METHOD AND APPARATUS FOR GASIFYING RAW MATERIAL AND GASEOUS PRODUCT
20170313951 · 2017-11-02
Assignee
Inventors
Cpc classification
C10J3/66
CHEMISTRY; METALLURGY
International classification
Abstract
A method and apparatus for gasifying raw material. The method includes feeding the raw material into an upper part of a fixed-bed gasifier, introducing the raw material from the upper part of the gasifier to a pyrolysis zone of the gasifier to form the fixed-bed and pyrolyzing the raw material in the presence of pyrolysis air to form a pyrolysis product. Introducing the pyrolysis product from the pyrolysis zone to a lower part of the gasifier, introducing primary air countercurrently to the lower part, carrying out a final gasification in a lower part of the gasifier in order to form a gasified gas. Introducing the gasified gas to a catalytic oxidation part and through a catalyst layer of the catalytic oxidation part, and reforming the gasified gas by way of the catalytic oxidation in the presence of reforming air in the catalytic oxidation part, forming a gaseous product.
Claims
1. A method for gasifying raw material, wherein the method comprises: feeding the raw material into an upper part of a fixed-bed gasifier, introducing the raw material from the upper part of the gasifier to a pyrolysis zone of the gasifier to form the fixed-bed in the pyrolysis zone and pyrolyzing the raw material in the presence of pyrolysis air in the pyrolysis zone to form a pyrolysis product, introducing the pyrolysis product from the pyrolysis zone to a lower part of the gasifier, introducing primary air countercurrently to the lower part, carrying out a final gasification in a lower part of the gasifier in order to form a gasified gas, introducing the gasified gas to a catalytic oxidation part and through a catalyst layer of the catalytic oxidation part, and reforming the gasified gas by way of the catalytic oxidation in the presence of reforming air in the catalytic oxidation part, in order to form a gaseous product.
2. The method according to claim 1, wherein temperature of the catalyst layer is between 600 to 900° C.
3. The method according to claim 1, wherein temperature of the gasified gas is between 400 to 600° C. before the catalytic oxidation part.
4. The method according to claim 1, wherein the fixed bed is pressed for compacting the bed.
5. The method according to claim 1, wherein the fixed bed is agitated by a rotating grate.
6. The method according to claim 1, wherein the reforming air is introduced just before the catalytic oxidation part.
7. The method according to claim 1, wherein the raw material is selected from the group consisting of wood containing material, biomass based material, organic material and their combinations.
8. An apparatus for gasifying raw material, wherein the apparatus comprises a fixed-bed gasifier which comprises an upper part, pyrolysis zone in a middle part of the gasifier and lower part, and catalytic oxidation part, at least one feeding device for feeding the raw material into the upper part of the gasifier from which the raw material is introduced to the pyrolysis zone to form the fixed-bed in the pyrolysis zone, the fixed-bed in the pyrolysis zone in which the raw material is pyrolyzed in the presence of pyrolysis air for forming a pyrolysis product which is introduced to the lower part, a first air feeding equipment for introducing the pyrolysis air to the pyrolysis zone, a second air feeding equipment for introducing primary air countercurrently to the lower part, gas introducing equipment for introducing a gasified gas formed by a final gasification in the lower part to the catalytic oxidation part, a third air feeding equipment for introducing re-forming air for the catalytic oxidation, and a catalyst layer in the catalytic oxidation part through which the gasified gas is led and in which the gasified gas is reformed by means of the catalytic oxidation and in the presence of the reforming air in order to form a gaseous product.
9. The apparatus according to claim 8, wherein the apparatus comprises at least one temperature adjustment device for adjusting temperature before the catalytic oxidation part.
10. The apparatus according to claim 8, wherein the apparatus comprises a mechanical bed pressing device for pressing the bed.
11. The apparatus according to claim 8, wherein the catalytic oxidation part is arranged to surround the pyrolysis zone.
12. The apparatus according to claim 8, wherein the apparatus comprises a rotating grate for agitating the fixed bed.
13. A gaseous product, wherein the gaseous product with low-tar content is formed by the method of claim 1.
Description
LIST OF FIGURES
[0035] In the following section, the invention will be described with the aid of detailed exemplary embodiments, referring to the accompanying figure wherein
[0036]
DETAILED DESCRIPTION OF THE INVENTION
[0037]
EXAMPLE 1
[0038] The apparatus of
[0039] Further, the apparatus comprises a bed tightening device (13) which is piston type device for pressing and tightening the bed. A bottom ash (14) can be removed from the apparatus from the bottom of the apparatus.
[0040] The devices used in this invention are known per se, and therefore they are not described in any more detail in this context.
EXAMPLE 2
[0041] In this test, the catalytic oxidation and its efficiency were studied in laboratory scale. The wood gasification gas was introduced to the catalytic oxidation device in which the gasification gas was treated according to the invention. Compositions of the gasified gas before the catalytic oxidation and the gaseous product after the catalytic oxidation are represented in table 1.
TABLE-US-00001 TABLE 1 Gaseous product Gasified gas prior after catalytic catalytic oxidation oxidation Gas components CO, vol-% 19.3 12.3 CO.sub.2, vol-% 7.8 13.6 H.sub.2, vol-% 8 13.7 CH.sub.4, vol-% 2.8 2.4 C.sub.2-C.sub.5, vol-% 2.5 1.5 H.sub.2O, vol-% 23.7 17 N.sub.2, vol-% 35.9 39.5 Higher hydrocarbon content, mg/m.sup.3n (dry gas) benzene 4690 2020 tars < naphthalene 2910 20 naphthalene 1080 50 tars > naphthalene 1065 <10
[0042] It was observed that residue tars can be oxidated and decomposed during the catalytic oxidation.
[0043] The method and apparatus according to the invention are suitable in different embodiments for gasifying different kinds of raw material. The method and apparatus according to the invention are suitable in different embodiments for forming different kinds of low-tar products.
[0044] The invention is not limited merely to the examples referred to above; instead many variations are possible within the scope of the inventive idea defined by the claims.