[\/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
Was ist Kohlevergasung<\/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
Die Kohlevergasung ist die Kerntechnologie der modernen Kohlechemie.<\/strong><\/p>\nKohlevergasung: bezeichnet eine unvollst\u00e4ndige Reaktion zwischen verschiedenen Kohlearten (Koks) und sauerstoffhaltigen Vergasungsmitteln (H2O, O2, CO2) in einem Vergaser. Bei hoher Temperatur und einem bestimmten Druck entsteht letztendlich Rohkohlegas, das aus H2, CH4, CO, CO2, N2, Spuren von H2S, COS usw. besteht.<\/p>\n
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Klassifizierung von Kohlevergasungsprozessen:<\/strong><\/p>\n\n- Rohstoffe: Kohlenstaub, zerkleinerte Kohle, Kohlewasseraufschl\u00e4mmung;<\/li>\n
- Vergasungsbett: Wirbelschicht, Flie\u00dfbett, Festbett;\n<\/li>\n
- Das Festbett besteht aus St\u00fcckkohle (15\u201350 mm) als Rohstoff;<\/li>\n
- Das Wirbelbett besteht aus zerkleinerter Kohle (weniger als 10 mm) als Rohmaterial.<\/li>\n
- Das Luftstrombett besteht aus pulverisierter Kohle (weniger als 0,1 mm) als Rohmaterial;\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
\u00dcbersichtstabelle der durch verschiedene Vergasungsverfahren erzeugten Rohgaskomponenten<\/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
Was ist eine Niedertemperatur-Methanolw\u00e4sche?<\/strong><\/h2>\nNiedertemperatur-Methanolwaschverfahren: Verwendung von kaltem Methanol als Absorptionsl\u00f6sungsmittel, Ausnutzung der hohen L\u00f6slichkeit von Methanol in sauren Gasen bei niedrigen Temperaturen, um saure Gase, haupts\u00e4chlich CO2 und H2S, aus dem Ausgangsgas zu entfernen.
Die Niedertemperatur-Methanolw\u00e4sche ist ein Anfang der 1950er Jahre gemeinsam von Linde und Lurgi entwickeltes Verfahren zur Entfernung saurer Gase aus Rohstoffgasen. 1954 wurde es erstmals zur Gasreinigung in der Kohledruckvergasungsindustrie in S\u00fcdafrika eingesetzt.
<\/strong><\/p>\n <\/p>\n
\n- Zu den Anbietern von Prozesspaketen f\u00fcr die Niedertemperatur-Methanolw\u00e4sche geh\u00f6ren Linde, Lurgi, die Technische Universit\u00e4t Dalian usw.<\/li>\n
- Es gibt verschiedene Vergasungsverfahren, die in drei Kategorien unterteilt werden k\u00f6nnen: Festbett, Wirbelschicht und Flie\u00dfbett;<\/li>\n
- Bei der Bestimmung, ob das emissionsarme Gas einen Restw\u00e4rmer\u00fcckgewinnungswert hat, wird haupts\u00e4chlich der CH4-Gehalt im Abgas ber\u00fccksichtigt.<\/li>\n
- Die CH4-Konzentration h\u00e4ngt vom Vergasungsprozess ab. Zu den Festbettvergasungsprozessen geh\u00f6ren Lurgi-\u00d6fen, BGL-\u00d6fen usw.<\/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=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Abgaseigenschaften<\/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
Eigenschaften des Niedertemperatur-Methanol-W\u00e4scheabgases:<\/p>\n
\n- Das Abgas ist grunds\u00e4tzlich mit Wasserdampf ges\u00e4ttigt<\/li>\n
- Hoher Gehalt an inerten Komponenten CO2 und N2<\/li>\n
- Das Abgas enth\u00e4lt grunds\u00e4tzlich keinen Sauerstoff<\/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
Bestimmung des Sauerstoff-Erg\u00e4nzungsluftvolumens<\/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
Da das Abgas nahezu keinen Sauerstoff enth\u00e4lt, ist es notwendig, dem Abgas Luft zuzuf\u00fchren, um den Sauerstoffbedarf f\u00fcr eine vollst\u00e4ndige Oxidation des Abgases zu decken.
Prinzip zur Bestimmung der Zusatzluftmenge:<\/p>\n
1) Sicherheitsaspekte: Explosionsgefahrenanalyse<\/strong><\/em><\/p>\nGem\u00e4\u00df der technischen Spezifikation f\u00fcr die Behandlung organischer Industrieabgase durch thermische Speicherverbrennung muss die Konzentration organischer Stoffe, die in das RTO-Ger\u00e4t gelangen, unter 25% der unteren Explosionsgrenze liegen. Berechnen Sie die untere Explosionsgrenze komplexer brennbarer Gasgemische mithilfe der Le Chatlier-Formel und vergleichen Sie dann die Konzentration brennbarer Komponenten im Abgas mit der Gr\u00f6\u00dfe von 25% UEG, um die Sicherheit der Konzentration brennbarer Komponenten im Abgas zu bestimmen.<\/p>\n
2) \u00dcberlegungen zur Reinigungsrate: \u201e3T1O\u201c<\/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 ist die untere Explosionsgrenze des Mischgases,%<\/li>\n
- Li ist die untere Explosionsgrenze der Komponente i,%<\/li>\n
- Vi ist der Volumenanteil einer bestimmten brennbaren Komponente an der brennbaren Komponente,%<\/li>\n<\/ul>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Normalerweise wird bei der Auslegung der Einfluss von Inertgasen nicht ber\u00fccksichtigt. Die untere Explosionsgrenze des Abgases wird berechnet und das Luftverd\u00fcnnungsverh\u00e4ltnis wird basierend auf der Beziehung zwischen der Abgaskonzentration und 25% UEG bestimmt. Diese Berechnung kann die Eigensicherheit gew\u00e4hrleisten, das Abgasvolumen ist jedoch relativ gro\u00df.<\/p>\n
Aufgrund des Vorhandenseins einer gro\u00dfen Menge an Inertgas CO2 im Niedertemperatur-Methanol-Waschabgas N2\uff0c Eine kleine Menge brennbarer Komponenten,
Nach der Berechnungsmethode f\u00fcr ein Gemisch aus n brennbaren Gasen und p Inertgasen kann festgestellt werden, dass das minderwertige Abgasgemisch aus brennbaren und Inertgasen nicht brennbar und nicht explosiv ist.<\/p>\n
Daher gibt es f\u00fcr das Abgas aus der Niedertemperatur-Methanolw\u00e4sche keine oberen oder unteren Explosionsgrenzen.
Die Menge der Lufterg\u00e4nzung f\u00fcr das Abgas der Niedertemperatur-Methanolw\u00e4sche kann anhand des Sauerstoffgehalts des Rauchgases nach vollst\u00e4ndiger Oxidation bestimmt werden, der gr\u00f6\u00dfer als 3% ist.<\/p>\n
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Berechnungsverfahren f\u00fcr die Brennbarkeit von Abgasgemischen in Luft\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
Das gemischte Abgas ist f\u00fcr eine Sauerstofferg\u00e4nzung auf Basis der Stoffbilanz ausgelegt, mit einem Sauerstoffgehalt von ca. 5% im Rauchgas<\/p>\n
Vergleich zwischen der Konzentration brennbarer Bestandteile im Abgas nach Sauerstoffzugabe und der unteren Explosionsgrenze des Abgases (ohne Inertgase)<\/p>\n
<\/p>\n
Verarbeitung des gesamten Luftvolumens<\/strong><\/h4>\n1) Geringes Abgasvolumen<\/em><\/strong>
2) Sauerstofferg\u00e4nzungsluftvolumen<\/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 Materialbilanz<\/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 W\u00e4rmebilanz<\/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
Typische Engineering-F\u00e4lle<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Situationsanalyse<\/h3>\n
Die Methanolanlage von Xinye Energy Chemical mit einer Kapazit\u00e4t von 525.000 Tonnen pro Jahr nutzt die Druckvergasungstechnologie von zerkleinerter Kohle. Neben den Hauptkomponenten CO2 und N2 enth\u00e4lt das Abgas der Niedertemperatur-Methanolw\u00e4sche auch Methan, Nicht-Methan-Gesamtkohlenwasserstoffe, CO, Methanol usw. Dieses Abgas wird derzeit \u00fcber den Kesselkamin abgeleitet. Gem\u00e4\u00df den Umweltschutzbestimmungen ist eine Behandlung zur Entfernung fl\u00fcchtiger organischer Verbindungen (VOCs) erforderlich. Dar\u00fcber hinaus fallen bei der Polyoxymethylenanlage drei weitere Abgase an, die behandelt werden m\u00fcssen.<\/p>\n
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Prozessroute<\/h3>\n
Aufgrund der Eigenschaften der brennbaren Bestandteile im Abgas haben sich unsere Ingenieure f\u00fcr die Behandlungstechnologie \u201eRTO-Reinigung + Mitteldruck-Dampfabhitzekessel zur W\u00e4rmer\u00fcckgewinnung\u201c entschieden. Gem\u00e4\u00df dem einzigartigen \u201eLe Chater&Inert Gas Correction Theory Safety Air Distribution Algorithm\u201c unseres Unternehmens haben wir uns f\u00fcr einen RTO mit einem Luftvolumen von 270.000 und einem Sauerstoffgehalt von 5% im Abgas nach der Verbrennung entschieden. Gleichzeitig haben wir einen 5,1 MPa\/46T-Dampfkessel mit einem 120 Meter langen Endkamin ausgew\u00e4hlt, um die Auswirkungen der Abgasemissionen auf die Fabrikumgebung zu reduzieren.<\/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
Das Hauptger\u00e4t verf\u00fcgt \u00fcber ein einzelnes Drehventil RTO mit einem Luftvolumen von 270.000, quadratischem Layout, ausgestattet mit 3 Drehluftverteilungsventilen und 36 W\u00e4rmespeicherkammern<\/p>\n
\n- Umfassende Behandlung:<\/strong>
Ausgestattet mit einem rotierenden RTO mit einem Luftvolumen von 270.000, Polyoxymethylen-Abgas gemischt mit Luft zur Sauerstofferg\u00e4nzung
Abw\u00e4rmenutzung: 46 t\/h, 5,1 MPa Sattdampf
<\/strong><\/li>\n- Umweltschutzstandards:<\/strong>
Gesamtkohlenwasserstoffemissionen ohne Methan <50 mg\/m\u00b3, j\u00e4hrliche Reduzierung der Kohlenstoffemissionen um etwa 860.000 Tonnen;
<\/strong><\/li>\n- Amortisationszeit:<\/strong> 3 Jahre<\/li>\n<\/ul>\n
![\"RTO-FALL](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-3.webp\" "\\"\\"")
<\/p>\n
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Sicherheitsanalyse<\/h3>\n\n- Komplexe Steuerung\/Kettenbesprechung<\/li>\n
- HAZOP-Analyse<\/li>\n
- SIL-Einstufung<\/li>\n<\/ol>\n
<\/p>\n
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Innovation 1 \u2013 Durchbruch bei der unteren Explosionsgrenze unter inerten Bedingungen<\/h3>\n
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125.000 vor Luftverteilung<\/strong><\/h4>\n\n\n\nBerechnung der Explosionsgrenzen des brennbaren Anteils eines Gemisches<\/td>\n<\/tr>\n \nFormel von Richard Chateli: Lf=100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \nMischgas-Explosionsgrenze Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \nGesamtkonzentration brennbarer Bestandteile<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\nKonventionelle Luftverteilung: Die Konzentration brennbarer Bestandteile wird auf <1,065 reduziert, was bedeutet, dass die Luftverteilung 2,6-mal so hoch sein muss und das Gesamtluftvolumen 330.000 erreicht.<\/p>\n
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Ber\u00fccksichtigen Sie den Einfluss von Inertgas auf die untere Explosionsgrenze<\/strong><\/h4>\n![\"RTO-FALL\"](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-4.webp\" "\\"\\"")
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Betrachtet man nur die Sauerstoffzufuhr, betr\u00e4gt die Luftzufuhr 100.000 und das Gesamtluftvolumen 220.000<\/p>\n
1. Lufthintergrund, die untere Explosionsgrenze bei 900 \u00b0C betr\u00e4gt 25%LEL;
2. Inerter Hintergrund, nicht brennbar und nicht explosiv bei Raumtemperatur, aber bei hohen Temperaturen?<\/p>\n
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Innovation 2 \u2013 Design und Anwendung einer quadratischen RTO-Struktur mit gro\u00dfem Luftvolumen<\/h3>\n
![\"RTO-FALL\"](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-5.webp\" "\\"\\"")
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\n\n\n\nLeistungsparameter<\/td>\n Drehventil RTO<\/td>\n Hubventil RTO<\/td>\n<\/tr>\n \nLuftmenge<\/td>\n 300.000 Nm\u00b3\/h<\/td>\n 300.000 Nm\u00b3\/h<\/td>\n<\/tr>\n \nWegeventilaufbau<\/td>\n Drehventil<\/td>\n Hubventil<\/td>\n<\/tr>\n \nAnzahl der Umschaltventile<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \nH\u00e4ufigkeit des Schaltsto\u00dfes des Umschaltventils<\/td>\n Dauerbetrieb ohne Ersch\u00fctterungen<\/td>\n 6,48 Millionen Mal\/Jahr<\/td>\n<\/tr>\n \nAnzahl der W\u00e4rmespeicherbetten<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \nLuftvolumen pro Kammer<\/td>\n 20000 Nm\u00b3\/h<\/td>\n 75000 Nm\u00b3\/h<\/td>\n<\/tr>\n \nQuerschnittsfl\u00e4che einer einzelnen W\u00e4rmespeicherkammer<\/td>\n 3 m\u00b2<\/td>\n 14 m\u00b2<\/td>\n<\/tr>\n \nF\u00fcllgewicht Einkammer-W\u00e4rmespeicherkeramik<\/td>\n 3300 kg<\/td>\n 15600 kg<\/td>\n<\/tr>\n \nAnzahl der Brenner (St\u00fcck)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \nBelegung (L\u00e4nge*Breite)<\/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 Wichtigste technische Indikatoren f\u00fcr den Umweltschutz<\/strong><\/p>\n\n\n\n\nParametername<\/td>\n Daten<\/td>\n<\/tr>\n \nMethanarmes Abgas\/10.000 m\u00b3\/h<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \nSauerstoff-Zusatzluft\/10.000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \nSauerstoffgehalt im Niedertemperatur-Rauchgas%<\/td>\n 5<\/td>\n<\/tr>\n \nOfentemperatur \u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \nAbgasstickstoffe mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \nAbgas Nicht-Methan Gesamtkohlenwasserstoffe 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 Wichtigste Wirtschaftsindikatoren<\/strong><\/p>\n\n\n\n\nParametername<\/td>\n Daten<\/td>\n<\/tr>\n \nInstallierte Stromverteilungsleistung<\/td>\n 1200KW\/h<\/td>\n<\/tr>\n \nStromkosten<\/td>\n 4,8 Millionen Yuan\/Jahr<\/td>\n<\/tr>\n \nDampfleistung des Abhitzekessels<\/td>\n 45 t\/h<\/td>\n<\/tr>\n \nDampfparameter<\/td>\n 4,9 MPa, 420 \u00b0C<\/td>\n<\/tr>\n \nSteam-Preis<\/td>\n 120 Yuan\/t<\/td>\n<\/tr>\n \nDirekter wirtschaftlicher Nutzen<\/td>\n 43,2 Millionen Yuan\/Jahr<\/td>\n<\/tr>\n \nReduzierung des Rohkohleverbrauchs<\/td>\n 50.000 Tonnen\/Jahr<\/td>\n<\/tr>\n \nReduzierung der Kohlenstoffemissionen<\/td>\n 860.000 Tonnen\/Jahr<\/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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Kohlevergasung: bezeichnet eine unvollst\u00e4ndige Reaktion zwischen verschiedenen Kohlearten (Koks) und sauerstoffhaltigen Vergasungsmitteln (H2O, O2, CO2) in einem Vergaser. Bei hoher Temperatur und einem bestimmten Druck entsteht letztendlich Rohkohlegas, das aus H2, CH4, CO, CO2, N2, Spuren von H2S, COS usw. besteht.<\/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
Klassifizierung von Kohlevergasungsprozessen:<\/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 Niedertemperatur-Methanolwaschverfahren: Verwendung von kaltem Methanol als Absorptionsl\u00f6sungsmittel, Ausnutzung der hohen L\u00f6slichkeit von Methanol in sauren Gasen bei niedrigen Temperaturen, um saure Gase, haupts\u00e4chlich CO2 und H2S, aus dem Ausgangsgas zu entfernen. <\/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=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\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 Eigenschaften des Niedertemperatur-Methanol-W\u00e4scheabgases:<\/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 Da das Abgas nahezu keinen Sauerstoff enth\u00e4lt, ist es notwendig, dem Abgas Luft zuzuf\u00fchren, um den Sauerstoffbedarf f\u00fcr eine vollst\u00e4ndige Oxidation des Abgases zu decken. 1) Sicherheitsaspekte: Explosionsgefahrenanalyse<\/strong><\/em><\/p>\n Gem\u00e4\u00df der technischen Spezifikation f\u00fcr die Behandlung organischer Industrieabgase durch thermische Speicherverbrennung muss die Konzentration organischer Stoffe, die in das RTO-Ger\u00e4t gelangen, unter 25% der unteren Explosionsgrenze liegen. Berechnen Sie die untere Explosionsgrenze komplexer brennbarer Gasgemische mithilfe der Le Chatlier-Formel und vergleichen Sie dann die Konzentration brennbarer Komponenten im Abgas mit der Gr\u00f6\u00dfe von 25% UEG, um die Sicherheit der Konzentration brennbarer Komponenten im Abgas zu bestimmen.<\/p>\n 2) \u00dcberlegungen zur Reinigungsrate: \u201e3T1O\u201c<\/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=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n Normalerweise wird bei der Auslegung der Einfluss von Inertgasen nicht ber\u00fccksichtigt. Die untere Explosionsgrenze des Abgases wird berechnet und das Luftverd\u00fcnnungsverh\u00e4ltnis wird basierend auf der Beziehung zwischen der Abgaskonzentration und 25% UEG bestimmt. Diese Berechnung kann die Eigensicherheit gew\u00e4hrleisten, das Abgasvolumen ist jedoch relativ gro\u00df.<\/p>\n Aufgrund des Vorhandenseins einer gro\u00dfen Menge an Inertgas CO2 im Niedertemperatur-Methanol-Waschabgas N2\uff0c Eine kleine Menge brennbarer Komponenten, Daher gibt es f\u00fcr das Abgas aus der Niedertemperatur-Methanolw\u00e4sche keine oberen oder unteren Explosionsgrenzen. [\/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 Das gemischte Abgas ist f\u00fcr eine Sauerstofferg\u00e4nzung auf Basis der Stoffbilanz ausgelegt, mit einem Sauerstoffgehalt von ca. 5% im Rauchgas<\/p>\n Vergleich zwischen der Konzentration brennbarer Bestandteile im Abgas nach Sauerstoffzugabe und der unteren Explosionsgrenze des Abgases (ohne Inertgase)<\/p>\n <\/p>\n 1) Geringes Abgasvolumen<\/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=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n Die Methanolanlage von Xinye Energy Chemical mit einer Kapazit\u00e4t von 525.000 Tonnen pro Jahr nutzt die Druckvergasungstechnologie von zerkleinerter Kohle. Neben den Hauptkomponenten CO2 und N2 enth\u00e4lt das Abgas der Niedertemperatur-Methanolw\u00e4sche auch Methan, Nicht-Methan-Gesamtkohlenwasserstoffe, CO, Methanol usw. Dieses Abgas wird derzeit \u00fcber den Kesselkamin abgeleitet. Gem\u00e4\u00df den Umweltschutzbestimmungen ist eine Behandlung zur Entfernung fl\u00fcchtiger organischer Verbindungen (VOCs) erforderlich. Dar\u00fcber hinaus fallen bei der Polyoxymethylenanlage drei weitere Abgase an, die behandelt werden m\u00fcssen.<\/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 Aufgrund der Eigenschaften der brennbaren Bestandteile im Abgas haben sich unsere Ingenieure f\u00fcr die Behandlungstechnologie \u201eRTO-Reinigung + Mitteldruck-Dampfabhitzekessel zur W\u00e4rmer\u00fcckgewinnung\u201c entschieden. Gem\u00e4\u00df dem einzigartigen \u201eLe Chater&Inert Gas Correction Theory Safety Air Distribution Algorithm\u201c unseres Unternehmens haben wir uns f\u00fcr einen RTO mit einem Luftvolumen von 270.000 und einem Sauerstoffgehalt von 5% im Abgas nach der Verbrennung entschieden. Gleichzeitig haben wir einen 5,1 MPa\/46T-Dampfkessel mit einem 120 Meter langen Endkamin ausgew\u00e4hlt, um die Auswirkungen der Abgasemissionen auf die Fabrikumgebung zu reduzieren.<\/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 Das Hauptger\u00e4t verf\u00fcgt \u00fcber ein einzelnes Drehventil RTO mit einem Luftvolumen von 270.000, quadratischem Layout, ausgestattet mit 3 Drehluftverteilungsventilen und 36 W\u00e4rmespeicherkammern<\/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 Konventionelle Luftverteilung: Die Konzentration brennbarer Bestandteile wird auf <1,065 reduziert, was bedeutet, dass die Luftverteilung 2,6-mal so hoch sein muss und das Gesamtluftvolumen 330.000 erreicht.<\/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 Betrachtet man nur die Sauerstoffzufuhr, betr\u00e4gt die Luftzufuhr 100.000 und das Gesamtluftvolumen 220.000<\/p>\n 1. Lufthintergrund, die untere Explosionsgrenze bei 900 \u00b0C betr\u00e4gt 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 Wichtigste technische Indikatoren f\u00fcr den Umweltschutz<\/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 Wichtigste Wirtschaftsindikatoren<\/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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\u00dcbersichtstabelle der durch verschiedene Vergasungsverfahren erzeugten Rohgaskomponenten<\/strong><\/h2>\n
Was ist eine Niedertemperatur-Methanolw\u00e4sche?<\/strong><\/h2>\n
Die Niedertemperatur-Methanolw\u00e4sche ist ein Anfang der 1950er Jahre gemeinsam von Linde und Lurgi entwickeltes Verfahren zur Entfernung saurer Gase aus Rohstoffgasen. 1954 wurde es erstmals zur Gasreinigung in der Kohledruckvergasungsindustrie in S\u00fcdafrika eingesetzt.
<\/strong><\/p>\n\n
Abgaseigenschaften<\/strong><\/h2>\n
\n
Bestimmung des Sauerstoff-Erg\u00e4nzungsluftvolumens<\/strong><\/h2>\n
Prinzip zur Bestimmung der Zusatzluftmenge:<\/p>\n\n
Nach der Berechnungsmethode f\u00fcr ein Gemisch aus n brennbaren Gasen und p Inertgasen kann festgestellt werden, dass das minderwertige Abgasgemisch aus brennbaren und Inertgasen nicht brennbar und nicht explosiv ist.<\/p>\n
Die Menge der Lufterg\u00e4nzung f\u00fcr das Abgas der Niedertemperatur-Methanolw\u00e4sche kann anhand des Sauerstoffgehalts des Rauchgases nach vollst\u00e4ndiger Oxidation bestimmt werden, der gr\u00f6\u00dfer als 3% ist.<\/p>\nBerechnungsverfahren f\u00fcr die Brennbarkeit von Abgasgemischen in Luft\u00a0<\/h3>\n
Verarbeitung des gesamten Luftvolumens<\/strong><\/h4>\n
2) Sauerstofferg\u00e4nzungsluftvolumen<\/em><\/strong><\/p>\n\u2460 Materialbilanz<\/strong><\/h2>\n
\u00a0\u2461 W\u00e4rmebilanz<\/strong><\/h2>\n
Typische Engineering-F\u00e4lle<\/strong><\/h2>\n
Situationsanalyse<\/h3>\n
Prozessroute<\/h3>\n
\n
Ausgestattet mit einem rotierenden RTO mit einem Luftvolumen von 270.000, Polyoxymethylen-Abgas gemischt mit Luft zur Sauerstofferg\u00e4nzung
Abw\u00e4rmenutzung: 46 t\/h, 5,1 MPa Sattdampf
<\/strong><\/li>\n
Gesamtkohlenwasserstoffemissionen ohne Methan <50 mg\/m\u00b3, j\u00e4hrliche Reduzierung der Kohlenstoffemissionen um etwa 860.000 Tonnen;
<\/strong><\/li>\n<\/p>\nSicherheitsanalyse<\/h3>\n
\n
Innovation 1 \u2013 Durchbruch bei der unteren Explosionsgrenze unter inerten Bedingungen<\/h3>\n
125.000 vor Luftverteilung<\/strong><\/h4>\n
\n\n
\n Berechnung der Explosionsgrenzen des brennbaren Anteils eines Gemisches<\/td>\n<\/tr>\n \n Formel von Richard Chateli: Lf=100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \n Mischgas-Explosionsgrenze Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n 25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \n Gesamtkonzentration brennbarer Bestandteile<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n Ber\u00fccksichtigen Sie den Einfluss von Inertgas auf die untere Explosionsgrenze<\/strong><\/h4>\n
<\/p>\n
2. Inerter Hintergrund, nicht brennbar und nicht explosiv bei Raumtemperatur, aber bei hohen Temperaturen?<\/p>\nInnovation 2 \u2013 Design und Anwendung einer quadratischen RTO-Struktur mit gro\u00dfem Luftvolumen<\/h3>\n
<\/p>\n\n\n
\n Leistungsparameter<\/td>\n Drehventil RTO<\/td>\n Hubventil RTO<\/td>\n<\/tr>\n \n Luftmenge<\/td>\n 300.000 Nm\u00b3\/h<\/td>\n 300.000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n Wegeventilaufbau<\/td>\n Drehventil<\/td>\n Hubventil<\/td>\n<\/tr>\n \n Anzahl der Umschaltventile<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \n H\u00e4ufigkeit des Schaltsto\u00dfes des Umschaltventils<\/td>\n Dauerbetrieb ohne Ersch\u00fctterungen<\/td>\n 6,48 Millionen Mal\/Jahr<\/td>\n<\/tr>\n \n Anzahl der W\u00e4rmespeicherbetten<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \n Luftvolumen pro Kammer<\/td>\n 20000 Nm\u00b3\/h<\/td>\n 75000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n Querschnittsfl\u00e4che einer einzelnen W\u00e4rmespeicherkammer<\/td>\n 3 m\u00b2<\/td>\n 14 m\u00b2<\/td>\n<\/tr>\n \n F\u00fcllgewicht Einkammer-W\u00e4rmespeicherkeramik<\/td>\n 3300 kg<\/td>\n 15600 kg<\/td>\n<\/tr>\n \n Anzahl der Brenner (St\u00fcck)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \n Belegung (L\u00e4nge*Breite)<\/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 Parametername<\/td>\n Daten<\/td>\n<\/tr>\n \n Methanarmes Abgas\/10.000 m\u00b3\/h<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \n Sauerstoff-Zusatzluft\/10.000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \n Sauerstoffgehalt im Niedertemperatur-Rauchgas%<\/td>\n 5<\/td>\n<\/tr>\n \n Ofentemperatur \u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \n Abgasstickstoffe mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \n Abgas Nicht-Methan Gesamtkohlenwasserstoffe mg\/m\u00b3<\/td>\n 40-60<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n \n\n
\n Parametername<\/td>\n Daten<\/td>\n<\/tr>\n \n Installierte Stromverteilungsleistung<\/td>\n 1200KW\/h<\/td>\n<\/tr>\n \n Stromkosten<\/td>\n 4,8 Millionen Yuan\/Jahr<\/td>\n<\/tr>\n \n Dampfleistung des Abhitzekessels<\/td>\n 45 t\/h<\/td>\n<\/tr>\n \n Dampfparameter<\/td>\n 4,9 MPa, 420 \u00b0C<\/td>\n<\/tr>\n \n Steam-Preis<\/td>\n 120 Yuan\/t<\/td>\n<\/tr>\n \n Direkter wirtschaftlicher Nutzen<\/td>\n 43,2 Millionen Yuan\/Jahr<\/td>\n<\/tr>\n \n Reduzierung des Rohkohleverbrauchs<\/td>\n 50.000 Tonnen\/Jahr<\/td>\n<\/tr>\n \n Reduzierung der Kohlenstoffemissionen<\/td>\n 860.000 Tonnen\/Jahr<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n