The electroless nickel plating of porous sintered iron-base parts
Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel pla...
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| Autor*in: |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
1965 |
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| Umfang: |
5 |
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| Reproduktion: |
Springer Online Journal Archives 1860-2002 |
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| Übergeordnetes Werk: |
in: Powder metallurgy and metal ceramics - 1962, 4(1965) vom: Mai, Seite 380-384 |
| Übergeordnetes Werk: |
volume:4 ; year:1965 ; month:05 ; pages:380-384 ; extent:5 |
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NLEJ191833746 |
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| 245 | 1 | 0 | |a The electroless nickel plating of porous sintered iron-base parts |
| 264 | 1 | |c 1965 | |
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| 520 | |a Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. | ||
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(DE-627)NLEJ191833746 DE-627 ger DE-627 rakwb eng The electroless nickel plating of porous sintered iron-base parts 1965 5 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. Springer Online Journal Archives 1860-2002 Apininskaya, L. M. oth Radomysel'skii, I. D. oth in Powder metallurgy and metal ceramics 1962 4(1965) vom: Mai, Seite 380-384 (DE-627)NLEJ188994661 (DE-600)2037317-X 1573-9066 nnns volume:4 year:1965 month:05 pages:380-384 extent:5 http://dx.doi.org/10.1007/BF00774619 GBV_USEFLAG_U ZDB-1-SOJ GBV_NL_ARTICLE AR 4 1965 5 380-384 5 |
| spelling |
(DE-627)NLEJ191833746 DE-627 ger DE-627 rakwb eng The electroless nickel plating of porous sintered iron-base parts 1965 5 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. Springer Online Journal Archives 1860-2002 Apininskaya, L. M. oth Radomysel'skii, I. D. oth in Powder metallurgy and metal ceramics 1962 4(1965) vom: Mai, Seite 380-384 (DE-627)NLEJ188994661 (DE-600)2037317-X 1573-9066 nnns volume:4 year:1965 month:05 pages:380-384 extent:5 http://dx.doi.org/10.1007/BF00774619 GBV_USEFLAG_U ZDB-1-SOJ GBV_NL_ARTICLE AR 4 1965 5 380-384 5 |
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(DE-627)NLEJ191833746 DE-627 ger DE-627 rakwb eng The electroless nickel plating of porous sintered iron-base parts 1965 5 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. Springer Online Journal Archives 1860-2002 Apininskaya, L. M. oth Radomysel'skii, I. D. oth in Powder metallurgy and metal ceramics 1962 4(1965) vom: Mai, Seite 380-384 (DE-627)NLEJ188994661 (DE-600)2037317-X 1573-9066 nnns volume:4 year:1965 month:05 pages:380-384 extent:5 http://dx.doi.org/10.1007/BF00774619 GBV_USEFLAG_U ZDB-1-SOJ GBV_NL_ARTICLE AR 4 1965 5 380-384 5 |
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(DE-627)NLEJ191833746 DE-627 ger DE-627 rakwb eng The electroless nickel plating of porous sintered iron-base parts 1965 5 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. Springer Online Journal Archives 1860-2002 Apininskaya, L. M. oth Radomysel'skii, I. D. oth in Powder metallurgy and metal ceramics 1962 4(1965) vom: Mai, Seite 380-384 (DE-627)NLEJ188994661 (DE-600)2037317-X 1573-9066 nnns volume:4 year:1965 month:05 pages:380-384 extent:5 http://dx.doi.org/10.1007/BF00774619 GBV_USEFLAG_U ZDB-1-SOJ GBV_NL_ARTICLE AR 4 1965 5 380-384 5 |
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(DE-627)NLEJ191833746 DE-627 ger DE-627 rakwb eng The electroless nickel plating of porous sintered iron-base parts 1965 5 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. Springer Online Journal Archives 1860-2002 Apininskaya, L. M. oth Radomysel'skii, I. D. oth in Powder metallurgy and metal ceramics 1962 4(1965) vom: Mai, Seite 380-384 (DE-627)NLEJ188994661 (DE-600)2037317-X 1573-9066 nnns volume:4 year:1965 month:05 pages:380-384 extent:5 http://dx.doi.org/10.1007/BF00774619 GBV_USEFLAG_U ZDB-1-SOJ GBV_NL_ARTICLE AR 4 1965 5 380-384 5 |
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in Powder metallurgy and metal ceramics 4(1965) vom: Mai, Seite 380-384 volume:4 year:1965 month:05 pages:380-384 extent:5 |
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the electroless nickel plating of porous sintered iron-base parts |
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The electroless nickel plating of porous sintered iron-base parts |
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Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. |
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Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. |
| abstract_unstemmed |
Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter. |
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<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">NLEJ191833746</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20210707175113.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">070526s1965 xx |||||o 00| ||eng c</controlfield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)NLEJ191833746</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">The electroless nickel plating of porous sintered iron-base parts</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">1965</subfield></datafield><datafield tag="300" ind1=" " ind2=" "><subfield code="a">5</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">nicht spezifiziert</subfield><subfield code="b">zzz</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">nicht spezifiziert</subfield><subfield code="b">z</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">nicht spezifiziert</subfield><subfield code="b">zu</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Summary 1. The electroless nickel plating of sintered parts should not be performed in alkaline solutions. The best results were obtained by nickel plating in acid solutions (pH 5–5.2). 2. For obtaining nickel deposits 20–25μ thick, capable of resisting 3% NaCl solution for 7 h or longer, nickel plating should be performed in two stages. 3. In order to prevent the corrosion of the internal surface, the pores must be impregnated with GKZh-94 liquid before plating, and polymerization must be carried out. 4. For raising the corrosion resistance of the nickel deposit, the latter should also be impregnated with a weak solution of GKZh-94 and then subjected to polymerization. 5. If the nickel plating solution is to operate in a stable manner and be capable of correction, sodium citrate (15 g/liter) and glycocoll (30 g/liter) must be added to it. 6. The nickel plating solution is replaced by a fresh one after 5–6 operating cycles, when its phosphite content has reached 50–60 g/liter.</subfield></datafield><datafield tag="533" ind1=" " ind2=" "><subfield code="f">Springer Online Journal Archives 1860-2002</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Apininskaya, L. M.</subfield><subfield code="4">oth</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Radomysel'skii, I. D.</subfield><subfield code="4">oth</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">in</subfield><subfield code="t">Powder metallurgy and metal ceramics</subfield><subfield code="d">1962</subfield><subfield code="g">4(1965) vom: Mai, Seite 380-384</subfield><subfield code="w">(DE-627)NLEJ188994661</subfield><subfield code="w">(DE-600)2037317-X</subfield><subfield code="x">1573-9066</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:4</subfield><subfield code="g">year:1965</subfield><subfield code="g">month:05</subfield><subfield code="g">pages:380-384</subfield><subfield code="g">extent:5</subfield></datafield><datafield tag="856" ind1="4" ind2="0"><subfield code="u">http://dx.doi.org/10.1007/BF00774619</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_USEFLAG_U</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">ZDB-1-SOJ</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_NL_ARTICLE</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">4</subfield><subfield code="j">1965</subfield><subfield code="c">5</subfield><subfield code="h">380-384</subfield><subfield code="g">5</subfield></datafield></record></collection>
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