NO117538B - - Google Patents

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Publication number
NO117538B
NO117538B NO164422A NO16442266A NO117538B NO 117538 B NO117538 B NO 117538B NO 164422 A NO164422 A NO 164422A NO 16442266 A NO16442266 A NO 16442266A NO 117538 B NO117538 B NO 117538B
Authority
NO
Norway
Prior art keywords
clinker
color
white
per cent
sulfuric acid
Prior art date
Application number
NO164422A
Other languages
Norwegian (no)
Inventor
K Uitti
T Okuma
Original Assignee
Universal Oil Prod Co
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
Application filed by Universal Oil Prod Co filed Critical Universal Oil Prod Co
Publication of NO117538B publication Critical patent/NO117538B/no

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/04Purification; Separation; Use of additives by distillation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S203/00Distillation: processes, separatory
    • Y10S203/11Batch distillation

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Investigating Materials By The Use Of Optical Means Adapted For Particular Applications (AREA)

Description

Fremgangsmåte for fremstilling av hvit Portlandsementklinker. Process for the manufacture of white Portland cement clinker.

For fremstilling av hvit Portland-se-mentklinker er det nødvendig å velge slike råmaterialer som er mest mulig fattige på farvegivende bestanddeler, særlig på farvegivende jern- eller manganoksyder. Råmaterialer som er frie for slike forbindelser forekommer imidlertid aldri i en tilstrek-kelig mengde i naturen til at man kunne basere fabrikasjonen av sement på dem. Man må derfor bestandig regne med at man får slike råmaterialer som inneholder større eller mindre mengder av forurensninger bestående av farvegivende bestanddeler. Klinker som blir brent av disse ma-terialer, er ikke rent hvit, men har gul-aktige, grønlige eller brunlige misfarvinger. For the production of white Portland cement clinker, it is necessary to select such raw materials as are as poor as possible in coloring components, in particular in coloring iron or manganese oxides. Raw materials that are free of such compounds, however, never occur in nature in a sufficient quantity to be able to base the manufacture of cement on them. One must therefore always expect that such raw materials are obtained that contain larger or smaller amounts of contaminants consisting of color-giving components. Clinker that is fired from these materials is not pure white, but has yellowish, greenish or brownish discolourations.

For å unngå slike misfarvinger av den To avoid such discolouration of it

hvite klinker er det blitt foreslått flere fremgangsmåter. Særlig er det blitt an-befalt å bråkjøle den varme klinker ved å dyppe den i vann eller ved påhelling av vann. white tiles, several methods have been proposed. In particular, it has been recommended to quench the hot clinker by dipping it in water or by pouring water on it.

Formålet for oppfinnelsen er en fremgangsmåte, hvorved klinker ikke bråkjøles med rent vann, men man anvender for dette formål fortynnete oppløsninger av visse kjemiske reagenser. Herved kommer slike kjemiske forbindelser i betraktning, som overfører de farvegivende oksyder eller andre forbindelser i klinkeren til far-veløse forbindelser, eller til forbindelser hvis farve er komplementær til den i klinkeren ellers herskende grunnfarve. Opp-finnelsens effekt skriver seg bl. a. fra den høye reaksjonsevne av det varme klinker-materiale. På grunn av den porøse struktur av klinkeren oppdager man den ved de The purpose of the invention is a method whereby clinker is not quenched with pure water, but dilute solutions of certain chemical reagents are used for this purpose. Hereby, such chemical compounds are taken into account, which transfer the coloring oxides or other compounds in the clinker to colorless compounds, or to compounds whose color is complementary to the base color otherwise prevailing in the clinker. The effect of the invention can be seen, among other things, in a. from the high reactivity of the hot clinker material. Due to the porous structure of the clinker, it can be detected by the

kjemiske reaksjoner fremkalte «hvithets- chemical reactions produced "whiteness-

effekt» ikke bare på overflaten av klinker-stykket. Det er blitt fastslått en dybde-virkning på inntil 2 cm. effect" not only on the surface of the clinker piece. A depth effect of up to 2 cm has been determined.

Ifølge oppfinnelsen blir klinkeren etter å ha kommet ut fra brennesonen bråkjøle ved å dyppes i eller fuktes med vandige oppløsninger eller suspensjoner, som inneholder halogenvannstoffsyrer, svovelsyre, svovelsyrling og/eiler undersvovelsyre, og/ eller deres alkali- eller Jordalkalisalter, som omdanner de farvegivende oksyder eller andre metallsalter i klinkeren til hvit eller en til den i klinkeren herskende farves komplementærfarve. Typen og mengden av de anvendte oppløsninger retter seg herved etter de forskjellige forurensninger i råmaterialet og den ønskete virkning. For å fjerne farven fra klinkeren for oppnåelse av en god hvithetseffekt, er det hensikts-messig å anvende oppløsninger eller suspensjoner med en konsentrasjon av fra 0,1 til 5 pst., særlig av 1 pst. Som allerede nevnt, er det mulig å variere de anvend-bare konsentrasjoner innenfor vide grenser. According to the invention, after emerging from the firing zone, the clinker is quenched by being dipped in or moistened with aqueous solutions or suspensions, which contain hydrohalic acids, sulfuric acid, sulfuric acid and/or hyposulphuric acid, and/or their alkali or alkaline earth salts, which convert the coloring oxides or other metal salts in the clinker to white or a complementary color to the prevailing color in the clinker. The type and quantity of the solutions used are based on the various contaminants in the raw material and the desired effect. In order to remove the color from the clinker to achieve a good whiteness effect, it is appropriate to use solutions or suspensions with a concentration of from 0.1 to 5 per cent, especially of 1 per cent. As already mentioned, it is possible to vary the applicable concentrations within wide limits.

Ved siden av den farvefjernende effekt kan det også skje en viss forandring i kvaliteten av klinkeren. Således er det f. eks. mulig å oppnå gunstig påvirkning på klinkerens avbindingstid, herdeevne og på dens tilbøyelighet til å svelle eller svinne. In addition to the color-removing effect, there may also be a certain change in the quality of the clinker. Thus, it is e.g. possible to achieve a favorable influence on the clinker's setting time, hardening ability and on its tendency to swell or shrink.

På den br åk j ølte klinker er det ennå etter tørkingen rester av kjemiske forbindelser fra bråkjølingsbadet, hva der er av mindre betydning for kvaliteten av klinkeren. Disse kan eventuelt bli fjernet ved å spyle klinkeren med rent vann før tørking. On the quenched clinker, after drying, there are still residues of chemical compounds from the quenching bath, which are of minor importance for the quality of the clinker. These can possibly be removed by rinsing the clinker with clean water before drying.

Klinkeren blir etter den beskrevne be-handling tørket og malt på vanlig måte. After the described treatment, the clinker is dried and painted in the usual way.

Claims (2)

1. Fremgangsmåte for å forbedre frem-stillingen av en hvit Portland-sementklin-ker, hvor klinkeren etter å ha kommet ut1. Process for improving the production of a white Portland cement clinker, where the clinker after coming out fra brennsonen bråkjøles, karakterisert ved at bråkjølingen utføres ved at klinkeren dyppes i eller påhelles vandige oppløsnin-ger eller suspensjoner som inneholder halogenvannstoffsyrer, svovelsyre, svovelsyrling og/eller undersvovelsyre og/eller deres alkali- eller jordalkalisalter, hvilke om- danner de farvegivende oksyder eller andre metallsalter i klinkeren til hvit eller til en komplementær farve til den i klinkeren herskende farve. 2. Fremgangsmåte som angitt i på-stand 1, karakterisert ved at konsentrasjo-nen av oppløsningene eller suspensjonene er fra 0.1 til 5 pst., fortrinnsvis 1 pst. from the combustion zone is quenched, characterized in that the quenching is carried out by dipping the clinker in or pouring over aqueous solutions or suspensions containing hydrohalic acids, sulfuric acid, sulfuric acid and/or hyposulphuric acid and/or their alkali or alkaline earth salts, which transform the coloring oxides or second metal salts in the clinker to white or to a complementary color to the prevailing color in the clinker. 2. Method as stated in claim 1, characterized in that the concentration of the solutions or suspensions is from 0.1 to 5 per cent, preferably 1 per cent. 2. Fremgangsmåte som angitt i på^ standene 1 og 2, karakterisert ved at de på klinkeren gjenværende kjemiske reagenser fjernes ved vasking med rent vann.2. Procedure as stated in items 1 and 2, characterized in that the chemical reagents remaining on the clinker are removed by washing with clean water.
NO164422A 1965-08-26 1966-08-25 NO117538B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US482685A US3367846A (en) 1965-08-26 1965-08-26 Utilization of recovered steam heat for heating the distillation zone

Publications (1)

Publication Number Publication Date
NO117538B true NO117538B (en) 1969-08-25

Family

ID=23917022

Family Applications (1)

Application Number Title Priority Date Filing Date
NO164422A NO117538B (en) 1965-08-26 1966-08-25

Country Status (11)

Country Link
US (1) US3367846A (en)
AT (1) AT272303B (en)
CH (1) CH486400A (en)
DE (1) DE1593652A1 (en)
DK (1) DK117136B (en)
ES (1) ES330435A1 (en)
FI (1) FI46732C (en)
GB (1) GB1149169A (en)
IL (1) IL26347A (en)
NL (1) NL6611788A (en)
NO (1) NO117538B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4041091A (en) * 1976-02-19 1977-08-09 Uop Inc. Fractionation of aromatic streams
US4555311A (en) * 1983-11-18 1985-11-26 Uop Inc. Integrated fractionation in the recovery of alkylaromatic hydrocarbons
US7249469B2 (en) * 2004-11-18 2007-07-31 Exxonmobil Chemical Patents Inc. Method for separating a multicomponent stream
CN110981835A (en) * 2019-12-16 2020-04-10 江苏怡达化学股份有限公司 Methanol recovery method in propylene oxide production
CN115430166B (en) * 2022-09-09 2024-06-21 天津大学 Process system and method for steam driven heat pump auxiliary bulkhead tower

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USRE22379E (en) * 1943-09-28 Recovery of pure aromatics
US1874387A (en) * 1922-11-13 1932-08-30 Semet Solvay Co Apparatus for the separation of liquids having different boiling points
US1882568A (en) * 1928-06-18 1932-10-11 E B Badger & Sons Company Method of distilling
US2406695A (en) * 1941-04-25 1946-08-27 Union Oil Co Separation of hydrocarbons by distillation
US2325379A (en) * 1942-05-26 1943-07-27 Shell Dev Distillation process
FR912978A (en) * 1944-03-29 1946-08-26 Woodall Duckham 1920 Ltd Distillation
US2577701A (en) * 1946-05-20 1951-12-04 Shell Dev Fractionation process
USRE26423E (en) * 1964-06-23 1968-07-16 Apparatus and method of fractionation op ethyl benzene
US3254024A (en) * 1965-03-03 1966-05-31 Halcon International Inc Process for separating c8-aromatic hydrocarbons by series column distillation

Also Published As

Publication number Publication date
CH486400A (en) 1970-02-28
FI46732B (en) 1973-02-28
AT272303B (en) 1969-07-10
DK117136B (en) 1970-03-23
FI46732C (en) 1973-06-11
ES330435A1 (en) 1967-06-16
NL6611788A (en) 1967-02-27
GB1149169A (en) 1969-04-16
IL26347A (en) 1970-05-21
US3367846A (en) 1968-02-06
DE1593652A1 (en) 1972-04-20

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