CN107353373A - A kind of preparation method of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive - Google Patents

A kind of preparation method of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive Download PDF

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CN107353373A
CN107353373A CN201710714840.8A CN201710714840A CN107353373A CN 107353373 A CN107353373 A CN 107353373A CN 201710714840 A CN201710714840 A CN 201710714840A CN 107353373 A CN107353373 A CN 107353373A
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parts
fluid loss
loss additive
graft polymers
drilling fluid
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CN107353373B (en
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鲍荣
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Civil Rights Dongxing Mud Material Co., Ltd.
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Xinyi Chino New Mstar Technology Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F289/00Macromolecular compounds obtained by polymerising monomers on to macromolecular compounds not provided for in groups C08F251/00 - C08F287/00
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02Well-drilling compositions
    • C09K8/03Specific additives for general use in well-drilling compositions
    • C09K8/035Organic additives

Abstract

A kind of preparation method the invention discloses drilling fluid with sulfomethylated humic acid potassium graft polymers fluid loss additive, with potassium humate, acrylamide, alkyl acrylic, the methyl propane sulfonic acid of 2 acrylamido 2, N vinyl pyrrolidones etc. are raw material, and heat resisting fluid loss reducing agent is prepared by aqueous solution polymerization method, and its synthesis optimum condition is:30 ~ 50 parts of potassium humate, 15 ~ 25 parts of acrylamide, 5 ~ 15 parts of alkyl acrylic, 10 ~ 20 parts of 2 acrylamido, 2 methyl propane sulfonic acid, 5 ~ 15 parts of N vinyl pyrrolidones.The present invention triggers monomer that polymerisation occurs by redox initiator, obtain a kind of macromolecular graft polymers fluid loss additive, the product has good filtrate loss controllability in fresh water, saturated brine and compound salt-water drilling fluid, is resistant to 200 DEG C of high temperature, easy to use.

Description

A kind of preparation of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive Method
Technical field
The present invention relates to filtrate reducer for drilling fluid preparation field, more particularly to a kind of drilling fluid is connect with sulfomethylated humic acid potassium The preparation method of branch polymer filtrate reducer.
Background technology
The loss of drilling fluid is not only resulted in when drilling fluid filtration is excessive, can also cause borehole well instability, cave-in, dirt Contaminate the various problems such as reservoir.Fluid loss additive is one of maximum material of drillng operation dosage, and appropriate drop is added in drilling fluid Fluid loss agents can reach good filtrate reducing effect.Once heat resisting fluid loss reducing agent is degraded in drilling fluid, drilling fluid resists Warm nature, which declines to a great extent, to cause drilling fluid rheology to be deteriorated, drilling fluid flocculation and delamination, or even the pernicious leak-off of appearance, mud cake are thickening The problems such as, cause the various accidents such as bit freezing, burying, well slough.Domestic conventional sulfonated phenol formaldehyde resin class fluid loss additive and sulphur at present It is good to change walchowite filtration reduction effect, is resistant to 180 DEG C of high temperature, but dosage is larger, and it is glutinous in the presence of having in salt solution when in use Degree loss, the defects of easily pollution by high valence ion, seriously limits its application.
In addition with the increasing of oil extraction, many oil fields all enter high temperature deep layer oil-producing region, and exploitation difficulty is increasingly Greatly, partial mining area requirement fluid loss additive is resistant to 200 DEG C of high temperature above.Temperature-resistant and anti-salt type polymerize species fluid loss additive in oil field There is very big application potential in exploitation, the present invention develop one kind can high temperature resistance, the fluid loss additive of and can salt resistance, can solve Certainly drilling fluid filtration problems of too during deep reservoir oil-gas mining, new breakthrough is provided for the exploitation of high temperature Deep Oil And Gas Exploration Mouthful.
The content of the invention
A kind of system it is an object of the invention to provide drilling fluid with sulfomethylated humic acid potassium graft polymers fluid loss additive Preparation Method, the fluid loss additive have good filtrate loss controllability in fresh water, saturated brine and compound salt-water drilling fluid, are resistant to 200 DEG C of high temperature, it is easy to use.
A kind of preparation method of drilling fluid heat resisting fluid loss reducing agent, it is characterised in that this method comprises the following steps:
1)60 ~ 100 parts of deionized waters are added in the reactor equipped with 30 ~ 50 parts of potassium humates, after dissolving is stirred at room temperature, use alkali Property reagent regulation pH to 10 ~ 11, then add 6 ~ 10 parts by weight of formaldehyde, 6 ~ 10 parts by weight sulfonating agent sodium hydrogensulfites, stirring rise Temperature cools to 70 ~ 75 DEG C after reacting 3 ~ 4h;
2)By 15 ~ 25 parts of acrylamides, 5 ~ 15 parts of alkyl acrylics, 10 ~ 20 parts of 2- acrylamide-2-methylpro panesulfonic acids, 5 ~ 15 parts of NVPs add step 1 after being dissolved in 70 ~ 150 parts of deionized waters)Middle reactor, 0.5h is stirred, simultaneously Add 0.13 ~ 0.25 part and trigger auxiliary agent lactic acid-chromium base bentonite clay material, heating, by 0.27 ~ 0.5 initiator(Sodium peroxydisulfate, Sodium hydrogensulfite)Wiring solution-forming, slowly it is alternately added in reactor, time for adding 0.5h, in 55 ~ 60 DEG C of guarantors after being added dropwise Warm 4h, discharging, cooling obtain sulfomethylated humic acid potassium graft polymers fluid loss additive.
Beneficial effect:The present invention provides a kind of preparation of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive Method, the fluid loss additive saline-alkaline tolerance is strong, and raw material relatively easily obtains, and process, which adds, in preparation process triggers auxiliary agent breast Acid-chromium base bentonite clay material, it is a kind of high-efficiency activated material, has surprising catalytic performance, is advantageous to synthetic sample mistake The polymerization of monomer in journey, by molecular chain length control within the required range.With acrylamide, alkyl acrylic, 2- acrylamides Base -2- methyl propane sulfonic acids, the product that NVP is principal monomer synthesis, heat and salinity tolerance ability protrude, and its Drilling fluid filtration can be greatly lowered in the dosage of low concentration in drilling fluid.
Embodiment
Embodiment 1
100 parts of deionized waters are added in the reactor equipped with 50 parts of potassium humates, after dissolving is stirred at room temperature, are adjusted with alkaline reagent PH to 10 ~ 11 is saved, then adds 10 parts by weight of formaldehyde, 10 parts by weight sulfonating agent sodium hydrogensulfites, stirring is warming up to 70 ~ 75 DEG C, Cool after 3 ~ 4h of reaction,
By 25 parts of acrylamides, 5 parts of alkyl acrylics, 10 parts of 2- acrylamide-2-methylpro panesulfonic acids, 10 parts of N- vinylpyridines Pyrrolidone adds step 1 after being dissolved in 100 parts of deionized waters)Middle reactor, 0.5h is stirred, while add 0.2 part of initiation auxiliary agent Lactic acid-chromium base bentonite clay material, heating, by 0.4 part of initiator(Sodium peroxydisulfate, sodium hydrogensulfite, n sodium peroxydisulfates:N sulfurous Sour sodium=1.3:1)Wiring solution-forming, slowly it is alternately added in reactor, time for adding 0.5h, in 55 ~ 60 DEG C of guarantors after being added dropwise Warm 4h, discharging, cooling obtain sulfomethylated humic acid potassium graft polymers fluid loss additive.
Above-mentioned lactic acid-chromium base bentonite clay material preparation method is as follows:
Step 1,7.08 parts of chromic nitrates, 18.91 parts of zinc nitrates, 7.35 parts of aluminum nitrates and 5.68 parts of ferric nitrates are dissolved in 100 parts of water In obtain mixing salt solution;5.35 parts of sodium hydroxides and 2.84 parts of sodium carbonate are dissolved in 50 parts, are configured to mixed ammonium/alkali solutions, will Mixed ammonium/alkali solutions are slowly dropped in the mixing salt solution being stirred vigorously, and stop that mixing alkali soluble is added dropwise after salt-mixture precipitates completely Liquid, bottom sediment is taken to stir washing filtering after crystallization 24h, drying for standby at 70 DEG C;
Step 2, excessive hydrochloric acid is evaporated after fully reacting 36 parts of neodymia and 4 parts of mixed in hydrochloric acid, add excessive water, add ammonia Water precipitates completely to rare earth, filtering, is washed to no chlorion, obtains neodymium hydroxide, neodymium hydroxide is mixed with excessive water, obtained Suspension, it is heated to adding lactic acid aqueous solution insulation reaction 5h after 60 DEG C while stirring, evaporation excessive water precipitation product, which is crossed, to be filtered dry It is dry to obtain lactic acid neodymium compound, 50 parts of sodium bentonites are added after lactic acid neodymium compound is mixed with product in step 1 and are pinched Conjunction obtains lactic acid-chromium base bentonite clay material.Embodiment 2
Identical with embodiment 1, difference is:Add 30 parts of potassium humate, 60 parts of deionized water, 6 parts of formaldehyde, bisulfite 6 parts of sodium;Add 15 parts of acrylamide, 10 parts of alkyl acrylic, 15 parts of 2- acrylamide-2-methylpro panesulfonic acids, N- vinyl 15 parts of pyrrolidones is dissolved in 110 parts of deionized waters, adds 0.17 part and triggers auxiliary agent lactic acid-chromium base bentonite clay material, 0.34 part Initiator.
Embodiment 3
Identical with embodiment 1, difference is:Add 30 parts of potassium humate, 60 parts of deionized water, 6 parts of formaldehyde, bisulfite 6 parts of sodium;Add 15 parts of acrylamide, 15 parts of alkyl acrylic, 15 parts of 2- acrylamide-2-methylpro panesulfonic acids, N- vinyl 5 parts of pyrrolidones is dissolved in 100 parts of deionized waters, adds 0.16 part and triggers auxiliary agent lactic acid-chromium base bentonite clay material, 0.32 part is drawn Send out agent.
Embodiment 4
Identical with embodiment 1, difference is:Add 35 parts of potassium humate, 70 parts of deionized water, 7 parts of formaldehyde, bisulfite 7 parts of sodium;Add 15 parts of acrylamide, 5 parts of alkyl acrylic, 20 parts of 2- acrylamide-2-methylpro panesulfonic acids, N- vinylpyridines 10 parts of pyrrolidone is dissolved in 100 parts of deionized waters, adds 0.17 part and triggers auxiliary agent lactic acid-chromium base bentonite clay material, 0.34 part is drawn Send out agent.
Embodiment 5
Identical with embodiment 1, difference is:Add 40 parts of potassium humate, 80 parts of deionized water, 8 parts of formaldehyde, bisulfite 8 parts of sodium;Add 20 parts of acrylamide, 5 parts of alkyl acrylic, 15 parts of 2- acrylamide-2-methylpro panesulfonic acids, N- vinylpyridines 10 parts of pyrrolidone is dissolved in 100 parts of deionized waters, adds 0.18 part and triggers auxiliary agent lactic acid-chromium base bentonite clay material, 0.36 part is drawn Send out agent.
Embodiment 6
Identical with embodiment 1, difference is:Add 40 parts of potassium humate, 80 parts of deionized water, 8 parts of formaldehyde, bisulfite 8 parts of sodium;Add 20 parts of acrylamide, 10 parts of alkyl acrylic, 15 parts of 2- acrylamide-2-methylpro panesulfonic acids, N- vinyl 5 parts of pyrrolidones is dissolved in 100 parts of deionized waters, adds 0.18 part and triggers auxiliary agent lactic acid-chromium base bentonite clay material, 0.36 part is drawn Send out agent.
Embodiment 7
Identical with embodiment 1, difference is:Add 45 parts of potassium humate, 90 parts of deionized water, 9 parts of formaldehyde, bisulfite 9 parts of sodium;Add 20 parts of acrylamide, 5 parts of alkyl acrylic, 15 parts of 2- acrylamide-2-methylpro panesulfonic acids, N- vinylpyridines 15 parts of pyrrolidone is dissolved in 110 parts of deionized waters, adds 0.2 part and triggers auxiliary agent lactic acid-chromium base bentonite clay material, 0.4 part of initiation Agent.
Embodiment 8
Identical with embodiment 1, difference is:Add 50 parts of potassium humate, 100 parts of deionized water, 10 parts of formaldehyde, sulfurous acid 10 parts of hydrogen sodium;Add 25 parts of acrylamide, 5 parts of alkyl acrylic, 15 parts of 2- acrylamide-2-methylpro panesulfonic acids, N- ethene 5 parts of base pyrrolidones is dissolved in 100 parts of deionized waters, adds 0.2 part and triggers auxiliary agent lactic acid-chromium base bentonite clay material, 0.4 part is drawn Send out agent.
Embodiment 9
Identical with embodiment 1, difference is:Add 45 parts of potassium humate, 90 parts of deionized water, 9 parts of formaldehyde, bisulfite 9 parts of sodium;Add 25 parts of acrylamide, 5 parts of alkyl acrylic, 15 parts of 2- acrylamide-2-methylpro panesulfonic acids, N- vinylpyridines 15 parts of pyrrolidone is dissolved in 120 parts of deionized waters, adds 0.21 part and triggers auxiliary agent lactic acid-chromium base bentonite clay material, 0.42 part is drawn Send out agent.
Comparative example 1
Identical with embodiment 1, difference is, is simply added without and triggers auxiliary agent lactic acid-chromium base bentonite clay material.
Comparative example 2
Identical with embodiment 1, difference is, the initiation auxiliary agent simply added be not lactic acid-chromium base bentonite clay material and It is conventional sodium bentonite.
Comparative example 3
Identical with embodiment 1, difference is:Simply prepare and be added without chromic nitrate when triggering auxiliary agent.
Comparative example 4
Identical with embodiment 1, difference is:Simply prepare and 8.05 parts of chromic nitrates, 9.82 parts of nitric acid are added when triggering auxiliary agent Zinc, 8.75 parts of aluminum nitrates and 4.04 parts of ferric nitrates.
Comparative example 5
2- acrylamide-2-methylpro panesulfonic acids are replaced with into p-methyl benzenesulfonic acid, remaining is identical with embodiment 1.
Comparative example 6
With embodiment 6, simply it is added without and triggers auxiliary agent lactic acid-chromium base bentonite clay material.
Comparative example 7
Identical with the process of embodiment 1, difference is, is added without potassium humate.
Comparative example 8
Identical with the process of embodiment 1, difference is, is added without alkaline reagent, and its pH is 7.
The drilling fluid prepared below to the present embodiment is carried out with sulfomethylated humic acid potassium graft polymers fluid loss additive Performance evaluation, comprise the following steps that:
1st, fluid loss additive filtrate loss controllability evaluation result
Base slurry is prepared:About 10L running water is measured with graduated cylinder, and is heated to 60 DEG C, soil paste bentonite is removed into preparation 400g is slowly added into hot water, is stirred when adding native, the fully dispersed uniformly rear addition 20gNa of bentonite2CO3After stirring 30min It is standby to conserve 24h.
Experiment slurry is prepared and test:Blank sample is used as using base slurry, be separately added into base is starched embodiment 1 ~ 9 and comparative example 1 ~ Addition fluid loss additive class sample is the 2% of base slurry weight during fluid loss additive sample is starched as test specimens, base in 6.
Filter loss is tested:Base is starched and tested to starch and determines API filtration, HTHP leak-off after heat rolling 16h at 200 DEG C Amount(HTHP fluid loss measurement temperature is its heat rolling temperature), test data is shown in Table 1.
Table 1 is filtration reduction evaluation result
As shown in Table 1, base slurry filter loss after 2% embodiment sample heat at 200 DEG C rolls 16h is added in base slurry to be had to some extent Reduce, the API filtration of base slurry is generally down to 10.6 ~ 17.8ml from 25.5ml, and high temperature and high pre ssure filtration is down to from 73.0ml 20.3~28.4ml.Its excellent performance of synthesized fluid loss additive in particular embodiment 1, API filtration is down to 4.2ml, high temperature is high Filter pressing loss is down to 10.5ml, it is seen that raw material produces with the performance for comparing sulfomethylated humic acid potassium graft polymers fluid loss additive Tremendous influence, when raw material proportioning reaches best of breed in embodiment 1, filtrate reducing effect reaches best.Other comparative example 1 ~ 5 is said The bentonitic addition of the bright initiation auxiliary agent lactic acid-chromium baseization and formula it is larger with fluid loss additive performance impact is compared.
Comparative example 7-8 illustrates that potassium humate and raw material ph regulation are also very big for product overall performance influence.
2nd, fluid loss additive temperature resistance evaluation result
Testing sample is prepared and test:Take 400ml clear water, add in embodiment 1 sample prepared, 200 DEG C, 220 DEG C, 240 Its rheological parameter is surveyed after heat rolling 16h at DEG C, it is the 2% of clear water weight to add fluid loss additive class sample.
Table 2 is heat rolling temperature to fluid loss additive aqueous solution rheology impact
As can be seen from Table 2, as heat rolls the rise of temperature, the solution viscosity of fluid loss additive declines with shear force.At 240 DEG C After lower heat rolling, the AV and PV of the fluid loss additive aqueous solution decline by a big margin, but fluid loss additive is not degradable, and its aqueous solution is still With certain viscosity, illustrate that the fluid loss additive temperature resistance is excellent, still there is certain temperature resistance at 240 DEG C.
3rd, fluid loss additive Assessment on Salt
Testing sample is prepared and test:Take 400ml drilling wells liquid-based to starch, add in 2% embodiment 1 the fluid loss additive sample prepared, it is high After speed stirring is thoroughly dispersed in drilling fluid to fluid loss additive, a certain amount of salt is added, tests drilling fluid rheology and filter loss, The salt of addition is the mass percent of drilling well liquid-based slurry.Test is reclaimed drilling fluid heat rolling 16h, test at 200 DEG C and bored after terminating Rheological characteristic, API filtration and the high temperature and high pre ssure filtration of well liquid.
Table 3 is fluid loss additive salt-resistance(NaCl)Evaluation
Table 4 is fluid loss additive salt-resistance(CaCl2)Evaluation
From table 3, table 4, the 20%NaCl drilling wells liquid-based slurry API filtration for adding fluid loss additive in the present invention is only 6.8ml, High temperature and high pre ssure filtration is 36.3ml, and add the present invention in fluid loss additive 1%CaCl2Drilling well liquid-based slurry API filtration is only For 7.2ml, high temperature and high pre ssure filtration 35.6ml, illustrate that fluid loss additive has good salt-resistance in the present invention, be a kind of preferable Salt resistance fluid loss additive.

Claims (9)

  1. A kind of 1. drilling fluid preparation method of sulfomethylated humic acid potassium graft polymers fluid loss additive, it is characterised in that this method Comprise the following steps:
    1)60 ~ 100 parts of deionized waters are added in the reactor equipped with 30 ~ 50 parts of potassium humates, after dissolving is stirred at room temperature, use alkali Property reagent regulation pH to 10 ~ 11, then add 6 ~ 10 parts by weight of formaldehyde, 6 ~ 10 parts by weight sulfonating agent sodium hydrogensulfites, stirring rise Temperature cools to 70 ~ 75 DEG C after reacting 3 ~ 4h;
    2)By 15 ~ 25 parts of acrylamides, 5 ~ 15 parts of alkyl acrylics, 10 ~ 20 parts of 2- acrylamide-2-methylpro panesulfonic acids, 5 ~ 15 parts of NVPs add step 1 after being dissolved in 70 ~ 150 parts of deionized waters)Middle reactor, 0.5h is stirred, simultaneously Add 0.13 ~ 0.25 part and trigger auxiliary agent lactic acid-chromium base bentonite clay material, heating, by 0.27 ~ 0.5 part of initiator(Persulfuric acid Sodium, sodium hydrogensulfite)Wiring solution-forming, slowly it is alternately added in reactor, time for adding 0.5h, 55 ~ 60 after being added dropwise DEG C insulation 4h, discharging, cooling obtain sulfomethylated humic acid potassium graft polymers fluid loss additive.
  2. A kind of 2. preparation side of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive according to claim 1 Method, it is characterised in that step 1)Neutral and alkali reagent is the one or more in sodium hydroxide, potassium hydroxide.
  3. A kind of 3. preparation side of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive according to claim 1 Method, it is characterised in that step 1)Middle potassium humate, formaldehyde, sodium hydrogensulfite, the mass ratio of deionized water are 5:1:1:2.
  4. A kind of 4. preparation side of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive according to claim 1 Method, it is characterised in that step 1)To step 2)Middle potassium humate, acrylamide, alkyl acrylic, 2- acrylamido -2- methyl Propane sulfonic acid, NVP mass ratio are 6:3:2:3:3~10:5:1:3:1.
  5. A kind of 5. preparation side of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive according to claim 1 Method, it is characterised in that step 2)Middle oxidation/reduction ratio of initiator n sodium peroxydisulfates:N sodium sulfite=1.3:1.
  6. A kind of 6. preparation side of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive according to claim 1 Method, it is characterised in that step 1)Middle mixing speed is 100 ~ 150r/min, step 2)Middle mixing speed is 300 ~ 400r/min.
  7. A kind of 7. preparation side of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive according to claim 1 Method, it is characterised in that step 1)To step 2)In reactor be ceramic electric heating reactor.
  8. A kind of 8. preparation side of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive according to claim 1 Method, it is characterised in that the polymer filtrate reducer is molecular weight 90 ~ 1,400,000 again.
  9. A kind of 9. preparation side of drilling fluid sulfomethylated humic acid potassium graft polymers fluid loss additive according to claim 1 Method, it is characterised in that the lactic acid-chromium base bentonite clay material preparation method is as follows:
    Step 1,7.08 parts of chromic nitrates, 18.91 parts of zinc nitrates, 7.35 parts of aluminum nitrates and 5.68 parts of ferric nitrates are dissolved in 100 parts of water In obtain mixing salt solution, 5.35 parts of sodium hydroxides and 2.84 parts of sodium carbonate are dissolved in 50 parts, are configured to mixed ammonium/alkali solutions, Mixed ammonium/alkali solutions are slowly dropped in the mixing salt solution being stirred vigorously, stop that mixed base is added dropwise after salt-mixture precipitates completely Solution, bottom sediment is taken to stir washing filtering after crystallization 24h, drying for standby at 70 DEG C;
    Step 2, excessive hydrochloric acid is evaporated after fully reacting 36 parts of neodymia and 4 parts of mixed in hydrochloric acid, add excessive water, add ammonia Water precipitates completely to rare earth, filtering, is washed to no chlorion, obtains neodymium hydroxide, neodymium hydroxide is mixed with excessive water, obtained Suspension, it is heated to adding lactic acid aqueous solution insulation reaction 5h after 60 DEG C while stirring, evaporation excessive water precipitation product, which is crossed, to be filtered dry It is dry to obtain lactic acid neodymium compound, 50 parts of sodium bentonites are added after lactic acid neodymium compound is mixed with product in step 1 and are pinched Conjunction obtains lactic acid-chromium base bentonite clay material.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108822812A (en) * 2018-07-25 2018-11-16 佛山陵朝新材料有限公司 A kind of preparation method of salt tolerant high heat stability fluid loss additive
CN110564381A (en) * 2019-09-28 2019-12-13 重庆威能钻井助剂有限公司 Composite filtrate reducer for drilling fluid and preparation method thereof
CN110591667A (en) * 2019-09-29 2019-12-20 重庆威能钻井助剂有限公司 High-temperature-resistant fluid loss additive for drilling fluid and preparation method thereof
CN111139042A (en) * 2018-11-02 2020-05-12 中国石油化工股份有限公司 Resin modified polymer fluid loss agent based on degradation and preparation method thereof
CN111139039A (en) * 2018-11-02 2020-05-12 中国石油化工股份有限公司 Sulfonated phenolic resin graft modified polymer filtrate reducer and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101851491A (en) * 2009-10-20 2010-10-06 新疆德蓝股份有限公司 Method for preparing fluid loss additive for drilling fluid
CN106318347A (en) * 2015-06-15 2017-01-11 中石化石油工程技术服务有限公司 Silicate-aluminate anti-sloughing drilling fluid
CN106336467A (en) * 2016-08-25 2017-01-18 中国石油大学(北京) Modified chitosan, preparation method thereof, application of chitosan as shale inhibitor, drilling fluid and application thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101851491A (en) * 2009-10-20 2010-10-06 新疆德蓝股份有限公司 Method for preparing fluid loss additive for drilling fluid
CN106318347A (en) * 2015-06-15 2017-01-11 中石化石油工程技术服务有限公司 Silicate-aluminate anti-sloughing drilling fluid
CN106336467A (en) * 2016-08-25 2017-01-18 中国石油大学(北京) Modified chitosan, preparation method thereof, application of chitosan as shale inhibitor, drilling fluid and application thereof

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108822812A (en) * 2018-07-25 2018-11-16 佛山陵朝新材料有限公司 A kind of preparation method of salt tolerant high heat stability fluid loss additive
CN111139042A (en) * 2018-11-02 2020-05-12 中国石油化工股份有限公司 Resin modified polymer fluid loss agent based on degradation and preparation method thereof
CN111139039A (en) * 2018-11-02 2020-05-12 中国石油化工股份有限公司 Sulfonated phenolic resin graft modified polymer filtrate reducer and preparation method thereof
CN111139039B (en) * 2018-11-02 2022-06-10 中国石油化工股份有限公司 Sulfonated phenolic resin graft modified polymer filtrate reducer and preparation method thereof
CN111139042B (en) * 2018-11-02 2022-06-10 中国石油化工股份有限公司 Resin modified polymer fluid loss agent based on degradation and preparation method thereof
CN110564381A (en) * 2019-09-28 2019-12-13 重庆威能钻井助剂有限公司 Composite filtrate reducer for drilling fluid and preparation method thereof
CN110564381B (en) * 2019-09-28 2021-07-20 重庆威能钻井助剂有限公司 Composite filtrate reducer for drilling fluid and preparation method thereof
CN110591667A (en) * 2019-09-29 2019-12-20 重庆威能钻井助剂有限公司 High-temperature-resistant fluid loss additive for drilling fluid and preparation method thereof
CN110591667B (en) * 2019-09-29 2021-07-20 重庆威能钻井助剂有限公司 High-temperature-resistant fluid loss additive for drilling fluid and preparation method thereof

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