| 摘要 |
<p>Bio formula 100 production process as an alternative material to substitute diesel fuel, essentially covers the following distillation stages: - refinery of oil waste originated from palm coconut through distillation - the end-product proceeds into R1 reactor while adding methanol and sulphuric acid - the result is put in E1 evaporator, - the result is being proceeded into D1 distillation column to be distilled - methanol distillation result is retained in TB1 bait tank and proceeded into R3 tank, at the same time NaOH/KOH is included, - then to have WVO flow in (oil waste of fruits/palm coconut) which have been evaporated in E1 and reserved in PR1 (Pre Reactor Reserved), mixed and put into the R2A and R2B (Main Reactor CSTR) through M1 together with the mixture result of R3 - the result of R2A and P2B is then proceeded into PR2 (Pre Reactor Reserved), - then is proceeded into D2 distillation column for continued process in D1 so that D1 input becomes two that is D2 and E1 , and hereafter distilled as in D1 initial stage - the bottom/liquid fraction, in the form of (glycerol + soap + methyl ester) through the reboiler, in liquid condition, is recovered/withdrawn through D3 distillation column, retained in TB2 Glycerol reserved tank, - at D3 distillation column, the top/vapour fraction, in the form of methanol through the condenser, in liquid condition is proceeded to TB2, methyl ester/biodiesel is proceeded into R4 Reactor, - at R4 neutralizing reactor being neutralized by adding sulphuric acid from TB3 tank (the sulphuric acid bait tank) and water from TB4 water reserve tank, processed as the second catalyst, which then being evaporated in E2, - the evaporation result, the top fraction consisting of water + soap + salt is retained in TB5 Dirty Water Reserved Tank, and the bottom fraction in the form of biodiesel 100 (futher-on called as Biodiesel B-100 being the substitution of diesel fuel) is reserved in the Biodiesel B-100 Product Tank.</p> |
