BE358043A - - Google Patents
Info
- Publication number
- BE358043A BE358043A BE358043DA BE358043A BE 358043 A BE358043 A BE 358043A BE 358043D A BE358043D A BE 358043DA BE 358043 A BE358043 A BE 358043A
- Authority
- BE
- Belgium
- Prior art keywords
- ashes
- gasifier
- ash
- desc
- gas
- Prior art date
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 13
- 239000002956 ash Substances 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 12
- 235000002918 Fraxinus excelsior Nutrition 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 6
- 239000001569 carbon dioxide Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 150000004679 hydroxides Chemical class 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 239000004449 solid propellant Substances 0.000 claims description 4
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 3
- 238000002309 gasification Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 150000003464 sulfur compounds Chemical class 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 2
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 239000003513 alkali Substances 0.000 claims 2
- 239000003795 chemical substances by application Substances 0.000 claims 2
- 230000008030 elimination Effects 0.000 claims 2
- 238000003379 elimination reaction Methods 0.000 claims 2
- 230000001376 precipitating effect Effects 0.000 claims 2
- 229910002090 carbon oxide Inorganic materials 0.000 claims 1
- 239000000446 fuel Substances 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 238000002360 preparation method Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J1/00—Production of fuel gases by carburetting air or other gases without pyrolysis
- C10J1/207—Carburetting by pyrolysis of solid carbonaceous material in a fuel bed
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Industrial Gases (AREA)
Description
<Desc/Clms Page number 1>
Méthode pour la production de gaz à haute teneur en oxyde de carbone moyennant classification de combustibles solides.
On sait qu'en gazéifiant des combustibles solides avec de l'oxygène mélangé . de la vapeur 8'eau ou bien à de l' anhy- dride carbonique on peut obtenir des gaz très riches en o xy- de de carbone qui peuvent être utilement employés soit pour la production de certains composés organiques oxygénés( tels que le méthamal et autres produits semblables), soit po ur la production d'hydrogène ou de mélanges d'azcte-hydrogène convenables pour la synthèse de l'ammoniaque, soit aussi comme gaz combustibles, en vue du haut pouvoir calorifique qu'ils possèdent.
La marche des gazogènes employés dans 1a gazéification
<Desc/Clms Page number 2>
dont mention ci-dessus, présente en pratique quelques diffi- cultés, tant dans le cas où l'on emploie des gazogènes dans lesquels les cendres sont déchargées en forme de scorie soli- de, que lorsque les cendres sont déchargées à l'état de masse fondue.
Ces difficultés dépendent dans le cas de la scorie solide de sorties de flammes ou d'entrées d'air pendant l'opé- ration d'élimination des cendres, opération qui comporte donc la nécessité de suspendre la marche du gazogène et dans le cas de gazogènes à fusion des cendres, du fait que les maté- riaux réfractaires qui entrent en contact avec les cendres tondues, bien qu'ils soient choisis de qualité spéciale, tôt ou tard se détériorent rendant ainsi nécessaire leur substi- tution.
Or on a trouvé que, si dans un gazogène pour la gazéifica- tion d'un combustible solide moyennant injection d'oxygène et de vapeur d'eau, und'oxygène et d' anhydride carbonique on a soin que la composition et la vitesse des gaz injectés soient telles que la combustion puisse avoir lieu d'une façon très vive et rapide, et par conséquent à haute température, les cendres subissent une transformation chimiquequi empêche qu'elles s'agglomèrent, et de cette façon elles peuvent être obtenues sous forme d'une poudre très fine, qui est emportée par les gaz sortant du gazogène même.
Dans ces conditions les composés des métaux alcalins et alcaline-terreux contenus dans les cendres sont transformés en les oxydes ou hydroxydes correspondants, et par conséquent, en lavant dans l'eau les gaz sortant du gazogène de manière qu'ils soient refroidis convenablement, cette eau dissout les ditsoxydes et hydroxydes et fixe complètement ou presque l'annydride carbonique et les composés du soufre que les gaz mêmes peuvent contenir.
**ATTENTION** fin du champ DESC peut contenir debut de CLMS **.
<Desc / Clms Page number 1>
Method for the production of gas with a high carbon monoxide content by classification of solid fuels.
It is known that by gasifying solid fuels with mixed oxygen. from water vapor or carbon dioxide it is possible to obtain gases very rich in carbon dioxide which can be usefully employed either for the production of certain oxygenated organic compounds (such as methamal and other similar products), either for the production of hydrogen or azct-hydrogen mixtures suitable for the synthesis of ammonia, or also as fuel gases, in view of the high calorific value they possess.
The progress of gasifiers used in gasification
<Desc / Clms Page number 2>
mentioned above, presents some difficulties in practice, both in the case where gasifiers are used in which the ashes are discharged in the form of solid slag, and when the ashes are discharged in the state of melt.
These difficulties depend in the case of the solid slag from the outlets of flames or the inlets of air during the ash removal operation, an operation which therefore involves the need to suspend the operation of the gasifier and in the case of Ash-melting gasifiers, since the refractory materials which come into contact with the sheared ash, although they are chosen of special quality, sooner or later deteriorate making their replacement necessary.
Now it has been found that, if in a gasifier for the gasification of a solid fuel by injecting oxygen and water vapor, oxygen and carbon dioxide, care must be taken that the composition and the speed of the injected gases are such that the combustion can take place in a very lively and rapid manner, and consequently at high temperature, the ashes undergo a chemical transformation which prevents their agglomeration, and in this way they can be obtained in the form of a very fine powder, which is carried away by the gases leaving the gasifier itself.
Under these conditions the compounds of the alkali metals and alkaline earth metals contained in the ashes are transformed into the corresponding oxides or hydroxides, and consequently, by washing the gases leaving the gasifier in water so that they are suitably cooled, this water dissolves the so-called oxides and hydroxides and completely or almost completely fixes carbon dioxide and sulfur compounds that the gases themselves may contain.
** ATTENTION ** end of DESC field can contain start of CLMS **.
Claims (1)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BE358043A true BE358043A (en) |
Family
ID=31826
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BE358043D BE358043A (en) |
Country Status (1)
| Country | Link |
|---|---|
| BE (1) | BE358043A (en) |
-
0
- BE BE358043D patent/BE358043A/fr unknown
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