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JPH0119619B2 - - Google Patents
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JPH0119619B2 - - Google Patents

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Publication number
JPH0119619B2
JPH0119619B2 JP56111829A JP11182981A JPH0119619B2 JP H0119619 B2 JPH0119619 B2 JP H0119619B2 JP 56111829 A JP56111829 A JP 56111829A JP 11182981 A JP11182981 A JP 11182981A JP H0119619 B2 JPH0119619 B2 JP H0119619B2
Authority
JP
Japan
Prior art keywords
cadmium
paste
fibers
battery
weight
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.)
Expired
Application number
JP56111829A
Other languages
Japanese (ja)
Other versions
JPS5814464A (en
Inventor
Minoru Yamaga
Shingo Tsuda
Hideo Kaiya
Isao Matsumoto
Mamoru Ishitobi
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP56111829A priority Critical patent/JPS5814464A/en
Publication of JPS5814464A publication Critical patent/JPS5814464A/en
Publication of JPH0119619B2 publication Critical patent/JPH0119619B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/626Metals
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/24Electrodes for alkaline accumulators
    • H01M4/246Cadmium electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/665Composites
    • H01M4/667Composites in the form of layers, e.g. coatings
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/70Carriers or collectors characterised by shape or form
    • H01M4/72Grids
    • H01M4/74Meshes or woven material; Expanded metal
    • H01M4/742Meshes or woven material; Expanded metal perforated material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/52Removing gases inside the secondary cell, e.g. by absorption
    • H01M10/526Removing gases inside the secondary cell, e.g. by absorption by gas recombination on the electrode surface or by structuring the electrode surface to improve gas recombination
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027Negative electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/669Steels
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Composite Materials (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はカドミウム負極の製造法に係り、負極
活物質利用率の向上、サイクル寿命の向上、充電
時におけるガス吸収能力の向上など電池特性の改
善を図ることを目的とする。 カドミウム負極の製造法は大別すると次の三つ
がある。その第1は焼結式で、これはニツケル粉
末を高温還元雰囲気下で焼結させて多孔性基体を
つくり、この基体孔隙中に活物質を充填したもの
であつて、高率放電特性に優れているが、ニツケ
ル焼結体を作製すること、および活物質充填工程
が煩雑になることなどから高価になるという欠点
がある。第2はプレス式で、これは活物質粉末を
導電性粉末などとともにプレス成型して電極とし
たものであつて、安価に製造できるという長所を
有するが、高率放電特性やサイクル寿命特性が劣
るという欠点がある。第3はペースト式といわれ
るもので、活物質を主体とする粉末を結着剤溶液
と混練してペーストを作製し、該ペーストを多孔
性芯金に塗着させてなるもので、高率放電特性も
ほぼ焼結式に等しく、かつ焼結式よりも安価に作
製できるという長所がある。このペースト式にお
いて、一般的なペースト組成は酸化カドミウムに
ニツケル粉や炭素粉のごとき導電材と、ポリ塩化
ビニル樹脂繊維のごとき合成樹脂製短繊維からな
る補強剤と、ポリエチレンやポリビニルアルコー
ルのごとき結着剤を溶媒に溶解してなる結着剤溶
液とからなつている。これら組成のうち、補強剤
としての合成樹脂製短繊維は多孔性芯金の孔部を
通じて芯金の両面に塗着されている活物質層間に
存在するため、特に活物質の芯金からの剥離を防
止するとともに、活物質相互間の結着にも効果が
ある。しかしながらその補強剤としての効果をさ
らに高めるためにその量的増大を図ると、電気伝
導性がないため電極の電気抵抗が増大し、活物質
利用率が劣るという欠点がでてくる。そこで代替
として細い金属繊維、例えばニツケル繊維、鉄繊
維を用いると活物質利用率は向上するが、金属繊
維は電極をプレスしても塑性変形しにくいため電
極表面上に針状に飛出し、電池に構成した時に多
孔性のセパレータを介して対向している正極と容
易に短絡してしまうという欠点がある。 本発明は前記従来のペースト式電極の製法にお
ける補強剤の改良に係るもので、カドミウムめつ
きを施した合成樹脂短繊維を用いて前記問題点を
解決したものであり、以下実施例をもつて説明す
る。 酸化カドミウム100重量部に導電材としてカー
ボニルニツケル粉を10重量部加えて混合粉末を作
り、次いで表面がカドミウムめつきされた5デニ
ールで繊維長さ3mmのポリ塩化ビニル樹脂製短繊
維を0.5重量部加えてさらに混合し、これに1重
量部のポリビニルアルコールを溶解せしめた30c.c.
のエチレングリコール溶液を加え、全体を混練し
てペーストとする。このペーストを厚さ0.8mmの
ニツケルめつき穿孔鋼板からなる芯金の両面に塗
着し、次いで乾燥してエチレングリコールを逸散
させた後、プレスを行なつて多孔度約40%の未化
成極板とする。次にこの未化成極板を20%のか性
ソーダ水溶液中で理論容量の50%を還元させたの
ち、水洗、乾燥、プレスして完成極板とする。こ
の完成極板を所定寸法に切断して単位極板とす
る。 この単位極板を用いて、焼結式正極、ポリアミ
ド樹脂製不織布からなるセパレータと組合せ、
500mAhの容量を有する密閉形ニツケル・カドミ
ウム蓄電池を作製した。 この電池Aと、従来のカドミウムめつきをして
いない合成樹脂製短繊維を補強剤としてペースト
中に混入したカドミウム負極を用いた電池Bとに
ついて高率放電特性、サイクル寿命特性およびガ
ス吸収能力特性について調べた。なお、電池A,
Bにおける相違は負極の補強剤が異なるのみで他
の条件は全く同一とした。 第1図は高率放電特性を示し、完全充電された
電池を各放電率で放電した時の放電容量である。
図から明らかなように5C(2.5A)放電以上になる
と本発明品Aのすぐれていることがわかる。 第2図はサイクル寿命特性であり、常温にて充
電を1/2C(250mA)で3時間、放電を1C
(500mA)で行なつた時の結果である。本発明品
Aは1000サイクル以上でも全く容量劣化がみられ
ないのに対し、従来品Bでは1000サイクル付近か
ら劣化する傾向が見られる。 第3図はガス吸収能力特性である。この実施例
における密閉形ニツケル・カドミウム蓄電池は過
充電時に正極より発生する酸素ガスを負極のカド
ミウムで吸収(酸化)することにより密閉化が保
たれているが、この酸素ガス吸収能力の向上は充
電時間の短縮につながる。そこで特にガス吸収反
応の遅い低温での吸収能力を調べた。第3図は0
℃にて各充電率で充電した時の電池内圧力の値で
ある。本発明品Aは従来品Bにくらべて電池内圧
力が低く、ガス吸収能力が向上していることが判
る。これら電池特性の改良は化成処理の際、カド
ミウムめつき部分の近傍の酸化カドミウムから還
元され、カドミウムめつきが施された繊維は芯金
の孔部を通じて、芯金の両面にある活物質と連通
しているために良好な導電ネツトワークが形成さ
れることによる。特に電極表面の金属カドミウム
量が従来にくらべて大幅に増加しており、これが
放電特性の向上、ガス吸収性の向上などに寄与し
ているものと考えられる。 以上のように電池特性上、本発明品は従来品に
くらべ向上しているが、カドミウム負極の利用率
について調べたところ、次のようになつた。 すなわち前記電池A,Bで使用したと同様の負
極A′,B′を濃度30%のか性カリ水溶液中にてニ
ツケル板を相手極として各放電率での活物質利用
率(%)を測定したところ次表のような結果を得
た。
The present invention relates to a method for producing a cadmium negative electrode, and aims to improve battery characteristics such as improving the utilization rate of negative electrode active material, improving cycle life, and improving gas absorption ability during charging. There are three main methods for producing cadmium negative electrodes: The first is the sintering method, in which nickel powder is sintered in a high-temperature reducing atmosphere to create a porous substrate, and the pores of this substrate are filled with an active material, which has excellent high-rate discharge characteristics. However, it has the disadvantage that it is expensive because it requires the production of a nickel sintered body and the active material filling process is complicated. The second type is the press type, which is an electrode made by press-molding active material powder together with conductive powder, etc., and has the advantage of being inexpensive to manufacture, but has poor high rate discharge characteristics and cycle life characteristics. There is a drawback. The third method is called a paste type, in which a paste is created by kneading powder mainly composed of active materials with a binder solution, and the paste is applied to a porous core metal, which allows high rate discharge. It has the advantage that it has almost the same characteristics as the sintered type and can be manufactured at a lower cost than the sintered type. In this paste type, the general paste composition is cadmium oxide, a conductive material such as nickel powder or carbon powder, a reinforcing agent consisting of short synthetic resin fibers such as polyvinyl chloride resin fiber, and a binder such as polyethylene or polyvinyl alcohol. It consists of a binder solution made by dissolving a binder in a solvent. Among these compositions, the short synthetic resin fibers as a reinforcing agent exist between the active material layers coated on both sides of the core metal through the pores of the porous core metal, so it is particularly difficult for the active material to peel off from the core metal. In addition to preventing this, it is also effective in binding the active materials to each other. However, when increasing its quantity in order to further enhance its effect as a reinforcing agent, the disadvantage is that the electrical resistance of the electrode increases due to its lack of electrical conductivity, and the utilization rate of the active material is poor. Therefore, if thin metal fibers such as nickel fibers or iron fibers are used as an alternative, the active material utilization rate will improve, but metal fibers are difficult to plastically deform even when electrodes are pressed, so they protrude into needle-like shapes on the electrode surface, causing the battery There is a drawback that when configured as shown in FIG. The present invention relates to an improvement of the reinforcing agent in the conventional paste-type electrode manufacturing method, and solves the above problems by using cadmium-plated short synthetic resin fibers. explain. A mixed powder was prepared by adding 10 parts by weight of carbonyl nickel powder as a conductive material to 100 parts by weight of cadmium oxide, and then 0.5 parts by weight of polyvinyl chloride resin short fibers with a cadmium-plated surface and 5 deniers and a fiber length of 3 mm. In addition, 30c.c. of 1 part by weight of polyvinyl alcohol was dissolved in the mixture and further mixed.
Add ethylene glycol solution and knead the whole to make a paste. This paste is applied to both sides of a core made of nickel-plated perforated steel plate with a thickness of 0.8 mm, then dried to dissipate the ethylene glycol, and then pressed to form an unformed material with a porosity of approximately 40%. Use it as a pole plate. Next, this unformed electrode plate is reduced to 50% of its theoretical capacity in a 20% caustic soda aqueous solution, then washed with water, dried, and pressed to form a completed electrode plate. This completed electrode plate is cut into a predetermined size to form a unit electrode plate. Using this unit electrode plate, combine it with a sintered positive electrode and a separator made of polyamide resin nonwoven fabric,
A sealed nickel-cadmium storage battery with a capacity of 500mAh was fabricated. High rate discharge characteristics, cycle life characteristics, and gas absorption capacity characteristics of this battery A and battery B that uses a cadmium negative electrode in which conventional short synthetic resin fibers without cadmium plating are mixed into the paste as a reinforcing agent. I looked into it. In addition, battery A,
The only difference in B was the reinforcing agent of the negative electrode, and the other conditions were completely the same. FIG. 1 shows high rate discharge characteristics, and shows the discharge capacity when a fully charged battery is discharged at various discharge rates.
As is clear from the figure, it can be seen that the product A of the present invention is superior when the discharge is 5C (2.5A) or higher. Figure 2 shows the cycle life characteristics, charging at 1/2C (250mA) for 3 hours and discharging at 1C at room temperature.
(500mA). Product A of the present invention shows no capacity deterioration even after 1000 cycles or more, whereas conventional product B tends to deteriorate from around 1000 cycles. Figure 3 shows the gas absorption capacity characteristics. The sealed nickel-cadmium storage battery in this example is kept sealed by absorbing (oxidizing) oxygen gas generated from the positive electrode during overcharging with the cadmium in the negative electrode. This leads to time savings. Therefore, we investigated the absorption capacity especially at low temperatures where gas absorption reactions are slow. Figure 3 is 0
This is the value of the internal pressure of the battery when charging at various charging rates at °C. It can be seen that product A of the present invention has lower internal battery pressure and improved gas absorption ability than conventional product B. These improvements in battery characteristics are achieved by reducing the cadmium oxide near the cadmium-plated portion during chemical conversion treatment, and the cadmium-plated fibers communicate with the active materials on both sides of the core through the holes in the core. This is due to the formation of a good conductive network. In particular, the amount of metallic cadmium on the electrode surface has increased significantly compared to conventional electrodes, and this is thought to contribute to improvements in discharge characteristics and gas absorption. As described above, the product of the present invention has improved battery characteristics compared to the conventional product, but when the utilization rate of the cadmium negative electrode was investigated, the results were as follows. That is, the active material utilization rate (%) at each discharge rate was measured using negative electrodes A' and B' similar to those used in batteries A and B above in a caustic potassium aqueous solution with a concentration of 30% and a nickel plate as the other electrode. I got the results as shown in the table below.

【表】 上表のように本発明A′の負極は活物質利用率
が向上したため、前記電池諸特性の改善がなされ
たものである。 なお、合成樹脂製短繊維のめつき法としては無
電解めつきや電解めつきなどがあるが、本実施例
で用いたものは、まず繊維表面に無電解ニツケル
めつきを行なつたのち、電解カドミウムめつきを
施したものである。このめつきにより0.5μ程度の
厚みにカドミウムめつきがなされた。 このカドミウムめつきを行なわずに、単にニツ
ケルめつきだけで使用することも考えられるが、
カドミウムめつきにくらべニツケルめつきのみで
は水素過電圧が小さく、低温で大きな充電率で充
電した時の充電効率が悪くなるので不十分であ
る。したがつて繊維の表面層はカドミウムめつき
とするのが良く、そのめつき方法については何ら
拘束されない。 なお前記実施例ではペースト組成中に導電材と
してニツケル粉末を加えているが、このニツケル
粉末の量的効果よりも、カドミウムめつきを施し
た短繊維の混入の方が効果的であることが確認さ
れた。そのカドミウムめつきを施した短繊維量に
ついては種々検討したところ、酸化カドミウム
100重量部当り0.1重量部以上で効果がみられる。
また上限としては2重量部がよく、これよりも多
量では繊維量が多すぎてペースト中での分散が悪
くなる。また0.1重量部よりも少量の場合はめつ
きされるカドミウム量が少なすぎてその効果が得
られない。したがつて酸化カドミウム100重量部
当り0.1〜2重量部が適切である。 また、繊維径や長さについて検討したが、上記
重量比率の影響がもつとも効果がみられる。 さらに実施例において化成処理は酸化カドミウ
ムの部分的還元について記したが、100%還元あ
るいは100%還元後に部分的に酸化させるなど化
成処理は還元、還元プラス酸化であつてもよく、
この化成処理法については何ら拘束されない。 以上のように本発明は負極ベースト中の補強剤
を変えることにより、電池性能を向上させたもの
であり、カドミウム負極を用いる電池、とくに密
閉形カドミウム負極使用電池において価値の大き
なものである。
[Table] As shown in the above table, the negative electrode of the present invention A' has an improved active material utilization rate, and thus the various battery characteristics described above are improved. Methods for plating synthetic resin short fibers include electroless plating and electrolytic plating, but the method used in this example first performs electroless nickel plating on the fiber surface, and then It is electrolytically cadmium plated. This plating resulted in cadmium plating to a thickness of approximately 0.5μ. It is conceivable to simply use nickel plating without this cadmium plating, but
Compared to cadmium plating, nickel plating alone is insufficient because the hydrogen overvoltage is small and the charging efficiency deteriorates when charging at a high charging rate at low temperatures. Therefore, the surface layer of the fibers is preferably plated with cadmium, and there are no restrictions on the method of plating. In the above example, nickel powder was added as a conductive material to the paste composition, but it was confirmed that the inclusion of cadmium-plated short fibers was more effective than the quantitative effect of this nickel powder. It was done. After conducting various studies on the amount of short fibers coated with cadmium, we found that cadmium oxide
Effects are seen at 0.1 parts by weight or more per 100 parts by weight.
A good upper limit is 2 parts by weight; if the amount is larger than this, the amount of fibers will be too large and dispersion in the paste will be poor. Further, if the amount is less than 0.1 part by weight, the amount of cadmium plated is too small to obtain the desired effect. Therefore, 0.1 to 2 parts by weight per 100 parts by weight of cadmium oxide is suitable. In addition, although the fiber diameter and length were studied, it was found that the effect of the above-mentioned weight ratio was also effective. Further, in the examples, the chemical conversion treatment is described as partial reduction of cadmium oxide, but the chemical conversion treatment may be reduction, reduction plus oxidation, such as 100% reduction or partial oxidation after 100% reduction.
There are no restrictions on this chemical conversion treatment method. As described above, the present invention improves battery performance by changing the reinforcing agent in the negative electrode base, and is of great value in batteries using cadmium negative electrodes, especially batteries using sealed cadmium negative electrodes.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施例におけるカドミウム負
極を用いた密閉形蓄電池の放電率特性を示す図、
第2図はサイクル寿命を示す図、第3図はガス吸
収能力特性を示す。 A……本発明品、B……従来品。
FIG. 1 is a diagram showing the discharge rate characteristics of a sealed storage battery using a cadmium negative electrode in an example of the present invention;
FIG. 2 shows the cycle life, and FIG. 3 shows the gas absorption capacity characteristics. A...Product of the present invention, B...Conventional product.

Claims (1)

【特許請求の範囲】 1 酸化カドミウムに結着剤を加えてなるペース
ト状物質中にカドミウムめつきを施した合成樹脂
短繊維を添加分散させ、前記ペーストを多孔性芯
金に塗着し、次いで化成処理することを特徴とす
るカドミウム負極の製造法。 2 前記カドミウムめつきを施した合成樹脂短繊
維が酸化カドミウム100重量部当り、0.1〜2重量
部ペースト中に添加されている特許請求の範囲第
1項記載のカドミウム負極の製造法。
[Claims] 1. Cadmium-plated short synthetic resin fibers are added and dispersed in a paste-like material made by adding a binder to cadmium oxide, and the paste is applied to a porous core, and then A method for producing a cadmium negative electrode characterized by chemical conversion treatment. 2. The method for producing a cadmium negative electrode according to claim 1, wherein the cadmium-plated short synthetic resin fibers are added to the paste in an amount of 0.1 to 2 parts by weight per 100 parts by weight of cadmium oxide.
JP56111829A 1981-07-16 1981-07-16 Manufacture of cadmium negative electrode Granted JPS5814464A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56111829A JPS5814464A (en) 1981-07-16 1981-07-16 Manufacture of cadmium negative electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56111829A JPS5814464A (en) 1981-07-16 1981-07-16 Manufacture of cadmium negative electrode

Publications (2)

Publication Number Publication Date
JPS5814464A JPS5814464A (en) 1983-01-27
JPH0119619B2 true JPH0119619B2 (en) 1989-04-12

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP56111829A Granted JPS5814464A (en) 1981-07-16 1981-07-16 Manufacture of cadmium negative electrode

Country Status (1)

Country Link
JP (1) JPS5814464A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5934263A (en) * 1997-07-09 1999-08-10 Ford Global Technologies, Inc. Internal combustion engine with camshaft phase shifting and internal EGR

Also Published As

Publication number Publication date
JPS5814464A (en) 1983-01-27

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