The method of synthesis of methanol from carbon monoxide and hydrogen was developed in 1913 and subsequently improved.
Today, the original gas for the synthesis of methanol is obtained as a result of the conversion (transformation) of hydrocarbon raw materials: natural gas, coke oven gas, liquid hydrocarbons (oil, fuel oil, light catalytic cracking) and solid fuels (coal, shale).
The original gas for the synthesis of methanol is obtained from almost all types of raw materials that are used in the production of hydrogen for the synthesis of ammonia. In addition, both technological schemes use similar processes and devices, so the production of methanol is often combined with the production of ammonia. Examples of such a mixed production is JSC Nevinnomyssky Azot, located in Nevinnomyssk (Stavropol Territory) and NPO Azot in Novomoskovsk.
The use of zinc-copper catalysts allows the synthesis of methanol at a temperature and pressure of MPa.The main stages of methanol production:- obtaining a mixture of carbon monoxide and hydrogen (synthesis gas);
- obtaining a raw methyl alcohol;
- Isolation and purification of methyl alcohol (rectification).
As in the production of ammonia, the principle of circulation is used in the synthesis of methanol. The synthesis gas purified from sulfur compounds is processed in a compressor and heated to the required temperature in exchanger. Then the synthesis gas enters the column with catalyst.
The mixture heated as a result of the exothermic reaction exits the synthesis column and cooled by a heat exchanger, giving its heat to the synthesis gas. The cooled reaction mixture is then sent to the refrigerator, enters the separator, in which methanol is condensed and collected in a receiver (collector). The unreacted synthesis gas is returned to the technological process. The use of the circulation principle helps to significantly increase the yield of methanol.