DK148914B - SUBSTANCES FOR THE REMOVAL OF HARMFUL SUBSTANCES, ISAER H2S, SO2, HCN, NOX, HF, HCL, PHENOL, FORMAL HYDROGEN AND LIKE, FROM GASES - Google Patents

SUBSTANCES FOR THE REMOVAL OF HARMFUL SUBSTANCES, ISAER H2S, SO2, HCN, NOX, HF, HCL, PHENOL, FORMAL HYDROGEN AND LIKE, FROM GASES Download PDF

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Publication number
DK148914B
DK148914B DK467577AA DK467577A DK148914B DK 148914 B DK148914 B DK 148914B DK 467577A A DK467577A A DK 467577AA DK 467577 A DK467577 A DK 467577A DK 148914 B DK148914 B DK 148914B
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Denmark
Prior art keywords
substances
gases
harmful substances
sorbent
hcn
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DK467577AA
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Danish (da)
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DK467577A (en
Inventor
Heinz Hoelter
Heinz Gresch
Heinrich Igelbuescher
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Heinz Hoelter
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 DE19762647520 external-priority patent/DE2647520A1/en
Application filed by Heinz Hoelter filed Critical Heinz Hoelter
Publication of DK467577A publication Critical patent/DK467577A/en
Publication of DK148914B publication Critical patent/DK148914B/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/30Pyrolysing
    • F23G2201/301Treating pyrogases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/30Pyrolysing
    • F23G2201/303Burning pyrogases

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

14891A14891A

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Den foreliggende opfindelse angår et sorptionsmid-del til fjernelse af skadelige stoffer, især H2S, S02, HCN, Ν0χ, HF, HC1, phenol, formaldehyd og lignende, fra gasser, der bringes i berøring med sorptionsmidlet.The present invention relates to a sorbent for removing harmful substances, in particular H2S, SO2, HCN, Ν0Ν, HF, HCl, phenol, formaldehyde and the like, from gases contacted with the sorbent.

5 I henhold til et forslag fra ansøgeren, der endnu ikke hører til den kendte teknik, kan sådanne skadelige stoffer fjernes fra gasser med alkalimetal- og/eller jord-alkalimetalforbindelser, der foreligger som støvformige, reaktionsdygtige og eventuelt formalede masser, idet sorp-10 tionsmidlet blæses ind i en gasstrøm, bringes i berøring med gassen og de skadelige stoffer og derefter atter fjernes fra gassen. Hertil kan der anvendes rørformede kanaler med venturiagtige indsatser, i hvilke der finder en intensiv kontakt sted mellem sorptionsmidlet og gassen og de 1g deri indeholdte skadelige stoffer. Efter en forholdsmæssig kort rørstrækning kan sorptionsmidlet fjernes fra gasstrømmen. Denne metode er i sig selv velegnet, men det er formålet med den foreliggende opfindelse at tilvejebringe et sorptionsmiddel med forbedrede sorptionsegenskaber, som 20 står til rådighed i store mængder og er økonomisk fordelagtigt.According to a proposal from the applicant, which is not yet known in the prior art, such harmful substances can be removed from gases with alkali metal and / or alkaline earth metal compounds which are present as dusty, reactive and possibly milled masses, the blowing agent is blown into a gas stream, brought into contact with the gas and the harmful substances and then removed from the gas again. For this purpose tubular ducts with venturi-like inserts can be used in which intensive contact between the sorbent and the gas and the harmful substances contained therein takes place. After a relatively short stretch of pipe, the sorbent can be removed from the gas stream. This method is suitable in itself, but it is the object of the present invention to provide a sorbent having improved sorption properties which are available in large quantities and are economically advantageous.

Dette formål opfyldes med et sorptionsmiddel af den i indledningen beskrevne art, hvilket sorptionsmiddel indeholder et ved en teknisk proces dannet støv, der i 25 det mindste indeholder jern-III-oxid og alkalimetaloxider og/eller jordalkalimetaloxider, og hvilket sorptionsmiddel er ejendommeligt ved, at et ved jern- eller stålfremstilling dannet støv, udrørt til en suspension, er påført på opblæret perlit som bærestof.This object is met with a sorbent of the kind described in the preamble, which sorbent contains a dust formed by a technical process which contains at least iron III oxide and alkali metal oxides and / or alkaline earth metal oxides, and which sorbent is characterized in that: a dust formed by iron or steel production, stirred to a suspension, is applied to the inflated perlite as a carrier.

30 Et støv af den ovenfor angivne art dannes ved jern- eller stålfremstilling i forholdsmæssigt store mængder. På grund af dets alkaliske egenskaber egner dette støv sig fremragende til fjernelse af skadelige stoffer fra gasser. I nedenstående tabel er der gengivet kvantitative 35 analyseværdier for tre forskellige støvprøver, der på forskellige tidspunkter er taget fra støvfjemingsanlæg i 2 14891430 A dust of the kind specified above is formed by iron or steel production in relatively large quantities. Due to its alkaline properties, this dust is excellent for removing harmful substances from gases. In the table below, quantitative 35 analysis values for three different dust samples were taken, which at different times were taken from dust removal systems in 2 148914

OISLAND

stålindustrien:Steel:

Sammensætning Prøve nr.Composition Sample no.

vægt-% _ 12 3_ 5 GlØdetab 6,07 2,38 3,02% by weight _ 12 3_ 5 Glow loss 6.07 2.38 3.02

Si02 1,97 1,04 0,93SiO2 1.97 1.04 0.93

Fe203 48,88 42,50 33,42 A1203 0,00 0,50 0,20Fe203 48.88 42.50 33.42 A1203 0.00 0.50 0.20

CaO 28,75 23,20 24,34 10 MgO 3,70 6,25 4,02CaO 28.75 23.20 24.34 MgO 3.70 6.25 4.02

Na20 3,80 2,80 2,45 K20 0,71 1,43 1,02Na20 3.80 2.80 2.45 K20 0.71 1.43 1.02

Pb - 1,04 1,62 V - 0,50 0,80 15 Ni - 0,08 0,12 P205 - 1,28 2,14 S03 1,54 4,58 16,33Pb - 1.04 1.62 V - 0.50 0.80 Ni - 0.08 0.12 P205 - 1.28 2.14 SO3 1.54 4.58 16.33

Zn 0,00 3,25 1,68 2o Når der i et specielt tilfælde ønskes en højere alka- litet hos støvet, kan der også tilsættes calciumhydroxid og/eller hvid, fin kalk. Endvidere kan støvets adsorptionsevne forbedres ved tilsætning af myremalm og/eller tungmetalsalte.Zn 0.00 3.25 1.68 2o When, in a special case, a higher alkalinity of the dust is desired, calcium hydroxide and / or white fine lime can also be added. Furthermore, the adsorption capacity of the dust can be enhanced by the addition of ant ore and / or heavy metal salts.

25 Afhængigt af det apparatur, som står til rådighed til fjernelse af de skadelige stoffer fra gasserne, kan støvet anvendes i naturlig form eller i pelletform.25 Depending on the apparatus available for removing the harmful substances from the gases, the dust may be used in natural or pellet form.

Endvidere kan støvet anvendes tørt eller fugtigt, hvorved metalandelene i støvet i sidstnævnte tilfælde danner 30 hydroxider, der har højaktive egenskaber til kvantitativ binding af skadelige stoffer, især H2S, HCN, NOx og SO2.Furthermore, the dust can be used dry or moist, whereby the metal particles in the dust in the latter case form 30 hydroxides which have highly active properties for the quantitative binding of harmful substances, especially H2S, HCN, NOx and SO2.

Hvis der er aluminium til stede, vil dette på grund af de amfotere egenskaber under alkaliske betingelser gå i opløsning som aluminatkompleks, men eventuelt også opløse en 35 del af de skadelige stoffer.If aluminum is present, this will, due to the amphoteric properties under alkaline conditions, dissolve as an aluminate complex, but may also dissolve some of the harmful substances.

33

1489U1489U

oisland

Ifølge opfindelsen opnår de særligt gunstige egenskaber ved, at sorptionsmidlet' påføres opblæret perlit som bærestof. Til dette formål røres sorptionsmidlet eller støvet sammen med vand til en sprøjtedygtig suspension, der 5 i en blandemaskine påføres eller påsprøjtes perliten.According to the invention, the particularly advantageous properties are that the sorbent is applied to the inflated perlite as a carrier. For this purpose, the sorbent or dust is stirred together with water for a sprayable suspension which is applied or sprayed onto the perlite in a mixer.

Opblæret perlit som bærestof frenibyder især ved tøradsorption en række fordele: deri lave vægtfylde tillader, at store mængder af suspensionen kan aflejres på bærestoffet uden at partiklernes flyveegenskaber i den luft- eller 10 gasstrøm, der skal renses, i væsentlig grad påvirkes negativt. Perlitkorneries uregelmæssige form og den store overflade sikrer en god vedhæftning og skaber gunstige forudsætninger for regenerering af -brugt sorptionsmiddel.Inflated perlite as a carrier, in particular by dry adsorption, offers a number of advantages: its low density allows large amounts of the suspension to be deposited on the carrier without significantly adversely affecting the flight properties of the particles in the air or gas stream to be purified. The irregular shape of the pearlite corners and the large surface ensure a good adhesion and create favorable conditions for the regeneration of -used sorbent.

Perlit er kemisk neutral, ikke brændbar og fri for 15 organiske urenheder. Desuden kan perlit modstå fugtigheds-påvirkninger. Da opblæret perlits porede struktur desuden tillader en høj vandabsorption, nemlig op til 70%, kan perliten også fugtes for derved, som allerede forklaret ovenfor, at forbedre sorptionsmidlets adsorptionsegenskaber.Perlite is chemically neutral, non-combustible and free of 15 organic impurities. In addition, perlite can withstand moisture impacts. Furthermore, since the pore structure of the inflated perlite allows a high water absorption, namely up to 70%, the perlite can also be wetted to thereby improve, as already explained above, the adsorption properties of the sorbent.

20 Til fugtningen kan der anvendes vand eller også natriumhydroxidopløsning, der samtidig forøger sorptionsmidlets alkalinitet.For the wetting, water or also sodium hydroxide solution may be used which simultaneously increases the alkalinity of the sorbent.

Den opblærede perlits høje sintringstemperatur på ca. 1000°C og høje, termiske blødgøringstemperatur på ca.The inflated pearl's high sintering temperature of approx. 1000 ° C and high thermal softening temperature of approx.

25 1220-1320°C virker ligeledes gunstigt, for derved er det muligt også at anvende det på et sådant bærestof påførte sorptionsmiddel til rensning af meget varme gasser, f.eks. fra kulforgasning under højt tryk eller fra affaldsforbrænding, hvilke gasser har temperaturer på op til 750°C 30 eller endog højere.25 1220-1320 ° C also works favorably, so that it is also possible to apply the sorbent applied to such a carrier to purify very hot gases, e.g. from high-pressure coal gasification or from waste incineration, which gases have temperatures up to 750 ° C 30 or even higher.

Opblæret perlits høje temperaturbestandighed virker også gunstigt på regenereringen af brugt sorptionsmiddel.The high temperature resistance of inflated perl also has a favorable effect on the regeneration of spent sorbent.

Ved ristning af brugt sorptionsmiddel opstår der S02-hol-dige ristegasser, der i et Claus-anlæg eller ved vådkataly-35 se kan omdannes til svovlsyre. Perliten bevares og kan afkøles ved påsprøjtning af vand og atter aktiveres, når · 14891Λ 4 0 ristningsfcemperatureri ikke overskrider 300°C, for ved højere temperatur er gendannelsen af jern-IIl-'hydroxid ikke længere mulig.Roasting of used sorbent produces SO2-containing rice gases which can be converted into sulfuric acid in a Claus plant or by wet catalysis. The perlite is retained and can be cooled by spraying water and re-energized when · roasting temperature does not exceed 300 ° C, because at higher temperature the recovery of iron IIl hydroxide is no longer possible.

Bærestoffet perlit bevares også ved svovludvinding 5 ved ekstrahering af de brugte og med luft til jem-III--hydroxid og svovl genomdannede sorptionsmidler ved hjælp af ammoniumpolysulfid eller carbondisulfid, da perlit ikke er opløselig i organiske opløsningsmidler.The carrier perlite is also retained by sulfur recovery 5 by extracting the spent and with air to iron III hydroxide and sulfur genomide sorbents by means of ammonium polysulfide or carbon disulphide, as perlite is not soluble in organic solvents.

Endelig frembyder det heller ikke nogen vanskelighe-10 der at deponere det brugte sorptionsmiddel efter optagelse af de skadelige stoffer sammen med bærestoffet, nemlig perlit, da der hertil kun behøves ringe plads. Opblæret perlit kan nemlig presses sammen til 1/10 af det oprindelige volumen og binder derved samtlige optagne skadelige stoffer.Finally, it does not present any difficulty in depositing the spent sorbent after absorption of the harmful substances together with the carrier, namely perlite, as little space is needed for this. Namely, inflated perlite can be compressed to 1/10 of the original volume, thereby binding all the absorbed harmful substances.

15 Det her omhandlede sorptionsmiddel er tilstrækkeligt alkalisk til regulerbar gennemførelse af adsorptionen af skadelige stoffer under stabile forhold. Tilstedeværelsen af baser muliggør også regenerering eller videre forarbejdning af sorptionsmidlerne f.eks. ved ristning og fugtning, 20 hvorved der er sikret en hurtig genomdannelse af jernbe-standdelene til jern-III-hydroxid.The present sorbent is sufficiently alkaline to regulate the adsorption of harmful substances under stable conditions. The presence of bases also allows regeneration or further processing of the sorbents e.g. by roasting and wetting, thereby ensuring a rapid genome formation of the iron constituents for iron III hydroxide.

Det her omhandlede sorptionsmiddel kan anvendes både tørt og fugtigt ved de mest forskelligartede fremgangsmåder og apparater, ved hvilke skadelige stoffer fjernes fra gas-25 ser ved adsorption.The present sorbent can be used both dry and moist in the most diverse methods and apparatus by which harmful substances are removed from gases by adsorption.

DK467577AA 1976-10-21 1977-10-20 SUBSTANCES FOR THE REMOVAL OF HARMFUL SUBSTANCES, ISAER H2S, SO2, HCN, NOX, HF, HCL, PHENOL, FORMAL HYDROGEN AND LIKE, FROM GASES DK148914B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19762647520 DE2647520A1 (en) 1976-04-10 1976-10-21 Iron oxide dust sorption agent - for removing pollutants from gases, e.g. hydrogen sulphide or sulphur dioxide
DE2647520 1976-10-21

Publications (2)

Publication Number Publication Date
DK467577A DK467577A (en) 1978-04-22
DK148914B true DK148914B (en) 1985-11-18

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JP (1) JPS5351192A (en)
AT (1) AT357985B (en)
BE (1) BE858632A (en)
DK (1) DK148914B (en)
FR (1) FR2368294A1 (en)
NL (1) NL7709845A (en)
SE (1) SE431717B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE875445A (en) * 1978-05-10 1979-07-31 Hoelter H MOTOR VEHICLE INTERIOR VENTILATION AIR FILTER
JP2742070B2 (en) * 1988-11-10 1998-04-22 藤沢薬品工業株式会社 Deodorant
JP2581656B2 (en) * 1991-07-09 1997-02-12 同和鉱業株式会社 Deodorant and method for producing the same

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE759979A (en) * 1965-02-10 1971-06-07 Grillo Werke Ag PROCESS FOR ELIMINATION OF SULFUR IN RESIDUAL GASES
FR1525085A (en) * 1967-01-16 1968-05-17 Yawata Iron & Steel Co Process for the separation or concentration of gas mixture
US3580702A (en) * 1968-09-10 1971-05-25 Us Interior Method of removing sulfur oxides from gases
US3579293A (en) * 1969-10-10 1971-05-18 Us Interior Removal of hydrogen sulfide from gaseous mixtures
AT363918B (en) * 1975-05-06 1981-09-10 Hoelter Heinz METHOD AND DEVICE FOR PURIFYING GAS

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SE7711608L (en) 1978-04-22
NL7709845A (en) 1978-04-25
AT357985B (en) 1980-08-11
SE431717B (en) 1984-02-27
DK467577A (en) 1978-04-22
JPS5351192A (en) 1978-05-10
FR2368294A1 (en) 1978-05-19
ATA612277A (en) 1980-01-15
BE858632A (en) 1978-01-02

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