Yüksek saflikta karbon dioksit üretmek için yöntem

Oksijen-yakit ateslemeli cam yapim firini atik gazindan, atik gazin sulu bir söndürme sivisi ile söndürülmesini, kükürt tuzunun gazdan kuru olarak süzülmesini, süzülmüs gazin geri kalan kükürt dioksidi sulu bir sülfit süspansiyonuna dönüstürmek üzere sulu karbonat ile yikanmasini ve bu süspansiyonun...

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Hauptverfasser: CARL SCHATZ, AKHILESH KAPOOR
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AKHILESH KAPOOR
description Oksijen-yakit ateslemeli cam yapim firini atik gazindan, atik gazin sulu bir söndürme sivisi ile söndürülmesini, kükürt tuzunun gazdan kuru olarak süzülmesini, süzülmüs gazin geri kalan kükürt dioksidi sulu bir sülfit süspansiyonuna dönüstürmek üzere sulu karbonat ile yikanmasini ve bu süspansiyonun, yukarida sözü edilen sulu söndürme sivisinin bir kismi veya tamami olarak kullanilmasini, kükürt dioksitten aritilmis atik gazin, azot oksitleri seçimli olarak azota dönüstüren bir katalizör varliginda amonyak ile temas ettirilmesini ve böylece azot oksitlerin esas itibariyla tamaminin atik gazdan uzaklastirlmasini ve meydana gelen atik gaz akiminin destillenmesini, böylece yüksek saflikta sivi karbon dioksit ile firina yakit olarak geri devredilen bir çikis gazi olusturulmasini içeren bir dizi kademe vasitasiyla gida kalitesinde karbon dioksit üretilir. Carbon dioxide is produced from oxyfuel fired glassmaking furnace effluent gas by a series of steps including quenching the waste gas with aqueous quench liquid, comprising a solution of carbonate having a pH in the range of 6-5 to 8, thereby cooling the effluent gas and converting at least part of said sulphate to particulate sulphur salt, filtering particulate sulphur salt from the gas, and returning the particular sulphur salt to the furnace. The filtered gas is preferably scrubbed with aqueous carbonate to convert any remaining sulphur dioxide to an aqueous sulphite suspension and using the suspension as part or all of the above-mentioned aqueous quench liquid. The sulphur dioxide-free waste gas is preferably contacted with ammonia in the presence of a catalyst that selectively converts nitrogen oxides to nitrogen, thereby removing substantially all nitrogen oxides from the waste gas, and the resulting effluent gas stream is separated to produce a pure carbon dioxide product. The catalytic conversion is preferably performed in a series of at least two reactors, the feed gas temperature decreasing and the ratio of ammonia to total nitrogen oxides increasing as the feed gas passes from reactor to reactor.
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Carbon dioxide is produced from oxyfuel fired glassmaking furnace effluent gas by a series of steps including quenching the waste gas with aqueous quench liquid, comprising a solution of carbonate having a pH in the range of 6-5 to 8, thereby cooling the effluent gas and converting at least part of said sulphate to particulate sulphur salt, filtering particulate sulphur salt from the gas, and returning the particular sulphur salt to the furnace. The filtered gas is preferably scrubbed with aqueous carbonate to convert any remaining sulphur dioxide to an aqueous sulphite suspension and using the suspension as part or all of the above-mentioned aqueous quench liquid. The sulphur dioxide-free waste gas is preferably contacted with ammonia in the presence of a catalyst that selectively converts nitrogen oxides to nitrogen, thereby removing substantially all nitrogen oxides from the waste gas, and the resulting effluent gas stream is separated to produce a pure carbon dioxide product. 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Carbon dioxide is produced from oxyfuel fired glassmaking furnace effluent gas by a series of steps including quenching the waste gas with aqueous quench liquid, comprising a solution of carbonate having a pH in the range of 6-5 to 8, thereby cooling the effluent gas and converting at least part of said sulphate to particulate sulphur salt, filtering particulate sulphur salt from the gas, and returning the particular sulphur salt to the furnace. The filtered gas is preferably scrubbed with aqueous carbonate to convert any remaining sulphur dioxide to an aqueous sulphite suspension and using the suspension as part or all of the above-mentioned aqueous quench liquid. The sulphur dioxide-free waste gas is preferably contacted with ammonia in the presence of a catalyst that selectively converts nitrogen oxides to nitrogen, thereby removing substantially all nitrogen oxides from the waste gas, and the resulting effluent gas stream is separated to produce a pure carbon dioxide product. The catalytic conversion is preferably performed in a series of at least two reactors, the feed gas temperature decreasing and the ratio of ammonia to total nitrogen oxides increasing as the feed gas passes from reactor to reactor.</abstract><edition>7</edition><oa>free_for_read</oa></addata></record>
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subjects BLASTING
CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY
CHEMISTRY
COMBINED HEATING AND REFRIGERATION SYSTEMS
COMPOUNDS THEREOF
GLASS
HEAT PUMP SYSTEMS
HEATING
INORGANIC CHEMISTRY
LIGHTING
LIQUEFACTION SOLIDIFICATION OF GASES
LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS
MANUFACTURE OR STORAGE OF ICE
MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
MECHANICAL ENGINEERING
METALLURGY
MINERAL OR SLAG WOOL
MIXTURES BY PRESSURE AND COLD TREATMENT
NON-METALLIC ELEMENTS
PERFORMING OPERATIONS
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
REFRIGERATION OR COOLING
SEPARATION
THEIR RELEVANT APPARATUS
TRANSPORTING
WEAPONS
title Yüksek saflikta karbon dioksit üretmek için yöntem
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