RU93052367A - REGENERATIVE GLASS-MAKED FURNACE AND THE METHOD OF HER WORK - Google Patents

REGENERATIVE GLASS-MAKED FURNACE AND THE METHOD OF HER WORK

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Publication number
RU93052367A
RU93052367A RU93052367/33A RU93052367A RU93052367A RU 93052367 A RU93052367 A RU 93052367A RU 93052367/33 A RU93052367/33 A RU 93052367/33A RU 93052367 A RU93052367 A RU 93052367A RU 93052367 A RU93052367 A RU 93052367A
Authority
RU
Russia
Prior art keywords
glass
furnace
exhaust gases
regenerators
regenerative
Prior art date
Application number
RU93052367/33A
Other languages
Russian (ru)
Other versions
RU2107667C1 (en
Inventor
Квирк Ричард
Алан Берд Дэвид
Найджел Вулльям Шалвер Ян
Максвелл Мкинтош Робин
Original Assignee
Пилкингтон Гласс Лимитед
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from GB929224852A external-priority patent/GB9224852D0/en
Application filed by Пилкингтон Гласс Лимитед filed Critical Пилкингтон Гласс Лимитед
Publication of RU93052367A publication Critical patent/RU93052367A/en
Application granted granted Critical
Publication of RU2107667C1 publication Critical patent/RU2107667C1/en

Links

Claims (1)

Предложен способ работы регенеративной стекловаренной печи для плавки стекла с целью изготовления стеклянных фасонных изделий, минимизирующий эмиссию NOx в отработавших газах, выходящих из печи, имеющей уплотненные регенераторы, действующие как теплообменики, предусматривающий подачу топлива в избытке от количества, которое требуется для стехиометрического сгорания, чтобы обеспечить заданное качество стекла при заданной производительности и наличие горючего материала в обработавших газах, покидающих печь через регенераторы, взаимодействие указанного горючего материала с достаточным количеством воздуха для обеспечения того, чтобы отработавшие газы, выходящие в атмосферу, содержали допустимые уровни горючего материала и допустимые уровни NOx. Альтернативно печь может работать при существенно стехиометрических условиях, а топливо подаваться в отработавшие газы, когда они покидают варочный бассейн. Изобретение также относится к регенеративной стекловаренной печи для реализации данного способа. Изобретение далее предусматривает способ сжигания эмиссии СО в отработавших газах, покидающих регенеративную стекловаренную печь с поперечным направлением пламени для плавки стекла с целью изготовления фасонных стеклянных изделий, имеющую уплотненные регенераторы, действующие как теплообменники, предусматривающий удаление СО из отработавших газов в регенераторе путем сжигания СО в ~ 8% избытка воздуха, считая на количество воздуха для горения поданного топлива, при температуре выше, чем 650oС.A method of operating a regenerative glass melting furnace for melting glass with the aim of manufacturing glass fittings that minimizes NO x emissions in exhaust gases leaving a furnace with condensed regenerators, acting as heat exchangers, providing fuel supply in excess of the amount required for stoichiometric combustion, in order to ensure the specified quality of glass at a given performance and the presence of combustible material in the treated gases leaving the furnace through regenerators, mutually the effect of the specified combustible material with a sufficient amount of air to ensure that the exhaust gases entering the atmosphere contain permissible levels of combustible material and permissible levels of NO x . Alternatively, the stove can operate under substantially stoichiometric conditions, and the fuel can be fed into the exhaust gases when they leave the cooking basin. The invention also relates to a regenerative glass furnace for the implementation of this method. The invention further provides a method for burning CO emissions in exhaust gases leaving a regenerative glass melting furnace with a flame transverse direction for melting glass for the manufacture of shaped glass products, having sealed regenerators acting as heat exchangers, including removing CO from exhaust gases in the regenerator by burning CO into ~ 8% of excess air, counting on the amount of air for combustion of the supplied fuel, at a temperature higher than 650 o C.
RU93052367A 1992-11-27 1993-11-25 Regenerative glass furnace and method of its operation RU2107667C1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
GB9224852.5 1992-11-27
GB929224852A GB9224852D0 (en) 1992-11-27 1992-11-27 Flat glass furnaces
GB9310720.9 1993-05-25
GB939310720A GB9310720D0 (en) 1992-11-27 1993-05-25 Glass furnaces

Publications (2)

Publication Number Publication Date
RU93052367A true RU93052367A (en) 1996-03-27
RU2107667C1 RU2107667C1 (en) 1998-03-27

Family

ID=26302050

Family Applications (1)

Application Number Title Priority Date Filing Date
RU93052367A RU2107667C1 (en) 1992-11-27 1993-11-25 Regenerative glass furnace and method of its operation

Country Status (19)

Country Link
US (4) US5573568A (en)
EP (1) EP0599547B1 (en)
JP (1) JP3313856B2 (en)
CN (1) CN1039899C (en)
AT (2) ATE181717T1 (en)
AU (1) AU667977B2 (en)
BR (1) BR9304854A (en)
CA (1) CA2103468C (en)
CZ (1) CZ285317B6 (en)
DE (3) DE599547T1 (en)
DK (1) DK0599547T3 (en)
ES (1) ES2106290T3 (en)
FI (1) FI935241A (en)
GR (1) GR3024758T3 (en)
HU (1) HU215813B (en)
NO (1) NO313512B1 (en)
PL (1) PL301224A1 (en)
RU (1) RU2107667C1 (en)
TR (1) TR27074A (en)

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CN104524939A (en) * 2014-12-12 2015-04-22 秦皇岛杰伯特环境科技有限公司 Glass denitrification system based on SNCR technology
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US10533743B2 (en) * 2015-06-18 2020-01-14 Praxair Technology, Inc. Thermochemical regeneration with soot formation
CN105797555A (en) * 2016-03-31 2016-07-27 中国中轻国际工程有限公司 Method for selective denitration through non-catalytic reduction method in glass melting furnace heat storage chamber
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CN111111439A (en) * 2020-02-28 2020-05-08 九江润诚新材料有限公司 Multistage denitration ultralow-emission method for regenerator of longitudinal flame energy-saving environment-friendly glass kiln, regenerator and application of method
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