From: Metabolic modelling of polyhydroxyalkanoate copolymers production by mixed microbial cultures
Reaction
Kinetics
R 4 : Growth on Acetyl-CoA
R 4 = R 4 , max ⋅ A c A c + K S ⋅ N N + K N MathType@MTEF@5@5@+=feaagaart1ev2aaatCvAUfKttLearuWrP9MDH5MBPbIqV92AaeXatLxBI9gBaebbnrfifHhDYfgasaacPC6xNi=xH8viVGI8Gi=hEeeu0xXdbba9frFj0xb9qqpG0dXdb9aspeI8k8fiI+fsY=rqGqVepae9pg0db9vqaiVgFr0xfr=xfr=xc9adbaqaaeGaciGaaiaabeqaaeqabiWaaaGcbaGaemOuai1aaSbaaSqaaiabisda0aqabaGccqGH9aqpcqWGsbGudaWgaaWcbaGaeGinaqJaeiilaWIagiyBa0MaeiyyaeMaeiiEaGhabeaakiabgwSixNqbaoaalaaabaGaemyqaeKaem4yamgabaGaemyqaeKaem4yamMaey4kaSIaem4saS0aaSbaaeaacqWGtbWuaeqaaaaakiabgwSixNqbaoaalaaabaGaemOta4eabaGaemOta4Kaey4kaSIaem4saS0aaSbaaeaacqWGobGtaeqaaaaaaaa@4A03@
R 5 : Growth on Propionyl-CoA
R 5 = R 5 , max ⋅ Pr o p Pr o p + K S ⋅ N N + K N MathType@MTEF@5@5@+=feaagaart1ev2aaatCvAUfKttLearuWrP9MDH5MBPbIqV92AaeXatLxBI9gBaebbnrfifHhDYfgasaacPC6xNi=xH8viVGI8Gi=hEeeu0xXdbba9frFj0xb9qqpG0dXdb9aspeI8k8fiI+fsY=rqGqVepae9pg0db9vqaiVgFr0xfr=xfr=xc9adbaqaaeGaciGaaiaabeqaaeqabiWaaaGcbaGaemOuai1aaSbaaSqaaiabiwda1aqabaGccqGH9aqpcqWGsbGudaWgaaWcbaGaeGynauJaeiilaWIagiyBa0MaeiyyaeMaeiiEaGhabeaakiabgwSixNqbaoaalaaabaGagiiuaaLaeiOCaiNaem4Ba8MaemiCaahabaGagiiuaaLaeiOCaiNaem4Ba8MaemiCaaNaey4kaSIaem4saS0aaSbaaeaacqWGtbWuaeqaaaaakiabgwSixNqbaoaalaaabaGaemOta4eabaGaemOta4Kaey4kaSIaem4saS0aaSbaaeaacqWGobGtaeqaaaaaaaa@501F@
R 6 : Catabolism
R 6 = R 6 , max ⋅ S S + K S MathType@MTEF@5@5@+=feaagaart1ev2aaatCvAUfKttLearuWrP9MDH5MBPbIqV92AaeXatLxBI9gBaebbnrfifHhDYfgasaacPC6xNi=xH8viVGI8Gi=hEeeu0xXdbba9frFj0xb9qqpG0dXdb9aspeI8k8fiI+fsY=rqGqVepae9pg0db9vqaiVgFr0xfr=xfr=xc9adbaqaaeGaciGaaiaabeqaaeqabiWaaaGcbaGaemOuai1aaSbaaSqaaiabiAda2aqabaGccqGH9aqpcqWGsbGudaWgaaWcbaGaeGOnayJaeiilaWIagiyBa0MaeiyyaeMaeiiEaGhabeaakiabgwSixNqbaoaalaaabaGaem4uamfabaGaem4uamLaey4kaSIaem4saS0aaSbaaeaacqWGtbWuaeqaaaaaaaa@3F32@
R 7 : Maintenance
R 7 = R 7 , max ⋅ S S + K S MathType@MTEF@5@5@+=feaagaart1ev2aaatCvAUfKttLearuWrP9MDH5MBPbIqV92AaeXatLxBI9gBaebbnrfifHhDYfgasaacPC6xNi=xH8viVGI8Gi=hEeeu0xXdbba9frFj0xb9qqpG0dXdb9aspeI8k8fiI+fsY=rqGqVepae9pg0db9vqaiVgFr0xfr=xfr=xc9adbaqaaeGaciGaaiaabeqaaeqabiWaaaGcbaGaemOuai1aaSbaaSqaaiabiEda3aqabaGccqGH9aqpcqWGsbGudaWgaaWcbaGaeG4naCJaeiilaWIagiyBa0MaeiyyaeMaeiiEaGhabeaakiabgwSixNqbaoaalaaabaGaem4uamfabaGaem4uamLaey4kaSIaem4saS0aaSbaaeaacqWGtbWuaeqaaaaaaaa@3F36@
R 9 : Acetyl-CoA* Production
R 9 = max { R 9 , max ⋅ S S + K S ⋅ [ 1 − ( f P H A f P H A , max ) α ] , 2 3 ⋅ R 10 } MathType@MTEF@5@5@+=feaagaart1ev2aaatCvAUfKttLearuWrP9MDH5MBPbIqV92AaeXatLxBI9gBaebbnrfifHhDYfgasaacPC6xNi=xH8viVGI8Gi=hEeeu0xXdbba9frFj0xb9qqpG0dXdb9aspeI8k8fiI+fsY=rqGqVepae9pg0db9vqaiVgFr0xfr=xfr=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@65EA@
R 10 : Propionyl-CoA* Production
R 10 = R 10 , max ⋅ S S + K S ⋅ [ 1 − ( f P H A f P H A , max ) α ] MathType@MTEF@5@5@+=feaagaart1ev2aaatCvAUfKttLearuWrP9MDH5MBPbIqV92AaeXatLxBI9gBaebbnrfifHhDYfgasaacPC6xNi=xH8viVGI8Gi=hEeeu0xXdbba9frFj0xb9qqpG0dXdb9aspeI8k8fiI+fsY=rqGqVepae9pg0db9vqaiVgFr0xfr=xfr=xc9adbaqaaeGaciGaaiaabeqaaeqabiWaaaGcbaGaemOuai1aaSbaaSqaaiabigdaXiabicdaWaqabaGccqGH9aqpcqWGsbGudaWgaaWcbaGaeGymaeJaeGimaaJaeiilaWIagiyBa0MaeiyyaeMaeiiEaGhabeaakiabgwSixNqbaoaalaaabaGaem4uamfabaGaem4uamLaey4kaSIaem4saS0aaSbaaeaacqWGtbWuaeqaaaaacqGHflY1daWadaqaaiabigdaXiabgkHiTmaabmaabaWaaSaaaeaacqWGMbGzdaWgaaqaaiabdcfaqjabdIeaijabdgeabbqabaaabaGaemOzay2aaSbaaeaacqWGqbaucqWGibascqWGbbqqcqGGSaalcyGGTbqBcqGGHbqycqGG4baEaeqaaaaaaiaawIcacaGLPaaadaahaaqabeaacqaHXoqyaaaacaGLBbGaayzxaaaaaa@58F9@