Modeling lifetime GHG emissions or global warming impact of materials
In this work, the atmospheric concentrations of GHGs associated with building materials, during manufacturing, and end-of-life treatments were simulated with a continuously stirred tank reactor (CSTR), as is done in chemical engineering. Figure 1 shows the schematic of the CSTR model, where the Earth’s atmosphere is represented by the volume of the CSTR. In this model, G is used as a generic variable representing the atmospheric concentration of any GHG. The inlet on the left side of the CSTR represents lifetime GHG emissions into the Earth’s atmosphere. These may come from the manufacture of building materials and from their disposal after the structure is demolished. The GHG emissions associated with manufacturing and from incineration of construction and demolition (C&D) debris are considered instantaneous pulse inputs into the CSTR, as their production times are extremely short. Biogenic carbon is the measure of the amount of GHG emitted when a material is incinerated or used for fuel. In this work, it represents the stored carbon in biological materials such as wood and in organic materials such as plastic. The emission of landfill gas (LFG) from decomposing building materials is a time-dependent source function that gradually releases GHGs into the atmosphere, which depends on the decay rate (k) and methane production potential (Lo) of landfilled materials.
The outlet represents the Earth’s physical, chemical, and biological mechanisms that remove CO2 and other GHGs from the atmosphere (Trussell and Hand 2005). The removal mechanisms include partitioning of CO2 into the oceans, CO2 uptake by trees and plants, and oxidation of CH4 by OH-radicals in the atmosphere. The removal mechanisms are a function of the atmospheric residence lifetime of the individual GHGs. Residence lifetime is a concept used in chemical engineering that describes the average amount of time a molecule spends in a reactor before exiting (Trussell and Hand 2005). The atmospheric residence lifetimes of CO2 and CH4 are estimated to be 50–200 years and 12 years respectively (EPA 2017).
The CSTR model is also adaptable to determine the GWP of other GHGs. Refrigerants (e.g., HFCs, CFCs) and dielectric gases (SF6) used in electrical distribution equipment also migrate to the stratosphere and are broken down photochemically by sunlight to produce halogen radicals that catalyze the reduction of O3 to O2.
GHG concentrations in the atmosphere
The derivation of the equation for the atmospheric concentration of a GHG due to an emission input (manufacturing, landfill disposal, incinerations, fugitive emissions, etc.) is shown below. Symbols for the variables and constants used in the GHG emissions model are defined in Table 1. Equation 1 represents the mass flow of a GHG (G) into the atmosphere and a first-order GHG removal mechanism (−QG) that is dependent on the atmospheric concentration (G) and the rate of removal (Q) due to ocean partitioning, plant uptake, etc.
$$ {V}_{\mathrm{atm}}\frac{dG}{dt}=- QG $$
(1)
Table 1 Variables and constants used in modeling GHG emissions Dividing Eq. 1 by the volume of Earth’s atmosphere (Vatm) gives a differential equation for the concentration of G in terms of the GHG residence time (θ) in the atmosphere:
$$ \frac{dG}{dt}=-\frac{1}{\theta }G $$
(2)
The solution for G(t) from Eq. 2 can be given by:
$$ G(t)={G}_0{e}^{-t/\theta } $$
(3)
with the initial condition G(0) = G0 at t = 0,
where, G0 is the initial concentration of GHG pulse emitted.
Modeling pulse GHG emissions
Equation 3 represents the concentration of the GHG in the atmosphere, emitted as pulse during manufacturing or incineration or as a fugitive emission, and subsequently removed from the atmosphere over time. If the source of the GHG pulse is combustion of the material during incineration, then G0 is given by the mass of the material combusted (m) multiplied by the carbon intensity coefficient, which is termed ECbio in the Inventory of Carbon and Energy (ICE) tables compiled by Hammond et al. (Hammond 2011). Hammond et al. use the subscript “bio” in the ECbio coefficient to refer to the biogenic carbon stored in wood that is released as CO2 upon combustion. In this work, the same coefficient is used to represent the CO2 released from any incinerated, flammable organic material, (e.g., plastic and rubber) and not just wood. Equation 4 gives the concentration of GHG emissions associated with the incineration of a mass (m) of flammable organic material.
$$ {G}_{\mathrm{bio}}(t)=\mathrm{m}\bullet {\mathrm{EC}}_{\mathrm{bio}}{e}^{-t/\theta } $$
(4)
Landfill gas production function
Landfill gas (LFG) production has been previously described by Mohan et al. and EPA (Mohan and MacDonald 2016a b; De La Cruz and Barlaz 2010). LFG production is a complex biological phenomenon carried out by microorganisms. The rate of production and amount of LFG produced by microbes depends on the methane generating potential (Lo) of the material and the microbial decay rate (k) of the material. Methane and CO2 production rates from decomposing building materials were modeled by a modified solution to a first-order landfill decay equation and are given by Eq. 5 (De La Cruz and Barlaz 2010). In Eq. 5, the physical constants are combined together and collectively termed B.
$$ \left[{\mathrm{CH}}_4\right](t)=\left[\frac{M_{\mathrm{o}}{L}_{\mathrm{o}}k\bullet p\bullet \mathrm{mw}}{V_{\mathrm{atm}} RT}\right]{e}^{- kt}=\frac{B}{V_{\mathrm{atm}}}{e}^{- kt} $$
(5)
$$ \mathrm{where}\ B=\left[\frac{M_{\mathrm{o}}{L}_{\mathrm{o}}k\bullet p\bullet \mathrm{mw}}{RT}\right] $$
The factors contained in B are the physical constants that affect the rate of CH4 production in a landfill. The constant M0 is the mass of biodegradable material disposed of in a landfill. The factors mw and R represent the molecular weight of CH4 (16 g/mol) and the ideal gas law constant (0.0821 L atm/mol K) respectively. The factors Lo and k represent the methane production potential of a particular material and the decay rate of biodegradable material. These constants can only be determined empirically, from both laboratory methods and field surveys, and vary widely (Bogner and Spokas 1993; Hansen et al. 2004; Schirmer et al. 2014). This work utilizes the constants Lo = 170 m3/MT and k = 0.05 1/year which are used as parameters for a conventional landfill, in the EPA’s Landfill Gas Emissions Model (LandGEM). Factors p and T represent the barometric pressure of CH4 within the interstices and the temperature within the landfill. For this work, conservative values of p = 1 atm and T = 20 °C (293 K) are used. Pressure and temperature change with landfill depth and season, but range around 1 atm and 20 °C (Yesiller and Hanson 2003).
Multiplying both sides of Eq. 5 by Vatm provides the mass of CH4 (instead of concentration [CH4]) at time t, emitted from landfilled material:
$$ {\mathrm{CH}}_4(t)=\left[\frac{M_{\mathrm{o}}{L}_{\mathrm{o}}k\bullet p\bullet \mathrm{mw}}{RT}\right]{e}^{- kt}=B{e}^{- kt} $$
(6)
Note that the symbols with square brackets represent concentration in mass/volume, while symbols with no brackets represent mass of CH4.
Landfill gas is generally considered to be a mixture of 50% CH4 and 50% CO2. The mass of CO2 produced by landfills is derived as a proportion of the mass of CH4 produced (EPA 2005; De La Cruz and Barlaz 2010). The amount of CO2 in LFG is given as a percentage of CH4 (PCH4) as shown below:
$$ \left(1-{P}_{\mathrm{CH}4}\right)\bullet \mathrm{LFG}(t)=\left(1-{P}_{\mathrm{CH}4}\right)\bullet \left[{\mathrm{CH}}_4(t)+{\mathrm{CO}}_2(t)\right]={\mathrm{CO}}_2(t) $$
(7)
Rearranging Eq. 7 for CO2(t) gives an equation for the mass of CO2 produced as a proportion of the mass of CH4 generated:
$$ {\mathrm{CO}}_2(t)=\left[\frac{1}{P_{\mathrm{CH}4}}-1\right]{\mathrm{CH}}_4(t) $$
(8)
The LFG(t) produced by the landfill is the sum of the masses of CH4(t) and CO2(t) as below. To report the GWP (in CO2 equivalents) of LFG(t) from landfilled materials, CH4 is multiplied by 25 to account for its 25-fold increased heat trapping efficiency of methane.
$$ \mathrm{LFG}(t)={\mathrm{CO}}_2(t)+25{\mathrm{CH}}_4(t) $$
(9)
Substituting Eqs. 7 and 8 into Eq. 9 gives Eq. 10, which provides an expression for GWP (in CO2 equivalents) from LFG production in terms of CH4 and time.
$$ \mathrm{LFG}(t)=\left[\frac{1}{P_{\mathrm{CH}4}}-1\right]{\mathrm{CH}}_4(t)+25{\mathrm{CH}}_4(t)=\left(\frac{1}{P_{\mathrm{CH}4}}+24\right){\mathrm{CH}}_4(t) $$
(10)
Substituting Eq. 6, for the mass of CH4 produced by a mass of landfilled material (CH4(t)), in Eq. 10, provides the expression for the time-dependent production of LFG (Eq. 11), based on the mass of the landfilled material and physical constants.
$$ \mathrm{LFG}(t)=\left(\frac{1}{P_{\mathrm{CH}4}}+24\right)B{e}^{- kt} $$
(11)
Removal of GHG emissions associated with landfilled building materials over time
When considering the time-dependent removal of GHGs from the material disposed of in a landfill, Eq. 1 (for a pulse input of GHG into the atmosphere) must be modified to include the time-dependent input of LFG into the CSTR as well as the time-dependent removal of the GHGs by Earth’s GHG removal mechanisms (sinks). Methane and CO2 emissions are modeled separately and added together at the end, since each gas has a different atmospheric residence time. Equation 12 represents the mass flow of CH4 produced by a mass of material in a landfill (Be−kt) flowing into the atmosphere and removal of CH4 by natural mechanisms (−QCH4[CH4]).
$$ {V}_{\mathrm{atm}}\frac{d\left[{\mathrm{CH}}_4\right]}{dt}=B{e}^{- kt}-{Q}_{\mathrm{CH}4}\left[{\mathrm{CH}}_4\right] $$
(12)
Equation 12 gives the production rate of CH4 from anaerobically digested biodegradable organic material. Dividing through by Vatm and rearranging Eq. 12 gives the non-homogeneous differential equation:
$$ \frac{d\left[{\mathrm{CH}}_4\right]}{dt}+\frac{1}{\theta_{\mathrm{CH}4}}\left[{\mathrm{CH}}_4\right]=\frac{B}{V_{\mathrm{atm}}}{e}^{- kt} $$
(13)
where θCH4 is the atmospheric residence time of CH4.
With the initial condition [CH4] = 0, at t = 0, the solution to Eq. 13 is an explicit, time-dependent expression for the atmospheric concentration of CH4.
$$ \left[{\mathrm{CH}}_4\right](t)=\frac{B}{V_{\mathrm{atm}}}\left[\frac{1}{\frac{1}{\theta_{\mathrm{CH}4}}-k}\right]\left[{e}^{- kt}-{e}^{-\frac{t}{\theta_{\mathrm{CH}4}}}\right] $$
(14)
Multiplying through by Vatm gives Eq. 15, which is the mass of atmospheric CH4 at each moment in time.
$$ {\mathrm{CH}}_4(t)=B\left[\frac{1}{\frac{1}{\theta_{\mathrm{CH}4}}-k}\right]\left[{e}^{- kt}-{e}^{-\frac{t}{\theta_{\mathrm{CH}4}}}\right] $$
(15)
To model CO2 production from landfilled materials, Eq. 8 gives the yield of CO2 as a percentage of CH4 produced in a landfill, and Eq. 16 gives the CO2 mass input from a landfill (\( \left[\frac{1}{P_{\mathrm{CH}4}}-1\right]B{e}^{- kt} \)), into the atmosphere with an exit (−QCO2[CO2]) representing Earth’s CO2 removal mechanisms.
$$ {V}_{\mathrm{atm}}\frac{d\left[{\mathrm{CO}}_2\right]}{dt}=\left[\frac{1}{P_{\mathrm{CH}4}}-1\right]B{e}^{- kt}-{Q}_{\mathrm{CO}2}\left[{\mathrm{CO}}_2\right] $$
(16)
Dividing by Vatm and rearranging Equation 16 gives a non-homogeneous differential, where (\( {\theta}_{\mathrm{CO}2}=\frac{V_{\mathrm{atm}}}{Q} \)) is the atmospheric residence time of CO2.
$$ \frac{d\left[{\mathrm{CO}}_2\right]}{dt}+\frac{1}{\theta_{\mathrm{CO}2}}\left[{\mathrm{CO}}_2\right]=\left[\frac{1}{P_{\mathrm{CH}4}}-1\right]\frac{B}{V_{\mathrm{atm}}}{e}^{-\mathrm{k}t} $$
(17)
The solution to Eq. 17, with the initial condition, [CO2] = 0, at t = 0, is an expression for the atmospheric concentration of CO2 from a mass of landfilled material, as a function of time.
$$ \left[{\mathrm{CO}}_2\right](t)=\frac{B}{V_{\mathrm{atm}}}\left[\frac{1}{\frac{1}{\theta_{\mathrm{CO}2}}-k}\right]\left[{e}^{- kt}-{e}^{-\frac{t}{\theta_{\mathrm{CO}2}}}\right] $$
(18)
Multiplying through by Vatm provides the mass of CO2 produced from the landfilled material.
$$ {\mathrm{CO}}_2(t)=B\left[\frac{1}{\frac{1}{\theta_{\mathrm{CO}2}}-k}\right]\left[{e}^{- kt}-{e}^{-\frac{t}{\theta_{\mathrm{CO}2}}}\right] $$
(19)
The total time-dependent GWP of the landfill gas emitted by material (in kgCO2e) is given by Eq. 9, where the mass of CH4 produced is multiplied by 25 to account for methane’s 25-fold greater heat trapping capacity. Substituting Eqs. 15 and 19 into the CH4 and CO2 masses in Eq. 9 gives Eq. 20, which is the GWP due to CH4 and CO2 (LFG) produced in time by a mass of landfilled material.
$$ \mathrm{LFG}(t)=B\left\{\left[\frac{25}{\frac{1}{\theta_{\mathrm{CH}4}}-k}\right]\left[{e}^{- kt}-{e}^{-\frac{t}{\theta_{\mathrm{CH}4}}}\right]+\left[\frac{1}{P_{\mathrm{CH}4}}-1\right]\left[\frac{1}{\frac{1}{\theta_{\mathrm{CO}2}}-k}\right]\left[{e}^{- kt}-{e}^{-\frac{t}{\theta_{\mathrm{CO}2}}}\right]\right\} $$
(20)
Lifetime embodied carbon GHG emissions associated with building materials
The GWP for the lifetime of a building material is the sum of the GHG emitted during manufacture (Eq. 3) and the end-of-life treatment: (i) incineration (Eq. 4) or (ii) landfill disposal (Eq. 20). The time of demolition (TDemo) of a building is the time span from its construction to its demolition. The amount of atmospheric GHG, due to the manufacture, demolition at TDemo, with incineration disposal of the material is given by Eq. 21.
$$ {G}_{\mathrm{I}}(t)=G(t)+{G}_{\mathrm{bio}}(t)={G}_0{e}^{-\frac{t}{\theta_{\mathrm{CO}2}}}+{G}_{\mathrm{bio}}(t)\left\{\begin{array}{c}0\kern9.25em \mathrm{for}\ t<{T}_{\mathrm{Demo}}\\ {}m\bullet {\mathrm{EC}}_{\mathrm{bio}}{e}^{-t/{\theta}_{\mathrm{CO}2}}\kern0.5em \mathrm{for}\ t\ge {T}_{\mathrm{Demo}}\end{array}\right. $$
(21)
Equation 22 represents the amount of atmospheric GHG remaining from the manufacture and landfill disposal of C&D debris at TDemo (GL(t) ).
$$ {G}_L(t)=G(t)+\mathrm{LFG}(t)={G}_0(t){e}^{-\frac{t}{\theta_{\mathrm{CO}2}}}+\mathrm{LFG}(t)\left\{\begin{array}{c}0\kern3.25em \mathrm{for}\ t<{T}_{\mathrm{Demo}}\\ {}\mathrm{LFG}(t)\kern0.5em \mathrm{for}\ t\ge {T}_{\mathrm{Demo}}\end{array}\right. $$
(22)
Embodied carbon GHG emissions associated with entire building, over time
Equation 23 provides the time-dependent (G(t)build), the sum of the G(t) values for manufacture of each building component plus the end-of-life treatments (incineration or landfill:
$$ {G}_{\mathrm{build}}(t)=\sum G(t)+\left\{\begin{array}{c}0\kern3.75em \mathrm{for}\ t<{T}_{\mathrm{Demo}}\\ {}\sum {G}_I(t)\kern1em \mathrm{for}\ t\ge {T}_{\mathrm{Demo}}\\ {}\sum {G}_L(t)\kern1em \mathrm{for}\ t\ge {T}_{\mathrm{Demo}}\end{array}\right. $$
(23)
where, G(t) = GHG emissions from manufacture of all materials in the building.
GI(t) = GHG emissions from combustion of incinerable materials.
GL(t) = GHG emissions from landfill disposal.
Global warming impact due to materials
In this work, a new term, Global Warming Impact of Materials (GWIM), is introduced and defined as below:
“Global Warming Impact of Materials (GWIM) includes all GHG emissions associated with a material including its manufacture (EC), and end-of-life treatment of demolition debris, over a time until they are reduced to zero.”
The GWIM of a material or an assembly of materials is determined from the area under the GHG emissions vs time profiles for materials or assemblies of materials (Eqs. 21, 22, and 23) and is given as Eq. 24.
$$ \mathrm{GWIM}={\int}_0^{T_{\infty }}G(t) dt $$
(24)
In the CSTR model, the atmospheric residence time of molecules is a statistical distribution of the lifetime of molecules in the reactor. The mean of this distribution is the residence time for each GHG (Trussell and Hand 2005). Because this is a statistical distribution, some of the GHG molecules will remain forever in the reactor. The mathematical exponential lifetime GHG emission models show that at 700 years, there are less than 1% of the original GHG molecules left in the atmosphere. Therefore, for purposes of calculating GWIM values, it is assumed that T∞ = 700 years.
Productive and non-productive impact of GHG emissions associated with materials
Any material that is manufactured has an impact on the Earth’s environment. Even the most environmentally friendly materials and manufacturing processes consume raw materials and require energy to produce. In this research, “productive GWIM” (GWIMp) is defined as the GWIM of materials during the time that the material or building is being utilized. Conversely, a non-productive GWIM (GWIMnp) is defined as the GWIM after a building is demolished at TDemo, at the end of its service life. After a building is demolished, some of the embodied carbon from manufacturing of the materials remains in the atmosphere. The remaining emissions can be considered a squandering of the original GHG emissions associated with the materials. These emissions provide no positive value and only negatively affect society by causing global warming. Greenhouse gas emissions from incineration or landfilling of debris are all considered non-productive as they only enhance global warming, but provide no use of the facility. It should be clarified that productive and non-productive do not imply any goodness or badness to the building, instead productive simply implies the material or building is being used and non-productive means it is not. Equations 25 and 26 give the productive and non-productive GWIMs:
$$ {\mathrm{GWIM}}_{\mathrm{p}}={\int}_0^{{\mathrm{T}}_{\mathrm{Demo}}}G(t) dt $$
(25)
$$ {\mathrm{GWIM}}_{\mathrm{np}}={\int}_{T_{\mathrm{Demo}}}^{T_{\infty }}G(t) dt $$
(26)
Added together, GWIMp and GWIMnp give the total GWIM for a material or assembly of materials (Eq. 24). The GWIMp and GWIMnp are of particular importance when describing materials such as cement or glass that have outstanding emissions from their manufacture, but do not emit GHGs after they are disposed of in landfills, against wood or plastics that emit GHGs after they are demolished and either incinerated or landfilled.
Simulations of lifetime GHG emissions for various service lives and various end-of-life treatments for a residential building
The simulations were performed using Microsoft® EXCEL spreadsheet. Integration of the GWIM curves was performed using the trapezoidal rule with the time step set to 0.25 years. In this paper, the lumber portion of the building materials was modeled for demonstrating the simulations. Modeling and computing lifetime GHG emissions, two service lives were selected: 50 years and 100 years, and three most used end-of-life treatments were selected for computations and for making objective comparisons between the treatments: incineration, landfill disposal, and deconstruction.