[\/et_pb_fullwidth_header][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
\u00bfQu\u00e9 es la gasificaci\u00f3n del carb\u00f3n?<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row column_structure=”1_2,1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
La gasificaci\u00f3n del carb\u00f3n es la tecnolog\u00eda central de la industria qu\u00edmica del carb\u00f3n moderna.<\/strong><\/p>\nGasificaci\u00f3n de carb\u00f3n: se refiere a una reacci\u00f3n incompleta entre diversos tipos de carb\u00f3n (coque) y agentes gasificantes portadores de ox\u00edgeno (H\u2082O, O\u2082, CO\u2082) en un gasificador. A alta temperatura y presi\u00f3n, se produce gas de carb\u00f3n crudo compuesto de H\u2082, CH\u2083, CO\u2082, CO\u2082, N\u2082, trazas de H\u2082S, COS, etc.<\/p>\n
[\/et_pb_text][\/et_pb_column][et_pb_column type=”1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Clasificaci\u00f3n de los procesos de gasificaci\u00f3n del carb\u00f3n:<\/strong><\/p>\n\n- Materias primas: carb\u00f3n pulverizado, carb\u00f3n triturado, suspensi\u00f3n de agua y carb\u00f3n;<\/li>\n
- Lecho de gasificaci\u00f3n: lecho fluidizado, lecho fluidizado, lecho fijo;\n<\/li>\n
- El lecho fijo est\u00e1 hecho de carb\u00f3n en trozos (15-50 mm) como materia prima;<\/li>\n
- El lecho fluidizado est\u00e1 hecho de carb\u00f3n triturado (menos de 10 mm) como materia prima;<\/li>\n
- El lecho de flujo de aire est\u00e1 hecho de carb\u00f3n pulverizado (menos de 0,1 mm) como materia prima;\u00a0<\/li>\n<\/ul>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Coal-chemical-gasification-method.webp” alt=”Coal chemical gasification method” title_text=”0-Coal chemical gasification method” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Tabla de encuesta de componentes de gas crudo producidos por diferentes procesos de gasificaci\u00f3n<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Coal-chemical-gasification-method-2.webp” alt=”-Coal chemical gasification method ” title_text=”0-Coal chemical gasification method 2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
\u00bfQu\u00e9 es el lavado con metanol a baja temperatura?<\/strong><\/h2>\nProceso de lavado con metanol a baja temperatura: se utiliza metanol fr\u00edo como disolvente de absorci\u00f3n, aprovechando la alta solubilidad del metanol en gases \u00e1cidos a bajas temperaturas, para eliminar los gases \u00e1cidos del gas de alimentaci\u00f3n, principalmente CO2 y H2S.
El lavado con metanol a baja temperatura es un m\u00e9todo desarrollado conjuntamente por Linde y Lurgi a principios de la d\u00e9cada de 1950 para eliminar los gases \u00e1cidos de las materias primas. En 1954, se utiliz\u00f3 por primera vez para la purificaci\u00f3n de gases en la industria de la gasificaci\u00f3n presurizada de carb\u00f3n en Sud\u00e1frica.
<\/strong><\/p>\n <\/p>\n
\n- Los proveedores de paquetes de procesos de lavado con metanol a baja temperatura incluyen a Linde, Lurgi, Universidad Tecnol\u00f3gica de Dalian, etc.<\/li>\n
- Existen diversos procesos de gasificaci\u00f3n, que pueden dividirse en tres categor\u00edas: lecho fijo, lecho fluidizado y lecho fluidizado;<\/li>\n
- La determinaci\u00f3n de si el gas de baja emisi\u00f3n tiene valor de recuperaci\u00f3n de calor residual considera principalmente el contenido de CH4 en el gas de escape;<\/li>\n
- La concentraci\u00f3n de CH4 depende del proceso de gasificaci\u00f3n, y los procesos de gasificaci\u00f3n de lecho fijo incluyen el horno Lurgi, el horno BGL, etc.<\/li>\n<\/ul>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=\u201d1\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredeterminado\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredeterminado\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredeterminado\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredeterminado\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Propiedades de los gases residuales<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row column_structure=”1_3,2_3″ use_custom_gutter=”on” gutter_width=”2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”1_3″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Caracter\u00edsticas de los gases de escape del lavado con metanol a baja temperatura:<\/p>\n
\n- El gas de escape est\u00e1 b\u00e1sicamente saturado de vapor de agua.<\/li>\n
- Alto contenido de componentes inertes CO2 y N2<\/li>\n
- Los gases de escape b\u00e1sicamente no contienen ox\u00edgeno.<\/li>\n<\/ol>\n
[\/et_pb_text][\/et_pb_column][et_pb_column type=”2_3″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component.webp” alt=” waste gas component” title_text=”0 waste gas component” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Determinaci\u00f3n del volumen de aire de suplementaci\u00f3n de ox\u00edgeno<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row column_structure=”1_2,1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Debido a que los gases de escape casi no contienen ox\u00edgeno, es necesario complementarlos con aire para satisfacer los requisitos de ox\u00edgeno para la oxidaci\u00f3n completa de los gases de escape.
Principio para determinar la cantidad de aire suplementario:<\/p>\n
1) Consideraciones de seguridad: an\u00e1lisis de riesgo de explosi\u00f3n<\/strong><\/em><\/p>\nSeg\u00fan la Especificaci\u00f3n T\u00e9cnica para el Tratamiento de Gases de Residuos Org\u00e1nicos Industriales mediante el M\u00e9todo de Combusti\u00f3n con Almacenamiento T\u00e9rmico, la concentraci\u00f3n de materia org\u00e1nica que entra al dispositivo RTO debe ser inferior a 25% del LIE. Calcule el LIE de mezclas complejas de gases combustibles mediante la f\u00f3rmula de Le Chatlier y, a continuaci\u00f3n, compare la concentraci\u00f3n de componentes combustibles en los gases de escape con el LIE de 25% para determinar la seguridad de dicha concentraci\u00f3n.<\/p>\n
2) Consideraciones sobre la tasa de purificaci\u00f3n: \u201c3T1O\u201d<\/em><\/strong><\/p>\n[\/et_pb_text][\/et_pb_column][et_pb_column type=”1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-oxygen-supplementation-air-volume.webp” alt=”oxygen supplementation air volume” title_text=”0 oxygen supplementation air volume” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
\n- LM es el l\u00edmite explosivo inferior del gas mezclado, %<\/li>\n
- Li es el l\u00edmite explosivo inferior del componente i,%<\/li>\n
- Vi es la fracci\u00f3n de volumen de un determinado componente combustible con respecto al componente combustible,%<\/li>\n<\/ul>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Generalmente, en el dise\u00f1o, se ignora la influencia de los gases inertes. El l\u00edmite inferior de explosividad de los gases de escape se calcula y la relaci\u00f3n de diluci\u00f3n en aire se determina con base en la relaci\u00f3n entre la concentraci\u00f3n de gases de escape y el LIE de 25%. Este c\u00e1lculo puede garantizar la seguridad intr\u00ednseca, pero el volumen de gases de escape es relativamente grande.<\/p>\n
Debido a la presencia de una gran cantidad de gas inerte CO2 en el gas de escape de lavado con metanol a baja temperatura N2, una peque\u00f1a cantidad de componentes combustibles,
De acuerdo con el m\u00e9todo de c\u00e1lculo para una mezcla que contiene n gases inflamables y p gases inertes, se puede determinar que el gas de escape mixto de baja calidad de gases inflamables e inertes no es inflamable ni explosivo.<\/p>\n
Por lo tanto, los gases de escape del lavado con metanol a baja temperatura no tienen l\u00edmites explosivos superiores o inferiores.
La cantidad de reposici\u00f3n de aire para los gases residuales del lavado con metanol a baja temperatura se puede determinar en funci\u00f3n de que el contenido de ox\u00edgeno de los gases de combusti\u00f3n despu\u00e9s de la oxidaci\u00f3n completa sea mayor que 3%.<\/p>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” custom_margin=”|auto|14px|auto||” custom_padding=”||62px|||” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Proceso de c\u00e1lculo de la combustibilidad de gases de escape mixtos en el aire\u00a0<\/h3>\n
[\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-2.webp” alt=”waste gas component” title_text=”0 waste gas component 2″ align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-3.webp” alt=”waste gas component” title_text=”0 waste gas component 3″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][et_pb_row column_structure=”2_5,3_5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”2_5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
El gas de escape mixto est\u00e1 dise\u00f1ado para la suplementaci\u00f3n de ox\u00edgeno en funci\u00f3n del balance de materiales, con un contenido de ox\u00edgeno de alrededor de 5% en los gases de combusti\u00f3n.<\/p>\n
Comparaci\u00f3n entre la concentraci\u00f3n de componentes combustibles en los gases de escape despu\u00e9s de la suplementaci\u00f3n de ox\u00edgeno y el l\u00edmite explosivo inferior de los gases de escape (excluidos los gases inertes)<\/p>\n
<\/p>\n
Procesamiento del volumen total de aire<\/strong><\/h4>\n1) Bajo volumen de gases de escape<\/em><\/strong>
2) Volumen de aire de suplementaci\u00f3n de ox\u00edgeno<\/em><\/strong><\/p>\n[\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-5.webp” alt=”waste gas component” title_text=”0 waste gas component 5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][et_pb_column type=”3_5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-4.webp” alt=”waste gas component” title_text=”0 waste gas component 4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-2-1.webp” alt=”waste gas component” title_text=”0 waste gas component 2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” custom_margin=”|auto|17px|auto||” custom_padding=”||50px|||” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
\u2460 Balance de materiales<\/strong><\/h2>\n[\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Low-methane-waste-gas.webp” alt=”Low-methane waste gas” title_text=”0 Low-methane waste gas” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
\u00a0\u2461 Equilibrio t\u00e9rmico<\/strong><\/h2>\n[\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Heat-balance.webp” alt=”Heat balance” title_text=”0 Heat balance” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Casos t\u00edpicos de ingenier\u00eda<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
An\u00e1lisis de la situaci\u00f3n<\/h3>\n
La unidad de metanol de Xinye Energy Chemical, con una capacidad de 525.000 toneladas anuales, utiliza tecnolog\u00eda de gasificaci\u00f3n presurizada con carb\u00f3n triturado. Adem\u00e1s de los componentes principales, CO\u2082 y N\u2082, los gases de escape del lavado con metanol a baja temperatura tambi\u00e9n contienen metano, hidrocarburos totales no met\u00e1nicos, CO\u2082, metanol, etc. Estos gases de escape se descargan actualmente a trav\u00e9s de la chimenea de la caldera. De acuerdo con los requisitos de protecci\u00f3n ambiental, se requiere un tratamiento para la eliminaci\u00f3n de COV. Adem\u00e1s, la unidad de polioximetileno tambi\u00e9n tiene tres gases de escape que requieren tratamiento.<\/p>\n
[\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE.webp” alt=”RTO CASE” title_text=”0 RTO CASE” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Ruta del proceso<\/h3>\n
Con base en las caracter\u00edsticas de los componentes combustibles en los gases de escape, nuestros ingenieros han decidido adoptar la ruta de tecnolog\u00eda de tratamiento de \u201cpurificaci\u00f3n RTO + caldera de calor residual de vapor de presi\u00f3n media para recuperaci\u00f3n de calor\u201d; De acuerdo con el exclusivo \u201cAlgoritmo de distribuci\u00f3n de aire de seguridad de la teor\u00eda de correcci\u00f3n de gas inerte y Le Chater\u201d de nuestra empresa, hemos decidido seleccionar un RTO de v\u00e1lvula rotativa de volumen de aire de 270000, con un contenido de ox\u00edgeno de 5% en los gases de escape despu\u00e9s de la incineraci\u00f3n; Simult\u00e1neamente, seleccionar una caldera de vapor de 5,1 MPa\/46 T con un dise\u00f1o de chimenea final de 120 metros para reducir el impacto de las emisiones de escape en el entorno de la f\u00e1brica;<\/p>\n
[\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-1-1.webp” _builder_version=”4.27.4″ _module_preset=”default” alt=” RTO CASE” title_text=”0 RTO CASE 1″ hover_enabled=”0″ sticky_enabled=”0″][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n
El dispositivo principal adopta una \u00fanica v\u00e1lvula rotativa RTO de 270.000 vol\u00famenes de aire, de dise\u00f1o cuadrado, equipada con 3 v\u00e1lvulas rotativas de distribuci\u00f3n de aire y 36 c\u00e1maras de almacenamiento de calor.<\/p>\n
\n- Tratamiento integral:<\/strong>
Equipado con un RTO rotatorio de 270.000 vol\u00famenes de aire, gas de cola de polioximetileno mezclado con aire para suplementar ox\u00edgeno.
Aprovechamiento del calor residual: 46 t\/h, vapor saturado de 5,1 MPa
<\/strong><\/li>\n- Normas de protecci\u00f3n del medio ambiente:<\/strong>
emisiones totales de hidrocarburos no metano <50 mg\/m\u00b3, reducci\u00f3n anual de emisiones de carbono de aproximadamente 860.000 toneladas;
<\/strong><\/li>\n- Periodo de recuperaci\u00f3n:<\/strong> 3 a\u00f1os<\/li>\n<\/ul>\n
![\"CASO](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-3.webp\" "\\"\\"")
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An\u00e1lisis de seguridad<\/h3>\n\n- Control complejo\/Informaci\u00f3n sobre la cadena<\/li>\n
- An\u00e1lisis HAZOP<\/li>\n
- Clasificaci\u00f3n SIL<\/li>\n<\/ol>\n
<\/p>\n
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Innovaci\u00f3n 1: Avance en el l\u00edmite inferior de explosi\u00f3n en condiciones inertes<\/h3>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” column_structure=”1_2,1_2″][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n
125.000 antes de la distribuci\u00f3n a\u00e9rea<\/strong><\/h4>\n\n\n\nC\u00e1lculo de los l\u00edmites de explosividad de la parte combustible de una mezcla<\/td>\n<\/tr>\n \nF\u00f3rmula de Richard Chateli: Lf = 100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \nL\u00edmite de explosi\u00f3n de gas mixto Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \nConcentraci\u00f3n total de componentes combustibles<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\nDistribuci\u00f3n de aire convencional: La concentraci\u00f3n de componentes combustibles se reduce a <1.065, lo que significa que la distribuci\u00f3n de aire debe ser 2,6 veces mayor y el volumen de aire total alcanza los 330.000.<\/p>\n
[\/et_pb_text][\/et_pb_column][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n
Considere el efecto del gas inerte en el l\u00edmite inferior de explosi\u00f3n<\/strong><\/h4>\n![\"CASO](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-4.webp\" "\\"\\"")
<\/p>\n
Considerando solo el suministro de ox\u00edgeno, el suministro de aire es de 100.000 y el volumen total de aire es de 220.000.<\/p>\n
1. Fondo de aire, el l\u00edmite inferior de explosi\u00f3n a 900 \u2103 es 25%LEL;
2. Fondo inerte, no inflamable y no explosivo a temperatura ambiente, \u00bfpero a alta temperatura?<\/p>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default”][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”4_4″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n
Innovaci\u00f3n 2\u2014Dise\u00f1o y aplicaci\u00f3n de una estructura RTO cuadrada con gran volumen de aire<\/h3>\n
![\"CASO](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-5.webp\" "\\"\\"")
<\/p>\n
<\/p>\n
\n\n\n\nPar\u00e1metros de rendimiento<\/td>\n V\u00e1lvula rotativa RTO<\/td>\n V\u00e1lvula de elevaci\u00f3n RTO<\/td>\n<\/tr>\n \nVolumen de aire<\/td>\n 300.000 Nm\u00b3\/h<\/td>\n 300.000 Nm\u00b3\/h<\/td>\n<\/tr>\n \nEstructura de la v\u00e1lvula direccional<\/td>\n v\u00e1lvula rotatoria<\/td>\n v\u00e1lvula de elevaci\u00f3n<\/td>\n<\/tr>\n \nN\u00famero de v\u00e1lvulas inversoras<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \nFrecuencia de choque de conmutaci\u00f3n de la v\u00e1lvula de inversi\u00f3n<\/td>\n Funcionamiento continuo sin descargas el\u00e9ctricas<\/td>\n 6,48 millones de veces al a\u00f1o<\/td>\n<\/tr>\n \nN\u00famero de camas de almacenamiento de calor<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \nVolumen de aire por c\u00e1mara<\/td>\n 20000 Nm\u00b3\/h<\/td>\n 75000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n\u00c1rea de la secci\u00f3n transversal de una c\u00e1mara de almacenamiento de calor individual<\/td>\n 3\u33a1<\/td>\n 14\u33a1<\/td>\n<\/tr>\n \nPeso de llenado de cer\u00e1mica de almacenamiento de calor de una sola c\u00e1mara<\/td>\n 3300 kilos<\/td>\n 15600 kilogramos<\/td>\n<\/tr>\n \nN\u00famero de quemadores (piezas)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \nOcupaci\u00f3n (largo*ancho)<\/td>\n 26 m \u00d7 8 m<\/td>\n 48 m \u00d7 5 m<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” column_structure=”1_2,1_2″][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n
\u221a Principales indicadores t\u00e9cnicos de protecci\u00f3n ambiental<\/strong><\/p>\n\n\n\n\nNombre del par\u00e1metro<\/td>\n Datos<\/td>\n<\/tr>\n \nGases de escape con bajo contenido de metano\/10.000 m\u00b3\/h<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \nAire suplementario de ox\u00edgeno\/10.000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \nContenido de ox\u00edgeno en gases de combusti\u00f3n a baja temperatura%<\/td>\n 5<\/td>\n<\/tr>\n \nTemperatura del horno\u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \n\u00d3xidos de nitr\u00f3geno de escape mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \nHidrocarburos totales no met\u00e1nicos de escape mg\/m\u00b3<\/td>\n 40-60<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n[\/et_pb_text][\/et_pb_column][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n
\u221a Principales indicadores econ\u00f3micos<\/strong><\/p>\n\n\n\n\nNombre del par\u00e1metro<\/td>\n Datos<\/td>\n<\/tr>\n \nDistribuci\u00f3n de potencia instalada<\/td>\n 1200 kW\/h<\/td>\n<\/tr>\n \nCosto de la electricidad<\/td>\n 4,8 millones de yuanes al a\u00f1o<\/td>\n<\/tr>\n \nSalida de vapor de la caldera de calor residual<\/td>\n 45 toneladas por hora<\/td>\n<\/tr>\n \nPar\u00e1metros de Steam<\/td>\n 4,9 MPa, 420 \u2103<\/td>\n<\/tr>\n \nPrecio de Steam<\/td>\n 120 yuanes\/t<\/td>\n<\/tr>\n \nBeneficios econ\u00f3micos directos<\/td>\n 43,2 millones de yuanes al a\u00f1o<\/td>\n<\/tr>\n \nReducci\u00f3n del consumo de carb\u00f3n crudo<\/td>\n 50.000 toneladas\/a\u00f1o<\/td>\n<\/tr>\n \nReducci\u00f3n de las emisiones de carbono<\/td>\n 860.000 toneladas\/a\u00f1o<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default”][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”4_4″][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-6.webp” _builder_version=”4.27.4″ _module_preset=”default” alt=”RTO CASE” title_text=”0 RTO CASE 6″ align=”center” hover_enabled=”0″ sticky_enabled=”0″][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section]<\/p>","protected":false},"excerpt":{"rendered":"
Discover advanced RTO (Regenerative Thermal Oxidizer) systems for efficient VOCs waste gas treatment in the coal chemical industry. Our solutions reduce emissions, comply with environmental regulations, and enhance operational efficiency. Learn how our RTO technology can help your business achieve sustainable growth.What is coal gasificationCoal gasification is the core technology of modern coal chemical industry. 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Gasificaci\u00f3n de carb\u00f3n: se refiere a una reacci\u00f3n incompleta entre diversos tipos de carb\u00f3n (coque) y agentes gasificantes portadores de ox\u00edgeno (H\u2082O, O\u2082, CO\u2082) en un gasificador. A alta temperatura y presi\u00f3n, se produce gas de carb\u00f3n crudo compuesto de H\u2082, CH\u2083, CO\u2082, CO\u2082, N\u2082, trazas de H\u2082S, COS, etc.<\/p>\n
[\/et_pb_text][\/et_pb_column][et_pb_column type=”1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Clasificaci\u00f3n de los procesos de gasificaci\u00f3n del carb\u00f3n:<\/strong><\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Coal-chemical-gasification-method.webp” alt=”Coal chemical gasification method” title_text=”0-Coal chemical gasification method” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Coal-chemical-gasification-method-2.webp” alt=”-Coal chemical gasification method ” title_text=”0-Coal chemical gasification method 2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n Proceso de lavado con metanol a baja temperatura: se utiliza metanol fr\u00edo como disolvente de absorci\u00f3n, aprovechando la alta solubilidad del metanol en gases \u00e1cidos a bajas temperaturas, para eliminar los gases \u00e1cidos del gas de alimentaci\u00f3n, principalmente CO2 y H2S. <\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=\u201d1\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredeterminado\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredeterminado\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredeterminado\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredeterminado\u201d global_colors_info=\u201d{}\u201d]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row column_structure=”1_3,2_3″ use_custom_gutter=”on” gutter_width=”2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”1_3″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n Caracter\u00edsticas de los gases de escape del lavado con metanol a baja temperatura:<\/p>\n [\/et_pb_text][\/et_pb_column][et_pb_column type=”2_3″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component.webp” alt=” waste gas component” title_text=”0 waste gas component” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row column_structure=”1_2,1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n Debido a que los gases de escape casi no contienen ox\u00edgeno, es necesario complementarlos con aire para satisfacer los requisitos de ox\u00edgeno para la oxidaci\u00f3n completa de los gases de escape. 1) Consideraciones de seguridad: an\u00e1lisis de riesgo de explosi\u00f3n<\/strong><\/em><\/p>\n Seg\u00fan la Especificaci\u00f3n T\u00e9cnica para el Tratamiento de Gases de Residuos Org\u00e1nicos Industriales mediante el M\u00e9todo de Combusti\u00f3n con Almacenamiento T\u00e9rmico, la concentraci\u00f3n de materia org\u00e1nica que entra al dispositivo RTO debe ser inferior a 25% del LIE. Calcule el LIE de mezclas complejas de gases combustibles mediante la f\u00f3rmula de Le Chatlier y, a continuaci\u00f3n, compare la concentraci\u00f3n de componentes combustibles en los gases de escape con el LIE de 25% para determinar la seguridad de dicha concentraci\u00f3n.<\/p>\n 2) Consideraciones sobre la tasa de purificaci\u00f3n: \u201c3T1O\u201d<\/em><\/strong><\/p>\n [\/et_pb_text][\/et_pb_column][et_pb_column type=”1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-oxygen-supplementation-air-volume.webp” alt=”oxygen supplementation air volume” title_text=”0 oxygen supplementation air volume” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n Generalmente, en el dise\u00f1o, se ignora la influencia de los gases inertes. El l\u00edmite inferior de explosividad de los gases de escape se calcula y la relaci\u00f3n de diluci\u00f3n en aire se determina con base en la relaci\u00f3n entre la concentraci\u00f3n de gases de escape y el LIE de 25%. Este c\u00e1lculo puede garantizar la seguridad intr\u00ednseca, pero el volumen de gases de escape es relativamente grande.<\/p>\n Debido a la presencia de una gran cantidad de gas inerte CO2 en el gas de escape de lavado con metanol a baja temperatura N2, una peque\u00f1a cantidad de componentes combustibles, Por lo tanto, los gases de escape del lavado con metanol a baja temperatura no tienen l\u00edmites explosivos superiores o inferiores. [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” custom_margin=”|auto|14px|auto||” custom_padding=”||62px|||” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-2.webp” alt=”waste gas component” title_text=”0 waste gas component 2″ align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-3.webp” alt=”waste gas component” title_text=”0 waste gas component 3″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][et_pb_row column_structure=”2_5,3_5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”2_5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n El gas de escape mixto est\u00e1 dise\u00f1ado para la suplementaci\u00f3n de ox\u00edgeno en funci\u00f3n del balance de materiales, con un contenido de ox\u00edgeno de alrededor de 5% en los gases de combusti\u00f3n.<\/p>\n Comparaci\u00f3n entre la concentraci\u00f3n de componentes combustibles en los gases de escape despu\u00e9s de la suplementaci\u00f3n de ox\u00edgeno y el l\u00edmite explosivo inferior de los gases de escape (excluidos los gases inertes)<\/p>\n <\/p>\n 1) Bajo volumen de gases de escape<\/em><\/strong> [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-5.webp” alt=”waste gas component” title_text=”0 waste gas component 5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][et_pb_column type=”3_5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-4.webp” alt=”waste gas component” title_text=”0 waste gas component 4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-2-1.webp” alt=”waste gas component” title_text=”0 waste gas component 2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” custom_margin=”|auto|17px|auto||” custom_padding=”||50px|||” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Low-methane-waste-gas.webp” alt=”Low-methane waste gas” title_text=”0 Low-methane waste gas” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Heat-balance.webp” alt=”Heat balance” title_text=”0 Heat balance” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n La unidad de metanol de Xinye Energy Chemical, con una capacidad de 525.000 toneladas anuales, utiliza tecnolog\u00eda de gasificaci\u00f3n presurizada con carb\u00f3n triturado. Adem\u00e1s de los componentes principales, CO\u2082 y N\u2082, los gases de escape del lavado con metanol a baja temperatura tambi\u00e9n contienen metano, hidrocarburos totales no met\u00e1nicos, CO\u2082, metanol, etc. Estos gases de escape se descargan actualmente a trav\u00e9s de la chimenea de la caldera. De acuerdo con los requisitos de protecci\u00f3n ambiental, se requiere un tratamiento para la eliminaci\u00f3n de COV. Adem\u00e1s, la unidad de polioximetileno tambi\u00e9n tiene tres gases de escape que requieren tratamiento.<\/p>\n [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE.webp” alt=”RTO CASE” title_text=”0 RTO CASE” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n Con base en las caracter\u00edsticas de los componentes combustibles en los gases de escape, nuestros ingenieros han decidido adoptar la ruta de tecnolog\u00eda de tratamiento de \u201cpurificaci\u00f3n RTO + caldera de calor residual de vapor de presi\u00f3n media para recuperaci\u00f3n de calor\u201d; De acuerdo con el exclusivo \u201cAlgoritmo de distribuci\u00f3n de aire de seguridad de la teor\u00eda de correcci\u00f3n de gas inerte y Le Chater\u201d de nuestra empresa, hemos decidido seleccionar un RTO de v\u00e1lvula rotativa de volumen de aire de 270000, con un contenido de ox\u00edgeno de 5% en los gases de escape despu\u00e9s de la incineraci\u00f3n; Simult\u00e1neamente, seleccionar una caldera de vapor de 5,1 MPa\/46 T con un dise\u00f1o de chimenea final de 120 metros para reducir el impacto de las emisiones de escape en el entorno de la f\u00e1brica;<\/p>\n [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-1-1.webp” _builder_version=”4.27.4″ _module_preset=”default” alt=” RTO CASE” title_text=”0 RTO CASE 1″ hover_enabled=”0″ sticky_enabled=”0″][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n El dispositivo principal adopta una \u00fanica v\u00e1lvula rotativa RTO de 270.000 vol\u00famenes de aire, de dise\u00f1o cuadrado, equipada con 3 v\u00e1lvulas rotativas de distribuci\u00f3n de aire y 36 c\u00e1maras de almacenamiento de calor.<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default”][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”4_4″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n <\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default”][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”4_4″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” column_structure=”1_2,1_2″][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n Distribuci\u00f3n de aire convencional: La concentraci\u00f3n de componentes combustibles se reduce a <1.065, lo que significa que la distribuci\u00f3n de aire debe ser 2,6 veces mayor y el volumen de aire total alcanza los 330.000.<\/p>\n [\/et_pb_text][\/et_pb_column][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n Considerando solo el suministro de ox\u00edgeno, el suministro de aire es de 100.000 y el volumen total de aire es de 220.000.<\/p>\n 1. Fondo de aire, el l\u00edmite inferior de explosi\u00f3n a 900 \u2103 es 25%LEL; [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default”][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”4_4″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n <\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” column_structure=”1_2,1_2″][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n \u221a Principales indicadores t\u00e9cnicos de protecci\u00f3n ambiental<\/strong><\/p>\n [\/et_pb_text][\/et_pb_column][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n \u221a Principales indicadores econ\u00f3micos<\/strong><\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default”][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”4_4″][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-6.webp” _builder_version=”4.27.4″ _module_preset=”default” alt=”RTO CASE” title_text=”0 RTO CASE 6″ align=”center” hover_enabled=”0″ sticky_enabled=”0″][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section]<\/p>","protected":false},"excerpt":{"rendered":" Discover advanced RTO (Regenerative Thermal Oxidizer) systems for efficient VOCs waste gas treatment in the coal chemical industry. Our solutions reduce emissions, comply with environmental regulations, and enhance operational efficiency. Learn how our RTO technology can help your business achieve sustainable growth.What is coal gasificationCoal gasification is the core technology of modern coal chemical industry. 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Tabla de encuesta de componentes de gas crudo producidos por diferentes procesos de gasificaci\u00f3n<\/strong><\/h2>\n
\u00bfQu\u00e9 es el lavado con metanol a baja temperatura?<\/strong><\/h2>\n
El lavado con metanol a baja temperatura es un m\u00e9todo desarrollado conjuntamente por Linde y Lurgi a principios de la d\u00e9cada de 1950 para eliminar los gases \u00e1cidos de las materias primas. En 1954, se utiliz\u00f3 por primera vez para la purificaci\u00f3n de gases en la industria de la gasificaci\u00f3n presurizada de carb\u00f3n en Sud\u00e1frica.
<\/strong><\/p>\n\n
Propiedades de los gases residuales<\/strong><\/h2>\n
\n
Determinaci\u00f3n del volumen de aire de suplementaci\u00f3n de ox\u00edgeno<\/strong><\/h2>\n
Principio para determinar la cantidad de aire suplementario:<\/p>\n\n
De acuerdo con el m\u00e9todo de c\u00e1lculo para una mezcla que contiene n gases inflamables y p gases inertes, se puede determinar que el gas de escape mixto de baja calidad de gases inflamables e inertes no es inflamable ni explosivo.<\/p>\n
La cantidad de reposici\u00f3n de aire para los gases residuales del lavado con metanol a baja temperatura se puede determinar en funci\u00f3n de que el contenido de ox\u00edgeno de los gases de combusti\u00f3n despu\u00e9s de la oxidaci\u00f3n completa sea mayor que 3%.<\/p>\nProceso de c\u00e1lculo de la combustibilidad de gases de escape mixtos en el aire\u00a0<\/h3>\n
Procesamiento del volumen total de aire<\/strong><\/h4>\n
2) Volumen de aire de suplementaci\u00f3n de ox\u00edgeno<\/em><\/strong><\/p>\n\u2460 Balance de materiales<\/strong><\/h2>\n
\u00a0\u2461 Equilibrio t\u00e9rmico<\/strong><\/h2>\n
Casos t\u00edpicos de ingenier\u00eda<\/strong><\/h2>\n
An\u00e1lisis de la situaci\u00f3n<\/h3>\n
Ruta del proceso<\/h3>\n
\n
Equipado con un RTO rotatorio de 270.000 vol\u00famenes de aire, gas de cola de polioximetileno mezclado con aire para suplementar ox\u00edgeno.
Aprovechamiento del calor residual: 46 t\/h, vapor saturado de 5,1 MPa
<\/strong><\/li>\n
emisiones totales de hidrocarburos no metano <50 mg\/m\u00b3, reducci\u00f3n anual de emisiones de carbono de aproximadamente 860.000 toneladas;
<\/strong><\/li>\n<\/p>\nAn\u00e1lisis de seguridad<\/h3>\n
\n
Innovaci\u00f3n 1: Avance en el l\u00edmite inferior de explosi\u00f3n en condiciones inertes<\/h3>\n
125.000 antes de la distribuci\u00f3n a\u00e9rea<\/strong><\/h4>\n
\n\n
\n C\u00e1lculo de los l\u00edmites de explosividad de la parte combustible de una mezcla<\/td>\n<\/tr>\n \n F\u00f3rmula de Richard Chateli: Lf = 100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \n L\u00edmite de explosi\u00f3n de gas mixto Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n 25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \n Concentraci\u00f3n total de componentes combustibles<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n Considere el efecto del gas inerte en el l\u00edmite inferior de explosi\u00f3n<\/strong><\/h4>\n
<\/p>\n
2. Fondo inerte, no inflamable y no explosivo a temperatura ambiente, \u00bfpero a alta temperatura?<\/p>\nInnovaci\u00f3n 2\u2014Dise\u00f1o y aplicaci\u00f3n de una estructura RTO cuadrada con gran volumen de aire<\/h3>\n
<\/p>\n\n\n
\n Par\u00e1metros de rendimiento<\/td>\n V\u00e1lvula rotativa RTO<\/td>\n V\u00e1lvula de elevaci\u00f3n RTO<\/td>\n<\/tr>\n \n Volumen de aire<\/td>\n 300.000 Nm\u00b3\/h<\/td>\n 300.000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n Estructura de la v\u00e1lvula direccional<\/td>\n v\u00e1lvula rotatoria<\/td>\n v\u00e1lvula de elevaci\u00f3n<\/td>\n<\/tr>\n \n N\u00famero de v\u00e1lvulas inversoras<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \n Frecuencia de choque de conmutaci\u00f3n de la v\u00e1lvula de inversi\u00f3n<\/td>\n Funcionamiento continuo sin descargas el\u00e9ctricas<\/td>\n 6,48 millones de veces al a\u00f1o<\/td>\n<\/tr>\n \n N\u00famero de camas de almacenamiento de calor<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \n Volumen de aire por c\u00e1mara<\/td>\n 20000 Nm\u00b3\/h<\/td>\n 75000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n \u00c1rea de la secci\u00f3n transversal de una c\u00e1mara de almacenamiento de calor individual<\/td>\n 3\u33a1<\/td>\n 14\u33a1<\/td>\n<\/tr>\n \n Peso de llenado de cer\u00e1mica de almacenamiento de calor de una sola c\u00e1mara<\/td>\n 3300 kilos<\/td>\n 15600 kilogramos<\/td>\n<\/tr>\n \n N\u00famero de quemadores (piezas)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \n Ocupaci\u00f3n (largo*ancho)<\/td>\n 26 m \u00d7 8 m<\/td>\n 48 m \u00d7 5 m<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n \n\n
\n Nombre del par\u00e1metro<\/td>\n Datos<\/td>\n<\/tr>\n \n Gases de escape con bajo contenido de metano\/10.000 m\u00b3\/h<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \n Aire suplementario de ox\u00edgeno\/10.000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \n Contenido de ox\u00edgeno en gases de combusti\u00f3n a baja temperatura%<\/td>\n 5<\/td>\n<\/tr>\n \n Temperatura del horno\u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \n \u00d3xidos de nitr\u00f3geno de escape mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \n Hidrocarburos totales no met\u00e1nicos de escape mg\/m\u00b3<\/td>\n 40-60<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n \n\n
\n Nombre del par\u00e1metro<\/td>\n Datos<\/td>\n<\/tr>\n \n Distribuci\u00f3n de potencia instalada<\/td>\n 1200 kW\/h<\/td>\n<\/tr>\n \n Costo de la electricidad<\/td>\n 4,8 millones de yuanes al a\u00f1o<\/td>\n<\/tr>\n \n Salida de vapor de la caldera de calor residual<\/td>\n 45 toneladas por hora<\/td>\n<\/tr>\n \n Par\u00e1metros de Steam<\/td>\n 4,9 MPa, 420 \u2103<\/td>\n<\/tr>\n \n Precio de Steam<\/td>\n 120 yuanes\/t<\/td>\n<\/tr>\n \n Beneficios econ\u00f3micos directos<\/td>\n 43,2 millones de yuanes al a\u00f1o<\/td>\n<\/tr>\n \n Reducci\u00f3n del consumo de carb\u00f3n crudo<\/td>\n 50.000 toneladas\/a\u00f1o<\/td>\n<\/tr>\n \n Reducci\u00f3n de las emisiones de carbono<\/td>\n 860.000 toneladas\/a\u00f1o<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n