JPH0710333B2 - Exhaust reducing agent onboard manufacturing method and apparatus - Google Patents
Exhaust reducing agent onboard manufacturing method and apparatusInfo
- Publication number
- JPH0710333B2 JPH0710333B2 JP3091769A JP9176991A JPH0710333B2 JP H0710333 B2 JPH0710333 B2 JP H0710333B2 JP 3091769 A JP3091769 A JP 3091769A JP 9176991 A JP9176991 A JP 9176991A JP H0710333 B2 JPH0710333 B2 JP H0710333B2
- Authority
- JP
- Japan
- Prior art keywords
- reformer
- reducing agent
- catalyst
- fuel oil
- ship
- 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 - Fee Related
Links
Landscapes
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Liquid Carbonaceous Fuels (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、船舶内の内燃機関の燃
料油自体で、この内燃機関の排気ガスを無害化するため
の還元剤を船内で製造する方法及び装置に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for producing onboard a reducing agent for detoxifying exhaust gas of an internal combustion engine by using fuel oil for the internal combustion engine in the vessel.
【0002】[0002]
【従来の技術】内燃機関の排気ガスには、窒素酸化物
(NOx)などの有害物質が含まれており、社会環境問
題のみならず、地球規模の環境問題を提起しており、船
用内燃機関の排出するNOxも低減しなければならない
という傾向は、時代の進展とともに強まって行く。従
来、脱硝装置には、還元剤として通常、アンモニアが使
用されることはよく知られている。また、排気ガスの脱
硝用還元剤として、低級炭化水素を用いる方法もよく知
られている(例えば、特開昭53−26270号公報参
照)。また、最近、ディーゼル車などの排気ガス中のN
Oxを、触媒として銅‐ゼオライト系のものを用い、還
元剤としてセタン(C16H34)を用いて除去する方法が
提案されている(技研新聞情報、平成2年11月14日
号)。炭化水素を軽質化する方法として、接触分解法が
知られており、石油精製工場において、ガソリン、軽油
などの製造に用いられている。2. Description of the Related Art Exhaust gas from an internal combustion engine contains harmful substances such as nitrogen oxides (NOx) and poses not only social and environmental problems but also global environmental problems. The tendency that NOx emitted by the automobile must also be reduced increases with the progress of the times. Conventionally, it is well known that ammonia is usually used as a reducing agent in a denitration device. Further, a method of using a lower hydrocarbon as a reducing agent for denitration of exhaust gas is also well known (see, for example, JP-A-53-26270). In addition, recently, N in the exhaust gas of diesel vehicles etc.
A method for removing Ox using a copper-zeolite-based catalyst as a catalyst and cetane (C 16 H 34 ) as a reducing agent has been proposed (GIKEN Shimbun Information, November 14, 1990 issue). A catalytic cracking method is known as a method for making hydrocarbons lighter, and is used in the production of gasoline, light oil, etc. in an oil refining plant.
【0003】[0003]
【発明が解決しようとする課題】還元剤としてアンモニ
アを用いる方法では、アンモニアを船舶、車両のような
密閉した空間で使用する場合、漏気し、爆発・火災など
を起こす可能性がある。また、相当量の貯蔵スペースが
占有される。さらにアンモニアはガス中のSO3と反応
して、脱硝装置の機能が低下する。また、上記の文献に
は、有効な排気還元剤を、船舶内の内燃機関の燃料油自
体から、船内で発生する熱源を利用して製造するという
技術的思想は、何も示唆されていない。本発明は、上記
の諸点に鑑みなされたもので、船舶内で発生する排気ガ
ス、燃焼ガス、スチームなどを熱源とするリフォーマ
に、内燃機関用燃料タンクの燃料油の一部を供給し、触
媒を用いて分解・改質して、排気ガス処理用に適した還
元剤を製造する方法及び装置を提供することを目的とす
るものである。In the method of using ammonia as a reducing agent, when ammonia is used in a sealed space such as a ship or a vehicle, there is a possibility of leaking air, causing an explosion or a fire. Also, a considerable amount of storage space is occupied. Furthermore, the ammonia reacts with SO 3 in the gas, and the function of the denitration device deteriorates. Further, the above document does not suggest any technical idea of manufacturing an effective exhaust gas reducing agent from fuel oil itself of an internal combustion engine in a ship by utilizing a heat source generated in the ship. The present invention has been made in view of the above points, and supplies a part of fuel oil of a fuel tank for an internal combustion engine to a reformer that uses exhaust gas generated in a ship, combustion gas, steam or the like as a heat source, and a catalyst. An object of the present invention is to provide a method and an apparatus for producing a reducing agent suitable for exhaust gas treatment by decomposing and reforming by using.
【0004】[0004]
【課題を解決するための手段】上記の目的を達成するた
めに、本発明の排気還元剤の船内製造方法は、つぎの
(a)〜(d)の4工程、すなわち、(a) 船舶内の
内燃機関に供給する燃料油(重油)の一部及び触媒をリ
フォーマに供給する工程、(b) リフォーマに、船舶
内で発生した熱源を供給する工程、(c) 上記
(a)、(b)の工程により、燃料油を軽質化して、船
舶内の内燃機関からの排気ガスの脱硝還元剤用炭化水素
を得る工程、(d) リフォーマの残渣油から触媒を分
離した後、残渣油を燃料油に混入させる工程、を包含す
ることを特徴としている。また、本発明の排気還元剤の
船内製造装置は、図面を参照して説明すれば、船舶内で
発生した熱源を導入する管群22、46を内部に備える
リフォーマ12と、 リフォーマ12と船舶内の内燃機
関20用の燃料油タンク28とを接続する還元剤原料供
給管30と、リフォーマ12に接続された触媒ホッパ1
4と、リフォーマ12で軽質化された炭化水素を脱硝装
置24へ供給するための還元剤抜出・供給管38と、リ
フォーマ12の底部と燃料油タンク28とを接続する残
渣油抜出・循環導管42と、残渣油抜出・循環導管42
に設けられた触媒分離手段と、を包含することを特徴と
している。本願明細書におけるリフォーマとは、重油の
ような高級炭化水素を加熱し、触媒と接触させて低級炭
化水素に分解・改質する装置を指称し、接触分解装置
(クラッカ)に近いものである。In order to achieve the above-mentioned object, the method for producing an exhaust gas reducing agent according to the present invention has the following four steps (a) to (d), that is, (a) Of supplying a part of the fuel oil (heavy oil) and the catalyst supplied to the internal combustion engine to the reformer, (b) supplying the heat source generated in the ship to the reformer, (c) above (a), (b) ) Process to lighten the fuel oil to obtain hydrocarbons for denitration reducing agent of exhaust gas from the internal combustion engine in the ship, (d) after separating the catalyst from the reformer residual oil, the residual oil is fueled And a step of mixing with oil. Further, the on-board manufacturing apparatus for an exhaust gas reducing agent of the present invention will be described with reference to the drawings. The reformer 12 includes therein the tube groups 22 and 46 for introducing the heat source generated in the ship, the reformer 12, and the inside of the ship. Reducing agent raw material supply pipe 30 that connects to the fuel oil tank 28 for the internal combustion engine 20 and the catalyst hopper 1 that is connected to the reformer 12.
4, a reducing agent extraction / supply pipe 38 for supplying the hydrocarbon lightened by the reformer 12 to the denitration device 24, and a residual oil extraction / circulation connecting the bottom of the reformer 12 and the fuel oil tank 28. Conduit 42 and residual oil extraction / circulation conduit 42
And a catalyst separating means provided in the. The reformer in the specification of the present application refers to a device that heats a higher hydrocarbon such as heavy oil and decomposes and reforms it into a lower hydrocarbon by contacting it with a catalyst, and is close to a catalytic cracking device (cracker).
【0005】[0005]
【作用】リフォーマ12に、燃料油タンク28からの燃
料油(重油)が還元剤原料として供給されるとともに、
触媒ホッパ14から触媒粒子が投入され、同時に、内燃
機関20の排気ガスの一部、又は排気ガスの一部と補助
燃焼機44からのスチームもしくは燃焼ガス、又は廃ガ
スボイラ26及び/又は補助ボイラ48からのスチーム
が熱源として供給される。リフォーマ12内で、燃料油
は軽質化され、軽質化された炭化水素は脱硝装置24へ
供給されて、排気ガスと接触し、排気ガス中のNOxは
窒素と酸素に効率よく転換する。The fuel oil (heavy oil) from the fuel oil tank 28 is supplied to the reformer 12 as a reducing agent raw material, and
The catalyst particles are fed from the catalyst hopper 14, and at the same time, a part of the exhaust gas of the internal combustion engine 20, or a part of the exhaust gas and steam or combustion gas from the auxiliary combustor 44, or the waste gas boiler 26 and / or the auxiliary boiler 48. Steam from is supplied as a heat source. In the reformer 12, the fuel oil is lightened and the lightened hydrocarbons are supplied to the denitration device 24 and contact with the exhaust gas, and NOx in the exhaust gas is efficiently converted into nitrogen and oxygen.
【0006】[0006]
【実施例】以下、図面を参照して本発明の好適な実施例
を詳細に説明する。ただし、この実施例に記載されてい
る構成機器の形状、その相対配置などは、とくに特定的
な記載がない限りは、本発明の範囲をそれらのみに限定
する趣旨のものではなく、単なる説明例にすぎない。 実施例1 本実施例における排気還元剤の船内製造装置は、図1に
示すように、排気分配器10、リフォーマ12、触媒ホ
ッパ14、触媒回収機16、フィルタ18などからな
る。排気分配器10は、船舶用の内燃機関20の排気ガ
ス導管に接続され、排気ガスを2系統の配管に分岐させ
るものである。そして、排気ガスの一方の系統の配管の
先に管群22が形成され、この管群22はリフォーマ1
2の内部に備えられる。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described in detail below with reference to the drawings. However, the shape of the constituent devices described in this embodiment, the relative arrangement thereof, and the like, unless otherwise specified, are not intended to limit the scope of the present invention only to them, but merely illustrative examples. Nothing more. Embodiment 1 As shown in FIG. 1, the onboard manufacturing apparatus for an exhaust gas reducing agent in this embodiment comprises an exhaust distributor 10, a reformer 12, a catalyst hopper 14, a catalyst recovery machine 16, a filter 18, and the like. The exhaust distributor 10 is connected to an exhaust gas conduit of an internal combustion engine 20 for a ship and branches the exhaust gas into two pipes. Then, a pipe group 22 is formed at the tip of one of the exhaust gas pipes, and the pipe group 22 is formed by the reformer 1
It is equipped inside 2.
【0007】内燃機関20から排出される排気ガスの一
部は、リフォーマ12へ分配・導入され、リフォーマ1
2での触媒との接触反応に必要な熱源とされる。リフォ
ーマ12を通過した排気ガスは、排気分配器10により
分配された残部の排気ガスに合流して、ともに脱硝装置
24を通って脱硝され、ついで、廃ガスボイラ26で熱
回収された後、煙突(図示せず)から排出される。内燃
機関用の船舶内の燃料油タンク28から、A重油、B重
油又はC重油が還元剤製造の原料として、還元剤原料供
給管30を介してリフォーマ12に送られ、リフォーマ
12では適当な温度、圧力の制御の下で、触媒ホッパ1
4から供給されるシリカ・アルミナなどの触媒粒子と接
触反応させて、より軽質の炭化水素に分解・改質する。
精製された炭化水素はコンデンサ32で凝集され、遠心
分離機などの触媒回収機34及び触媒フィルタ36を通
った後、脱硝装置24に供給され、還元剤として使用さ
れる。38は還元剤抜出・供給管、40は内燃機関への
燃料油供給管である。A part of the exhaust gas discharged from the internal combustion engine 20 is distributed to and introduced into the reformer 12, and the reformer 1
It is used as a heat source necessary for the catalytic reaction with the catalyst in 2. The exhaust gas that has passed through the reformer 12 joins with the remaining exhaust gas distributed by the exhaust distributor 10, is denitrified through the denitration device 24, and is then heat-recovered by the waste gas boiler 26, and then the chimney ( (Not shown). From a fuel oil tank 28 in a vessel for an internal combustion engine, heavy fuel oil A, heavy fuel oil B or heavy fuel oil C is sent to a reformer 12 as a raw material for producing a reducing agent through a reducing agent raw material supply pipe 30, and at an appropriate temperature in the reformer 12. , Under control of pressure, catalyst hopper 1
4, catalytically reacts with catalyst particles such as silica and alumina supplied from No. 4, and decomposes and reforms into lighter hydrocarbons.
The purified hydrocarbons are condensed in the condenser 32, passed through the catalyst recovery device 34 such as a centrifugal separator and the catalyst filter 36, and then supplied to the denitration device 24 and used as a reducing agent. 38 is a reducing agent extraction / supply pipe, and 40 is a fuel oil supply pipe to the internal combustion engine.
【0008】上記は、精製された炭化水素をコンデンサ
32で一旦凝縮した後、液体状で脱硝装置24に供給す
る場合であるが、精製された炭化水素を液化することな
く、そのまま気体状で脱硝装置24に供給することも可
能である。この場合は、コンデンサ32、触媒回収機3
4、触媒フィルタ36が不要となる。また、リフォーマ
12の底部と燃料油タンク28とは、残渣油(スラリ
ー)抜出・循環導管42を介して接続され、この導管4
2に遠心分離機などの触媒回収機16及び触媒フィルタ
18などからなる触媒分離手段が設けられる。リフォー
マ12としては、例えば、大型石油精製プラントである
FCC装置(接触分解装置)などの原理を適用の上、簡
易化した流動床方式あるいは移動床方式などが考えられ
る。リフォーマ12の底部から出て来るスラリー(残渣
油)は、前述のように、別の触媒回収機16と触媒フィ
ルタ18で触媒を回収した後、燃料油タンク28へ戻さ
れ、内燃機関用燃料として使用される。なお、リフォー
マのコンデンサ32は、海水ラインなどの別系統の冷却
手段で冷却される。上記の各機器は、すべて船舶内に設
置される。本実施例では、内燃機関の排気ガスをリフォ
ーマの熱源として有効に利用できるという利点がある。The above is the case where the purified hydrocarbon is once condensed in the condenser 32 and then supplied to the denitration device 24 in a liquid state. However, the purified hydrocarbon is deliquefied in a gaseous state as it is without liquefying it. It is also possible to supply the device 24. In this case, the condenser 32 and the catalyst recovery machine 3
4. The catalyst filter 36 becomes unnecessary. The bottom of the reformer 12 and the fuel oil tank 28 are connected to each other via a residual oil (slurry) extraction / circulation conduit 42.
2 is provided with a catalyst separating means including a catalyst recovering device 16 such as a centrifugal separator and a catalyst filter 18. As the reformer 12, for example, a simplified fluidized bed system or moving bed system can be considered by applying the principle of an FCC device (catalytic cracking device) which is a large oil refining plant. As described above, the slurry (residual oil) coming out from the bottom of the reformer 12 is returned to the fuel oil tank 28 after the catalyst is recovered by another catalyst recovery device 16 and the catalyst filter 18, and is used as fuel for the internal combustion engine. used. The condenser 32 of the reformer is cooled by a cooling means of another system such as a seawater line. All of the above devices are installed in the ship. The present embodiment has an advantage that the exhaust gas of the internal combustion engine can be effectively used as the heat source of the reformer.
【0009】実施例2 本実施例の排気還元剤の船内製造装置は、図2に示すよ
うに、リフォーマ12内に、内燃機関20からの排気ガ
スの管群22を設けるとともに、油焚きボイラ、燃焼ガ
ス発生機などの補助燃焼機44からのスチーム又は燃焼
ガスの管群46を設けたものである。本実施例では、内
燃機関20が軽負荷状態などの場合に、手軽に熱源を得
ることができるという利点がある。他の構成、作用は実
施例1の場合と同様である。Embodiment 2 As shown in FIG. 2, the apparatus for manufacturing an exhaust gas reducing agent according to the present embodiment has a reformer 12 in which a pipe group 22 for exhaust gas from an internal combustion engine 20 is provided and an oil-fired boiler, A tube group 46 of steam or combustion gas from an auxiliary combustor 44 such as a combustion gas generator is provided. The present embodiment has an advantage that the heat source can be easily obtained when the internal combustion engine 20 is in a light load state or the like. Other configurations and operations are similar to those of the first embodiment.
【0010】実施例3 本実施例の排気還元剤の船内製造装置は、内燃機関から
の排気ガスを排気分配器で分配してリフォーマの熱源と
する代わりに、図3に示すように、廃ガスボイラ26
に、追焚き油焚きボイラなどの補助ボイラ48を設け、
廃ガスボイラ26及び補助ボイラ48からのスチーム
を、リフォーマ12内の管群22に供給するようにした
ものである。本実施例では、内燃機関20の負荷に影響
されることなく、リフォーマ12の熱源を得ることがで
きるという利点がある。他の構成、作用は実施例1の場
合と同様である。Embodiment 3 The on-board manufacturing apparatus for an exhaust gas reducing agent according to this embodiment uses an exhaust gas boiler as shown in FIG. 3, instead of distributing exhaust gas from an internal combustion engine by an exhaust distributor to use as a heat source for a reformer. 26
Is provided with an auxiliary boiler 48 such as a reheating oil-fired boiler,
The steam from the waste gas boiler 26 and the auxiliary boiler 48 is supplied to the pipe group 22 in the reformer 12. The present embodiment has an advantage that the heat source of the reformer 12 can be obtained without being affected by the load of the internal combustion engine 20. Other configurations and operations are similar to those of the first embodiment.
【0011】[0011]
【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。 (1) 内燃機関の燃料油と還元剤の原料とは、同一の
燃料油タンクに貯蔵できるので、原料は容易に入手でき
る上、船舶内でも容易に取り扱うことができる。 (2) アンモニアを還元剤として使用する場合と異な
り、硫酸アンモニウムの生成がなく、脱硝装置の機能低
下が著しく軽減する。 (3) 船舶内においては、通常、燃料油タンクはA重
油タンクとC重油タンクとがあり、還元剤原料としてA
重油を使用すれば、還元能力の強い軽質分を容易に取り
出すことができる。Since the present invention is configured as described above, it has the following effects. (1) Since the fuel oil of the internal combustion engine and the raw material of the reducing agent can be stored in the same fuel oil tank, the raw material can be easily obtained and can be easily handled in a ship. (2) Unlike the case where ammonia is used as a reducing agent, ammonium sulfate is not generated, and the functional deterioration of the denitration device is remarkably reduced. (3) In a ship, a fuel oil tank usually has an A heavy oil tank and a C heavy oil tank, and A is used as a reducing agent raw material.
If heavy oil is used, it is possible to easily take out light components having a strong reducing ability.
【図1】本発明の排気還元剤の船内製造装置の一実施例
を示す系統説明図である。FIG. 1 is a system explanatory view showing an embodiment of an onboard manufacturing apparatus for an exhaust gas reducing agent of the present invention.
【図2】本発明の装置の他の実施例を示す系統説明図で
ある。FIG. 2 is a system diagram showing another embodiment of the device of the present invention.
【図3】本発明の装置のさらに他の実施例を示す系統説
明図である。FIG. 3 is a system explanatory view showing still another embodiment of the device of the present invention.
10 排気分配器 12 リフォーマ 14 触媒ホッパ 16 触媒回収機 18 触媒フィルタ 20 内燃機関 22 管群 24 脱硝装置 26 廃ガスボイラ 28 燃料油タンク 30 還元剤原料供給管 32 コンデンサ 34 触媒回収機 36 触媒フィルタ 38 還元剤抜出・供給管 40 燃料油供給管 42 残渣油抜出・循環導管 44 補助燃焼機 46 管群 48 補助ボイラ 10 Exhaust Distributor 12 Reformer 14 Catalyst Hopper 16 Catalyst Recovery Machine 18 Catalyst Filter 20 Internal Combustion Engine 22 Tube Group 24 Denitration Device 26 Waste Gas Boiler 28 Fuel Oil Tank 30 Reductant Raw Material Supply Pipe 32 Condenser 34 Catalyst Recovery Machine 36 Catalyst Filter 38 Reducing Agent Extraction / supply pipe 40 Fuel oil supply pipe 42 Residual oil extraction / circulation pipe 44 Auxiliary combustor 46 Tube group 48 Auxiliary boiler
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B63H 21/32 B01D 53/36 101 Z ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location B63H 21/32 B01D 53/36 101 Z
Claims (2)
ち、(a) 船舶内の内燃機関に供給する燃料油の一部
及び触媒をリフォーマに供給する工程、(b) リフォ
ーマに、船舶内で発生した熱源を供給する工程、(c)
上記(a)、(b)の工程により、燃料油を軽質化し
て、船舶内の内燃機関からの排気ガスの脱硝還元剤用炭
化水素を得る工程、(d) リフォーマの残渣油から触
媒を分離した後、残渣油を燃料油に混入させる工程、を
包含することを特徴とする排気還元剤の船内製造方法。1. The following four steps (a) to (d), namely, (a) a step of supplying a part of fuel oil to be supplied to an internal combustion engine in a ship and a catalyst to a reformer, and (b) a reformer. A step of supplying a heat source generated in the ship, (c)
By the above steps (a) and (b), the fuel oil is lightened to obtain hydrocarbons for the denitration reducing agent of the exhaust gas from the internal combustion engine in the ship, (d) the catalyst is separated from the residual oil of the reformer And then mixing the residual oil with the fuel oil.
(22)、(46)を内部に備えるリフォーマ(12)
と、リフォーマ(12)と船舶内の内燃機関(20)用
の燃料油タンク(28)とを接続する還元剤原料供給管
(30)と、リフォーマ(12)に接続された触媒ホッ
パ(14)と、リフォーマ(12)で軽質化された炭化
水素を脱硝装置(24)へ供給するための還元剤抜出・
供給管(38)と、リフォーマ(12)の底部と燃料油
タンク(28)とを接続する残渣油抜出・循環導管(4
2)と、残渣油抜出・循環導管(42)に設けられた触
媒分離手段と、を包含することを特徴とする排気還元剤
の船内製造装置。2. A reformer (12) having therein pipe groups (22), (46) for introducing a heat source generated in a ship.
And a reducing agent raw material supply pipe (30) connecting the reformer (12) to a fuel oil tank (28) for an internal combustion engine (20) in a ship, and a catalyst hopper (14) connected to the reformer (12). And withdrawal of reducing agent for supplying the hydrocarbon lightened by the reformer (12) to the denitration device (24).
A residual oil extraction / circulation conduit (4) connecting the supply pipe (38), the bottom of the reformer (12) and the fuel oil tank (28).
2) and a catalyst separating means provided in the residual oil extraction / circulation conduit (42), and an onboard manufacturing apparatus for an exhaust gas reducing agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3091769A JPH0710333B2 (en) | 1991-03-28 | 1991-03-28 | Exhaust reducing agent onboard manufacturing method and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3091769A JPH0710333B2 (en) | 1991-03-28 | 1991-03-28 | Exhaust reducing agent onboard manufacturing method and apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04300629A JPH04300629A (en) | 1992-10-23 |
| JPH0710333B2 true JPH0710333B2 (en) | 1995-02-08 |
Family
ID=14035779
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3091769A Expired - Fee Related JPH0710333B2 (en) | 1991-03-28 | 1991-03-28 | Exhaust reducing agent onboard manufacturing method and apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0710333B2 (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6012985B2 (en) | 2012-02-28 | 2016-10-25 | 株式会社吉野工業所 | Tube container |
-
1991
- 1991-03-28 JP JP3091769A patent/JPH0710333B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6012985B2 (en) | 2012-02-28 | 2016-10-25 | 株式会社吉野工業所 | Tube container |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04300629A (en) | 1992-10-23 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |