ORGANIC CHEMICAL SYNTHESES ON MARS Robert J. Milligan 4Frontiers 10th Annual International Mars Society Convention August 31, 2007 DIFFERENCES • Mars has no Coal, no Oil, no Biomass. • The Only Readily Available Source of Carbon Available on Mars is its CO2 Atmosphere. • This, Along with Electrolysis of Water to Provide Hydrogen, Proves to be Entirely Adequate for Our Needs. Aug 31, ‘07 © 4Frontiers Corporation SYNGAS PREPARATION • Syngas is created by the Incomplete Burning of Methane. It is Comprised of Water, Carbon Monoxide, Carbon Dioxide, Hydrogen and Unreacted Methane. Water-Gas Shift: CO + H2O Aug 31, ‘07 CO2 + H2 © 4Frontiers Corporation METHANOL SYNTHESIS • It was Found That Carbon Dioxide and Hydrogen are the only Constituents in Syngas to form Methanol. CO2 + 3H2 Cu CH3OH + H2O • The Reaction is Simply a Reduction of Carbon Dioxide Over a Copper Catalyst. Aug 31, ‘07 © 4Frontiers Corporation METHANOL SYNTHESIS ON MARS CH3OH CO2 Cu, ZnO, 250oC, 50 - 100 bar H2 electrolysis Martian Atmosphere O2 Aug 31, ‘07 © 4Frontiers Corporation + H2O other processes MTO REACTION • The Principal Industrial use for Methanol on Earth is as a Precursor for Polyethylene. • This Reaction is Called the MTO (Methanol to Olefins) Reaction. Depending on the Zeolite Catalyst Used, a Range of Olefins can be Built. The Catalyst of Choice for our Purposes Prepares C2C4 Alkenes (Ethene, Propene, Butenes) in 90% Yield. Most of the Remaining is Carbon Soot. This has to be Burned Out Periodically to Renew the Catalyst. Aug 31, ‘07 © 4Frontiers Corporation METHANOL TO OLEFIN (MTO) REACTION 40% CH3OH methanol 350-550oC, 1 to 3 bar, gage CH2=CH2 ethene 40% CH2=CHCH3 propene MTO-100 Zeolite Catalyst 10% CH3CH2CH=CH2 1 and 2 -butene CH3CH=CHCH3 Aug 31, ‘07 © 4Frontiers Corporation DISTILLATION • The Ethene, Propene and the Butenes have to be Separated From Each Other. • In Addition Enough 1-Butene has to be Separated From the Mixed Butenes to Provide Branching for the Polyethylenes. 1- Butene Fraction can be Subsequently Passed Through a Preparative GLC Column to Remove Traces of Trans 2-Butene. The Remainder can be Hydrolyzed to 2-Butanone and/or Hydrogenated to Butane a Precursor to Maleic Anhydride. Both are Needed for Polyester Synthesis. Aug 31, ‘07 © 4Frontiers Corporation SCHEMATIC FOR SEPARATING OLEFINS ethene 2 propene butenes heavies 1. 2. Aug 31, ‘07 1 alkenes Compressor Distillation Columns © 4Frontiers Corporation MTO SCHEMATIC FOR ISOLATION OF 1-BUTENE 1-butene butane 1. 2. Aug 31, ‘07 H2 heavies 2 1 Compressor Distillation Columns © 4Frontiers Corporation butenes POLYETHYLENE • Besides Ethene, Polyethylene Synthesis Requires 1-Butene, a Zieglar-Natta Catalyst and is done in an Isobutane Solvent. The Zieglar-Natta Catalyst will be Brought From Earth. The Isobutane will be Prepared From Carbon Monoxide (CO) and H2 by What is Known as Isosynthesis. Aug 31, ‘07 © 4Frontiers Corporation ISOSYNTHESIS (CH3)3CH (CH3)2C=CH2 CO ZrO2, > 400oC, 50 - 150 bar H2 electrolysis Martian Atmosphere or other source O2 Aug 31, ‘07 © 4Frontiers Corporation + H2O other processes SOME COMMENTS ON ISOSYNTHESIS • Isosynthesis has Two Drawbacks. It Does Not Provide a Clean Yield. The Products have to be Distilled and the Isobutene has to be Hydrogenated. The Water-Gas Shift (Above) Works Against the Reaction. It is Found that the CO2 Produced Collects on the Catalyst Retarding the Reaction. An Alternative is Cracking Butane. Aug 31, ‘07 © 4Frontiers Corporation POLYETHYLENE SYNTHESIS • Continuous Loop Process Reactants have to be Free of Water, Alcohols, Carbon Dioxide and Sulfur Compounds as they Adversely Affect the Zieglar-Natta Catalyst. Pressure is 40 Bar. Temperature is Kept Below 130ºC. The Polyethylene is Isolated as Particulate and the Isobutane is Flashed off to be Collected for a Future Run. Aug 31, ‘07 © 4Frontiers Corporation ALIPHATIC SYNTHESES FROM METHANOL Ag CH2-CH2 O oxirane CH2=CH2 ethene CO2 cat. 3b. CO O O CH2CH2 CH3OH cat. 3c. HOCH2CH2OH + CH3OCOOCH3 dihydroxyethane dimethyl carbonate To ethylbenzene To polyethylene To cumene H2 CO2 + CO MTO CH3OH methanol CH3CH=CH2 propene Cl2 CH2ClCH=CH2 3-chloropropene LEGEND: polycarbonate and polyester polyester epoxy resin polyethylene Aug 31, ‘07 Cl2, H2O CaO HOAc ClCH2CHOHCH2Cl glycerol dichlorohydrin As co-reactant for LDPE H2 CH3CH2CH=CH2 + CH3CH=CHCH3 1 and 2-butenes CH3CH2CH2CH3 butane 7/2O2, 400 - 480oC 0.3 - 0.4 Mpa H2O, H2SO4 Cu D CH3CH2CHOHCH3 8b. 2-butanol © 4Frontiers Corporation CH3CH2COCH3 2-butanone, MEK CaO O O=C C=O CH=CH maleic anhydride H2S2O8 CH2-CHCH2Cl O epichlorohydrin CH3CH2 CH3 HOOCOOCOOH CH3 CH2CH3 MEKPO dimer OTHER SYNTHESES • In Addition to Polyethylene, We have Devised Synthesis Routes to: Polyester Epoxy Resin Polycarbonate • Polycarbonate is Needed for Greenhouse Windows Once it Became Apparent that Large Quantities of Useable Silica are not Immediately Available on Mars. Aug 31, ‘07 © 4Frontiers Corporation POLYCARBONATE SYNTHESIS • The Polycarbonate in Question is Based on Bisphenol-A. This is also the backbone for the epoxy resin so the synthesis will be shared. Preparation goes back to CO2 Aug 31, ‘07 © 4Frontiers Corporation BENZENE FROM CO2 9H2 400ºC 6CO2 + 24H2 [6CH4] Sabatier Ru, 4bars 12H2O CO2 700ºC Mo, Zeolite METAMARS 15H2 15H2O + electrolysis 7.5O2 3H2O O2 Aug 31, ‘07 H2O © 4Frontiers Corporation Benzene CUMENE Benzene + 30 bar, 250oC Zeolite catalyst Cumene (2-Propylbenzene) CH3CH=CH2 Aug 31, ‘07 © 4Frontiers Corporation PHENOL Phenol 1-10 bar., O2 [Cumene Hydro Cumene (2-Phenylpropane) 82 - 90oC, -peroxide (CHP)] radical initiator Ca. 30% 60-70oC H+, H20 + Acetone Vacuum distill unreacted cumene Weak caustic scrub to remove phenol, acids Aug 31, ‘07 © 4Frontiers Corporation BISPHENOL - A Phenol Ion exchange resin Excess + CH3COCH3 CH3COCH3 Aug 31, ‘07 Bisphenol A H2O © 4Frontiers Corporation OXIRANE (ETHYLENE OXIDE, EO) CO2 CH2=CH2 O2, 200-250oC Ag/Al2O3, 10 to 30 bar CH2-CH2 O EO MTO Aug 31, ‘07 © 4Frontiers Corporation 1,3-DIOXOLAN-2-ONE (ETHYLENE CARBONATE, EC) CO2 + CH2-CH2 O 100ºC, 50 bar O-CO-O EC 3:1 CO2:EO ratio Aug 31, ‘07 CH2-CH2 © 4Frontiers Corporation DIMETHYL CARBONATE (DMC) To polyester CH2-CH2 HOCH2CH2OH O-CO-O 1+ bar, 90ºC excess TiSiO4 matrix K2CO3 CH3OH + CH3OCO2CH3 DMC Aug 31, ‘07 © 4Frontiers Corporation POLY[2,2-PROPANEBIS(4-PHENYL CARBONATE)] CH3 CH3 -OH + (CH3O)2CO DMC HO- 1-3 bar 90ºC O- CH3 Bisphenol A Aug 31, ‘07 © 4Frontiers Corporation -OCO CH3 + 2CH3OH n REFERENCES D. J. O’Rear and N. Branc accio, “Gas-to-Liquid CO2 Reduc tion by Use of H2 as a Fuel”, US patent 6,890,962 , (to Chevron U SA, Inc. ), May 10, 2005. A.Frei, “Lurgi Megamethano lR Techno logy”, Chap t 7.1, in R. A. Mey ers, ed., Handbook of Petroche mi cals Produc tion Processes, Part 7, Methano l, 2005. K. Hadidi, “Methano l Produc tion from Syn Gas”, http:/ /www.n rel. gov/do cs/fy04os ti/ 34929.pd f P. R. Pujado and J. M. Ande rsen, “UO P/Hyd ro MTO Process”, Chap t 10.2, in R. A. Meyer s, ed., Handbook of Petrochemicals Produc tion Processes, Part 10, Propylene and Ligh t Olefins, McGraw-Hill, 2005. M. Smit h, “Chevron– Philli ps Slurry-Loop-Reactor Process fo r Polymerizing Linea r Polyethylene” , Chap t 14.3, in R . A. Meye rs, ed., Handbook o f Petroche mi cals Produc tion Processes, Part 14, Polyethylene, McGraw-Hill , 2005. A.C. Muscatell o, R. Zubrin, M, Bergg ren and B. Birnb aum, “Final Report for Methane to Aromatics on Mars (METAMARS), NAS 10-01003 Pionee r Astronau tics, Aug. 16, 2001. G. A. Peterson and R. J. Schmi dt, UOP Q-MaxTM Process”, Chap t 4.2, in R. A. Mey ers, ed., Handbook of Petrochemic als Produc tion Processes, Part 4, Cumene, McGraw-Hill , 2005. Aug 31, ‘07 © 4Frontiers Corporation R. J. Schmi dt, Sunoco /UOP Pheno l Process”, Chap t 9.2, in R . A. Meye rs, ed., Handbook of Petroche micals Produc tion Processes, Part 9, Pheno ls and Acetone, McGraw-Hill , 2005. E. J. Pressman, e t. al. “Process for Recove ring B is pheno ls”, U.S. 5,723,689 (to Gene ral Electric Co., Schenec tady NY), Mar. 3, 1996. E. Fraini, D. West and G. Mign in, “QBISTM Process fo r High- Purity Bis pheno l A”, Chap t 9.4, in R . A. Meye rs, ed., Handbook of Petrochemi cals Production Processes, Part 9, Pheno ls and Acetone , McGraw-Hill, 2005 J. S. Buchanan , L. C. DeCaul and H-K C. Tim ken, “Heterogeneous Ca talysts for Ethy le ne Carbonate Produc tion”, \abstracts\O_111.pdf T. Tatsumi, Y. Wartanabe and K. A. Koyano, “ Synthes is of Dim ethyl Carbona te from Ethy le ne Carbonate and M ethanol us ing TS-1 as Soli d Base Catalyst”, Chemic al Comm unications, 1996, 2281 Frank Crossman and Robert Milli gan , Polymer Synthes is & Manu facturing Systems, Proc. 8th Mars Soc. Conf . (2005) Aug 31, ‘07 © 4Frontiers Corporation