LU83658A1 - PROCESS FOR USING A MIXTURE OF CALCIUM SULPHITE HALF HYDRATE AND CALCIUM SULFATE DI HYDRATE IN THE MANUFACTURE OF CEMENT - Google Patents
PROCESS FOR USING A MIXTURE OF CALCIUM SULPHITE HALF HYDRATE AND CALCIUM SULFATE DI HYDRATE IN THE MANUFACTURE OF CEMENT Download PDFInfo
- Publication number
- LU83658A1 LU83658A1 LU83658A LU83658A LU83658A1 LU 83658 A1 LU83658 A1 LU 83658A1 LU 83658 A LU83658 A LU 83658A LU 83658 A LU83658 A LU 83658A LU 83658 A1 LU83658 A1 LU 83658A1
- Authority
- LU
- Luxembourg
- Prior art keywords
- hydrate
- calcium
- cement
- mixture
- manufacture
- Prior art date
Links
- GBAOBIBJACZTNA-UHFFFAOYSA-L calcium sulfite Chemical compound [Ca+2].[O-]S([O-])=O GBAOBIBJACZTNA-UHFFFAOYSA-L 0.000 title claims description 12
- 235000010261 calcium sulphite Nutrition 0.000 title claims description 12
- 239000004568 cement Substances 0.000 title claims description 10
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 239000000203 mixture Substances 0.000 title claims description 9
- PASHVRUKOFIRIK-UHFFFAOYSA-L calcium sulfate dihydrate Chemical compound O.O.[Ca+2].[O-]S([O-])(=O)=O PASHVRUKOFIRIK-UHFFFAOYSA-L 0.000 title claims description 7
- 238000000034 method Methods 0.000 title claims description 7
- 239000004295 calcium sulphite Substances 0.000 title claims description 5
- 239000007789 gas Substances 0.000 claims description 14
- 239000000779 smoke Substances 0.000 claims description 11
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Inorganic materials [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 6
- 239000011575 calcium Substances 0.000 claims description 5
- 229910052791 calcium Inorganic materials 0.000 claims description 5
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 4
- 239000000725 suspension Substances 0.000 claims description 4
- 235000011132 calcium sulphate Nutrition 0.000 claims description 3
- 239000002803 fossil fuel Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 239000001175 calcium sulphate Substances 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 claims description 2
- VCSZKSHWUBFOOE-UHFFFAOYSA-N dioxidanium;sulfate Chemical compound O.O.OS(O)(=O)=O VCSZKSHWUBFOOE-UHFFFAOYSA-N 0.000 claims description 2
- 239000011344 liquid material Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 239000002562 thickening agent Substances 0.000 claims description 2
- 150000001669 calcium Chemical class 0.000 claims 1
- ZHZFKLKREFECML-UHFFFAOYSA-L calcium;sulfate;hydrate Chemical compound O.[Ca+2].[O-]S([O-])(=O)=O ZHZFKLKREFECML-UHFFFAOYSA-L 0.000 claims 1
- 238000006477 desulfuration reaction Methods 0.000 description 6
- 230000023556 desulfurization Effects 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 229910021653 sulphate ion Inorganic materials 0.000 description 2
- AGVJBLHVMNHENQ-UHFFFAOYSA-N Calcium sulfide Chemical compound [S-2].[Ca+2] AGVJBLHVMNHENQ-UHFFFAOYSA-N 0.000 description 1
- 241000283984 Rodentia Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052925 anhydrite Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 150000004683 dihydrates Chemical class 0.000 description 1
- HLGRRZFWTBVGMM-UHFFFAOYSA-L disodium;sulfate;dihydrate Chemical compound O.O.[Na+].[Na+].[O-]S([O-])(=O)=O HLGRRZFWTBVGMM-UHFFFAOYSA-L 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- VLPFTAMPNXLGLX-UHFFFAOYSA-N trioctanoin Chemical compound CCCCCCCC(=O)OCC(OC(=O)CCCCCCC)COC(=O)CCCCCCC VLPFTAMPNXLGLX-UHFFFAOYSA-N 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/38—Preparing or treating the raw materials individually or as batches, e.g. mixing with fuel
- C04B7/42—Active ingredients added before, or during, the burning process
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B22/00—Use of inorganic materials as active ingredients for mortars, concrete or artificial stone, e.g. accelerators, shrinkage compensating agents
- C04B22/08—Acids or salts thereof
- C04B22/14—Acids or salts thereof containing sulfur in the anion, e.g. sulfides
- C04B22/142—Sulfates
- C04B22/143—Calcium-sulfate
- C04B22/145—Gypsum from the desulfuration of flue gases
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
ί 1 i ί la présente invention concerne l'emploi, dans la fa- î bricatim du ciment, d'un mélange de demi-hydrate de \ jj sulfite de calcium et de di-hydr&te de sulfate de I , calcium obtenu, en proportion de 1 à 99 ^ (et de pré- j 5 férence de 1 à 30 de demi-hydrate de sulfite de i calcium et de 1 à 99 ^ (et de préférence de 60 à 99 de di—hjdrate de sulfate de calcium, dans un procédé J de désulfuration de gaz de fumée dans lequel le gaz il ' de fumer, produit par la combustion de combustibles I fossile·· , est traité, avec une suspension contenant du cale:· um, dans un appareil laveur où se formera, entre autres, du demi-hydrate de sulfite de calcium qui per;· partiellement oxydé par addition d'oxygène de l'air pour donner du di-hydrate de sulfate de cal-15 cium, v.r courant partiel de la suspension ainsi formée, contenu· t, entre autres, eu di-hydrate de sulfate de ; calcium, étant retiré du circuit de l'srpareil laveur i; et à des épaississeurs où il sera considérable-ί 1 i ί the present invention relates to the use, in the manufacture of cement, of a mixture of half hydrate of calcium sulfite and of sodium sulfate dihydrate, calcium obtained in proportion from 1 to 99 ^ (and preferably from 1 to 30 of calcium sulfite half hydrate and from 1 to 99 ^ (and preferably from 60 to 99 of calcium sulfate dihydrate, in a process J for the desulphurization of smoke gases in which the smoking gas, produced by the combustion of fossil fuels ··, is treated, with a suspension containing wedge: · um, in a washing machine where will form, inter alia, calcium sulfite half hydrate which per; · partially oxidized by addition of oxygen from the air to give cal-15 cium sulfate dihydrate, vr partial flow of the suspension thus formed, content · T, inter alia, had calcium sulphate di-hydrate, being withdrawn from the circuit of the washing machine i; and to thickeners where it will be considerable-
HH
ment déshydraté, la matière solide, d'humidité rési-dehydrated, solid matter, moisture resis-
• PO• PO
! w duelle réduite, étant ensuite extraire du circuit et la mati- re liquide étant, de préférence, ramenée à !' # l'appareil laveur .! w reduced dual, then being extracted from the circuit and the liquid material preferably being brought back to! ' # the washing machine.
" Dans I? fabrication du ciment, on ajoute du gypse à i |. titre cretardateur de solidification . Jusau'à ce !: 25 0 cur, ,-s produit d'addition étant mélangé, nar broy-: s.ge, &·. clinker de ciment sous fcrm.e de rvtse naturel ou d'a: crite naturel ."In the manufacture of cement, gypsum is added to the solidifying agent. Up to this point: 25 ° C., with the addition product being mixed, nar groy-: s.ge, & ·. Clinker of cement under form of natural coating or natural coating.
t»ans Ir traitement ces gaz ce fumée produits tar la ccm.Dus" - on de combustibles fossiles or. ccü en raison 30 , , . .t "years Ir processing these gases this smoke produced tar the ccm.Dus" - on fossil fuels gold. ccü due 30,,.
s ou aur; -ssem.ent des treecriptions relatives à la tol- t1 lut i or. us l'air, prendre ces dispositions pour abais- 2 ser la teneur en soufre de ces gaz de fumée . la désul- % furatxon des gaz de fumée peut s'effectuer, de façon connue, dans le cadre d'une désulfuration par voie humide ces gaz de fumée . Selon le déroulement du pro-, 5 cessus de désulfuration par voie humide des gaz de t fumée, on obtient un mélange de demi-hydrate de sul fite de calcium et de di-hydr&te de sulfate de cal-' cium, la teneur en demi-hydrate de sulfite de calcium pouvant être réglée à des parties en poids déterminées par rapport à la teneur totale en matières solides .s or aur; -ssem.ent treecriptions relating to tolt1 lut i or. In the air, take these steps to lower the sulfur content of these smoke gases. the desul-% furatxon smoke gases can be carried out, in known manner, in the context of wet desulfurization these smoke gases. Depending on the progress of the process, by the wet desulfurization of the smoke gases, a mixture of calcium sulphite half hydrate and calcium sulphate dihydrate is obtained, the content of half - calcium sulfite hydrate which can be adjusted to parts by weight determined relative to the total solids content.
1 0 pour la fabrication du piètre de construction, on ne peut employer que des produits dont la teneur en demi-hydrate ce sulfite de calcium est nettement inférieure à 1 λ · Pour obtenir un tel produit à partir d'une désulfuration car voie humide de gaz de fumée, il est1 0 for the manufacture of poor construction, one can only use products whose content of half-hydrate this calcium sulfite is significantly less than 1 λ · To obtain such a product from a desulfurization because wet smoke gas it's
1 P1 P
indiepensable d'employer un procédé Particulier utilisant un appareillage conformément compliqué » On ne cre-rche p.&s toujours & obtenir de la désulfuration par vote humide ces gaz de fumée un produit a forte teneur 2q en sulfate rais un produit approprié à d'autres usages .essential to use a particular process using a device in accordance with complicated »We do not always cr-rche & get desulfurization by wet vote these smoke gases a product with a high content 2q sulphate rais a product suitable for others uses.
, Comme des ec-s&is l'ont révélé, le demi-hydrate de sul- l-'e fie calcium reut remplacer le d' -u-.-.'rato » Ie demi-hycr&xe, ou l'anhydrite de sulfate de calcium dans leE fonctions de régulateur de solidification dans la xacrication du ciment .As has been shown, half-hydrate of calcium sulphide can replace that of -u -.- 'rato', the half-hydrate, or the sulphate anhydrite calcium in the solidification regulator functions in cement manufacturing.
2 P2 P
J-’5· Présente invention & donc pour objet d'utiliser, cotte régulateur de solidification dans la fabrication ^u ciment, un mélange de demi-hydrate de sulfite de c&iciun et de di-hydrate de sulfate de calcium au lieu ,/), naturel ou ce l'anhyirite naturel» utilisés : ' j-eau'ici .J-'5 · Present invention & therefore object of using, solidification regulator coat in the manufacture ^ cement, a mixture of half sulphite of c & ciunun and di-hydrate of calcium sulphate instead, /) , natural or that natural anhyirite ”used: 'j-eau' here.
3 t3 t
Pour atteindre cebut, la présente invention propose » d'utiliser un mélange de demi-hydrate de sulfite.de calcium et de di-hydrate de sulfate de calcium en composition de 1 à 99 fi (et âe préférence de 1 à 30 fi) 5 de demi-hydrate de sulfite de calcium, et de 1 à 99 fi (et de préférence de 60 à 99 fi) de di-hydrate de . sulfate de calcium .To achieve this goal, the present invention proposes to use a mixture of calcium sulfite half hydrate and calcium sulfate di hydrate in composition from 1 to 99% (and preferably from 1 to 30%). of calcium sulfite half hydrate, and from 1 to 99 μl (and preferably from 60 to 99 μl) of dihydrate. calcium sulfate.
l'avantage procuré par l'invention réside dans la possibilité d'utiliser, dans des conditions économiaue-ment favorables, pour la production du ciment, un produit se formant au cours de la désulfuration par voie humide ces gas de fumée . le coût de la désulfuration par voie humide des gaz de filmée se trouve sensiblement ahaisse par le fait que la marche du processus de 1 Sthe advantage provided by the invention lies in the possibility of using, under economically favorable conditions, for the production of cement, a product formed during the wet desulfurization these smoke gases. the cost of wet desulphurization of the film gases is appreciably increased by the fact that the progress of the 1 S process
aesulfuration par voie humide ces gau de fumée oeut être axée sur l'obtention d’un mélange de demi-hydrate âe sulfite de calcium et de di-hydrate de sulfate de calcium ainsi que par la simplification de l'annareil- lage . l'emploi d'un tel produit comme rroduit d'acdi-20 „ . , , „ , .wet desulfurization these smoke gases can be focused on obtaining a mixture of calcium sulphite half hydrate and calcium sulphate di-hydrate as well as by simplifying the apparatus. the use of such a product as an acid-20 product. ,, „,.
* i-mon \reguxateur ce εοΧίqnic &tionj cars la fabrica— * tion du ciment n'entraîne pas la formation d'un dén5t polluant l'environnement, car on doit xout ra^ticu-^ *' ; ~'tremenx souligner 0ue les sels nocifs r.our l'envi- ; ^ bonnement restent en partie dans le mélange de demi- I b . , : r-Pcrate de sulfite de calcium et de di-hydrate de I sulfate de calcium, tandis qu'avec d'autres procédés j —Os S£is doiv cr. c t «γθ évacues, soix xar les eaux d'é— I vacuation, soit par la formaxion de dépôts - En outre, 11 emploi ce ces déchets inévitables diminue l'épuise-“-r.t des giser.er.ts ce gypse naturel brut .* i-mon \ reguxateur ce εοΧίqnic & tionj cars the manufacture of cement * * cement does not lead to the formation of a damaging pollutant the environment, because one must xout ra ^ ticu- ^ * '; ~ 'very underline 0ue harmful salts r.our envi-; ^ simply remain partly in the mixture of half I b. ,: r-Pcrate of calcium sulphite and calcium sulphate di-hydrate, while with other methods i - Os S £ is cr. ct "γθ evacuated, six xar the evacuation water, either by the formation of deposits - In addition, 11 use that this inevitable waste decreases the exhaustion -" - rt des giser.er.ts this raw natural gypsum .
Claims (1)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19803037056 DE3037056A1 (en) | 1980-10-01 | 1980-10-01 | USE OF A MIXTURE OF CALCIUM SULFIT SEMI-HYDRATE AND CALCIUM SULFATE DIHYDRATE FOR THE PRODUCTION OF CEMENT |
DE3037056 | 1980-10-01 |
Publications (1)
Publication Number | Publication Date |
---|---|
LU83658A1 true LU83658A1 (en) | 1982-02-17 |
Family
ID=6113333
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
LU83658A LU83658A1 (en) | 1980-10-01 | 1981-09-30 | PROCESS FOR USING A MIXTURE OF CALCIUM SULPHITE HALF HYDRATE AND CALCIUM SULFATE DI HYDRATE IN THE MANUFACTURE OF CEMENT |
Country Status (12)
Country | Link |
---|---|
JP (1) | JPS5788053A (en) |
BE (1) | BE890558A (en) |
DD (1) | DD201667A5 (en) |
DE (1) | DE3037056A1 (en) |
DK (1) | DK431681A (en) |
FR (1) | FR2491054A1 (en) |
GB (1) | GB2084562B (en) |
GR (1) | GR75013B (en) |
IE (1) | IE51795B1 (en) |
IT (1) | IT1138682B (en) |
LU (1) | LU83658A1 (en) |
NL (1) | NL8104481A (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59195560A (en) * | 1983-04-21 | 1984-11-06 | 日本セメント株式会社 | Manufacture of concrete products |
DE3821657A1 (en) * | 1988-06-27 | 1989-12-28 | Rheine Kalkwerke Gmbh | METHOD FOR PRODUCING A BINDER AND ITS USE |
DE59005950D1 (en) * | 1989-11-20 | 1994-07-07 | Wsz Wolfener Schwefelsaeure Un | METHOD FOR PRODUCING CEMENT CLINKER AND RECOVERY OF SULFUR DIOXIDE. |
JP4775045B2 (en) * | 2006-03-14 | 2011-09-21 | 宇部興産株式会社 | Reducing gypsum composition, method for producing the same, cement-based solidifying material, and solidifying method |
JP7406994B2 (en) * | 2020-01-08 | 2023-12-28 | Ube三菱セメント株式会社 | Method for manufacturing cement composition |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3855391A (en) * | 1973-01-23 | 1974-12-17 | Dravo Corp | Sludge stabilization with gypsum |
SU563376A1 (en) * | 1975-03-10 | 1977-06-30 | Харьковский Ордена Ленина Политехнический Институт Им. В.И.Ленина | Expanding binding material |
-
1980
- 1980-10-01 DE DE19803037056 patent/DE3037056A1/en not_active Ceased
-
1981
- 1981-09-29 GB GB8129302A patent/GB2084562B/en not_active Expired
- 1981-09-29 DK DK431681A patent/DK431681A/en not_active Application Discontinuation
- 1981-09-30 BE BE0/206114A patent/BE890558A/en not_active IP Right Cessation
- 1981-09-30 GR GR66169A patent/GR75013B/el unknown
- 1981-09-30 FR FR8118455A patent/FR2491054A1/en not_active Withdrawn
- 1981-09-30 LU LU83658A patent/LU83658A1/en unknown
- 1981-10-01 JP JP56154891A patent/JPS5788053A/en active Pending
- 1981-10-01 DD DD81233790A patent/DD201667A5/en unknown
- 1981-10-01 NL NL8104481A patent/NL8104481A/en not_active Application Discontinuation
- 1981-10-01 IT IT24262/81A patent/IT1138682B/en active
- 1981-10-01 IE IE2280/81A patent/IE51795B1/en unknown
Also Published As
Publication number | Publication date |
---|---|
DD201667A5 (en) | 1983-08-03 |
GB2084562A (en) | 1982-04-15 |
IE51795B1 (en) | 1987-04-01 |
FR2491054A1 (en) | 1982-04-02 |
DE3037056A1 (en) | 1982-04-22 |
GB2084562B (en) | 1984-03-07 |
IT1138682B (en) | 1986-09-17 |
DK431681A (en) | 1982-04-02 |
JPS5788053A (en) | 1982-06-01 |
NL8104481A (en) | 1982-05-03 |
IE812280L (en) | 1982-04-01 |
BE890558A (en) | 1982-01-18 |
GR75013B (en) | 1984-07-12 |
IT8124262A0 (en) | 1981-10-01 |
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