Model Description
Background Information
In order to determine the efficacy of our final product, we built a mathematical model based on differential equations to simulate the change of surrounding CO2 concentration over time caused by the altered levels of carbon fixation in our genetically engineered cyanobacteria. Employing this model, we are able to compare the efficiency of our final product and other commercially available technologies, such as CO2 scrubbers for industrial plant exhausts.
The Fundamentals
The most fundamental differential equations used in our model are multivariate. Specifically, they are bivariate functions of two variables r and t, where r stands for the distance from the center of a hypothetical, spherical cyanobacteria cell, and t stands for time. The two variables allow our model to describe information through CO2- and HCO3--relevant functions, such as concentration and flux, at all spaces and times within the hypothetical cell.
We are greatly informed and inspired through reading Dr. Niall Mangan’s paper “Systems analysis of the CO2 concentrating mechanism in cyanobacteria”. We appreciate the research conducted by her and her colleagues, which has tremendously enriched our understanding of this field.
We also had an online meeting with Dr. Mangan, seeking her advice on how biological efficiency is defined within computational models and how various environmental and enzymatic factors influence CO2 fixation. During this discussion, she emphasized the crucial roles of carbonic anhydrase and carboxysomes in mediating CO2 uptake and delivery to RuBisCO, noting that their capacity can become limiting factors in photosynthetic efficiency, which we accounted for in our modeling equations.
A Guide to Michaelis-Menten Kinetics
To understand enzymatic activity, visualize substrate affinity, and model the rate of reaction in BCT1’s HCO3- transport pathway across wild-type and engineered (particularly, the CmpAB and CmpCD fusion proteins’ functionalities are examined both in a separate and holistic manner) strains of S. elongatus PCC 7942, the team employs the concept of Michaelis-Menten Kinetics. Conceptually, the Michaelis-Menten Kinetics model explains how reaction rates are dependent on enzyme and substrate concentrations.
Below is a step-by-step guide for deriving the Michaelis-Menten equation (Libretexts, 2024).
General reaction scheme of a single-substrate enzyme-catalyzed reaction, where E=enzyme, S=substrate, ES=enzyme-substrate complex, P=product, and k1, -1, 2=rate constants.
Using the Steady-State approximation, a method of deriving rate laws with the assumption of a constant intermediate concentration (in this case, [ES]), where its rate of formation (RF=k1[E][S], assuming [P]=0) equals the rate of breakdown, or the reverse reaction (RR=k2[ES]+k-1[ES]=(k2+k-1)[ES]),
where KM is a constant describing half-filled enzyme active sites, calculated with the equation KM = k2 + k-1 k1 .
Given that the total amount of enzymes, ET, could be represented by ET=[ES]+[EF], where EF=free-bound enzymes, equation (4) could be rewritten as:
Lastly, plug in the rate law of the rate-limiting step, v0=k2[ES], where v0=instantaneous rate of reaction.
Assuming that S>>KM, v0~k2[ET], and v0=vmax, where vmax corresponds to the maximum reaction velocity with most enzymes fully saturated with substrate, the Michaelis-Menten Equation is obtained:
where v=reaction rate.
In conclusion, with known values of Vmax and KM and substrate concentrations obtained through functional assays, the Michaelis-Menten equation could be used to specifically compute the flux of HCO3- across the cyanobacterial inner membrane.
Overall Flow Diagram:
Figure 1. Schematic representation of the inorganic carbon transport pathway in the cyanobacterial carbon-concentrating mechanism (CCM) that is being modelled. Each distinct stage is referenced in subsequent modeling sections. Firstly, extracellular CO2 diffuses into the periplasm in the outer membrane. Then, inside the periplasm, both CO2 and HCO3- equilibrate, and CO2 is directly transported into the cytoplasm. Periplasmic HCO3- then binds to inner membrane transporters, including the CmpA component of the BCT1 transporter, initiating the HCO3- uptake mechanism. Subsequent to that, HCO3- is actively transported across the inner membrane into the cytosol via the BCT1 complex comprising A, B (a homodimer), C, and D subunits, driven by ATP hydrolysis from component C and D and multiple other transporters. Once in the cytosol, HCO3- enters the carboxysome by diffusion. Inside the carboxysome, HCO3- is converted to CO2 by carbonic anhydrase (CA), elevating the local CO2 concentration. Finally, CO2 is fixed by RuBisCO, producing 3-phosphoglycerate (3-PG). The figure is not drawn to scale.
A Guide to Fick’s Laws
In intracellular locations without membranes or shells, Fick’s Laws are commonly used to describe the diffusion of CO2 and HCO3-. Here, we briefly introduce Fick’s two key laws related to diffusion flux and rate of change of concentration (Dickson, n.d.).
Fick’s First Law of Diffusion states that the flux due to diffusion is proportional to the negative concentration gradient of that substance. Specifically, the flux is equal to the negative diffusion coefficient of the solvent through which that substance diffuses multiplied by the change in that substance’s concentration gradient — also interpreted as difference in concentration across space. This law is used as an anchor point within the cytosol for each change in concentration within distances as small as the thickness of a phosphobilipid layer.
On the other hand, Fick’s Second Law of Diffusion relates the rate of change of a solute’s concentration to the concentration’s second partial derivative; in other words, it connects “how fast” the concentration diffuses with “how curved” the concentration gradient is. Through allowing us to interchange between partial derivatives with respect to time and position, this law is very useful for our two molecules diffusion through the cytoplasm and any other non-membrane or non-shell spaces.
General Assumptions
To simplify the model, the following assumptions were made:
- The outer membrane, inner membrane, and carboxysome are assumed to be perfect concentric spheres, with the cell radius set to 1.446 µm. All membranes are treated as infinitesimally thin, and thus membrane thickness is neglected.
- The extracellular CO2 concentration is assumed to remain constant and saturated. Under air-equilibrated conditions (0.04% CO2), the external CO2 concentration is 13 µM, whereas under flue gas conditions (15%CO2) it is 5mM.
- The periplasmic sodium concentration is fixed at [Na+]=18mM, and the cytoplasmic ATP concentration is assumed to be saturated
- The model assumes that inorganic carbon is limited in the extracellular environment.
- The model requires efficient carbon fixation at the following two conditions:
- The CO₂ concentration within the carboxysome must be sufficiently high to saturate RuBisCO while suppressing its competitive oxygenation reaction.
- The carbonic anhydrase within the carboxysome remains unsaturated, enduring that excess HCO₃⁻ transport does not result in unnecessary energy expenditure.
- The enzymatic parameters of MalK were used to calculate the kinetic properties of CmpC and CmpD.
- In modeling the RuBisCO reaction rate, the concentration of RuBP is assumed to be saturating, and no oxygenation reaction occurs under the modeled conditions.
Pathway & Checkpoints
To understand the entire pathway involving CO2 and HCO3- changes in concentration, we have broken it down into seven key checkpoints. For our convenience and mathematical purposes, the checkpoints are assigned to account for concentration changes at different positions (or r, the distance from the theoretical “central carboxysome”). The only exceptions are checkpoints #6 and #7, where, although carbonic anhydrase and RuBisCO are both in the carboxysome, they function differently and therefore must be separately calculated.
Checkpoint #1: CO2 and HCO3- intake through the cyanobacterial outer membrane
The first checkpoint marks the entry of CO2 into the cyanobacteria through simple diffusion since small gas molecules easily pass through the membrane. Focusing on the entry of CO2, we employ the Fick's first law that relates the flux to the concentration gradient, which gives us the following equation.
Legend
JC: the flux of CO2 through the outer membrane into the periplasm (in units)
PC: the outer membrane’s permeability for CO2 (in units)
ΔC: the difference in CO2 concentration between the extracellular environment and the periplasm
We also have a formula further describing the outer membrane’s permeability for CO2.
Legend
K: the partition coefficient, a ratio that describes a compound’s (CO2) distribution between two immiscible solvents (the lipid bilayer outer membrane and aqueous periplasm) at equilibrium, = 0.95
D: the diffusion coefficient of CO2, = 5×10-8 cm2/s
Δx: the thickness of the outer membrane, = 8×10-9 m
Combining the previous two equations and elaborating on the ΔC, we get this equation for checkpoint #1.
Legend
Cec: extracellular CO2 concentration
Cperi: periplasmic CO2 concentration
On the other hand, since HCO3- is a charged molecule, its simple diffusion through the phospholipid bilayer is negligible and will not be accounted for. Therefore, periplasmic HCO3- concentrations are assumed to be completely due to the reversible CO2 hydration and subsequent carbonic acid dissociation reactions, as shown below.
We assume that the intermediate reaction is at quasi-steady state, which means that the rate of change of the intermediate (H₂CO₃) periplasmic concentration is equal to zero. The rate of change of H₂CO₃ concentration is equal to the sum of two rates that cause its formation minus the other two rates that cause its depletion. Equating the two statements above, we can list the equation shown below.
Rearranging the terms and solving for the concentration of H₂CO₃, we get the following equation.
Then, the rate of change of the concentration of HCO3- is equal to the rate of the reaction that produces HCO3- minus the rate of the reaction that depletes HCO3-. Furthermore, substituting the expression for the concentration of H₂CO₃, we get an expanded expression shown below.
Since k₂ has a much larger numerical value than k₋₁, k₂ + k₋₁ is approximately equal to k₂. The mathematical expression of this approximation is presented below as well.
As a result, we are able to simplify the denominator of the previous expression for the rate of change of the concentration of HCO3-, and cancel out common coefficients in the numerator and denominator. After crossing out some more canceled terms, we get the resulting expression presented below.
From this proof, we know that the rate of change of HCO3- concentration is equal to k₁ multiplied by the concentration of CO2. The final equation for HCO3- production, which can be viewed similarly as flux here in the periplasm, is written as the following equation concluding this checkpoint.
Checkpoint #2: CO2 and HCO3- Transport Across the Inner Membrane
The second checkpoint is a key point where our model differentiates our overexpression strain from wild-type S. elongatus PCC 7942. On the inner membrane, there are multiple transporters and reactions that influence the influx of HCO3-. The main ones included in our modeling are HCO3- active transporter, BCT1; Na⁺-dependent HCO3- transporters, BicA and StbA; and local alkaline pockets (LAP) resulting from proton outflux in the electron transport chain on the thylakoid membrane, which causes an increase in HCO3- ion concentration due to Le Chatelier’s Principle that is dependent on internal (cytoplasmic) CO2 concentration. For BCT1, since they are encoded by our overexpressed CmpABCD operon, there is an expected increase in the amount of BCT1. As a result, we decided to use XBCT1, a coefficient representing the concept of “fold change”, to describe the accumulated effects of overexpressing CmpABCD on HCO3- influx. This coefficient is mainly influenced by light intensity due to the light-induced nature of our promoter ppsbA1. Summing up all the effects, we get a general equation of the HCO3- flux through the inner membrane as shown below.
Legend
JH: the net inward flux of HCO3- through the cyanobacterial inner membrane
JBCT1: the flux of HCO3- due to BCT1
XBCT1: the fold change of BCT1 concentration due to CmpABCD overexpression compared to wild-type
JBicA: the flux of HCO3- due to HCO3- transporter BicA
JSbtA: the flux of HCO3- due to HCO3- transporter SbtA
JLAP: the flux of HCO3- due to local alkaline pockets (LAP)
Then, we expand the equations by substituting the Michaelis-Menten equations that describe each of them, as shown below.
To determine the concentration of CmpA bound to HCO3- ([A-H]), which can be understood as the effective CmpA components that actually contribute to HCO3- transport, we have to take the total CmpA concentration and multiply it by a ratio that accurately counts the HCO3--bound CmpA components. As the periplasmic HCO3- concentration approaches the dissociation constant, more spare CmpA components “grab” onto HCO3-, taking the concentration of bound CmpA near the total concentration of CmpA components. As a result, we can use this equation, shown below, to substitute for all bound CmpA components in the previous long equation.
Legend
[A-H]: the concentration of CmpA components bound to HCO3-
[A]: the concentration of total CmpA components
Hperi: the periplasmic HCO3- concentration
Kd: the dissociation constant of CmpA for HCO3-
Substituting this expression, we get the final equation for HCO3- net influx through the inner membrane, as shown below.
Legend
JC: the net inward flux of CO2 through the inner membrane
VBCT1: the maximum reaction rate of BCT1
[A]: the concentration of total CmpA components
Hperi: the periplasmic HCO3- concentration
Kd: the dissociation constant of CmpA for HCO3-
KBCT1: the dissociation constant of BCT1 for HCO3--binded CmpA
XBCT1: the fold change of BCT1 concentration due to CmpABCD overexpression compared to wild-type
VBicA: the maximum reaction rate of the HCO3- transporter BicA
VSbtA: the maximum reaction rate of the HCO3- transporter SbtA
[Na+]: the periplasmic Na+ concentration
α: maximal reaction rate of conversion from HCO3- to CO2
Kα: CO2 concentration at half maximal activity of the conversion reaction
On the other hand, we also have an equation for CO2 influx through the inner membrane. Since the small nonpolar molecule diffuses through the inner membrane, we have term one that describes its diffusion. The second term, however, has a negative sign because it describes the depletion of CO2 due to conversion reactions caused by local alkaline pockets, as described previously. Combining these two effects, we get the equation shown below.
Legend
JC: the net inward flux of CO2 through the inner membrane
PC: the permeability of the inner membrane to CO2
ΔC: the difference in CO2 concentration between the periplasm and the cytoplasm
α: the maximal reaction rate of conversion from CO2 to HCO3-
Cin: the internal, or cytoplasmic, CO2 concentration
Kα: the CO2 concentration at half maximal activity of the conversion reaction
Checkpoint #3: CO2 and HCO3- Concentration Rate of Change in the Cytoplasm
The third checkpoint describes the diffusion of CO2 and HCO3- through the cytoplasm until outside of the carboxysome. Due to the tridimensionality of our model, we need an extra step to confine the gradient of both molecules into one single direction — that is, along the position axis x pointing from the center of the carboxysome to outside of the cell. The other two components perpendicular to the x-axis, namely the y and z components, do not contribute to fluxes along that axis, and therefore should be ignored.
This brings us Fick’s Second Law, which states that the time partial derivative of a molecule undergoing diffusion is proportional to the laplacian (denoted by nabla squared, where nabla is the upside down triangle), a second derivative for multivariate functions, of that molecule’s concentration as a function of position and time. This applies for both CO2 and HCO3- and is described through the two equations below.
Legend
∂C
∂t
: rate of change of CO2 concentration
C: CO2 concentration as a function of position and time
∂H
∂t
: rate of change of HCO3- concentration
H: HCO3- concentration as a function of position and time
Essentially, in this checkpoint, we are turning time partial derivatives into position partial derivatives through removing unwanted portions and focusing on one direction only: the direction that contributes to recording flux from the carboxysome straight to outside of the cell.
Checkpoint #4: CO2 and HCO3- Diffusion into the Carboxysome
Transport of CO2 and HCO3- across the proteinaceous carboxysome shell is modeled as permeability-limited diffusion. The flux is proportional to the concentration difference between the cytosol and the carboxysome interior, which is scaled by the permeability coefficient Kcbxs. This process follows Fick’s law and defines the inward fluxes of inorganic carbon species into the carboxysomal microenvironment.
Legend
D
∂C
∂r
: the diffusive flux of CO2
D
∂H
∂r
: the diffusive flux of HCO3-
Kcbxs: the optimal carboxysome permeability
Ccyt: the concentration of CO2 in the cytosol
Ccbxs: the concentration of CO2 in the carboxysome
Hcyt: the concentration of HCO3- in the cytosol
Hcbxs: the concentration of HCO3- in the carboxysome
Although previous structural studies have suggested that the positively charged pores on the carboxysome surface could preferentially facilitate diffusion of negatively charged HCO3-, direct experimental measurements of permeability remain unavailable. Therefore, in this model, we adopt the simplest assumption that HCO3- and CO2 share the same permeability across the carboxysome shell (Yeates et al., 2008; Dou et al., 2008; Cheng et al., 2008).
Checkpoint #5: Inside the Carboxysome
The fifth checkpoint, governed by these two partial differential equations, describes how the concentrations of the two molecules change in the carboxysome over time.
Legend
∂C
∂t
: the rate of change of carboxysomal CO2 concentration
D∇2C: the effects of diffusion that drive CO2 movement
∂H
∂t
: the rate of change of carboxysomal HCO3- concentration
D∇2H: the effects of diffusion that drive HCO3- movement
RCA: the reaction rate of carbonic anhydrase
RRub: the reaction rate of RuBisCO
Breaking them down into individual terms has helped us understand these two equations. First of all, the first terms are identical to those in checkpoint #3, which uses Fick’s Second Law to confine concentration changes to one single direction. Secondly, carbonic anhydrase turns HCO3- into CO2, which means that its reaction rate is reflected as a positive contribution to the concentration of CO2, and on the other hand, a negative depletion to the concentration of HCO3-. Thus, it takes on a positive coefficient, denoted by the plus sign, on the equation for CO2, but a negative coefficient, denoted by the minus sign, on the equation for HCO3-. Last but not least, since RuBisCO binds with CO2 and causes a decrease in CO2 concentration, its rate of change is negative for CO2. However, RuBisCO does not affect the concentration of HCO3-, so its rate is not accounted for in the second equation describing the rate of change of HCO3- concentration.
In the two following checkpoints, the reaction rates of both enzymes will be elaborated and explained with detail.
Checkpoint #6: Carbonic anhydrase reaction rate
Inside the carboxysome, HCO3- reacts with protons to form carbonic acid, which rapidly decomposes into CO2 and water:
This reaction is catalyzed by carbonic anhydrase (CA), an enzyme that accelerates the interconversion of HCO3-and CO2. In addition, as a part of being in the local alkaline pocket, CO2 also directly reacts to become HCO3- without having the intermediate carbonic acid. Chemically, this step is crucial because it elevates the local CO2 concentration within the carboxysome, driving efficient carbon fixation by RuBisCO (in the next checkpoint).
The rate of the carbonic anhydrases catalyzed reaction is described by a bidirectional Michaelis-Menten formulation that accounts for both the hydration and dehydration reactions.
Legend
RCA: the reaction rate of carbonic anhydrase
[CA]: concentration of carbonic anhydrase
CCbxs: concentration of CO2 in carboxysome
HCbxs: concentration of HCO3- in carboxysome
[H+]: concentration of H+
Keq: equilibrium constant
Kh,c: equilibrium constant of concentration of CO2 at which hydration is half-maximum
Kh,b: equilibrium constant of concentration of HCO3- at which hydration is half-maximum
kh,cat: hydration catalytic constant for dehydration reaction
nCbxs: the total amount of carboxysomes
Because the reaction is reversible, we modeled CA activity with a bi-directional Michaelis-Menten expression in a bivariate equation. Inside the carboxysome, the predominant direction of reaction is toward CO2 formation. Consequently, RCA functions as a sink for HCO3- and a local source of CO2, effectively elevating the carboxysomal CO2 concentration above equilibrium and driving efficient RuBisCO carboxylation.
Checkpoint #7: RuBisCO Reaction Rate
The terminal step in our model describes the fixation of CO2 by RuBisCO, which catalyzes the carboxylation of RuBP to yield two molecules of 3PG.
RuBisCO kinetics are described using a Michaelis-Menten form that accounts for the competing interaction of CO2 at the enzyme’s active site. The overall reaction rate is given by:
Legend
RRuBisCO: reaction of carbon fixation
CCbxs: local CO2 concentration inside the carboxysome
[RuBisCO]: concentration of RuBisCO enzyme
kcat: rate constant of RuBisCO carboxylation
Km: Michaelis constant for RuBisCO
nCbxs: the total amount of carboxysomes
Effect of light intensity:
Light intensity exerts a significant influence on the regulation of carbon uptake and fixation in the carbon concentrating mechanism for our model through the psbA1 promoter we cloned in, exhibiting strong light-responsive behavior. Previous studies using psbA1-lacZ fusion constructs have demonstrated that transcriptional activity from this promoter is significantly enhanced under high irradiance, reflecting its natural role in coordinating photosynthetic protein expression with photon flux (Nair et al., 2001).
Likewise, in our engineered strain, the CmpAB and CmpCD operon, which encodes the BCT1 bicarbonate transporter, is placed under the control of the psbA1 promoter. Consequently, increased light intensity directly elevates CmpABCD expression, thereby enhancing HCO3- transport efficiency across the inner membrane. This regulatory effect strengthens the cell’s capacity to accumulate inorganic carbon within the cytosol, ultimately supplying higher substrate concentrations to the carboxysome.
Enhanced carbon uptake under high light is further coupled with upregulation of carbonic anhydrase and RuBisCO expression within the carboxysome (checkpoints 6-7). Elevated CA activity facilitates rapid interconversion between HCO3- and CO2, sustaining high localized CO2 concentrations, while increased RuBisCO abundance allows more active sites for carboxylation reactions. In parallel, high irradiance has been associated with an increase in carboxysome biogenesis, providing additional microcompartments to accommodate the augmented enzymatic machinery.
Appendix
Table 1. Parameters, values, and sources
| Checkpoint | Notation | Meaning | Value | Reference |
|---|---|---|---|---|
| 1 | Pc | the outer membrane’s permeability for CO2 | 0.0035 m/s-1 | McGrath & Long, 2014 |
| 1 | K | the partition coefficient, a ratio that describes a compound’s (CO2) distribution between two immiscible solvents (the lipid bilayer outer membrane and aqueous periplasm) at equilibrium | 0.95 (mL CO2/mL lipid) | Gutknecht et al., 1977 |
| 1 | D | the diffusion coefficient of CO2 | 10-5 cm2/s | Mangan & Brenner, 2014 |
| 1 | ΔX | the thickness of the outer membrane | 8 nm | Assumed |
| 2 | XBCT1 | the fold change of BCT1 concentration due to CmpABCD overexpression compared to wild-type | 1 | Assumed |
| 2 | Kd | the dissociation constant of CmpA for HCO3- | 5μM | Koropatkin et al., 2007 |
| 2 | VBCT1 | the maximum reaction rate of BCT1 | 5.5 × 10-5 mol m-2s-1 | McGrath & Long, 2014 |
| 2 | KBCT1 | the dissociation constant of BCT1 for HCO3--binded CmpA | 0.015 mol m-3 | McGrath & Long, 2014 |
| 2 | VBicA | the maximum reaction rate of the HCO3- transporter BicA | 1.85 × 10-4 mol m-3 | McGrath & Long, 2014 |
| 2 | VSbtA | the maximum reaction rate of the HCO3- transporter SbtA | 2.246 × 10-5 | McGrath & Long, 2014 |
| 2 | α | maximal reaction rate of conversion from HCO3- to CO2 | 0.012 mol m-3 | McGrath & Long, 2014 |
| 2 | Kα | CO2 concentration at half maximal activity of the conversion reaction | 0.075 mol m-2s-1 | McGrath & Long, 2014 |
| 2 | PC | the permeability of the inner membrane to CO2 | 0.3 cm s | Mangan & Brenner, 2014 |
| 2 | [A] | The concentration of CmpA in the periplasm |
WT: 2.7 × 10-3mM
Engineered: LL: 2.806 × 10-3mM ML: 2.792 × 10-3mM HL: 2.777 × 10-3mM |
Calculated using Michaelis Menten equation.
Miller and Jeffrey, 1972; Schaefer and Golden, 1989 |
| 4 | Kcbxs | the optimal carboxysome permeability | 0.3 cm s | Managan & Brenner, 2014 |
| 6 | Kh,cat | hydration catalytic constant | 0.3 × 10-6s-1 | McGrath & Long, 2014 |
| 6 | [CA] | concentration of carbonic anhydrase |
LL: 8 × 10-4 mM
ML: 1.01 × 10-3 mM HL: 1.45 × 10-3 mM |
Calculated from Sun et al., 2019 |
| 6 | Keq | equilibrium constant | 5.6 × 10-5 mol m-3 | McGrath & Long, 2014 |
| 6 | Kh,c | equilibrium constant of concentration of CO2 at which hydration is half-maximum | 1.5 mol m-3 | McGrath & Long, 2014 |
| 6 | Kh,b | equilibrium constant of concentration of HCO3- at which hydration is half-maximum | 34 mol m-3 | McGrath & Long, 2014 |
| 6, 7 | nCbxs | the total amount of carboxysomes |
LL: 2.6 per cell
ML: 5 per cell HL: 9.5 per cell |
Calculated from Sun et al., 2019 |
| 7 | [RuBisCO] | concentration of RuBisCO enzyme |
LL: 0.027 mM
ML: 0.062 mM HL: 0.109 mM |
Calculated from Sun et al., 2019 |
| 7 | kcat | rate constant of RuBisCO carboxylation | 1.5 mol m-3 | McGrath & Long, 2014 |
| 7 | Km | Michaelis constant for RuBisCO | 1.5 mol m-3 | McGrath & Long, 2014 |
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