GB2112414A - Palladium-based alloy - Google Patents

Palladium-based alloy Download PDF

Info

Publication number
GB2112414A
GB2112414A GB08138677A GB8138677A GB2112414A GB 2112414 A GB2112414 A GB 2112414A GB 08138677 A GB08138677 A GB 08138677A GB 8138677 A GB8138677 A GB 8138677A GB 2112414 A GB2112414 A GB 2112414A
Authority
GB
United Kingdom
Prior art keywords
palladium
alloys
hydrogen
ruthenium
alloy
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
GB08138677A
Other versions
GB2112414B (en
Inventor
Natalia Robertovna Roshan
Natalia Ignatievna Parfenova
Viktoria Petrovna Polyakova
Evgeny Mikhailovich Savitsky
Alexandr Petrovich Mischenko
Vladimir Mikhailovich Gryaznov
Maria Evgrafovna Sarylova
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Institut Metallurgii Imeni A A Baikova Akademii Nauk Sssr
METALLURG IM A A BAIKOVA AKADE
NEFTEKHIMICHESKOGO SINTEZA IM
AV Topchiev Institute of Petrochemical Synthesis
Original Assignee
Institut Metallurgii Imeni A A Baikova Akademii Nauk Sssr
METALLURG IM A A BAIKOVA AKADE
NEFTEKHIMICHESKOGO SINTEZA IM
AV Topchiev Institute of Petrochemical Synthesis
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Institut Metallurgii Imeni A A Baikova Akademii Nauk Sssr, METALLURG IM A A BAIKOVA AKADE, NEFTEKHIMICHESKOGO SINTEZA IM, AV Topchiev Institute of Petrochemical Synthesis filed Critical Institut Metallurgii Imeni A A Baikova Akademii Nauk Sssr
Priority to GB08138677A priority Critical patent/GB2112414B/en
Publication of GB2112414A publication Critical patent/GB2112414A/en
Application granted granted Critical
Publication of GB2112414B publication Critical patent/GB2112414B/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/63Platinum group metals with rare earths or actinides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/50Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • C01B3/501Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by diffusion
    • C01B3/503Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by diffusion characterised by the membrane
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C5/00Alloys based on noble metals
    • C22C5/04Alloys based on a platinum group metal
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0405Purification by membrane separation
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465Composition of the impurity
    • C01B2203/048Composition of the impurity the impurity being an organic compound

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Catalysts (AREA)

Abstract

The alloy contains: ruthenium, 4 to 8 wt.%; at least one rare-earth element 0.3 to 8 wt.% (total); palladium, the balance. The alloy can be useful for purification of hydrogen by diffusion and as a catalyst for chemical processes, as well as processes associated with transfer of hydrogen.

Description

SPECIFICATION Palladium-based alloy The present invention relates to palladium-based alloys. In this specification, all percentages are by weight.
Palladium-based alloys are used as membranes for purification of hydrogen by diffusion, as catalysts in the chemical industry, for processes associated with hydrogen transfer, as well as in medicine, electrical engineering, and instrument manufacture as electrodes, thermo-couples, electrical contacts, potentiometric materials, and soldering compositions, for example.
To obtain super-pure hydrogen by way of purification by diffusion of commercial hydrogen or isolation thereof from hydrogen-containing mixtures, use is made of hydrogen-permeable membranes made of palladium and palladium-based alloys. At the present time use if made of alloys containing up to 40% of silver (cf. German Patent No. 2,305,595; U.S. Patent No. 3,247,648: A. A. Rodina et al., Journal of Physical Chemistry, 1979, No. 5, p. 1350 in Russian). A maximum hydrogen-permeability is inherent in alloys containing 7.6-9.6% of silver. Also employed are alloys containing 1 8 to 25% of silver. To obtain a higher stability of the latter alloys, other elements such as indium are incorporated (cf.
A. A. Rodina et al.,JournalofphysicalChemistry, 1980, No. 6, p. 1551). However, silver-containing alloys are less active in chemical processes associated with hydrogenation and dehydrogenation.
Other palladium-based alloys employed for hydrogen purification and containing gold, copper, boron, nickel, rhodium, cerium, yttrium, and platinum either possess insufficient mechanical strength (e.g alloys with gold and copper additions), or get broken under the effect of hydrogen and other aggressive medium (cf. A. G. Knapton, Platinum Metals Review, 1 977, V21 (2), p. 44).
Incorporation into palladium or additions of gold, copper, and likewise silver lowers catalytic activity of palladium in dehydrogenation reactions. Incorporation of platinum additions make palladium more durable, increases its catalytic activity, but considerably reduces the values of hydrogenpermeability of the alloys. Furthermore, in the majority of these alloys two hydride phases a an /3 are formed which when present together lower the selectivity of catalysts made from palladium alloys and serve as the cause of destruction under the effect of hydrogen.
U.S. Patent No. 3,238,700 discloses a membrane for purification of hydrogen which is made of a palladium alloy containing 4.5% of ruthenium. Hydrogen-permeability of this alloy exceeds that of pure palladium; however, this alloy has but a short service life when operated in the atmosphere of hydrogen and hydrocarbon upon multiple cycles of heating and cooling and has a low selectivity in carrying out catalytic processes, which is likely to be associated with the presence of two hydride phases ( and ).
During operation of the membrane there occurs the transition a > ,B which results in breaking of the membrane. Furthermore, the presence of two hydride phases substantially lowers the selectivity of catalytic processes of hydrogenation and dehydrogenation, owing to different mechanisms and kinetics of reactions occurring at active centres of these phases.
What is desired is an alloy based on palladium which would not break in an atmosphere of hydrogen and would make it possible to increase selectivity of catalytic processes.
The present invention provides a palladium-based alloy which contains ruthenium and a rare-eartY element and has the following composition: ruthenium 4 to 8% by mass rare-earth element 0.3 to 8% by mass palladium the balance.
The rare-earth elements are scandium, yttrium, and the lanthanides.
An alloy of the above-specified composition is stable in operation; it withstands 4 times as many heating-cooling cycles as the prior art alloy containing 5% of ruthenium, balance palladium.
The range of content of ruthenium is limited by values of hydrogen-permeability and durability of a particular alloy. Hydrogen-permeabiiity of alloys at a minimum (4%) and maximum (8%) content of ruthenium does not substantially differ from that of an alloy having an optimal composition with 6% of ruthenium (cf. V. M. Gryaznov et al., DAN SSSR, 1973, vol. 211, No. 3, p. 624). If the content of ruthenium were more than 8%, hydrogen-permeability of the alloys would become substantially reduced. Alloys containing more than 10% of ruthenium would already be binary ones and would be non-processable.
Palladium-based alloys containing less than 4% of ruthenium, though possessing sufficient hydrogen-permeability, would have an insufficient durability in operation in an atmosphere of hydrogen.
The lower limit of the (total) content of the rare-earth element(s) (REE) is defined by the presence of hydride phases. If the REE content were below 0.3% a considerable amount of the undesirable hydride ,B-phase would be present. If the REE content were above 8% the majority of the alloys would be binary and non-processable.
Consequently, violation of the above-specified range of contents of ruthenium and REE would not provide the expected results.
Various modifications of palladium alloys according to the present invention are possible.
For alloys containing lanthanum and yttrium the following compositions are recommended as the most efficient for the purpose of high hydrogen-permeability, heat-resistance, and selectivity in catalytic processes: ruthenium 4 to 8% lanthanum 0.3 to 2% palladium the balance; and ruthenium 4 to 8% yttrium 0.3 to 8% palladium the balance.
Alloys of palladium with ruthenium and REE may be melted in an electric-arc vacuum furnace with a non-consumable tungsten electrode on a copper water-cooled hearth in an atmosphere of purified helium under a superatmospheric pressure of from 600 to 800 mm Hg. The preliminary vacuum in the furnace chamber is not less than 3.10-4 mm Hg. The alloying additions of rare-earth metals are introduced into the alloys through an intermediate ligature. The composition of the alloys is controlled by chemical analysis.
All the smelted alloys have a fine-grain structure and are within the range of a solid solution.
Membrane-foils with a thickness of 100 jum can be produced from the alloys by the method of cold deformation with intermediate vacuum annealing.
For measurement of hydrogen-permeability, the thus-made foils are fixed along the periphery in a reactor cell into which hydrogen is introduced from one side. The amount of hydrogen that has passed through the foil is determined chromatographically. During operation the foils are subjected to cyclic heating at a temperature within the range of from 50 to 4000C.
The accompanying drawing is a graph of the relationship between hydrogen-permeability (QH (ml/s.cm2 x 102) and temperature (OC) of some palladium alloys, namely: a well-known alloy of palladium and 6% ruthenium (curve 1), and palladium-ruthenium alloys with additions of lanthanum: Pd -- 6% Ru - 0.3% (curve 2); Pd - 6% Ru - 0.6% La (curve 3); and Pd - 6% Ru - 1% La (curve 4).
The arrows on the curves show the direction of temperature variation.
It is seen from the graph that, within the investigated temperature range, a very insignificant hysteresis is observed in curve 2, whereas it is absent in curves 3 and 4. The absence of hysteresis in the hydrogen-permeability curves for the alloys Pd -6% Ru - 0.6% La and Pd t 6% Ru - 1% La points to the absence of the a ss p transition in these alloys in operation of these alloys in an atmosphere of hydrogen or hydrogen-containing media.
The presence, in the alloys, of only one hydride a-phase substantially increases heat-resistance and extends service life of membranes made of these alloys.
Similar values of hydrogen-permeability and the absence of hysteresis in the curves of relationship between hydrogen-permeability and temperature are exhibited by alloys of palladium-ruthenium with additions of yttrium, cerium, neodymium, and samarium.
In carrying-out catalytic processes (hydrogenation of pentadiene and nitrobenzene) the starting feed is supplied into the reactor from one side of the foil membrane under a vapour pressure of 10 mm Hf, and from the other side hydrogen is supplied under a pressure of 1 atm. The rate of supply of vapours of the starting compounds is 75 ml/min.
EXAMPLE 1 Alloys of palladium with ruthenium and additions of lanthanum have been produced; their compositions and strength characteristics are shown in Table 1.
TABLE 1 Hardness Tensile Alloy Hv kg/mm2 strength kg/mm2 Pa-6%Ru 116 60 Pa-6%Ru-0.3%La 126 75 Pa-6%Ru-0.6%La 140 90 Pa-6%Ru-1%La 146 95 It is seen from Table 1 that additions of lanthanum increase the mechanical strength of the known Pa~6% Ru alloy.
Higher selectivity of the catalytic process on the membrane made from an alloy with a lanthanum addition is shown in pentadiene hydrogenation. The process parameters are shown in Table 2.
TABLE 2 Reaction products, % Temperature Alloy oc pentane pentene-1 pentene-2 pentadiene Pa-6%Ru 50 53 2 11 balance 120 23 2.5 74.5 none Pa-6%Ru-1%La 50 0.8 11.5 38 balance 120 none 28 72 none In the reaction of hydrogenation of pentadiene at the temperature of 120 C the membrane of a palladium alloy with 6% of ruthenium withstood 150 thermal cycles of heating and cooling; a membrane of a palladium alloy with 6% ruthenium and 0.3% of lanthanum withstood 500 cycles, while membranes made of alloys of palladium with 6% of ruthenium and 0.6% of lanthanum and palladium with 6% of ruthenium and 1% of lanthanum remained unbroken during the entire operation period (800 cycles).
EXAMPLE 2 Alloys of palladium with ruthenium and additions of yttrium have been produced; their compositions and strength characteristics are shown in Table 3.
TABLE 3 Hardness Tensile Alloy Hv kg/mm2 strength kg/mm2 Pa-6%Ru 116 60 Pa-6%#u-0.3%Y 131 78 Pa-6%Ru-1%Y 148 98 Pa-6%Ru-2%Y 154 118 Pa-4%Ru-8%Y 134 102 It is seen that the addition of yttrium increases the mechanical strength of the known Pa-Ru alloy.
Improvement of the selectivity of a catalystic process on membranes made from alloys with additions of yttrium is shown in hydrogenation of nitrobenzene. The process characteristics are shown in Table 4.
TABLE 4 Reaction products % Temperature nitroso- cyclo- nitro Alloy 0C aniline benzene hexylamine benzene P'a -6% Ru 170 66 2 12 20 250 72 traces 28 none Pa-6%Ru-0.3%Y 170 69 traces 8 23 250 78 none 22 none Pa-6%Ru-1%Y 170 85 none 4 11 250 100 - - - Pa-6%Ru-2%Y 170 93 none none 7 250 100 - - - The alloy containing palladium, 6% of ruthenium, and 2% of yttrium in this reaction at the temperature of 2500C withstands 4 times as many cycles as the alloy comprising palladium and 6% of ruthenium.
The addition of yttrium increase the mechanical strength, heat-resistance, and selectivity of the prior art alloy.
EXAMPLE 3 In much the same manner there have been prepared alloys of palladium with ruthenium and additions of cerium, neodymium, and samarium; their compositions and mechanical strength characteristics are shown in Table 5.
TABLE 5 Hardness Tensile Alloy kg/mm2 strength kg/mm2 Pa -6% Ru 116 60 Pa-6%Ru-1%Ce 138 86 Pa-6%Ru-5%Ce 162 104 Pa-6%Ru-2%Nd 146 92 Pa-6%Ru-2%Sm 140 89 Pa-6%Ru-7%Sm 170 132 Additions of cerium, neodymium, and samarium increase the mechanical strength of palladium and, like lanthanum and yttrium, enhance the heat-resistance and extend the service life of membranes made of these alloys, as well as improving the selectivity of catalytical processes carried out on them.

Claims (2)

1. A palladium-based alloy containing: ruthenium 4to8wt.% at least one rare-earth element 0.3 to 8 wt.% (total) palladium the balance.
2. A palladium-based alloy according to claim 1, substantially as described in any of the Examples given.
GB08138677A 1981-12-23 1981-12-23 Palladium-based alloy Expired GB2112414B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB08138677A GB2112414B (en) 1981-12-23 1981-12-23 Palladium-based alloy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB08138677A GB2112414B (en) 1981-12-23 1981-12-23 Palladium-based alloy

Publications (2)

Publication Number Publication Date
GB2112414A true GB2112414A (en) 1983-07-20
GB2112414B GB2112414B (en) 1985-07-03

Family

ID=10526793

Family Applications (1)

Application Number Title Priority Date Filing Date
GB08138677A Expired GB2112414B (en) 1981-12-23 1981-12-23 Palladium-based alloy

Country Status (1)

Country Link
GB (1) GB2112414B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001049396A1 (en) * 1999-12-31 2001-07-12 Dieter Seipler Catalytic converter for cleaning exhaust gases and method for the production thereof
WO2003039743A1 (en) * 2001-11-08 2003-05-15 Degussa Ag Supported catalyst for hydrogenation of nitroaromatics
US6818720B2 (en) 2001-11-08 2004-11-16 Degussa Ag Supported hydrogenating catalyst in powder form
US8071503B2 (en) 2006-07-27 2011-12-06 Johnson Matthey Public Limited Company Catalyst

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001049396A1 (en) * 1999-12-31 2001-07-12 Dieter Seipler Catalytic converter for cleaning exhaust gases and method for the production thereof
WO2003039743A1 (en) * 2001-11-08 2003-05-15 Degussa Ag Supported catalyst for hydrogenation of nitroaromatics
US6818720B2 (en) 2001-11-08 2004-11-16 Degussa Ag Supported hydrogenating catalyst in powder form
US8071503B2 (en) 2006-07-27 2011-12-06 Johnson Matthey Public Limited Company Catalyst

Also Published As

Publication number Publication date
GB2112414B (en) 1985-07-03

Similar Documents

Publication Publication Date Title
US3243387A (en) Palladium-silver-iron oxide on alphaalumina catalyst composition for the selective hydrogenation of acetylene
US20070038008A1 (en) Process for the selective hydrogenation of phenylacetylene
US3344582A (en) Irreversible hydrogen membrane
GB2112414A (en) Palladium-based alloy
US4489039A (en) Palladium-based alloy
US4727202A (en) Process for the production of catalytically-active metallic glasses
KR100337971B1 (en) Process for the generation of low dew-point, oxygen-free protective atmosphere for the performance of thermal treatments
KR920002205A (en) Method for Purifying Inert Gas Streams
Gryaznov Surface catalytic properties and hydrogen diffusion in palladium alloy membranes
US3150930A (en) Process for the dehydrogenation of a tetrahydroanthraquinone to an anthraquinone
US3086945A (en) Catalytic decomposition of 1, 1-dimethylhydrazine
WO2019175128A1 (en) Improved catalysts comprising silver based intermetallic compounds
US5220108A (en) Amorphous alloy catalysts for decomposition of flons
KR960029226A (en) Method for removing impurities contained in a composite gas
US4250118A (en) Process for the preparation of cyclohexanone
JPS6140739B2 (en)
JP2977606B2 (en) Noble gas purification method
CA2037160C (en) Amorphous alloy catalysts for decomposition of flons
US4308413A (en) Process for the preparation of alkylbenzenes
RU2126781C1 (en) Method of producing unsaturated hydrocarbons
US3931345A (en) Hydrogenation and hydrodealkylation process
EP0446710B1 (en) The use of an amorphous alloy catalyst for conversion of carbon dioxide
US3799889A (en) Hydrogenation and hydrodealkylation catalyst
US4285777A (en) Process for the purification of benzaldehyde
EP1098952B2 (en) Hydrogenation process

Legal Events

Date Code Title Description
PCNP Patent ceased through non-payment of renewal fee