Difference between revisions of "Basic mevalonate pathway model with limonene synthesis: Construction and Ensemble analysis"

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(Kinetic parameters)
(Determining growth curve parameters)
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== Parameters ==
 
== Parameters ==
 
=== Determining growth curve parameters ===
 
=== Determining growth curve parameters ===
[[File:MVA_v16_growthcurve.png|thumb|400px|left|none|alt=Alt text|'''Fig. 3:''' Growth curve parameters were predicted from using the logistic equation. Table shows the initial and predicted parameters from this fitting ]]
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[[File:MVA_v16_growthcurve.png|thumb|500px|left|none|alt=Alt text|'''Fig. 3:''' Growth curve parameters were predicted from using the logistic equation. Table shows the initial and predicted parameters from this fitting ]]
  
 
To identify the growth curve parameters required to simulate the cell growth, we’ve fitted the experimental OD<sub>600</sub> readings onto a logistic growth curve ('''Fig. 3'''). We have tried to fit with a more complex Baranyi (ref) growth with a lag-phase. Doing so gave a better fit however a test using Akaike Information Criterion (AIC) indicates that a less complex model is better; so we chose to proceed using this logistic growth curve to model the MVA pathway.
 
To identify the growth curve parameters required to simulate the cell growth, we’ve fitted the experimental OD<sub>600</sub> readings onto a logistic growth curve ('''Fig. 3'''). We have tried to fit with a more complex Baranyi (ref) growth with a lag-phase. Doing so gave a better fit however a test using Akaike Information Criterion (AIC) indicates that a less complex model is better; so we chose to proceed using this logistic growth curve to model the MVA pathway.

Revision as of 11:43, 8 February 2018

This model serves as the preliminary MVA pathway framework that we have used as the foundation to debug and design improved MVA models. Although basic, this model was able to provide useful insights into the control of the MVA pathway and suggests strategies for possible engineering. The ensemble analysis carried out for this model have generated a total 8 model generations that have shown a significant improvement in their model scores after each reiteration. A step-by-step ensemble analysis that included scoring the models based on experimental data and identifying influential parameters have found that the proteins that are influential to the pathway are LIMS, MDC, GPPS and IDI. The analysis was also able to shed light on product inhibitions in the pathway that would influence the production of limonene, and also suggests an possible topological engineering design that could accelerate the pathway even more.


The simulation

Alt text
Fig. 1: Overview of the basic MVA model simulation
Alt text
Fig. 2: (Top) Plasmid used in our experiment, and (bottom) plasmid used in Weaver et. al. Right plot shows the measured OD readings in our experiment, with induction at timepoint 0 when cell cultures reached OD=0.75

Experiment

This simulation is based on an experiment on the DH10B strain of E. coli cell cultures that produces limonene that are sequestered into an organic layer. Brief description of the experimental method is as follows:

    • -The DH10B strain of E. coli was transformed with the limonene production plasmid pJBEI6410.
    • -Three 60 ml cultures (A, B and C), inoculated from individual colonies, were grown in flasks at 30 oC in a shaker incubator.
  • -When cultures reached OD600 of 0.75 they were split into multiple 5 ml aliquots and 1 ml of dodecane overlay was added (timepoint zero). At this point some samples were Induced by the addition of IPTG (25 uM final concentration), other samples were left Uninduced. In addition controls were set-up with limonene added (500 ug/L) to one aliquot of each culture.
  • -All cultures were then incubated at 30 oC in a shaker incubator until the designated timepoints.
  • -At each timepoint (0, 2, 4, 8, 24 hr) samples were removed, OD600 was measured, the dodecane overlay was recovered for limonene quantification, and total RNA was prepared (but no RNAseq was performed on the 24hr samples as RNA quality was too low). The limonene control samples were analysed only at the 8 hr timepoint. The protein fraction of each sample was recovered and stored at -80oC.
  • -The total RNA samples were treated to deplete ribosomal RNA (rRNA) and RNA integrity (RIN values) were determined for each sample prior to sending them for RNAseq

In silico simulation

To simulate the experiment described above, the model was simulated for 72 hours and E. coli was grown until OD_{600}= 5. For each model generation (iteration) 5000 ensemble models were generated, which means for each iteration, 5000 values were sampled from each distribution to describe the ensemble models. The concentration for input metabolites such as Acetyl coA along with the reductants (NADP, NADPH) and energy metabolites (ATP, ADP) were made constant in the model. The values for these concentrations were based on measured absolute concentrations in E. coli from (ref1=Park2006). The enzyme concentration in this model is also fixed, with the concentration values based on measured intercellular concentrations from (ref2=Weaver 2015). In that study, intercellular concentrations of enzymes of the bottom mevalonate pathway with amorphadiene (A different type of terpene) synthesis were measured, and these genes were from pbMIS plasmid that uses a the pTrc promoter for all of its bottom mevalonate pathway genes. This differs that what is used in our experiment in two ways: 1) We study limonene synthesis instead of amorphadiene; and 2) Our experiment used pjBEI-6410 plasmid that used pLac promoter for the upstream pathway genes, pTrc promoter for the bottom mevalonate pathway genes including for limonene synthesis ( Fig. 2). Therefore, there is a high level of uncertainty for the concentrations used for the enzymes in the pathway, especially for LIMS and GPPS (Fig. 1).

Parameters

Determining growth curve parameters

Alt text
Fig. 3: Growth curve parameters were predicted from using the logistic equation. Table shows the initial and predicted parameters from this fitting

To identify the growth curve parameters required to simulate the cell growth, we’ve fitted the experimental OD600 readings onto a logistic growth curve (Fig. 3). We have tried to fit with a more complex Baranyi (ref) growth with a lag-phase. Doing so gave a better fit however a test using Akaike Information Criterion (AIC) indicates that a less complex model is better; so we chose to proceed using this logistic growth curve to model the MVA pathway.

Kinetic parameters

Alt text
Fig. 4: Heterologous mevalonate pathway with limonene synthesis with the source of genes highlighted in blue. The gene source is based on the genes in plasmid pjBEI-6410 (ref)

In this model, there is a total of 65 parameters. Table below lists the Mode, CI factor, mu and sigma used to generate the prior lognormal distributions used for its ensemble models.

index Reaction Parameter Mode CI mu sigma
1 AACT Keq_AACT 7.80E-06 5.4983 -10.8582 0.6059
2 AACT Km_acoa_AACT 333.3936 8.5216 6.522 0.8442
3 AACT Km_aacoa_AACT 26.4941 7.0054 3.8928 0.7848
4 AACT Km_coa_AACT 17.868 8.0717 3.5685 0.828
5 AACT Kcat_AACT 5.21E+03 41.8813 10.1562 1.2642
6 HMGS Keq_HMGS 6.27E+06 1.08E+02 17.8363 1.4783
7 HMGS Km_acoa_HMGS 16.8418 9.4143 3.587 0.8736
8 HMGS Km_aacoa_HMGS 1.325 8.9642 1.0196 0.8592
9 HMGS Km_hmgcoa_HMGS 16.8418 9.4143 3.587 0.8736
10 HMGS Km_coa_HMGS 1.325 8.9642 1.0196 0.8592
11 HMGS Kcat_HMGS 261.0095 4.1687 5.9424 0.6147
12 HMGR Keq_HMGR 0.0189 7.98E+02 -0.4531 1.8745
13 HMGR kcatF_HMGR 232.1936 2.7395 5.6588 0.4595
14 HMGR kcatR_HMGR 232.1936 2.7395 5.6588 0.4595
15 HMGR Km_hmgcoa_HMGR 11.6277 8.7446 3.179 0.8519
16 HMGR Km_nadph_HMGR 54.5006 5.1882 4.4728 0.6889
17 HMGR Km_mev_HMGR 667.918 4.9009 6.953 0.6699
18 HMGR Km_coa_HMGR 384.006 5.7179 6.4699 0.7206
19 HMGR Km_nadp_HMGR 578.749 4.9418 6.8134 0.6727
20 MK Keq_MK 5.00E+03 5.65E+04 15.1185 2.5691
21 MK Km_mev_MK 65.452 10.6482 5.0079 0.9092
22 MK Km_atp_MK 362.6772 10.7217 6.7237 0.9112
23 MK Km_mevp_MK 65.452 10.6482 5.0079 0.9092
24 MK Km_adp_MK 362.6772 10.7217 6.7237 0.9112
25 MK kcat_MK 1.81E+03 4.1609 7.8778 0.614
26 PMK Keq_PMK 8.5501 2.1771 2.2798 0.3659
27 PMK Km_mevp_PMK 25.393 3.6469 3.5563 0.5673
28 PMK Km_atp_PMK 67.5286 2.6683 4.4143 0.4491
29 PMK Km_mevpp_PMK 38.1145 3.3212 3.9247 0.533
30 PMK Km_adp_PMK 53.2536 3.215 4.2464 0.5209
31 PMK kcat_PMK 224.2657 2.8912 5.6437 0.4805
32 MDC Keq_MDC 4.18E+04 4.5814 11.0602 0.6472
33 MDC Km_mevpp_MDC 28.1891 5.1085 3.8064 0.6837
34 MDC Km_atp_MDC 77.174 5.1482 4.8171 0.6863
35 MDC Km_ipp_MDC 28.1891 5.1085 3.8064 0.6837
36 MDC Km_adp_MDC 77.174 5.1482 4.8171 0.6863
37 MDC Km_pi_MDC 77.174 5.1482 4.8171 0.6863
38 MDC Km_co2_MDC 77.174 5.1482 4.8171 0.6863
39 MDC kcatF_MDC 315.0646 2.0572 5.8695 0.3417
40 MDC kcatR_MDC 315.0646 2.0572 5.8695 0.3417
41 IDI Km_ipp_IDI 1.83E+01 7.57E+01 4.8659 1.4
42 IDI Km_dmapp_IDI 1.62E+01 8.84E+00 3.5183 0.8551
43 IDI Kcat_IDI 1.99E+03 5.18E+02 10.8126 1.794
44 IDI Keq_IDI 0.4801 14.3967 1.0219 0.9934
45 GPPS Km_dmapp_gpps 376.3912 7.8616 6.603 0.82
46 GPPS Km_ipp_gpps 7.4096 8.4234 2.7096 0.8407
47 GPPS Km_gpp_gpps 20.2782 6.4021 3.5821 0.7566
48 GPPS Km_pp_gpps 20.2782 6.4021 3.5821 0.7566
49 GPPS Kcat_gpps 80.9145 6.8878 5.001 0.7795
50 GPPS Keq_GPPS 3.46E+09 1.80E+04 27.71 2.4
51 LIMS Km_gpp_LIMS 376.3912 7.8616 3.1693 1.0857
52 LIMS Km_lim_LIMS 376.3912 7.8616 3.1693 1.0857
53 LIMS Km_pp_LIMS 376.3912 7.8616 3.1693 1.0857
54 LIMS Kcat_LIMS 376.3912 7.8616 1.5742 1.0982
55 LIMS Keq_LIMS 376.3912 7.8616 49.7827 1.9157
56 constant m_coa 1370 15.4949 8.2494 1.0133
57 constant m_ATP 9630 1.1842 9.1797 0.0842
58 constant m_ADP 555 1.2692 6.333 0.1184
59 constant m_NADP 2.86 15.6513 2.0831 1.016
60 constant m_NADPH 121 1.1037 4.7982 0.0493
61 constant m_pi 23900 1.25 10.0939 0.1109
62 constant m_ppi 23900 1.25 10.0939 0.1109
63 constant m_co2 75.2 1.2503 4.3325 0.111
64 constant m_acoa 606 1.1454 15.6218 0.0677
65 diffusion rate D 23900 1.25 21.2956 0.7565

Acknowledgements

Special thanks to Dr. Christopher Robinson from the SynBioChem Centre University of Manchester for carrying out the experiment and supplying all of the OD readings and limonene titers for this simulation.