ES2542601T3 - Mezcla combustible e inflamable utilizado como sustituto de los combustibles fósiles en centrales termoeléctricas, hornos industriales y de calefacción central - Google Patents

Mezcla combustible e inflamable utilizado como sustituto de los combustibles fósiles en centrales termoeléctricas, hornos industriales y de calefacción central Download PDF

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ES2542601T3
ES2542601T3 ES10779034.7T ES10779034T ES2542601T3 ES 2542601 T3 ES2542601 T3 ES 2542601T3 ES 10779034 T ES10779034 T ES 10779034T ES 2542601 T3 ES2542601 T3 ES 2542601T3
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combustible
substitute
flammable mixture
solid
fossil fuels
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Drago Cosic
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COR BREVIS doo
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    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/10—Treating solid fuels to improve their combustion by using additives
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
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Abstract

La mezcla inflamable, que consiste en las fases sólida y líquida, caracterizada en que la fase sólida comprende: polvo de aluminio; al menos un M1X2, donde M1 puede ser cualquier metal en estado de oxidación +2, y X cualquier halógeno; M2CO3, donde M2 puede ser cualquier metal en estado de oxidación +2; cloruro de zinc y amonio; SiO2; y cal viva; y la fase líquida comprende: al menos un ácido carboxílico C1 a C6, o al menos un anhídrido de los dichos ácidos carboxílicos, o al menos un éster o amida suyos; metilcelulosa; y formaldehído, es decir, su solución disponible comercialmente - formol; y agua, donde la proporción de fase sólida en la mezcla varía entre 32 % p/p y 46 % p/p, y el de la fase líquida entre 54 % p/p y 68 % p/p, mientras que los componentes de la fase sólida están presentes en los siguientes porcentajes en peso: polvo de aluminio 3 % a 10 % M1X2 1 % a 4 % M2CO3 1 % a 3 % cloruro de zinc y amonio 2 % a 5 % SiO2 3 % a 8 % cal viva 70 % a 90 %, y los componentes de la fase líquida están presentes en los siguientes porcentajes en peso de: al menos un ácido carboxílico, o al menos un anhídrido de ácido carboxílico, o al menos un éster o amida suyos 10 % a 27 %; metilcelulosa 20 % - 40 %; formaldehído, 1 % a 10 %; y el resto hasta el 100 % es agua.

Description

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E10779034
14-07-2015
invención, se genera hidrógeno no solo dentro del combustible sino, también, mediante la reacción de gasificación del vapor de agua. Responsable de la generación de hidrógeno mediante la reacción de gasificación del vapor de agua es el agua del combustible, es decir, la mezcla inflamable, y la humedad del carbón.
5 La potencia calorífica inferior del carbón varía desde los 29310 kJ/kg de la antracita a los 12250 kJ/kg del lignito. En términos de potencia calorífica, para sustituir el 50 % de masa de carbón, calculados sobre 1000 kg de base, son necesarios 1250 Nm³ de hidrógeno para el lignito y 521 Nm³ para la antracita. Convertidos a masa,
10 son 110 kg de hidrógeno para la antracita y 42,7 kg de hidrógeno para el lignito.
Por consiguiente, 1000 kg de antracita producen tanto calor como 500 kg de antracita enriquecida con 110 kg de hidrógeno o, en el segundo caso, 500 kg de lignito enriquecidos con 42,7 kg de hidrógeno. En otras palabras, 8 porcentajes en 15 peso del combustible inventado sustituyen aproximadamente al menos a 50 porcentajes en peso de carbón. Además, suponiendo que, por su composición la antracita tiene un 100 % de carbón, la relación carbón/ hidrógeno para una mezcla de 500 kg de carbón y 110 kg de hidrógeno equivale a C:H = 1:1,32. La relación carbón vs. hidrógeno es uno de los índices básicos energético y medioambiental. 20 Para el gas natural esta proporción C:H = 1:4, para el petróleo C:H = 1:2. A este respecto, cuanto mayor es la proporción de carbono, más perjudicial es el impacto medioambiental, porque se producen mayores cantidades de anhídrido carbónico por la combustión. Esto es por lo que la mezcla inflamable, o el combustible acorde a la Invención se preparan de una forma para reducir los riesgos medioambientales
25 basada en la reacción listada en 12 anterior.

Claims (1)

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ES10779034.7T 2010-09-08 2010-09-08 Mezcla combustible e inflamable utilizado como sustituto de los combustibles fósiles en centrales termoeléctricas, hornos industriales y de calefacción central Active ES2542601T3 (es)

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PCT/HR2010/000031 WO2012032363A1 (en) 2010-09-08 2010-09-08 Fuel and combustible mixture used as a substitute for fossil fuels in thermoelectric power plants, industrial and central heating furnaces

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US (1) US20130167761A1 (es)
EP (1) EP2614130B1 (es)
JP (1) JP2013538904A (es)
KR (1) KR20130107294A (es)
CN (1) CN103119138A (es)
AP (1) AP2013006792A0 (es)
AU (1) AU2010360471A1 (es)
BR (1) BR112013005477A2 (es)
CA (1) CA2808790A1 (es)
CU (1) CU20130032A7 (es)
EA (1) EA023454B1 (es)
EC (1) ECSP13012479A (es)
ES (1) ES2542601T3 (es)
MA (1) MA34594B1 (es)
ME (1) ME02168B (es)
MX (1) MX2013002540A (es)
PL (1) PL2614130T3 (es)
RS (1) RS54134B1 (es)
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TN (1) TN2013000072A1 (es)
UA (1) UA107033C2 (es)
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EP2826703B1 (en) 2013-06-14 2015-11-04 Mehmet Nevres Ülgen A modular underwater foil for a marine vessel
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AP2013006792A0 (en) 2013-04-30
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EP2614130A1 (en) 2013-07-17
SG187939A1 (en) 2013-03-28
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ECSP13012479A (es) 2013-04-30
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EP2614130B1 (en) 2015-04-15
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