NL2034691A - Recycling method of core drilling waste mud - Google Patents
Recycling method of core drilling waste mud Download PDFInfo
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- NL2034691A NL2034691A NL2034691A NL2034691A NL2034691A NL 2034691 A NL2034691 A NL 2034691A NL 2034691 A NL2034691 A NL 2034691A NL 2034691 A NL2034691 A NL 2034691A NL 2034691 A NL2034691 A NL 2034691A
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- mud
- waste
- waste mud
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- 239000002699 waste material Substances 0.000 title claims abstract description 90
- 238000000034 method Methods 0.000 title claims abstract description 51
- 238000005553 drilling Methods 0.000 title claims abstract description 41
- 238000004064 recycling Methods 0.000 title claims abstract description 36
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 90
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000007788 liquid Substances 0.000 claims abstract description 40
- 239000002245 particle Substances 0.000 claims abstract description 31
- 244000030166 artemisia Species 0.000 claims abstract description 29
- 239000002910 solid waste Substances 0.000 claims abstract description 10
- 238000010276 construction Methods 0.000 claims abstract description 9
- 229920002401 polyacrylamide Polymers 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims description 28
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 239000007864 aqueous solution Substances 0.000 claims description 16
- 239000002253 acid Substances 0.000 claims description 14
- 239000003638 chemical reducing agent Substances 0.000 claims description 12
- 239000004850 liquid epoxy resins (LERs) Substances 0.000 claims description 12
- 238000002156 mixing Methods 0.000 claims description 11
- 239000000243 solution Substances 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000002791 soaking Methods 0.000 claims description 8
- 239000008247 solid mixture Substances 0.000 claims description 8
- 239000010902 straw Substances 0.000 claims description 8
- VKZRWSNIWNFCIQ-WDSKDSINSA-N (2s)-2-[2-[[(1s)-1,2-dicarboxyethyl]amino]ethylamino]butanedioic acid Chemical compound OC(=O)C[C@@H](C(O)=O)NCCN[C@H](C(O)=O)CC(O)=O VKZRWSNIWNFCIQ-WDSKDSINSA-N 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 6
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 5
- 239000000292 calcium oxide Substances 0.000 claims description 5
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 5
- 238000012360 testing method Methods 0.000 claims description 5
- MPJQXAIKMSKXBI-UHFFFAOYSA-N 2,7,9,14-tetraoxa-1,8-diazabicyclo[6.6.2]hexadecane-3,6,10,13-tetrone Chemical compound C1CN2OC(=O)CCC(=O)ON1OC(=O)CCC(=O)O2 MPJQXAIKMSKXBI-UHFFFAOYSA-N 0.000 claims description 4
- 235000001405 Artemisia annua Nutrition 0.000 claims description 4
- 240000000011 Artemisia annua Species 0.000 claims description 4
- 239000012670 alkaline solution Substances 0.000 claims description 4
- 230000003113 alkalizing effect Effects 0.000 claims description 4
- 229940071087 ethylenediamine disuccinate Drugs 0.000 claims description 4
- 238000000227 grinding Methods 0.000 claims description 4
- 238000005086 pumping Methods 0.000 claims description 4
- 238000005303 weighing Methods 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 claims 4
- 239000000701 coagulant Substances 0.000 claims 3
- 238000002203 pretreatment Methods 0.000 claims 2
- 238000005520 cutting process Methods 0.000 claims 1
- 239000001384 succinic acid Substances 0.000 claims 1
- 238000007711 solidification Methods 0.000 abstract description 27
- 230000008023 solidification Effects 0.000 abstract description 27
- 230000003068 static effect Effects 0.000 abstract description 16
- 239000000126 substance Substances 0.000 abstract description 11
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 7
- 239000002923 metal particle Substances 0.000 abstract description 6
- 238000001556 precipitation Methods 0.000 description 13
- 235000011121 sodium hydroxide Nutrition 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 239000003921 oil Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000002834 transmittance Methods 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 239000010426 asphalt Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000002829 reductive effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 235000003826 Artemisia Nutrition 0.000 description 1
- 235000003261 Artemisia vulgaris Nutrition 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 206010020751 Hypersensitivity Diseases 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229920001938 Vegetable gum Polymers 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 208000030961 allergic reaction Diseases 0.000 description 1
- 235000009052 artemisia Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000007596 consolidation process Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000012530 fluid Substances 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
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000011499 joint compound Substances 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28057—Surface area, e.g. B.E.T specific surface area
- B01J20/28066—Surface area, e.g. B.E.T specific surface area being more than 1000 m2/g
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/008—Sludge treatment by fixation or solidification
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
- C02F11/148—Combined use of inorganic and organic substances, being added in the same treatment step
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/06—Arrangements for treating drilling fluids outside the borehole
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/06—Arrangements for treating drilling fluids outside the borehole
- E21B21/063—Arrangements for treating drilling fluids outside the borehole by separating components
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/06—Arrangements for treating drilling fluids outside the borehole
- E21B21/063—Arrangements for treating drilling fluids outside the borehole by separating components
- E21B21/065—Separating solids from drilling fluids
- E21B21/066—Separating solids from drilling fluids with further treatment of the solids, e.g. for disposal
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/06—Arrangements for treating drilling fluids outside the borehole
- E21B21/068—Arrangements for treating drilling fluids outside the borehole using chemical treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Mining & Mineral Resources (AREA)
- Geology (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The disclosure relates to a recycling method of core drilling waste mud. The innovation is that core drilling waste mud is subjected to step-by-step treatment by using a pretreatment agent and a posttreatment agent, wherein nonionic polyacrylamide in the pretreatment agent coordinates with modified activated carbon particles to wrap, adsorb and flocculate oil residues, heavy metal particles and macromolecular chemicals in the waste mud to finally form a “clear liquid” on an upper layer and a “turbid liquid” on a lower layer. The “clear liquid” on the upper layer is extracted back to core drilling construction for recycling; the “turbid liquid” on the lower layer is pumped into a static solidification tank, and solidified through coordination of an amidoamine mud solidifying agent in the posttreatment agent with artemisia plants so that “turbid liquid” forms a solid waste whose volume is 5%-8% of that of the original waste mud.
Description
RECYCLING METHOD OF CORE DRILLING WASTE MUD
[0001] The disclosure belongs to the field of geological drilling, and relates to a drilling waste mud treatment technology, particularly to a recycling method of core drilling waste mud.
[0002] Core drilling mud plays the roles in cooling a drill, maintaining a hole wall, carrying rock debris and balancing strata pressure and the like. To exert the above functions, it is needed to add chemical products such as bentonite, a fluid loss additive, carboxymethyl cellulose, vegetable gum, potassium humate, sulfonated asphalt, a high-viscosity plugging agent and caustic soda in core drilling mud. In order to maintain the performance of the core drilling mud, the mud needs to be continuously added and replaced. In this process, a large amount of waste mud is generated, which contains fine grain mud and sand, oily residues, heavy metal particles, macromolecular chemicals (such as plant gum molecules and sulfonated asphalt molecules) contained in the original drilling mud, and macromolecular polymers wrapped with colloidal substances such as mud and sand, oils and heavy metal particles. These waste residues are mixed with waste mud so as not to be properly treated and utilized, and improper disposal (such as random discharge) can cause greater pollution to the environment.
[0003] Construction positions for core drilling are generally located in mountainous and hilly areas, and therefore a large amount of waste mud cannot be properly treated. In the existing technology, it usually requires a lot of manpower, material resources and financial resources to transfer and treat the waste mud, which is not economical and environmental-friendly, so that the waste mud cannot be effectively and properly treated for a long time. Therefore, it is particularly important to provide a cheap and simple waste mud treatment method which has huge transformation, promotion and application values in the industry.
[0004] In order to overcome the inconvenience in the prior art, the disclosure provides a recycling method of core drilling waste mud, which can be efficiently and practically applied to the field of solid mineral exploration. Through the recycling method, oil residues in the waste mud are adsorbed and flocculated, and heavy metal particles and macromolecular chemicals in the waste mud are precipitated and flocculated to finally form a “clear liquid” on an upper layer and a “turbid liquid” on a lower layer. The “clear liquid” on the upper layer is extracted back to recycling of core drilling, and the “turbid liquid” on the lower layer is pumped into a static solidification tank to be treated by a solidifying agent so as to concrete blocky solid wastes which are convenient to treat, and economic and environmental-friendly.
[0005] The technical problems of the disclosure are solved by using the following technical solution:
[0006] Provided is an recycling method of core drilling waste mud, comprising the following steps:
[0007] (1) preparing a precipitation treatment tank and a static solidification tank around a construction field, wherein the bottoms and the peripheries of the precipitation treatment tank and the static solidification tank are both wrapped by using waterproof materials;
[0008] (2) pouring core drilling waste mud into the precipitation treatment tank, testing the A-pH value of waste mud to be treated, adding the pretreatment agent according to the A-pH value range, sufficiently mixing and stirring and then standing for 12-24 h; wherein, at the pH of 8.0-8.5 or less than 8.0, 20-25 L of pretreatment agent aqueous solution needs to be added to treat waste mud per cubic meter; at the pH of 8.5-9.0 or more than 9.0, 15-20 L of pretreatment agent aqueous solution needs to be added to treat waste mud per cubic meter;
[0009] (3) standing and layering the waste mud in the precipitation treatment tank after addition of the pretreatment agent to form a “clear liquid” on an upper layer and a “turbid liquid” on a lower layer, extracting the “clear liquid” on the upper layer back to core drilling construction for recycling, and pumping the “turbid liquid” on the lower layer into the static solidification tank; and
[0010] (4) after pretreatment, when the waste mud enters the static solidification tank, sprinkling 5-10 parts by mass of posttreatment agent based on waste mud per cubic meter for treatment, standing for 3-5 d after fully mixing and stirring to finally form a blocky “solidified layer” whose volume is 5%-8% of the volume of the original waste mud, then recycling the solid waste of the “solidified layer”.
[0011] The pretreatment agent comprises the following components in parts by mass:
[0012] 8-10 parts of nonionic polyacrylamide;
[0013] 2-3 parts of calcium oxide;
[0014] 4-5 parts of modified activated carbon particles,
[0015] a method for preparing the pretreatment agent comprises: various components in the pretreatment agent are ground in a grinding machine and then screened by a 100-mesh sieve to obtain a pretreatment agent solid mixture; when in use, the pretreatment agent aqueous solution is prepared: 10 kg of pretreatment agent solid mixture is added into pure water per cubic meter to be sufficiently stirred to obtain the pretreatment agent aqueous solution.
[0016] A method for preparing the modified activated carbon particles comprises:
[0017] (1) soaking powdered activated carbon particles into a H20: solution for 10-12 h, and then evenly stirring every 2 h followed by extracting and filtering to obtain per-oxidized activated carbon particles after treatment; and
[0018] (2) soaking the per-oxidized activated carbon particles in a 60-80wt%
NaOH strong alkaline solution for 10-12 h, and then evenly stirring every 2 h followed by extracting and filtering to obtain modified activated carbon particles after treatment, wherein the modified activated carbon particle has a specific surface area of 1625.33-1695.16 m?/g and a porosity of 55-57% which are significantly improved compared with those of commercially available common activated carbon (specific area is 1200-1400 m?/g, and a porosity of 45-50%).
[0019] The posttreatment agent comprises an amidoamine mud solidifying agent and an alkalized artemisia grass plant which are mixed in a ratio of 1:0.5,
[0020] The amidoamine mud solidifying agent comprises the following components in parts by mass:
[0021] 20-25 parts of ethylenediamine disuccinate;
[0022] 25-30 parts of polycarboxylic acid water reducer;
[0023] 15-20 parts of liquid epoxy resin.
[0024] Specifically, a method for preparing the above amidoamine mud solidifying agent comprises the following steps:
[0025] (1) weighing ethylenediamine disuccinic acid, a polycarboxylic acid water reducer and a liquid epoxy resin;
[0026] (2) evenly mixing ethylenediamine disuccinic acid with the liquid epoxy resin, heating to 150-170°C, and then stirring to react for 2-4 h;
[0027] (3) adding the polycarboxylic acid water reducer, and heating to 150-170°C, and then stirring to react for 2-4 h; and
[0028] (4) cooling the mixture obtained in step (3) to < 40°C, evenly stirring and then discharging, so as to obtain the amidoamine mud solidifying agent.
[0029] The artemisia plant is preferably artemisia annua. A method for alkalizing the artemisia plant comprises: the artemisia plant is smashed into 1-2 mm straws, the straws are mixed and soaked into a 10-20wt% NaOH solution for 10-12 h, the above mixture is evenly stirred every 2 h, and then the treated artemisia plant is obtained after 8-10 h.
[0030] During the solidification, the artemisia plant plays the roles in “bridging”, accelerating the solidification and enhancing the stability of the block after solidification to a certain extent, meanwhile, combination of the artemisia plant with a solidifying agent can appropriately reduce the use amount of the solidifying agent, makes a chemical reagent and a plant jointly coordinate to take a synergistic effect, which accelerates the solidification and has positive environment-friendly effect while reducing the solidification treatment
[0031] The disclosure has the advantages and beneficial effects:
[0032] 1. The pretreatment agent in the method of the disclosure uses the nonionic polyacrylamide and the modified activated carbon which are cheap to cooperate with the waste mud to flocculate the mud sand, heavy metal particle residues and other wastes in the waste mud, and wrap the flocculates with other 5 macromolecular chemicals. Through the modified activated carbon, the adsorption effect on heavy metal large particle substances and oily residue wastes is increased; meanwhile on the one hand, calcium oxide releases heat when encountering water to accelerate the treatment reaction; on the other hand, calcium hydroxide generated after encountering water can neutralize a small amount of free acids and acid salt substances in the waste mud, and forms a water-insoluble sediment with metal ions in the waste mud, so as to further separate the waste mud and accelerate the separation, adsorption and flocculation of the waste mud.
[0033] 2. The main action mechanism of the posttreatment agent in the method of the disclosure is that an ion exchange adsorption mechanism is established through the amidoamine mud solidifying agent so that the “turbid liquid” can achieve rapid water loss and consolidation. Meanwhile, the alkalized artemisia plants are added, and the artemisia micro-fine stalks play a “bridging” role in the solidification of the residues so as to further accelerate the solidification reaction of “turbid liquid”.
[0034] The design of the disclosure is scientific and reasonable, and the innovation is that core drilling waste mud is subjected to step-by-step treatment by using the pretreatment agent and the posttreatment agent, wherein nonionic polyacrylamide in the pretreatment agent coordinates with modified activated carbon particles to wrap, adsorb and flocculate oil residues, heavy metal particles and macromolecular chemicals in the waste mud to finally form a “clear liquid” on an upper layer and a “turbid liquid” on a lower layer, the “clear liquid” on the upper layer is extracted back to core drilling construction for recycling; the “turbid liquid” on the lower layer is pumped into the static solidification tank, and solidified through coordination of the amidoamine mud solidifying agent in the posttreatment agent with the artemisia plants so that the “turbid liquid” is accelerated to form the solid waste whose volume is 5%-8% of that of the original waste mud. The method of the disclosure is convenient to recycle, improves the recycling rate of the waste mud and greatly reduces the pollution of the waste mud on environments.
[0035] FIG.1 is a structural diagram of a precipitation treatment tank and a static solidification tank according to the disclosure;
[0036] FIG.2 1s a diagram showing effects before and after a pretreatment agent and a posttreatment agent are added in a two-stage treatment pool in FIG. 1;
[0037] FIG.3 is a use effect diagram of a treatment method according to the disclosure.
[0038] Next, the disclosure will be further described in detail through specific embodiments. The following examples are only descriptive but not limiting, and cannot thereby limit the protective scope of the disclosure.
[0039] By using the method of the disclosure, a test is conducted in the gold resource exploration base in Wulashan area, Baotou, Inner Mongolia. The main working method is geological core drilling, and the drilling mud is an indispensable fluid material in the drilling process. However, in this process, the waste mud that is difficult to treat is formed after the mud is used.
[0040] The disclosure provides a recycling method of core drilling waste mud, comprising the following steps:
[0041] (1) as shown in FIG.1, preparing a precipitation treatment tank and a static solidification tank around a construction field, wherein the bottoms and the peripheries of the precipitation treatment tank and the static solidification tank are both wrapped by using waterproof materials;
[0042] (2) pouring core drilling waste mud into the precipitation treatment tank, testing the A-pH value of waste mud to be treated, adding the pretreatment agent according to the A-pH value range, sufficiently mixing and stirring and then standing for 12-24 h; wherein, at the pH of 8.0-8.5 or less than 8.0, 20-25 L of pretreatment agent aqueous solution needs to be added into waste mud per cubic meter for treatment; at the pH of 8.5-9.0 or more than 9.0, 15-20 L of pretreatment agent aqueous solution needs to be added into the waste mud per cubic meter for treatment
[0043] (3) standing and layering the waste mud in the precipitation treatment tank after addition of the pretreatment agent to form a “clear liquid” on an upper layer and a “turbid liquid” on a lower layer, extracting the “clear liquid” on the upper layer back to recycling of core drilling, and pumping the “turbid liquid” on the lower layer into a static solidification tank; and
[0044] (4) after pretreatment, when the waste mud enters the static solidification tank, sprinkling 5-10 parts by mass of posttreatment agent based on waste mud per cubic meter for treatment, standing for 1-2 d after fully mixing and stirring to finally form a blocky “solidified layer” whose volume is 5%-8% of the volume of the original waste mud, then recycling the solid waste of the “solidified layer”.
The effects of the two-stage treatment pool after the pretreatment agent and the posttreatment agent are added are as shown in FIG.2.
[0045] The innovation of the disclosure is to develop the pretreatment agent and the posttreatment agent to treat the core drilling waste mud. The pretreatment agent comprises the following components in parts by mass: 8-10 parts of nonionic polyacrylamide, 2-3 parts of calcium oxide and 4-5 parts of modified activated carbon particles. A method for preparing the pretreatment agent comprises: various components in the pretreatment agent are ground in a grinding machine and then screened by a 100-mesh sieve to obtain a pretreatment agent solid mixture; when in use, the pretreatment agent aqueous solution is prepared: 10 kg of pretreatment agent solid mixture is added into pure water per cubic meter to be sufficiently stirred to obtain the pretreatment agent aqueous solution.
[0046] In the disclosure, the common activated carbon powders are modified, and a method for preparing the modified activated carbon particles comprises:
[0047] (1) soaking powdered activated carbon particles into a H202 solution for 10-12 h, and then evenly stirring every 2 h followed by extracting and filtering to obtain per-oxidized activated carbon particles after treatment; and
[0048] (2) soaking the per-oxidized activated carbon particles in a 60-80wt%
NaOH strong alkaline solution for 10-12 h, and then evenly stirring every 2 h followed by extracting and filtering to obtain modified activated carbon particles after treatment, wherein the modified activated carbon particle has a specific surface area of 1625.33-1695.16 m?/g and a porosity of 55-57% which are significantly improved compared with those of commercially available common activated carbon (specific area is 1200-1400 m?/g, and a porosity of 45-50%).
[0049] The posttreatment agent comprises an amidoamine mud solidifying agent and an alkalized artemisia grass plant which are mixed in a ratio of 1:0.5. The amidoamine mud solidifying agent comprises the following components in parts by mass: 20-25 parts of ethylenediamine disuccinate, 25-30 parts of polycarboxylic acid water reducer and 15-20 parts of liquid epoxy resin.
Specifically, a method for preparing the above amidoamine mud solidifying agent comprises the following steps:
[0050] (1) weighing ethylenediamine disuccinic acid, a polycarboxylic acid water reducer and a liquid epoxy resin;
[0051] (2) evenly mixing ethylenediamine disuccinic acid with the liquid epoxy resin, heating to 150-170°C, and then stirring to react for 2-4 h;
[0052] (3) adding the polycarboxylic acid water reducer, and heating to 150-170°C, and then stirring to react for 2-4 h; and
[0053] (4) cooling the mixture obtained in step (3) to < 40°C, evenly stirring and then discharging, so as to obtain the amidoamine mud solidifying agent.
[0054] The artemisia plant is preferably artemisia annua. A method for alkalizing the artemisia plant comprises: the artemisia plant is smashed into 1-2 mm straws, the straws are mixed and soaked into a 10-20wt% NaOH solution for 10-12 h, the above mixture is evenly stirred every 2 h, and then the treated artemisia plant is obtained after 8-10 h.
[0055] During the solidification, the artemisia plant plays the roles in “bridging”, accelerating the solidification and enhancing the stability of the block after solidification to a certain extent; moreover, the artemisia plant is widely developed in Inner Mongolia, its pollens cause people in most regions to have allergic reaction, and the artemisia plant is alkalized and then can serve as a utilization object to be applied in the field of solidifying agents and has an important practical values.
[0056] In the disclosure, an untreated waste mud is compared with a treated waste mud, and the comparison results are seen in FIG.3. Meanwhile, specified determination is conducted, and specific determination results as shown in table below: “Turbid liquid on the lower
Determination Untreated liquid” on Add a index waste solution | the upper | Stand for 10 | solidifying layer h agent and stand for 1 d
Amount % of mud separated by 35 9 45 centrifuge transmittance%o
Volatile phenol
Suspended solids Consolidated
Chemical oxygen
[0057] In summary, after treatment with the method disclosed by this parent application, the amounts of mud, suspended solids and oils in the “clear liquid” are greatly reduced, and the light transmittance 1s increased, which is consistent with the recycling of drilling mud; after treatment, the amounts of sludge, suspended solids, oils, metal ions, chemical oxygen demand and the like in the “turbid liquid” are increased to varying degrees, and the light transmittance is decreased.
[0058] It can also be observed intuitively from FIG.3 that in the method disclosed by this patent application, the untreated waste mud in the process of core drilling has achieved obvious separation effect of “clear liquid” and “turbid liquid” after the treatment of the above steps in this application, wherein the “clear liquid” can be recycled, and the “turbid liquid” can form a solid waste after standing and solidification treatment, the volume of the solid waste is 5%-8% of the volume of the original waste mud, then, the solid waste of the “solidified layer” can be recycled, and therefore recycling is convenient, and the pollution of the waste mud to the environment is greatly reduced.
[0059] Although the embodiments of the disclosure are disclosed for the purpose of illustration, those skilled in the art should be understood that various replacements, changes and modifications are all made without departing from the spirit and scope of the disclosure and appended claims. Therefore, the scope of the disclosure is not limited to the contents disclosed by the embodiments.
[0060] PREFERRED EMBODIMENTS
[0061] An recycling method of core drilling waste mud, comprising the following steps:
[0062] (1) preparing a precipitation treatment tank and a static solidification tank around a construction field, wherein the bottoms and the peripheries of the precipitation treatment tank and the static solidification tank are both wrapped with waterproof materials;
[0063] (2) pouring core drilling waste mud into the precipitation treatment tank, testing the A-pH value of waste mud to be treated, adding the pretreatment agent according to the A-pH value range, sufficiently mixing and stirring and then standing for 12-24 h;
[0064] (3) standing and layering the waste mud in the precipitation treatment tank after addition of the pretreatment agent to form a “clear liquid” on an upper layer and a “turbid liquid” on a lower layer, extracting the “clear liquid” on the upper layer back to core drilling construction for recycling, and pumping the “turbid liquid” on the lower layer into the static solidification tank; and
[0065] (4) after completion of pretreatment, when the waste mud enters the static solidification tank, sprinkling 5-10 parts by mass of posttreatment agent based on waste mud per cubic meter for treatment, standing for 3-5 d after fully mixing and stirring to finally form a blocky “solidified layer” whose volume is 5%-8% of the volume of the original waste mud, and then recycling solid wastes in the “solidified layer”,
[0066] the pretreatment agent comprises the following components in parts by mass:
[0067] 8-10 parts of nonionic polyacrylamide;
[0068] 2-3 parts of calcium oxide;
[0069] 4-5 parts of modified activated carbon particles,
[0070] the posttreatment agent comprises an amidoamine mud solidifying agent and an alkalized artemisia grass plant which are mixed in a ratio of 1:0.5,
[0071] the amidoamine mud solidifying agent comprises the following components in parts by mass:
[0072] 20-25 parts of ethylenediamine disuccinate;
[0073] 25-30 parts of polycarboxylic acid water reducer;
[0074] 15-20 parts of liquid epoxy resin.
[0075]
[0076] 2. The recycling method of core drilling waste mud according to embodiment 1, wherein at the pH of 8.0-8.5 or less than 8.0, 20-25 L of pretreatment agent aqueous solution needs to be added into waste mud per cubic meter for treatment; at the pH of 8.5-9.0 or more than 9.0, 15-20 L of pretreatment agent aqueous solution needs to be added into the waste mud per cubic meter for treatment.
[0077] 3. The recycling method of core drilling waste mud according to embodiment 1, wherein a method for preparing the pretreatment agent comprises: various components in the pretreatment agent are ground in a grinding machine and then screened by a 100-mesh sieve to obtain a pretreatment agent solid mixture; when in use, the pretreatment agent aqueous solution is prepared: 10 kg of pretreatment agent solid mixture is added into pure water per cubic meter to be sufficiently stirred to obtain the pretreatment agent aqueous solution.
[0078] 4. The recycling method of core drilling waste mud according to embodiment 1, wherein a method for preparing the modified activated carbon particles comprises:
[0079] (1) soaking powdered activated carbon particles in a H202 solution for 10-12 h, evenly stirring every 2 h, followed by extracting and filtering to obtain per-oxidized activated carbon particles; and
[0080] (2) soaking the per-oxidized activated carbon particles in a 60-80wt%
NaOH strong alkaline solution for 10-12 h, and then evenly stirring every 2 h followed by extracting and filtering to obtain modified activated carbon particles after treatment, wherein the modified activated carbon particle has a specific surface area of 1625.33-1695.16 m2/g and a porosity of 55-57%.
[0081] 5. The recycling method of core drilling waste mud according to embodiment 1, wherein a method for preparing the amidoamine mud solidifying agent comprises the following steps:
[0082] (1) weighing ethylenediamine disuccinic acid, a polycarboxylic acid water reducer and a liquid epoxy resin;
[0083] (2) evenly mixing ethylenediamine disuccinic acid with the liquid epoxy resin, heating to 150-170°C, and then stirring to react for 2-4 h;
[0084] (3) adding the polycarboxylic acid water reducer and heating to 150-170°C, and then stirring to react for 2-4 h; and
[0085] (4) cooling the mixture obtained in step (3) to < 40°C, evenly stirring and then discharging, so as to obtain the amidoamine mud solidifying agent.
[0086] 6. The recycling method of core drilling waste mud according to embodiment 1, wherein a method for alkalizing the artemisia plant comprises: the artemisia plant is smashed into 1-2 mm straws, the straws are mixed and soaked into a 10-20wt% NaOH solution for 10-12 h, the above mixture is evenly stirred every 2 h, and then the treated artemisia plant is obtained after 8-10 h.
[0087] 7. The recycling method of core drilling waste mud according to embodiment 1 or 6, wherein the artemisia plant is preferably artemisia annua.
Claims (7)
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DE2410394A1 (en) * | 1973-03-07 | 1974-09-12 | Andco Inc | PROCESS FOR DRAINING AN AQUATIC SLUDGE OF DISPERSED, FINELY CRUSHED SOLIDS |
DE2802066C2 (en) * | 1978-01-18 | 1986-05-28 | Passavant-Werke AG & Co KG, 6209 Aarbergen | Process for the chemical-mechanical treatment of groundwater, surface or wastewater |
DE10336534A1 (en) * | 2003-08-05 | 2005-02-24 | Stockhausen Gmbh | Process to remove heavy metals from industrial liquid effluent arising from one- or two-stage sulfur dioxide gas washers by admixture of flocculent to sludge |
CN101538096B (en) * | 2009-04-24 | 2011-04-06 | 司军 | Method for processing waste slurry |
WO2010121399A1 (en) * | 2009-04-24 | 2010-10-28 | 北京国油联合油田技术服务有限公司 | Method and device for treating waste mud |
CN101618935A (en) * | 2009-08-12 | 2010-01-06 | 中国铁道科学研究院节能环保劳卫研究所 | Process for treating waste sludge resulted from bridge drilling |
CN101693572A (en) * | 2009-10-28 | 2010-04-14 | 雅化集团绵阳实业有限公司 | Dinitrodiazophenol waste water processing method |
CN101774746B (en) * | 2010-01-29 | 2012-02-01 | 濮阳市天地人环保工程技术有限公司 | Treatment method of waste slurry generated by gigging well and drilling |
CA2787745C (en) * | 2012-08-17 | 2013-10-08 | Kenmore Holdings Inc. | System, apparatus, and methods for disposal of fluid wastes |
CN103409034A (en) * | 2013-06-21 | 2013-11-27 | 天长市润达金属防锈助剂有限公司 | Skid-resistant coating and application thereof |
CN104386861B (en) * | 2014-12-08 | 2016-04-20 | 付炜 | The broken glue nucleation treatment process of rejected well drilling liquid |
CN104671635B (en) * | 2015-01-27 | 2017-03-08 | 上海隧道工程有限公司 | For processing the construction method of bored pile construction discarded slurry |
JP5969099B1 (en) * | 2015-09-07 | 2016-08-10 | 太平洋セメント株式会社 | Treatment method of mud generated by bubble shield method |
CN105625989A (en) * | 2016-02-29 | 2016-06-01 | 德惠同利(北京)石油技术服务有限公司 | Treatment equipment, treatment system and treatment method for enabling drilling fluid not to fall to ground |
CN112876037A (en) * | 2020-12-29 | 2021-06-01 | 青海煤炭地质一0五勘探队 | Special composite waste slurry curing agent for geological drilling and preparation and use methods thereof |
CN215520813U (en) * | 2021-06-30 | 2022-01-14 | 中国人民武装警察部队黄金第二支队 | Core drilling mud waste liquid cyclic utilization system |
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