. "Na \u010Dtvrtprovozn\u00EDm za\u0159\u00EDzen\u00ED pro tepeln\u011B \u2013 tlakovou hydrol\u00FDzu o vstupn\u00EDm v\u00FDkonu 30 kg . h-1 bylo prov\u00E1d\u011Bno zpracov\u00E1n\u00ED lignocelulozov\u00FDch odpad\u016F na zkvasiteln\u00E9 cukry a dal\u0161\u00ED produkty, zejm\u00E9na 92% fural, \u010Dist\u00FD lignin a organick\u00E9 kyseliny. K hydrol\u00FDzn\u00EDm experiment\u016Fm byla pou\u017Eita p\u0161eni\u010Dn\u00E1 sl\u00E1ma jako modelov\u00FD substr\u00E1t, d\u00E1le d\u0159evn\u00ED a pap\u00EDrensk\u00E9 odpady a odpady z ve\u0159ejn\u00E9 zelen\u011B. Hydrol\u00FDza byla prov\u00E1d\u011Bna z hydromodulem 5 : 1, p\u0159i teplot\u011B 167 \u2013 198\u00B0C, p\u0159i tlaku 1,0 \u2013 1,5 MPa a p\u0159i expozici 10 \u2013 15 minut. Nejvy\u0161\u0161\u00ED v\u00FDt\u011B\u017Eky hydrol\u00FDzn\u00EDch produkt\u016F byly z\u00EDsk\u00E1ny p\u0159i teplot\u00E1ch 195 \u2013 198\u00B0C a p\u0159i n\u00E1st\u0159iku kyselin do vs\u00E1zky a to a\u017E na pH 3,5. Mezi chemick\u00FDm slo\u017Een\u00EDm hydrolaz\u00E1t\u016F z testovan\u00FDch lignocelulozov\u00FDch odpad\u016F jsou z\u00E1sadn\u00ED rozd\u00EDly v z\u00E1vislosti na obsahu celulozy a hemicelulozy v testovan\u00FDch odpadech. Alkoholov\u00E1 v\u00FDt\u011B\u017Enost 1 t su\u0161iny lignocelulozov\u00FDch odpad\u016F p\u0159edstavuje v pr\u016Fm\u011Bru 330 l bezvod\u00E9ho alkoholu. V z\u00E1v\u011Bru p\u0159\u00EDsp\u011Bvku jsou uv\u00E1d\u011Bny technicko ekonomick\u00E9 \u00FAdaje obdobn\u00E9ho za\u0159\u00EDzen\u00ED na zpracov\u00E1n\u00ED lignocelulozov\u00FDch odpad\u016F"@cs . . "Zpracov\u00E1n\u00ED lignocelul\u00F3zov\u00FDch odpad\u016F na zkvasiteln\u00E9 cukry a dal\u0161\u00ED produkty v biorafinerii"@cs . . "Na \u010Dtvrtprovozn\u00EDm za\u0159\u00EDzen\u00ED pro tepeln\u011B \u2013 tlakovou hydrol\u00FDzu o vstupn\u00EDm v\u00FDkonu 30 kg . h-1 bylo prov\u00E1d\u011Bno zpracov\u00E1n\u00ED lignocelulozov\u00FDch odpad\u016F na zkvasiteln\u00E9 cukry a dal\u0161\u00ED produkty, zejm\u00E9na 92% fural, \u010Dist\u00FD lignin a organick\u00E9 kyseliny. K hydrol\u00FDzn\u00EDm experiment\u016Fm byla pou\u017Eita p\u0161eni\u010Dn\u00E1 sl\u00E1ma jako modelov\u00FD substr\u00E1t, d\u00E1le d\u0159evn\u00ED a pap\u00EDrensk\u00E9 odpady a odpady z ve\u0159ejn\u00E9 zelen\u011B. Hydrol\u00FDza byla prov\u00E1d\u011Bna z hydromodulem 5 : 1, p\u0159i teplot\u011B 167 \u2013 198\u00B0C, p\u0159i tlaku 1,0 \u2013 1,5 MPa a p\u0159i expozici 10 \u2013 15 minut. Nejvy\u0161\u0161\u00ED v\u00FDt\u011B\u017Eky hydrol\u00FDzn\u00EDch produkt\u016F byly z\u00EDsk\u00E1ny p\u0159i teplot\u00E1ch 195 \u2013 198\u00B0C a p\u0159i n\u00E1st\u0159iku kyselin do vs\u00E1zky a to a\u017E na pH 3,5. Mezi chemick\u00FDm slo\u017Een\u00EDm hydrolaz\u00E1t\u016F z testovan\u00FDch lignocelulozov\u00FDch odpad\u016F jsou z\u00E1sadn\u00ED rozd\u00EDly v z\u00E1vislosti na obsahu celulozy a hemicelulozy v testovan\u00FDch odpadech. Alkoholov\u00E1 v\u00FDt\u011B\u017Enost 1 t su\u0161iny lignocelulozov\u00FDch odpad\u016F p\u0159edstavuje v pr\u016Fm\u011Bru 330 l bezvod\u00E9ho alkoholu. V z\u00E1v\u011Bru p\u0159\u00EDsp\u011Bvku jsou uv\u00E1d\u011Bny technicko ekonomick\u00E9 \u00FAdaje obdobn\u00E9ho za\u0159\u00EDzen\u00ED na zpracov\u00E1n\u00ED lignocelulozov\u00FDch odpad\u016F" . "Zpracov\u00E1n\u00ED lignocelul\u00F3zov\u00FDch odpad\u016F na zkvasiteln\u00E9 cukry a dal\u0161\u00ED produkty v biorafinerii" . "1" . . "Processing of lignocelulose wastes into fermentable sugars and other products through biorefineries"@en . "P(QH81265)" . "Agritech Science" . "Processing of lignocelulose wastes into fermentable sugars and other products through biorefineries"@en . . "2"^^ . . "thermal-pressure hydrolysis; lignocelluloses waste; agricultural biomass; fermentable sugars; furfural; lignin"@en . . "2"^^ . "3" . "[38D94F5655EA]" . . "Zpracov\u00E1n\u00ED lignocelul\u00F3zov\u00FDch odpad\u016F na zkvasiteln\u00E9 cukry a dal\u0161\u00ED produkty v biorafinerii"@cs . . . . "353477" . "Us\u0165ak, Sergej" . . . . "RIV/00027006:_____/09:00000937!RIV10-MZE-00027006" . . "V\u00E1\u0148a, Jaroslav" . "Zpracov\u00E1n\u00ED lignocelul\u00F3zov\u00FDch odpad\u016F na zkvasiteln\u00E9 cukry a dal\u0161\u00ED produkty v biorafinerii" . "6"^^ . . . . "RIV/00027006:_____/09:00000937" . . "CZ - \u010Cesk\u00E1 republika" . "1802-8942" . "The lignocellulosic waste processing into fermentable sugars, furfural and lignin was carried out on a quarter \u2013 pilot processing scale with a input power 30 kg . h-1. The hydrolysis was carried out at a hydromodul ratio of 5: 1, at 167 to 198 \u00B0 C, at a pressure from 1.0 to 1.5 MPa with exposure time from 10 to 15 minutes. The highest yields of hydrolytic products were gained at temperatures from 195 to 198 \u00B0C with acid addiction into to substrate to pH 3.5. There are major differences in the content of cellulose and hemicellulose among the tested lignocellulosic hydrolytic wastes. The wheat straw, the wood, paper waste and waste from the public green areas were used as model substrates for hydrolytic experiments. The alcohol yield of 1 t of dry matter of lignocellulosic waste is on average 330 l of anhydrous alcohol. In conclusion of this contribution are the technical and economic data of a similar arrangement for lignocellulosic processing wastes with initial output of 1000 kg of dry matter. h-1,"@en .