CN1526529A - A burn-free brick made from oilfield sludge and its production method - Google Patents
A burn-free brick made from oilfield sludge and its production method Download PDFInfo
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- CN1526529A CN1526529A CNA031390536A CN03139053A CN1526529A CN 1526529 A CN1526529 A CN 1526529A CN A031390536 A CNA031390536 A CN A031390536A CN 03139053 A CN03139053 A CN 03139053A CN 1526529 A CN1526529 A CN 1526529A
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- river sand
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- 239000010802 sludge Substances 0.000 title claims abstract description 52
- 239000011449 brick Substances 0.000 title claims abstract description 34
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 16
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 41
- 239000004568 cement Substances 0.000 claims abstract description 38
- 239000004576 sand Substances 0.000 claims abstract description 17
- 239000010881 fly ash Substances 0.000 claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 8
- 239000002994 raw material Substances 0.000 claims description 20
- 229910052602 gypsum Inorganic materials 0.000 claims description 10
- 239000010440 gypsum Substances 0.000 claims description 10
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 8
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 8
- 239000011162 core material Substances 0.000 claims description 8
- 239000004571 lime Substances 0.000 claims description 8
- 239000004925 Acrylic resin Substances 0.000 claims description 7
- 229920000178 Acrylic resin Polymers 0.000 claims description 7
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 7
- 108010010803 Gelatin Proteins 0.000 claims description 7
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims description 7
- VSGNNIFQASZAOI-UHFFFAOYSA-L calcium acetate Chemical compound [Ca+2].CC([O-])=O.CC([O-])=O VSGNNIFQASZAOI-UHFFFAOYSA-L 0.000 claims description 7
- 239000001639 calcium acetate Substances 0.000 claims description 7
- 229960005147 calcium acetate Drugs 0.000 claims description 7
- 235000011092 calcium acetate Nutrition 0.000 claims description 7
- 239000001110 calcium chloride Substances 0.000 claims description 7
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 7
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- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 7
- 235000013539 calcium stearate Nutrition 0.000 claims description 7
- 239000008116 calcium stearate Substances 0.000 claims description 7
- 239000010436 fluorite Substances 0.000 claims description 7
- 239000008273 gelatin Substances 0.000 claims description 7
- 229920000159 gelatin Polymers 0.000 claims description 7
- 235000019322 gelatine Nutrition 0.000 claims description 7
- 235000011852 gelatine desserts Nutrition 0.000 claims description 7
- 239000002002 slurry Substances 0.000 claims description 7
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims description 4
- 229910052943 magnesium sulfate Inorganic materials 0.000 claims description 4
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims 1
- 229910004298 SiO 2 Inorganic materials 0.000 claims 1
- 235000019341 magnesium sulphate Nutrition 0.000 claims 1
- 238000001125 extrusion Methods 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 30
- 239000011148 porous material Substances 0.000 description 22
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 18
- JLDKGEDPBONMDR-UHFFFAOYSA-N calcium;dioxido(oxo)silane;hydrate Chemical compound O.[Ca+2].[O-][Si]([O-])=O JLDKGEDPBONMDR-UHFFFAOYSA-N 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 239000011575 calcium Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 12
- 229910001653 ettringite Inorganic materials 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 9
- 239000000499 gel Substances 0.000 description 9
- 238000012360 testing method Methods 0.000 description 9
- 229910000831 Steel Inorganic materials 0.000 description 8
- 239000000378 calcium silicate Substances 0.000 description 8
- 229910052918 calcium silicate Inorganic materials 0.000 description 8
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 8
- 238000006703 hydration reaction Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 239000010959 steel Substances 0.000 description 8
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Substances [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 7
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- 230000000694 effects Effects 0.000 description 7
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- 239000002245 particle Substances 0.000 description 7
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- 239000012153 distilled water Substances 0.000 description 6
- 238000001035 drying Methods 0.000 description 6
- 238000011160 research Methods 0.000 description 6
- 238000007711 solidification Methods 0.000 description 6
- 230000008023 solidification Effects 0.000 description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 5
- 230000009471 action Effects 0.000 description 5
- 239000004566 building material Substances 0.000 description 5
- 229910000019 calcium carbonate Inorganic materials 0.000 description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 description 5
- 239000011707 mineral Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000003825 pressing Methods 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 5
- -1 calcium carbonate aluminate Chemical class 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 238000000635 electron micrograph Methods 0.000 description 4
- 230000005855 radiation Effects 0.000 description 4
- 238000002441 X-ray diffraction Methods 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 229910052681 coesite Inorganic materials 0.000 description 3
- 229910052593 corundum Inorganic materials 0.000 description 3
- 229910052906 cristobalite Inorganic materials 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
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- 238000004458 analytical method Methods 0.000 description 2
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- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
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- 238000010438 heat treatment Methods 0.000 description 2
- 150000004677 hydrates Chemical class 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 239000003440 toxic substance Substances 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 229910021532 Calcite Inorganic materials 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 1
- 241000282414 Homo sapiens Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
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- 239000011149 active material Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
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- Curing Cements, Concrete, And Artificial Stone (AREA)
- Treatment Of Sludge (AREA)
Abstract
The present invention relates to no-baking brick, and is especially no-baking brick made of oil field sludge and its production process. The no-baking brick of the present invention is produced with the following material and through mixing and extrusion in extruder: oil field sludge 30-60 wt%, river sand 15-40 wt%, cement 15-30 wt%, flyash 0-35 wt% and curing agent 1-8 wt%. The no-baking brick of the present invention has high strength, no pollution and simple production process, and the present invention solves the problem of pollution and exhaust of oil field sludge.
Description
(I) in the field of technology
The invention relates to a baking-free brick and a production method thereof, in particular to a baking-free brick prepared from oil field sludge and a production method thereof.
(II) background of the invention
Oil-well muds are blood of oil drilling engineering, and with the development of the oil industry, the yield of the oil-well muds is increasing, and the oil-well muds generally contain a large amount of substances such as heavy metals, oils, alkalis and chemicals (including organic matters) which are extremely harmful to human beings, livestock and the environment. If the mud is discarded after use, the substances can seriously pollute the environment, harm the life and the body health of people and influence the growth and development of animals and plants if the mud is not treated.
The treatment and application of the oily sludge are the problems which are difficult to solve in the treatment process of the oily sewage. The technologies of oily sludge treatment and sludge comprehensive utilization by adopting biotechnology, physical and chemical methods and the like in western europe and the united states have been used for decades, the main processes comprise sludge concentration, conditioning, dehydration, harmless solidification, heat treatment, biological treatment, high-temperature treatment and the like, wherein the researches on biological treatment, disposal technology, high-temperature technology and solidification technology for drying oily sludge are more important, and as the oily sludge is an organic matter taking petroleum hydrocarbons as a main organic component, the biological treatment and disposal technology is to reduce the harm of the oily sludge to the environment by degrading the petroleum hydrocarbons by using microorganisms; the high-temperature treatment technology is used forrecovering hydrocarbon substances from the oily sludge by utilizing heat energy, and the process is carried out under a closed condition, so that the pollution to the surrounding environment can be reduced; the solidification treatment method is mainly characterized in that a certain composition of a curing agent is added into the oil field sludge to cause certain physical and chemical reactions, so that the water and a part of toxic substances in the oil field sludge are solidified and have certain strength so as to be convenient for stacking or storing.
In the aspect of comprehensive utilization of the oily sludge, the main utilization direction is the research of building materials, namely, the oil field sludge is taken as a main raw material, and a certain process is adopted to produce the ecological building materials, so that the oil field sludge is recycled, the waste is changed into the valuable, and a certain value is created for the society. On the other hand, the method solidifies toxic substances in the oil field sludge, prevents pollution of the oil field sludge, protects the ecological environment, prevents underground water from being polluted and harms personal safety, accords with national policies and industrialization policies, and is a sustainable development technology.
At present, China is more suitable for treating the oil field sludge by utilizing a solidification technology. However, in the prior art, the curing strength can not meet the requirements of building bricks on one hand, and can not meet the requirements of ecological building materials on the other hand, and the alkalinity, toxicity and radioactivity tests of the prior art do not meet the building material standards.
Disclosure of the invention
In order to overcome the defects, the invention provides the baking-free brick which is prepared from the oil field sludge and has high strength and meets the ecological environment-friendly requirement, and the production method thereof.
The invention is realized by the following measures:
a baking-free brick prepared from oil field sludge is prepared from the raw materials (by weight proportion) through mixing, and extruding with press,
oil field sludge: 30 to 60 percent
River sand: 15 to 40 percent of
Cement: 15 to 30 percent of
Fly ash: 0 to 35 percent
Curing agent: 1 to 8 percent
The curing agent is prepared from the following raw materials in parts by weight:
sulphoaluminate salt: 15% -25% of calcium stearate: 0 to 10 percent
Calcium chloride: 0-25% calcium acetate: 0 to 15 percent
Fluorite: 0-10% gelatin: 5 to 10 percent of
Gypsum: 10% -25% of lime: 10 to 30 percent
0 to 5 percent of acrylic resin
The baking-free brick of the invention comprises the following raw materials in parts by weight:
oil field sludge: 30 to 50 percent of
River sand: 15 to 30 percent of
Cement: 15 to 25 percent
Fly ash: 10 to 30 percent
Curing agent: 2 to 6 percent
The curing agent is prepared from the following raw materials in parts by weight,
sulphoaluminate salt: 15% -25% of calcium stearate: 0 to 10 percent
Calcium chloride: 10% -25% of calcium acetate: 0 to 15 percent
Fluorite: 4% -10% gelatin: 5 to 10 percent of
Gypsum: 10% -25% of lime: 10 to 30 percent
0 to 5 percent of acrylic resin
In order to improve the curing effect, the baking-free brick of the invention is also added with a core material accounting for 8-10% of the curing agent by weight, wherein the core material comprises the following raw materials in parts by weight:
| CaO | MgO | Fe2O3 | SiO2 | Al2O3 | Al2(SO4)4 | Na2CO3 | FeSO4 | MgSO4 |
| 5-10 | 5-10 | 5-10 | 6-15 | 8-15 | 2-20 | 10-20 | 5-20 | 5-20 |
the production method of the baking-free brick comprises the following steps,
1) adding appropriate amount of water into oil field sludge, river sand, cement, fly ash and curing agent, and mixing
The mixture is uniform and the mixture is uniform,
2) the slurry is filled into a die, the pressure of 500-700KN is applied on a press machine for pressing and forming,
demoulding and drying to obtain the finished product.
The curing mechanism of the present invention will now be further described:
the research utilizes testing means such as a D/max-rA type X-ray diffractometer, an S-2500 type scanning electron microscope and the like to research the curing mechanism of the baking-free bricks of the oil field sludge building.
X-ray diffraction analysis
As shown in figure 1, the main crystal phase-calcite in the sludge raw material is rarely seen in the cured baking-free brick, and besides quartz in the river sand as the filler, more minerals such as ettringite, calcium silicate hydrate, calcium carbonate aluminate, calcium aluminate hydrate and the like are seen.
2. Electron microscopy analysis
Scanning electron micrographs are shown in fig. 2 and fig. 3, fig. 2 is an electron micrograph of the laan oil field sludge baking-free brick cured for 7 days, fig. 3 is an electron micrograph of the oil field sludge baking-free brick cured for 28 days, and comparing fig. 2 and fig. 3, it can be found that the structure of fig. 2 is loose, and the solid particles are less in cementing and bonding minerals and are generally only hydration products of cement, namely calcium silicate hydrate; fig. 3 shows a compact structure, and various needle-shaped, rod-shaped and sheet-shaped cementing substances are filled among solid particles, and most of the cementing substances are minerals such as ettringite, calcium carbonate aluminate and calcium aluminate hydrate, which are formed by the combined action of curing agents, cement and some components in the le' an oilfield sludge.
3. Study of curing mechanism
From the above X-ray diffraction analysis and electron microscopic analysis, it is known that there are two main parts, C in cement, which play a role in solidification during the whole solidification process of oilfield sludge3S、C2S and other minerals are hydrated to form hydrated calcium silicate, and the action can be represented by a formula (5-1): (formula 5-1)
Secondly, calcium carbonate in the sludge of the oil field and C in the cement3A reacts to form acicular calcium carbonate aluminate (C)3A·3CaCO3·32H2Oand C3A·CaCO3·12H2O) its action can be represented by formulas 5-2 and 5-3: (formula 5-2) (formula 5-3)
Finally, the curing agent, the cement and the aluminum ions, the sulfate ions, the calcium ions and the like in the oil field sludge act together to form the ettringite.
1) The effect of cement
The cement and the waste mud are mixed with water and then have hydration reaction in cement hydrate, and the Calcium Silicate Hydrate (CSH) with the cementing effect is the main component which has the greatest contribution to the strength. Studies of cement chemistry have shown that:
(1) hydrated Calcium Silicate (CSH) produced in the liquid phase has a substantially constant Ca/S ratio, and Ca/Si is about 1.2. The thermodynamic equilibrium equation generated by CSH can be written as:
(2) liquid phase original Ca/Si, OH-The ratio of Si influences the type of hydration product when the original Ca/Si, OH of the liquid phase-When the ratio/Si is smaller, the silicic acid gel without the binding effect occupies a larger proportion in the hydration product along with the original Ca/Si, OH of the solution-The increase in the ratio/Si increases the proportion of CSH in the hydration product. From the thermodynamic equilibrium equation, liquid phase Ca2+、OH-Reduction of Ca (OH) in the pore water of cement2Under unsaturated conditions, the slurry must absorb a large amount of Ca necessary for the formation of CSH in order to achieve saturation adsorption2+、OH-This results in a decrease in the amount of CSHproduced. In the process of forming cement soil, the slurry is coupled with OH-，Ca2+The absorption and cement hydration of (2) release Ca (OH)2Are performed simultaneously. Early mud to OH-，Ca2+The large amount of absorption may result in the original Ca/Si, OH of the cement pore water-The ratio of Si is too low, so that the amount of silicic acid gel without binding capacity in the cement hydration product is increased, and OH is further consumed-、Ca2+The production amount of CSH is further reduced. Slurry pair OH-，Ca2+The higher the absorption amount of (A), OH in the cement pore water-，Ca2+The lower the concentration, the less CSH is produced by hydration of the cement in the cement soil. The curing agent contains minerals with high calcium content such as lime, gypsum, etc. so that Ca (OH)2Ca in supersaturated concentration to form CSH gel2+And OH-The concentration is sufficiently high so that the bonding effect of the curing agent is good. In addition, the active material slag is greatly mixed to replace part of cement, and Ca (OH)2After the reaction is carried out, more hydrates such as CSH gel are generated and the strength of the hydrates is continuously developed.
2) The action of the curing agent
The oil field sludge sample has weak interparticle connection, and a large amount of pore water causes the strength of the sample to be low, so that the strength of the sample is improved, an ideal curing agent has double functions of cementing particles and filling pores, and experimental research shows that cement is used as the curing agent, main hydrate of the cement is hydrated calcium silicate, CSH has strong cementing capacity, loose sample particles can be cemented into a whole, but the efficiency of filling the pores is low, CSH gel is generated between the sample particles and particles, the CSH gel is attached to the pore walls of the pores of the sample, the pore wall sample is cemented into a whole, but the effect of filling the pores is weak, and a large amount of pores still exist. Although CSH enhances the interparticle connection, the curing strength is improved to a certain extent; however, it cannot compensate for the strength loss caused by the voids in the specimen, and the curing strength is not ideal. The curing agent contains gypsum, and when the curing agent is hydrated, the gypsum reacts with aluminum-containing phase to generate a large amount of ettringite besides the same reaction as that of cement. The ettringite is a needle-like crystal under certain conditions, and the solid phase volume of the ettringite can be increased by about 120 percent in the crystal forming process. On one hand, the ettringite exists, and on the other hand, the ettringite fills partial pores due to the expansion of the solid phase volume of the ettringite, so that the amount of the pores of the test body is reduced; on the other hand, larger needle-like crystals are generated in the pores, are mutually crossed to form a space structure together with calcium silicate hydrate, and are supported and filled in the pores with higher efficiency to thin the pore size distribution of a solidified body, and researches on porous materials show that: the strength of a material is inversely related to its amount of porosity, with less porosity giving a higher strength. When the pore volume is the same, the smaller the average pore diameter is, the higher the strength is, the pore volume in the solidified soil is reduced, the average pore diameter in the solidified body is reduced, the pores between the particles are connected through the CSH gel, compared with the case of no curing agent is added, the strength of the sample is greatly increased due to the generation of the CSH gel, the curing agent not only generates a large amount of CSH gel, but also generates a plurality of fine needle-shaped stones, the ettringite is mutually crossed with calcium silicate hydrate, and the two stones interact with each other, so that the curing effect of the curing agent is better.
From the above analysis, it can be seen that what plays a role in curing in the baking-free brick of the oilfield sludge building is the result of the combined action of the curing agent, the cement and the oilfield sludge.
In conclusion, the baking-free brick has high strength and no pollution, and meets the requirements of ecological environment protection; the problems of pollution and discharge of sludge in the oil field are solved; the production method has the advantages of simple process and convenient manufacture.
(IV) description of the drawings
FIG. 1 is an X-ray diffraction pattern of the baking-free brick of the present invention
FIG. 2 is an electron micrograph of a baking-free brick of the present invention cured for 7 days
FIG. 3 is an electron micrograph of a non-fired brick of the present invention cured for 28 days
(V) detailed description of the preferred embodiments
1. Example 1
The raw material mixture ratio of the embodiment is 30% of oil field sludge, 40% of river sand, 26% of cement and 4% of curing agent.
Wherein, the curing agent is prepared by mixing the following raw materials in parts by weight:
sulphoaluminate salt: 22% calcium stearate: 5 percent of
Calcium chloride: 20% of calcium acetate: 0
Fluorite: 0 gelatin: 5 percent of
Gypsum: 20% of lime: 18 percent of
Acrylic resin 0
Core material: 10 percent of
Wherein the core material is prepared from the following components in parts by weightThe raw materials are mixed to obtain:
| CaO | MgO | Fe2O3 | SiO2 | Al2O3 | Al2(SO4)4 | Na2CO3 | FeSO4 | MgSO4 |
| 10 | 8 | 10 | 8 | 10 | 5 | 12 | 19 | 18 |
the production method comprises the following steps:
after the oil field sludge, the river sand, the cement and the curing agent are uniformly mixed, the mud slurry is filled into a die, the pressure of 550KN is applied to a press machine for pressing and forming, and the finished product is prepared after demoulding and drying.
According to the experimental method of the building materials specified by the national standard, the physical size, the volume weight, the water absorption rate, the mechanical properties (compression strength and rupture strength), the freezing resistance, the alkalinity content, the toxicity and the radioactivity of the baking-free brick are tested according to the standard of GB11945-89 autoclaved sand-lime brick and the standard of JC239-77 fly ash brick.
1) And (3) testing physical properties: physical size 240 x 116 x 52 cubic mm, capacity 2.17g/cm3The water absorption was 2.45%.
2) Mechanical properties: the average compressive strength of the steel plate after 28 days is 48.07Mpa, and the average flexural strength of the steel plate after 28 days is 12.26 Mpa.
3) And (3) freezing resistance test: every ten baking-free bricks are combined into a group, after 15 times of freeze-thaw cycles, the average compressive strength of the bricks is 46.43MPa, and the dry mass loss of a single brick is 1.13%.
4) Testing the alkali content: adding distilled water until the distilled water overflows the baking-free brick body, and heating to boil for 2-3 hours. After cooling, the pH value of the distilled water is 7-8, the distilled water is alkalescent, and no blooming phenomenon is caused.
5) And (3) toxicity testing: adding distilled water into the baking-free brick according to a certain proportion, oscillating and soaking for 8 hours, standing overnight, filtering by using 0.45-micron filter paper, taking filter residue as first leaching solution, adding distilled water into the filter residue according to the same proportion, soaking for multiple times according to the same method, and then compactingThe results are shown in the following table:
| number of immersion times | CODcr(mg/L) | pH value | Cr2+，Pb2+，Zn2+ |
| 1 | 2.14 | 7.5 | Not measured out |
| 2 | 0.89 | 7.0 | Not measured out |
| 3 | 0.30 | 6.0 | Not measured out |
| 4 | 0.25 | 5.5 | Not measured out |
6) And (3) radioactivity testing: the test is carried out by adopting an FD-3007K-A type pocket-sized radiometer, the radiation dose rate is 0.14uSV/h, and the radiation dose per month is 15.3 uSV. The radioactivity of the radiation is close to the radiance and radiation dose of the atmosphere.
The test results show that all the performances of the baking-free brick greatly exceed the national relevant standards of building bricks.
2. Example 2
The raw materials of the embodiment comprise 35% of oilfield sludge, 20% of river sand, 20% of cement, 24% of fly ash and 1% of curing agent.
Wherein, the curing agent is prepared by mixing the following raw materials in parts by weight:
sulphoaluminate salt: 15% calcium stearate: 2 percent of
Calcium chloride: 10% of calcium acetate: 15 percent of
Fluorite: 10% gelatin: 9 percent of
Gypsum: 10% of lime: 25 percent of
Acrylic resin 4%
After the oil field sludge, river sand, cement, fly ash and curing agent are uniformly mixed, the mud material is filled into a die, the pressure of 650KN is applied on a press machine for pressing and forming, and the finished product is prepared after demoulding and drying.
The performance test results are: the average compressive strength of the steel plate after 28 days is 16.66MPa, and the flexural strength of the steel plate after 28 days is 5.65 MPa. The mechanical property of the material can still meet the relevant national standard. Other properties were substantially the same as in example 1.
3. Example 3
The raw material mixture ratio of the embodiment is 55% of oil field sludge, 20% of river sand, 18% of cement and 7% of curing agent.
Wherein, the proportion of the curing agent is as follows:
sulphoaluminate salt: 20% calcium stearate: 5 percent of
Calcium chloride: 15% of calcium acetate: 10 percent of
Fluorite: 0 gelatin: 5 percent of
Gypsum: 15% of lime: 10 percent of
Acrylic resin 0 monoethylene glycol 5%
5 percent of sucrose
Core material: 10 percent of
Wherein the core material consists of the following raw materials in percentage by weight: CaO MgO Fe2O3SiO2Al2O3Al2(SO4)4Na2CO3FeSO4MgSO45 5 6 15 12 20 20 7 10
The production method comprises the following steps: after the oil field sludge, river sand, cement, fly ash and curing agent are uniformly mixed, the mud material is filled into a die, the pressure of 650KN is applied on a press machine for pressing and forming, and the finished product is prepared after demoulding and drying.
The performance test results are: the average compressive strength of the steel plate after 28 days is 35.26Mpa, and the flexural strength of the steel plate after 28 days is 8.65 Mpa. The mechanical property of the material can still meet the relevant national standard. Other properties were substantially the same as in example 1.
4. Example 4
The raw materials of the embodiment comprise 30% of oilfield sludge, 26% of river sand, 25% of cement, 16% of fly ash and 3% of curing agent.
The production method comprises the following steps: after the oil field sludge, river sand, cement, fly ash and a curing agent are uniformly mixed, the mud material is put into a die, the pressure of 700KN is applied on a press machine for pressing and forming, and the finished product is prepared after demoulding and drying.
The compounding ratio of the curing agent was the same as in example 3.
The performance test results are: the average compressive strength of the steel plate after 28 days is 25.28Mpa, and the flexural strength of the steel plate after 28 days is 7.25 Mpa. The mechanical property of the material can still meet the relevant national standard. Other properties were substantially the same as in example 1.
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| CN100358816C (en) * | 2005-11-22 | 2008-01-02 | 刘茂平 | Solidified agent for drilling well waste mud |
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| CN102503253A (en) * | 2011-10-12 | 2012-06-20 | 无锡晨驰江河科技有限公司 | Lake and river sludge processing method |
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