Toyo's DME Process Toyo's DME Process
Toyo's DME Process Toyo's DME Process
Toyo's DME Process Toyo's DME Process
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Field of Activities - 2TEC <strong>DME</strong>Total Solution Provider : EPC Solution BusinessINDUSTRIAL SYSTEMS• Pharmaceuticals• Food & Beverage• Fine Chemicals• Electronics & Semiconductor• Overseas Expansion Support© 2005 TOYO ENGINEERING CORPORATION 5Field of Activities - 3TEC <strong>DME</strong>Total Solution Provider : e-Solution BusinessINFORMATION TECHNOLOGY ERP: Enterprise Resource Planning WMS: Warehouse Management System SCM: Supply Chain Management MES: Manufacturing Execution System CRM: Customer Relationship Management© 2005 TOYO ENGINEERING CORPORATION 6
Why <strong>DME</strong> ?In Japan,TEC <strong>DME</strong>© 2005 TOYO ENGINEERING CORPORATION 9Why <strong>DME</strong> ? TEC <strong>DME</strong>© 2005 TOYO ENGINEERING CORPORATION 10
Why <strong>DME</strong> ?TEC <strong>DME</strong>© 2005 TOYO ENGINEERING CORPORATION 11Why <strong>DME</strong> ?TEC <strong>DME</strong>Why do you need <strong>DME</strong> ?© 2005 TOYO ENGINEERING CORPORATION 12
Direct Synthesis Route (Typical)TEC <strong>DME</strong>CO 2Recycle gasPurge gas<strong>DME</strong>H2/CO=1NGREF<strong>DME</strong>SYNCO 2REMOVALOxygenAirASUMeOHWaterN 2© 2005 TOYO ENGINEERING CORPORATION 15Feature of Direct Synthesis (Typical)TEC <strong>DME</strong>• Syn Gas Requirement H 2/CO=1==> Large O2 consumption• CO 2Removal (and Recycle)• High heat generation in <strong>DME</strong> synthesis reaction‣ No Commercial Experience‣ JFE Pilot Plant in Japan (100 t/d)© 2005 TOYO ENGINEERING CORPORATION 16
Methanol Dehydration RouteTEC <strong>DME</strong>Reaction:kJ/molMeOH -1 CO + 2 H 2= CH 3OH (90.3)MeOH -2 CO 2+ 3 H 2= CH 3OH + H 2O (49.4)--------------------------------------------------------------------------MeOH De-H 2O 2CH 3OH = CH 3OCH 3+ H 2O (23.4)© 2005 TOYO ENGINEERING CORPORATION 17TEC <strong>DME</strong><strong>DME</strong> Production by Methanol DehydrationCombination of Methanol and <strong>DME</strong> SynthesisRecycle gasPurge gasMeOH<strong>DME</strong>NGREFMeOHSYN<strong>DME</strong>SYNWaterMethanol Plant<strong>DME</strong> Synthesis Plant© 2005 TOYO ENGINEERING CORPORATION 18
Features of Methanol DehydrationTEC <strong>DME</strong>• Combination with well-proven MeOH technology• No Oxygen required ( ≤ 3,500 t/d)• No CO 2produced in <strong>DME</strong> Synthesis• Any Ratio (0~100%) between MeOH and <strong>DME</strong>© 2005 TOYO ENGINEERING CORPORATION 19Features of Methanol DehydrationTEC <strong>DME</strong>(continued)•Commercially proven Scheme and <strong>DME</strong> catalystLutianhua <strong>DME</strong> Plant in China started in 2003•Simple Scheme for <strong>DME</strong> Synthesis‣ Less Total Investment Cost‣ Easy to Scale-up with Proven Technologies ofLarge Scale MeOH© 2005 TOYO ENGINEERING CORPORATION 20
TEC <strong>DME</strong>Background of TOYO’s s <strong>DME</strong> TechnologyFeedback of <strong>DME</strong> existing plant know-how• 3,000 t/y for chemical with ten years operation• 10,000 t/y at Lutianhua in China (started in 2003)Own Technologies applied• High active steam reforming catalyst (ISOP)• Steam reforming technology (42 units)• Methanol converterMRF-Z ® )Scale-up technology applied based on TOYO’sJumbo Methanol Plant• Development of a Jumbo <strong>DME</strong> Plant© 2005 TOYO ENGINEERING CORPORATION 23TOYO’s s ISOP Catalyst(ISOP : Innovative Steam reforming Optimized <strong>Process</strong>)TEC <strong>DME</strong>ServiceActivitySteam reforming(steam reformer, adiabatic reformer,reformer exchanger)4 times higher than conventional catalystAdvantage tube skin temperature decreasedtube number decreasedExperience more than 4 years in commercial plantSupplierSüd Chemie Group G90-ISOP© 2005 TOYO ENGINEERING CORPORATION 24
TOYO’s s Steam ReformerTEC <strong>DME</strong> Down-Firing Box TypeNaphtha Steam Reformer for90 MMSCFD Hydrogen Plant,Ssangyong Oil Refining Co., Ltd.,Korea (1995)Largest Capacity inHydrogen Plant based onNaphtha FeedstockTOYO’s experiences :Total 42 units© 2005 TOYO ENGINEERING CORPORATION 25TOYO’s s MRF-Z ® Methanol ReactorTEC <strong>DME</strong>MRF-Z ® : Multi-stage indirect cooling Radial Flow & its temp. profile Z• A single train for 6,000 t/d Methanol• M.P steam generation by reaction heat recovery• Small catalyst volume due to optimization oftemperature profile in the reactor• Small pressure drop of the reactor due to radial flowcatalystMRF-Z ® estimated size(Corresponding to <strong>DME</strong> 3,500 t/d)I.D.:T-T :5,100 mm18,440 mmNo. of Shell : Only One© 2005 TOYO ENGINEERING CORPORATION 26
MethanolTEC <strong>DME</strong>Typical Flow Scheme of <strong>DME</strong> SynthesisFuel Gas<strong>DME</strong> ReactorCWCWSTMProduct<strong>DME</strong> TankSTMSTMSTMCWMethanol requirement for <strong>DME</strong> productionapprox. 1.4 ton-MeOH / ton-<strong>DME</strong>CWWater© 2005 TOYO ENGINEERING CORPORATION 27TEC <strong>DME</strong>TOYO’s s Jumbo <strong>DME</strong> Plant from Natural GasCombination of Methanol and <strong>DME</strong> SynthesisRecycle gasPurge gasMeOH<strong>DME</strong>NGREFMeOHSYN<strong>DME</strong>SYNWaterMethanol Plant<strong>DME</strong> Synthesis Plant© 2005 TOYO ENGINEERING CORPORATION 28
Features of Jumbo <strong>DME</strong> <strong>Process</strong>TEC <strong>DME</strong>Methanol Dehydration Route• Scheme and <strong>DME</strong> catalyst commercially provenLutianhua <strong>DME</strong> Plant in China started in 2003• Any ratio (0~100%) of methanol and <strong>DME</strong> can beproduced• <strong>DME</strong> synthesis is very simple and investment costis less• Minimum train concept can be applied• Oxygen(O 2 ) is not required (for ≤ 3,500 t/d)• Less total investment cost• CO 2 is not produced in <strong>DME</strong> synthesis© 2005 TOYO ENGINEERING CORPORATION 29TEC <strong>DME</strong>Syn. Gas Preparation & Methanol SynthesisFor <strong>DME</strong> 3,500 t/d(MeOH 5,000 t/d)STKSTEAMREFOMERBFWMRF-ZSTMIDFSSHAIRFDFDSCWCWSYNSYNLOOPNGSTMADIABATICREFORMERHEATRECCOMPCRUDEMeOHNo oxygen required with TOYO’s ISOP Catalyst© 2005 TOYO ENGINEERING CORPORATION 30
<strong>DME</strong> Synthesis & DistillationTEC <strong>DME</strong>Fuel gasFuel Gas<strong>DME</strong> Reactor<strong>DME</strong>ColumnMethanolColumnChillingUnit<strong>DME</strong>TankWaterCrudeMethanol© 2005 TOYO ENGINEERING CORPORATION 31TEC <strong>DME</strong>Performance of Jumbo <strong>DME</strong> Plant (typical)Capacity : 3,500 t/d including Utility & OffsiteNatural Gas : 163 mmSCFD(182,000Nm 3 /h)Raw WaterRequired Area<strong>Process</strong> & UtilityStorage <strong>DME</strong>: 8 m 3 /t-<strong>DME</strong> (1,150 m 3 /h)approx. 15 ha: 400 m x 250 m: 300 m x 120 m© 2005 TOYO ENGINEERING CORPORATION 32
TEC <strong>DME</strong>Syn. Gas Preparation & Methanol SynthesisFor <strong>DME</strong> 7,000 t/d(MeOH 10,000 t/d)MRF-Z ®O 2SteamReformerO2ReformerSTMIDFAIRDE-SCWSYN. GASCOMPRESSORCWTRAIN “A”SYN LOOPNGH-RECSTMAdiabatic ReformerTRAIN “B”SYN LOOPCRUDEMeOH© 2005 TOYO ENGINEERING CORPORATION 33TEC <strong>DME</strong>Performance of TOYO’s s Jumbo <strong>DME</strong> Plant (typical)Capacity : 7,000 t/d including Utility & OffsiteNatural Gas : 305 MMSCFDR.W: 6.2 m 3 /t-<strong>DME</strong> (1,800 m 3 /H)Required Area ( Total ~ 20 ha )<strong>Process</strong> & UtilityStorage <strong>DME</strong>: 505 m x 310 m: 360 m x 140 m© 2005 TOYO ENGINEERING CORPORATION 34
SummaryTEC <strong>DME</strong>• <strong>DME</strong> Production <strong>Process</strong>es- Direct Synthesis Route- Methanol Dehydration Route (TOYO)• TOYO’s <strong>DME</strong> <strong>Process</strong> Background- Own technologies applied- Already commercialized in China• A Jumbo <strong>DME</strong> Plant- Technically feasible based on commerciallyproven technologies- Total investment cost is less© 2005 TOYO ENGINEERING CORPORATION 35TEC <strong>DME</strong>Thank you very muchfor your attention !URL : http:/www.toyo-eng.co.jp© 2005 TOYO ENGINEERING CORPORATION 36