[\/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
Co je zply\u0148ov\u00e1n\u00ed uhl\u00ed<\/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
Zply\u0148ov\u00e1n\u00ed uhl\u00ed je z\u00e1kladn\u00ed technologi\u00ed modern\u00edho uheln\u00e9ho chemick\u00e9ho pr\u016fmyslu.<\/strong><\/p>\nZply\u0148ov\u00e1n\u00ed uhl\u00ed: ozna\u010duje ne\u00faplnou reakci mezi r\u016fzn\u00fdmi druhy uhl\u00ed (koks) a kysl\u00edkat\u00fdmi zply\u0148ovac\u00edmi \u010dinidly (H2O, O2, CO2) ve zply\u0148ova\u010di. Za vysok\u00e9 teploty a ur\u010dit\u00e9ho tlaku nakonec vznik\u00e1 surov\u00fd sv\u00edtiplyn slo\u017een\u00fd z H2, CH4, CO, CO2, N2, stopov\u00e9ho mno\u017estv\u00ed H2S, COS atd.<\/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
Klasifikace proces\u016f zply\u0148ov\u00e1n\u00ed uhl\u00ed:<\/strong><\/p>\n\n- Suroviny: pr\u00e1\u0161kov\u00e9 uhl\u00ed, drcen\u00e9 uhl\u00ed, uheln\u00e1 vodn\u00ed suspenze;<\/li>\n
- Zply\u0148ovac\u00ed lo\u017ee: fluidn\u00ed lo\u017ee, fluidn\u00ed lo\u017ee, pevn\u00e9 lo\u017ee;\n<\/li>\n
- Pevn\u00e9 lo\u017ee je vyrobeno z kusov\u00e9ho uhl\u00ed (15-50 mm) jako suroviny;<\/li>\n
- Fluidn\u00ed lo\u017ee je vyrobeno z drcen\u00e9ho uhl\u00ed (m\u00e9n\u011b ne\u017e 10 mm) jako suroviny;<\/li>\n
- Vzduchov\u00e9 lo\u017ee je vyrobeno z pr\u00e1\u0161kov\u00e9ho uhl\u00ed (m\u00e9n\u011b ne\u017e 0,1 mm) jako 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
P\u0159ehledov\u00e1 tabulka slo\u017eek surov\u00e9ho plynu produkovan\u00fdch r\u016fzn\u00fdmi procesy zply\u0148ov\u00e1n\u00ed<\/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
Co je to n\u00edzkoteplotn\u00ed methanolov\u00e9 pran\u00ed<\/strong><\/h2>\nProces prom\u00fdv\u00e1n\u00ed methanolem p\u0159i n\u00edzk\u00fdch teplot\u00e1ch: pou\u017eit\u00ed studen\u00e9ho methanolu jako absorp\u010dn\u00edho rozpou\u0161t\u011bdla s vyu\u017eit\u00edm vysok\u00e9 rozpustnosti methanolu v kysel\u00fdch plynech p\u0159i n\u00edzk\u00fdch teplot\u00e1ch k odstran\u011bn\u00ed kysel\u00fdch plyn\u016f, zejm\u00e9na CO2 a H2S, ze vstupn\u00edho plynu.
N\u00edzkoteplotn\u00ed pran\u00ed methanolem je metoda, kterou spole\u010dn\u011b vyvinuly spole\u010dnosti Linde a Lurgi na po\u010d\u00e1tku 50. let 20. stolet\u00ed k odstran\u011bn\u00ed kysel\u00fdch plyn\u016f ze surovinov\u00fdch plyn\u016f. V roce 1954 byla poprv\u00e9 pou\u017eita k \u010di\u0161t\u011bn\u00ed plynu v pr\u016fmyslu tlakov\u00e9ho zply\u0148ov\u00e1n\u00ed uhl\u00ed v Ji\u017en\u00ed Africe.
<\/strong><\/p>\n <\/p>\n
\n- Mezi dodavatele bal\u00ed\u010dk\u016f pro n\u00edzkoteplotn\u00ed pran\u00ed methanolem pat\u0159\u00ed Linde, Lurgi, Daliansk\u00e1 technologick\u00e1 univerzita atd.;<\/li>\n
- Existuj\u00ed r\u016fzn\u00e9 procesy zply\u0148ov\u00e1n\u00ed, kter\u00e9 lze rozd\u011blit do t\u0159\u00ed kategori\u00ed: pevn\u00e9 lo\u017ee, fluidn\u00ed lo\u017ee a fluidn\u00ed lo\u017ee;<\/li>\n
- P\u0159i ur\u010dov\u00e1n\u00ed, zda m\u00e1 n\u00edzkoemisn\u00ed plyn hodnotu zp\u011btn\u00e9ho z\u00edsk\u00e1v\u00e1n\u00ed zbytkov\u00e9ho tepla, se zohled\u0148uje p\u0159edev\u0161\u00edm obsah CH4 ve v\u00fdfukov\u00fdch plynech;<\/li>\n
- Koncentrace CH4 z\u00e1vis\u00ed na procesu zply\u0148ov\u00e1n\u00ed a procesy zply\u0148ov\u00e1n\u00ed s pevn\u00fdm lo\u017eem zahrnuj\u00ed Lurgiho pec, pec BGL atd.;<\/li>\n<\/ul>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=\u201d1\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Vlastnosti odpadn\u00edch plyn\u016f<\/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 plyn\u016f z n\u00edzkoteplotn\u00edho pran\u00ed methanolem:<\/p>\n
\n- V\u00fdfukov\u00e9 plyny jsou v podstat\u011b nasycen\u00e9 vodn\u00ed p\u00e1rou<\/li>\n
- Vysok\u00fd obsah inertn\u00edch slo\u017eek CO2 a N2<\/li>\n
- V\u00fdfukov\u00e9 plyny v podstat\u011b neobsahuj\u00ed 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
Stanoven\u00ed objemu vzduchu pro dopl\u0148ov\u00e1n\u00ed kysl\u00edku<\/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
Vzhledem k tomu, \u017ee v\u00fdfukov\u00e9 plyny neobsahuj\u00ed t\u00e9m\u011b\u0159 \u017e\u00e1dn\u00fd kysl\u00edk, je nutn\u00e9 je dopl\u0148ovat vzduchem, aby se splnila pot\u0159eba kysl\u00edku pro \u00faplnou oxidaci v\u00fdfukov\u00fdch plyn\u016f.
Princip pro ur\u010den\u00ed mno\u017estv\u00ed p\u0159\u00eddavn\u00e9ho vzduchu:<\/p>\n
1) Bezpe\u010dnostn\u00ed aspekty: anal\u00fdza nebezpe\u010d\u00ed v\u00fdbuchu<\/strong><\/em><\/p>\nPodle technick\u00e9 specifikace pro \u010di\u0161t\u011bn\u00ed pr\u016fmyslov\u00fdch organick\u00fdch odpadn\u00edch plyn\u016f metodou tepeln\u00e9ho akumula\u010dn\u00edho spalov\u00e1n\u00ed by koncentrace organick\u00e9 hmoty vstupuj\u00edc\u00ed do za\u0159\u00edzen\u00ed RTO m\u011bla b\u00fdt ni\u017e\u0161\u00ed ne\u017e 25% doln\u00ed meze v\u00fdbu\u0161nosti. Vypo\u010d\u00edtejte doln\u00ed mez v\u00fdbu\u0161nosti komplexn\u00edch sm\u011bs\u00ed ho\u0159lav\u00fdch plyn\u016f pomoc\u00ed Le Chatlierova vzorce a pot\u00e9 porovnejte koncentraci ho\u0159lav\u00fdch slo\u017eek ve v\u00fdfukov\u00fdch plynech s velikost\u00ed 25% LEL, abyste ur\u010dili bezpe\u010dnost koncentrace ho\u0159lav\u00fdch slo\u017eek ve v\u00fdfukov\u00fdch plynech.<\/p>\n
2) \u00davahy o rychlosti \u010di\u0161t\u011bn\u00ed: \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\u00ed mez v\u00fdbu\u0161nosti sm\u011bsi plyn\u016f, %<\/li>\n
- Li je doln\u00ed mez v\u00fdbu\u0161nosti slo\u017eky i,%<\/li>\n
- Vi je objemov\u00fd pod\u00edl ur\u010dit\u00e9 ho\u0159lav\u00e9 slo\u017eky k ho\u0159lav\u00e9 slo\u017ece,%<\/li>\n<\/ul>\n
[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Obvykle se navrhuj\u00ed bez ohledu na vliv inertn\u00edch plyn\u016f, spodn\u00ed mez v\u00fdbu\u0161nosti v\u00fdfukov\u00fdch plyn\u016f se vypo\u010d\u00edt\u00e1v\u00e1 a pom\u011br \u0159ed\u011bn\u00ed vzduchem se ur\u010duje na z\u00e1klad\u011b vztahu mezi koncentrac\u00ed v\u00fdfukov\u00fdch plyn\u016f a limitn\u00ed hodnotou v\u00fdbu\u0161nosti 25%. Tento v\u00fdpo\u010det m\u016f\u017ee zajistit jiskrovou bezpe\u010dnost, ale objem v\u00fdfukov\u00fdch plyn\u016f je relativn\u011b velk\u00fd.<\/p>\n
Vzhledem k p\u0159\u00edtomnosti velk\u00e9ho mno\u017estv\u00ed inertn\u00edho plynu CO2 ve v\u00fdfukov\u00e9m plynu N2 z n\u00edzkoteplotn\u00edho prom\u00fdv\u00e1n\u00ed methanolem a mal\u00e9ho mno\u017estv\u00ed ho\u0159lav\u00fdch slo\u017eek,
Podle v\u00fdpo\u010dtov\u00e9 metody pro sm\u011bs obsahuj\u00edc\u00ed n ho\u0159lav\u00fdch plyn\u016f a p inertn\u00edch plyn\u016f lze ur\u010dit, \u017ee n\u00edzkokvalitn\u00ed sm\u011bs v\u00fdfukov\u00fdch plyn\u016f ho\u0159lav\u00fdch a inertn\u00edch plyn\u016f je neho\u0159lav\u00e1 a nev\u00fdbu\u0161n\u00e1.<\/p>\n
V\u00fdfukov\u00e9 plyny z n\u00edzkoteplotn\u00edho pran\u00ed methanolem proto nemaj\u00ed horn\u00ed ani doln\u00ed mez v\u00fdbu\u0161nosti.
Mno\u017estv\u00ed dopl\u0148ovan\u00e9ho vzduchu pro odpadn\u00ed plyn z n\u00edzkoteplotn\u00edho pran\u00ed methanolem lze ur\u010dit na z\u00e1klad\u011b obsahu kysl\u00edku ve spalin\u00e1ch po \u00fapln\u00e9 oxidaci vy\u0161\u0161\u00edho ne\u017e 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
V\u00fdpo\u010det ho\u0159lavosti sm\u011bsi v\u00fdfukov\u00fdch plyn\u016f ve 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
Sm\u011bs v\u00fdfukov\u00fdch plyn\u016f je navr\u017eena pro dopln\u011bn\u00ed kysl\u00edku na z\u00e1klad\u011b materi\u00e1lov\u00e9 bilance s obsahem kysl\u00edku ve spalin\u00e1ch okolo 5%.<\/p>\n
Porovn\u00e1n\u00ed koncentrace ho\u0159lav\u00fdch slo\u017eek ve v\u00fdfukov\u00fdch plynech po dopln\u011bn\u00ed kysl\u00edkem a doln\u00ed mez\u00ed v\u00fdbu\u0161nosti v\u00fdfukov\u00fdch plyn\u016f (bez inertn\u00edch plyn\u016f)<\/p>\n
<\/p>\n
Zpracov\u00e1n\u00ed celkov\u00e9ho objemu vzduchu<\/strong><\/h4>\n1) N\u00edzk\u00fd objem v\u00fdfukov\u00fdch plyn\u016f<\/em><\/strong>
2) Objem vzduchu pro dopl\u0148ov\u00e1n\u00ed kysl\u00edku<\/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 bilance<\/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 bilance<\/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\u017een\u00fdrsk\u00e9 p\u0159\u00edpady<\/strong><\/h2>\n[\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n
Anal\u00fdza situace<\/h3>\n
Jednotka metanolu spole\u010dnosti Xinye Energy Chemical s kapacitou 525 000 tun\/rok vyu\u017e\u00edv\u00e1 technologii tlakov\u00e9ho zply\u0148ov\u00e1n\u00ed drcen\u00e9ho uhl\u00ed. Krom\u011b hlavn\u00edch slo\u017eek CO2 a N2 obsahuje n\u00edzkoteplotn\u00ed odpadn\u00ed plyn z prop\u00edr\u00e1n\u00ed metanolem tak\u00e9 metan, celkov\u00e9 nemetanov\u00e9 uhlovod\u00edky, CO, methanol atd. Tento odpadn\u00ed plyn je v sou\u010dasn\u00e9 dob\u011b odv\u00e1d\u011bn kom\u00ednem kotle. Podle po\u017eadavk\u016f na ochranu \u017eivotn\u00edho prost\u0159ed\u00ed je nutn\u00e9 prov\u00e9st \u010di\u0161t\u011bn\u00ed VOC. Krom\u011b toho m\u00e1 jednotka polyoxymethylenu tak\u00e9 t\u0159i odpadn\u00ed plyny, kter\u00e9 je t\u0159eba \u010distit.<\/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
Trasa procesu<\/h3>\n
Na z\u00e1klad\u011b charakteristik ho\u0159lav\u00fdch slo\u017eek ve v\u00fdfukov\u00fdch plynech se na\u0161i in\u017een\u00fd\u0159i rozhodli pro technologickou cestu \u010di\u0161t\u011bn\u00ed \u201e\u010di\u0161t\u011bn\u00ed RTO + st\u0159edotlak\u00fd parn\u00ed kotel na odpadn\u00ed teplo pro rekuperaci tepla\u201c. V souladu s unik\u00e1tn\u00edm \u201eLe Chater & Inert Gas Correction Theory Safety Air Distribution Algorithm\u201c na\u0161\u00ed spole\u010dnosti jsme se rozhodli zvolit RTO s rota\u010dn\u00edm ventilem o objemu vzduchu 270 000 a obsahem kysl\u00edku 5% ve v\u00fdfukov\u00fdch plynech po spalov\u00e1n\u00ed. Sou\u010dasn\u011b jsme zvolili parn\u00ed kotel s tlakem 5,1 MPa\/46T a 120metrov\u00fdm koncov\u00fdm kom\u00ednem, abychom sn\u00ed\u017eili dopad v\u00fdfukov\u00fdch emis\u00ed na \u017eivotn\u00ed prost\u0159ed\u00ed v tov\u00e1rn\u011b.<\/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\u00ed za\u0159\u00edzen\u00ed vyu\u017e\u00edv\u00e1 jeden rota\u010dn\u00ed ventil RTO s objemem vzduchu 270 000, \u010dtvercov\u00e9ho uspo\u0159\u00e1d\u00e1n\u00ed, vybaven\u00fd 3 rota\u010dn\u00edmi ventily pro rozvod vzduchu a 36 komorami pro akumulaci tepla.<\/p>\n
\n- Komplexn\u00ed l\u00e9\u010dba:<\/strong>
Vybaven rota\u010dn\u00edm RTO o objemu 270 000 vzduchu, polyoxymethylenov\u00fd koncov\u00fd plyn sm\u00edchan\u00fd se vzduchem pro dopln\u011bn\u00ed kysl\u00edku
Vyu\u017eit\u00ed odpadn\u00edho tepla: 46 t\/h, nasycen\u00e1 p\u00e1ra 5,1 MPa
<\/strong><\/li>\n- Normy ochrany \u017eivotn\u00edho prost\u0159ed\u00ed:<\/strong>
celkov\u00e9 emise nemetanov\u00fdch uhlovod\u00edk\u016f <50 mg\/m\u00b3, ro\u010dn\u00ed sn\u00ed\u017een\u00ed emis\u00ed uhl\u00edku o p\u0159ibli\u017en\u011b 860 000 tun;
<\/strong><\/li>\n- Doba n\u00e1vratnosti:<\/strong> 3 roky<\/li>\n<\/ul>\n
![\"POUZDRO](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-3.webp\" "\\"\\"")
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[\/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- Briefing komplexn\u00edho \u0159\u00edzen\u00ed\/\u0159et\u011bzce<\/li>\n
- Anal\u00fdza HAZOP<\/li>\n
- Hodnocen\u00ed 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
Inovace 1 \u2013 Pr\u016flom v oblasti doln\u00ed meze v\u00fdbu\u0161nosti za inertn\u00edch podm\u00ednek<\/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 p\u0159ed rozvodem vzduchu<\/strong><\/h4>\n\n\n\nV\u00fdpo\u010det mez\u00ed v\u00fdbu\u0161nosti ho\u0159lav\u00e9 slo\u017eky sm\u011bsi<\/td>\n<\/tr>\n \nVzorec Richarda Chateliho: Lf=100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \nMez v\u00fdbu\u0161nosti sm\u011bsi plyn\u016f Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \nCelkov\u00e1 koncentrace ho\u0159lav\u00fdch slo\u017eek<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\nKonven\u010dn\u00ed distribuce vzduchu: Koncentrace ho\u0159lav\u00fdch slo\u017eek je sn\u00ed\u017eena na <1,065, co\u017e znamen\u00e1, \u017ee distribuce vzduchu mus\u00ed b\u00fdt 2,6kr\u00e1t v\u011bt\u0161\u00ed a celkov\u00fd objem vzduchu dosahuje 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
Zva\u017ete vliv inertn\u00edho plynu na doln\u00ed mez v\u00fdbu\u0161nosti.<\/strong><\/h4>\n![\"POUZDRO](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-4.webp\" "\\"\\"")
<\/p>\n
Pokud vezmeme v \u00favahu pouze p\u0159\u00edvod kysl\u00edku, je p\u0159\u00edvod vzduchu 100 000 a celkov\u00fd objem vzduchu je 220 000.<\/p>\n
1. Vzdu\u0161n\u00e9 pozad\u00ed, doln\u00ed mez v\u00fdbu\u0161nosti p\u0159i 900 \u00b0C je 25%LEL;
2. Inertn\u00ed pozad\u00ed, neho\u0159lav\u00e9 a nev\u00fdbu\u0161n\u00e9 p\u0159i pokojov\u00e9 teplot\u011b, ale p\u0159i vysok\u00e9 teplot\u011b?<\/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
Inovace 2 \u2013 N\u00e1vrh a pou\u017eit\u00ed \u010dtvercov\u00e9 struktury RTO s velk\u00fdm objemem vzduchu<\/h3>\n
![\"POUZDRO](\"https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-RTO-CASE-5.webp\" "\\"\\"")
<\/p>\n
<\/p>\n
\n\n\n\nV\u00fdkonnostn\u00ed parametry<\/td>\n Rota\u010dn\u00ed ventil RTO<\/td>\n Zdvihov\u00fd 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 \nStruktura sm\u011brov\u00e9ho ventilu<\/td>\n Rota\u010dn\u00ed ventil<\/td>\n Zdvihov\u00fd ventil<\/td>\n<\/tr>\n \nPo\u010det reverzn\u00edch ventil\u016f<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \nFrekvence r\u00e1z\u016f p\u0159i p\u0159ep\u00edn\u00e1n\u00ed reverzn\u00edho ventilu<\/td>\n Nep\u0159etr\u017eit\u00fd provoz bez ot\u0159es\u016f<\/td>\n 6,48 milionkr\u00e1t\/rok<\/td>\n<\/tr>\n \nPo\u010det akumula\u010dn\u00edch l\u016f\u017eek<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \nObjem vzduchu na komoru<\/td>\n 20000 Nm\u00b3\/h<\/td>\n 75000 Nm\u00b3\/h<\/td>\n<\/tr>\n \nPlocha pr\u016f\u0159ezu jedn\u00e9 akumula\u010dn\u00ed komory tepla<\/td>\n 3\u33a1<\/td>\n 14\u33a1<\/td>\n<\/tr>\n \nPlnic\u00ed hmotnost jednokomorov\u00e9 keramick\u00e9 akumula\u010dn\u00ed n\u00e1dr\u017ee tepla<\/td>\n 3300 kg<\/td>\n 15600 kg<\/td>\n<\/tr>\n \nPo\u010det ho\u0159\u00e1k\u016f (kus\u016f)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \nObsazenost (d\u00e9lka*\u0161\u00ed\u0159ka)<\/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\u00ed technick\u00e9 ukazatele ochrany \u017eivotn\u00edho prost\u0159ed\u00ed<\/strong><\/p>\n\n\n\n\nN\u00e1zev parametru<\/td>\n Data<\/td>\n<\/tr>\n \nN\u00edzkometanov\u00e9 v\u00fdfukov\u00e9 plyny\/10 000 m\u00b3\/h<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \nDopl\u0148kov\u00fd kysl\u00edk ve vzduchu\/10 000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \nObsah kysl\u00edku ve spalin\u00e1ch za n\u00edzk\u00fdch teplot %<\/td>\n 5<\/td>\n<\/tr>\n \nTeplota pece \u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \nOxidy dus\u00edku ve v\u00fdfukov\u00fdch plynech mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \nCelkov\u00e9 nemetanov\u00e9 uhlovod\u00edky ve v\u00fdfukov\u00fdch plynech 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\u00ed ekonomick\u00e9 ukazatele<\/strong><\/p>\n\n\n\n\nN\u00e1zev parametru<\/td>\n Data<\/td>\n<\/tr>\n \nInstalovan\u00fd v\u00fdkon rozvodn\u00e9 s\u00edt\u011b<\/td>\n 1200 kW\/h<\/td>\n<\/tr>\n \nN\u00e1klady na elekt\u0159inu<\/td>\n 4,8 milionu juan\u016f\/rok<\/td>\n<\/tr>\n \nV\u00fdkon p\u00e1ry kotle na odpadn\u00ed teplo<\/td>\n 45 t\/h<\/td>\n<\/tr>\n \nParametry p\u00e1ry<\/td>\n 4,9 MPa, 420 \u00b0C<\/td>\n<\/tr>\n \nCena ve slu\u017eb\u011b Steam<\/td>\n 120 juan\u016f\/t<\/td>\n<\/tr>\n \nP\u0159\u00edm\u00e9 ekonomick\u00e9 v\u00fdhody<\/td>\n 43,2 milionu juan\u016f\/rok<\/td>\n<\/tr>\n \nSn\u00ed\u017een\u00ed spot\u0159eby surov\u00e9ho uhl\u00ed<\/td>\n 50 000 tun\/rok<\/td>\n<\/tr>\n \nSn\u00ed\u017een\u00ed emis\u00ed uhl\u00edku<\/td>\n 860 000 tun\/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. 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Zply\u0148ov\u00e1n\u00ed uhl\u00ed: ozna\u010duje ne\u00faplnou reakci mezi r\u016fzn\u00fdmi druhy uhl\u00ed (koks) a kysl\u00edkat\u00fdmi zply\u0148ovac\u00edmi \u010dinidly (H2O, O2, CO2) ve zply\u0148ova\u010di. Za vysok\u00e9 teploty a ur\u010dit\u00e9ho tlaku nakonec vznik\u00e1 surov\u00fd sv\u00edtiplyn slo\u017een\u00fd z H2, CH4, CO, CO2, N2, stopov\u00e9ho mno\u017estv\u00ed H2S, COS atd.<\/p>\n
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Klasifikace proces\u016f zply\u0148ov\u00e1n\u00ed uhl\u00ed:<\/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 prom\u00fdv\u00e1n\u00ed methanolem p\u0159i n\u00edzk\u00fdch teplot\u00e1ch: pou\u017eit\u00ed studen\u00e9ho methanolu jako absorp\u010dn\u00edho rozpou\u0161t\u011bdla s vyu\u017eit\u00edm vysok\u00e9 rozpustnosti methanolu v kysel\u00fdch plynech p\u0159i n\u00edzk\u00fdch teplot\u00e1ch k odstran\u011bn\u00ed kysel\u00fdch plyn\u016f, zejm\u00e9na CO2 a H2S, ze vstupn\u00edho 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=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row column_structure=”1_3,2_3″ use_custom_gutter=”on” gutter_width=”2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”1_3″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n Charakteristiky v\u00fdfukov\u00fdch plyn\u016f z n\u00edzkoteplotn\u00edho pran\u00ed methanolem:<\/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 Vzhledem k tomu, \u017ee v\u00fdfukov\u00e9 plyny neobsahuj\u00ed t\u00e9m\u011b\u0159 \u017e\u00e1dn\u00fd kysl\u00edk, je nutn\u00e9 je dopl\u0148ovat vzduchem, aby se splnila pot\u0159eba kysl\u00edku pro \u00faplnou oxidaci v\u00fdfukov\u00fdch plyn\u016f. 1) Bezpe\u010dnostn\u00ed aspekty: anal\u00fdza nebezpe\u010d\u00ed v\u00fdbuchu<\/strong><\/em><\/p>\n Podle technick\u00e9 specifikace pro \u010di\u0161t\u011bn\u00ed pr\u016fmyslov\u00fdch organick\u00fdch odpadn\u00edch plyn\u016f metodou tepeln\u00e9ho akumula\u010dn\u00edho spalov\u00e1n\u00ed by koncentrace organick\u00e9 hmoty vstupuj\u00edc\u00ed do za\u0159\u00edzen\u00ed RTO m\u011bla b\u00fdt ni\u017e\u0161\u00ed ne\u017e 25% doln\u00ed meze v\u00fdbu\u0161nosti. Vypo\u010d\u00edtejte doln\u00ed mez v\u00fdbu\u0161nosti komplexn\u00edch sm\u011bs\u00ed ho\u0159lav\u00fdch plyn\u016f pomoc\u00ed Le Chatlierova vzorce a pot\u00e9 porovnejte koncentraci ho\u0159lav\u00fdch slo\u017eek ve v\u00fdfukov\u00fdch plynech s velikost\u00ed 25% LEL, abyste ur\u010dili bezpe\u010dnost koncentrace ho\u0159lav\u00fdch slo\u017eek ve v\u00fdfukov\u00fdch plynech.<\/p>\n 2) \u00davahy o rychlosti \u010di\u0161t\u011bn\u00ed: \u201e3T1O\u201c<\/em><\/strong><\/p>\n [\/et_pb_text][\/et_pb_column][et_pb_column type=”1_2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-oxygen-supplementation-air-volume.webp” alt=”oxygen supplementation air volume” title_text=”0 oxygen supplementation air volume” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n Obvykle se navrhuj\u00ed bez ohledu na vliv inertn\u00edch plyn\u016f, spodn\u00ed mez v\u00fdbu\u0161nosti v\u00fdfukov\u00fdch plyn\u016f se vypo\u010d\u00edt\u00e1v\u00e1 a pom\u011br \u0159ed\u011bn\u00ed vzduchem se ur\u010duje na z\u00e1klad\u011b vztahu mezi koncentrac\u00ed v\u00fdfukov\u00fdch plyn\u016f a limitn\u00ed hodnotou v\u00fdbu\u0161nosti 25%. Tento v\u00fdpo\u010det m\u016f\u017ee zajistit jiskrovou bezpe\u010dnost, ale objem v\u00fdfukov\u00fdch plyn\u016f je relativn\u011b velk\u00fd.<\/p>\n Vzhledem k p\u0159\u00edtomnosti velk\u00e9ho mno\u017estv\u00ed inertn\u00edho plynu CO2 ve v\u00fdfukov\u00e9m plynu N2 z n\u00edzkoteplotn\u00edho prom\u00fdv\u00e1n\u00ed methanolem a mal\u00e9ho mno\u017estv\u00ed ho\u0159lav\u00fdch slo\u017eek, V\u00fdfukov\u00e9 plyny z n\u00edzkoteplotn\u00edho pran\u00ed methanolem proto nemaj\u00ed horn\u00ed ani doln\u00ed mez 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 Sm\u011bs v\u00fdfukov\u00fdch plyn\u016f je navr\u017eena pro dopln\u011bn\u00ed kysl\u00edku na z\u00e1klad\u011b materi\u00e1lov\u00e9 bilance s obsahem kysl\u00edku ve spalin\u00e1ch okolo 5%.<\/p>\n Porovn\u00e1n\u00ed koncentrace ho\u0159lav\u00fdch slo\u017eek ve v\u00fdfukov\u00fdch plynech po dopln\u011bn\u00ed kysl\u00edkem a doln\u00ed mez\u00ed v\u00fdbu\u0161nosti v\u00fdfukov\u00fdch plyn\u016f (bez inertn\u00edch plyn\u016f)<\/p>\n <\/p>\n 1) N\u00edzk\u00fd objem v\u00fdfukov\u00fdch plyn\u016f<\/em><\/strong> [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-5.webp” alt=”waste gas component” title_text=”0 waste gas component 5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][et_pb_column type=”3_5″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-4.webp” alt=”waste gas component” title_text=”0 waste gas component 4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-waste-gas-component-2-1.webp” alt=”waste gas component” title_text=”0 waste gas component 2″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” custom_margin=”|auto|17px|auto||” custom_padding=”||50px|||” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Low-methane-waste-gas.webp” alt=”Low-methane waste gas” title_text=”0 Low-methane waste gas” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][et_pb_image src=”https:\/\/regenerative-thermal-oxidizers.com\/wp-content\/uploads\/2024\/12\/0-Heat-balance.webp” alt=”Heat balance” title_text=”0 Heat balance” align=”center” _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][\/et_pb_image][\/et_pb_column][\/et_pb_row][\/et_pb_section][et_pb_section fb_built=”1″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_row _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_column type=”4_4″ _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”][et_pb_text _builder_version=”4.27.4″ _module_preset=”default” global_colors_info=”{}”]<\/p>\n [\/et_pb_text][\/et_pb_column][\/et_pb_row][et_pb_row _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_column type=\u201d4_4\u2033 _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d][et_pb_text _builder_version=\u201d4.27.4\u2033 _module_preset=\u201ddefault\u201d global_colors_info=\u201d{}\u201d]<\/p>\n Jednotka metanolu spole\u010dnosti Xinye Energy Chemical s kapacitou 525 000 tun\/rok vyu\u017e\u00edv\u00e1 technologii tlakov\u00e9ho zply\u0148ov\u00e1n\u00ed drcen\u00e9ho uhl\u00ed. Krom\u011b hlavn\u00edch slo\u017eek CO2 a N2 obsahuje n\u00edzkoteplotn\u00ed odpadn\u00ed plyn z prop\u00edr\u00e1n\u00ed metanolem tak\u00e9 metan, celkov\u00e9 nemetanov\u00e9 uhlovod\u00edky, CO, methanol atd. Tento odpadn\u00ed plyn je v sou\u010dasn\u00e9 dob\u011b odv\u00e1d\u011bn kom\u00ednem kotle. Podle po\u017eadavk\u016f na ochranu \u017eivotn\u00edho prost\u0159ed\u00ed je nutn\u00e9 prov\u00e9st \u010di\u0161t\u011bn\u00ed VOC. Krom\u011b toho m\u00e1 jednotka polyoxymethylenu tak\u00e9 t\u0159i odpadn\u00ed plyny, kter\u00e9 je t\u0159eba \u010distit.<\/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\u00e1klad\u011b charakteristik ho\u0159lav\u00fdch slo\u017eek ve v\u00fdfukov\u00fdch plynech se na\u0161i in\u017een\u00fd\u0159i rozhodli pro technologickou cestu \u010di\u0161t\u011bn\u00ed \u201e\u010di\u0161t\u011bn\u00ed RTO + st\u0159edotlak\u00fd parn\u00ed kotel na odpadn\u00ed teplo pro rekuperaci tepla\u201c. V souladu s unik\u00e1tn\u00edm \u201eLe Chater & Inert Gas Correction Theory Safety Air Distribution Algorithm\u201c na\u0161\u00ed spole\u010dnosti jsme se rozhodli zvolit RTO s rota\u010dn\u00edm ventilem o objemu vzduchu 270 000 a obsahem kysl\u00edku 5% ve v\u00fdfukov\u00fdch plynech po spalov\u00e1n\u00ed. Sou\u010dasn\u011b jsme zvolili parn\u00ed kotel s tlakem 5,1 MPa\/46T a 120metrov\u00fdm koncov\u00fdm kom\u00ednem, abychom sn\u00ed\u017eili dopad v\u00fdfukov\u00fdch emis\u00ed na \u017eivotn\u00ed prost\u0159ed\u00ed v tov\u00e1rn\u011b.<\/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\u00ed za\u0159\u00edzen\u00ed vyu\u017e\u00edv\u00e1 jeden rota\u010dn\u00ed ventil RTO s objemem vzduchu 270 000, \u010dtvercov\u00e9ho uspo\u0159\u00e1d\u00e1n\u00ed, vybaven\u00fd 3 rota\u010dn\u00edmi ventily pro rozvod vzduchu a 36 komorami pro akumulaci 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\u00ed distribuce vzduchu: Koncentrace ho\u0159lav\u00fdch slo\u017eek je sn\u00ed\u017eena na <1,065, co\u017e znamen\u00e1, \u017ee distribuce vzduchu mus\u00ed b\u00fdt 2,6kr\u00e1t v\u011bt\u0161\u00ed a celkov\u00fd objem vzduchu dosahuje 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 Pokud vezmeme v \u00favahu pouze p\u0159\u00edvod kysl\u00edku, je p\u0159\u00edvod vzduchu 100 000 a celkov\u00fd objem vzduchu je 220 000.<\/p>\n 1. Vzdu\u0161n\u00e9 pozad\u00ed, doln\u00ed mez v\u00fdbu\u0161nosti p\u0159i 900 \u00b0C 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\u00ed technick\u00e9 ukazatele ochrany \u017eivotn\u00edho prost\u0159ed\u00ed<\/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\u00ed ekonomick\u00e9 ukazatele<\/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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P\u0159ehledov\u00e1 tabulka slo\u017eek surov\u00e9ho plynu produkovan\u00fdch r\u016fzn\u00fdmi procesy zply\u0148ov\u00e1n\u00ed<\/strong><\/h2>\n
Co je to n\u00edzkoteplotn\u00ed methanolov\u00e9 pran\u00ed<\/strong><\/h2>\n
N\u00edzkoteplotn\u00ed pran\u00ed methanolem je metoda, kterou spole\u010dn\u011b vyvinuly spole\u010dnosti Linde a Lurgi na po\u010d\u00e1tku 50. let 20. stolet\u00ed k odstran\u011bn\u00ed kysel\u00fdch plyn\u016f ze surovinov\u00fdch plyn\u016f. V roce 1954 byla poprv\u00e9 pou\u017eita k \u010di\u0161t\u011bn\u00ed plynu v pr\u016fmyslu tlakov\u00e9ho zply\u0148ov\u00e1n\u00ed uhl\u00ed v Ji\u017en\u00ed Africe.
<\/strong><\/p>\n\n
Vlastnosti odpadn\u00edch plyn\u016f<\/strong><\/h2>\n
\n
Stanoven\u00ed objemu vzduchu pro dopl\u0148ov\u00e1n\u00ed kysl\u00edku<\/strong><\/h2>\n
Princip pro ur\u010den\u00ed mno\u017estv\u00ed p\u0159\u00eddavn\u00e9ho vzduchu:<\/p>\n\n
Podle v\u00fdpo\u010dtov\u00e9 metody pro sm\u011bs obsahuj\u00edc\u00ed n ho\u0159lav\u00fdch plyn\u016f a p inertn\u00edch plyn\u016f lze ur\u010dit, \u017ee n\u00edzkokvalitn\u00ed sm\u011bs v\u00fdfukov\u00fdch plyn\u016f ho\u0159lav\u00fdch a inertn\u00edch plyn\u016f je neho\u0159lav\u00e1 a nev\u00fdbu\u0161n\u00e1.<\/p>\n
Mno\u017estv\u00ed dopl\u0148ovan\u00e9ho vzduchu pro odpadn\u00ed plyn z n\u00edzkoteplotn\u00edho pran\u00ed methanolem lze ur\u010dit na z\u00e1klad\u011b obsahu kysl\u00edku ve spalin\u00e1ch po \u00fapln\u00e9 oxidaci vy\u0161\u0161\u00edho ne\u017e 3%.<\/p>\nV\u00fdpo\u010det ho\u0159lavosti sm\u011bsi v\u00fdfukov\u00fdch plyn\u016f ve vzduchu\u00a0<\/h3>\n
Zpracov\u00e1n\u00ed celkov\u00e9ho objemu vzduchu<\/strong><\/h4>\n
2) Objem vzduchu pro dopl\u0148ov\u00e1n\u00ed kysl\u00edku<\/em><\/strong><\/p>\n\u2460 Materi\u00e1lov\u00e1 bilance<\/strong><\/h2>\n
\u00a0\u2461 Tepeln\u00e1 bilance<\/strong><\/h2>\n
Typick\u00e9 in\u017een\u00fdrsk\u00e9 p\u0159\u00edpady<\/strong><\/h2>\n
Anal\u00fdza situace<\/h3>\n
Trasa procesu<\/h3>\n
\n
Vybaven rota\u010dn\u00edm RTO o objemu 270 000 vzduchu, polyoxymethylenov\u00fd koncov\u00fd plyn sm\u00edchan\u00fd se vzduchem pro dopln\u011bn\u00ed kysl\u00edku
Vyu\u017eit\u00ed odpadn\u00edho tepla: 46 t\/h, nasycen\u00e1 p\u00e1ra 5,1 MPa
<\/strong><\/li>\n
celkov\u00e9 emise nemetanov\u00fdch uhlovod\u00edk\u016f <50 mg\/m\u00b3, ro\u010dn\u00ed sn\u00ed\u017een\u00ed emis\u00ed uhl\u00edku o p\u0159ibli\u017en\u011b 860 000 tun;
<\/strong><\/li>\n<\/p>\nAnal\u00fdza bezpe\u010dnosti<\/h3>\n
\n
Inovace 1 \u2013 Pr\u016flom v oblasti doln\u00ed meze v\u00fdbu\u0161nosti za inertn\u00edch podm\u00ednek<\/h3>\n
125 000 p\u0159ed rozvodem vzduchu<\/strong><\/h4>\n
\n\n
\n V\u00fdpo\u010det mez\u00ed v\u00fdbu\u0161nosti ho\u0159lav\u00e9 slo\u017eky sm\u011bsi<\/td>\n<\/tr>\n \n Vzorec Richarda Chateliho: Lf=100\/\uff08V1\/L1+V2\/L2+\u2026\u2026+Vn\/Ln\uff09<\/td>\n<\/tr>\n \n Mez v\u00fdbu\u0161nosti sm\u011bsi plyn\u016f Lf, %<\/td>\n 4.26<\/td>\n<\/tr>\n \n 25%LEL<\/td>\n 1.065<\/td>\n<\/tr>\n \n Celkov\u00e1 koncentrace ho\u0159lav\u00fdch slo\u017eek<\/td>\n 2.777<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n Zva\u017ete vliv inertn\u00edho plynu na doln\u00ed mez v\u00fdbu\u0161nosti.<\/strong><\/h4>\n
<\/p>\n
2. Inertn\u00ed pozad\u00ed, neho\u0159lav\u00e9 a nev\u00fdbu\u0161n\u00e9 p\u0159i pokojov\u00e9 teplot\u011b, ale p\u0159i vysok\u00e9 teplot\u011b?<\/p>\nInovace 2 \u2013 N\u00e1vrh a pou\u017eit\u00ed \u010dtvercov\u00e9 struktury RTO s velk\u00fdm objemem vzduchu<\/h3>\n
<\/p>\n\n\n
\n V\u00fdkonnostn\u00ed parametry<\/td>\n Rota\u010dn\u00ed ventil RTO<\/td>\n Zdvihov\u00fd 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 Struktura sm\u011brov\u00e9ho ventilu<\/td>\n Rota\u010dn\u00ed ventil<\/td>\n Zdvihov\u00fd ventil<\/td>\n<\/tr>\n \n Po\u010det reverzn\u00edch ventil\u016f<\/td>\n 3<\/td>\n 27<\/td>\n<\/tr>\n \n Frekvence r\u00e1z\u016f p\u0159i p\u0159ep\u00edn\u00e1n\u00ed reverzn\u00edho ventilu<\/td>\n Nep\u0159etr\u017eit\u00fd provoz bez ot\u0159es\u016f<\/td>\n 6,48 milionkr\u00e1t\/rok<\/td>\n<\/tr>\n \n Po\u010det akumula\u010dn\u00edch l\u016f\u017eek<\/td>\n 36<\/td>\n 9<\/td>\n<\/tr>\n \n Objem vzduchu na komoru<\/td>\n 20000 Nm\u00b3\/h<\/td>\n 75000 Nm\u00b3\/h<\/td>\n<\/tr>\n \n Plocha pr\u016f\u0159ezu jedn\u00e9 akumula\u010dn\u00ed komory tepla<\/td>\n 3\u33a1<\/td>\n 14\u33a1<\/td>\n<\/tr>\n \n Plnic\u00ed hmotnost jednokomorov\u00e9 keramick\u00e9 akumula\u010dn\u00ed n\u00e1dr\u017ee tepla<\/td>\n 3300 kg<\/td>\n 15600 kg<\/td>\n<\/tr>\n \n Po\u010det ho\u0159\u00e1k\u016f (kus\u016f)<\/td>\n 3<\/td>\n 5<\/td>\n<\/tr>\n \n Obsazenost (d\u00e9lka*\u0161\u00ed\u0159ka)<\/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\u00e1zev parametru<\/td>\n Data<\/td>\n<\/tr>\n \n N\u00edzkometanov\u00e9 v\u00fdfukov\u00e9 plyny\/10 000 m\u00b3\/h<\/td>\n 10.8-12.5<\/td>\n<\/tr>\n \n Dopl\u0148kov\u00fd kysl\u00edk ve vzduchu\/10 000 m\u00b3\/h<\/td>\n 10.5-11.5<\/td>\n<\/tr>\n \n Obsah kysl\u00edku ve spalin\u00e1ch za n\u00edzk\u00fdch teplot %<\/td>\n 5<\/td>\n<\/tr>\n \n Teplota pece \u2103<\/td>\n 960-990<\/td>\n<\/tr>\n \n Oxidy dus\u00edku ve v\u00fdfukov\u00fdch plynech mg\/m\u00b3<\/td>\n 4.5-10<\/td>\n<\/tr>\n \n Celkov\u00e9 nemetanov\u00e9 uhlovod\u00edky ve v\u00fdfukov\u00fdch plynech mg\/m\u00b3<\/td>\n 40-60<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n \n\n
\n N\u00e1zev parametru<\/td>\n Data<\/td>\n<\/tr>\n \n Instalovan\u00fd v\u00fdkon rozvodn\u00e9 s\u00edt\u011b<\/td>\n 1200 kW\/h<\/td>\n<\/tr>\n \n N\u00e1klady na elekt\u0159inu<\/td>\n 4,8 milionu juan\u016f\/rok<\/td>\n<\/tr>\n \n V\u00fdkon p\u00e1ry kotle na odpadn\u00ed teplo<\/td>\n 45 t\/h<\/td>\n<\/tr>\n \n Parametry p\u00e1ry<\/td>\n 4,9 MPa, 420 \u00b0C<\/td>\n<\/tr>\n \n Cena ve slu\u017eb\u011b Steam<\/td>\n 120 juan\u016f\/t<\/td>\n<\/tr>\n \n P\u0159\u00edm\u00e9 ekonomick\u00e9 v\u00fdhody<\/td>\n 43,2 milionu juan\u016f\/rok<\/td>\n<\/tr>\n \n Sn\u00ed\u017een\u00ed spot\u0159eby surov\u00e9ho uhl\u00ed<\/td>\n 50 000 tun\/rok<\/td>\n<\/tr>\n \n Sn\u00ed\u017een\u00ed emis\u00ed uhl\u00edku<\/td>\n 860 000 tun\/rok<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n