In this work

a model of hydrogen production by double chemical looping is introduced. The efficiency benefit obtained was investigated. The chemical looping hydrogen generation unit is connected in series to the downstream of a chemical looping gasification unit as an additional system for 100 MW·h coal gasification

with the function of supplementary combustion to produce hydrogen. Using Aspen Plus software for process simulation

the production of H

2

and N

2

in the series system is higher than that in the independent Chemical looping gasification and Chemical looping hydrogen generation systems

and the production of hydrogen is approximately 25.63% and 12.90% higher

respectively; The study found that when the gasification temperature is 900℃

steam-carbon ratio is 0.84 and oxygen-carbon ratio is 1.5

the hydrogen production rate of the system was the maximum. At the same time

through heat exchange between logistics

high-pressure steam at 8.010×10

4

kg·h

-1

and medium-pressure steam at 1.101×10

4

kg·h

-1

are generated

and utility consumption is reduced by 61.58%

with utility costs decreasing by 48.69%. An economic estimati

on study found that the production cost of ammonia is 108.66 USD·(t NH

3

)

-1

. Finally

cost of equipment is the main factors influencing ammonia production cost were proposed by sensitivity analysis.