NOVELTY - The aromatization of methanol involves hydrocarbon synthesis and separation steps, where hydrocarbon synthesis involves connecting at least two reactors mutually in series with each other, adding catalyst to a starting end of reactor, after reaction entering into a regenerator for regeneration, heating methanol after adding into leading end of reactor, using the reaction product as raw material for subsequent reactor, and using the reaction product of reactor as a heat exchange medium.    USE - Aromatization of methanol and cogeneration of liquefied gas using high efficient heat integrated type moving bed reactor (claimed).    ADVANTAGE - The method enables aromatization of methanol, increases the refining process, achieves the effective use and integration between the raw materials, increases the product yield, and reduces the energy consumption and environmental pollution.    DETAILED DESCRIPTION - The aromatization of methanol and cogeneration of liquefied gas using high efficient heat integrated type moving bed reactor involves hydrocarbon synthesis and separation steps, where hydrocarbon synthesis involves connecting at least two reactors mutually in series with each other, adding catalyst to a starting end of reactor, after reaction entering into a regenerator for regeneration, returning to beginning of the reactor, heating methanol after adding into leading end of reactor, using the reaction product as a raw material for subsequent reactor, adding the reaction product of the second reactor as a raw material into the end reactor, where the reactor is a moving bed radial reactor, using the reaction product of reactor as a heat exchange medium, using methyl alcohol as raw material for heat exchange, processing methyl alcohol raw material, where the reactor comprises starting reactor and end reactor, dividing the reaction product of end reactor into strands, heating at least one stream for methanol feedstock to the end of the reaction product of reactor for temperature control through the flow into the reactor from the beginning to change the stock of reaction products, and control the reaction temperature at the beginning to end of the reactor, separating the reaction products into three-phase at the end of the stock exchange with reactor after cooling by gas water three-phase separation device, separating the aqueous portion and sending to oil-containing sewage processing device, separating the obtained oil phase to depentanizer to partially remove pentane and extracting 6-10C aromatic hydrocarbon product, performing gas phase separation for compressing the gas by a circulation gas compressor, returning to the hydrocarbon synthesis step after heating the raw material and removing the small portion of circulation gas to liquefied gas fractionation extraction tower to extract 3-4C liquid gas product.