[\/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
\u010co je sply\u0148ovanie uhlia<\/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
Sply\u0148ovanie uhlia je z\u00e1kladnou technol\u00f3giou modern\u00e9ho uho\u013en\u00e9ho chemick\u00e9ho priemyslu.<\/strong><\/p>\nSply\u0148ovanie uhlia: ozna\u010duje ne\u00fapln\u00fa reakciu medzi r\u00f4znymi druhmi uhlia (koks) a sply\u0148ovac\u00edmi \u010dinidlami pren\u00e1\u0161aj\u00facimi kysl\u00edk (H2O, O2, CO2) v sply\u0148ova\u010di. Pri vysokej teplote a ur\u010ditom tlaku sa nakoniec vytv\u00e1ra surov\u00fd uho\u013en\u00fd plyn zlo\u017een\u00fd z H2, CH4, CO, CO2, N2, stopov\u00fdch mno\u017estiev H2S, COS at\u010f.<\/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
Klasifik\u00e1cia procesov sply\u0148ovania uhlia:<\/strong><\/p>\n\n- Suroviny: pr\u00e1\u0161kov\u00e9 uhlie, drven\u00e9 uhlie, uho\u013en\u00e1 vodn\u00e1 suspenzia;<\/li>\n
- Sply\u0148ovacie l\u00f4\u017eko: fluidn\u00e9 l\u00f4\u017eko, fluidn\u00e1 vrstva, pevn\u00e1 vrstva;\n<\/li>\n
- Pevn\u00e9 l\u00f4\u017eko je vyroben\u00e9 z kusov\u00e9ho uhlia (15-50 mm) ako suroviny;<\/li>\n
- Fluidn\u00e9 l\u00f4\u017eko je vyroben\u00e9 z drven\u00e9ho uhlia (menej ako 10 mm) ako suroviny;<\/li>\n
- Vzduchov\u00e9 l\u00f4\u017eko je vyroben\u00e9 z pr\u00e1\u0161kov\u00e9ho uhlia (menej ako 0,1 mm) ako suroviny;\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
Preh\u013eadov\u00e1 tabu\u013eka zlo\u017eiek surov\u00e9ho plynu vyroben\u00fdch r\u00f4znymi procesmi sply\u0148ovania<\/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
\u010co je to n\u00edzkoteplotn\u00e9 metanolov\u00e9 pranie<\/strong><\/h2>\nProces prem\u00fdvania metanolom pri n\u00edzkej teplote: pou\u017eitie studen\u00e9ho metanolu ako absorp\u010dn\u00e9ho rozp\u00fa\u0161\u0165adla s vyu\u017eit\u00edm vysokej rozpustnosti metanolu v kysl\u00fdch plynoch pri n\u00edzkych teplot\u00e1ch na odstr\u00e1nenie kysl\u00fdch plynov, najm\u00e4 CO2 a H2S, zo vstupn\u00e9ho plynu.
N\u00edzkoteplotn\u00e9 pranie metanolom je met\u00f3da, ktor\u00fa spolo\u010dne vyvinuli spolo\u010dnosti Linde a Lurgi za\u010diatkom 50. rokov 20. storo\u010dia na odstr\u00e1nenie kysl\u00fdch plynov zo surov\u00edn. V roku 1954 bola prv\u00fdkr\u00e1t pou\u017eit\u00e1 na \u010distenie plynu v priemysle tlakov\u00e9ho sply\u0148ovania uhlia v Ju\u017enej Afrike.
<\/strong><\/p>\n <\/p>\n
\n- Medzi poskytovate\u013eov bal\u00edkov na n\u00edzkoteplotn\u00e9 pranie metanolom patria Linde, Lurgi, Dalian University of Technology at\u010f.;<\/li>\n
- Existuj\u00fa r\u00f4zne procesy sply\u0148ovania, ktor\u00e9 mo\u017eno rozdeli\u0165 do troch kateg\u00f3ri\u00ed: s pevn\u00fdm l\u00f4\u017ekom, fluidn\u00fdm l\u00f4\u017ekom a fluidn\u00fdm l\u00f4\u017ekom;<\/li>\n
- Pri ur\u010dovan\u00ed, \u010di m\u00e1 n\u00edzkoemisn\u00fd plyn hodnotu sp\u00e4tn\u00e9ho z\u00edskavania zvy\u0161kov\u00e9ho tepla, sa zoh\u013ead\u0148uje najm\u00e4 obsah CH4 vo v\u00fdfukov\u00fdch plynoch;<\/li>\n
- Koncentr\u00e1cia CH4 z\u00e1vis\u00ed od procesu sply\u0148ovania a medzi procesy sply\u0148ovania s pevn\u00fdm l\u00f4\u017ekom patr\u00ed Lurgiho pec, pec BGL at\u010f.;<\/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=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Vlastnosti odpadov\u00fdch plynov<\/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
Charakteristiky v\u00fdfukov\u00fdch plynov z n\u00edzkoteplotn\u00e9ho prania metanolom:<\/p>\n
\n- V\u00fdfukov\u00e9 plyny s\u00fa v podstate nas\u00fdten\u00e9 vodnou parou<\/li>\n
- Vysok\u00fd obsah inertn\u00fdch zlo\u017eiek CO2 a N2<\/li>\n
- V\u00fdfukov\u00e9 plyny v podstate neobsahuj\u00fa kysl\u00edk<\/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
Stanovenie objemu vzduchu dop\u013a\u0148an\u00e9ho kysl\u00edkom<\/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
Vzh\u013eadom na to, \u017ee v\u00fdfukov\u00e9 plyny neobsahuj\u00fa takmer \u017eiadny kysl\u00edk, je potrebn\u00e9 doplni\u0165 v\u00fdfukov\u00e9 plyny vzduchom, aby sa splnila potreba kysl\u00edka pre \u00fapln\u00fa oxid\u00e1ciu v\u00fdfukov\u00fdch plynov.
Princ\u00edp ur\u010denia mno\u017estva dodato\u010dn\u00e9ho vzduchu:<\/p>\n
1) Bezpe\u010dnostn\u00e9 aspekty: anal\u00fdza nebezpe\u010denstva v\u00fdbuchu<\/strong><\/em><\/p>\nPod\u013ea technickej \u0161pecifik\u00e1cie pre spracovanie priemyseln\u00fdch organick\u00fdch odpadov\u00fdch plynov met\u00f3dou tepeln\u00e9ho akumula\u010dn\u00e9ho spa\u013eovania by koncentr\u00e1cia organickej hmoty vstupuj\u00facej do zariadenia RTO mala by\u0165 ni\u017e\u0161ia ako 25% dolnej medze v\u00fdbu\u0161nosti. Vypo\u010d\u00edtajte doln\u00fa medzu v\u00fdbu\u0161nosti komplexn\u00fdch hor\u013eav\u00fdch zmes\u00ed plynov pomocou Le Chatlierovej rovnice a potom porovnajte koncentr\u00e1ciu hor\u013eav\u00fdch zlo\u017eiek vo v\u00fdfukov\u00fdch plynoch s ve\u013ekos\u0165ou 25% LEL, aby ste ur\u010dili bezpe\u010dnos\u0165 koncentr\u00e1cie hor\u013eav\u00fdch zlo\u017eiek vo v\u00fdfukov\u00fdch plynoch.<\/p>\n
2) \u00davahy o r\u00fdchlosti \u010distenia: \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 je doln\u00e1 medza v\u00fdbu\u0161nosti zmesi plynov, %<\/li>\n
- Li je doln\u00e1 medza v\u00fdbu\u0161nosti zlo\u017eky i,%<\/li>\n
- Vi je objemov\u00fd podiel ur\u010ditej hor\u013eavej zlo\u017eky k hor\u013eavej zlo\u017eke,%<\/li>\n<\/ul>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Zvy\u010dajne sa navrhuj\u00fa bez zoh\u013eadnenia vplyvu inertn\u00fdch plynov, doln\u00e1 medza v\u00fdbu\u0161nosti v\u00fdfukov\u00fdch plynov sa vypo\u010d\u00edta a pomer riedenia vzduchu sa ur\u010d\u00ed na z\u00e1klade vz\u0165ahu medzi koncentr\u00e1ciou v\u00fdfukov\u00fdch plynov a limitom v\u00fdbu\u0161nosti 25% LEL. Tento v\u00fdpo\u010det m\u00f4\u017ee zaru\u010di\u0165 vn\u00fatorn\u00fa bezpe\u010dnos\u0165, ale objem v\u00fdfukov\u00fdch plynov je relat\u00edvne ve\u013ek\u00fd.<\/p>\n
Vzh\u013eadom na pr\u00edtomnos\u0165 ve\u013ek\u00e9ho mno\u017estva inertn\u00e9ho plynu CO2 vo v\u00fdfukovom plyne N2 z n\u00edzkoteplotn\u00e9ho prania metanolom, mal\u00e9ho mno\u017estva hor\u013eav\u00fdch zlo\u017eiek,
Pod\u013ea v\u00fdpo\u010dtovej met\u00f3dy pre zmes obsahuj\u00facu n hor\u013eav\u00fdch plynov a p inertn\u00fdch plynov mo\u017eno ur\u010di\u0165, \u017ee n\u00edzkokvalitn\u00fd zmie\u0161an\u00fd v\u00fdfukov\u00fd plyn hor\u013eav\u00fdch a inertn\u00fdch plynov je nehor\u013eav\u00fd a nev\u00fdbu\u0161n\u00fd.<\/p>\n
Preto v\u00fdfukov\u00fd plyn z n\u00edzkoteplotn\u00e9ho prania metanolom nem\u00e1 horn\u00fa ani doln\u00fa medzu v\u00fdbu\u0161nosti.
Mno\u017estvo dop\u013a\u0148an\u00e9ho vzduchu pre odpadov\u00fd plyn z n\u00edzkoteplotn\u00e9ho prania metanolom mo\u017eno ur\u010di\u0165 na z\u00e1klade obsahu kysl\u00edka v spalin\u00e1ch po \u00faplnej oxid\u00e1cii, ktor\u00fd je vy\u0161\u0161\u00ed ako 3%.<\/p>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” custom_margin=”|auto|14px|auto||” custom_padding=”||62px|||” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n
Proces v\u00fdpo\u010dtu hor\u013eavosti zmesi v\u00fdfukov\u00fdch plynov vo vzduchu\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
Zmes v\u00fdfukov\u00fdch plynov je navrhnut\u00e1 na doplnenie kysl\u00edka na z\u00e1klade materi\u00e1lovej bilancie s obsahom kysl\u00edka v spalin\u00e1ch okolo 5%.<\/p>\n
Porovnanie koncentr\u00e1cie hor\u013eav\u00fdch zlo\u017eiek vo v\u00fdfukov\u00fdch plynoch po doplnen\u00ed kysl\u00edka a dolnej medze v\u00fdbu\u0161nosti v\u00fdfukov\u00fdch plynov (okrem inertn\u00fdch plynov)<\/p>\n
<\/p>\n
Spracovanie celkov\u00e9ho objemu vzduchu<\/strong><\/h4>\n1) N\u00edzky objem v\u00fdfukov\u00fdch plynov<\/em><\/strong>
2) Objem vzduchu na doplnenie kysl\u00edka<\/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 Materi\u00e1lov\u00e1 bilancia<\/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 Tepeln\u00e1 bilancia<\/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
Typick\u00e9 in\u017einierske pr\u00edpady<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Anal\u00fdza situ\u00e1cie<\/h3>\n
Metanolov\u00e1 jednotka spolo\u010dnosti Xinye Energy Chemical s kapacitou 525 000 ton\/rok vyu\u017e\u00edva technol\u00f3giu tlakov\u00e9ho sply\u0148ovania drven\u00e9ho uhlia. Okrem hlavn\u00fdch zlo\u017eiek CO2 a N2 obsahuje n\u00edzkoteplotn\u00fd odpadov\u00fd plyn z preplachovania metanolom aj met\u00e1n, celkov\u00e9 nemet\u00e1nov\u00e9 uh\u013eovod\u00edky, CO, metanol at\u010f. Tento odpadov\u00fd plyn sa v s\u00fa\u010dasnosti vyp\u00fa\u0161\u0165a cez kom\u00edn kotla. Pod\u013ea po\u017eiadaviek ochrany \u017eivotn\u00e9ho prostredia je potrebn\u00e9 odstr\u00e1ni\u0165 prchav\u00e9 organick\u00e9 zl\u00fa\u010denia (VOC). Okrem toho polyoxymetyl\u00e9nov\u00e1 jednotka obsahuje aj tri odpadov\u00e9 plyny, ktor\u00e9 je potrebn\u00e9 \u010disti\u0165.<\/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
Procesn\u00e1 trasa<\/h3>\n
Na z\u00e1klade charakterist\u00edk hor\u013eav\u00fdch zlo\u017eiek vo v\u00fdfukov\u00fdch plynoch sa na\u0161i in\u017einieri rozhodli pre technologick\u00fa cestu \u00fapravy \u201e\u010distenie RTO + strednotlakov\u00fd parn\u00fd kotol na odpadov\u00e9 teplo na sp\u00e4tn\u00e9 z\u00edskavanie tepla\u201c. Pod\u013ea jedine\u010dn\u00e9ho \u201eLe Chater & Inert Gas Correction Theory Safety Air Distribution Algorithm\u201c na\u0161ej spolo\u010dnosti sme sa rozhodli zvoli\u0165 RTO s rota\u010dn\u00fdm ventilom s objemom vzduchu 270 000 a obsahom kysl\u00edka 5% vo v\u00fdfukov\u00fdch plynoch po sp\u00e1len\u00ed. S\u00fa\u010dasne sme zvolili parn\u00fd kotol s tlakom 5,1 MPa\/46T a kon\u0161trukciou 120 metrov\u00e9ho koncov\u00e9ho kom\u00edna, aby sa zn\u00ed\u017eil vplyv v\u00fdfukov\u00fdch emisi\u00ed na \u017eivotn\u00e9 prostredie v tov\u00e1rni.<\/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
Hlavn\u00e9 zariadenie vyu\u017e\u00edva jeden rota\u010dn\u00fd ventil RTO s objemom vzduchu 270 000 kJ, \u0161tvorcov\u00e9 usporiadanie, vybaven\u00fd 3 rota\u010dn\u00fdmi ventilmi na rozde\u013eovanie vzduchu a 36 komorami na akumul\u00e1ciu tepla.<\/p>\n
\n- Komplexn\u00e1 lie\u010dba:<\/strong>
Vybaven\u00fd rota\u010dn\u00fdm RTO s objemom vzduchu 270 000, polyoxymetyl\u00e9nov\u00fd koncov\u00fd plyn zmie\u0161an\u00fd so vzduchom ako doplnok kysl\u00edka
Vyu\u017eitie odpadov\u00e9ho tepla: 46 t\/h, nas\u00fdten\u00e1 para 5,1 MPa
<\/strong><\/li>\n- Normy ochrany \u017eivotn\u00e9ho prostredia:<\/strong>
celkov\u00e9 emisie nemet\u00e1nov\u00fdch uh\u013eovod\u00edkov <50 mg\/m\u00b3, ro\u010dn\u00e9 zn\u00ed\u017eenie emisi\u00ed uhl\u00edka pribli\u017ene o 860 000 ton;
<\/strong><\/li>\n- Doba n\u00e1vratnosti:<\/strong> 3 roky<\/li>\n<\/ul>\n
![\"PR\u00cdPAD](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-3.webp\" "\\"\\"")
<\/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
Anal\u00fdza bezpe\u010dnosti<\/h3>\n\n- Br\u00edfing komplexn\u00e9ho riadenia\/re\u0165azca<\/li>\n
- Anal\u00fdza HAZOP<\/li>\n
- Hodnotenie SIL<\/li>\n<\/ol>\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
Inov\u00e1cia 1 \u2013 Prielom v dolnej medzi v\u00fdbu\u0161nosti za inertn\u00fdch podmienok<\/h3>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” column_structure=”1_2,1_2″][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n
125 000 pred rozvodom vzduchu<\/strong><\/h4>\n\n\n\nV\u00fdpo\u010det medz\u00ed v\u00fdbu\u0161nosti hor\u013eavej zlo\u017eky zmesi<\/td>\n<\/tr>\n \nVzorec Richarda Chateliho: Lf=100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \nMedza v\u00fdbu\u0161nosti zmesi plynov Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \nCelkov\u00e1 koncentr\u00e1cia hor\u013eav\u00fdch zlo\u017eiek<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\nKonven\u010dn\u00e1 distrib\u00facia vzduchu: Koncentr\u00e1cia hor\u013eav\u00fdch zlo\u017eiek sa zn\u00ed\u017ei na <1,065, \u010do znamen\u00e1, \u017ee distrib\u00facia vzduchu mus\u00ed by\u0165 2,6-kr\u00e1t v\u00e4\u010d\u0161ia a celkov\u00fd objem vzduchu dosiahne 330 000.<\/p>\n
[\/et_pb_text][\/et_pb_column][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n
Zv\u00e1\u017ete vplyv inertn\u00e9ho plynu na doln\u00fa medzu v\u00fdbu\u0161nosti<\/strong><\/h4>\n![\"PR\u00cdPAD](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-4.webp\" "\\"\\"")
<\/p>\n
Ak vezmeme do \u00favahy iba pr\u00edvod kysl\u00edka, pr\u00edvod vzduchu je 100 000 a celkov\u00fd objem vzduchu je 220 000.<\/p>\n
1. Vzdu\u0161n\u00e9 pozadie, doln\u00e1 medza v\u00fdbu\u0161nosti pri 900 \u2103 je 25%LEL;
2. Inertn\u00e9 pozadie, nehor\u013eav\u00e9 a nev\u00fdbu\u0161n\u00e9 pri izbovej teplote, ale pri vysokej teplote?<\/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
Inov\u00e1cia 2 \u2013 N\u00e1vrh a aplik\u00e1cia \u0161tvorcovej \u0161trukt\u00fary RTO s ve\u013ek\u00fdm objemom vzduchu<\/h3>\n
![\"PR\u00cdPAD](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-5.webp\" "\\"\\"")
<\/p>\n
<\/p>\n
\n\n\n\nV\u00fdkonnostn\u00e9 parametre<\/td>\n Rota\u010dn\u00fd ventil RTO<\/td>\n Zdv\u00edhac\u00ed ventil RTO<\/td>\n<\/tr>\n \nObjem vzduchu<\/td>\n 300 000 Nm\u00b3\/h<\/td>\n 300 000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n\u0160trukt\u00fara smerov\u00e9ho ventilu<\/td>\n Rota\u010dn\u00fd ventil<\/td>\n Zdv\u00edhac\u00ed ventil<\/td>\n<\/tr>\n \nPo\u010det reverzn\u00fdch ventilov<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \nFrekvencia \u0161okov pri prep\u00ednan\u00ed reverzn\u00e9ho ventilu<\/td>\n Nepretr\u017eit\u00e1 prev\u00e1dzka bez otrasov<\/td>\n 6,48 mili\u00f3na kr\u00e1t\/rok<\/td>\n<\/tr>\n \nPo\u010det akumula\u010dn\u00fdch l\u00f4\u017eok<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \nObjem vzduchu na komoru<\/td>\n 20 000 Nm\u00b3\/h<\/td>\n 75 000 Nm\u00b3\/h<\/td>\n<\/tr>\n \nPrierezov\u00e1 plocha jednej akumula\u010dnej komory tepla<\/td>\n 3\u33a1<\/td>\n 14\u33a1<\/td>\n<\/tr>\n \nPlniaca hmotnos\u0165 jednokomorovej keramickej akumul\u00e1cie tepla<\/td>\n 3300 kg<\/td>\n 15600 kg<\/td>\n<\/tr>\n \nPo\u010det hor\u00e1kov (kusy)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \nObsadenos\u0165 (d\u013a\u017eka*\u0161\u00edrka)<\/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 Hlavn\u00e9 technick\u00e9 ukazovatele ochrany \u017eivotn\u00e9ho prostredia<\/strong><\/p>\n\n\n\n\nN\u00e1zov parametra<\/td>\n D\u00e1ta<\/td>\n<\/tr>\n \nN\u00edzkomet\u00e1nov\u00e9 v\u00fdfukov\u00e9 plyny\/10 000 m\u00b3\/h<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \nDoplnok kysl\u00edka vo vzduchu\/10 000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \nObsah kysl\u00edka v n\u00edzkoteplotn\u00fdch spalin\u00e1ch %<\/td>\n 5<\/td>\n<\/tr>\n \nTeplota pece \u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \nOxidy dus\u00edka vo v\u00fdfukov\u00fdch plynoch mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \nCelkov\u00e9 nemet\u00e1nov\u00e9 uh\u013eovod\u00edky vo v\u00fdfukov\u00fdch plynoch 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 Hlavn\u00e9 ekonomick\u00e9 ukazovatele<\/strong><\/p>\n\n\n\n\nN\u00e1zov parametra<\/td>\n D\u00e1ta<\/td>\n<\/tr>\n \nIn\u0161talovan\u00fd v\u00fdkon rozvodu energie<\/td>\n 1200 kW\/h<\/td>\n<\/tr>\n \nN\u00e1klady na elektrinu<\/td>\n 4,8 mili\u00f3na juanov\/rok<\/td>\n<\/tr>\n \nV\u00fdkon pary z kotla na odpadov\u00e9 teplo<\/td>\n 45 t\/h<\/td>\n<\/tr>\n \nParametre pary<\/td>\n 4,9 MPa, 420 \u2103<\/td>\n<\/tr>\n \nCena v Steame<\/td>\n 120 juanov\/t<\/td>\n<\/tr>\n \nPriame ekonomick\u00e9 v\u00fdhody<\/td>\n 43,2 mili\u00f3na juanov\/rok<\/td>\n<\/tr>\n \nZn\u00ed\u017eenie spotreby surov\u00e9ho uhlia<\/td>\n 50 000 ton\/rok<\/td>\n<\/tr>\n \nZn\u00ed\u017eenie emisi\u00ed uhl\u00edka<\/td>\n 860 000 ton\/rok<\/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. […]<\/p>","protected":false},"author":1,"featured_media":0,"parent":0,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":{"_et_pb_use_builder":"on","_et_pb_old_content":"","_et_gb_content_width":"","footnotes":""},"class_list":["post-4298","page","type-page","status-publish","hentry"],"rankMath":{"parentDomain":"regenerative-thermal-oxidizers.com","noFollowDomains":[],"noFollowExcludeDomains":[],"noFollowExternalLinks":false,"featuredImageNotice":"The featured image should be at least 200 by 200 pixels to be picked up by Facebook and other social media sites.","pluginReviewed":false,"postSettings":{"linkSuggestions":true,"useFocusKeyword":false},"frontEndScore":false,"postName":"vocs-waste-gas-treatment-in-coal-chemical-industry","permalinkFormat":"https:\/\/regenerative-thermal-oxidizers.com\/sk\/%pagename%\/","showLockModifiedDate":true,"assessor":{"focusKeywordLink":"https:\/\/regenerative-thermal-oxidizers.com\/wp-admin\/edit.php?focus_keyword=%focus_keyword%&post_type=%post_type%","hasTOCPlugin":{"stackable-ultimate-gutenberg-blocks\/plugin.php":"Stackable"},"primaryTaxonomy":false,"serpData":{"title":"","description":"","focusKeywords":"","pillarContent":false,"canonicalUrl":"","breadcrumbTitle":"","advancedRobots":{"max-snippet":"-1","max-video-preview":"-1","max-image-preview":"large"},"facebookTitle":"","facebookDescription":"","facebookImage":"","facebookImageID":"","facebookHasOverlay":false,"facebookImageOverlay":"","facebookAuthor":"","twitterCardType":"","twitterUseFacebook":true,"twitterTitle":"","twitterDescription":"","twitterImage":"","twitterImageID":"","twitterHasOverlay":false,"twitterImageOverlay":"","twitterPlayerUrl":"","twitterPlayerSize":"","twitterPlayerStream":"","twitterPlayerStreamCtype":"","twitterAppDescription":"","twitterAppIphoneName":"","twitterAppIphoneID":"","twitterAppIphoneUrl":"","twitterAppIpadName":"","twitterAppIpadID":"","twitterAppIpadUrl":"","twitterAppGoogleplayName":"","twitterAppGoogleplayID":"","twitterAppGoogleplayUrl":"","twitterAppCountry":"","robots":{"index":true},"twitterAuthor":"username","primaryTerm":0,"authorName":"rtoadmin","titleTemplate":"Singapore %title% Supplier Solution%sep% %sitename%","descriptionTemplate":"%excerpt%","showScoreFrontend":true,"lockModifiedDate":false},"powerWords":[],"diacritics":{"A":"[\\u0041\\u24B6\\uFF21\\u00C0\\u00C1\\u00C2\\u1EA6\\u1EA4\\u1EAA\\u1EA8\\u00C3\\u0100\\u0102\\u1EB0\\u1EAE\\u1EB4\\u1EB2\\u0226\\u01E0\\u00C4\\u01DE\\u1EA2\\u00C5\\u01FA\\u01CD\\u0200\\u0202\\u1EA0\\u1EAC\\u1EB6\\u1E00\\u0104\\u023A\\u2C6F]","AA":"[\\uA732]","AE":"[\\u00C6\\u01FC\\u01E2]","AO":"[\\uA734]","AU":"[\\uA736]","AV":"[\\uA738\\uA73A]","AY":"[\\uA73C]","B":"[\\u0042\\u24B7\\uFF22\\u1E02\\u1E04\\u1E06\\u0243\\u0182\\u0181]","C":"[\\u0043\\u24B8\\uFF23\\u0106\\u0108\\u010A\\u010C\\u00C7\\u1E08\\u0187\\u023B\\uA73E]","D":"[\\u0044\\u24B9\\uFF24\\u1E0A\\u010E\\u1E0C\\u1E10\\u1E12\\u1E0E\\u0110\\u018B\\u018A\\u0189\\uA779]","DZ":"[\\u01F1\\u01C4]","Dz":"[\\u01F2\\u01C5]","E":"[\\u0045\\u24BA\\uFF25\\u00C8\\u00C9\\u00CA\\u1EC0\\u1EBE\\u1EC4\\u1EC2\\u1EBC\\u0112\\u1E14\\u1E16\\u0114\\u0116\\u00CB\\u1EBA\\u011A\\u0204\\u0206\\u1EB8\\u1EC6\\u0228\\u1E1C\\u0118\\u1E18\\u1E1A\\u0190\\u018E]","F":"[\\u0046\\u24BB\\uFF26\\u1E1E\\u0191\\uA77B]","G":"[\\u0047\\u24BC\\uFF27\\u01F4\\u011C\\u1E20\\u011E\\u0120\\u01E6\\u0122\\u01E4\\u0193\\uA7A0\\uA77D\\uA77E]","H":"[\\u0048\\u24BD\\uFF28\\u0124\\u1E22\\u1E26\\u021E\\u1E24\\u1E28\\u1E2A\\u0126\\u2C67\\u2C75\\uA78D]","I":"[\\u0049\\u24BE\\uFF29\\u00CC\\u00CD\\u00CE\\u0128\\u012A\\u012C\\u0130\\u00CF\\u1E2E\\u1EC8\\u01CF\\u0208\\u020A\\u1ECA\\u012E\\u1E2C\\u0197]","J":"[\\u004A\\u24BF\\uFF2A\\u0134\\u0248]","K":"[\\u004B\\u24C0\\uFF2B\\u1E30\\u01E8\\u1E32\\u0136\\u1E34\\u0198\\u2C69\\uA740\\uA742\\uA744\\uA7A2]","L":"[\\u004C\\u24C1\\uFF2C\\u013F\\u0139\\u013D\\u1E36\\u1E38\\u013B\\u1E3C\\u1E3A\\u0141\\u023D\\u2C62\\u2C60\\uA748\\uA746\\uA780]","LJ":"[\\u01C7]","Lj":"[\\u01C8]","M":"[\\u004D\\u24C2\\uFF2D\\u1E3E\\u1E40\\u1E42\\u2C6E\\u019C]","N":"[\\u004E\\u24C3\\uFF2E\\u01F8\\u0143\\u00D1\\u1E44\\u0147\\u1E46\\u0145\\u1E4A\\u1E48\\u0220\\u019D\\uA790\\uA7A4]","NJ":"[\\u01CA]","Nj":"[\\u01CB]","O":"[\\u004F\\u24C4\\uFF2F\\u00D2\\u00D3\\u00D4\\u1ED2\\u1ED0\\u1ED6\\u1ED4\\u00D5\\u1E4C\\u022C\\u1E4E\\u014C\\u1E50\\u1E52\\u014E\\u022E\\u0230\\u00D6\\u022A\\u1ECE\\u0150\\u01D1\\u020C\\u020E\\u01A0\\u1EDC\\u1EDA\\u1EE0\\u1EDE\\u1EE2\\u1ECC\\u1ED8\\u01EA\\u01EC\\u00D8\\u01FE\\u0186\\u019F\\uA74A\\uA74C]","OI":"[\\u01A2]","OO":"[\\uA74E]","OU":"[\\u0222]","P":"[\\u0050\\u24C5\\uFF30\\u1E54\\u1E56\\u01A4\\u2C63\\uA750\\uA752\\uA754]","Q":"[\\u0051\\u24C6\\uFF31\\uA756\\uA758\\u024A]","R":"[\\u0052\\u24C7\\uFF32\\u0154\\u1E58\\u0158\\u0210\\u0212\\u1E5A\\u1E5C\\u0156\\u1E5E\\u024C\\u2C64\\uA75A\\uA7A6\\uA782]","S":"[\\u0053\\u24C8\\uFF33\\u1E9E\\u015A\\u1E64\\u015C\\u1E60\\u0160\\u1E66\\u1E62\\u1E68\\u0218\\u015E\\u2C7E\\uA7A8\\uA784]","T":"[\\u0054\\u24C9\\uFF34\\u1E6A\\u0164\\u1E6C\\u021A\\u0162\\u1E70\\u1E6E\\u0166\\u01AC\\u01AE\\u023E\\uA786]","TZ":"[\\uA728]","U":"[\\u0055\\u24CA\\uFF35\\u00D9\\u00DA\\u00DB\\u0168\\u1E78\\u016A\\u1E7A\\u016C\\u00DC\\u01DB\\u01D7\\u01D5\\u01D9\\u1EE6\\u016E\\u0170\\u01D3\\u0214\\u0216\\u01AF\\u1EEA\\u1EE8\\u1EEE\\u1EEC\\u1EF0\\u1EE4\\u1E72\\u0172\\u1E76\\u1E74\\u0244]","V":"[\\u0056\\u24CB\\uFF36\\u1E7C\\u1E7E\\u01B2\\uA75E\\u0245]","VY":"[\\uA760]","W":"[\\u0057\\u24CC\\uFF37\\u1E80\\u1E82\\u0174\\u1E86\\u1E84\\u1E88\\u2C72]","X":"[\\u0058\\u24CD\\uFF38\\u1E8A\\u1E8C]","Y":"[\\u0059\\u24CE\\uFF39\\u1EF2\\u00DD\\u0176\\u1EF8\\u0232\\u1E8E\\u0178\\u1EF6\\u1EF4\\u01B3\\u024E\\u1EFE]","Z":"[\\u005A\\u24CF\\uFF3A\\u0179\\u1E90\\u017B\\u017D\\u1E92\\u1E94\\u01B5\\u0224\\u2C7F\\u2C6B\\uA762]","a":"[\\u0061\\u24D0\\uFF41\\u1E9A\\u00E0\\u00E1\\u00E2\\u1EA7\\u1EA5\\u1EAB\\u1EA9\\u00E3\\u0101\\u0103\\u1EB1\\u1EAF\\u1EB5\\u1EB3\\u0227\\u01E1\\u00E4\\u01DF\\u1EA3\\u00E5\\u01FB\\u01CE\\u0201\\u0203\\u1EA1\\u1EAD\\u1EB7\\u1E01\\u0105\\u2C65\\u0250]","aa":"[\\uA733]","ae":"[\\u00E6\\u01FD\\u01E3]","ao":"[\\uA735]","au":"[\\uA737]","av":"[\\uA739\\uA73B]","ay":"[\\uA73D]","b":"[\\u0062\\u24D1\\uFF42\\u1E03\\u1E05\\u1E07\\u0180\\u0183\\u0253]","c":"[\\u0063\\u24D2\\uFF43\\u0107\\u0109\\u010B\\u010D\\u00E7\\u1E09\\u0188\\u023C\\uA73F\\u2184]","d":"[\\u0064\\u24D3\\uFF44\\u1E0B\\u010F\\u1E0D\\u1E11\\u1E13\\u1E0F\\u0111\\u018C\\u0256\\u0257\\uA77A]","dz":"[\\u01F3\\u01C6]","e":"[\\u0065\\u24D4\\uFF45\\u00E8\\u00E9\\u00EA\\u1EC1\\u1EBF\\u1EC5\\u1EC3\\u1EBD\\u0113\\u1E15\\u1E17\\u0115\\u0117\\u00EB\\u1EBB\\u011B\\u0205\\u0207\\u1EB9\\u1EC7\\u0229\\u1E1D\\u0119\\u1E19\\u1E1B\\u0247\\u025B\\u01DD]","f":"[\\u0066\\u24D5\\uFF46\\u1E1F\\u0192\\uA77C]","g":"[\\u0067\\u24D6\\uFF47\\u01F5\\u011D\\u1E21\\u011F\\u0121\\u01E7\\u0123\\u01E5\\u0260\\uA7A1\\u1D79\\uA77F]","h":"[\\u0068\\u24D7\\uFF48\\u0125\\u1E23\\u1E27\\u021F\\u1E25\\u1E29\\u1E2B\\u1E96\\u0127\\u2C68\\u2C76\\u0265]","hv":"[\\u0195]","i":"[\\u0069\\u24D8\\uFF49\\u00EC\\u00ED\\u00EE\\u0129\\u012B\\u012D\\u00EF\\u1E2F\\u1EC9\\u01D0\\u0209\\u020B\\u1ECB\\u012F\\u1E2D\\u0268\\u0131]","j":"[\\u006A\\u24D9\\uFF4A\\u0135\\u01F0\\u0249]","k":"[\\u006B\\u24DA\\uFF4B\\u1E31\\u01E9\\u1E33\\u0137\\u1E35\\u0199\\u2C6A\\uA741\\uA743\\uA745\\uA7A3]","l":"[\\u006C\\u24DB\\uFF4C\\u0140\\u013A\\u013E\\u1E37\\u1E39\\u013C\\u1E3D\\u1E3B\\u017F\\u0142\\u019A\\u026B\\u2C61\\uA749\\uA781\\uA747]","lj":"[\\u01C9]","m":"[\\u006D\\u24DC\\uFF4D\\u1E3F\\u1E41\\u1E43\\u0271\\u026F]","n":"[\\u006E\\u24DD\\uFF4E\\u01F9\\u0144\\u00F1\\u1E45\\u0148\\u1E47\\u0146\\u1E4B\\u1E49\\u019E\\u0272\\u0149\\uA791\\uA7A5]","nj":"[\\u01CC]","o":"[\\u006F\\u24DE\\uFF4F\\u00F2\\u00F3\\u00F4\\u1ED3\\u1ED1\\u1ED7\\u1ED5\\u00F5\\u1E4D\\u022D\\u1E4F\\u014D\\u1E51\\u1E53\\u014F\\u022F\\u0231\\u00F6\\u022B\\u1ECF\\u0151\\u01D2\\u020D\\u020F\\u01A1\\u1EDD\\u1EDB\\u1EE1\\u1EDF\\u1EE3\\u1ECD\\u1ED9\\u01EB\\u01ED\\u00F8\\u01FF\\u0254\\uA74B\\uA74D\\u0275]","oi":"[\\u01A3]","ou":"[\\u0223]","oo":"[\\uA74F]","p":"[\\u0070\\u24DF\\uFF50\\u1E55\\u1E57\\u01A5\\u1D7D\\uA751\\uA753\\uA755]","q":"[\\u0071\\u24E0\\uFF51\\u024B\\uA757\\uA759]","r":"[\\u0072\\u24E1\\uFF52\\u0155\\u1E59\\u0159\\u0211\\u0213\\u1E5B\\u1E5D\\u0157\\u1E5F\\u024D\\u027D\\uA75B\\uA7A7\\uA783]","s":"[\\u0073\\u24E2\\uFF53\\u015B\\u1E65\\u015D\\u1E61\\u0161\\u1E67\\u1E63\\u1E69\\u0219\\u015F\\u023F\\uA7A9\\uA785\\u1E9B]","ss":"[\\u00DF]","t":"[\\u0074\\u24E3\\uFF54\\u1E6B\\u1E97\\u0165\\u1E6D\\u021B\\u0163\\u1E71\\u1E6F\\u0167\\u01AD\\u0288\\u2C66\\uA787]","tz":"[\\uA729]","u":"[\\u0075\\u24E4\\uFF55\\u00F9\\u00FA\\u00FB\\u0169\\u1E79\\u016B\\u1E7B\\u016D\\u00FC\\u01DC\\u01D8\\u01D6\\u01DA\\u1EE7\\u016F\\u0171\\u01D4\\u0215\\u0217\\u01B0\\u1EEB\\u1EE9\\u1EEF\\u1EED\\u1EF1\\u1EE5\\u1E73\\u0173\\u1E77\\u1E75\\u0289]","v":"[\\u0076\\u24E5\\uFF56\\u1E7D\\u1E7F\\u028B\\uA75F\\u028C]","vy":"[\\uA761]","w":"[\\u0077\\u24E6\\uFF57\\u1E81\\u1E83\\u0175\\u1E87\\u1E85\\u1E98\\u1E89\\u2C73]","x":"[\\u0078\\u24E7\\uFF58\\u1E8B\\u1E8D]","y":"[\\u0079\\u24E8\\uFF59\\u1EF3\\u00FD\\u0177\\u1EF9\\u0233\\u1E8F\\u00FF\\u1EF7\\u1E99\\u1EF5\\u01B4\\u024F\\u1EFF]","z":"[\\u007A\\u24E9\\uFF5A\\u017A\\u1E91\\u017C\\u017E\\u1E93\\u1E95\\u01B6\\u0225\\u0240\\u2C6C\\uA763]"},"researchesTests":["contentHasTOC","contentHasShortParagraphs","contentHasAssets","keywordInTitle","keywordInMetaDescription","keywordInPermalink","keywordIn10Percent","keywordInContent","keywordInSubheadings","keywordInImageAlt","keywordDensity","keywordNotUsed","lengthContent","lengthPermalink","linksHasInternal","linksHasExternals","linksNotAllExternals","titleStartWithKeyword","titleSentiment","titleHasPowerWords","titleHasNumber","hasContentAI"],"hasRedirection":false,"hasBreadcrumb":false},"homeUrl":"https:\/\/regenerative-thermal-oxidizers.com\/sk","objectID":4298,"objectType":"post","locale":"sk","localeFull":"sk_SK","overlayImages":{"play":{"name":"Ikona prehr\u00e1vania","url":"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/icon-play.png","path":"\/var\/www\/html\/public_html\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/icon-play.png","position":"middle_center"},"gif":{"name":"Ikona GIFu","url":"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/icon-gif.png","path":"\/var\/www\/html\/public_html\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/icon-gif.png","position":"middle_center"}},"defautOgImage":"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/social-placeholder.jpg","customPermalinks":true,"isUserRegistered":false,"autoSuggestKeywords":false,"connectSiteUrl":"https:\/\/rankmath.com\/auth?site=https%3A%2F%2Fregenerative-thermal-oxidizers.com%2Fsk&r=https%3A%2F%2Fregenerative-thermal-oxidizers.com%2Fsk%2Fwp-json%2Fwp%2Fv2%2Fpages%2F4298%3Fnonce%3D14855dbf90","maxTags":5,"trendsIcon":"
Sply\u0148ovanie uhlia: ozna\u010duje ne\u00fapln\u00fa reakciu medzi r\u00f4znymi druhmi uhlia (koks) a sply\u0148ovac\u00edmi \u010dinidlami pren\u00e1\u0161aj\u00facimi kysl\u00edk (H2O, O2, CO2) v sply\u0148ova\u010di. Pri vysokej teplote a ur\u010ditom tlaku sa nakoniec vytv\u00e1ra surov\u00fd uho\u013en\u00fd plyn zlo\u017een\u00fd z H2, CH4, CO, CO2, N2, stopov\u00fdch mno\u017estiev H2S, COS at\u010f.<\/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
Klasifik\u00e1cia procesov sply\u0148ovania uhlia:<\/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 Proces prem\u00fdvania metanolom pri n\u00edzkej teplote: pou\u017eitie studen\u00e9ho metanolu ako absorp\u010dn\u00e9ho rozp\u00fa\u0161\u0165adla s vyu\u017eit\u00edm vysokej rozpustnosti metanolu v kysl\u00fdch plynoch pri n\u00edzkych teplot\u00e1ch na odstr\u00e1nenie kysl\u00fdch plynov, najm\u00e4 CO2 a H2S, zo vstupn\u00e9ho plynu. <\/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=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\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 Charakteristiky v\u00fdfukov\u00fdch plynov z n\u00edzkoteplotn\u00e9ho prania metanolom:<\/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 Vzh\u013eadom na to, \u017ee v\u00fdfukov\u00e9 plyny neobsahuj\u00fa takmer \u017eiadny kysl\u00edk, je potrebn\u00e9 doplni\u0165 v\u00fdfukov\u00e9 plyny vzduchom, aby sa splnila potreba kysl\u00edka pre \u00fapln\u00fa oxid\u00e1ciu v\u00fdfukov\u00fdch plynov. 1) Bezpe\u010dnostn\u00e9 aspekty: anal\u00fdza nebezpe\u010denstva v\u00fdbuchu<\/strong><\/em><\/p>\n Pod\u013ea technickej \u0161pecifik\u00e1cie pre spracovanie priemyseln\u00fdch organick\u00fdch odpadov\u00fdch plynov met\u00f3dou tepeln\u00e9ho akumula\u010dn\u00e9ho spa\u013eovania by koncentr\u00e1cia organickej hmoty vstupuj\u00facej do zariadenia RTO mala by\u0165 ni\u017e\u0161ia ako 25% dolnej medze v\u00fdbu\u0161nosti. Vypo\u010d\u00edtajte doln\u00fa medzu v\u00fdbu\u0161nosti komplexn\u00fdch hor\u013eav\u00fdch zmes\u00ed plynov pomocou Le Chatlierovej rovnice a potom porovnajte koncentr\u00e1ciu hor\u013eav\u00fdch zlo\u017eiek vo v\u00fdfukov\u00fdch plynoch s ve\u013ekos\u0165ou 25% LEL, aby ste ur\u010dili bezpe\u010dnos\u0165 koncentr\u00e1cie hor\u013eav\u00fdch zlo\u017eiek vo v\u00fdfukov\u00fdch plynoch.<\/p>\n 2) \u00davahy o r\u00fdchlosti \u010distenia: \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=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d]<\/p>\n Zvy\u010dajne sa navrhuj\u00fa bez zoh\u013eadnenia vplyvu inertn\u00fdch plynov, doln\u00e1 medza v\u00fdbu\u0161nosti v\u00fdfukov\u00fdch plynov sa vypo\u010d\u00edta a pomer riedenia vzduchu sa ur\u010d\u00ed na z\u00e1klade vz\u0165ahu medzi koncentr\u00e1ciou v\u00fdfukov\u00fdch plynov a limitom v\u00fdbu\u0161nosti 25% LEL. Tento v\u00fdpo\u010det m\u00f4\u017ee zaru\u010di\u0165 vn\u00fatorn\u00fa bezpe\u010dnos\u0165, ale objem v\u00fdfukov\u00fdch plynov je relat\u00edvne ve\u013ek\u00fd.<\/p>\n Vzh\u013eadom na pr\u00edtomnos\u0165 ve\u013ek\u00e9ho mno\u017estva inertn\u00e9ho plynu CO2 vo v\u00fdfukovom plyne N2 z n\u00edzkoteplotn\u00e9ho prania metanolom, mal\u00e9ho mno\u017estva hor\u013eav\u00fdch zlo\u017eiek, Preto v\u00fdfukov\u00fd plyn z n\u00edzkoteplotn\u00e9ho prania metanolom nem\u00e1 horn\u00fa ani doln\u00fa medzu v\u00fdbu\u0161nosti. [\/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 Zmes v\u00fdfukov\u00fdch plynov je navrhnut\u00e1 na doplnenie kysl\u00edka na z\u00e1klade materi\u00e1lovej bilancie s obsahom kysl\u00edka v spalin\u00e1ch okolo 5%.<\/p>\n Porovnanie koncentr\u00e1cie hor\u013eav\u00fdch zlo\u017eiek vo v\u00fdfukov\u00fdch plynoch po doplnen\u00ed kysl\u00edka a dolnej medze v\u00fdbu\u0161nosti v\u00fdfukov\u00fdch plynov (okrem inertn\u00fdch plynov)<\/p>\n <\/p>\n 1) N\u00edzky objem v\u00fdfukov\u00fdch plynov<\/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=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201dpredvolen\u00e9\u201d global_colors_info=\u201d{}\u201d]<\/p>\n Metanolov\u00e1 jednotka spolo\u010dnosti Xinye Energy Chemical s kapacitou 525 000 ton\/rok vyu\u017e\u00edva technol\u00f3giu tlakov\u00e9ho sply\u0148ovania drven\u00e9ho uhlia. Okrem hlavn\u00fdch zlo\u017eiek CO2 a N2 obsahuje n\u00edzkoteplotn\u00fd odpadov\u00fd plyn z preplachovania metanolom aj met\u00e1n, celkov\u00e9 nemet\u00e1nov\u00e9 uh\u013eovod\u00edky, CO, metanol at\u010f. Tento odpadov\u00fd plyn sa v s\u00fa\u010dasnosti vyp\u00fa\u0161\u0165a cez kom\u00edn kotla. Pod\u013ea po\u017eiadaviek ochrany \u017eivotn\u00e9ho prostredia je potrebn\u00e9 odstr\u00e1ni\u0165 prchav\u00e9 organick\u00e9 zl\u00fa\u010denia (VOC). Okrem toho polyoxymetyl\u00e9nov\u00e1 jednotka obsahuje aj tri odpadov\u00e9 plyny, ktor\u00e9 je potrebn\u00e9 \u010disti\u0165.<\/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 Na z\u00e1klade charakterist\u00edk hor\u013eav\u00fdch zlo\u017eiek vo v\u00fdfukov\u00fdch plynoch sa na\u0161i in\u017einieri rozhodli pre technologick\u00fa cestu \u00fapravy \u201e\u010distenie RTO + strednotlakov\u00fd parn\u00fd kotol na odpadov\u00e9 teplo na sp\u00e4tn\u00e9 z\u00edskavanie tepla\u201c. Pod\u013ea jedine\u010dn\u00e9ho \u201eLe Chater & Inert Gas Correction Theory Safety Air Distribution Algorithm\u201c na\u0161ej spolo\u010dnosti sme sa rozhodli zvoli\u0165 RTO s rota\u010dn\u00fdm ventilom s objemom vzduchu 270 000 a obsahom kysl\u00edka 5% vo v\u00fdfukov\u00fdch plynoch po sp\u00e1len\u00ed. S\u00fa\u010dasne sme zvolili parn\u00fd kotol s tlakom 5,1 MPa\/46T a kon\u0161trukciou 120 metrov\u00e9ho koncov\u00e9ho kom\u00edna, aby sa zn\u00ed\u017eil vplyv v\u00fdfukov\u00fdch emisi\u00ed na \u017eivotn\u00e9 prostredie v tov\u00e1rni.<\/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 Hlavn\u00e9 zariadenie vyu\u017e\u00edva jeden rota\u010dn\u00fd ventil RTO s objemom vzduchu 270 000 kJ, \u0161tvorcov\u00e9 usporiadanie, vybaven\u00fd 3 rota\u010dn\u00fdmi ventilmi na rozde\u013eovanie vzduchu a 36 komorami na akumul\u00e1ciu tepla.<\/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 Konven\u010dn\u00e1 distrib\u00facia vzduchu: Koncentr\u00e1cia hor\u013eav\u00fdch zlo\u017eiek sa zn\u00ed\u017ei na <1,065, \u010do znamen\u00e1, \u017ee distrib\u00facia vzduchu mus\u00ed by\u0165 2,6-kr\u00e1t v\u00e4\u010d\u0161ia a celkov\u00fd objem vzduchu dosiahne 330 000.<\/p>\n [\/et_pb_text][\/et_pb_column][et_pb_column _builder_version=”4.27.4″ _module_preset=”default” type=”1_2″][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” hover_enabled=”0″ sticky_enabled=”0″]<\/p>\n Ak vezmeme do \u00favahy iba pr\u00edvod kysl\u00edka, pr\u00edvod vzduchu je 100 000 a celkov\u00fd objem vzduchu je 220 000.<\/p>\n 1. Vzdu\u0161n\u00e9 pozadie, doln\u00e1 medza v\u00fdbu\u0161nosti pri 900 \u2103 je 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 Hlavn\u00e9 technick\u00e9 ukazovatele ochrany \u017eivotn\u00e9ho prostredia<\/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 Hlavn\u00e9 ekonomick\u00e9 ukazovatele<\/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. […]<\/p>","protected":false},"author":1,"featured_media":0,"parent":0,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":{"_et_pb_use_builder":"on","_et_pb_old_content":"","_et_gb_content_width":"","footnotes":""},"class_list":["post-4298","page","type-page","status-publish","hentry"],"rankMath":{"parentDomain":"regenerative-thermal-oxidizers.com","noFollowDomains":[],"noFollowExcludeDomains":[],"noFollowExternalLinks":false,"featuredImageNotice":"The featured image should be at least 200 by 200 pixels to be picked up by Facebook and other social media sites.","pluginReviewed":false,"postSettings":{"linkSuggestions":true,"useFocusKeyword":false},"frontEndScore":false,"postName":"vocs-waste-gas-treatment-in-coal-chemical-industry","permalinkFormat":"https:\/\/regenerative-thermal-oxidizers.com\/sk\/%pagename%\/","showLockModifiedDate":true,"assessor":{"focusKeywordLink":"https:\/\/regenerative-thermal-oxidizers.com\/wp-admin\/edit.php?focus_keyword=%focus_keyword%&post_type=%post_type%","hasTOCPlugin":{"stackable-ultimate-gutenberg-blocks\/plugin.php":"Stackable"},"primaryTaxonomy":false,"serpData":{"title":"","description":"","focusKeywords":"","pillarContent":false,"canonicalUrl":"","breadcrumbTitle":"","advancedRobots":{"max-snippet":"-1","max-video-preview":"-1","max-image-preview":"large"},"facebookTitle":"","facebookDescription":"","facebookImage":"","facebookImageID":"","facebookHasOverlay":false,"facebookImageOverlay":"","facebookAuthor":"","twitterCardType":"","twitterUseFacebook":true,"twitterTitle":"","twitterDescription":"","twitterImage":"","twitterImageID":"","twitterHasOverlay":false,"twitterImageOverlay":"","twitterPlayerUrl":"","twitterPlayerSize":"","twitterPlayerStream":"","twitterPlayerStreamCtype":"","twitterAppDescription":"","twitterAppIphoneName":"","twitterAppIphoneID":"","twitterAppIphoneUrl":"","twitterAppIpadName":"","twitterAppIpadID":"","twitterAppIpadUrl":"","twitterAppGoogleplayName":"","twitterAppGoogleplayID":"","twitterAppGoogleplayUrl":"","twitterAppCountry":"","robots":{"index":true},"twitterAuthor":"username","primaryTerm":0,"authorName":"rtoadmin","titleTemplate":"Singapore %title% Supplier Solution%sep% %sitename%","descriptionTemplate":"%excerpt%","showScoreFrontend":true,"lockModifiedDate":false},"powerWords":[],"diacritics":{"A":"[\\u0041\\u24B6\\uFF21\\u00C0\\u00C1\\u00C2\\u1EA6\\u1EA4\\u1EAA\\u1EA8\\u00C3\\u0100\\u0102\\u1EB0\\u1EAE\\u1EB4\\u1EB2\\u0226\\u01E0\\u00C4\\u01DE\\u1EA2\\u00C5\\u01FA\\u01CD\\u0200\\u0202\\u1EA0\\u1EAC\\u1EB6\\u1E00\\u0104\\u023A\\u2C6F]","AA":"[\\uA732]","AE":"[\\u00C6\\u01FC\\u01E2]","AO":"[\\uA734]","AU":"[\\uA736]","AV":"[\\uA738\\uA73A]","AY":"[\\uA73C]","B":"[\\u0042\\u24B7\\uFF22\\u1E02\\u1E04\\u1E06\\u0243\\u0182\\u0181]","C":"[\\u0043\\u24B8\\uFF23\\u0106\\u0108\\u010A\\u010C\\u00C7\\u1E08\\u0187\\u023B\\uA73E]","D":"[\\u0044\\u24B9\\uFF24\\u1E0A\\u010E\\u1E0C\\u1E10\\u1E12\\u1E0E\\u0110\\u018B\\u018A\\u0189\\uA779]","DZ":"[\\u01F1\\u01C4]","Dz":"[\\u01F2\\u01C5]","E":"[\\u0045\\u24BA\\uFF25\\u00C8\\u00C9\\u00CA\\u1EC0\\u1EBE\\u1EC4\\u1EC2\\u1EBC\\u0112\\u1E14\\u1E16\\u0114\\u0116\\u00CB\\u1EBA\\u011A\\u0204\\u0206\\u1EB8\\u1EC6\\u0228\\u1E1C\\u0118\\u1E18\\u1E1A\\u0190\\u018E]","F":"[\\u0046\\u24BB\\uFF26\\u1E1E\\u0191\\uA77B]","G":"[\\u0047\\u24BC\\uFF27\\u01F4\\u011C\\u1E20\\u011E\\u0120\\u01E6\\u0122\\u01E4\\u0193\\uA7A0\\uA77D\\uA77E]","H":"[\\u0048\\u24BD\\uFF28\\u0124\\u1E22\\u1E26\\u021E\\u1E24\\u1E28\\u1E2A\\u0126\\u2C67\\u2C75\\uA78D]","I":"[\\u0049\\u24BE\\uFF29\\u00CC\\u00CD\\u00CE\\u0128\\u012A\\u012C\\u0130\\u00CF\\u1E2E\\u1EC8\\u01CF\\u0208\\u020A\\u1ECA\\u012E\\u1E2C\\u0197]","J":"[\\u004A\\u24BF\\uFF2A\\u0134\\u0248]","K":"[\\u004B\\u24C0\\uFF2B\\u1E30\\u01E8\\u1E32\\u0136\\u1E34\\u0198\\u2C69\\uA740\\uA742\\uA744\\uA7A2]","L":"[\\u004C\\u24C1\\uFF2C\\u013F\\u0139\\u013D\\u1E36\\u1E38\\u013B\\u1E3C\\u1E3A\\u0141\\u023D\\u2C62\\u2C60\\uA748\\uA746\\uA780]","LJ":"[\\u01C7]","Lj":"[\\u01C8]","M":"[\\u004D\\u24C2\\uFF2D\\u1E3E\\u1E40\\u1E42\\u2C6E\\u019C]","N":"[\\u004E\\u24C3\\uFF2E\\u01F8\\u0143\\u00D1\\u1E44\\u0147\\u1E46\\u0145\\u1E4A\\u1E48\\u0220\\u019D\\uA790\\uA7A4]","NJ":"[\\u01CA]","Nj":"[\\u01CB]","O":"[\\u004F\\u24C4\\uFF2F\\u00D2\\u00D3\\u00D4\\u1ED2\\u1ED0\\u1ED6\\u1ED4\\u00D5\\u1E4C\\u022C\\u1E4E\\u014C\\u1E50\\u1E52\\u014E\\u022E\\u0230\\u00D6\\u022A\\u1ECE\\u0150\\u01D1\\u020C\\u020E\\u01A0\\u1EDC\\u1EDA\\u1EE0\\u1EDE\\u1EE2\\u1ECC\\u1ED8\\u01EA\\u01EC\\u00D8\\u01FE\\u0186\\u019F\\uA74A\\uA74C]","OI":"[\\u01A2]","OO":"[\\uA74E]","OU":"[\\u0222]","P":"[\\u0050\\u24C5\\uFF30\\u1E54\\u1E56\\u01A4\\u2C63\\uA750\\uA752\\uA754]","Q":"[\\u0051\\u24C6\\uFF31\\uA756\\uA758\\u024A]","R":"[\\u0052\\u24C7\\uFF32\\u0154\\u1E58\\u0158\\u0210\\u0212\\u1E5A\\u1E5C\\u0156\\u1E5E\\u024C\\u2C64\\uA75A\\uA7A6\\uA782]","S":"[\\u0053\\u24C8\\uFF33\\u1E9E\\u015A\\u1E64\\u015C\\u1E60\\u0160\\u1E66\\u1E62\\u1E68\\u0218\\u015E\\u2C7E\\uA7A8\\uA784]","T":"[\\u0054\\u24C9\\uFF34\\u1E6A\\u0164\\u1E6C\\u021A\\u0162\\u1E70\\u1E6E\\u0166\\u01AC\\u01AE\\u023E\\uA786]","TZ":"[\\uA728]","U":"[\\u0055\\u24CA\\uFF35\\u00D9\\u00DA\\u00DB\\u0168\\u1E78\\u016A\\u1E7A\\u016C\\u00DC\\u01DB\\u01D7\\u01D5\\u01D9\\u1EE6\\u016E\\u0170\\u01D3\\u0214\\u0216\\u01AF\\u1EEA\\u1EE8\\u1EEE\\u1EEC\\u1EF0\\u1EE4\\u1E72\\u0172\\u1E76\\u1E74\\u0244]","V":"[\\u0056\\u24CB\\uFF36\\u1E7C\\u1E7E\\u01B2\\uA75E\\u0245]","VY":"[\\uA760]","W":"[\\u0057\\u24CC\\uFF37\\u1E80\\u1E82\\u0174\\u1E86\\u1E84\\u1E88\\u2C72]","X":"[\\u0058\\u24CD\\uFF38\\u1E8A\\u1E8C]","Y":"[\\u0059\\u24CE\\uFF39\\u1EF2\\u00DD\\u0176\\u1EF8\\u0232\\u1E8E\\u0178\\u1EF6\\u1EF4\\u01B3\\u024E\\u1EFE]","Z":"[\\u005A\\u24CF\\uFF3A\\u0179\\u1E90\\u017B\\u017D\\u1E92\\u1E94\\u01B5\\u0224\\u2C7F\\u2C6B\\uA762]","a":"[\\u0061\\u24D0\\uFF41\\u1E9A\\u00E0\\u00E1\\u00E2\\u1EA7\\u1EA5\\u1EAB\\u1EA9\\u00E3\\u0101\\u0103\\u1EB1\\u1EAF\\u1EB5\\u1EB3\\u0227\\u01E1\\u00E4\\u01DF\\u1EA3\\u00E5\\u01FB\\u01CE\\u0201\\u0203\\u1EA1\\u1EAD\\u1EB7\\u1E01\\u0105\\u2C65\\u0250]","aa":"[\\uA733]","ae":"[\\u00E6\\u01FD\\u01E3]","ao":"[\\uA735]","au":"[\\uA737]","av":"[\\uA739\\uA73B]","ay":"[\\uA73D]","b":"[\\u0062\\u24D1\\uFF42\\u1E03\\u1E05\\u1E07\\u0180\\u0183\\u0253]","c":"[\\u0063\\u24D2\\uFF43\\u0107\\u0109\\u010B\\u010D\\u00E7\\u1E09\\u0188\\u023C\\uA73F\\u2184]","d":"[\\u0064\\u24D3\\uFF44\\u1E0B\\u010F\\u1E0D\\u1E11\\u1E13\\u1E0F\\u0111\\u018C\\u0256\\u0257\\uA77A]","dz":"[\\u01F3\\u01C6]","e":"[\\u0065\\u24D4\\uFF45\\u00E8\\u00E9\\u00EA\\u1EC1\\u1EBF\\u1EC5\\u1EC3\\u1EBD\\u0113\\u1E15\\u1E17\\u0115\\u0117\\u00EB\\u1EBB\\u011B\\u0205\\u0207\\u1EB9\\u1EC7\\u0229\\u1E1D\\u0119\\u1E19\\u1E1B\\u0247\\u025B\\u01DD]","f":"[\\u0066\\u24D5\\uFF46\\u1E1F\\u0192\\uA77C]","g":"[\\u0067\\u24D6\\uFF47\\u01F5\\u011D\\u1E21\\u011F\\u0121\\u01E7\\u0123\\u01E5\\u0260\\uA7A1\\u1D79\\uA77F]","h":"[\\u0068\\u24D7\\uFF48\\u0125\\u1E23\\u1E27\\u021F\\u1E25\\u1E29\\u1E2B\\u1E96\\u0127\\u2C68\\u2C76\\u0265]","hv":"[\\u0195]","i":"[\\u0069\\u24D8\\uFF49\\u00EC\\u00ED\\u00EE\\u0129\\u012B\\u012D\\u00EF\\u1E2F\\u1EC9\\u01D0\\u0209\\u020B\\u1ECB\\u012F\\u1E2D\\u0268\\u0131]","j":"[\\u006A\\u24D9\\uFF4A\\u0135\\u01F0\\u0249]","k":"[\\u006B\\u24DA\\uFF4B\\u1E31\\u01E9\\u1E33\\u0137\\u1E35\\u0199\\u2C6A\\uA741\\uA743\\uA745\\uA7A3]","l":"[\\u006C\\u24DB\\uFF4C\\u0140\\u013A\\u013E\\u1E37\\u1E39\\u013C\\u1E3D\\u1E3B\\u017F\\u0142\\u019A\\u026B\\u2C61\\uA749\\uA781\\uA747]","lj":"[\\u01C9]","m":"[\\u006D\\u24DC\\uFF4D\\u1E3F\\u1E41\\u1E43\\u0271\\u026F]","n":"[\\u006E\\u24DD\\uFF4E\\u01F9\\u0144\\u00F1\\u1E45\\u0148\\u1E47\\u0146\\u1E4B\\u1E49\\u019E\\u0272\\u0149\\uA791\\uA7A5]","nj":"[\\u01CC]","o":"[\\u006F\\u24DE\\uFF4F\\u00F2\\u00F3\\u00F4\\u1ED3\\u1ED1\\u1ED7\\u1ED5\\u00F5\\u1E4D\\u022D\\u1E4F\\u014D\\u1E51\\u1E53\\u014F\\u022F\\u0231\\u00F6\\u022B\\u1ECF\\u0151\\u01D2\\u020D\\u020F\\u01A1\\u1EDD\\u1EDB\\u1EE1\\u1EDF\\u1EE3\\u1ECD\\u1ED9\\u01EB\\u01ED\\u00F8\\u01FF\\u0254\\uA74B\\uA74D\\u0275]","oi":"[\\u01A3]","ou":"[\\u0223]","oo":"[\\uA74F]","p":"[\\u0070\\u24DF\\uFF50\\u1E55\\u1E57\\u01A5\\u1D7D\\uA751\\uA753\\uA755]","q":"[\\u0071\\u24E0\\uFF51\\u024B\\uA757\\uA759]","r":"[\\u0072\\u24E1\\uFF52\\u0155\\u1E59\\u0159\\u0211\\u0213\\u1E5B\\u1E5D\\u0157\\u1E5F\\u024D\\u027D\\uA75B\\uA7A7\\uA783]","s":"[\\u0073\\u24E2\\uFF53\\u015B\\u1E65\\u015D\\u1E61\\u0161\\u1E67\\u1E63\\u1E69\\u0219\\u015F\\u023F\\uA7A9\\uA785\\u1E9B]","ss":"[\\u00DF]","t":"[\\u0074\\u24E3\\uFF54\\u1E6B\\u1E97\\u0165\\u1E6D\\u021B\\u0163\\u1E71\\u1E6F\\u0167\\u01AD\\u0288\\u2C66\\uA787]","tz":"[\\uA729]","u":"[\\u0075\\u24E4\\uFF55\\u00F9\\u00FA\\u00FB\\u0169\\u1E79\\u016B\\u1E7B\\u016D\\u00FC\\u01DC\\u01D8\\u01D6\\u01DA\\u1EE7\\u016F\\u0171\\u01D4\\u0215\\u0217\\u01B0\\u1EEB\\u1EE9\\u1EEF\\u1EED\\u1EF1\\u1EE5\\u1E73\\u0173\\u1E77\\u1E75\\u0289]","v":"[\\u0076\\u24E5\\uFF56\\u1E7D\\u1E7F\\u028B\\uA75F\\u028C]","vy":"[\\uA761]","w":"[\\u0077\\u24E6\\uFF57\\u1E81\\u1E83\\u0175\\u1E87\\u1E85\\u1E98\\u1E89\\u2C73]","x":"[\\u0078\\u24E7\\uFF58\\u1E8B\\u1E8D]","y":"[\\u0079\\u24E8\\uFF59\\u1EF3\\u00FD\\u0177\\u1EF9\\u0233\\u1E8F\\u00FF\\u1EF7\\u1E99\\u1EF5\\u01B4\\u024F\\u1EFF]","z":"[\\u007A\\u24E9\\uFF5A\\u017A\\u1E91\\u017C\\u017E\\u1E93\\u1E95\\u01B6\\u0225\\u0240\\u2C6C\\uA763]"},"researchesTests":["contentHasTOC","contentHasShortParagraphs","contentHasAssets","keywordInTitle","keywordInMetaDescription","keywordInPermalink","keywordIn10Percent","keywordInContent","keywordInSubheadings","keywordInImageAlt","keywordDensity","keywordNotUsed","lengthContent","lengthPermalink","linksHasInternal","linksHasExternals","linksNotAllExternals","titleStartWithKeyword","titleSentiment","titleHasPowerWords","titleHasNumber","hasContentAI"],"hasRedirection":false,"hasBreadcrumb":false},"homeUrl":"https:\/\/regenerative-thermal-oxidizers.com\/sk","objectID":4298,"objectType":"post","locale":"sk","localeFull":"sk_SK","overlayImages":{"play":{"name":"Ikona prehr\u00e1vania","url":"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/icon-play.png","path":"\/var\/www\/html\/public_html\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/icon-play.png","position":"middle_center"},"gif":{"name":"Ikona GIFu","url":"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/icon-gif.png","path":"\/var\/www\/html\/public_html\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/icon-gif.png","position":"middle_center"}},"defautOgImage":"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/plugins\/seo-by-rank-math\/assets\/admin\/img\/social-placeholder.jpg","customPermalinks":true,"isUserRegistered":false,"autoSuggestKeywords":false,"connectSiteUrl":"https:\/\/rankmath.com\/auth?site=https%3A%2F%2Fregenerative-thermal-oxidizers.com%2Fsk&r=https%3A%2F%2Fregenerative-thermal-oxidizers.com%2Fsk%2Fwp-json%2Fwp%2Fv2%2Fpages%2F4298%3Fnonce%3D14855dbf90","maxTags":5,"trendsIcon":"\n
Preh\u013eadov\u00e1 tabu\u013eka zlo\u017eiek surov\u00e9ho plynu vyroben\u00fdch r\u00f4znymi procesmi sply\u0148ovania<\/strong><\/h2>\n
\u010co je to n\u00edzkoteplotn\u00e9 metanolov\u00e9 pranie<\/strong><\/h2>\n
N\u00edzkoteplotn\u00e9 pranie metanolom je met\u00f3da, ktor\u00fa spolo\u010dne vyvinuli spolo\u010dnosti Linde a Lurgi za\u010diatkom 50. rokov 20. storo\u010dia na odstr\u00e1nenie kysl\u00fdch plynov zo surov\u00edn. V roku 1954 bola prv\u00fdkr\u00e1t pou\u017eit\u00e1 na \u010distenie plynu v priemysle tlakov\u00e9ho sply\u0148ovania uhlia v Ju\u017enej Afrike.
<\/strong><\/p>\n\n
Vlastnosti odpadov\u00fdch plynov<\/strong><\/h2>\n
\n
Stanovenie objemu vzduchu dop\u013a\u0148an\u00e9ho kysl\u00edkom<\/strong><\/h2>\n
Princ\u00edp ur\u010denia mno\u017estva dodato\u010dn\u00e9ho vzduchu:<\/p>\n\n
Pod\u013ea v\u00fdpo\u010dtovej met\u00f3dy pre zmes obsahuj\u00facu n hor\u013eav\u00fdch plynov a p inertn\u00fdch plynov mo\u017eno ur\u010di\u0165, \u017ee n\u00edzkokvalitn\u00fd zmie\u0161an\u00fd v\u00fdfukov\u00fd plyn hor\u013eav\u00fdch a inertn\u00fdch plynov je nehor\u013eav\u00fd a nev\u00fdbu\u0161n\u00fd.<\/p>\n
Mno\u017estvo dop\u013a\u0148an\u00e9ho vzduchu pre odpadov\u00fd plyn z n\u00edzkoteplotn\u00e9ho prania metanolom mo\u017eno ur\u010di\u0165 na z\u00e1klade obsahu kysl\u00edka v spalin\u00e1ch po \u00faplnej oxid\u00e1cii, ktor\u00fd je vy\u0161\u0161\u00ed ako 3%.<\/p>\nProces v\u00fdpo\u010dtu hor\u013eavosti zmesi v\u00fdfukov\u00fdch plynov vo vzduchu\u00a0<\/h3>\n
Spracovanie celkov\u00e9ho objemu vzduchu<\/strong><\/h4>\n
2) Objem vzduchu na doplnenie kysl\u00edka<\/em><\/strong><\/p>\n\u2460 Materi\u00e1lov\u00e1 bilancia<\/strong><\/h2>\n
\u00a0\u2461 Tepeln\u00e1 bilancia<\/strong><\/h2>\n
Typick\u00e9 in\u017einierske pr\u00edpady<\/strong><\/h2>\n
Anal\u00fdza situ\u00e1cie<\/h3>\n
Procesn\u00e1 trasa<\/h3>\n
\n
Vybaven\u00fd rota\u010dn\u00fdm RTO s objemom vzduchu 270 000, polyoxymetyl\u00e9nov\u00fd koncov\u00fd plyn zmie\u0161an\u00fd so vzduchom ako doplnok kysl\u00edka
Vyu\u017eitie odpadov\u00e9ho tepla: 46 t\/h, nas\u00fdten\u00e1 para 5,1 MPa
<\/strong><\/li>\n
celkov\u00e9 emisie nemet\u00e1nov\u00fdch uh\u013eovod\u00edkov <50 mg\/m\u00b3, ro\u010dn\u00e9 zn\u00ed\u017eenie emisi\u00ed uhl\u00edka pribli\u017ene o 860 000 ton;
<\/strong><\/li>\n<\/p>\nAnal\u00fdza bezpe\u010dnosti<\/h3>\n
\n
Inov\u00e1cia 1 \u2013 Prielom v dolnej medzi v\u00fdbu\u0161nosti za inertn\u00fdch podmienok<\/h3>\n
125 000 pred rozvodom vzduchu<\/strong><\/h4>\n
\n\n
\n V\u00fdpo\u010det medz\u00ed v\u00fdbu\u0161nosti hor\u013eavej zlo\u017eky zmesi<\/td>\n<\/tr>\n \n Vzorec Richarda Chateliho: Lf=100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \n Medza v\u00fdbu\u0161nosti zmesi plynov Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n 25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \n Celkov\u00e1 koncentr\u00e1cia hor\u013eav\u00fdch zlo\u017eiek<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n Zv\u00e1\u017ete vplyv inertn\u00e9ho plynu na doln\u00fa medzu v\u00fdbu\u0161nosti<\/strong><\/h4>\n
<\/p>\n
2. Inertn\u00e9 pozadie, nehor\u013eav\u00e9 a nev\u00fdbu\u0161n\u00e9 pri izbovej teplote, ale pri vysokej teplote?<\/p>\nInov\u00e1cia 2 \u2013 N\u00e1vrh a aplik\u00e1cia \u0161tvorcovej \u0161trukt\u00fary RTO s ve\u013ek\u00fdm objemom vzduchu<\/h3>\n
<\/p>\n\n\n
\n V\u00fdkonnostn\u00e9 parametre<\/td>\n Rota\u010dn\u00fd ventil RTO<\/td>\n Zdv\u00edhac\u00ed ventil RTO<\/td>\n<\/tr>\n \n Objem vzduchu<\/td>\n 300 000 Nm\u00b3\/h<\/td>\n 300 000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n \u0160trukt\u00fara smerov\u00e9ho ventilu<\/td>\n Rota\u010dn\u00fd ventil<\/td>\n Zdv\u00edhac\u00ed ventil<\/td>\n<\/tr>\n \n Po\u010det reverzn\u00fdch ventilov<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \n Frekvencia \u0161okov pri prep\u00ednan\u00ed reverzn\u00e9ho ventilu<\/td>\n Nepretr\u017eit\u00e1 prev\u00e1dzka bez otrasov<\/td>\n 6,48 mili\u00f3na kr\u00e1t\/rok<\/td>\n<\/tr>\n \n Po\u010det akumula\u010dn\u00fdch l\u00f4\u017eok<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \n Objem vzduchu na komoru<\/td>\n 20 000 Nm\u00b3\/h<\/td>\n 75 000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n Prierezov\u00e1 plocha jednej akumula\u010dnej komory tepla<\/td>\n 3\u33a1<\/td>\n 14\u33a1<\/td>\n<\/tr>\n \n Plniaca hmotnos\u0165 jednokomorovej keramickej akumul\u00e1cie tepla<\/td>\n 3300 kg<\/td>\n 15600 kg<\/td>\n<\/tr>\n \n Po\u010det hor\u00e1kov (kusy)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \n Obsadenos\u0165 (d\u013a\u017eka*\u0161\u00edrka)<\/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 N\u00e1zov parametra<\/td>\n D\u00e1ta<\/td>\n<\/tr>\n \n N\u00edzkomet\u00e1nov\u00e9 v\u00fdfukov\u00e9 plyny\/10 000 m\u00b3\/h<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \n Doplnok kysl\u00edka vo vzduchu\/10 000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \n Obsah kysl\u00edka v n\u00edzkoteplotn\u00fdch spalin\u00e1ch %<\/td>\n 5<\/td>\n<\/tr>\n \n Teplota pece \u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \n Oxidy dus\u00edka vo v\u00fdfukov\u00fdch plynoch mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \n Celkov\u00e9 nemet\u00e1nov\u00e9 uh\u013eovod\u00edky vo v\u00fdfukov\u00fdch plynoch mg\/m\u00b3<\/td>\n 40-60<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n \n\n
\n N\u00e1zov parametra<\/td>\n D\u00e1ta<\/td>\n<\/tr>\n \n In\u0161talovan\u00fd v\u00fdkon rozvodu energie<\/td>\n 1200 kW\/h<\/td>\n<\/tr>\n \n N\u00e1klady na elektrinu<\/td>\n 4,8 mili\u00f3na juanov\/rok<\/td>\n<\/tr>\n \n V\u00fdkon pary z kotla na odpadov\u00e9 teplo<\/td>\n 45 t\/h<\/td>\n<\/tr>\n \n Parametre pary<\/td>\n 4,9 MPa, 420 \u2103<\/td>\n<\/tr>\n \n Cena v Steame<\/td>\n 120 juanov\/t<\/td>\n<\/tr>\n \n Priame ekonomick\u00e9 v\u00fdhody<\/td>\n 43,2 mili\u00f3na juanov\/rok<\/td>\n<\/tr>\n \n Zn\u00ed\u017eenie spotreby surov\u00e9ho uhlia<\/td>\n 50 000 ton\/rok<\/td>\n<\/tr>\n \n Zn\u00ed\u017eenie emisi\u00ed uhl\u00edka<\/td>\n 860 000 ton\/rok<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n