Process and equipment for producing synthesis gas from biomass
A process for producing synthesis gas (S) from biomass, includes drying the biomass and gasifying the biomass. An equipment to carry out the process is also disclosed. The process further includes: subjecting the outgoing gases (CO 2 , N 2 and H 2 O) from the gasifying step to a first heat exchange, where the outgoing gases (CO 2 , N 2 and H 2 O) are cooled, purifying the outgoing gases (CO 2 , N 2 and H 2 O) to achieve a process gas (P), the purification being effected by eliminating nitrogen (N 2 ) from the outgoing gases (CO 2 , N 2 and H 2 O), subjecting the process gas (P) to heat exchange, where the process gas (P) is heated, reducing the process gas (P) to synthesis gas (S), subjecting the synthesis gas (S) to heat exchange, where the synthesis gas (S) is cooled and supply air to the gasification is heated.
1. A process for producing synthesis gas (S) from biomass, said process comprising a drying step, a pyrolysis step and a combustion step, and further comprising:
subjecting outgoing gases comprising CO 2 , N 2 and H 2 O from the combustion step to heat exchange, where the outgoing gases are cooled,
purifying the cooled outgoing gases to achieve a process gas (P), by separating and removing nitrogen (N 2 ) from the outgoing gases,
subjecting the process gas (P) to heat exchange, where the process gas (P) is heated,
reducing the process gas (P) to synthesis gas (S), and
subjecting the synthesis gas (S) to heat exchange, where the synthesis gas (S) is cooled.
2. The process according to claim 1 , wherein the cooling of the outgoing gases and the heating of the process gas (P) are effected in a common heat exchange step.
3. The process according to claim 1 , wherein the cooling of the outgoing gases by heat exchange is effected in two separate steps.
4. The process according to claim 1 , wherein the separated nitrogen gas (N 2 ) is used to dry the biomass.
5. The process according to claim 1 , wherein reducing the process gas (P) to synthesis gas (S) is effected in a series of at least two reduction steps.
6. The process according to claim 5 , wherein, in a first of the at least two reduction steps, a reaction with coked fuel from the pyrolysis and combustion steps is initiated, and said coked fuel has participated in previous reduction steps.
7. The process according to claim 1 , wherein reducing the process gas (P) to synthesis gas (S) is effected in a single step.
8. The process according to claim 1 , wherein the synthesis gas (S) comprises H 2 and CO.
9. A process for producing synthesis gas (S) from biomass, comprising:
drying the biomass;
pyrolyzing and combusting the dried biomass to produce a coked fuel and combustion gases of CO 2 , N 2 and H 2 O;
subjecting the combustion gases to a heat exchange to cool the combustion gases;
separating the N 2 gas from the cooled combustion gases to produce N 2 gas and a process gas (P) comprising of CO 2 and H 2 O;
subjecting the process gas (P) to a heat exchange to heat the process gas;
subjecting the heated process gas (P) to one or more reduction step to produce the synthesis gas (S) comprising H 2 and CO.
10. The process according to claim 9 , wherein the one or more reduction step comprises reacting the process gas (P) with the coked fuel, to reduce the process gas (P) comprising CO 2 and H 2 O to the synthesis gas (S) comprising H 2 and CO.
11. The process according to claim 9 , further comprising cooling the synthesis gas (S).
12. The process according to claim 9 , wherein the heat exchange used to cool the combustion gases is also a same heat exchange used to heat the process gases.
13. The process according to claim 9 , wherein the biomass is dried with the separated N 2 gas that is produced when separating the N 2 gas from the cooled combustion gases.
14. The process according to claim 9 , wherein the one or more reduction step is a single reduction step.
15. The process according to claim 9 , wherein the synthesis gas (S) comprises less than 1% CO 2 and less than 7% N 2 .
16. The process according to claim 9 , wherein the synthesis gas (S) comprises 48% H 2 and 44% CO.
17. The process according to claim 1 , wherein the synthesis gas (S) comprises less than 1% CO 2 and less than 7% N 2 .
18. The process according to claim 1 , wherein the synthesis gas (S) comprises 48% H 2 and 44% CO.