US3416918A - Process of making dispersion strengthened lead - Google Patents

Process of making dispersion strengthened lead Download PDF

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Publication number
US3416918A
US3416918A US549449A US54944966A US3416918A US 3416918 A US3416918 A US 3416918A US 549449 A US549449 A US 549449A US 54944966 A US54944966 A US 54944966A US 3416918 A US3416918 A US 3416918A
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United States
Prior art keywords
lead
powder
oxide
particles
alumina
Prior art date
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Expired - Lifetime
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US549449A
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English (en)
Inventor
Roberts David Henry
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St Joseph Lead Co
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St Joseph Lead Co
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Publication date
Application filed by St Joseph Lead Co filed Critical St Joseph Lead Co
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Publication of US3416918A publication Critical patent/US3416918A/en
Anticipated expiration legal-status Critical
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Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C32/00Non-ferrous alloys containing at least 5% by weight but less than 50% by weight of oxides, carbides, borides, nitrides, silicides or other metal compounds, e.g. oxynitrides, sulfides, whether added as such or formed in situ
    • C22C32/001Non-ferrous alloys containing at least 5% by weight but less than 50% by weight of oxides, carbides, borides, nitrides, silicides or other metal compounds, e.g. oxynitrides, sulfides, whether added as such or formed in situ with only oxides
    • C22C32/0015Non-ferrous alloys containing at least 5% by weight but less than 50% by weight of oxides, carbides, borides, nitrides, silicides or other metal compounds, e.g. oxynitrides, sulfides, whether added as such or formed in situ with only oxides with only single oxides as main non-metallic constituents
    • C22C32/0042Matrix based on low melting metals, Pb, Sn, In, Zn, Cd or alloys thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/04Making non-ferrous alloys by powder metallurgy
    • C22C1/05Mixtures of metal powder with non-metallic powder
    • C22C1/059Making alloys comprising less than 5% by weight of dispersed reinforcing phases

Definitions

  • ABSTRACT OF THE DISCLOSURE discloses a process for producing dispersion strengthened lead by mixing a small amount of a refractory oxide powder, such as alumina, with lead powder in an oxidizing atmosphere so as to coat the lead particles with lead oxide and thereby inhibit agglomeration thereof, while obtaining a substantially uniform dispersion of the refractory oxide.
  • the mixture may be subjected to chemical reduction of the lead oxide preferentially, while avoiding significant reduction of the refractory oxide and the so reduced powder mixture may be subjected to a forming process to amalgamate the lead particles into a coherent matrix with the refractory oxide dispersed throughout.
  • This invention relates to the production of dispersion strengthened lead and of lead powder from which the same can be made.
  • lead powder having its constituent particles coated with lead oxide is subjected to a forming process which subjects the powder particles to shear deformation so that their oxide coatings become fragmented and dispersed, a coherent dispersion strengthened lead product can be obtained which exhibits considerably increased strength as compared with ordinary lead.
  • a particularly effective forming process is extrusion, carried out at room temperature or at some higher temperature below the melting point of the lead in the powder.
  • the production of dispersion strengthened lead in this manner is relatively simple and economic.
  • the presence of the free lead oxide which is not a refractory material in the generally accepted sense, tends to impart some susceptibility to corrosion, so that in this respect the product may be less good than ordinary lead.
  • the oxide coatings in general have a certain amount of lead carbonate associated with them and this can result in a tendency for the product to swell (due to liberation of carbon dioxide from the carbonate) at elevated temperatures.
  • Dispersion strengthening of various metals by the incorporation of dispersed refractory oxides such as alumina, silica and magnesia is a well known technique and attempts have been made to use it for dispersion strengthening of lead by mixing such refractory oxide with lead powder prior to extrusion or other forming process.
  • these attempts have met with only limited success, in part due to the difficulty of mixing the lead powder and refractory oxide to a satisfactory degree of dispersion while avoiding premature agglomeraiton of the lead particles due to their inherent softness and pliability.
  • a process for the production of dispersion strengthened lead comprises the steps of intimately mixing lead powder and a minor proportion of a refractory oxide powder in an oxidizing,
  • oxygen, atmosphere such as to coat the lead particles with lead oxide and thereby inhibit agglomeration thereof by a pressure welding effect while obtaining a substantially uniform dispersion of the refractory oxide, subjecting the mixture to a reduction process for chemically reducing the majority of the lead oxide preferentially with respect to the refractory oxide by reason of the greater stability of the latter, and subjecting the so reduced powder mixture to a forming process to amalgamate the lead particles into a coherent matrix with the refractory oxide dispersed throughout.
  • the reduction process must be performed below the melting point of lead (so as to retain the powder form) reduction of all the lead oxide and simultaneously of lead carbonate tending to be present with it is not readily practicable.
  • the presence of only a small amount of lead oxide and lead carbonate in the powder mixture when subjected to the forming process and therefore in the final product means that the susceptibility of the final product to corrosion and swelling may be correspondingly small.
  • a refractory oxide powder consisting of particles of submicron size
  • the lead powder particles may in the majority have an average size of about 50 microns or less.
  • a ratio of about *:1 between the average lead particle size and average refractory oxide particle size has been found to give good results but this is not limiting and better results may be obtainable with a different ratio, especially if lead powder of significantly smaller particle size becomes readily obtainable.
  • ballmilling in which the lead particles would be particularly prone to amalgamate if it were not for the presence of the oxidizing atmosphere, the charge of balls in the mill subjects the oxide coated lead particles to severe deformation and in doing so punches the alumina particles into the lead, thus producing a particularly homogeneous mix from which an extruded product with a more uniform refractory oxide distribution is obtained.
  • the mixed powders were all subjected to chemical reduction by hydrogen in order to eliminate the majority of the lead oxide originally present on the lead powder and subsequently produced during the mixing process.
  • extensive lead oxide reduction could be achieved by subjection of oxidised lead powder at about 300 C. to a stream of purified dry hydrogen for 24 hours. Consequently the powder mixtures were given this treatment.
  • the reduced powder mixtures were in each case cooled to room temperature in hydrogen and then rapidly transferred (so as to avoid re-oxidation of the lead) to an extrusion press by which the subsequent forming process was to be performed.
  • a charge of about 100 grams of powder was required to fill the extrusion press.
  • the powder was compacted and extruded in a single direct operation to produce a wire of 0.100 inch diameter.
  • the extrusion ratio was 40:1 and no lubrication was used.
  • the extrusion was performed at a rate of about 11% feet per minute at room temperature, but the temperature of the extrudate was about 60 C. because of the severe deformation involved.
  • Agglomerations of alumina would tend to be broken up by these two processes although any tendency for such agglomerations to form due to build up of electrostatic charges of the alumina particles would be minimised by the presence of the metallic lead. This would assist in dissipating such charges, especially in the case of the ball milling machine with its metal container as compared with the blender with its insulating glass container.
  • Creep tests were conducted on samples of material made from a mixture of lead powder and 1% alumina by weight ball-milled reduced and extruded in accordance with the invention. This particular material had a tensile strength of 5500 lb./in. and elongation of 14%. Some of these creep tests were performed at room temperature (20 C.) and others at 80 C. For comparison, similar tests were performed on samples of pure lead at room temperature. The tests were stress-rupture tests, which consist in applying a fixed stress to a specimen at a fixed temperature and determining the time required under these conditions to bring about fracture of the specimen. The total elongation which had occurred was also measured after fracture. The results are given in the following table, in which a plus sign (-1-) indicates that at the time stated fracture had not occurred and the test was still continuing.
  • the present invention also includes a process for producing as a vendible product in its own right, a lead powder mixture suitable for the manufacture of dispersion strengthened lead by extrusion or other forming process preceded by chemical reduction, which powder production process consists in mixing lead powder and a refractory oxide powder in an oxidising atmosphere preferably in a ball-milling apparatusto produce an intimate mixture of the refractory oxide powder dispersed through the lead powder with the lead particles coated with lead oxide. It is contemplated that powder so prepared, being reasonably stable, may be kept for substantial periods before use for the production of dispersion strengthened lead by chemical reduction and subsequent forming.
  • the invention further contemplates within its scope lead oxide coated lead powder with a minor proportion of refractory oxide powder particles intimately dispersed therein in an amount preferably between 0.1 and 10 vol. percent inclusive, with at least a substantial proportion of the refractory oxide particles embedded in the lead particles, and also dispersion strengthened lead comprising a lead matrix with a substantially uniform dispersion of sub-micron alumina particles as the principal dispersion strengthening agent and a lead oxide content less than 1 wt. percent PbO and preferably less than 0.5 wt. percent, the alumina content being preferably between 0.1 and 10 vol. percent inclusive.
  • the lead may contain antimony in amounts as high as about 0.8%.
  • a process for the production of dispersion strengthened lead comprising the step of intimately mixing lead powder and about 0.1 to 10% by volume of a refractory oxide powder in an oxidizing atmosphere so as to coat the lead particles with lead oxide and thereby inhibit agglomeration thereof by a pressure welding effect while obtaining a substantially uniform dispersion of the refractory oxide, subjecting the mixture to a reduction process for chemically reducing the lead oxide preferentially with respect to the refractory oxide by reason of the greater stability of the refractory oxide, and subjecting the so reduced powder mixture to a forming process to amalgamate the lead particles into a coherent matrix with the refractory oxide dispersed throughout.
  • a process as] claimed in claim 1 wherein the reduction process consists in subjecting the mixed powders to a temperature of about 300 C. in a stream of dry hydrogen for about 24 hours to give a residual lead oxide content of less than 1.0% PbO by weight.
  • a process as claimed in claim 1 wherein the forming process consists in extruding the reduced mixed powders.
  • a process for producing a lead powder mixture suitable for making dispersion strengthened lead by subsequent chemical reduction followed by forming comprising the step of mixing lead powder and about 0.1 to 10% by volume of a refractory oxide powder in an oxidizing atmosphere to produce an intimate mixture of the refractory oxide powder dispersed through the lead powder with the lead powder particles coated with lead oxide.
  • a process as claimed in claim 4 wherein the mixing step consists in ball milling the lead powder and the refractory oxide powder together.
  • a powder mixture for the production of dispersion strengthened lead by chemical reduction and subsequent forming of the powder comprising lead oxide coated lead powder particles with about 0.1 to 10% by volume of refractory oxide powder particles intimately dispersed therein with refractory oxide particles embedded in the lead particles.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Powder Metallurgy (AREA)
  • Compositions Of Oxide Ceramics (AREA)
  • Cosmetics (AREA)
US549449A 1965-05-19 1966-05-12 Process of making dispersion strengthened lead Expired - Lifetime US3416918A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB21225/65A GB1122823A (en) 1965-05-19 1965-05-19 Improvements relating to dispersion strengthened lead

Publications (1)

Publication Number Publication Date
US3416918A true US3416918A (en) 1968-12-17

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US549449A Expired - Lifetime US3416918A (en) 1965-05-19 1966-05-12 Process of making dispersion strengthened lead

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US (1) US3416918A (enExample)
DE (1) DE1533156A1 (enExample)
GB (1) GB1122823A (enExample)
SE (1) SE304865B (enExample)

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3694536A (en) * 1970-02-06 1972-09-26 Dow Chemical Co Method of preparing lead article
US20080069716A1 (en) * 2006-09-14 2008-03-20 The Timken Company Micron size powders having nano size reinforcement
WO2008034043A3 (en) * 2006-09-14 2008-05-22 Iap Res Inc Method of producing uniform blends of nano and micron powders
US9605508B2 (en) 2012-05-08 2017-03-28 Baker Hughes Incorporated Disintegrable and conformable metallic seal, and method of making the same
US9631138B2 (en) 2011-04-28 2017-04-25 Baker Hughes Incorporated Functionally gradient composite article
US9643144B2 (en) 2011-09-02 2017-05-09 Baker Hughes Incorporated Method to generate and disperse nanostructures in a composite material
US9682425B2 (en) 2009-12-08 2017-06-20 Baker Hughes Incorporated Coated metallic powder and method of making the same
US9707739B2 (en) 2011-07-22 2017-07-18 Baker Hughes Incorporated Intermetallic metallic composite, method of manufacture thereof and articles comprising the same
US9802250B2 (en) 2011-08-30 2017-10-31 Baker Hughes Magnesium alloy powder metal compact
US9816339B2 (en) 2013-09-03 2017-11-14 Baker Hughes, A Ge Company, Llc Plug reception assembly and method of reducing restriction in a borehole
US9833838B2 (en) 2011-07-29 2017-12-05 Baker Hughes, A Ge Company, Llc Method of controlling the corrosion rate of alloy particles, alloy particle with controlled corrosion rate, and articles comprising the particle
US9856547B2 (en) 2011-08-30 2018-01-02 Bakers Hughes, A Ge Company, Llc Nanostructured powder metal compact
US9910026B2 (en) 2015-01-21 2018-03-06 Baker Hughes, A Ge Company, Llc High temperature tracers for downhole detection of produced water
US9925589B2 (en) 2011-08-30 2018-03-27 Baker Hughes, A Ge Company, Llc Aluminum alloy powder metal compact
US9926766B2 (en) 2012-01-25 2018-03-27 Baker Hughes, A Ge Company, Llc Seat for a tubular treating system
US9926763B2 (en) 2011-06-17 2018-03-27 Baker Hughes, A Ge Company, Llc Corrodible downhole article and method of removing the article from downhole environment
US10016810B2 (en) 2015-12-14 2018-07-10 Baker Hughes, A Ge Company, Llc Methods of manufacturing degradable tools using a galvanic carrier and tools manufactured thereof
US10092953B2 (en) 2011-07-29 2018-10-09 Baker Hughes, A Ge Company, Llc Method of controlling the corrosion rate of alloy particles, alloy particle with controlled corrosion rate, and articles comprising the particle
US10221637B2 (en) 2015-08-11 2019-03-05 Baker Hughes, A Ge Company, Llc Methods of manufacturing dissolvable tools via liquid-solid state molding
US10240419B2 (en) 2009-12-08 2019-03-26 Baker Hughes, A Ge Company, Llc Downhole flow inhibition tool and method of unplugging a seat
US10301909B2 (en) 2011-08-17 2019-05-28 Baker Hughes, A Ge Company, Llc Selectively degradable passage restriction
US10335858B2 (en) 2011-04-28 2019-07-02 Baker Hughes, A Ge Company, Llc Method of making and using a functionally gradient composite tool
US10378303B2 (en) 2015-03-05 2019-08-13 Baker Hughes, A Ge Company, Llc Downhole tool and method of forming the same
US11167343B2 (en) 2014-02-21 2021-11-09 Terves, Llc Galvanically-active in situ formed particles for controlled rate dissolving tools
US11365164B2 (en) 2014-02-21 2022-06-21 Terves, Llc Fluid activated disintegrating metal system
US11649526B2 (en) 2017-07-27 2023-05-16 Terves, Llc Degradable metal matrix composite
US12018356B2 (en) 2014-04-18 2024-06-25 Terves Inc. Galvanically-active in situ formed particles for controlled rate dissolving tools

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2424084C1 (ru) * 2010-05-05 2011-07-20 Федеральное государственное унитарное предприятие "Научно-исследовательский машиностроительный институт" (ФГУП "НИМИ") Способ диспергирования металла на частицы, лишенные оксидной пленки

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US846384A (en) * 1902-06-26 1907-03-05 United Lead Company Lead product.
US2985571A (en) * 1956-11-09 1961-05-23 North American Aviation Inc Lead-uranium oxide nuclear fuel element
US3044867A (en) * 1957-05-15 1962-07-17 Messrs Aktiebolaget Svenska Me Method for the production of metallicceramic materials
US3085876A (en) * 1960-03-01 1963-04-16 Du Pont Process for dispersing a refractory metal oxide in another metal
US3158473A (en) * 1962-08-27 1964-11-24 Gen Electric Method for producing composite bodies
US3297415A (en) * 1963-03-22 1967-01-10 Nat Res Corp Dispersion strengthened ultra-fine wires
US3315342A (en) * 1962-05-21 1967-04-25 St Joseph Lead Co Dispersion strengthening of lead
US3320664A (en) * 1962-04-26 1967-05-23 St Joseph Lead Co Process for the production of dispersion strengthened lead

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US846384A (en) * 1902-06-26 1907-03-05 United Lead Company Lead product.
US2985571A (en) * 1956-11-09 1961-05-23 North American Aviation Inc Lead-uranium oxide nuclear fuel element
US3044867A (en) * 1957-05-15 1962-07-17 Messrs Aktiebolaget Svenska Me Method for the production of metallicceramic materials
US3085876A (en) * 1960-03-01 1963-04-16 Du Pont Process for dispersing a refractory metal oxide in another metal
US3320664A (en) * 1962-04-26 1967-05-23 St Joseph Lead Co Process for the production of dispersion strengthened lead
US3315342A (en) * 1962-05-21 1967-04-25 St Joseph Lead Co Dispersion strengthening of lead
US3158473A (en) * 1962-08-27 1964-11-24 Gen Electric Method for producing composite bodies
US3297415A (en) * 1963-03-22 1967-01-10 Nat Res Corp Dispersion strengthened ultra-fine wires

Cited By (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3694536A (en) * 1970-02-06 1972-09-26 Dow Chemical Co Method of preparing lead article
US8889065B2 (en) 2006-09-14 2014-11-18 Iap Research, Inc. Micron size powders having nano size reinforcement
WO2008034043A3 (en) * 2006-09-14 2008-05-22 Iap Res Inc Method of producing uniform blends of nano and micron powders
WO2008034042A3 (en) * 2006-09-14 2008-05-22 Iap Res Inc Micron size powders having nano size reinforcement
US20100124514A1 (en) * 2006-09-14 2010-05-20 The Timken Company Method of producing uniform blends of nano and micron powders
US7758784B2 (en) * 2006-09-14 2010-07-20 Iap Research, Inc. Method of producing uniform blends of nano and micron powders
US20080069716A1 (en) * 2006-09-14 2008-03-20 The Timken Company Micron size powders having nano size reinforcement
US10240419B2 (en) 2009-12-08 2019-03-26 Baker Hughes, A Ge Company, Llc Downhole flow inhibition tool and method of unplugging a seat
US9682425B2 (en) 2009-12-08 2017-06-20 Baker Hughes Incorporated Coated metallic powder and method of making the same
US10669797B2 (en) 2009-12-08 2020-06-02 Baker Hughes, A Ge Company, Llc Tool configured to dissolve in a selected subsurface environment
US10335858B2 (en) 2011-04-28 2019-07-02 Baker Hughes, A Ge Company, Llc Method of making and using a functionally gradient composite tool
US9631138B2 (en) 2011-04-28 2017-04-25 Baker Hughes Incorporated Functionally gradient composite article
US9926763B2 (en) 2011-06-17 2018-03-27 Baker Hughes, A Ge Company, Llc Corrodible downhole article and method of removing the article from downhole environment
US10697266B2 (en) 2011-07-22 2020-06-30 Baker Hughes, A Ge Company, Llc Intermetallic metallic composite, method of manufacture thereof and articles comprising the same
US9707739B2 (en) 2011-07-22 2017-07-18 Baker Hughes Incorporated Intermetallic metallic composite, method of manufacture thereof and articles comprising the same
US9833838B2 (en) 2011-07-29 2017-12-05 Baker Hughes, A Ge Company, Llc Method of controlling the corrosion rate of alloy particles, alloy particle with controlled corrosion rate, and articles comprising the particle
US10092953B2 (en) 2011-07-29 2018-10-09 Baker Hughes, A Ge Company, Llc Method of controlling the corrosion rate of alloy particles, alloy particle with controlled corrosion rate, and articles comprising the particle
US10301909B2 (en) 2011-08-17 2019-05-28 Baker Hughes, A Ge Company, Llc Selectively degradable passage restriction
US9925589B2 (en) 2011-08-30 2018-03-27 Baker Hughes, A Ge Company, Llc Aluminum alloy powder metal compact
US9856547B2 (en) 2011-08-30 2018-01-02 Bakers Hughes, A Ge Company, Llc Nanostructured powder metal compact
US9802250B2 (en) 2011-08-30 2017-10-31 Baker Hughes Magnesium alloy powder metal compact
US10737321B2 (en) 2011-08-30 2020-08-11 Baker Hughes, A Ge Company, Llc Magnesium alloy powder metal compact
US11090719B2 (en) 2011-08-30 2021-08-17 Baker Hughes, A Ge Company, Llc Aluminum alloy powder metal compact
US9643144B2 (en) 2011-09-02 2017-05-09 Baker Hughes Incorporated Method to generate and disperse nanostructures in a composite material
US9926766B2 (en) 2012-01-25 2018-03-27 Baker Hughes, A Ge Company, Llc Seat for a tubular treating system
US9605508B2 (en) 2012-05-08 2017-03-28 Baker Hughes Incorporated Disintegrable and conformable metallic seal, and method of making the same
US10612659B2 (en) 2012-05-08 2020-04-07 Baker Hughes Oilfield Operations, Llc Disintegrable and conformable metallic seal, and method of making the same
US9816339B2 (en) 2013-09-03 2017-11-14 Baker Hughes, A Ge Company, Llc Plug reception assembly and method of reducing restriction in a borehole
US11613952B2 (en) 2014-02-21 2023-03-28 Terves, Llc Fluid activated disintegrating metal system
US11167343B2 (en) 2014-02-21 2021-11-09 Terves, Llc Galvanically-active in situ formed particles for controlled rate dissolving tools
US11365164B2 (en) 2014-02-21 2022-06-21 Terves, Llc Fluid activated disintegrating metal system
US12031400B2 (en) 2014-02-21 2024-07-09 Terves, Llc Fluid activated disintegrating metal system
US12018356B2 (en) 2014-04-18 2024-06-25 Terves Inc. Galvanically-active in situ formed particles for controlled rate dissolving tools
US9910026B2 (en) 2015-01-21 2018-03-06 Baker Hughes, A Ge Company, Llc High temperature tracers for downhole detection of produced water
US10378303B2 (en) 2015-03-05 2019-08-13 Baker Hughes, A Ge Company, Llc Downhole tool and method of forming the same
US10221637B2 (en) 2015-08-11 2019-03-05 Baker Hughes, A Ge Company, Llc Methods of manufacturing dissolvable tools via liquid-solid state molding
US10016810B2 (en) 2015-12-14 2018-07-10 Baker Hughes, A Ge Company, Llc Methods of manufacturing degradable tools using a galvanic carrier and tools manufactured thereof
US11649526B2 (en) 2017-07-27 2023-05-16 Terves, Llc Degradable metal matrix composite
US11898223B2 (en) 2017-07-27 2024-02-13 Terves, Llc Degradable metal matrix composite

Also Published As

Publication number Publication date
DE1533156A1 (de) 1970-01-02
SE304865B (enExample) 1968-10-07
GB1122823A (en) 1968-08-07

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