[\/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
Wat is kolenvergassing?<\/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
Vergassing van steenkool is de kerntechnologie van de moderne steenkoolchemische industrie.<\/strong><\/p>\nVergassing van steenkool: verwijst naar een onvolledige reactie tussen verschillende soorten steenkool (cokes) en zuurstofdragende vergassers (H\u2082O, O\u2082, CO\u2082) in een vergasser. Onder hoge temperatuur en een bepaalde druk ontstaat uiteindelijk ruw steenkoolgas, bestaande uit H\u2082, CH\u2082, CO, CO\u2082, N\u2082, sporen H\u2082S, CO\u2082, enz.<\/p>\n
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Classificatie van steenkoolvergassingsprocessen:<\/strong><\/p>\n\n- Grondstoffen: gemalen steenkool, gebroken steenkool, steenkoolwaterstofslib;<\/li>\n
- Vergassingsbed: wervelbed, wervelbed, vast bed;\n<\/li>\n
- Vast bed wordt gemaakt van brokken steenkool (15-50mm) als grondstof;<\/li>\n
- Wervelbed wordt gemaakt van gebroken steenkool (kleiner dan 10 mm) als grondstof;<\/li>\n
- Het luchtstroombed wordt gemaakt van gemalen steenkool (kleiner dan 0,1 mm) als grondstof;\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
Overzichtstabel van ruwe gascomponenten geproduceerd door verschillende vergassingsprocessen<\/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
Wat is lagetemperatuurmethanolwas?<\/strong><\/h2>\nMethanolwasproces bij lage temperaturen: koude methanol wordt gebruikt als absorptiemiddel, waarbij gebruik wordt gemaakt van de hoge oplosbaarheid van methanol in zure gassen bij lage temperaturen, om zure gassen uit het toevoergas te verwijderen, voornamelijk CO2 en H2S.
Methanolwassen bij lage temperatuur is een methode die begin jaren vijftig gezamenlijk door Linde en Lurgi is ontwikkeld om zure gassen uit grondstofgassen te verwijderen. In 1954 werd het voor het eerst gebruikt voor gaszuivering in de Zuid-Afrikaanse kolenvergassingsindustrie.
<\/strong><\/p>\n <\/p>\n
\n- Leveranciers van pakketpakketten voor methanolwasprocessen bij lage temperaturen zijn onder meer Linde, Lurgi, Dalian University of Technology, enz.<\/li>\n
- Er bestaan verschillende vergassingsprocessen, die in drie categorie\u00ebn kunnen worden onderverdeeld: vast bed, wervelbed en wervelbed;<\/li>\n
- Bij de bepaling of het rookgas een restwarmteterugwinningswaarde heeft, wordt vooral gekeken naar het CH4-gehalte in het rookgas;<\/li>\n
- De concentratie van CH4 is afhankelijk van het vergassingsproces. Vastebedvergassingsprocessen omvatten Lurgi-oven, BGL-oven, enz.<\/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=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Afgaseigenschappen<\/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
Kenmerken van uitlaatgassen van methanolwassing op lage temperatuur:<\/p>\n
\n- Het uitlaatgas is in principe verzadigd met waterdamp<\/li>\n
- Hoog gehalte aan inerte componenten CO2 en N2<\/li>\n
- Het uitlaatgas bevat in principe geen zuurstof<\/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
Bepaling van het zuurstofsuppletieluchtvolume<\/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
Omdat de uitlaatgassen vrijwel geen zuurstof bevatten, is het noodzakelijk om de uitlaatgassen aan te vullen met lucht om aan de zuurstofbehoefte te voldoen voor een volledige oxidatie van de uitlaatgassen.
Principe voor het bepalen van de hoeveelheid extra lucht:<\/p>\n
1) Veiligheidsoverwegingen: analyse van explosiegevaar<\/strong><\/em><\/p>\nVolgens de technische specificatie voor de behandeling van industrieel organisch afvalgas met behulp van thermische opslagverbranding moet de concentratie organisch materiaal dat het RTO-apparaat binnenkomt, lager zijn dan 25% van de onderste explosiegrens. Bereken de onderste explosiegrens van complexe brandbare gasmengsels met behulp van de Le-Chatlier-formule en vergelijk vervolgens de concentratie brandbare componenten in het rookgas met de grootte van 25% LEL om de veiligheid van de concentratie brandbare componenten in het rookgas te bepalen.<\/p>\n
2) Overwegingen met betrekking tot de zuiveringssnelheid: \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 is de onderste explosiegrens van het gemengde gas, %<\/li>\n
- Li is de onderste explosiegrens van component i,%<\/li>\n
- Vi is de volumefractie van een bepaalde brandbare component ten opzichte van de brandbare component,%<\/li>\n<\/ul>\n
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Meestal ontworpen zonder rekening te houden met de invloed van inerte gassen, wordt de onderste explosiegrens van het uitlaatgas berekend en de luchtverdunningsverhouding bepaald op basis van de verhouding tussen de uitlaatgasconcentratie en de 25% LEL. Deze berekening kan intrinsieke veiligheid garanderen, maar het uitlaatgasvolume is relatief groot.<\/p>\n
Vanwege de aanwezigheid van een grote hoeveelheid inert gas CO2 in het uitlaatgas N2 van de methanolwas bij lage temperaturen, een kleine hoeveelheid brandbare componenten,
Volgens de berekeningsmethode voor een mengsel dat n brandbare gassen en p inerte gassen bevat, kan worden vastgesteld dat het laagwaardige gemengde uitlaatgas van brandbare en inerte gassen niet brandbaar en niet explosief is.<\/p>\n
Daarom heeft het uitlaatgas van methanolwassing bij lage temperaturen geen bovenste of onderste explosiegrenzen.
De hoeveelheid luchtverversing voor het rookgas dat bij het wassen van methanol op lage temperatuur wordt gebruikt, kan worden bepaald op basis van het zuurstofgehalte van het rookgas na volledige oxidatie, dat groter is dan 3%.<\/p>\n
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Berekeningsproces van de brandbaarheid van gemengd uitlaatgas in de lucht\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
Het gemengde rookgas is ontworpen voor zuurstofsuppletie op basis van materiaalbalans, met een zuurstofgehalte van ongeveer 5% in het rookgas<\/p>\n
Vergelijking tussen de concentratie van brandbare componenten in uitlaatgas na zuurstofsuppletie en de onderste explosiegrens van uitlaatgas (exclusief inerte gassen)<\/p>\n
<\/p>\n
Verwerking van het totale luchtvolume<\/strong><\/h4>\n1) Laag uitlaatgasvolume<\/em><\/strong>
2) Luchtvolume voor zuurstofsuppletie<\/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 Materiaalbalans<\/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 Warmtebalans<\/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 technische cases<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Situatieanalyse<\/h3>\n
De methanolinstallatie van Xinye Energy Chemical met een capaciteit van 525.000 ton\/jaar maakt gebruik van vergassingstechnologie met gebroken steenkool onder druk. Naast de hoofdcomponenten CO\u2082 en N\u2082 bevat de rookgasreiniging met lage temperatuur methanol ook methaan, niet-methaan totale koolwaterstoffen, CO\u2082, methanol, enz. Deze rookgassen worden momenteel via de ketelschoorsteen afgevoerd. Volgens de milieueisen is een behandeling voor de verwijdering van vluchtige organische stoffen (VOS) vereist. Daarnaast heeft de polyoxymethyleeninstallatie ook drie rookgassen die behandeld moeten worden.<\/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
Procesroute<\/h3>\n
Op basis van de kenmerken van brandbare componenten in uitlaatgassen hebben onze ingenieurs besloten om de behandelingstechnologie van "RTO-zuivering + middeldruk stoomafvalwarmteketel voor warmteterugwinning" te gebruiken. Volgens het unieke "Le Chater & Inert Gas Correction Theory Safety Air Distribution Algorithm" van ons bedrijf hebben we besloten om een RTO-roterende klep met een luchtvolume van 270.000 te selecteren, met een zuurstofgehalte van 5% in het uitlaatgas na verbranding. Tegelijkertijd hebben we een stoomketel van 5,1 MPa\/46 T geselecteerd met een schoorsteenontwerp van 120 meter aan het uiteinde om de impact van uitlaatgassen op de fabrieksomgeving te verminderen.<\/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
Het hoofdapparaat maakt gebruik van een enkele roterende klep RTO met een luchtvolume van 270.000, vierkante indeling, uitgerust met 3 roterende luchtverdelingskleppen en 36 warmteopslagkamers<\/p>\n
\n- Uitgebreide behandeling:<\/strong>
Uitgerust met een roterende RTO met een luchtvolume van 270.000, polyoxymethyleen-staartgas gemengd met lucht voor zuurstoftoevoeging
Benutting van restwarmte: 46 t\/u, 5,1 MPa verzadigde stoom
<\/strong><\/li>\n- Milieubeschermingsnormen:<\/strong>
totale koolwaterstofemissies anders dan methaan <50mg\/m\u00b3, jaarlijkse vermindering van de koolstofemissie van ongeveer 860.000 ton;
<\/strong><\/li>\n- Terugverdientijd:<\/strong> 3 jaar<\/li>\n<\/ul>\n
![\"RTO-ZAAK](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-3.webp\" "\\"\\"")
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Veiligheidsanalyse<\/h3>\n\n- Complexe controle\/ketenbriefing<\/li>\n
- HAZOP-analyse<\/li>\n
- SIL-classificatie<\/li>\n<\/ol>\n
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Innovatie 1 \u2013 Doorbraak in de onderste explosiegrens onder inerte omstandigheden<\/h3>\n
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125.000 v\u00f3\u00f3r luchtdistributie<\/strong><\/h4>\n\n\n\nBerekening van de explosiegrenzen van het brandbare deel van een mengsel<\/td>\n<\/tr>\n \nFormule van Richard Chateli: Lf=100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \nExplosiegrens van gemengd gas Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \nTotale concentratie van brandbare componenten<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\nConventionele luchtverdeling: De concentratie van brandbare componenten wordt teruggebracht tot <1,065, wat betekent dat de luchtverdeling 2,6 keer moet zijn en het totale luchtvolume 330.000 bedraagt.<\/p>\n
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Houd rekening met het effect van inert gas op de onderste explosiegrens<\/strong><\/h4>\n![\"RTO-ZAAK\"](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-4.webp\" "\\"\\"")
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Als we alleen de zuurstoftoevoer in ogenschouw nemen, bedraagt de luchttoevoer 100.000 en het totale luchtvolume 220.000.<\/p>\n
1. Lucht achtergrond, de onderste explosiegrens bij 900\u2103 is 25%LEL;
2. Inerte achtergrond, niet ontvlambaar en niet explosief bij kamertemperatuur, maar bij hoge temperatuur?<\/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
Innovatie 2 - Ontwerp en toepassing van vierkante RTO-structuur met groot luchtvolume<\/h3>\n
![\"RTO-ZAAK\"](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-5.webp\" "\\"\\"")
<\/p>\n
<\/p>\n
\n\n\n\nPrestatieparameters<\/td>\n Roterende klep RTO<\/td>\n Liftklep RTO<\/td>\n<\/tr>\n \nLuchtvolume<\/td>\n 300.000 Nm\u00b3\/u<\/td>\n 300.000 Nm\u00b3\/u<\/td>\n<\/tr>\n \nRichtingsklepstructuur<\/td>\n Roterende klep<\/td>\n Liftklep<\/td>\n<\/tr>\n \nAantal omkeerkleppen<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \nFrequentie van de omkeerklep-schakelschok<\/td>\n Continue werking zonder schokken<\/td>\n 6,48 miljoen keer\/jaar<\/td>\n<\/tr>\n \nAantal warmteopslagbedden<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \nLuchtvolume per kamer<\/td>\n 20000 Nm\u00b3\/u<\/td>\n 75000 Nm\u00b3\/u<\/td>\n<\/tr>\n \nDwarsdoorsnede van een enkele warmteopslagkamer<\/td>\n 3\u33a1<\/td>\n 14\u33a1<\/td>\n<\/tr>\n \nVulgewicht van eenkamer warmteopslagkeramiek<\/td>\n 3300 kg<\/td>\n 15600 kg<\/td>\n<\/tr>\n \nAantal branders (stuks)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \nBezetting (lengte*breedte)<\/td>\n 26m\u00d78m<\/td>\n 48m\u00d75m<\/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 Belangrijkste technische indicatoren voor milieubescherming<\/strong><\/p>\n\n\n\n\nParameternaam<\/td>\n Gegevens<\/td>\n<\/tr>\n \nLaagmethaan uitlaatgas\/10.000 m\u00b3\/u<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \nZuurstofsupplement lucht\/10.000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \nZuurstofgehalte van rookgas bij lage temperaturen%<\/td>\n 5<\/td>\n<\/tr>\n \nOventemperatuur\u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \nUitlaatstikstofoxiden mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \nUitlaat niet-methaan totale koolwaterstoffen 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 Belangrijkste economische indicatoren<\/strong><\/p>\n\n\n\n\nParameternaam<\/td>\n Gegevens<\/td>\n<\/tr>\n \nGe\u00efnstalleerd vermogensverdelingsvermogen<\/td>\n 1200 kW\/u<\/td>\n<\/tr>\n \nElektriciteitskosten<\/td>\n 4,8 miljoen yuan\/jaar<\/td>\n<\/tr>\n \nStoomproductie van afvalwarmteketel<\/td>\n 45t\/u<\/td>\n<\/tr>\n \nStoomparameters<\/td>\n 4,9 MPa, 420\u2103<\/td>\n<\/tr>\n \nSteam-prijs<\/td>\n 120 yuan\/t<\/td>\n<\/tr>\n \nDirecte economische voordelen<\/td>\n 43,2 miljoen yuan\/jaar<\/td>\n<\/tr>\n \nVermindering van het verbruik van ruwe steenkool<\/td>\n 50.000 ton\/jaar<\/td>\n<\/tr>\n \nVermindering van de koolstofuitstoot<\/td>\n 860.000 ton\/jaar<\/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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Vergassing van steenkool: verwijst naar een onvolledige reactie tussen verschillende soorten steenkool (cokes) en zuurstofdragende vergassers (H\u2082O, O\u2082, CO\u2082) in een vergasser. Onder hoge temperatuur en een bepaalde druk ontstaat uiteindelijk ruw steenkoolgas, bestaande uit H\u2082, CH\u2082, CO, CO\u2082, N\u2082, sporen H\u2082S, CO\u2082, enz.<\/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
Classificatie van steenkoolvergassingsprocessen:<\/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 Methanolwasproces bij lage temperaturen: koude methanol wordt gebruikt als absorptiemiddel, waarbij gebruik wordt gemaakt van de hoge oplosbaarheid van methanol in zure gassen bij lage temperaturen, om zure gassen uit het toevoergas te verwijderen, voornamelijk CO2 en 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=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\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 Kenmerken van uitlaatgassen van methanolwassing op lage temperatuur:<\/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 Omdat de uitlaatgassen vrijwel geen zuurstof bevatten, is het noodzakelijk om de uitlaatgassen aan te vullen met lucht om aan de zuurstofbehoefte te voldoen voor een volledige oxidatie van de uitlaatgassen. 1) Veiligheidsoverwegingen: analyse van explosiegevaar<\/strong><\/em><\/p>\n Volgens de technische specificatie voor de behandeling van industrieel organisch afvalgas met behulp van thermische opslagverbranding moet de concentratie organisch materiaal dat het RTO-apparaat binnenkomt, lager zijn dan 25% van de onderste explosiegrens. Bereken de onderste explosiegrens van complexe brandbare gasmengsels met behulp van de Le-Chatlier-formule en vergelijk vervolgens de concentratie brandbare componenten in het rookgas met de grootte van 25% LEL om de veiligheid van de concentratie brandbare componenten in het rookgas te bepalen.<\/p>\n 2) Overwegingen met betrekking tot de zuiveringssnelheid: \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=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d]<\/p>\n Meestal ontworpen zonder rekening te houden met de invloed van inerte gassen, wordt de onderste explosiegrens van het uitlaatgas berekend en de luchtverdunningsverhouding bepaald op basis van de verhouding tussen de uitlaatgasconcentratie en de 25% LEL. Deze berekening kan intrinsieke veiligheid garanderen, maar het uitlaatgasvolume is relatief groot.<\/p>\n Vanwege de aanwezigheid van een grote hoeveelheid inert gas CO2 in het uitlaatgas N2 van de methanolwas bij lage temperaturen, een kleine hoeveelheid brandbare componenten, Daarom heeft het uitlaatgas van methanolwassing bij lage temperaturen geen bovenste of onderste explosiegrenzen. [\/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 Het gemengde rookgas is ontworpen voor zuurstofsuppletie op basis van materiaalbalans, met een zuurstofgehalte van ongeveer 5% in het rookgas<\/p>\n Vergelijking tussen de concentratie van brandbare componenten in uitlaatgas na zuurstofsuppletie en de onderste explosiegrens van uitlaatgas (exclusief inerte gassen)<\/p>\n <\/p>\n 1) Laag uitlaatgasvolume<\/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=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dstandaard\u201d global_colors_info=\u201d{}\u201d]<\/p>\n De methanolinstallatie van Xinye Energy Chemical met een capaciteit van 525.000 ton\/jaar maakt gebruik van vergassingstechnologie met gebroken steenkool onder druk. Naast de hoofdcomponenten CO\u2082 en N\u2082 bevat de rookgasreiniging met lage temperatuur methanol ook methaan, niet-methaan totale koolwaterstoffen, CO\u2082, methanol, enz. Deze rookgassen worden momenteel via de ketelschoorsteen afgevoerd. Volgens de milieueisen is een behandeling voor de verwijdering van vluchtige organische stoffen (VOS) vereist. Daarnaast heeft de polyoxymethyleeninstallatie ook drie rookgassen die behandeld moeten worden.<\/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 Op basis van de kenmerken van brandbare componenten in uitlaatgassen hebben onze ingenieurs besloten om de behandelingstechnologie van "RTO-zuivering + middeldruk stoomafvalwarmteketel voor warmteterugwinning" te gebruiken. Volgens het unieke "Le Chater & Inert Gas Correction Theory Safety Air Distribution Algorithm" van ons bedrijf hebben we besloten om een RTO-roterende klep met een luchtvolume van 270.000 te selecteren, met een zuurstofgehalte van 5% in het uitlaatgas na verbranding. Tegelijkertijd hebben we een stoomketel van 5,1 MPa\/46 T geselecteerd met een schoorsteenontwerp van 120 meter aan het uiteinde om de impact van uitlaatgassen op de fabrieksomgeving te verminderen.<\/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 Het hoofdapparaat maakt gebruik van een enkele roterende klep RTO met een luchtvolume van 270.000, vierkante indeling, uitgerust met 3 roterende luchtverdelingskleppen en 36 warmteopslagkamers<\/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 Conventionele luchtverdeling: De concentratie van brandbare componenten wordt teruggebracht tot <1,065, wat betekent dat de luchtverdeling 2,6 keer moet zijn en het totale luchtvolume 330.000 bedraagt.<\/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 Als we alleen de zuurstoftoevoer in ogenschouw nemen, bedraagt de luchttoevoer 100.000 en het totale luchtvolume 220.000.<\/p>\n 1. Lucht achtergrond, de onderste explosiegrens bij 900\u2103 is 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 Belangrijkste technische indicatoren voor milieubescherming<\/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 Belangrijkste economische indicatoren<\/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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Overzichtstabel van ruwe gascomponenten geproduceerd door verschillende vergassingsprocessen<\/strong><\/h2>\n
Wat is lagetemperatuurmethanolwas?<\/strong><\/h2>\n
Methanolwassen bij lage temperatuur is een methode die begin jaren vijftig gezamenlijk door Linde en Lurgi is ontwikkeld om zure gassen uit grondstofgassen te verwijderen. In 1954 werd het voor het eerst gebruikt voor gaszuivering in de Zuid-Afrikaanse kolenvergassingsindustrie.
<\/strong><\/p>\n\n
Afgaseigenschappen<\/strong><\/h2>\n
\n
Bepaling van het zuurstofsuppletieluchtvolume<\/strong><\/h2>\n
Principe voor het bepalen van de hoeveelheid extra lucht:<\/p>\n\n
Volgens de berekeningsmethode voor een mengsel dat n brandbare gassen en p inerte gassen bevat, kan worden vastgesteld dat het laagwaardige gemengde uitlaatgas van brandbare en inerte gassen niet brandbaar en niet explosief is.<\/p>\n
De hoeveelheid luchtverversing voor het rookgas dat bij het wassen van methanol op lage temperatuur wordt gebruikt, kan worden bepaald op basis van het zuurstofgehalte van het rookgas na volledige oxidatie, dat groter is dan 3%.<\/p>\nBerekeningsproces van de brandbaarheid van gemengd uitlaatgas in de lucht\u00a0<\/h3>\n
Verwerking van het totale luchtvolume<\/strong><\/h4>\n
2) Luchtvolume voor zuurstofsuppletie<\/em><\/strong><\/p>\n\u2460 Materiaalbalans<\/strong><\/h2>\n
\u00a0\u2461 Warmtebalans<\/strong><\/h2>\n
Typische technische cases<\/strong><\/h2>\n
Situatieanalyse<\/h3>\n
Procesroute<\/h3>\n
\n
Uitgerust met een roterende RTO met een luchtvolume van 270.000, polyoxymethyleen-staartgas gemengd met lucht voor zuurstoftoevoeging
Benutting van restwarmte: 46 t\/u, 5,1 MPa verzadigde stoom
<\/strong><\/li>\n
totale koolwaterstofemissies anders dan methaan <50mg\/m\u00b3, jaarlijkse vermindering van de koolstofemissie van ongeveer 860.000 ton;
<\/strong><\/li>\n<\/p>\nVeiligheidsanalyse<\/h3>\n
\n
Innovatie 1 \u2013 Doorbraak in de onderste explosiegrens onder inerte omstandigheden<\/h3>\n
125.000 v\u00f3\u00f3r luchtdistributie<\/strong><\/h4>\n
\n\n
\n Berekening van de explosiegrenzen van het brandbare deel van een mengsel<\/td>\n<\/tr>\n \n Formule van Richard Chateli: Lf=100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \n Explosiegrens van gemengd gas Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n 25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \n Totale concentratie van brandbare componenten<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n Houd rekening met het effect van inert gas op de onderste explosiegrens<\/strong><\/h4>\n
<\/p>\n
2. Inerte achtergrond, niet ontvlambaar en niet explosief bij kamertemperatuur, maar bij hoge temperatuur?<\/p>\nInnovatie 2 - Ontwerp en toepassing van vierkante RTO-structuur met groot luchtvolume<\/h3>\n
<\/p>\n\n\n
\n Prestatieparameters<\/td>\n Roterende klep RTO<\/td>\n Liftklep RTO<\/td>\n<\/tr>\n \n Luchtvolume<\/td>\n 300.000 Nm\u00b3\/u<\/td>\n 300.000 Nm\u00b3\/u<\/td>\n<\/tr>\n \n Richtingsklepstructuur<\/td>\n Roterende klep<\/td>\n Liftklep<\/td>\n<\/tr>\n \n Aantal omkeerkleppen<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \n Frequentie van de omkeerklep-schakelschok<\/td>\n Continue werking zonder schokken<\/td>\n 6,48 miljoen keer\/jaar<\/td>\n<\/tr>\n \n Aantal warmteopslagbedden<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \n Luchtvolume per kamer<\/td>\n 20000 Nm\u00b3\/u<\/td>\n 75000 Nm\u00b3\/u<\/td>\n<\/tr>\n \n Dwarsdoorsnede van een enkele warmteopslagkamer<\/td>\n 3\u33a1<\/td>\n 14\u33a1<\/td>\n<\/tr>\n \n Vulgewicht van eenkamer warmteopslagkeramiek<\/td>\n 3300 kg<\/td>\n 15600 kg<\/td>\n<\/tr>\n \n Aantal branders (stuks)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \n Bezetting (lengte*breedte)<\/td>\n 26m\u00d78m<\/td>\n 48m\u00d75m<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n \n\n
\n Parameternaam<\/td>\n Gegevens<\/td>\n<\/tr>\n \n Laagmethaan uitlaatgas\/10.000 m\u00b3\/u<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \n Zuurstofsupplement lucht\/10.000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \n Zuurstofgehalte van rookgas bij lage temperaturen%<\/td>\n 5<\/td>\n<\/tr>\n \n Oventemperatuur\u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \n Uitlaatstikstofoxiden mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \n Uitlaat niet-methaan totale koolwaterstoffen mg\/m\u00b3<\/td>\n 40-60<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n \n\n
\n Parameternaam<\/td>\n Gegevens<\/td>\n<\/tr>\n \n Ge\u00efnstalleerd vermogensverdelingsvermogen<\/td>\n 1200 kW\/u<\/td>\n<\/tr>\n \n Elektriciteitskosten<\/td>\n 4,8 miljoen yuan\/jaar<\/td>\n<\/tr>\n \n Stoomproductie van afvalwarmteketel<\/td>\n 45t\/u<\/td>\n<\/tr>\n \n Stoomparameters<\/td>\n 4,9 MPa, 420\u2103<\/td>\n<\/tr>\n \n Steam-prijs<\/td>\n 120 yuan\/t<\/td>\n<\/tr>\n \n Directe economische voordelen<\/td>\n 43,2 miljoen yuan\/jaar<\/td>\n<\/tr>\n \n Vermindering van het verbruik van ruwe steenkool<\/td>\n 50.000 ton\/jaar<\/td>\n<\/tr>\n \n Vermindering van de koolstofuitstoot<\/td>\n 860.000 ton\/jaar<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n