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Research article Topical Sections

An economic evaluation of alternative biofuel deployment scenarios in the USA

  • Energy market conditions have shifted dramatically since the USA renewable fuel standards (RFS1 in 2005; RFS2 in 2007) were enacted. The USA has transitioned from an increasing dependence on oil imports to abundant domestic oil production. In addition, increases in the use of ethanol, the main biofuel currently produced in the USA, is now limited by the blend wall constraint. Given this, the current study evaluates alternative biofuel deployment scenarios in the USA, accounting for changes in market conditions. The analysis is performed with a general equilibrium model that reflects the structure of the USA biofuel market as the transition to advanced biofuels begins. Results suggest that ethanol consumption would increase, albeit slowly, if current biofuel deployment rates of about 10% are maintained as persistently lower oil prices lead to a gradual increase in the consumption of liquid transportation fuels. Without the blend wall constraint, this study finds that the overall economic impact of a full implementation of the USA RFS2 policy is largely neutral before 2022. However, the economic impacts become slightly negative under the blend wall constraint since more expensive bio-hydrocarbons are needed to meet the RFS2 mandates. Results for a scenario with reduced advanced biofuel deployment based on current policy plans show near neutral economic impacts up to 2027. This scenario is also consistent with another scenario where the volume of bio-hydrocarbons deployed is reduced to adjust for its higher cost and energy content relative to deploying the mandated RFS2 advanced biofuel volumes as ethanol. The important role of technological change is demonstrated under pioneer and accelerated technology scenarios, with the latter leading to neutral or positive economic effects up to 2023 under most blend wall scenarios. All scenarios evaluated in this study are found to have positive long-term benefits for the USA economy.

    Citation: Gbadebo Oladosu. An economic evaluation of alternative biofuel deployment scenarios in the USA[J]. AIMS Energy, 2017, 5(3): 374-396. doi: 10.3934/energy.2017.3.374

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  • Energy market conditions have shifted dramatically since the USA renewable fuel standards (RFS1 in 2005; RFS2 in 2007) were enacted. The USA has transitioned from an increasing dependence on oil imports to abundant domestic oil production. In addition, increases in the use of ethanol, the main biofuel currently produced in the USA, is now limited by the blend wall constraint. Given this, the current study evaluates alternative biofuel deployment scenarios in the USA, accounting for changes in market conditions. The analysis is performed with a general equilibrium model that reflects the structure of the USA biofuel market as the transition to advanced biofuels begins. Results suggest that ethanol consumption would increase, albeit slowly, if current biofuel deployment rates of about 10% are maintained as persistently lower oil prices lead to a gradual increase in the consumption of liquid transportation fuels. Without the blend wall constraint, this study finds that the overall economic impact of a full implementation of the USA RFS2 policy is largely neutral before 2022. However, the economic impacts become slightly negative under the blend wall constraint since more expensive bio-hydrocarbons are needed to meet the RFS2 mandates. Results for a scenario with reduced advanced biofuel deployment based on current policy plans show near neutral economic impacts up to 2027. This scenario is also consistent with another scenario where the volume of bio-hydrocarbons deployed is reduced to adjust for its higher cost and energy content relative to deploying the mandated RFS2 advanced biofuel volumes as ethanol. The important role of technological change is demonstrated under pioneer and accelerated technology scenarios, with the latter leading to neutral or positive economic effects up to 2023 under most blend wall scenarios. All scenarios evaluated in this study are found to have positive long-term benefits for the USA economy.


    In real control problems, there exited many uncertainties, like model structure, measurement, external disturbance and so on, tradition PID and type-1 fuzzy controller can’t deal with these uncertainties [1,2,3,4,5]. Type-2 fuzzy controller can handle uncertainties more robust than PID and type-1 fuzzy controller for it was described by type-2 fuzzy sets proposed by Zadeh in 1975 [6]. Type-2 fuzzy sets mainly included interval type-2 fuzzy sets whose secondary membership degree was 1 and general type-2 fuzzy sets whose secondary membership degree was decided by a function, such as triangular, Gaussian, trapezoid. As the secondary membership degree of interval type-2 fuzzy sets was 1, so it was easily to be implemented and Karnik-Mendel (KM) algorithm was the most widely applied type reduction for interval type-2 fuzzy sets [7]. Interval type-2 fuzzy logic systems has been applied in many applications, like face recognition [8], prediction problems [9,10,11], pattern recognition [12], clustering [13], intelligent control [14], industrial [15], neuro-fuzzy systems [16], interval type-2 fuzzy PID controller [17,18], sculpting the state space [19], peer-to-peer e-commerce [20], classification [21,22], regression [23], diagnosis problems [24], metaheuristics [25], gravitational search algorithm [26], healthcare problem [27], unmanned aerial vehicles [28], deep neural network [29], pursuit evasion game [30], analytical structure of interval type-2 fuzzy controller [31,32,33] and so on.

    As the secondary membership degree of general type-2 fuzzy sets was determined by a function rather than 1, so general type-2 fuzzy sets contained more uncertain information than interval type-2 fuzzy sets. And general type-2 fuzzy logic systems had more design parameters when describing reality. Thus, general type-2 fuzzy systems can obtain a better performance in some control systems with high uncertainties. Now there existed some efficient type reduction algorithms for general type-2 fuzzy sets, for example, α-plane representation method [34,35,36], zSlices-based representation method [37,38], sample method [39], geometric method [40,41], hierarchical collapsing method [42] and so on. In these algorithms, α-plane representation method was widely applied in general type-2 fuzzy sets type reduction. By α-plane representation, general type-2 fuzzy sets will be assembled by some interval type-2 fuzzy sets (α-planes). Some exiting interval type-2 fuzzy sets type reduction algorithms can be applied to these α-planes, like KM, EKM [46], IASC [47] or EIASC [48]. General type-2 fuzzy logic systems have been applied in many situations, like: mobile robots [38,46,47,48,49,50,51], water tank [52], traffic signal scheduling [53], inverted pendulum plant [54], 5-agents system [55], nonlinear power systems [56], water level and DC motor speed [57], aerospace [58], airplane flight [59], steam temperature [60], power-line inspection robots [61,62], fractional order general type-2 fuzzy controller [63,64], medical diagnosis [65,66,67], fuzzy classifier and clustering [68,69], sculpting the state space [70], similarity measures [71], forecasting [72], brain-machine interface [73] and so on. [74,75,76] made a detailed introduction on type 2 fuzzy logic applications.

    The type reduction of general type-2 fuzzy sets was converted to type reduction of several interval type-2 fuzzy sets. And KM type reduction algorithm was applied to these interval type-2 fuzzy sets in most applications. KM algorithm was an iterative process without analytic solution. The number of α-planes and iterative process of KM algorithm decided the execution time of general type-2 fuzzy sets type reduction. Thus the real time of general type-2 fuzzy controller was weaker than type-1 and interval type-2 fuzzy controller. In according with these problems, a simplified general type-2 fuzzy PID (SGT2F-PID) controller is studied. The SGT2F-PID controller applies triangular function as the primary and secondary membership function. The inputs of SGT2F-PID controller are error and error derivative, and each input defines 2 fuzzy membership functions in fuzzy domains, thus only 4 rules will be derived in this SGT2F-PID controller. This paper mainly contains the following 3 contributions:

    Ⅰ). The primary membership degree of apex for secondary membership degree is applied to get the centroid of SGT2F-PID controller. Then the real time of SGT2F-PID controller is almost the same as conventional type-1 fuzzy PID (T1F-PID) controller and better than interval and general type-2 fuzzy PID controller.

    Ⅱ). The primary membership degree of apex for secondary membership degree is decided by the up and low bounds of footprint of uncurtains, which inherits the benefits of type-2 fuzzy PID controller. So the SGT2F-PID controller contains more design freedom and handles uncertainties better than PID or type-1 fuzzy PID controller.

    Ⅲ). The accurate mathematical expression of SGT2F-PID controller is obtained and compared with mathematical expressions of interval type-2 fuzzy PID controller (IT2F-PID) and conventional T1F-PID controller. The mathematical expressions indicate that these 3 fuzzy PID controllers are all PID type controller. Furthermore, we obtain the relationship of controller gains and explain why SGT2F-PID controller can get better controlling effects.

    A type-1 fuzzy set in the universe X is characterized by a membership function μA(x) as Eq (1).

    A={(x,μA(x))|xX} (1)

    where μA:X[0,1], and μA(x) represents the membership degree of the element xX to the set A.

    A general type-2 fuzzy sets ˜A defined in universal sets X can be described as Eq (2) [77].

    ˜A={(x,u),μ˜A(x,u)|xX,u[0,1]} (2)

    u is the primary membership degree and μ˜A(x,u) is the secondary membership degree related to input variable x and primary membership degree u.

    If the secondary membership degrees μ˜A(x,u) are set to 1, then interval type-2 fuzzy sets can be shown as Eq (3).

    ˜A={(x,u),1|xX,u[0,1]} (3)

    Figure 1 shows the definition of type-1 fuzzy sets, interval type-2 fuzzy sets and general type-2 fuzzy sets whose secondary membership function is triangular.

    Figure 1.  Definition of (a). Type-1 fuzzy sets (b). Interval type-2 fuzzy sets (c). General type-2 fuzzy sets.

    Liu introduced an α-plane representation for general type-2 fuzz sets [34], and pointed that α-plane denoted as ˜Aα can be defined as Eq (4).

    ˜Aα={(x,u),μ˜A(x,u) (4)

    If assemble all α-planes {\boldsymbol{\tilde A}_\alpha }, then general type-2 fuzzy sets \boldsymbol{\tilde A} can be described as Eq (5).

    \boldsymbol{\tilde A} = \bigcup\limits_{\alpha \in [0, 1]} {FOU({{\boldsymbol{\tilde A}}_\alpha })} (5)

    The centroid of general type-2 fuzzy sets can be calculated by the centroids of its all α-planes {\boldsymbol{\tilde A}_\alpha }.

    {C_{\boldsymbol{\tilde A}(x)}} = \bigcup\limits_{\alpha \in [0, 1]} {\alpha /{C_{{{\boldsymbol{\tilde A}}_\alpha }(x)}}} (6)
    {C_{{{\boldsymbol{\tilde A}}_\alpha }(x)}} = [{l_{{{\boldsymbol{\tilde A}}_\alpha }}}, {r_{{{\boldsymbol{\tilde A}}_\alpha }}}] (7)

    {l_{{{\boldsymbol{\tilde A}}_\alpha }}} and {r_{{{\boldsymbol{\tilde A}}_\alpha }}} are the left and right end points of interval type-2 fuzzy sets {\boldsymbol{\tilde A}_\alpha } whose secondary membership degree is α.

    The general structure of fuzzy PID controller can be depicted as Figure 2 [76]. The antecedent parts can be type-1, interval type-2 or general type-2 fuzzy sets and the consequent parameters are crisp values.

    Figure 2.  Structure of fuzzy PID controller.

    In this paper, triangular primary function is applied. The inputs of general type-2 fuzzy PID controller are normalize error (E) defined in [-de-d1, de+d1] and error derivative (\dot E) defined in [ - d\dot e - d2, d\dot e + d2], which is shown as Figure 3. d1 and d2 decide the footprint of uncertain for primary membership degree, for simplify, de = d\dot e and d1 = d2.

    Figure 3.  Error and error derivative triangular primary membership function.

    The consequent parameters are symmetric and from Figure 3, 4 rules will be generated as follows, here H1 > H2 > -H2 > -H1.

    Figure 4.  Type-1 triangular membership function.

    Rule 1: If \dot E is \tilde N and E is \tilde N, then {y_1} = - {H_1}

    Rule 2: If \dot E is \tilde P and E is \tilde N, then {y_2} = - {H_2}

    Rule 3: If \dot E is \tilde N and E is \tilde P, then {y_3} = {H_2}

    Rule 4: If \dot E is \tilde P and E is \tilde P, then {y_4} = {H_1}

    Around the steady state, that is in interval [-de+d1, de-d1] for error and [ - d\dot e{\rm{ + }}d{\rm{2}}, d\dot e - d2] for error derivative, the upper and lower bounds of the primary membership degree of error and error derivative can be calculated by Eqs (8–11).

    \left\{ \begin{gathered} \bar \mu _E^{\tilde P} = \frac{{E + de + d1}}{{2 \times de}} \\ \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _E^{\tilde P} = \frac{{E + de - d1}}{{2 \times de}} \\ \end{gathered} \right. (8)
    \left\{ \begin{gathered} \bar \mu _E^{\tilde N} = \frac{{de + d1 - E}}{{2 \times de}} \\ \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _E^{\tilde N} = \frac{{de - d1 - E}}{{2 \times de}} \\ \end{gathered} \right. (9)
    \left\{ \begin{gathered} \bar \mu _{\dot E}^{\tilde P} = \frac{{\dot E + d\dot e + d2}}{{2 \times d\dot e}} \\ \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _{\dot E}^{\tilde P} = \frac{{\dot E + d\dot e - d2}}{{2 \times d\dot e}} \\ \end{gathered} \right. (10)
    \left\{ \begin{gathered} \bar \mu _{\dot E}^{\tilde N} = \frac{{d\dot e + d2 - \dot E}}{{2 \times d\dot e}} \\ \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _{\dot E}^{\tilde N} = \frac{{d\dot e - d2 - \dot E}}{{2 \times d\dot e}} \\ \end{gathered} \right. (11)

    By fuzzy inference of interval type-2 fuzzy logic systems and product operation, the fired membership degrees of fuzzy rules can be described as Eq (12).

    \text{Rule 1: }\ [{\bar f_1}, {\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _1}] = [\bar \mu _{\dot E}^{\tilde N} \times \bar \mu _E^{\tilde N}, \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _{\dot E}^{\tilde N} \times \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _E^{\tilde N}] (12.1)
    \text{Rule 2:}\ [{\bar f_2}, {\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _2}] = [\bar \mu _{\dot E}^{\tilde P} \times \bar \mu _E^{\tilde N}, \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _{\dot E}^{\tilde P} \times \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _E^{\tilde N}] (12.1)
    \text{Rule 3:}\ [{\bar f_3}, {\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _3}] = [\bar \mu _{\dot E}^{\tilde N} \times \bar \mu _E^{\tilde P}, \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _{\dot E}^{\tilde N} \times \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _E^{\tilde P}] (12.1)
    \text{Rule 4: }\ [{\bar f_4}, {\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _4}] = [\bar \mu _{\dot E}^{\tilde P} \times \bar \mu _E^{\tilde P}, \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _{\dot E}^{\tilde P} \times \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{\mu } _E^{\tilde P}] (12.1)

    The triangular membership function of type-1 fuzzy PID controller is depicted as Figure 4, also for simplify, de = d\dot e.

    In interval [-de, de] for error and [ - d\dot e, d\dot e] for error derivative, the membership degree of error and error derivative can be calculated as Eqs (13–16).

    \mu _E^P = \frac{{E + de}}{{2 \times de}} (13)
    \mu _E^N = \frac{{ - E + de}}{{2 \times de}} (14)
    \mu _{\dot E}^P = \frac{{\dot E + d\dot e}}{{2 \times d\dot e}} (15)
    \mu _{\dot E}^N = \frac{{ - \dot E + d\dot e}}{{2 \times d\dot e}} (16)

    So the fired membership degrees of fuzzy rules for type-1 fuzzy PID controller can be described as Eq (17).

    \text{Rule 1:}\ {f_1} = \mu _{\dot E}^N \times \mu _E^N (17.1)
    \text{Rule 2:}\ {f_2} = \mu _{\dot E}^P \times \mu _E^N (17.1)
    \text{Rule 3:}\ {f_3} = \mu _{\dot E}^N \times \mu _E^P (17.1)
    \text{Rule 4:}\ {f_4} = \mu _{\dot E}^P \times \mu _E^P (17.1)

    Figure 5 shows an example of membership degrees for fuzzy rules corresponding to consequent parameters using TIF-PID.

    Figure 5.  Type-1 fuzzy PID membership degrees of fuzzy rules and consequent parameters.

    From Figure 5 and defuzzification process of type-1 fuzzy sets, the output of type-1 fuzzy inference U(t) in Figure 2 can be calculated as Eq (18).

    {U_{T1}}{\rm{ = }}\frac{{\sum\limits_{i = 1}^4 {{f_i} \times {y_i}} }}{{\sum\limits_{i = 1}^4 {{f_i}} }} (18)

    where, fi is described as Eq (17) and yi = [-H1, -H2, H2, H1]. By the mathematical expression of Eqs (13–17) and yi, the final solution of UT1 can be expressed as Eq (19).

    \begin{gathered} {U_{T1}}{\rm{ = }}\frac{{({H_1} - {H_2}) \times \dot E + ({H_1} + {H_2}) \times E}}{{2de}} \\ {\rm{ = }}\frac{{({H_1} - {H_2}) \times {G_{CE}} \times \dot e + ({H_1} + {H_2}) \times {G_E} \times e}}{{2de}} \\ \end{gathered} (19)

    According to Eq (19) and Figure 2, the final output of T1F-PID controller can be expressed as Eq (20).

    {u_{T1}} = {G_{PD}} \times {U_{T1}} + {G_{PI}} \times \int {{U_{T1}}} (20)

    Combine Eq (19) and Eq (20), the output of T1F-PID controller is a PID type controller as Eq (21).

    {u_{T1}} = K_P^{T1} \times e + K_I^{T1} \times \int e + K_D^{T1} \times \dot e (21)

    where:

    K_P^{T1} = \frac{{{G_{PD}}({H_1} + {H_2}) \times {G_E} + {G_{PI}}({H_1} - {H_2}) \times {G_{CE}}}}{{2de}}
    K_I^{T1} = \frac{{{G_{PI}}({H_1} + {H_2}) \times {G_E}}}{{2de}}
    K_D^{T1} = \frac{{{G_{PD}}({H_1} - {H_2}) \times {G_{CE}}}}{{2de}}

    Figure 6 shows the shape of control surface of type-1 fuzzy controller, here H1 = 1 and H2 = 0.

    Figure 6.  The shape of control surface of type-1 fuzzy controller.

    For KM algorithm didn’t have analytic solution, so NT type reduction [78,79] algorithm will be applied to get the mathematical expression of IT2F-PID controller. Figure 7 shows an example of upper and lower bounds for fuzzy rules corresponding to consequent parameters using IT2F-PID controller.

    Figure 7.  Interval type-2 fuzzy PID membership degrees of fuzzy rules and consequent parameters.

    From Figure 7, by defuzzification process and NT algorithm, the output of interval type-2 fuzzy inference U(t) in Figure 2 can be calculated as Eq (22).

    {U_{IT2}}{\rm{ = }}\frac{{\sum\limits_{i = 1}^4 {({{\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} }_i} + {{\bar f}_i}) \times {y_i}} }}{{\sum\limits_{i = 1}^4 {({{\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} }_i} + {{\bar f}_i})} }} (22)

    where, [{\bar f_i}, {\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _i}] is described as Eq (12) and yi = [-H1, -H2, H2, H1]. By the mathematical expression of Eqs (8–12) and yi, the final solution of U can be expressed as Eq (23).

    \begin{gathered} {U_{IT2}}{\rm{ = }}\frac{{de[({H_1} - {H_2})\dot E + ({H_1} + {H_2})E]}}{{2(d{e^2}{\rm{ + }}d{1^2})}} \\ {\rm{ = }}\frac{{de[({H_1} - {H_2}){G_{CE}} \times \dot e + ({H_1} + {H_2}){G_E} \times e]}}{{2(d{e^2}{\rm{ + }}d{1^2})}} \\ \end{gathered} (23)

    According to Eq (23) and Figure 2, the final output of IT2F-PID controller can be expressed as Equation (24).

    {u_{IT2}} = {G_{PD}} \times {U_{IT2}} + {G_{PI}} \times \int {{U_{IT2}}} (24)

    Combine Eq (23) and Eq (24), the output of IT2F-PID controller can be calculated as Eq (25).

    {u_{IT2}} = K_P^{IT2} \times e + K_I^{IT2} \times \int e + K_D^{IT2} \times \dot e (25)

    where:

    K_P^{IT2} = \frac{{de \times [{G_{PD}}({H_1} + {H_2}) \times {G_E} + {G_{PI}}({H_1} - {H_2}) \times {G_{CE}}]}}{{2(d{e^2}{\rm{ + }}d{1^2})}}
    K_I^{IT2} = \frac{{de \times {G_{PI}}({H_1} + {H_2}) \times {G_E}}}{{2(d{e^2}{\rm{ + }}d{1^2})}}
    K_D^{IT2} = \frac{{de \times {G_{PD}}({H_1} - {H_2}) \times {G_{CE}}}}{{2(d{e^2}{\rm{ + }}d{1^2})}}

    Figure 8 shows the shape of control surface of interval type-2 fuzzy controller, here H1 = 1 and H2 = 0.

    Figure 8.  The shape of control surface of interval type-2 fuzzy controller.

    For type reduction of general type-2 fuzzy sets was converted to type reduction of several interval type-2 fuzzy sets, so the number of α-planes will affect the real time of GT2F-PID controller.

    Figure 9 shows an example of membership degrees for fuzzy rules corresponding to consequent parameters using GT2F-PID controller.

    Figure 9.  General type-2 fuzzy PID membership degrees of fuzzy rules and consequent parameters.

    The differences of GT2F-PID and SGT2F-PID controller can be seen from Figure 10.

    Figure 10.  Difference of GT2F-PID and SGT2F-PID controller.

    From Figure 10, GT2F-PID controller firstly fixes the number of α-planes, that is D. Then derives D intervals [{\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _i}({\alpha _j}), {\bar f_i}({\alpha _j})] (j = 1, 2, …, D) whose secondary membership degree is αj. KM or other interval type-2 type reduction algorithm will be applied for each interval type-2 fuzzy sets. And the last, assembles all the centroids of α-plane and gets the output of GT2F-PID controller.

    In this paper, the SGT2F-PID controller adapts the primary membership degree of α-plane (α = 1) as the membership degree of fuzzy rules, which is calculated as Eq (26).

    {f_i}(1) = {\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _i} + w({\bar f_i} - {\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _i}) (26)

    here, w is an adjustable parameter.

    The output of simplified general type-2 fuzzy inference U(t) in Figure 2 can be calculated as Equation (27).

    {U_{SGT2}}{\rm{ = }}\frac{{\sum\limits_{i = 1}^4 {{f_i}(1) \times {y_i}} }}{{\sum\limits_{i = 1}^4 {{f_i}(1)} }} = \frac{{\sum\limits_{i = 1}^4 {({{\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} }_i} + w({{\bar f}_i} - {{\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} }_i})) \times {y_i}} }}{{\sum\limits_{i = 1}^4 {({{\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} }_i} + w({{\bar f}_i} - {{\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} }_i}))} }} (27)

    where, [{\bar f_i}, {\underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{f} _i}] is described as Eq (12) and yi = [-H1, -H2, H2, H1]. By the mathematical expression of Eqs (8–12) and yi, the final solution of U can be expressed as Eq (28).

    \begin{gathered} {U_{SGT2}} = \frac{{(de - d1 + 2d1 \times w)[({H_1} - {H_2})\dot E + ({H_1} + {H_2})E]}}{{2(d{e^2} - 2de \times d1{\rm{ + }}d{1^2} + 4de \times d1 \times w)}} \\ {\rm{ }} = \frac{{(de - d1 + 2d1 \times w)[({H_1} - {H_2}){G_{CE}} \times \dot e + ({H_1} + {H_2}){G_E} \times e]}}{{2(d{e^2} - 2de \times d1{\rm{ + }}d{1^2} + 4de \times d1 \times w)}} \\ \end{gathered} (28)

    According to Eq (28) and Figure 2, the final output of SGT2F-PID controller can be expressed as Eq (29).

    {u_{SGT2}} = {G_{PD}} \times {U_{SGT2}} + {G_{PI}} \times \int {{U_{SGT2}}} (29)

    Combine Eq (28) and Eq (29), the output of SGT2F-PID controller can be calculated as Eq (30).

    {u_{SGT2}} = K_P^{SGT2} \times e + K_I^{SGT2} \times \int e + K_D^{SGT2} \times \dot e (30)

    where:

    K_P^{SGT2} = \frac{{(de - d1 + 2d1 \times w) \times [{G_{PD}}({H_1} + {H_2}) \times {G_E} + {G_{PI}}({H_1} - {H_2}) \times {G_{CE}}]}}{{2(d{e^2} - 2de \times d1{\rm{ + }}d{1^2} + 4de \times d1 \times w)}}
    K_I^{SGT2} = \frac{{(de - d1 + 2d1 \times w) \times {G_{PI}}({H_1} + {H_2}) \times {G_E}}}{{2(d{e^2} - 2de \times d1{\rm{ + }}d{1^2} + 4de \times d1 \times w)}}
    K_D^{SGT2} = \frac{{(de - d1 + 2d1 \times w) \times {G_{PD}}({H_1} - {H_2}) \times {G_{CE}}}}{{2(d{e^2} - 2de \times d1{\rm{ + }}d{1^2} + 4de \times d1 \times w)}}

    Figure 11 shows the shape of control surface of simplified general type-2 fuzzy controller, here H1 = 1, H2 = 0 and w = 0.

    Figure 11.  The shape of control surface of simplified general type-2 fuzzy controller.

    From the control surface curve of T1-FPID, IT2-FPID and SGT2-FPID controller, when the system error is near the endpoint, the output of SGT2-FPID controller is larger than T1-FPID and IT2-FPID, so the SGT2-FPID controller has the faster rising time. When the error is near zero, the output of SGT2-FPID controller is smoother than T1-FPID and IT2-FPID, so the SGT2-FPID controller has faster steady time and smaller overshoot.

    In summary, the unified T1-FPID, IT2F-PID and SGT2F-PID controller mathematical expressions can be indicated as Eq (31).

    \begin{gathered} {u_{FPID}} = K({G_{PD}}({H_1} + {H_2}) \times {G_E} + {G_{PI}}({H_1} - {H_2}) \times {G_{CE}}) \times e \\ {\rm{ }} + K{G_{PI}}({H_1} + {H_2}){G_E} \times \int e + K{G_{PD}}({H_1} - {H_2}) \times {G_{CE}} \times \dot e \\ \end{gathered} (31)

    where:

    {K_{T1}} = \frac{1}{{2de}} (32.1)
    {K_{IT2}} = \frac{{de}}{{2(d{e^2}{\rm{ + }}d{1^2})}} (32.2)
    {K_{SGT2}} = \frac{{(de - d1 + 2d1 \times w)}}{{2(d{e^2} - 2de \times d1{\rm{ + }}d{1^2} + 4de \times d1 \times w)}} (32.3)

    If calculate the derivative of KSGT2 to w, then the partial derivative is Eq (33).

    \frac{{\partial {K_{SGT2}}}}{{\partial w}} = \frac{{ - d1(d{e^2} - d{1^2})}}{{{{(d{e^2} - 2dede{1^2} + 4ded1w)}^2}}} \lt 0 (33)

    From Eq (33), KSGT2 is a decreasing function of w and in general, w is in range [0, 1]. So the ranges of KSGT2 is denoted as Eq (34).

    \left\{ \begin{gathered} K_{SGT2}^{\min } = \frac{1}{{2(de + d1)}}, w = 1 \\ K_{SGT2}^{\max } = \frac{1}{{2(de - d1)}}, w = 0 \\ \end{gathered} \right. (34)

    For de > d1, so, K_{SGT2}^{\max } > {K_{T1}} > {K_{IT2}} and K_{SGT2}^{\min } < {K_{IT2}} < {K_{T1}}, Figure 12 shows the curve of KSGT2 as w is rising from 0 to 1.

    Figure 12.  The curve of KSGT2 as w is rising from 0 to 1.

    when w = w1, KSGT2 = KT1 and w = w2, KSGT2 = KIT2, then w1 = (de-d1)/(2de) and w2 = 0.5.

    According to the characteristics of PID controller, the advantage of proportional action is timely. If increase proportional gain, then the system response speed will be enhanced (that is reducing the rising time and steady time) but the system overshoot will be increased. The integral action can eliminate static error, if increase integral gain, the system overshoot will be decreased. The differential action also has the advantage of timely, which is belonging to ‘future control’. If increase differential gain, the steady time and system overshoot will be reduced.

    From above analysis, if a control system maintains both faster response speed and smaller overshoot, the PID controller should chose larger proportional gain, integral gain and differential gain. Figure 12 shows that if w < w1, then the proportional gain, integral gain and differential gain of SGTF-PID are larger than T1F-PID and IT2F-PID.Thus the controlling efforts of SGTF-PID will be better than T1F-PID and IT2F-PID, which is proved by section 5 of four simulation examples.

    In simulations, 3 plants and a practical inverted pendulum system are tested to demonstrate the robustness and efficiency of SGT2F-PID. The controlling efforts of SGTF-PID are also compared with PID, T1F-PID, and IT2F-PID controller using NT type reduction algorithm.

    G(s) = \frac{1}{{{s^2} + 2\zeta {\omega _n}s + \omega _n^2}}{e^{ - Ls}} (35)

    The tuning PID controller parameters are KP = 0.4088, KI = 0.1084, KD = 0.3547 under case 1 plant parameters. Fuzzy PID controller parameters are GE = 0.7757, GCE = 0.7442, GPD = 3.5336, GPI = 0.6996, de = d\dot e = 1, d1 = d2 = 0.5, H1 = 1, H2 = 0, w = 0.1.

    Case 1: ζ = 1.125, ωn = 0.45, L = 0.4.

    Figure 13.  Step response curve of P1 in case 1.

    Case 2: ζ = 1.6875, ωn = 0.225, L = 0.4.

    Figure 14.  Step response curve of P1 in case 2.

    Case 3: ζ = 0.5624, ωn = 0.675, L = 0.4.

    Figure 15.  Step response curve of P1 in case 3.

    Case 4: ζ = 1.6875, ωn = 0.675, L = 0.6.

    Figure 16.  Step response curve of P1 in case 4.

    Table 1 summarizes some controlling performance comparisons of SGT2F-PID controller with other 3 controllers. In Table 1, ts is steady state time, tris rising time, OS is system overshoot and three error integral criterions ISE, ITSE, ITAE.

    ISE = \int_0^{ts} {e{{(t)}^2}dt}
    ITSE = \int_0^{ts} {t \times e{{(t)}^2}dt}
    ITAE = \int_0^{ts} {t \times \left| {e(t)} \right|dt}
    Table 1.  The controlling performance comparisons of 4 controllers (P1).
    P1 PID T1F-PID IT2F-PID SGT2F-PID
    case 1 ts(s) 12.3 6.1 6.69 4.96
    tr(s) 5.05 2.01 2.3 2.07
    OS (%) 5.1 22.2 19.1 14.9
    ISE 1.44 1.15 1.24 1.13
    ITSE 1.49 0.84 0.96 0.74
    ITAE 5.37 2.23 2.53 1.58
    case 2 ts(s) 17.68 8.5 9.3 7.01
    tr(s) 3.18 1.84 2.07 1.88
    OS (%) 29.8 39.2 35.1 28.0
    ISE 1.59 1.26 1.32 1.15
    ITSE 3.27 1.26 1.35 0.87
    ITAE 14.77 4.07 4.49 2.55
    Case3 ts(s) > 20 9.18 9.72 7.95
    tr(s) > 20 1.94 2.25 2.01
    OS (%) - 17.8 11.7 11.0
    ISE 1.74 1.13 1.21 1.11
    ITSE 3.78 0.86 0.93 0.76
    ITAE 20.26 2.98 3.04 2.27
    case 4 ts(s) > 20 8.85 9.61 8.0
    tr(s) 12.06 3.05 3.59 3.06
    OS (%) 2.3 9.9 9.9 7.1
    ISE 2.67 1.47 1.61 1.46
    ITSE 5.73 1.30 1.60 1.23
    ITAE 17.08 3.87 4.77 3.10

     | Show Table
    DownLoad: CSV
    G(s) = \frac{K}{{Ts - 1}}{e^{ - Ls}} (36)

    The tuning PID controller parameters are KP = 9.999, KI = 0.9483, KD = 0.2785 under case 1 plant parameters. Fuzzy PID controller parameters are GE = 1.9956, GCE = 0.9387, GPD = 0.2532, GPI = 20.0573, de = d\dot e = 1, d1 = d2 = 0.5, H1 = 1, H2 = 0, w = 0.

    Case 1: K = 1, T = 10, L = 0.2.

    Figure 17.  Step response curve of P2 in case 1.

    Case 2: K = 1, T = 10, L = 0.4.

    Figure 18.  Step response curve of P2 in case 2.

    Case 3: K = 1, T = 20, L = 0.2.

    Figure 19.  Step response curve of P2 in case 3.

    Case 4: K = 2, T = 20, L = 0.35.

    Figure 20.  Step response curve of P2 in case 4.

    Table 2. shows the P2 controlling performance comparisons of SGT2F-PID controller with other 3 controllers.

    Table 2.  The controlling performance comparisons of 4 controllers (P2).
    P2 PID T1F-PID IT2F-PID SGT2F-PID
    case 1 ts(s) 22.9 9.36 10.49 3.94
    tr(s) 1.78 2.0 2.31 2.49
    OS (%) 16.7 27.9 28.2 5.2
    ISE 0.71 1.09 1.23 1.09
    ITSE 1.53 0.96 1.23 0.72
    ITAE 16.02 3.62 4.70 1.37
    case 2 ts(s) 22.71 13.44 14.91 9.72
    tr(s) 1.56 1.95 2.2 2.14
    OS (%) 19.1 44.9 46.9 30.5
    ISE 0.90 1.44 1.60 1.26
    ITSE 1.64 1.92 2.51 1.10
    ITAE 15.86 7.56 10.00 3.77
    case 3 ts(s) 26.3 18.33 19.76 8.14
    tr(s) 3.37 2.62 3.01 2.96
    OS (%) 20.4 43.5 40.04 17.01
    ISE 1.27 1.78 1.91 1.44
    ITSE 4.13 3.63 4.02 1.36
    ITAE 29.76 15.44 17.88 3.69
    case 4 ts(s) 20.94 9.25 12.28 5.68
    tr(s) 1.71 1.98 2.27 2.25
    OS (%) 12.8 35.3 36.2 16.7
    ISE 0.75 1.27 1.41 1.17
    ITSE 0.96 1.30 1.65 0.82
    ITAE 11.26 4.60 6.28 1.84

     | Show Table
    DownLoad: CSV
    \frac{{{d^2}y(t)}}{{d{t^2}}} + 2\varepsilon \sigma \frac{{dy(t)}}{{dt}} + {\sigma ^2}{y^2}(t) = {\sigma ^2}u(t - L) (37)

    PID controller parameters are KP = 0.8028, KI = 1.8548, KD = 0.4609 selected from article [1] optimized by hybridized ABC-GA algorithm. Fuzzy PID controller parameters are GE = 0.8359, GCE = 0.1944, GPD = 20.5501, GPI = 20.2681, de = d\dot e = 1, d1 = d2 = 0.5, H1 = 1, H2 = 0, w = 0.

    Case 1: ε = 1, σ = 1, L = 0.

    Figure 21.  Step response curve of P3 in case 1.

    Case 2: ε = 1, σ = 1, L = 0.1.

    Figure 22.  Step response curve of P3 in case 2.

    Case 3: ε = 1, σ = 0.7, L = 0.

    Figure 23.  Step response curve of P3 in case 3.

    Case 4: ε = 1.3, σ = 1, L = 0.

    Figure 24.  Step response curve of P3 in case 4.

    Table 3 shows the P3 controlling performance comparisons of SGT2F-PID controller with other 3 controllers.

    Table 3.  The controlling performance comparisons of 4 controllers (P3).
    P3 PID T1F-PID IT2F-PID SGT2F-PID
    case 1 ts(s) 6.32 2.69 2.91 0.52
    tr(s) 1.41 0.62 0.69 0.6
    OS (%) 16.3 21.9 20.6 13.1
    ISE 0.52 0.28 0.31 0.25
    ITSE 0.26 0.07 0.08 0.04
    ITAE 1.34 0.33 0.38 0.15
    case 2 ts(s) 6.65 4.08 4.34 2.84
    tr(s) 1.42 0.61 0.69 0.58
    OS (%) 20.1 38.5 34.0 27.2
    ISE 0.62 0.41 0.43 0.34
    ITSE 0.36 0.16 0.16 0.08
    ITAE 1.73 0.64 0.7 0.30
    case 3 ts(s) 7.52 3.15 3.44 2.07
    tr(s) 1.3 0.6 0.67 0.58
    OS (%) 22.6 27.2 26.0 16.1
    ISE 0.54 0.29 0.33 0.25
    ITSE 0.33 0.09 0.11 0.04
    ITAE 1.93 0.43 0.51 0.18
    case 4 ts(s) 2.73 2.19 2.37 1.56
    tr(s) 1.27 0.53 0.6 0.55
    OS (%) 5.7 12.1 11.1 4.1
    ISE 0.36 0.21 0.23 0.20
    ITSE 0.10 0.03 0.04 0.02
    ITAE 0.33 0.15 0.17 0.07

     | Show Table
    DownLoad: CSV

    The inverted pendulum system was often applied to demonstrate the reliability of a new controller, as shown in Figure 25.

    Figure 25.  Inverted pendulum system.

    The inverted pendulum system is consisted of a cart and a pendulum, the controlling aim is to keep pendulum angle at a certain value under external force. Equation (38) describes the state equations of the inverted pendulum system [80].

    \left[ \begin{gathered} {{\dot x}_1} \\ {{\dot x}_2} \\ \end{gathered} \right] = \left[ \begin{gathered} {\rm{ }}{x_2} \\ \frac{{g\sin ({x_1}) - \frac{{({m_p} + \Delta {m_p})lx_2^2\sin ({x_1})\cos ({x_1})}}{{({m_p} + \Delta {m_p} + {m_c})}}}}{{\frac{{4l}}{3} - \frac{{(({m_p} + \Delta {m_p})l\cos {{({x_1})}^2}}}{{({m_p} + \Delta {m_p} + {m_c})}}}} \\ \end{gathered} \right] + \Delta A\left[ \begin{gathered} {x_1} \\ {x_2} \\ \end{gathered} \right] + \left[ \begin{gathered} {\rm{ }}0 \\ \frac{{\frac{{\cos ({x_1})}}{{({m_p} + \Delta {m_p} + {m_c})}}}}{{\frac{{4l}}{3} - \frac{{(({m_p} + \Delta {m_p})l\cos {{({x_1})}^2}}}{{({m_p} + \Delta {m_p} + {m_c})}}}} \\ \end{gathered} \right]u (38)

    In (38), x1is the pendulum angle θ and x2 is the pendulum angular velocity \dot \theta . u is the external force horizontally acted on the cart and the unit of u is Newton. mcis the cart mass, mp is the pendulum mass and 2l is the pendulum length. The values of these parameters are mc = 0.5kg, mc = 0.2kg, l = 0.5m, g = 9.8m/s2. Δmpand ΔA are respectively the uncertainty of pendulum mass and inverted pendulum structure.

    PID controller parameters are KP = 40, KI = 100, KD = 8. Fuzzy PID controller parameters are GE = 0.1009, GCE = 0.1944, GPD = 30.5501, GPI = 30.2681, de = d\dot e = 0.2, d1 = d2 = 0.1, H1 = 10, H2 = 5, w = 0.04.

    Case 1: Normal case.

    The initial conditions x1 = 0.1rad and x2 = 0rad/s, the setting value is x1 = 0rad. In normal case, Δmp = 0 and \Delta A = \left[ {\begin{array}{*{20}{c}} 0&0 \\ 0&0 \end{array}} \right].

    Figure 26.  System response curve of P4 in case 1.

    Case 2: Normal case.

    The initial conditions x1 = 0.4rad and x2 = 0rad/s, the setting value is x1 = 0rad. In normal case, Δmp = 0 and \Delta A = \left[ {\begin{array}{*{20}{c}} 0&0 \\ 0&0 \end{array}} \right].

    Figure 27.  System response curve of P4 in case 2.

    From case 3 to case 6, we will indicate the controlling effects of SGT2-FPID controller when the system adding uncertainties.

    Case 3: Pendulum mass uncertainty.

    Here, we will add pendulum mass uncertainty (Δmp = 2.7kg) at 2s.

    Figure 28.  System response curve of P4 in case 3.

    Case 4: Measurement uncertainty in pendulum angle.

    Here, we will add measurement uncertainty in pendulum angle θ (∆x1 = 0.052) at 3s.

    Figure 29.  System response curve of P4 in case 4.

    Case 5: Structure uncertainty. Here, we will add structural uncertainty in the inverted pendulum as 2s (\Delta A = \left[ {\begin{array}{*{20}{c}} {0.03}&{0.03} \\ {0.03}&{0.03} \end{array}} \right]), and the initial conditions x1 = 0.1rad and x2 = 0rad/s, the setting value is x1 = 0rad.

    Figure 30.  System response curve of P4 in case 5.

    Case 6: External disturbance uncertainty.

    Here, we will add an external disturbance of controlling force at 2s (∆d = 29N).

    Figure 31.  System response curve of P4 in case 6.

    Table 4 shows the P4 controlling performance comparisons of SGT2F-PID controller with other 5 controllers for case 1 and case 2. As compares with controlling performances of [80] and [81], another two error integral criterions are added as follows.

    RMSE = \sqrt {\frac{1}{N}\sum\limits_{i = 1}^N {e{{(i)}^2}} }
    IAE = \int_0^{ts} {\left| {e(t)} \right|dt}
    Table 4.  The controlling performance comparisons of 6 controllers (P4).
    P4 IT2F-PID [80] IT2F-PD+I [81] PID T1F-PID IT2F-PID SGT2F-PID
    case 1 ISE 0.036 - 2.78 × 10-4 3.32 × 10-4 2.53 × 10-4 1.9 × 10-4
    ITSE - - 2.34 × 10-5 2.0 × 10-5 7.22 × 10-6 3.64 × 10-6
    ITAE - - 0.0036 9.35 × 10-4 4.52 × 10-4 1.62 × 10-4
    RMSE 0.0085 - 0.0118 0.0129 0.013 0.0097
    IAE 1.8001 - 0.0101 0.0076 0.0051 0.0033
    case 2 ISE - 1.5844 0.0045 0.0064 0.0069 0.005
    ITSE - - 3.33 × 10-4 2.34 × 10-4 2.43 × 10-4 1.23 × 10-4
    ITAE - - 0.0119 0.003 0.0029 0.0014
    RMSE - 0.0514 0.0472 0.0568 0.0586 0.0499
    IAE - 7.4692 0.0379 0.029 0.0287 0.0191

     | Show Table
    DownLoad: CSV

    Table 5 shows the P4 controlling performance comparisons of SGT2F-PID controller with other 4 controllers for case 3 to case 6.

    Table 5.  The controlling performance comparisons of 5 controllers (P4).
    P4 IT2F-PD+I [81] PID T1F-PID IT2F-PID SGT2F-PID
    case 3 ISE 1.9203 0.0045 0.0064 0.0069 0.005
    ITSE - 3.56 × 10-4 2.34 × 10-4 2.43 × 10-4 1.25 × 10-4
    ITAE - 0.0288 0.0035 0.0037 0.0019
    RMSE 0.04 0.0273 0.0328 0.0338 0.0288
    IAE 14.7056 0.0419 0.0292 0.0290 0.0192
    case 4 ISE 2.527 0.0046 0.0066 0.007 0.0051
    ITSE - 6.47 × 10-4 5.9 × 10-4 5.5 × 10-4 4.0 × 10-4
    ITAE - 0.0316 0.0172 0.0154 0.011
    RMSE 0.0649 0.0276 0.0331 0.0341 0.0291
    IAE 13.3876 0.044 0.033 0.032 0.022
    case 5 ISE 0.094 2.78 × 10-4 3.32 × 10-4 2.53 × 10-4 1.90 × 10-4
    ITSE - 2.34 × 10-5 2.04 × 10-5 7.73 × 10-6 3.64 × 10-6
    ITAE - 0.0036 0.0010 5.08 × 10-4 1.89 × 10-4
    RMSE 0.0125 0.0068 0.0074 0.0065 0.0056
    IAE 2.2475 0.0101 0.0077 0.0052 0.0033
    case 6 ISE - 0.0046 0.0065 0.0069 0.005
    ITSE - 7.53 × 10-4 3.67 × 10-4 3.79 × 10-4 1.75 × 10-4
    ITAE - 0.0447 0.0169 0.0185 0.0091
    RMSE - 0.0278 0.0329 0.0340 0.0289
    IAE - 0.0508 0.0345 0.0347 0.022

     | Show Table
    DownLoad: CSV

    We discuss 3 kinds of fuzzy PID controllers and derive the mathematical expressions of TIF-PID, IT2F-PID and SGT2F-PID described by Eq (21), Eq (25) and Eq (30). The SGT2F-PID controller contains more adjustable parameters and only 4 fuzzy rules are generated. For the primary membership degree of α-plane (α = 1) is used to get the defuzzification result of SGT2F-PID controller, thus the SGT2F-PID controller maintains the ability of handing uncertainties as general type-2 fuzzy controller and higher real-time. By the mathematical expressions of TIF-PID, IT2F-PID and SGT2F-PID controller, the controlling performance is discussed and explains why SGT2F-PID controller has better controlling effects than TIF-PID and IT2F-PID controller.

    And 4 simulations including a second order linear plant, an unstable first order linear plant and two second order nonlinear plants are tested. In addition, the controller parameters of each plant are the same when the plant parameters are changed, which demonstrate the robustness of SGT2F-PID controller. From the 4 simulation results, when the controlled object changes, the SGT2F-PID controller can still maintain small overshoot, faster response time and stable time. Also the controller performance evaluation indexes (ISE, ITSE, ITAE) of SGT2F-PID controller are better than other 3 compared controllers. The results of simulation 4 indicates that, when the controlled object exists uncertainties of measurement, structure and external disturbance, the SGT2F-PID controller can handle these uncertainties more robust than PID, TIF-PID and IT2F-PID controller.

    The next researches will focus on the following 4 aspects:

    Ⅰ). Although SGT2F-PID controller can achieve better control performances, but the determined parameters are more than other controllers. How to determine the appropriate parameters will be a major work.

    Ⅱ). Triangular function is applied as primary and secondary membership function, other membership function like Gaussian, trapezoid will be discussed in the future.

    Ⅲ). In this paper, we fix the parameters de and d1 and discuss the influence of w on the controller parameters gains. In the future, we will study the influence of de and d1 on the controller parameters gains.

    Ⅳ). The fractional order simplified general type-2 fuzzy PID controller will be investigated and compared with existing PID and fuzzy PID controllers.

    This study was funded by the scientific research fund project of Nanjing Institute of Technology (YKJ201523, QKJ201802).

    The authors declare there is no conflict of interest.

    [1] Bracmort, Kelsi (2016) The Renewable Fuel Standard (RFS): Waiver Authority and Modification of Volumes. Congressional Service Report 7-5700. Available from: https://www.fas.org/sgp/crs/misc/R44045.pdf.
    [2] United States Department of Energy-DOE (2011) "US billion-ton update: Biomass supply for a bioenergy and bioproducts Industry. RD Perlack and BJ Stokes (Leads)." ORNL/TM-2011/224. Oak Ridge National Laboratory. Available from: http://www1.eere.energy.gov/biomass/pdfs/ billion_ton_update.Pdf.
    [3] U.S. Department of Energy 2016. 2016 Billion-Ton Report: Advancing Domestic Resources for a Thriving Bioeconomy, Volume 1: Economic Availability of Feedstocks. M. H. Langholtz, B. J. Stokes, and L. M. Eaton (Leads), ORNL/TM-2016/160. Oak Ridge National Laboratory, Oak Ridge, TN. 448p. Available from: http://energy.gov/sites/prod/files/2016/07/f33/2016_ billion_ton_report_0.pdf.
    [4] National Research Council-NRC (2010) Limiting the magnitude of future climate change. The National Academies Press, Washington, DC.
    [5] Kahouli S (2011) "Effects of technological learning and uranium price on nuclear cost: preliminary insights from a multiple factors learning curve and uranium market modeling". Energ Econ 33: 840–852. doi: 10.1016/j.eneco.2011.02.016
    [6] Tao Lin, Dan Schell, Ryan Davis, et al. (2014) NREL 2012 Achievement of Ethanol Cost Targets: Biochemical Ethanol Fermentation via Dilute-Acid Pretreatment and Enzymatic Hydrolysis of Corn Stover, Technical Report: NREL/TP-5100-61563, April 2014. Available from: http://www.nrel.gov/docs/fy14osti/61563.pdf.
    [7] Karatzos S, McMillan JD, Saddler JN (2014) The potential and challenges of drop-in biofuels. Report for IEA Bioenergy Task, 39. Available from: http://task39.sites.olt.ubc.ca/files/2014/01/Task-39-Drop-in-Biofuels-Report-FINAL-2-Oct-2014-ecopy.pdf.
    [8] Johnson C, Emily N, Aaron B, et al. (2015) High Octane Mid-Level Ethanol Blend Market Assessment. NREL/TP-5400-63698. Available from: http://www.afdc.energy.gov/uploads/ publication/high-octane_mid-level_ethanol_mkt_ assessment.pdf.
    [9] Oladosu G, Kline K, Leiby P, et al. (2012) Global economic effects of USA biofuel policy and the potential contribution from advanced biofuels. Biofuels 3: 703–723. doi: 10.4155/bfs.12.60
    [10] Oladosu G, Kline K (2013) A dynamic simulation of the ILUC effects of biofuel use in the USA. Energ policy 61: 1127–1139. doi: 10.1016/j.enpol.2013.06.124
    [11] Oladosu G (2012) Estimates of the global indirect energy-use emission impacts of USA biofuel policy. Appl Energ 99: 85–96. doi: 10.1016/j.apenergy.2012.04.045
    [12] Schumacher K, Sands RD (2006) Innovative energy technologies and climate policy in Germany. Energ Policy 34: 3929–3941. doi: 10.1016/j.enpol.2005.09.022
    [13] Schumacher K, Sands RD (2007) Where are the industrial technologies in energy-economy models? An innovative CGE approach for steel production in Germany. Energ Econ 29: 799–825.
    [14] Dutta A, Talmadge M, Hensley J, et al. (2011) Process design and economics for conversion of lignocellulosic biomass to ethanol. Thermochemical pathway by indirect gasification and mixed alcohol synthesis. Report by National Renewable Energy Laboratory for US Department of Energy Contract 303: 275–300.
    [15] Darzins A, Pienkos P, Edye L (2010) Current status and potential for algal biofuels production. A report to IEA Bioenergy Task, 39.
    [16] Wright MM, Daugaard DE, Satrio JA, et al. (2010) Techno-economic analysis of biomass fast pyrolysis to transportation fuels. Fuel 89: S2–S10. doi: 10.1016/j.fuel.2010.07.029
    [17] Swanson RM, Platon A, Satrio JA, et al. (2010) Techno-economic analysis of biomass-to-liquids production based on gasification. Fuel 89: S11–S19. doi: 10.1016/j.fuel.2010.07.027
    [18] Fortman J, Anex R, Kothandaraman G, et al. (2010) Techno-economic analysis of biochemical scenarios for production of cellulosic ethanol. Golden, CO: National Renewable Energy Laboratory.
    [19] Zhou X, Kojima S (2011) Biofuels data and social accounting matrices prepared for policy assessment models based on the GTAP 7 data base. Technical Report February, Institute for Global Environmental Strategies, Arlington, VA.
    [20] Grinsted JH, Bjoernsson AH, Lind KM (2013) By-products from ethanol production-the forgotten part of the equation: Possibilities and challenges. Report-Institute of Food and Resource Economics, University of Copenhagen.
    [21] Oladosu G, Kline K, Uria‐Martinez R, et al. (2011) Sources of corn for ethanol production in the United States: a decomposition analysis of the empirical data. Biofuel Bioprod Bior 5: 640–653. doi: 10.1002/bbb.305
    [22] Dantas GA, Legey LF, Mazzone A (2013) Energy from sugarcane bagasse in Brazil: an assessment of the productivity and cost of different technological routes. Renew Sust Energ Rev 21: 356–364. doi: 10.1016/j.rser.2012.11.080
    [23] Argo AJ, Gesick BD, Haq Z (2012) "Application of learning curves to IBR pioneer plant data, estimating transition of cellulosics to maturity". USDOE Communication.
    [24] IMF-International Monetary Fund (2015) World Economic and Financial Surveys World Economic Outlook Database Available from: https://www.imf.org/external/ pubs/ft/weo/2015/02/weodata/index.aspx.
    [25] EIA-United States Energy Information Administration (2015) "Annual Energy Outlook. Available from: http://www.eia.gov/forecasts/aeo/.
    [26] EIA-United States Energy Information Administration (2013) "International Energy Outlook. Available from: http://www.eia.gov/forecasts/ieo/pdf/0484(2013).pdf.
    [27] EPA-United States Environmental Protection Agency (2016) Proposed Renewable Fuel Standards for 2017, and the Biomass-Based Diesel Volume for 2018. Available from: https://www.epa.gov/renewable-fuel-standard-program/proposed-renewable-fuel-standards-2017-and-biomass-based-diesel.
    [28] Oladosu G, Msangi S (2013) Biofuel-food market interactions: a review of modeling approaches and findings. Agriculture 3: 53–71. doi: 10.3390/agriculture3010053
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