JPH02267107A - Nitrate briquette and production thereof - Google Patents

Nitrate briquette and production thereof

Info

Publication number
JPH02267107A
JPH02267107A JP8931089A JP8931089A JPH02267107A JP H02267107 A JPH02267107 A JP H02267107A JP 8931089 A JP8931089 A JP 8931089A JP 8931089 A JP8931089 A JP 8931089A JP H02267107 A JPH02267107 A JP H02267107A
Authority
JP
Japan
Prior art keywords
nitrate
raw material
briquettes
silver nitrate
briquette
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
JP8931089A
Other languages
Japanese (ja)
Other versions
JP2729316B2 (en
Inventor
Kunihisa Tabuchi
田渕 訓久
Yoshio Omi
近江 善夫
Toshio Endo
利雄 遠藤
Hiroshi Maezawa
前澤 博司
Shuji Watanabe
渡邉 修二
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.)
Konica Minolta Inc
Original Assignee
Konica Minolta Inc
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 Konica Minolta Inc filed Critical Konica Minolta Inc
Priority to JP1089310A priority Critical patent/JP2729316B2/en
Publication of JPH02267107A publication Critical patent/JPH02267107A/en
Application granted granted Critical
Publication of JP2729316B2 publication Critical patent/JP2729316B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G5/00Compounds of silver

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Glanulating (AREA)

Abstract

PURPOSE:To obtain the title briquettes of safe and efficient drug form by dry compression forming of fine granular nitrate pieces as raw material. CONSTITUTION:Fine granular nitrate pieces such as of silver nitrate as raw material R is fed through a hopper 1. It is preferable that the size of said raw material be ca.0.1-3mm and its distribution broad. The raw material R is then pref. put to deaeration treatment in a deaeration tank 2, and fed, through a hopper 3, using a taper screw 4, to a pair of high-pressure kneader rolls 5, where the raw material is subjected to dry compression forming through high- pressure kneader rolls 51, 52 with circumferential pockets 6 of desired size into the objective nitrate briquettes B.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は硝酸塩微粒片原料を用いる乾式圧縮成形法に関
し、特に硝酸銀ブリケット及びその製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a dry compression molding method using a raw material of nitrate fine particles, and particularly to a silver nitrate briquette and a method for producing the same.

(発明の背景) 硝酸塩は一般に不安定であり、アルカリ金属塩は酸素を
放って亜硝酸塩に変り、また重金属塩は酸素及び窒素を
遊離して金属酸化物或いは金属を生成する。更に有機物
や酸化され易い金属と混在すると爆発性混合物を作る。
BACKGROUND OF THE INVENTION Nitrate salts are generally unstable, alkali metal salts liberate oxygen and turn into nitrites, and heavy metal salts liberate oxygen and nitrogen to form metal oxides or metals. Furthermore, when mixed with organic matter or metals that are easily oxidized, it forms an explosive mixture.

従って硝酸塩はその製造工程中及び保管中において品質
保持及び危険防止の面から充分な注意が必要であり、特
に重金属硝酸塩の場合には更に厳重な注意が必要である
Therefore, sufficient care must be taken to maintain quality and prevent risks during the manufacturing process and storage of nitrates, and even stricter care is required especially in the case of heavy metal nitrates.

重金属硝酸塩の代表例として硝酸銀が挙げられるが写真
用、医薬品その他として甚だ重要である。
Silver nitrate is a typical example of heavy metal nitrates, and is extremely important for use in photography, medicine, and other uses.

硝酸銀は一般にその水溶液中からの晶析によって得られ
、その純度を重視する場合には大結晶として析出させる
ことが多い。この大結晶は使い勝手のよい適当な大きさ
の小片にまで砕かれ、洗浄し、遠心脱水し、遮光容器に
収納し保管される。
Silver nitrate is generally obtained by crystallizing it from an aqueous solution, and when purity is important, it is often precipitated as large crystals. These large crystals are crushed into conveniently sized pieces, washed, centrifugally dehydrated, and stored in a light-shielding container.

或は析出条件を整え撹拌しながら適当な大きさの結晶片
に止めて取出される。
Alternatively, the precipitation conditions are adjusted and the crystal pieces of an appropriate size are collected while stirring.

このように適当な大きさに調えられた硝酸銀結晶片は遮
光容器に収納しておくと、保管中に吸湿固結するのが常
であって、その防止には調温調湿管理にコストを必要と
し、また固結した結晶片塊は使用時取出しに解砕の手数
を要する。また解砕及び使用時の投入に際し−ては、結
晶片が砕け、弾は飛んだ微結晶片は人体に障害を与え、
作業環境を汚損し、更に少量使用の際には秤量の精度を
失う。
When silver nitrate crystal pieces adjusted to an appropriate size are stored in a light-shielding container, they tend to absorb moisture and solidify during storage, and to prevent this, it is costly to control temperature and humidity. In addition, the solidified crystal fragments require a lot of effort to be disintegrated to take them out during use. In addition, during crushing and feeding during use, the crystal fragments are broken, and the microcrystal fragments that fly off the bullet can cause injury to the human body.
It contaminates the work environment, and furthermore, when used in small quantities, the accuracy of weighing is lost.

更に消防法において、硝酸銀結晶は規制の対象になって
おり、製造及び取扱い施設、保管、運搬の全般に亘り、
危険物管理に関する法に則った処置が必要であって、安
全で且つ効率的な硝酸銀薬品形態が求められる。
Furthermore, under the Fire Service Act, silver nitrate crystals are subject to regulations, and all manufacturing and handling facilities, storage, and transportation are subject to regulations.
Measures must be taken in accordance with laws regarding hazardous materials management, and a safe and efficient silver nitrate drug form is required.

尚硝酸銀に限らず硝酸塩についても一般的に前記の配慮
が必要である。
The above considerations are generally required not only for silver nitrate but also for nitrates.

(発明の目的) 本発明の目的は硝酸塩、特に硝酸銀の安全且つ効率的な
薬品形態及び該薬品形態への製造方法を提供することに
ある。
OBJECTS OF THE INVENTION It is an object of the present invention to provide a safe and efficient drug form of nitrates, particularly silver nitrate, and a method for producing the drug form.

(発明の構成及び作用効率) 前記本発明の目的は、硝酸塩微粒片原料を用い乾式圧縮
成形することを特徴とする硝酸塩ブリケットの製造方法
及び該製造方法によって製造された硝酸塩ブリケットに
よって達成される。
(Structure and efficiency of the invention) The object of the present invention is achieved by a method for producing nitrate briquettes characterized by dry compression molding using a raw material of fine nitrate particles, and a nitrate briquette produced by the method.

尚本発明の態様としては乾式圧縮成形に先立って硝酸塩
微粒片原料に脱気処理を施すことが好ましい。
In an embodiment of the present invention, it is preferable to subject the raw material of nitrate fine particles to deaeration treatment prior to dry compression molding.

また本発明は写真用硝酸銀に対し適用するとその効果は
著明ある。
Further, when the present invention is applied to photographic silver nitrate, its effects are remarkable.

次に本発明を図を用いて説明する。Next, the present invention will be explained using figures.

本発明に従って量産する場合にはタブレッティングマシ
ーン或はブリケラティングマシーンが有用である。第1
図に本発明に使用可能なブリケラティングマシーンの概
要図を示した。
For mass production according to the present invention, a tabletting machine or a briquetting machine is useful. 1st
The figure shows a schematic diagram of a briquetting machine that can be used in the present invention.

1は原料(微粒片)を投入するホッパ、2は微粒片原料
中の空気を除きブリケットの歩留りを上げる脱気槽、3
は脱気原料を供給するホッパ、4は原料を圧入するテー
パスクリュー 5は高圧圧縮成形(以後造粒と称す)を
行う高圧ニーダロール対であり、51及び52は対をな
す高圧ニーダロールである。両ロール面にはブリケット
に与える形状、大きさに対応するポケット6がその圧接
点で正確にポケット周縁が合致するように配列されてい
る。ポケット底部の深さ、形状は周縁が合致している限
り自由に選ぶことができる。
1 is a hopper into which the raw material (fine particles) is input, 2 is a deaeration tank that removes air from the fine particle raw material and increases the yield of briquettes, 3
5 is a pair of high-pressure kneader rolls for performing high-pressure compression molding (hereinafter referred to as granulation), and 51 and 52 are a pair of high-pressure kneader rolls. Pockets 6 corresponding to the shape and size to be given to the briquettes are arranged on both roll surfaces so that the circumferential edges of the pockets match exactly at the pressure contact points. The depth and shape of the pocket bottom can be freely selected as long as the peripheries match.

圧接圧力は油圧方式等によって与えられ、ブリケットの
使用目的に適した崩壊強度となるように調節される。ま
た造粒に必要ならば適温に調整してもよい。
The contact pressure is applied by a hydraulic system or the like, and is adjusted to provide a collapse strength suitable for the intended use of the briquettes. Further, if necessary for granulation, the temperature may be adjusted to an appropriate temperature.

またポケットを穿つ表面層は原料の物化性及び圧に耐え
うる剛性をもつ材質が選ばれ、差換可能であることが好
ましい。
Further, the surface layer for punching the pockets is preferably made of a material that is rigid enough to withstand the materialization of the raw material and the pressure, and is preferably replaceable.

写真用硝酸銀の造粒条件として、微粒片原料の含水率は
0〜1%が好ましく、更に0.1〜0.8%が好ましい
。0.1%未満は遠心脱水で到着するには困離があり、
また取扱時微粉が発生し易い。また1%を越えるとブリ
ケット表面に搾り出された水分が付着し、ブリケット間
の固結、容器壁への付着など好ましくない事態を招く。
As for the granulation conditions for photographic silver nitrate, the water content of the raw material for fine particles is preferably 0 to 1%, more preferably 0.1 to 0.8%. If it is less than 0.1%, it is difficult to reach it by centrifugal dehydration.
Also, fine powder is likely to be generated during handling. Moreover, if it exceeds 1%, the squeezed out water will adhere to the surface of the briquettes, causing undesirable situations such as caking between the briquettes and adhesion to the container wall.

また原料微粒片の大きさは、0.1〜3mmの範囲が好
ましく、またこの範囲で分布がブロードである方が最密
充填に都合がよく造粒性がよい。
The size of the raw material fine particles is preferably in the range of 0.1 to 3 mm, and a broad distribution within this range is convenient for closest packing and improves granulation properties.

またブリケットの薬品形態は、使用態様に合った最小有
効数値単位の重量、実用上充分な崩壊強度、見掛比重が
大きく小体積であること、更に溶解速度が大きいこと等
が勘案されて定められる。
In addition, the chemical form of briquettes is determined by taking into consideration the minimum effective numerical unit weight suitable for the usage mode, practically sufficient disintegration strength, large apparent specific gravity, small volume, and high dissolution rate. .

尚崩壊、擦れ合い等によって発生いる粉末は、固結、容
器壁等への付着を起こすので全くないことが好ましいが
lQwt%程度までの混在は実用上左程問題にならない
Powder generated by disintegration, rubbing, etc. causes caking and adhesion to container walls, so it is preferable that there is no powder at all, but mixing up to about 1Qwt% does not pose a problem in practice.

下記表1に径2.5cm、 309の硝酸銀ブリケット
の造粒条件例とそれに対応した特性を示した。
Table 1 below shows examples of granulation conditions for 309 silver nitrate briquettes with a diameter of 2.5 cm and the corresponding characteristics.

以上のように諸種事項を勘案し、実用に最も適した硝酸
銀ブリケット薬品形態が選ばれる。
As mentioned above, the most suitable silver nitrate briquette chemical form is selected in consideration of various matters.

またアモルファス塊としての本発明に係る硝酸銀ブリケ
ットは、日本カーリット(株);危険性評価試験所の評
価結果では、原料の微粒片硝酸銀は、落球式打撃感度試
験により、落球重量1.4gで10回の試験中すべて「
不爆」となったものの、落球重量261gでは10回の
試験中すべて「爆」となり「危険性中」に分類され、ま
た、燃焼試験によると、燃焼時間が22秒となり「危険
性大」に分類され、従って、「第1種酸化固体」と評価
される。
In addition, the silver nitrate briquette according to the present invention in the form of an amorphous lump is manufactured by Nippon Carlit Co., Ltd.; According to the evaluation results of the Hazard Evaluation Laboratory, the raw material fine particle silver nitrate was determined by a falling ball impact sensitivity test to have a falling ball weight of 1.4 g. During the exam, all
However, when the weight of the falling ball was 261g, all of the 10 tests resulted in an explosion, and it was classified as ``moderately dangerous.'' Also, according to the combustion test, the burning time was 22 seconds, making it ``highly dangerous.'' It is classified as a "Type 1 oxidized solid".

一方、硝酸銀ブリケットについては、50/60鉄管起
爆試験ではブースタ部の鉄管が破壊されているのみで、
試料の残留が認められることから、「不爆」となり「危
険性態」と評価される。また、500g燃焼試験では約
90程度度燃焼した。この燃焼によりすべての木粉は燃
え尽きたものの、はとんどの硝酸銀は残留していること
が確認された。従って、500g燃焼試験では「燃焼中
断」と判断される。
On the other hand, regarding silver nitrate briquettes, in the 50/60 iron tube detonation test, only the iron tube in the booster section was destroyed.
Since some sample remains, it is considered "non-explosive" and is rated as "hazardous". Also, in a 500g combustion test, it burned approximately 90 degrees. Although all of the wood powder was burned out by this combustion, it was confirmed that some silver nitrate remained. Therefore, in the 500g combustion test, it is determined that "combustion is interrupted."

従って、硝酸銀ブリケットは「危険性態」となり、「非
危険物」と評価される。
Therefore, silver nitrate briquettes are in a "hazardous state" and are evaluated as a "non-hazardous material."

尚、前記試験方法については、法規に則り定められた前
記危険性評価試験所の定める「不安定性物質の危険性評
価試験方法」に紹介されている。
The above test method is introduced in the ``Danger Evaluation Test Method for Unstable Substances'' established by the above-mentioned Hazard Evaluation Laboratory, which is regulated in accordance with laws and regulations.

以上述べたように本発明に沿って調製された硝酸銀ブリ
ケットは、 (1)造粒することによって危険性が消え、造粒後は一
般薬品としての取扱いが可能になる。
As described above, the silver nitrate briquettes prepared according to the present invention are as follows: (1) The danger disappears by granulation, and after granulation, the silver nitrate briquettes can be handled as general chemicals.

(2)ブリケット形態を採ることによって、取扱い性が
甚だ向上し、輸送、包装或は供給操作が簡便になり、自
動化、連続化更に定量化が容易になる。
(2) By adopting the briquette form, handling properties are greatly improved, transportation, packaging, and supply operations are simplified, and automation, continuity, and quantification are facilitated.

(3)ブリケット形態を選ぶことによって、溶解速度の
制御が再現性よく確実になり、工程の進捗が安定する。
(3) By selecting the briquette form, the dissolution rate can be reliably controlled with good reproducibility, and the process progress can be stabilized.

(4)容器その他の器壁への固着、固結塊の生成がなく
、ロスが減少しかつ取扱い工数が減る。
(4) There is no adhesion to the walls of containers or other vessels, and no formation of solidified lumps, reducing losses and reducing handling man-hours.

(5)硝酸銀微粉塵による人体の傷害、作業環境の汚損
がなくなる。
(5) Eliminates human injury and pollution of the working environment due to silver nitrate fine dust.

等の数々のメリットを有している。It has many advantages such as.

(実施例) 次に実施例を示し説明する。(Example) Next, examples will be shown and explained.

従来の方法によって純度のよい大結晶硝酸銀を析出させ
、0.1〜3+n+nの範囲にブロードな分布をもつ微
粒片に破砕し、洗浄、遠心脱水し、含水率0.13vt
%とし、第1図に示すブリケラティングマシーン(ブリ
ケッタ■;新東工業(株)製)を用い、径9mm、30
gのブリケットとし、褐色のガス不透性ラミネート処理
を施した厚手ビニル袋に密封した。この状態で30日に
及ぶ明所室内放置によって固結を起こすことはなかった
。かつ物性、化学性及び純度にも変化がなく、更に化学
的に甚だ鋭敏な写真感光材料用の硝酸銀として何らの問
題も生じなかった。
Large crystalline silver nitrate with good purity is precipitated by a conventional method, crushed into fine particles with a broad distribution in the range of 0.1 to 3+n+n, washed and centrifugally dehydrated to have a water content of 0.13vt.
%, and using a briquetting machine (briquette ■; manufactured by Shinto Kogyo Co., Ltd.) shown in Fig. 1, a diameter of 9 mm, 30
briquettes and sealed in a thick vinyl bag treated with a brown gas-impermeable laminate. In this state, no caking occurred when left in a bright room for 30 days. Moreover, there were no changes in physical properties, chemical properties, or purity, and furthermore, no problems occurred as silver nitrate for use in chemically extremely sensitive photographic materials.

方前記大結晶硝酸銀を従来の形態に従って含水率0.1
3wt%の2mm以下の微粒片とし前記ビニル袋に密封
した比較試料は僅か3日で固結を起こした。
The large crystalline silver nitrate was prepared according to the conventional form with a water content of 0.1.
A comparative sample containing 3 wt % of fine particles of 2 mm or less and sealed in the above-mentioned vinyl bag solidified in just 3 days.

また実施例、比較例の試料の危険性については前記の通
りであった。
Further, the risks of the samples of Examples and Comparative Examples were as described above.

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

第1図は本発明に使用されるブリケラティングマシーン
の概要図である。 2・・・脱気槽、  4・・・テーバスクリュー5・・
・高圧ニーダロール対、 51及び52・・高圧ニーダロール、 6・・・ポケット R・・・原料、  B・・・ブリケット。
FIG. 1 is a schematic diagram of a briquetting machine used in the present invention. 2... Deaeration tank, 4... Taber screw 5...
- High pressure kneader roll pair, 51 and 52... High pressure kneader roll, 6... Pocket R... Raw material, B... Briquette.

Claims (3)

【特許請求の範囲】[Claims] (1)硝酸塩微粒片原料から乾式圧縮成形された硝酸塩
ブリケット。
(1) Nitrate briquettes formed by dry compression molding from raw nitrate fine particles.
(2)硝酸塩微粒片原料を用い乾式圧縮成形することを
特徴とする硝酸塩ブリケットの製造方法。
(2) A method for producing nitrate briquettes, which comprises dry compression molding using a raw material of nitrate fine particles.
(3)前記製造方法において、硝酸塩微粒片原料に予め
脱気処理を施し乾式圧縮成形にかけることを特徴とする
請求項2に記載の硝酸塩ブリケットの製造方法。
(3) The method for producing nitrate briquettes according to claim 2, characterized in that in the production method, the raw material of nitrate fine particles is previously deaerated and subjected to dry compression molding.
JP1089310A 1989-04-07 1989-04-07 Nitrate briquette and method for producing the same Expired - Lifetime JP2729316B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1089310A JP2729316B2 (en) 1989-04-07 1989-04-07 Nitrate briquette and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1089310A JP2729316B2 (en) 1989-04-07 1989-04-07 Nitrate briquette and method for producing the same

Publications (2)

Publication Number Publication Date
JPH02267107A true JPH02267107A (en) 1990-10-31
JP2729316B2 JP2729316B2 (en) 1998-03-18

Family

ID=13967097

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2729316B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5240669A (en) * 1989-12-28 1993-08-31 Sumitomo Rubber Industries, Ltd. Method for vulcanizing an elastomeric product including alternate heating and pressurizing steps
US5364418A (en) * 1992-03-09 1994-11-15 Eastman Kodak Company Process for compacting silver nitrate
JP2008546615A (en) * 2005-06-15 2008-12-25 エスエヌペーウー マテリオー エネルジェティク Pyrotechnics and dry manufacturing method of pyrotechnics
JP2009511411A (en) * 2005-10-13 2009-03-19 エスエヌペーウー マテリオー エネルジェティク High-speed gas generating agent and method for producing the same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6221701A (en) * 1985-07-23 1987-01-30 Sumitomo Cement Co Ltd Method for continuous production of ultrafine metal oxide powder and apparatus therefor

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6221701A (en) * 1985-07-23 1987-01-30 Sumitomo Cement Co Ltd Method for continuous production of ultrafine metal oxide powder and apparatus therefor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5240669A (en) * 1989-12-28 1993-08-31 Sumitomo Rubber Industries, Ltd. Method for vulcanizing an elastomeric product including alternate heating and pressurizing steps
US5364418A (en) * 1992-03-09 1994-11-15 Eastman Kodak Company Process for compacting silver nitrate
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