development. JM acquired funding and contributed to the conceptualization of the model, interpretation, and writing of the manuscript. MM contributed to the conceptualization of the model, interpretation, and writing. SL and SM contributed data for model development. KS contributed technically with model implementation and analyses. DO designed the model, contributed to model development and interpretation, and writing of the manuscript. All authors contributed to the article and approved the submitted version.
Funding
This research has been performed in the scope of the EU SponGES project, which received funding from the European Union’s Horizon 2020 Research and Innovation Program under grant agreement no. 679849. Further support included ERC starting grant agreement no. 715513 to JG and the Netherlands Earth System Science Center to JM. This document reflects only the authors’ views, and the Executive Agency for Small and Medium-sized Enterprises (EASME) is not responsible for any use that may be made of the information it contains.
Acknowledgments
Titus Rombouts and Pieter Slot (UvA) and Sharyn Ossebaar (NIOZ) are acknowledged for their analytical assistance with the nutrient measurements of the incubation experiments. We thank Asimenia Gavriilidou and Detmer Sipkema (WUR, SponGES) for their input on the microbial genome in G. barretti. We thank last Hans Tore Rapp (UiB) for the excellent project coordination. We would like to thank CF and CR for their valuable and constructive reviews.
Conflict of interest
The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.
Supplementary material
The Supplementary Material for this article can be found online at: https://www.frontiersin.org/articles/10.3389/fmars.2020.596251/full#supplementary-material
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Summary
Keywords
allometry, metabolic network model, sponge holobiont metabolism, production, biogeochemistry, chemoautotrophy, sponge ground, LIM
Citation
de Kluijver A, Bart MC, van Oevelen D, de Goeij JM, Leys SP, Maier SR, Maldonado M, Soetaert K, Verbiest S and Middelburg JJ (2021) An Integrative Model of Carbon and Nitrogen Metabolism in a Common Deep-Sea Sponge (Geodia barretti). Front. Mar. Sci. 7:596251. doi: 10.3389/fmars.2020.596251
Received
18 August 2020
Accepted
30 November 2020
Published
18 January 2021
Volume
7 - 2020
Edited by
Daniela Zeppilli, Institut Français de Recherche pour l’Exploitation de la Mer (IFREMER), France
Reviewed by
Christopher Freeman, College of Charleston, United States; Clara F. Rodrigues, University of Aveiro, Portugal
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Copyright
© 2021 de Kluijver, Bart, van Oevelen, de Goeij, Leys, Maier, Maldonado, Soetaert, Verbiest and Middelburg.
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*Correspondence: Anna de Kluijver, a.dekluijver@uu.nl; anna.dekluijver@rvo.nl
This article was submitted to Deep-Sea Environments and Ecology, a section of the journal Frontiers in Marine Science
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