• Chloromethanes are produced from methane by chlorination route.
Process Technology
Chloromethanes namely methyl chloride (CH3Cl), methylene chloride (CH3Cl2), Chloroform (CHCl3) and Carbon Tetrachloride (CCl4) are produced by direct chlorination of Cl2 in a gas phase reaction without any catalyst.
Reactions
CH4 + Cl2 → CH3Cl + HCl
CH3Cl + Cl2 → CH2Cl2 + HCl
CH2Cl2 + Cl2 → CHCl3 + HCl
CHCl3 + H2 → CCl4 + HCl
CH4 + Cl2 → CH3Cl + HCl
CH3Cl + Cl2 → CH2Cl2 + HCl
CH2Cl2 + Cl2 → CHCl3 + HCl
CHCl3 + H2 → CCl4 + HCl
- • The reactions are very exothermic.
• The feed molar ratio affects the product distribution. When CH4/Cl2 is about 1.8, then more CH3Cl is produced. On the other hand, when CH4 is chosen as a limiting reactant, more of CCl4 is produced. Therefore, depending upon the product demand, the feed ratio is adjusted.
Process Technology
- • Methane and Cl2 are mixed and sent to a furnace
• The furnace has a jacket or shell and tube system to accommodate feed pre-heating to desired furnace inlet temperature (about 280 – 300°C).
• To control temperature, N2 is used as a diluent at times.
• Depending on the product distribution desired, the CH4/Cl2 ratio is chosen.
• The product gases enter an integrated heat exchanger that receives separated CH4 (or a mixture of CH4 + N2) and gets cooled from the furnace exit temperature (about 400°C).
• Eventually, the mixture enters an absorber where water is used as an absorbent and water absorbs the HCl to produce 32 % HCl.
• The trace amounts of HCl in the vapour phase are removed in a neutralizer fed with NaOH
• The gas eventually is compressed and sent to a partial condenser followed with a phase separator. The phase separator produces two streams namely a liquid stream consisting of the chlorides and the unreacted CH4/N2.
• The gaseous product enters a dryer to remove H2O from the vapour stream using 98% H2SO4 as the absorbent for water from the vapour.
• The chloromethanes enter a distillation sequence. The distillation sequence consists of columns that sequentially separate CH3Cl, CH2Cl2, CHCl3 and CCl4.
Figure. Flowsheet of Chloromethane production