The invention relates to a low-pressure
methanol synthesizing process. In the low-pressure
methanol synthesizing process, both a primary reactor and a secondary reactor adopt a boiler feed water forced circulating
heat transfer technology,
heat transfer is fast and efficient, the device
layout can be effectively simplified, the project investment of a device frame is reduced, and the problems of circulating ratio decrease, a non-ideal
heat effect and the like, which are caused by inaccurate calculation of the
layout height of a steam pocket, do not appear; through
forced circulation, the circulating ratio can be effectively increased, reaction heat can be efficiently and reasonably utilized, and the
heat transfer effect is enhanced; a
jumper wire is arranged between an outlet of a synthetic
gas compressor and an inlet of the secondary reactor, so that stable operation of catalysts in the two stages of reactors in different stages of the service life is achieved, and through the
jumper wire, loads of the reactors are conveniently and forcibly adjusted, so that the production ratio of medium-pressure steam to low-pressure steam is flexibly adjusted; a connection position of fresh synthetic gas is arranged behind a synthetic gas
thermostat, so that the heat transfer area and the specification of the synthetic gas
thermostat can be reduced and the project investment is reduced.