2. Interim results Generic Approach Interim results

3. Goal Copyright Longer timeframe - Current state of technology as benchmark - BUT MAIN GOAL: Develop NEW process flow diagrammes (PFDs), two main reasons

4. Current processes (bioprocesses and conventional): State-of-the-art Future bioprocesses  Horizon value for productivity  Concentration glucose  Scale PFDs - Principle considerations (1/2)

5. Future separation processes  Only continuous fermentation processes  Plant size: Assume TODAY  FUTURE  Wherever possible, avoidance of energy intensive processes (e.g., distillation and evaporation); on the other hand relatively high fuel requirements may be acceptable in view of the use of renewable energy from biowaste streams.  Membrane processes are generally preferred due to their (expected) low energy use and the avoidance of high salt loads.  The avoidance of salt loads also makes electrodialysis an attractive option for the future. The high power requirements are considered acceptable in view of on-site electricity production from biowaste streams.  Extraction should be avoided, wherever possible. Alternatively, benign solvents should be used. Properties of compounds and process design determine energy use.  Adsorption may be somewhat less attractive due to common use of solvents for regeneration. PFDs - Principle considerations (2/2)

6. Overview of schemes O:\BREW\WPs\WP2(TechnoEcon)\Generic_approach\Separation\MassBalances\ TO_DO__MASS-BAL.xls FOR EXCEL VERSION WITH LIST OF SCHEMES TO BE REVIEWED BY EACH PARTNER SEE: Workpackages -> WP2 -> Overview of generic mass balance schemes

7. Overview of key data O:\WPs\WP2(TechnoEcon)\Generic_approach\Separation\MassBalances\CPY_1.xls THIS VERSION NOW UPDATED. SEE: Workpackages -> WP2 -> Overview of Key data (CORRECTED VERSION, 24. Sept 2004)

8. ABE

9. ABE (1/7): ABE_TODAY_1_(Distillation)

10. ABE (2/7): ABE_TODAY_2_(GasStripping)

11. ABE (3/7): ABE_FUTURE_1_(DistMembDist)

12. ABE (4/7): ABE_FUTURE_2_(MembDistDist)

13. ABE (5/7): ABE_FUTURE_3_(Pervaporation)

14. ABE (6/7): ABE_FUTURE_4_(RO)

15. ABE (7/7): ABE_FUTURE_5_(ADS)

16. Acetic acid

17. Ethanol

18. PDO

19. PDO (1/3): PDO_TODAY_1_(Evap)

20. PDO (2/3): PDO_FUTURE_1_(Pervap)

21. PDO (3/3): PDO_FUTURE_2_(HyphobMembr)

22. Acetic acid

23. Ac.acid (1/5): AceticAc_TODAY_1_(Extraction)

24. Ac.acid (2/5): AceticAc_TODAY_2_(Evap&Dist)

25. Ac.acid (3/5): AceticAc_FUTURE_1_(Extraction)

26. Ac.acid (4/5): AceticAc_FUTUR_2_(Evap&Dist)

27. Ac.acid (5/5): AceticAc_FUTURE_3_(ED)

28. Lactic acid

29. LA (1/4): LA_FUTURE_1_(Electrodialysis)

30. LA (2/4): LA_FUTURE_2_(Extraction)

31. LA (3/4): LA_FUTURE_3_(SRIlowpH)

32. LA (4/4): LA_FUTURE_4_(Adsorption)

33. Adipic acid

34. Ad.ac (1/5): AdipAc_TODAY_1_(Cryst)

35. Ad.ac (2/5): AdipAc_FUTURE_1_(Cryst)

36. Ad.ac (3/5): AdipAc_FUTURE_2_(Electrodialys)

37. Ad.ac (4/5): AdipAc_TODAY_1_(Solvent)

38. Ad.ac (5/5): AdipAc_TODAY_1_(Ester+Distill)

39. Succinic acid

40. Succ.ac (1/4): SA_TODAY_1_(Cryst)

41. Succ.ac (2/4): SA_TODAY_2_(1stageED)

42. Succ.ac (3/4): SA_FUTURE_1_(Cryst)

43. Succ.ac (4/4): SA_FUTURE_2_(2stageED)

44. Citric acid

45. Caprolactam (1/1): CL_FUTURE_1_GEN

46. Lysine (1/2): Lysine_TODAY (IonExch)

47. Lysine (2/2): Lysine_FUTURE_1_(ADS) For Lysine_FUTURE_1_(ADS): Is it realistic to assume that Ultrafiltration can be skipped before adsorption (Degussa patent)?

48. PHA (1/2): PHA_TODAY_1_(Extraction)

49. PHA (2/2): PHA_FUTURE_1_(Extraction)

50. Technology frontiers (“How long is the string?“)  Membrane: f(polarity) see e.g. PDO and LA  Electrodialysis: i) 2-stage ii) NF + WS-ED iii) 1-stage  Extracellular PHA  [(Bio-based) Syngas as feedstock ]  (Bio-based) Methanol as feedstock  Biotechnological methanol

51. Products selection O:\BREW\WPs\WP2(TechnoEcon)\CostData\Prices\PriceBREWproducts_1.xls

52. Collection of energy data  …jump to Shortcut to GenericEnergy_1.xls

53. O:\WPs\WP2(TechnoEcon)\Generic_approach\Separation\Chai nCompar\&[File] Generic Approach - Comparative energy analysis (1/3)

54. O:\WPs\WP2(TechnoEcon)\Generic_appro ach\Separation\ChainCompar\&[File] Generic Approach - Comparative energy analysis (2/3)

55. O:\WPs\WP2(TechnoEcon)\Generic_ approach\Separation\ChainCompar\ &[File] Generic Approach - Comparative energy analysis (3/3)

56. O:\WPs\WP2(TechnoE con)\Generic_approach \Separation\ChainCom par\&[File] Calibrated energy data for the Generic Approach

57. Interim results Additional slides Interim results

58. Prices of sugar from sugarcane (reproduction with kind permission from Tim Nisbet, Shell)  CHECK WITH TIM NISBET WHETHER USE IS OK DISCUSS: TAKE ONE SINGLE PRICE FOR SUGARS TODAY OR DISTINGUISH BETWEEN ORIGINS (SUGARCANE ETC? Assumed prices of fermentable sugar in Europe (NREL, 2002) L:\BioBasedMat_Lit\feedstocks\sugars\Sugar_price\ Updated Sugar Price.xls

59. L:\BioBasedMat_Lit\feedstocks\sugars\Sugar_ cane\Sugarcane_feedstock_A_2.xls\Sheet Definition NREU and REU Energy use and GHG emissions of sugar cane use AVERAGE (medium sucrose content)

60. L:\BioBasedMat_Lit\feedstocks\sugars\ Sugar_cane\Sugarcane_feedstock_B_ 2.xls\Sheet Definition NREU and REU Energy use and GHG emissions of sugar cane use ADVANCED (high sucrose content)

61. L:\BioBasedMat_Lit\feedstocks\sugars\ Sugar_cane\Sugarcane_feedstock_A_ 2.xls\Sheet Definition NREU and REU