The invention discloses a process for gasification production of synthesis gas through a low temperature entrained-flow
bed by using ultrafine
powder. The process comprises the steps: spraying an ultrafine gasified
raw material which is pulverized to less than 75 [mu]m and a gasification agent into a gasification furnace from the top of the gasification furnace of the entrained-flow
bed, performing a reaction on the gasified
raw material and the gasification agent so as to generate the synthesis gas containing
carbon monoxide and
hydrogen at a gasification temperature of lower than 1300 DEG C, spraying
chilled water during downward flow of the synthesis gas, and reducing the temperature of the gas so as to meet requirements for the entrance temperature of a
cyclone separator, wherein the entrance temperature of the
cyclone separator is generally lower than 900 DEG C; discharging the gas with ash
slag from a lower outlet of the gasification furnace after cooling, introducing the gas directly into the
cyclone separator, removing most of coarse particles and a part of fine ash which are carried by the gas, then introducing the obtained gas into a
waste heat boiler for further cooling of the gas, generating steam at the same time, finally introducing the gas into a filter so as to remove fine dust entrained in the gas, and sending the obtained gas to a subsequent section. In the gasification process, the ash
slag does not have to reach a melt flow state, and the process is particularly suitable for production processes of low-activity
coal and gasification of
coal with a high-ash fusion point.