CN1587158A - Method for preparing cement clinker with oil field oil-containing calcium sludge - Google Patents
Method for preparing cement clinker with oil field oil-containing calcium sludge Download PDFInfo
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- CN1587158A CN1587158A CNA2004100606785A CN200410060678A CN1587158A CN 1587158 A CN1587158 A CN 1587158A CN A2004100606785 A CNA2004100606785 A CN A2004100606785A CN 200410060678 A CN200410060678 A CN 200410060678A CN 1587158 A CN1587158 A CN 1587158A
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- oil
- oil field
- mud
- calcareous
- cement clinker
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
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- Treatment Of Sludge (AREA)
Abstract
The preparation process of cement clinker with oil field oil-bearing calcium sludge includes the following steps: washing oil field oil-bearing calcium sludge with water to eliminate sodium; compounding the cement material with oil field oil-bearing calcium sludge after baking at 900 deg.c, lime, quartzite and Fe2O3 powder, pulverizing the mixture material and sintering; and pulverizing the sintered clinker and sieving in sieve with 0.08 mm meshes to obtain the product. The present invention prepares cement clinker with oil field oil-bearing calcium sludge as one main kind of industrial material and disposes the industrial waste successfully.
Description
Technical field
The present invention relates to the method that the calcareous recycling sludge of a kind of oil field oil-containing is handled, be specifically related to a kind of method for preparing cement clinker with the calcareous mud of oil field oil-containing.
Background technology
Some oil field makes the oil field produce the calcareous mud of a kind of butyraceous for the technology that the etching problem that solves oil field equipment adopts.The calcareous mud of oil-containing is the wet mud of a kind of heavy-gravity, is khaki color.When being hygrometric state, has good plasticity-; But behind the complete drying, the calcareous mud of doing of oil-containing dissolves no longer easily or is dispersed in the water.This is a kind of trade waste, at present non-processor good recipe still.
Summary of the invention
The method that the purpose of this invention is to provide the calcareous mud of a kind of recycling treatment oil field oil-containing prepares cement clinker with the calcareous mud of oil field oil-containing as main raw material.
Technical scheme of the present invention is: prepare the method for cement clinker with the calcareous mud of oil field oil-containing, its step is as follows:
1). with the calcareous mud water of oil field oil-containing flush away sodium;
2). by removing the calcareous mud of sodium oil field oil-containing and unslaked lime, quartz sand, Fe after 900 ℃ of roastings
2O
3Powder is prepared burden and is formed the material of cement slurry, and described each component is respectively the calcareous mud of sodium oil field oil-containing by weight: 35.48-47.39, unslaked lime: 33.74-43.64, quartz sand: 13.50-16.40, Fe
2O
3Powder: 2.2-5.32 carries out sintering behind the combined grinding to material;
3). the grog piece grinding that sinters, the sieve in 0.08mm aperture gets product excessively;
The chemical constitution of removing the calcareous mud of sodium oil field oil-containing after described 900 ℃ of roastings is SiO
26.76-12.07wt%, Al
2O
35.15-15.54wt%, Fe
2O
31.36-5.20wt%, CaO 54.31-71.16wt%, MgO 9.59-11.37wt%.
The present invention is a main raw material with the calcareous mud of waste oil field oil-containing, and water flush away sodium dries, perhaps with regard to the wet mud formation cement slurry of filling a prescription; Be equipped with some other raw material, successfully prepare ordinary portland cement clinker.This cement clinker is equipped with other material, as flyash, forms Portland fly ash cement, or other ordinary Portland cement.Because the calcareous mud of oil field oil-containing contains relatively large water, oil and CO
2Deng not participating in the material that forms the cement clinker reaction, during the preparation cement slurry, should be according to prescription through the chemical composition design cement slurry of the calcareous mud of oil field oil-containing of 900 ℃ of roastings.By the mud annual production (the calcareous mud of the dried oil-containing of about 2.9 ten thousand steres) of Zhongyuan Oil Field, a small-sized cement factory just can consume light with the 2.9 ten thousand stere dewatered sludges in this every year.The investor not only can win direct economic interests, but also has successfully handled a kind of industrial waste.
Embodiment
The feature of the calcareous mud of oil field oil-containing:
1. states of matter feature
The calcareous mud of oil-containing is the wet mud of a kind of khaki thickness, has good plasticity-, but is dispersed in the water no longer easily when complete drying.This mud contains higher Na, and this component has detrimentally affect to soundness, and belonging to must removing person.The calcareous mud of oil-containing is cleaned with clear water, leave standstill the back and remove supernatant liquor; Oven dry after cleaning 4 times repeatedly.The content of Na and Cl is listed in table 1 in the dried mud in cleaning front and back.Table 1 shows that Na form with NaCl in mud exists, and is removed after the cleaning substantially fully.
The content (wt%) of Na and Cl in the calcareous mud of the table 1 cleaning dried oil-containing in front and back
Na
2O?????????Cl
Clean back 0.58 0.38
Clean preceding 5.17 7.44
Go the basic thing phase composite of the calcareous mud of the dried oil-containing of Na as shown in table 2.
The basic thing phase composite (wt%) of the calcareous mud of table 2 oil-containing
Oil+volatile matter removes the calcareous mud of Na oil-containing
Roasting base (900 ℃)
42.33??????????57.67
2. go the chemical ingredients feature of the calcareous sludge roasting base of Na oil-containing
The chemical ingredients of removing the calcareous sludge roasting base of Na oil-containing is the basis of preparation cement clinker, and its analytical results is listed in the table 3.
Table 3 goes the chemical constitution (wt%) of the calcareous sludge roasting base of Na oil-containing
SiO
2Al
2O
3Fe
2O
3CaO MgO burns and loses total amount
6.76-12.07????5.15-15.54?????1.36-5.20?????54.31-71.16??9.59-11.37??0.93-1.51??100
Because the calcareous mud of oil field oil-containing contains relatively large water, oil and CO
2Deng not participating in the material that forms the cement clinker reaction, during the preparation cement slurry, should be according to prescription through the chemical composition design cement slurry of the calcareous mud of oil field oil-containing of 900 ℃ of roastings.
Prepare the method for cement clinker with the calcareous mud of oil field oil-containing, its step is as follows:
1). with the calcareous mud water of oil field oil-containing flush away sodium;
2). by removing the calcareous mud of sodium oil field oil-containing and unslaked lime, quartz sand, Fe after 900 ℃ of roastings
2O
3Powder is prepared burden and is formed the material of cement slurry, and described each component is respectively the calcareous mud of sodium oil field oil-containing by weight: 35.48-47.39, unslaked lime: 33.74-43.64, quartz sand: 13.50-16.40, Fe
2O
3Powder: 2.2-5.32 carries out sintering behind the combined grinding to material;
3). the grog piece grinding that sinters, the sieve in 0.08mm aperture gets product excessively;
The chemical constitution of removing the calcareous mud of sodium oil field oil-containing after described 900 ℃ of roastings is SiO
26.76-12.07wt%, Al
2O
35.15-15.54wt%, Fe
2O
31.36-5.20wt%, CaO 54.31-71.16wt%, MgO 9.59-11.37wt%.
Embodiment 1:
Table 4 is to spend the chemical constitution of the cement clinker prescription that the calcareous dewatered sludge of Na oil-containing is one of raw material (prescription 1) and the rate value of this prescription thereof.Table 5 is that the material of prescription 1 cement slurry is formed.China qualified cement clinker rate value KH, the implication of IM and SM and and scope list in down:
KH (lime saturation factor)=(CaO-1.65Al
2O
3-0.35Fe
2O
3)/2.8SiO
2, scope 0.86-0.90;
IM (aluminium rate)=SiO
2/ (Al
2O
3+ Fe
2O
3), scope 1.00-1.50;
SM (sial)=Al
2O
3/ Fe
2O
3, scope 1.80-2.20.
Above rate value mainly is applicable to the cement (small-sized cement factory) that shaft kiln is produced.Produce qualified cement and must be strict remove to design the prescription of cement clinker/raw material by the rate value, promptly no matter use which kind of raw material, the rate value of final cement clinker must drop in the above-mentioned rate value scope.Therefore, employed different material and quantity strictness thereof were subject to the scope of above-mentioned rate value during the present invention respectively filled a prescription.
The chemical constitution (wt%) and the rate value thereof of the calcareous mud cement clinker of table 4 oil-containing
SiO
2Al
2O
3Fe
2O
3Other total amount of CaO MgO KH (0.86-0.90) IM (1.00-1.50) SM (1.80-2.20)
20.40????6.76??????4.51?????62.72??4.95????0.66???100.00???0.87????????????1.50????????????1.81
Table 5 prescription 1 removes the composition of raw materials (kg) of the calcareous mud cement clinker of Na oil-containing
Remove the calcareous mud CaO of the dried oil-containing of Na (calcium lime powder) quartz sand Fe
2O
3Powder
75.46?????????????????39.08????????????15.15?????2.25
1. will carry out grinding by the raw material of prescription 1 (table 5) preparation and all mix, then 1300-1350 ℃ of insulation 2 hours.With the cooling of lowering the temperature rapidly of agglomerating grog.
2. with the abundant grinding of agglomerating grog, make it 90% sieve by the 0.08mm aperture.So far, the calcareous mud ordinary portland cement clinker of oil-containing is made.
Embodiment 2:
Embodiment 2 is on the basis of table 4 and table 5 (prescription 1), with containing Fe
2O
3The iron ore of low ore grade of 46.43wt% substitutes Fe
2O
3(high purity iron ore) powder, thus prescription 2 (tables 8) formed.
The chemical constitution of table 6 iron ore of low ore grade
????SiO 2 | ????Al 2O 3 | ????Fe 2O 3 | Other | Add up to |
????43.71 | ????6.26 | ????47.43 | ????2.60 | ????100 |
The chemical constitution (wt%) and the rate value thereof of the calcareous mud cement clinker of table 7 oil-containing
SiO
2Al
2O
3Fe
2O
3Other total amount of CaO MgO KH (0.86-0.90) IM (1.00-1.50) SM (1.80-2.20)
20.62????6.70???????4.48??????62.76???4.68????0.75???100.00???0.87???????????1.50????????????1.84
Table 8 prescription 2 removes the composition of raw materials (kg) of the calcareous mud cement clinker of Na oil-containing
Remove the calcareous mud CaO of the dried oil-containing of Na (calcium lime powder) quartz sand low-grade iron ore stone flour
71.35????????????????40.41????????????13.50?????4.94
1. will carry out grinding by the raw material of prescription 2 (tables 8) preparation and all mix, then 1300-1350 ℃ of insulation 2 hours.With the cooling of lowering the temperature rapidly of agglomerating grog.
2. with the abundant grinding of agglomerating grog, make it 90% sieve by the 0.08mm aperture.So far, the calcareous mud ordinary portland cement clinker of oil-containing is made.
Embodiment 3:
Embodiment 3 is on the basis of prescription 2, substitutes SiO with river sand
2Powder and the prescription 3 (table 11) that forms.
The chemical constitution of table 9 river sand
????SiO 2 | ????Al 2O 3 | ????Fe 2O 3 | ????MgO | ????CaO | Burn and lose | Add up to |
????89.68 | ????6.22 | ????1.43 | ????0.75 | ????0.47 | ????1.45 | ????100.00 |
The chemical constitution (wt%) and the rate value thereof of the calcareous mud cement clinker of table 10 oil-containing
SiO
2Al
2O
3Fe
2O
3Other total amount of CaO MgO KH (0.86-0.90) IM (1.00-1.50) SM (1.80-2.20)
20.61????6.82???????4.58???????63.09???4.15???0.75??100.00???0.87???????????1.49???????????1.81
Table 11 prescription 3 removes the composition of raw materials (kg) of the calcareous mud cement clinker of Na oil-containing
Remove the calcareous mud CaO of the dried oil-containing of Na (calcium lime powder) river sand low-grade iron ore stone flour
61.52?????????????????43.64????????????15.56????5.32
1. will carry out grinding by the raw material of prescription 3 (tables 11) preparation and all mix, then 1300-1350 ℃ of insulation 2 hours.With the cooling of lowering the temperature rapidly of agglomerating grog.
2. with the abundant grinding of agglomerating grog, make it 90% sieve by the 0.08mm aperture.So far, the calcareous mud ordinary portland cement clinker of oil-containing is made.
Embodiment 4:
Embodiment 4 is on prescription 3 basis, and the calcareous mud of the wet Na of going oil-containing that adopts moisture 100wt% replaces the calcareous mud of the dried Na of going oil-containing and the prescription 4 (table 12) that forms.
The table 12 prescription 4 wet composition of raw materials (kg) that remove the calcareous mud cement clinker of Na oil-containing
Remove the calcareous mud CaO of the dried oil-containing of Na (calcium lime powder) river sand low-grade iron ore stone flour
123.04????????????????43.64????????????15.56????5.32
1. will carry out batch mixing in washing mud sump by the raw material of prescription 4 (tables 11) preparation, oven dry then is again 1300-1350 ℃ of insulation 2 hours.With the cooling of lowering the temperature rapidly of agglomerating grog.
3. with the abundant grinding of agglomerating grog, make it 90% sieve by the 0.08mm aperture.So far, the calcareous mud ordinary silicon of oil-containing
4. the acid salt cement grog is made.
The sintering technology process of the calcareous mud ordinary portland cement clinker of oil-containing:
1. press the raw grinding of formulated;
2. raw material cool off sintered material rapidly rapidly then 1300-1350 ℃ of sintering two hours;
3. the refrigerative sintered material powder is ground to certain fineness, promptly gets qualified cement clinker;
4. cement clinker and other material are mixed by a certain percentage and promptly form various ordinary Portland cements.The related properties of the calcareous mud ordinary portland cement clinker of oil-containing:
A) time of coagulation
With the cement clinker made in water: the ratio of cement clinker=1: 3 (volume) stirs, and into the diameter=2.5cm of pouring then, in the mould of height=1.2cm.Presetting period is 30 minutes, and final setting time is 10 hours.
B) mechanical property
The ultimate compression strength of cement block 3 days and 14 days is respectively 28.6MPa and 48.86Mpa.This mechanical property has met and exceeded the mechanical property of present commodity ordinary Portland cement.
Claims (3)
1. prepare the method for cement clinker with the calcareous mud of oil field oil-containing, it is characterized in that step is as follows:
1). with the calcareous mud water of oil field oil-containing flush away sodium,
2). by removing the calcareous mud of sodium oil field oil-containing and unslaked lime, quartz sand, Fe after 900 ℃ of roastings
2O
3Powder is prepared burden and is formed the material of cement slurry, and described each component is respectively the calcareous mud of sodium oil field oil-containing by weight: 35.48-47.39, unslaked lime: 33.74-43.64, quartz sand: 13.50-16.40, Fe
2O
3Powder: 2.2-5.32 carries out sintering behind the combined grinding to material;
3). the grog piece grinding that sinters, the sieve in 0.08mm aperture gets product excessively;
The chemical constitution of removing the calcareous mud of sodium oil field oil-containing after described 900 ℃ of roastings is SiO
26.76-12.07wt%, Al
2O
35.15-15.54wt%, Fe
2O
31.36-5.20wt%, CaO 54.31-71.16wt%, MgO 9.59-11.37wt%.
2. according to claim 1ly prepare the method for cement clinker, it is characterized in that: Fe described step 2) with the calcareous mud of oil field oil-containing
2O
3Powder can be used Fe
2O
3The iron ore of low ore grade of 46.43wt% is replaced.
3, according to claim 1ly prepare the method for cement clinker with the calcareous mud of oil field oil-containing, it is characterized in that: quartz sand can be replaced with river sand described step 2).
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CNB2004100606785A CN1298656C (en) | 2004-08-03 | 2004-08-03 | Method for preparing cement clinker with oil field oil-containing calcium sludge |
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CNB2004100606785A CN1298656C (en) | 2004-08-03 | 2004-08-03 | Method for preparing cement clinker with oil field oil-containing calcium sludge |
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CN1587158A true CN1587158A (en) | 2005-03-02 |
CN1298656C CN1298656C (en) | 2007-02-07 |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102050586A (en) * | 2010-11-08 | 2011-05-11 | 华南理工大学 | Method for producing silicate cement by utilizing urban sewage plant sludge |
CN101723427B (en) * | 2009-12-09 | 2011-05-25 | 中国石油天然气股份有限公司 | Resource utilization method for oil field oil extraction sludge |
CN104446052A (en) * | 2014-11-25 | 2015-03-25 | 广西鱼峰水泥股份有限公司 | Method for producing cement from 28-day strength clinkers |
CN109293190A (en) * | 2018-11-02 | 2019-02-01 | 南华大学 | A kind of processing method of oily sludge |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6176187B1 (en) * | 1994-03-16 | 2001-01-23 | Cement Industry Environmental Consortium | Sludge handling and feeding system |
CN1232457C (en) * | 2001-02-27 | 2005-12-21 | 天津水泥工业设计研究院 | Treating method of industrial and domestic sludge |
-
2004
- 2004-08-03 CN CNB2004100606785A patent/CN1298656C/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101723427B (en) * | 2009-12-09 | 2011-05-25 | 中国石油天然气股份有限公司 | Resource utilization method for oil field oil extraction sludge |
CN102050586A (en) * | 2010-11-08 | 2011-05-11 | 华南理工大学 | Method for producing silicate cement by utilizing urban sewage plant sludge |
CN102050586B (en) * | 2010-11-08 | 2012-10-31 | 华南理工大学 | Method for producing silicate cement by utilizing urban sewage plant sludge |
CN104446052A (en) * | 2014-11-25 | 2015-03-25 | 广西鱼峰水泥股份有限公司 | Method for producing cement from 28-day strength clinkers |
CN109293190A (en) * | 2018-11-02 | 2019-02-01 | 南华大学 | A kind of processing method of oily sludge |
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