A kind of drilling wastes high strength solidification processing method and technology
Technical field
The present invention relates to oil-gas field offal treatment and recycling field thereof.
Background technology
Drilling wastes is meant that mainly rejected well drilling liquid and drilling cuttings etc. form solid waste after dehydration in the petroleum drilling or the mummification among the present invention.
This class solid waste that produces in the drilling process mainly contains clay, drilling cuttings, high-density weighting material and organic additive for drilling fluid.Undressed drilling wastes can bring certain harm to surrounding enviroment.For this type of refuse processing method, mainly contain methods such as direct discharging, landfill, curing, annular space or safe formation re-injection.At first, such waste is mainly used direct discharging and burying method is handled, and along with the further raising of environmental requirement, these two kinds of methods have been subjected to certain restriction.Annular space and safe formation re-injection, required equipment processing requirement complexity, cost height are not also used on a large scale in China at present.Solidification method is a drilling wastes treatment process commonly used.
At present, China's drilling wastes solidification treatment adopts single or composite curing agents such as portland cement, flyash more, directly uses the long-armed stirring of excavator at situ of drilling well, carries out scene or in-situ solidifying and handles, and fixed back landfill or earthing are restoreed abandoned land to cultivation.It is inhomogeneous that this method processing exists processing, defectives such as Pollutants Diffusion and migration.Having grown up with discarded drilling cuttings recycling abroad gradually is the stabilization/solidification technology of purpose.This class technology mainly is divided into two aspects: the one, and the oil-containing drilling wastes is mixed bituminous concrete mix, as road-making material; The 2nd, drilling cuttings mummification, pulverizing back are mixed with other materials (as clay), under hot conditions, be fired into building brick.There are problems such as the high and energy consumption of transportation cost is big in these two kinds of treatment processs.Above method there is no the effective solidified utilisation technology of waste salt-containing drilling thing (bore and meet saline bed or use the drilling wastes that salt-water drilling fluid produces).
Magnesium oxychloride cementing material technology is simple, and production energy consumption is little, and product has intensity height, advantage such as wear-resisting, can return halogen, distortion, water tolerance by what mix that materials such as flyash, slag, fiber or styrene emulsion improve this series products.Magnesium oxychloride cementing material has bigger application potential at environmental pollution control and solid waste resource recovery aspect utilizing, U.S. Pat 5439318 has been invented and has been used refuse and the soil technology that the glued envelope of magnesium oxychloride material is wrapped up in heavy metal contamination, makes the pollutent immobilization.Waste TCLP test result after the curing, heavy metal ion such as arsenic, barium, cadmium, chromium, lead, mercury, silver all are lower than the normality limit value.Chinese patent CN101823869 has invented a kind of fiber reinforced magnesium oxychloride red mud plate and preparation method, and the sheet material of preparation can have higher economy and environmental benefit with the utilization of aluminum oxide industry waste material red mud building materials.
Chlorion participates in the hydration process of magnesium oxychloride material, is that chlorion is a kind of important chemical composition in its hydrated product, can make the chlorion immobilization.It is consolidating material that the present invention adopts chlorine oxygen magnesium, and flyash and properties-correcting agent are subsidiary material, and with drilling wastes, waste salt-containing drilling thing solidification treatment, cured article has high compression strength and heavy metal ion leaching level is lower than the national requirements concentration limit.
Summary of the invention
Purpose of the present invention is for drilling wastes provides solidification processing method and the technology that a kind of technology is simple, intensity is high and Environmental compatibility is good.The Environmental compatibility and the potential recycling that utilize this method and technology can increase substantially drilling wastes are worth.
Know-why of the present invention: magnesium oxide, magnesium chloride and water are formed the MgO-MgCl of magnesia oxychloride cement hydration reaction
2-H
2The O ternary system, MgO-MgCl under the normal temperature
2-H
2Chemical reaction that the O system is finished and generation product can be simply suc as formula shown in (1)~(2).
MgO+H
2O→Mg(OH)
2 (1)
mMgO+MgCl
2+nH
2O→mMg(OH)
2·MgCl
2·(n-1)H
2O (2)
MMg (OH)
2MgCl
2(n-1) H
2O is mainly 5Mg (OH)
2MgCl
28H
2O (5 phase) and, 3Mg (OH)
2MgCl
28H
2O (3 phase), wherein 5 is main intensity phase mutually.Active SiO in the flyash
2And Al
2O
3Under alkaline condition, coagulate rigid reaction, can generate siliceous 5 phases, can reduce by 5 in opposite directions 3 mutually and Mg (OH)
2Conversion, improve condensate performance.
Main contents of the present invention: solidifying agent mainly contains magnesium oxide, magnesium chloride, flyash, properties-correcting agent and water to be formed, wherein, and light calcined magnesia 20~40%, magnesium chloride 10%~30%, flyash 20~45%, properties-correcting agent 0.5%~1.2%, water 10%~30%.
Wherein, properties-correcting agent mainly consists of quartz 10%~30%, gypsum 15~20%, potassiumphosphate 0~20%, Tai-Ace S 150 0~30%.
The drilling wastes dosage is 40%~60%, compaction moulding, and natural curing 28d under the envrionment temperature, ultimate compression strength can reach 40MPa.
Concrete grammar: in drilling wastes, add flyash, light calcined magnesia and properties-correcting agent successively, after mixing, add magnesium chloride solution, after puddling evenly, change mould over to, compression moulding, the fixed back demoulding, natural curing is at ambient temperature solidified drilling wastes 28d ultimate compression strength and can be reached 40MPa, and leach liquor heavy metal ion level is lower than national solid dangerous waste and leaches the toxicity limit value.
Compared with prior art, advantage of the present invention is as follows:
1, the present invention uses the solidification treatment system that magnesium oxide-magnesium chloride-flyash constitutes, and has promptly realized the stabilization/solidification treatment to drilling wastes, gives its stronger ultimate compression strength simultaneously, makes it to have than the large resource utility value.
2, magnesium oxide is mainly fired by magnesite among the present invention, and its calcining temperature is about 700 ℃, is lower than portland cement calcining temperature and clay brick firing temperature, has power savings advantages.
3, the flyash that uses among the present invention is power plant's industrial waste, and treatment of wastes with processes of wastes against one another environment protection significance is great.
4, curing process is simple to operation among the present invention, is easy to large-scale promotion.
Embodiment
Embodiment 1
Get the solid waste 1kg that solid controlling system is discharged in certain oilfield drilling, after the solidifying agent of different compositions mixes, compaction moulding, the fixed back demoulding, 3d is measured in natural curing under the envrionment temperature respectively, 7d, 14d, 28d ultimate compression strength the results are shown in Table 1.
Table 1 drilling wastes high strength solidification treatment solidifying agent is formed and ultimate compression strength
Annotate: " * " expression " is not surveyed "
Embodiment 2
Get drilling wastes in the example 1, add sodium-chlor respectively, make the simulation waste salt-containing drilling thing 1kg of different sodium chloride contents, form according to No. 5 solidifying agent in the table 1, be cured processing, its ultimate compression strength the results are shown in Table 2.
Table 2 waste salt-containing drilling object height intensity is solidified and ultimate compression strength
Annotate: " * " expression " is not surveyed "
Embodiment 3
Get above-mentioned drilling wastes, solidify the drilling wastes sample No. 5, No. 6, No. 10, be crushed to particle diameter less than 9.5mm, with sulfuric acid-nitric acid (mass ratio 2: 1) the laboratory pure water is regulated pH to 3.25, take by weighing according to solid sample and digestion agent in 1: 10 ratio, (frequency 110 ± 2 times/min), static 16h is with 0.45 cellulose acetate membrane filtration for level concussion 8h, heavy metal ion is formed in the test leach liquor, the results are shown in Table 3.
Table 3 solidifies drilling wastes leach liquor heavy metal ion to be formed
Annotate: "-" indicates " not detecting "
Embodiment 4
Get domestic certain oil field and deposit the solid waste of various oil field working fluid pollution discharge pond such as rejected well drilling liquid, flushing fluid, fracturing liquid, add 0.4kg flyash, 0.36kg magnesium oxide, 0.26kg magnesium chloride, 0.012kg properties-correcting agent and 0.1kg water according to every kilogram of solid waste (dry weight), puddle evenly, compaction moulding, after the fixed demoulding, natural curing 30d under the envrionment temperature, its ultimate compression strength is 40MPa.To solidify the waste sample, be crushed to particle diameter less than 9.5mm, with sulfuric acid-nitric acid (mass ratio 2: 1) the laboratory pure water is regulated pH to 3.25, take by weighing according to solid sample and digestion agent in 1: 10 ratio, (frequency 110 ± 2 times/min), static 16h is with 0.45 cellulose acetate membrane filtration for level concussion 8h, heavy metal ion is formed in the test leach liquor, the results are shown in Table four.
Table four solidifies waste leach liquor contaminant detection results
Project |
Emission standard |
Detected result |
PH value |
<=6~9 |
8.72mg/L |
Chemical oxygen demand (COD) |
<=150mg/L |
103.2mg/L |
Petroleum-type |
<=10.0mg/L |
2.0mg/L |
Vegetable and animals oils |
<=15.0mg/L |
1.8mg/L |
Sulfide |
<=1.0mg/L |
0.015mg/L |
Suspended substance |
<=150mg/L |
9mg/L |
Colourity |
<=80 |
8 |
Ammonia nitrogen |
<=25mg/L |
0.685mg/L |
Arsenic |
<=0.5mg/L |
0.01mg/L |
Copper |
<=1.0mg/L |
0.023mg/L |
Zinc |
<=5.0mg/L |
0.039mg/L |
Plumbous |
<=1.0mg/L |
0.038mg/L |
Every |
<=0.1mg/L |
0.024mg/L |
Nickel |
<=1.0mg/L |
0.486mg/L |
Manganese |
<=5.0mg/L |
- |
Annotate: "-" indicates " not detecting "