JP2006256930A - Environment cleaning formed article and its producing method - Google Patents

Environment cleaning formed article and its producing method Download PDF

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JP2006256930A
JP2006256930A JP2005079187A JP2005079187A JP2006256930A JP 2006256930 A JP2006256930 A JP 2006256930A JP 2005079187 A JP2005079187 A JP 2005079187A JP 2005079187 A JP2005079187 A JP 2005079187A JP 2006256930 A JP2006256930 A JP 2006256930A
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bamboo
charcoal
furnace
white
black
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金藏 ▼高▼杉
Kinzo Takasugi
Hisao Negishi
久夫 根岸
Hajime Nakada
中田  肇
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an environment cleaning formed article which exhibits synergistically respective positive effects of bamboo black charcoal, bamboo white charcoal and zeolite and maintains the synergistic positive effect semipermanently, and which can be formed into a desired shape; and a method for producing the same. <P>SOLUTION: The environment cleaning formed article α used for improving the environment is obtained by kneading 30-25 wt% of a bamboo black charcoal powder 1, 30-25 wt% of a bamboo white charcoal powder 2, and 40-50 wt% of a zeolite powder 3 together with water, then extrusion molding the kneaded material into spherical granules, and sintering the granules. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、居住・生活空間等の屋内気中、水中、土中の環境改善に利用される環境浄化成形体及びその製造方法に係り、詳細には、環境改善に有効な効能を相乗的に発揮且つ半永久的に持続可能であるとともに、所望の形状に成形可能である環境浄化成形体及びその製造方法に関する。   The present invention relates to an environmental purification molded body used for improving the environment in indoor air, water, and soil, such as a living / living space, and a manufacturing method thereof, and more specifically, synergistically effective efficacy for environmental improvement. The present invention relates to an environmental purification molded body that can be exhibited and semipermanently sustainable and can be molded into a desired shape, and a method for manufacturing the same.

近年、地球環境等の問題に対する関心の高まりにより、省エネ対策等の観点から、住居やオフィス等の居住・生活空間の高気密化・高断熱化が促進されている。   In recent years, due to increasing interest in problems such as the global environment, airtightness and high thermal insulation of residences and living spaces such as houses and offices have been promoted from the viewpoint of energy saving measures.

一方、これに伴い居住・生活空間の換気回数やその機会が大幅に減ることで、同空間内にプラスイオンが過剰になり、臭気が発生するなどの弊害が齎されている。さらに、居住・生活空間内に設置された家電製品やOA機器等が電磁波を放射するため、それに拍車が掛かっている。   On the other hand, due to this, the number of ventilations and the chances of living / living space are greatly reduced, and there are problems such as excessive positive ions in the space and odor generation. In addition, home appliances and OA devices installed in living and living spaces radiate electromagnetic waves, which has spurred it.

そこで、このような悪循環を解消する一環として、炭焼き窯内で生成された竹炭の粉末、ゼオライト粉末、及び粘土からなる混合物に水を加えて所望の形状に成形後、その炭焼き窯内で焼結することにより構成される多孔質セラミックが開示されている。
特開2004−339042号公報
Therefore, as a part of eliminating such a vicious circle, water is added to a mixture of bamboo charcoal powder, zeolite powder, and clay produced in a charcoal kiln and molded into a desired shape and then sintered in the charcoal kiln. A porous ceramic constructed by doing so is disclosed.
JP 2004-339042 A

ところで、近年、竹炭の中で竹黒炭や竹白炭がそれぞれ特異の機能性の高さから注目されており、それらの使用が強く要望されている。ところが、炭焼き窯内の細かな温調が殆ど不可能である故に温度ムラが不可避であるとともに、窯内に塵等の不純物が浮遊等する状態で炭化物の生成が行われるため、上記文献の開示技術は高純度且つ高品質な竹黒炭の均質量産に不向きである。まして、炭焼き窯内の最高到達温度を800℃としているため、その開示技術では竹白炭の生成自体不可能である。   By the way, in recent years, bamboo black charcoal and bamboo white charcoal are attracting attention among bamboo charcoal because of their unique high functionality, and their use is strongly desired. However, since fine temperature control in the charcoal kiln is almost impossible, temperature unevenness is unavoidable, and carbides are generated in a state where impurities such as dust float in the kiln, so the disclosure of the above document is disclosed. The technology is not suitable for homogeneous mass production of high purity and high quality bamboo black charcoal. In addition, since the maximum temperature reached in the charcoal kiln is 800 ° C., the disclosed technology cannot produce bamboo white charcoal.

そもそも上記文献では、竹白炭の特徴やその製造方法等に関する記載及びその示唆が一切見られないばかりか、炭焼き窯内最高到達温度のかかる設定値から、良質な竹炭として想定されているものは、精々竹黒炭(炭化温度が約700℃)までである。従って、同文献の開示技術によれば、竹白炭が多孔質セラミックの素材に採用されることはない。   In the first place, in the above document, there is no description about the characteristics of bamboo white charcoal and its manufacturing method and its suggestion, and what is assumed as a good quality bamboo charcoal from the set value that requires the highest temperature in the charcoal kiln, Up to bamboo charcoal (carbonization temperature is about 700 ° C). Therefore, according to the disclosed technique of the same document, bamboo white charcoal is not employed as the material for the porous ceramic.

そこで、仮に竹黒炭や竹白炭、ゼオライトそれぞれを別個に利用するとしても、竹黒炭や竹白炭は、プラスイオンをその除去のため吸着し得る微細孔の数が有限であるとともに、文字通り「炭」であるため壊れ易いことから、使用可能な期間には限度がある。そのため、目標の環境改善を達成するまで、竹黒炭や竹白炭をその効能が切れたり、壊れたりする度に入手する必要があり、煩わしい。   Therefore, even if bamboo black charcoal, bamboo white charcoal, and zeolite are separately used, bamboo black charcoal and bamboo white charcoal have a finite number of micropores that can adsorb positive ions for their removal, and literally "charcoal" Therefore, the usable period is limited. Therefore, it is necessary to obtain bamboo black charcoal and bamboo white charcoal every time their effectiveness is cut or broken until the target environmental improvement is achieved, which is troublesome.

一方、ゼオライトは、陽イオン交換能を有するため、吸着能を長期間に亙り維持可能なものの、加工の困難さから採り得る形状が限定されてしまう。このことは、竹黒炭や竹白炭についてもその壊れ易さ等のため言えることである。   On the other hand, since zeolite has a cation exchange capacity, the adsorption capacity can be maintained over a long period of time, but the shape that can be taken is limited due to the difficulty of processing. This is also true for bamboo black charcoal and bamboo white charcoal due to their fragility.

また、竹黒炭や竹白炭、ゼオライト個々の効能を全て享受するためには、それらを全て入手して使用するとともに、効能が切れたり、壊れたりする度に補充する必要があることから、費用が嵩み極めて不経済的である。   In addition, in order to enjoy all the effects of bamboo black charcoal, bamboo white charcoal, and zeolite, it is necessary to obtain and use all of them, and it is necessary to replenish each time the effect expires or breaks, so there is a cost. Bulky and extremely uneconomical.

ここにおいて、本発明の解決すべき主要な目的は、次のとおりである。
即ち、本発明の第1の目的は、半永久的に使用可能な環境浄化成形体及びその製造方法を提供せんとするものである。
Here, the main objects to be solved by the present invention are as follows.
That is, the first object of the present invention is to provide an environmental purification molded body that can be used semi-permanently and a method for producing the same.

本発明の第2の目的は、様々な形状に成形可能な環境浄化成形体及びその製造方法を提供せんとするものである。   The second object of the present invention is to provide an environmental purification molded body that can be molded into various shapes and a method for producing the same.

本発明の第3の目的は、環境改善に有益な複数の効能を相乗的に発揮可能な環境浄化成形体及びその製造方法を提供せんとするものである。   The third object of the present invention is to provide an environmental purification molded body capable of synergistically exhibiting a plurality of effects useful for environmental improvement and a method for producing the same.

本発明の第4の目的は、高純度且つ高品質な竹黒炭粉末及び竹白炭粉末を成分とする環境浄化成形体及びその製造方法を提供せんとするものである。   The fourth object of the present invention is to provide an environment purification molded article containing high purity and high quality bamboo black charcoal powder and bamboo white charcoal powder as a component and a method for producing the same.

本発明の他の目的は、明細書、図面、特に特許請求の範囲の各請求項の記載から、自ずと明らかとなろう。   Other objects of the present invention will become apparent from the specification, drawings, and particularly the description of each claim.

本発明環境浄化成形体においては、竹黒炭粉末、竹白炭粉末、及びゼオライト粉末を混合形成することで構成される、という特徴的構成手段を講じる。   In the environmental purification molded body of the present invention, the characteristic constitution means that it is constituted by mixing and forming bamboo black charcoal powder, bamboo white charcoal powder, and zeolite powder is taken.

また、本発明環境浄化成形体の製造方法においては、竹黒炭粉末、竹白炭粉末、及びゼオライト粉末を加水混練し、所望の形状に成形後、焼結する、という特徴的構成手段を講じる。   Moreover, in the manufacturing method of an environmental purification molded body of the present invention, characteristic constitution means is taken such that bamboo black charcoal powder, bamboo white charcoal powder, and zeolite powder are hydro-kneaded, molded into a desired shape, and sintered.

さらに、具体的詳細に述べると、当該課題の解決では、本発明が次に列挙する上位概念から下位概念に亙る新規な特徴的構成手段を採用することにより、前記目的を達成するよう為される。   More specifically, in order to solve the problem, the present invention achieves the above-mentioned object by adopting a new characteristic configuration means ranging from the superordinate concept listed below to the subordinate concept. .

即ち、本発明環境浄化成形体の第1の特徴は、所定割合の竹黒炭粉末、竹白炭粉末、及びゼオライト粉末を加水混練し、所望の形状に成形後、焼結することで構成されてなる、環境浄化成形体の構成採用にある。   That is, the first feature of the environmental purification molded body of the present invention is constituted by hydro-kneading a predetermined ratio of bamboo black charcoal powder, bamboo white charcoal powder, and zeolite powder, forming the desired shape, and then sintering. The configuration of the environmental purification molded body is employed.

本発明環境浄化成形体の第2の特徴は、上記本発明環境浄化成形体の第1の特徴における前記竹黒炭粉末、前記竹白炭粉末、及び前記ゼオライト粉末の割合が、順次、組成重量比、30%〜25%、30%〜25%、及び40%〜50%にそれぞれ設定されてなる、環境浄化成形体の構成採用にある。   A second feature of the environmental purification molded body of the present invention is that the ratio of the bamboo black charcoal powder, the bamboo white coal powder, and the zeolite powder in the first characteristic of the environmental purification molded body of the present invention is, in turn, a composition weight ratio, The configuration of the environmental purification molded body is set to 30% to 25%, 30% to 25%, and 40% to 50%, respectively.

本発明環境浄化成形体の第3の特徴は、上記本発明環境浄化成形体の第1又は第2の特徴における前記竹黒炭粉末及び前記竹白炭粉末が、その加工原料を孟宗竹、真竹、苦竹、淡竹を含む竹材としてなる、環境浄化成形体の構成採用にある。   A third feature of the environmental purification molded body of the present invention is that the bamboo black charcoal powder and the bamboo white charcoal powder in the first or second characteristic of the environmental purification molded body of the present invention are processed raw materials, It is in the configuration adoption of an environmental purification molded body that is made of bamboo including light bamboo.

本発明環境浄化成形体の第4の特徴は、上記本発明環境浄化成形体の第1、第2又は第3の特徴における前記竹材が、黒炭化又は白炭化される前に、過マンガン酸カリウム溶液又はニッケルが溶け込んだ硝酸溶液に漬け込まれてなる、環境浄化成形体の構成採用にある。   The fourth feature of the environmental purification molded body of the present invention is that the bamboo material in the first, second or third characteristics of the environmental purification molded body of the present invention is potassium permanganate before being black carbonized or white carbonized. The present invention employs a configuration of an environmental purification molded body that is immersed in a solution or a nitric acid solution in which nickel is dissolved.

本発明環境浄化成形体の第5の特徴は、上記本発明環境浄化成形体の第1、第2、第3又は第4の特徴における前記ゼオライト粉末が、珪酸アルミナ含水塩鉱物(沸石)に焼成処理を施すことで生成されてなる、環境浄化成形体の構成採用にある。   A fifth feature of the environmental purification molded body of the present invention is that the zeolite powder according to the first, second, third or fourth characteristics of the environmental purification molded body of the present invention is calcined into a silicate alumina hydrate salt mineral (zeolite). The present invention is to adopt a configuration of an environmental purification molded body that is generated by processing.

本発明環境浄化成形体の第6の特徴は、上記本発明環境浄化成形体の第1、第2、第3、第4又は第5の特徴における前記形状が、玉粒状を含んでなる、環境浄化成形体の構成採用にある。   A sixth feature of the environmental purification molded body of the present invention is the environment in which the shape in the first, second, third, fourth, or fifth characteristic of the environmental purification molded body of the present invention includes a ball-like shape. It is in the configuration adoption of the purification molded body.

一方、本発明環境浄化成形体の製造方法の第1の特徴は、黒炭化又は白炭化される竹材を加工処理する前工程と、真空引きされた竹炭化炉内で当該竹材をこれが黒炭化する目標温度まで加熱・温調することにより、竹黒炭を生成する竹黒炭生成工程と、真空引きされた前記竹炭化炉内で前記竹材をこれが白炭化する目標温度まで加熱・温調することにより、竹白炭を生成する竹白炭生成工程と、前記竹黒炭及び当該竹白炭を微粉末化する竹炭微粉末化工程と、所定割合の前記竹黒炭及び前記竹白炭それぞれの粉末からなる混合物に所定割合のゼオライト粉末をさらに混入するゼオライト粉末混入工程と、当該ゼオライト粉末混入工程の円滑化のために水を加える第1加水工程と、前記竹黒炭粉末と前記竹白炭粉末と前記ゼオライト粉末とを均等に混練する混練工程と、当該混練工程で得られた混練物に水を加えることで、これに含まれる前記ゼオライト粉末のバインダ作用とともに必要に応じ成形展性作用を現出させる第2加水工程と、当該混練物を所望の形状に成形する成形工程と、当該成形工程で得られた成形物を焼結する焼結工程と、を順次実施してなる、環境浄化成形体の製造方法の構成採用にある。   On the other hand, the first feature of the method for producing an environmental purification molded body of the present invention is that the bamboo material to be black carbonized or white carbonized is processed, and the bamboo material is black carbonized in a vacuum carbonized bamboo carbonization furnace. By heating and adjusting the temperature to the target temperature, the bamboo black charcoal generation step for generating bamboo black charcoal, and by heating and adjusting the temperature to the target temperature at which the bamboo material is white carbonized in the vacuumed bamboo carbonization furnace, Bamboo white charcoal producing step for producing bamboo white charcoal, bamboo charcoal and bamboo charcoal pulverizing step for finely pulverizing said bamboo black charcoal, and a mixture of powder of each of said bamboo black charcoal and said bamboo white charcoal in a predetermined proportion The zeolite powder mixing step for further mixing the zeolite powder, the first hydration step for adding water to facilitate the zeolite powder mixing step, the bamboo black charcoal powder, the bamboo white charcoal powder, and the zeolite powder are averaged. A kneading step for kneading, and a second hydration step for producing a moldability work as needed together with the binder action of the zeolite powder contained therein by adding water to the kneaded product obtained in the kneading process; , Adopting the configuration of the method for producing an environmental purification molded body, which is sequentially performed by a molding process for molding the kneaded product into a desired shape and a sintering process for sintering the molded product obtained in the molding process. It is in.

本発明環境浄化成形体の製造方法の第2の特徴は、上記本発明環境浄化成形体の製造方法の第1の特徴における前記竹黒炭生成工程及び前記竹白炭生成工程が、前記加工処理された前記竹材を前者は約700℃、後者は約1,000℃の炉内温度管理の厳密な峻別の下にそれぞれ焼成されてなる、環境浄化成形体の製造方法の構成採用にある。   According to a second feature of the method for producing an environmental purification molded body of the present invention, the bamboo black coal production step and the bamboo white coal production step in the first feature of the method for producing an environmental purification molded body of the present invention are processed. The bamboo material is fired under the strict distinction of furnace temperature control of about 700 ° C. in the former and about 1,000 ° C. in the latter, respectively.

本発明環境浄化成形体の製造方法の第3の特徴は、上記本発明環境浄化成形体の製造方法の第1又は第2の特徴における前記竹黒炭生成工程及び前記竹白炭生成工程が、前記加工処理された前記竹材を複数収容する前記炉内の真空引き用の排気管と、当該炉内の真空度を検出する真空度検出手段と、当該炉内の温度を検出する温度検出手段と、当該炉内を一様に制御加熱する加熱手段と、を具備した前記竹炭化炉を用いて、前記排気管から前記真空度検出手段の検出値に基づいて、前記加工処理された前記竹材を収容した前記炉内を密封真空雰囲気にするため真空引きする処理手順と、前記温度検出手段の検出値に基づき前記加熱手段を制御することにより、前記炉内に収容された前記加工処理済みの前記竹材が黒炭化又は白炭化する目標温度までそれぞれ前記密封真空雰囲気とした当該炉内を一様に加熱する処理手順と、を含んでなる、環境浄化成形体の製造方法の構成採用にある。   According to a third feature of the method for producing an environmental purification molded body of the present invention, the bamboo black charcoal generation step and the bamboo white charcoal generation step in the first or second characteristic of the method for manufacturing an environmental purification molded body of the present invention are the processing described above. An exhaust pipe for evacuation in the furnace containing a plurality of the processed bamboo materials, a vacuum degree detecting means for detecting the degree of vacuum in the furnace, a temperature detecting means for detecting the temperature in the furnace, and Using the bamboo carbonization furnace equipped with heating means for uniformly heating the inside of the furnace, the processed bamboo material was accommodated from the exhaust pipe based on the detection value of the vacuum degree detection means. A processing procedure for evacuating the inside of the furnace to make a sealed vacuum atmosphere, and controlling the heating means based on the detection value of the temperature detecting means, the processed bamboo material accommodated in the furnace is Target temperature for black carbonization or white carbonization A processing procedure for uniformly heating the respective said sealing vacuum atmosphere was the furnace up, comprising a, in the configuration adopting the manufacturing method of the environmental clean moldings.

本発明環境浄化成形体の製造方法の第4の特徴は、上記本発明環境浄化成形体の製造方法の第1、第2又は第3の特徴における前記竹黒炭生成工程及び前記竹白炭生成工程が、供給された冷却済み窒素ガスを前記炉内にて均等に噴射する窒素ガス噴射手段を、さらに具備した前記竹炭化炉を用いて、前記竹黒炭又は前記竹白炭の生成から間もない前記炉内にて前記窒素ガス噴射手段により前記窒素ガスを均等に噴射する処理手順を、さらに含んでなる、環境浄化成形体の製造方法の構成採用にある。   According to a fourth feature of the method for producing an environmental purification molded body of the present invention, the bamboo black charcoal production step and the bamboo white coal production step in the first, second, or third characteristics of the method for producing an environmental purification molded body of the present invention described above are provided. The furnace immediately after the production of the bamboo black charcoal or the bamboo white charcoal using the bamboo carbonization furnace further comprising nitrogen gas injection means for uniformly injecting the supplied cooled nitrogen gas in the furnace The configuration of the method for producing an environmental purification molded body further includes a processing procedure for uniformly injecting the nitrogen gas by the nitrogen gas injection means.

本発明環境浄化成形体の製造方法の第5の特徴は、上記本発明環境浄化成形体の製造方法の第4の特徴における前記竹白炭生成工程が、外気から取入れた空気を前記炉内にて均等に噴射する空気噴射手段を、さらに具備した前記竹炭化炉を用いて、前記窒素ガス噴射前の前記炉内にて前記空気噴射手段により前記空気を均等に噴射する処理手順を、さらに含んでなる、環境浄化成形体の製造方法の構成採用にある。   According to a fifth feature of the method for producing an environmental purification molded body of the present invention, the bamboo white charcoal producing step in the fourth feature of the method for producing an environmental purification molded body of the present invention is performed by supplying air taken from outside air in the furnace. A processing procedure for evenly injecting the air by the air injection means in the furnace before the nitrogen gas injection using the bamboo carbonization furnace further provided with air injection means for uniformly injecting the air. Thus, the configuration of the manufacturing method of the environmental purification molded body is employed.

本発明環境浄化成形体の製造方法の第6の特徴は、上記本発明環境浄化成形体の製造方法の第1、第2、第3、第4又は第5の特徴における前記前工程が、伐採・切断した前記竹材を一旦乾燥してから所定寸法に割竹し、板状化したものを複数結束する一連の処理手順の実施の後、当該結束した板状竹群を過マンガン酸カリウム溶液又はニッケルが溶け込んだ硝酸溶液に漬け込む処理手順を実施した上で乾燥仕上げする処理手順に至ってなる、環境浄化成形体の製造方法の構成採用にある。   A sixth feature of the method for producing an environmental purification molded body of the present invention is that the preceding step in the first, second, third, fourth, or fifth feature of the method for producing an environmental purification molded body of the present invention described above is felling. The dried bamboo material is once dried and then split to a predetermined size, and after carrying out a series of processing procedures for binding a plurality of plate-like materials, the bound plate-like bamboo group is added to a potassium permanganate solution or The configuration of the method for producing an environmental purification molded body is such that a treatment procedure is carried out after a treatment procedure of dipping in a nitric acid solution in which nickel is dissolved, followed by a drying finish.

本発明に係る環境浄化成形体によれば、竹黒炭粉末、竹白炭粉末、及びゼオライト粉末を混練後に焼結することでセラミック化するため、壊れ難く、非常識な力を加えられて破壊されない限り長持ちする。   According to the environmental purification molded body according to the present invention, since bamboo black charcoal powder, bamboo white charcoal powder, and zeolite powder are ceramicized by sintering after kneading, it is difficult to break, unless insensible force is applied and destroyed. long lasting.

また、本発明に係る環境浄化成形体によれば、竹黒炭粉末、竹白炭粉末、及びゼオライト粉末それぞれの微細孔が共存することで極めて高い吸着能が実現されて、過剰なプラスイオンがそれら微細孔に吸着されるだけでなく、ゼオライト粉末がその触媒作用により、各粉末の微細孔に吸着されたプラスイオンをマイナスイオンに還元する、即ち、マイナスイオンに交換すること(陽イオン交換能)でその微細孔から脱着させるため、各粉末の有効な吸着能を半永久的に持続可能であり、消臭作用、調湿作用、滅菌作用、浄水作用、及びシックハウス防止作用(原因物質のホルムアルデヒド等を除去)等、吸着能からの帰結作用が常に高い水準で発揮される。そして、このことに加えて、竹白炭粉末が独自にマイナスイオンを発生させて周囲のプラスイオンと中和させるため、以上の諸作用の発揮水準が一層高められることとなる。   In addition, according to the environmental purification molded body of the present invention, extremely high adsorptive capacity is realized by the coexistence of the fine pores of bamboo black charcoal powder, bamboo white charcoal powder, and zeolite powder, and excess plus ions are fine. In addition to being adsorbed in the pores, the zeolite powder can reduce the positive ions adsorbed in the fine pores of each powder to negative ions, that is, by exchanging them into negative ions (cation exchange ability). Because it is desorbed from the micropores, the effective adsorption capacity of each powder can be maintained semipermanently, and it can be used for deodorization, humidity control, sterilization, water purification, and sick house prevention (removes causative substances such as formaldehyde) ), Etc., the resulting effect from the adsorption capacity is always exhibited at a high level. In addition, in addition to this, the bamboo white charcoal powder independently generates negative ions and neutralizes the surrounding positive ions, so that the level of performance of the above various actions is further enhanced.

さらに、本発明に係る環境浄化成形体によれば、竹黒炭粉末、竹白炭粉末、及びゼオライト粉末の各粉末を混練することで構成されるため、各粉末の効能が相乗的に発揮されて、複数の環境改善を同時並行に図ることが可能となるだけでなく、竹白炭粉末やゼオライト粉末から放出されるマイナスイオンの働きにより、人間や動物の体を健康にさせたり、その精神を落ち着かせたりするなどのメリットも得られる。そもそも、その環境浄化成形体は、これを構成する各粉末の何れの原料も天然に得られるために、地球に優しい。   Furthermore, according to the environmental purification molded body according to the present invention, because it is composed by kneading each powder of bamboo black charcoal powder, bamboo white charcoal powder, and zeolite powder, the efficacy of each powder is exhibited synergistically, Not only can multiple environmental improvements be made simultaneously, but also negative ions released from bamboo white charcoal powder and zeolite powder can make human and animal bodies healthy and calm their spirit. You can also get merits. In the first place, the environment-purified molded article is kind to the earth because any raw material of each powder constituting it can be obtained naturally.

また、本発明によれば、竹黒炭粉末及び竹白炭粉末をゼオライト粉末で混練することから、様々な形状に成形することが可能であり、人形や仏像、皿、花瓶等の置物形状に成形することとすれば、居住・生活空間に花を添えるインテリアとしても利用可能である。   In addition, according to the present invention, bamboo black charcoal powder and bamboo white charcoal powder are kneaded with zeolite powder, so it can be molded into various shapes, and shaped into figurines such as dolls, Buddha statues, dishes, vases, etc. In other words, it can be used as an interior that adds flowers to living and living spaces.

さらに、本発明に係る環境浄化成形体の製造方法によれば、真空引きされた竹炭化炉(細かな温調可能)を用いて、竹を黒炭化又は白炭化それぞれに必要な目標温度まで振り分けて加熱・温調するため、塵等の不純物を含まないため高純度であるとともに、繊維質まで充分に黒炭化又は白炭化されるため高品質且つ均質な竹黒炭及び竹白炭を生成し、環境浄化成形体の素材として用いることが初めて可能となる。   Furthermore, according to the method for producing an environmental purification molded body according to the present invention, bamboo is distributed to a target temperature required for black carbonization or white carbonization using a vacuumed bamboo carbonization furnace (fine temperature control is possible). Because it is heated and temperature-controlled, it does not contain impurities such as dust, so it is highly pure, and even carbon fiber is sufficiently black carbonized or white carbonized to produce high quality and homogeneous bamboo black and bamboo white charcoal. It becomes possible for the first time to be used as a material for a purified molded body.

(発明の前提)
本発明の実施の形態を説明する上での前提として、竹黒炭及び竹白炭を含めた竹炭について説明する。
竹黒炭及び竹白炭は、竹(孟宗竹,真竹,苦竹,淡竹等)を炭化させた竹炭の一種である。竹は、炭化物の原料に採用される他の材料(木,ヤシガラ等)に比べて、その蘇生機能により毎年同じ場所で採集可能なことから、資源性が非常に良く、製炭場所を殆ど変える必要がない。
(Premise of invention)
As a premise for explaining the embodiment of the present invention, bamboo charcoal including bamboo black charcoal and bamboo white charcoal will be described.
Bamboo black charcoal and bamboo white charcoal are a kind of bamboo charcoal obtained by carbonizing bamboo (Moso bamboo, true bamboo, maitake, light bamboo, etc.) Bamboo can be collected at the same place every year due to its resuscitation function compared to other materials (wood, coconut, etc.) used as a raw material for carbides, so it is very resource-rich and changes the place of charcoal production. There is no need.

また、竹は、維管束が表皮側では密に、内側では粗く分布するという独自の構造を有するため、その表皮が、木やヤシガラ等の表皮に比べて硬いとともに、珪酸化合物(二酸化珪素等)を多く含んでいる。従って、竹を炭化しても、その表皮細胞組織内に炭化前から多く存在する微細孔や珪酸化合物の殆どが失われずに残ることとなる。次の表1は、炭化後における孟宗竹及び真竹それぞれの灰分組成(一部)を示している。この表1からも、竹の表皮等に含まれる珪酸化合物が炭化後も多く残存することが分かる。

Figure 2006256930
In addition, bamboo has a unique structure in which the vascular bundle is distributed densely on the epidermis side and coarsely on the inner side, so that the epidermis is harder than the epidermis such as wood and coconut husks, and silicate compounds (silicon dioxide, etc.) Contains a lot. Therefore, even if bamboo is carbonized, most of the fine pores and silicate compounds that exist in the epidermal cell tissue before carbonization remain without being lost. The following Table 1 shows the ash composition (part) of each of Munetake bamboo and true bamboo after carbonization. Table 1 also shows that a large amount of the silicate compound contained in the bamboo skin remains after carbonization.
Figure 2006256930

このように竹炭は、多数の微細孔が残存しているが故に高い吸着能を有することから、消臭作用、調湿作用、滅菌作用、浄水作用、及びシックハウス防止作用等を発揮する。特に、竹炭が有するような滅菌作用は、他の炭化物(例えば、木炭,カシ炭,ヤシガラ炭)では発揮不可能なものである。竹炭は、これらの作用以外に、触媒作用、及びマイナスイオンや遠赤外線を発生する作用等をも発揮することから、広範囲・多岐に亙る適用が期待されている。なお、マイナスイオンや遠赤外線の効能については後述する。   As described above, bamboo charcoal has a high adsorbing ability because a large number of fine pores remain, and thus exhibits a deodorizing action, a humidity control action, a sterilization action, a water purification action, a sick house prevention action, and the like. In particular, the sterilization effect that bamboo charcoal has cannot be exhibited by other charcoal (for example, charcoal, oak charcoal, coconut charcoal). In addition to these effects, bamboo charcoal also exhibits catalytic action and the action of generating negative ions and far-infrared rays. The effects of negative ions and far infrared rays will be described later.

そして、後述する「真空乾留炭化法」によれば、比重が0.35程度と極めて軽量であるとともに、上述した各作用を極めて顕著に発揮する高機能性竹炭を得ることが可能となる。   And according to the “vacuum carbonization carbonization method” described later, it is possible to obtain a highly functional bamboo charcoal that is extremely lightweight with a specific gravity of about 0.35 and that exhibits each of the above-described functions extremely remarkably.

竹炭が有するこれら特性の一部を裏付けるものとして、例えば、大阪市立工学研究所の安部郁夫氏による研究報告が知られている。同氏は、次の測定1,2を実施している。
<測定1>
ヨウ素液を竹炭表面に塗布してヨウ素原子を竹炭の微細孔に吸着させることにより、竹炭の実質的な表面積を測定。ヤシガラ炭及びカシ炭についても同様の測定を実施。
<測定2>
水銀圧入法に則って竹炭の微細孔の半径を測定。ヤシガラ炭及びカシ炭についても同様の測定を実施。
To support some of these properties of bamboo charcoal, for example, a research report by Mr. Ikuo Abe of Osaka City Institute of Engineering is known. He performs the following measurements 1 and 2.
<Measurement 1>
The surface area of bamboo charcoal is measured by applying iodine solution to the surface of bamboo charcoal and adsorbing iodine atoms into the fine pores of bamboo charcoal. The same measurement was conducted for coconut shell charcoal and oak charcoal.
<Measurement 2>
Measures the radius of fine pores in bamboo charcoal according to the mercury intrusion method. The same measurement was conducted for coconut shell charcoal and oak charcoal.

そして、<測定1>については、「竹炭は、ヤシガラ炭やカシ炭と同様、1g当たり300mという極めて大きな比表面積を有する。」との測定結果が公表されている。 Then, the <Measurement 1> is "charcoal, like PKS charcoal and oak charcoal has a very large specific surface area of 1g per 300 meters 2." And the measurement results of the have been published.

また、<測定2>については、「竹炭の微細孔の半径が最大27nmであったのに対して、ヤシガラ炭では、112nm、カシ炭では、129nmにも達する半径の微細孔が見受けられる。」との測定結果が公表されている。なお、「1nm=10−9m」である。 Regarding <Measurement 2>, “the radius of the fine pores of bamboo charcoal was 27 nm at the maximum, whereas the fine pores with radius reaching 112 nm for coconut charcoal and 129 nm for oak charcoal” were observed. The measurement results are published. Note that “1 nm = 10 −9 m”.

さらに、これらとは別に、「竹炭は、赤潮の原因物質たるリン酸塩やケイ酸塩を短期間(例えば、3日)で消滅させるなどの、高い浄化作用を有するため、磯焼け防止対策等多方面への利用が期待される。」との展望が発表されている。   In addition to these, “Bamboo charcoal has a high purification action, such as the disappearance of phosphates and silicates that cause red tide in a short period of time (for example, 3 days). The prospects are expected to be used in many ways. "

以上説明してきた竹炭の特性を踏まえて、以下、本発明の実施の形態につき、添付図面を参照しつつ、環境浄化成形体例を挙げて詳細に説明する。   Based on the above-described characteristics of bamboo charcoal, embodiments of the present invention will be described in detail below with reference to the accompanying drawings with examples of environmental purification molded bodies.

(成形体例)
図1(a)は、本発明の実施形態の一例たる環境浄化成形体の概略外観図であり、(b)は、この一使用例を示す図である。
同図に図示の環境浄化成形体(イオン還元カーボンセラミックボール)αは、竹黒炭粉末1、竹白炭粉末2、及びゼオライト粉末3を次の表2に示す組成重量比で加水混練し、所望の形状(同図では、丸粒状)に成形後、焼結することで構成されている。この環境浄化成形体αは、その多数を収納した入物形状の篭Aを住居やオフィス等の居住・生活空間内における所望の場所に置くことで使用に供される。なお、使用に供される多数の環境浄化成形体αを収納するのに、金網ケースや布製の袋等を用いても良い。

Figure 2006256930
(Example of molded product)
Fig.1 (a) is a schematic external view of the environmental purification molded object which is an example of embodiment of this invention, (b) is a figure which shows this one example of use.
The environmental purification molded body (ion-reduced carbon ceramic ball) α shown in the figure is obtained by kneading and mixing bamboo black charcoal powder 1, bamboo white charcoal powder 2 and zeolite powder 3 with the composition weight ratio shown in Table 2 below. After forming into a shape (in the figure, round granular shape), it is configured by sintering. This environmental purification molded body α is provided for use by placing a container-shaped bag A containing a large number thereof in a desired place in a living / living space such as a residence or office. Note that a metal mesh case, a cloth bag, or the like may be used to store a large number of environmental purification molded bodies α to be used.
Figure 2006256930

環境浄化成形体αに含まれる竹黒炭粉末1は、竹を約700℃で炭化(黒炭化)させた竹黒炭の粉末である。竹黒炭は、竹炭の一種であり吸着能が優れているため、消臭作用、調湿作用、滅菌作用、浄水作用、及びシックハウス防止作用等、吸着能からの帰結作用を如何なく発揮する。竹黒炭は、これらの作用を有する他、感熱により遠赤外線を発生する作用等も有している。   The bamboo black charcoal powder 1 contained in the environmental purification molded body α is a powder of bamboo black charcoal obtained by carbonizing bamboo at about 700 ° C. (black carbonization). Bamboo black charcoal is a kind of bamboo charcoal and has excellent adsorbing ability, and thus exhibits any effects resulting from adsorbing ability such as deodorizing action, humidity control action, sterilization action, water purification action, and sick house prevention action. In addition to these functions, bamboo black charcoal has an effect of generating far infrared rays by heat sensitivity.

一方、環境浄化成形体αに含まれる竹白炭粉末2は、竹を約1,000℃で炭化(白炭化)させた竹白炭の粉末である。竹白炭は、竹黒炭と同様竹炭の一種であるため吸着能が優れているのは勿論、竹黒炭に比べて硬いとともに、電気抵抗が低いという特性を有する。特に、竹白炭は、電気抵抗の低さ故に導電性が良いため、マイナスイオンを容易に発生する。このような特性を有する竹白炭は、窒素ガスに曝されると、賦活(活性化)されて活性竹炭となる。なお、竹黒炭もマイナスイオンを発生するが、竹白炭程顕著ではない。   On the other hand, the bamboo white charcoal powder 2 contained in the environmental purification molded body α is a bamboo white charcoal powder obtained by carbonizing (white carbonizing) bamboo at about 1,000 ° C. Bamboo white charcoal is a kind of bamboo charcoal similar to bamboo black charcoal, so that it has excellent adsorptivity and is harder than bamboo black charcoal and has low electrical resistance. In particular, bamboo white coal easily generates negative ions because of its low electrical resistance and good conductivity. When exposed to nitrogen gas, bamboo white coal having such characteristics is activated (activated) to become activated bamboo charcoal. Bamboo black charcoal also generates negative ions, but not as pronounced as bamboo white charcoal.

ここで、マイナスイオンは、プラスイオンと中和する効果の他、(1)人間や動物(以下、「人間等」という)の体を電磁波から保護する、(2)人間等の副交感神経に作用することで気分を安定化させたり、リラックスさせたり、ストレスを解消したりする、(3)鎮静作用により人間等の細胞を活性化してその生命力を強くするなどの効果(マイナスイオン効果)を有することから、近年注目されている。   Here, in addition to neutralizing positive ions, negative ions (1) protect humans and animals (hereinafter referred to as “humans”) from electromagnetic waves, and (2) act on human parasympathetic nerves. (3) has the effect (minus ion effect) of activating cells such as humans by sedation and strengthening their vitality. Therefore, it has been attracting attention in recent years.

環境浄化成形体αに含まれるゼオライト粉末3は、焼成処理されたゼオライトの粉末である。ゼオライトは、天然産出砿材の1つたる珪酸アルミナ含水塩鉱物(邦名「沸石」)の別称であり、その表面に均質な分子レベル(1nm〜70nm程度)の微細孔が規則的に並んでいる。このような構造を有するゼオライトを特定温度以下の焼成処理にて脱水すると、水分子があった空洞(微細孔)が壊れずにそのまま残るため、以下に説明するゼオライトの特性が充分に引き出されることとなる。   The zeolite powder 3 contained in the environmental purification molded body α is a calcined zeolite powder. Zeolite is another name for silicate-alumina hydrated mineral (Japanese name "Zeolite"), one of the naturally produced talc materials, and its surface has regularly arranged fine pores of uniform molecular level (about 1nm to 70nm). Yes. When the zeolite having such a structure is dehydrated by a calcination treatment at a specific temperature or lower, cavities (micropores) containing water molecules remain intact without being broken, and the characteristics of the zeolite described below are sufficiently extracted. It becomes.

即ち、ゼオライトは、焼成処理されると高い吸着能を有することとなり、消臭作用、調湿作用、滅菌作用、浄水作用、及びシックハウス防止作用等を発揮するようになるだけでなく、(1)微細孔の孔径より小さい分子のみ吸着する、即ち、微細孔の孔径より小さい分子と大きい分子とを振り分ける分子篩作用、並びに(2)双極子,四極子,不飽和結合を有する物質、及び分極性の高い物質を一般的な極性吸着剤(例えば、シリカゲル,活性アルミナ)におけるよりも一層強力に吸着するという、極めて高い極性等をも発揮するようになる。   That is, the zeolite has a high adsorbing ability when it is calcined, and not only exhibits a deodorizing action, a humidity control action, a sterilization action, a water purification action, and a sick house prevention action, but also (1) Adsorb only molecules smaller than the pore size of the micropores, that is, molecular sieve action that sorts molecules smaller than the pore size of the micropores and larger molecules, and (2) materials with dipoles, quadrupoles, unsaturated bonds, and polarizability It also exhibits extremely high polarity and the like, which adsorbs a high substance more strongly than in a general polar adsorbent (for example, silica gel, activated alumina).

また、ゼオライトは、その触媒作用により、微細孔に吸着されたプラスイオンをマイナスイオンに還元してそこから脱着させる、即ち、プラスイオンをマイナスイオンに交換する陽イオン交換能を有する。ゼオライトのこれら特性は、他の一般的鉱物では決して見られないことから、かかる特性を有するゼオライトは、高機能エコロジー建材等に利用されることがある。   In addition, zeolite has a cation exchange ability for reducing positive ions adsorbed in the micropores to negative ions and desorbing them, that is, exchanging positive ions for negative ions, due to its catalytic action. Since these properties of zeolite are never found in other general minerals, zeolites having such properties may be used for high-performance ecological building materials and the like.

(製造方法例)
次に、図2乃至図6を参照しつつ、環境浄化成形体αの製造工程の一例について説明する。
ここで、図2は、環境浄化成形体αの製造工程の一処理手順例を示す工程図、図3は、同製造工程を構成する前工程の一処理手順例を示す工程図、図4は、同製造工程を構成する竹黒炭生成工程の一処理手順例を示す工程図、及び図5は、同製造工程を構成する竹白炭生成工程の一処理手順例を示す工程図である。
また、図6(a)は、同竹黒炭生成工程及び同竹白炭生成工程で用いる竹炭化炉の概略構成図、(b)は、同竹炭化炉のクラッチ炉蓋付近拡大図、(c)は、同竹炭化炉のI−I線視簡略断面図、及び(d)は、同竹炭化炉の噴射細管一部拡大図である。
(Example of manufacturing method)
Next, an example of a manufacturing process of the environmental purification molded body α will be described with reference to FIGS. 2 to 6.
Here, FIG. 2 is a process diagram showing an example of a processing procedure of the manufacturing process of the environmental purification molded body α, FIG. 3 is a process diagram showing an example of a processing procedure of a previous process constituting the manufacturing process, and FIG. FIG. 5 is a process diagram showing an example of a processing procedure example of a bamboo white charcoal generation process constituting the manufacturing process.
6 (a) is a schematic configuration diagram of a bamboo carbonization furnace used in the bamboo black coal production process and the bamboo white coal production process, FIG. 6 (b) is an enlarged view of the vicinity of the clutch furnace lid of the bamboo carbonization furnace, (c). Fig. 4 is a simplified sectional view taken along line II of the bamboo carbonization furnace, and (d) is a partially enlarged view of the injection thin tube of the bamboo carbonization furnace.

本実施形態例においては、環境浄化成形体αの製造工程が、図2に示すように前工程(ST1)、竹黒炭生成工程(ST2a)、竹白炭生成工程(ST2b)、竹炭微粉末化工程(ST3)、ゼオライト粉末混入工程(ST4)、加水工程(ST5)、混練工程(ST6)、加水工程(ST7)、成形工程(ST8)、及び焼結工程(ST9)という10工程に区分されており、これら各工程がこの順序にて実施される。なお、下記の処理手順となる前工程(ST1)と、竹黒炭生成工程(ST2a)又は竹白炭生成工程(ST2b)とを順に行うことにより、高純度且つ高品質な竹黒炭又は竹白炭を均質量産する方法が、前述の「真空乾留炭化法」である。   In the present embodiment, as shown in FIG. 2, the manufacturing process of the environmental purification molded body α includes the previous process (ST1), the bamboo black charcoal production process (ST2a), the bamboo white charcoal production process (ST2b), and the bamboo charcoal fine powdering process. (ST3), zeolite powder mixing step (ST4), hydration step (ST5), kneading step (ST6), hydration step (ST7), molding step (ST8), and sintering step (ST9) are divided into 10 steps. These steps are performed in this order. In addition, a high-purity and high-quality bamboo black charcoal or bamboo white charcoal is made homogeneous by sequentially performing a pre-process (ST1) and a bamboo black charcoal production process (ST2a) or a bamboo white charcoal production process (ST2b) which are the following processing procedures. The method of mass production is the aforementioned “vacuum carbonization carbonization method”.

環境浄化成形体αの製造工程を構成する前工程(ST1)は、主に、黒炭化又は白炭化される竹材の加工処理を目的として行われる。この前工程は、図3に図示の加工処理手順により行われる。
即ち、まず、伐採した竹を適当な長さ(例えば、1m程度)に切断・分割する(ST11)。なお、竹の伐採時期は、竹が糖を多量に蓄えている10月〜12月が最適である。
The pre-process (ST1) constituting the manufacturing process of the environmental purification molded body α is performed mainly for the purpose of processing the bamboo material that is black carbonized or white carbonized. This pre-process is performed according to the processing procedure shown in FIG.
That is, first, the harvested bamboo is cut and divided into an appropriate length (for example, about 1 m) (ST11). The best time to cut bamboo is from October to December, when bamboo stores a large amount of sugar.

次に、ST11にて得られた竹材をさらに4乃至6ツ割することで、板状の割竹にする(ST12)。なお、一旦乾燥させた竹材であれば、簡単に割竹とすることが可能である。ST12にて得られた割竹は、節の除去等をされた後、他の幾つかの割竹と結束される(ST13)。   Next, the bamboo material obtained in ST11 is further divided into 4 to 6 pieces to obtain plate-like split bamboo (ST12). In addition, if it is a bamboo material once dried, it can be easily made into split bamboo. The split bamboo obtained in ST12 is bonded to some other split bamboo after removing the nodes and the like (ST13).

その後直ちに、互いに結束された複数の割竹を濃度0.05%〜0.07%の過マンガン酸カリウム希溶液に入れ、一定の期間(例えば、24時間)漬け込む(ST14)。この漬込を行えば、過マンガン酸カリウム希溶液の消毒・殺菌作用により割竹の虫食い予防となるとともに、この溶液の収斂作用により割竹の微細孔の数が増えるなどのメリットが得られる。   Immediately thereafter, a plurality of split bamboos bound together are put into a potassium permanganate dilute solution having a concentration of 0.05% to 0.07% and soaked for a certain period (for example, 24 hours) (ST14). If this soaking is carried out, the sterilization and disinfection action of the dilute potassium permanganate solution can prevent the worm-eaten of the split bamboo, and the astringent action of this solution can provide the advantage that the number of micropores in the split bamboo is increased.

なお、ST14において、過マンガン酸カリウム希溶液の代わりに、ニッケルが溶け込んだ硝酸溶液を用いることとしても、かかるメリットを得ることは可能である。然るにこの場合には、その硝酸溶液による漬込後、この溶液中から取り出された結束済み割竹を酸除去のため水洗いする必要がある。   In ST14, such a merit can be obtained by using a nitric acid solution in which nickel is dissolved instead of the potassium permanganate dilute solution. However, in this case, after being soaked with the nitric acid solution, it is necessary to wash the bound split bamboo taken out from this solution with water for acid removal.

何れにしても、かかる漬込が施された結束済み割竹は、虫食い予防されているため長期間に亙る保存が可能であることから、糖を多量に蓄えている10月〜12月に伐採収穫時期が限定されるため、多量に伐採された竹の加工物たる良質な竹材(結束済み割竹)を、急ぎ炭化加工を施さずとも需要量に合わせ漸次行えるので、多量にストックすることができる。   In any case, the bundled split bamboo that has been soaked in can be preserved for a long period of time because it is worm-eaten-prevented, so it is harvested by harvesting from October to December when a large amount of sugar is stored. Because the time is limited, high-quality bamboo material (bundled split bamboo), which is a processed material of bamboo that has been harvested in large quantities, can be gradually stocked according to demand without urgent carbonization, so it can be stocked in large quantities .

そして、充分に漬け込まれた結束済み割竹を過マンガン酸カリウム希溶液中から取り出して充分に乾燥させることにより(ST15)、黒炭化又は白炭化に適した加工処理済み竹材が得られることとなる。   Then, by removing the fully-bundled split bamboo from the potassium permanganate dilute solution and drying it sufficiently (ST15), a processed bamboo material suitable for black carbonization or white carbonization can be obtained. Become.

図2に図示するように、前工程(ST1)の次には、竹黒炭生成を目的とする竹黒炭生成工程(ST2a)と、竹白炭生成を目的とする竹白炭生成工程(ST2b)とが並行又は前後して行われる。これら竹黒炭生成工程及び竹白炭生成工程は、図4又は図5にそれぞれ図示の各処理手順により、図6に示す竹炭化炉を用いて行われる。   As shown in FIG. 2, next to the previous step (ST1), there are a bamboo black coal production step (ST2a) for the purpose of bamboo black coal production and a bamboo white coal production step (ST2b) for the purpose of bamboo white coal production. Performed in parallel or back and forth. These bamboo black charcoal production process and bamboo white charcoal production process are performed using the bamboo carbonization furnace shown in FIG. 6 by the respective processing procedures shown in FIG. 4 or FIG.

ここで、図2に図示する竹黒炭生成工程(ST2a)及び竹白炭生成工程(ST2b)各々の詳細な処理手順を説明する前に、図6を参照しつつ、これら2つの工程を行うのに好適に用いられる竹炭化炉について説明する。
同図に図示の竹炭化炉(以下、単に「炭化炉」ともいう)Cは、その内部に対して搬出入可能な車輪4a付き引出作業車4を備えている。この引出作業車4は、炭化炉Cによる竹黒炭又は竹白炭生成開始前には、同炉C外に置かれた台車D上に通常載置・固定されており、少なくとも竹黒炭又は竹白炭生成開始直前までに、竹材B(図3に詳細に図示の前工程に従う加工処理済み。以下、同様)を複数積載した上で炭化炉C内の所定位置(二点鎖線図示)に搬入・固定される。なお、図6に図示する竹材Bの引出作業車4への積載例は簡易な図示例であって、炭化炉C内に対する引出作業車4の搬出入の妨げとならないように複数の竹材Bを引出作業車4上に積載するのは言うまでもない。
Here, before explaining the detailed processing procedure of each of the bamboo black charcoal generating step (ST2a) and the bamboo white charcoal generating step (ST2b) shown in FIG. 2, these two steps are performed with reference to FIG. The bamboo carbonization furnace used suitably is demonstrated.
A bamboo carbonization furnace (hereinafter, also simply referred to as “carbonization furnace”) C shown in the figure includes a drawing work vehicle 4 with wheels 4 a that can be carried into and out of the inside. This drawer work vehicle 4 is normally placed and fixed on a carriage D placed outside the furnace C before the start of production of bamboo black charcoal or bamboo white charcoal in the carbonization furnace C, and at least bamboo black charcoal or bamboo white charcoal is produced. Immediately before the start, bamboo material B (processed in accordance with the preceding process shown in detail in FIG. 3 has been processed. The same applies hereinafter) is loaded and fixed at a predetermined position (shown by a two-dot chain line) in the carbonization furnace C. The Note that the example of loading bamboo material B onto the drawing work vehicle 4 shown in FIG. 6 is a simple example of illustration, and a plurality of bamboo materials B are provided so as not to interfere with the loading / unloading of the drawing work vehicle 4 into the carbonization furnace C. Needless to say, the vehicle is loaded on the extraction work vehicle 4.

炭化炉C内の断熱性等を挙げるため、炉壁5には、内底部を除きその内側から、ステンレス層5a、断熱層たるファインセラミックス層5b、及びステンレス層又は鋼鉄層5cをこの順に重層させてなる3層構造が採用されている。なお、炭化炉C内の断熱性等を挙げるために炉壁5に採用される構造は、かかる3層構造に限定されず、ファインセラミックス等の断熱素材からなる断熱層を少なくとも1つ含む複数の層が重層してなる複層構造であれば良い。   In order to raise the heat insulating property in the carbonization furnace C, the stainless steel layer 5a, the fine ceramics layer 5b as a heat insulating layer, and the stainless steel layer or the steel layer 5c are laminated on the furnace wall 5 in this order from the inside except the inner bottom portion. A three-layer structure is adopted. Note that the structure adopted for the furnace wall 5 in order to increase the heat insulating property in the carbonization furnace C is not limited to such a three-layer structure, and includes a plurality of heat insulating layers including at least one heat insulating material such as fine ceramics. What is necessary is just a multilayer structure in which layers are stacked.

炭化炉Cの炉壁5には、同炉C内真空引き用の排気管6が貫設されており、この排気管6の外口端(同炉Cから紙面右方向に露出)は、炭化炉C外に置かれた真空ポンプEと繋げられている一方、内口端には、所定粒径以上の異物(例えば、竹黒炭又は竹白炭生成後の残滓たるこれらの微粉末)が真空ポンプEに吸引されるのを防ぐためのフィルタ部材24が取り付けられている。この真空ポンプEが、真空度検出手段として炭化炉C内に設置された2つの真空ゲージ7,8(1つ以上あれば良い)の各検出値に基づき制御されることで、同炉C内が目標圧力値の真空度に減圧・維持される。   The furnace wall 5 of the carbonization furnace C is provided with an exhaust pipe 6 for evacuating the furnace C. The outer end of the exhaust pipe 6 (exposed from the furnace C to the right in the drawing) is carbonized. While connected to a vacuum pump E placed outside the furnace C, foreign matter having a predetermined particle size or more (for example, these fine powders remaining after the formation of bamboo black charcoal or bamboo white charcoal) is vacuum pumped at the inner end. A filter member 24 for preventing suction by E is attached. The vacuum pump E is controlled based on the detected values of two vacuum gauges 7 and 8 (one or more is sufficient) installed in the carbonization furnace C as a vacuum degree detection means, so that the inside of the furnace C Is reduced and maintained at the vacuum level of the target pressure value.

また、炭化炉Cは、紙面上下方向に開閉可能なクラッチ炉蓋9を備えており、このクラッチ炉蓋9の開閉動作は、同クラッチ炉蓋9を炉蓋開閉支持機構10で開閉可能に支持しつつ、手動にて制御される。このクラッチ炉蓋9が開かれて初めて、炭化炉C内に対する引出作業車4の搬出入を行うことが可能となる。本実施形態例においては、クラッチ炉蓋9が閉められた炭化炉C内の気密・密封性をさらに高めるとともに、閉められたクラッチ炉蓋9が濫りに開けられないようにするため、炉壁5外に設置された油圧モータ11の駆動力を油圧シリンダ12経由で油圧式回転クラッチ環13に伝達させることにより、この油圧式回転クラッチ環13を所定方向に所定角回転させて炉壁5開口端に密着閉締させる機構が採用されている。   The carbonization furnace C includes a clutch furnace lid 9 that can be opened and closed in the vertical direction of the drawing. The clutch furnace lid 9 is opened and closed by a furnace lid opening / closing support mechanism 10 so that the clutch furnace lid 9 can be opened and closed. However, it is controlled manually. Only when the clutch furnace lid 9 is opened can the drawer work vehicle 4 be carried into and out of the carbonization furnace C. In the present embodiment, in order to further improve the airtightness and sealing performance in the carbonization furnace C in which the clutch furnace lid 9 is closed, and to prevent the closed clutch furnace lid 9 from being flooded, By transmitting the driving force of the hydraulic motor 11 installed outside 5 to the hydraulic rotary clutch ring 13 via the hydraulic cylinder 12, the hydraulic rotary clutch ring 13 is rotated by a predetermined angle in a predetermined direction to open the furnace wall 5 A mechanism that tightly closes the end is adopted.

炭化炉C内には、炉壁5開口端側で円弧状部14cに立ち上げ折り返し曲折する管形状のステンレス・パイプ(素材がステンレス鋼であるため、以下、「SUSパイプ」ともいう)14が紙面左右方向と平行となるように炉壁5内面に沿って設置されており、その両端とも炭化炉Cから紙面右方向に露出する外口端14a,14bとなっている。SUSパイプ14の外口端14aは、オイルバーナ15と繋げられている一方、外口端14bは、紙面上方向に延びる煙突16(二点鎖線図示)と繋げられている。このオイルバーナ15が、温度検出手段として炭化炉Cの炉壁5(同炉C内でも可)に設置された温度センサ17(例えば、熱電対からなる)の検出値に基づき制御されることで、炭化炉C内が目標温度値に加熱・維持される。   In the carbonization furnace C, there is a tube-shaped stainless steel pipe 14 (which is also referred to as “SUS pipe” hereinafter) because the material is made of stainless steel. It is installed along the inner surface of the furnace wall 5 so as to be parallel to the left and right direction on the paper surface, and both ends thereof are outer end portions 14a and 14b exposed from the carbonization furnace C in the right direction on the paper surface. The outer end 14a of the SUS pipe 14 is connected to the oil burner 15, while the outer end 14b is connected to a chimney 16 (shown by a two-dot chain line) extending in the upward direction on the paper surface. The oil burner 15 is controlled based on a detection value of a temperature sensor 17 (for example, composed of a thermocouple) installed on the furnace wall 5 of the carbonization furnace C (which may be inside the furnace C) as temperature detection means. The carbonization furnace C is heated and maintained at the target temperature value.

さらに、炭化炉Cは、その外部に設置された窒素ボンベ(図示せず)から冷却済み窒素ガスが供給される窒素ガス導入管18と、同炉C周囲の外気から空気を取込可能な空気導入管19とを備えている。   Furthermore, the carbonization furnace C has a nitrogen gas introduction pipe 18 to which cooled nitrogen gas is supplied from a nitrogen cylinder (not shown) installed outside thereof, and air that can take in air from outside air around the furnace C. And an introduction pipe 19.

窒素ガス導入管18は、その頂部が炭化炉Cから露出する外口端18aに連通し、両側下端が閉塞端18bとなった、炉壁5内面に沿った円弧又は馬蹄形状管である。窒素ガス導入管18の外口端18aには、窒素ガスの導入・停止切替用のバルブ20が取り付けられている。空気導入管19も、その頂部が炭化炉Cから露出する外口端19aに連通し、両側下端が閉塞端19bとなった、炉壁5内面に沿った円弧又は馬蹄形状管である。空気導入管19の外口端19aには、空気の導入・停止切替用のバルブ21が取り付けられている。   The nitrogen gas introduction pipe 18 is an arc or horseshoe-shaped pipe along the inner surface of the furnace wall 5, the top portion of which communicates with the outer opening end 18 a exposed from the carbonization furnace C and the lower ends on both sides become the closed ends 18 b. A nitrogen gas introduction / stop switching valve 20 is attached to the outer end 18 a of the nitrogen gas introduction pipe 18. The air introduction pipe 19 is also an arc or horseshoe-shaped pipe along the inner surface of the furnace wall 5, the top portion of which communicates with the outer opening end 19 a exposed from the carbonization furnace C and the lower ends on both sides become the closed ends 19 b. A valve 21 for air introduction / stop switching is attached to the outer end 19 a of the air introduction pipe 19.

それら両管18,19の間は、複数の噴射細管22で繋げられて両管18,19は相互に連通しており、この噴射細管22には、窒素ガス及び空気噴射用の噴射口22a,22b,22c,・・・がその長手方向に対して等間隔に開けられている。要するに、本実施形態例においては、窒素ガス噴射手段が、窒素ガス導入管18、バルブ20、及び噴射細管22から構成されているとともに、空気噴射手段が、空気導入管19、バルブ21、及び噴射細管22から構成されて廉用している。なお、窒素ガス噴射の場合と空気噴射の場合とのそれぞれにおいて、噴射細管22を本実施形態例のように廉用とせずに選択使用するように、窒素ガス導入管18、空気導入管19、及び噴射細管22をそれぞれ配置し、組み合わせても良い。   The pipes 18 and 19 are connected by a plurality of injection thin tubes 22, and the pipes 18 and 19 communicate with each other. The injection thin tubes 22 have injection holes 22 a for injecting nitrogen gas and air. 22b, 22c,... Are equally spaced with respect to the longitudinal direction. In short, in this embodiment, the nitrogen gas injection means includes the nitrogen gas introduction pipe 18, the valve 20, and the injection thin tube 22, and the air injection means includes the air introduction pipe 19, the valve 21, and the injection. It is composed of a thin tube 22 and is inexpensive. In addition, in each of the case of nitrogen gas injection and the case of air injection, the nitrogen gas introduction pipe 18, the air introduction pipe 19, and the injection thin tube 22 are selectively used without being inexpensive as in the present embodiment. And the injection thin tubes 22 may be arranged and combined.

次に、図4又は図5を参照しつつ、図2に図示する竹黒炭生成工程(ST2a)及び竹白炭生成工程(ST2b)各々の詳細な処理手順について説明する。
両図4,5に図示するように、まず、充分に乾燥させた竹材Bを炭化炉C内に詰め込む(ST21)。この詰込は、詳細には次の作業手順で行われる。(1)炭化炉C外の台車D上に載置・固定された引出作業車4上に竹材Bを積載する。(2)引出作業車4の車輪4aが炭化炉Cの引出作業車収納床面23と同レベルの高さとなっているので、引出作業車4を台車D上の停車位置から炭化炉C内の所定位置(二点鎖線図示)まで移動・固定させる。
Next, with reference to FIG. 4 or FIG. 5, the detailed processing procedure of each of the bamboo black charcoal generation step (ST2a) and the bamboo white charcoal generation step (ST2b) illustrated in FIG. 2 will be described.
As shown in FIGS. 4 and 5, first, the sufficiently dried bamboo material B is packed into the carbonization furnace C (ST21). This clogging is performed in detail by the following work procedure. (1) Bamboo material B is loaded on the drawer work vehicle 4 placed and fixed on the carriage D outside the carbonization furnace C. (2) Since the wheel 4a of the drawing work vehicle 4 is at the same level as the drawing work vehicle storage floor 23 of the carbonization furnace C, the drawing work vehicle 4 is moved from the stop position on the carriage D to the inside of the carbonization furnace C. Move and fix to a predetermined position (two-dot chain line shown).

次に、炭化炉C内を真空ポンプEで真空引きする(ST22)。この真空引きは、詳細には次の作業手順で行われる。即ち、(1)窒素ガス導入管18備付けのバルブ20と、空気導入管19備付けのバルブ21とを手で締める、又は、各バルブ20,21がそれぞれ締まっていることを確認する。(2)炉蓋開閉支持機構10に開閉可能に支持されたクラッチ炉蓋9を手動で閉める。(3)炭化炉C内の真空引きに備えるため、油圧モータ11の駆動力を油圧シリンダ12経由で油圧式回転クラッチ環13に伝達させることにより、この油圧式回転クラッチ環13を所定方向に所定角回転させて炉壁5開口端に密着閉締させる。こうすることで、炉壁5と油圧式回転クラッチ環13との間に僅かに存在する空隙等が解消されて、炭化炉C内の気密・密封性がさらに高まるとともに濫りに開かないようにする。(4)真空ゲージ7,8の各検出値が目標圧力値に下がるまで、真空ポンプEを作動させて炭化炉C内を減圧する。   Next, the inside of the carbonizing furnace C is evacuated by the vacuum pump E (ST22). This evacuation is performed in detail by the following work procedure. That is, (1) The valve 20 with the nitrogen gas introduction pipe 18 and the valve 21 with the air introduction pipe 19 are tightened by hand, or it is confirmed that the valves 20 and 21 are tight. (2) The clutch furnace lid 9 supported by the furnace lid opening / closing support mechanism 10 so as to be opened and closed is manually closed. (3) In order to prepare for evacuation in the carbonizing furnace C, the driving force of the hydraulic motor 11 is transmitted to the hydraulic rotary clutch ring 13 via the hydraulic cylinder 12 so that the hydraulic rotary clutch ring 13 is predetermined in a predetermined direction. The angle is rotated to close and close the open end of the furnace wall 5. By doing so, a slight gap or the like existing between the furnace wall 5 and the hydraulic rotary clutch ring 13 is eliminated, so that the airtightness / sealing performance in the carbonization furnace C is further enhanced and it does not open to the flood. To do. (4) The vacuum pump E is operated to depressurize the carbonization furnace C until the detected values of the vacuum gauges 7 and 8 are reduced to the target pressure value.

この真空引き(ST22)により、炭化炉C内から塵等の不純物の殆どが除去されるため、不純物の含有率が極めて低い高純度な竹黒炭や竹白炭を生成することが初めて可能となる。   By this evacuation (ST22), most of impurities such as dust are removed from the inside of the carbonizing furnace C, so that it becomes possible for the first time to produce high-purity bamboo black charcoal or bamboo white charcoal with a very low impurity content.

次に、竹黒炭生成工程の場合には、図4に示すように、温度センサ17の検出値が炭化炉Cの最高加熱限界値約800℃の直前温度値約700℃に達するまで、オイルバーナ15を作動させて炭化炉C内を加熱する(ST23)。この間、オイルバーナ15から外口端14aを介してSUSパイプ14内に送風された熱風が同パイプ14内を外口端14bに向けて流れつつ周囲へ熱放射することにより、竹材Bが黒炭化する温度値約700℃まで炭化炉C内が一様に昇温されて、温度ムラが発生することなく同炉C内の隅々まで、竹黒炭生成に必要な熱が充分に行き渡るために均されることから(ST24)、竹材Bがその繊維物質まで充分且つ確実に黒炭化されることとなる。   Next, in the case of the bamboo black charcoal production process, as shown in FIG. 4, the oil burner is used until the detected value of the temperature sensor 17 reaches a temperature value of about 700 ° C. just before the maximum heating limit value of the carbonization furnace C is about 800 ° C. 15 is operated to heat the inside of the carbonization furnace C (ST23). During this time, the hot air blown into the SUS pipe 14 from the oil burner 15 through the outer end 14a radiates heat to the surroundings while flowing in the pipe 14 toward the outer end 14b, whereby the bamboo material B is black carbonized. The temperature inside the carbonization furnace C is uniformly raised to a temperature value of about 700 ° C., and the heat necessary for the production of bamboo black coal is sufficiently distributed to every corner of the furnace C without causing temperature unevenness. As a result, the bamboo material B is black carbonized sufficiently and reliably up to the fiber material.

次に、炭化炉C内に詰め込まれた竹材Bが全て完全に黒炭化したらその時点でST23の加熱を終了し、その後の適当な時点でバルブ20を緩めて窒素ガス導入管18内に窒素ガスを導入することにより、両管18,19間を繋いで連通する各噴射細管22の噴射口22a,22b,22c,・・・から窒素ガスを均等に噴射させて炭化炉C内を冷却する(ST25)。このようにすることで、炭焼き窯を用いる場合におけるよりも、生成から間もない竹黒炭の温度を室温程度まで下げるのに要する時間が遥かに短縮されることとなる。このことは、次に説明する竹白炭生成工程の場合についても同様である。   Next, when all of the bamboo material B packed in the carbonization furnace C is completely black carbonized, the heating of ST23 is finished at that time, and the valve 20 is loosened at an appropriate time thereafter, and the nitrogen gas is introduced into the nitrogen gas introduction pipe 18. To cool the inside of the carbonization furnace C by uniformly injecting nitrogen gas from the injection ports 22a, 22b, 22c,... ST25). By doing in this way, the time required for lowering the temperature of bamboo black charcoal shortly after generation to room temperature will be much shorter than when using a charcoal kiln. The same applies to the case of the bamboo white charcoal generation step described below.

一方、竹白炭生成工程の場合には、図5に示すように、温度センサ17の検出値が炭化炉Cの最高加熱限界値約800℃に達するまで、オイルバーナ15を作動させて炭化炉C内を加熱する(ST23′)。   On the other hand, in the case of the bamboo white charcoal production process, the oil burner 15 is operated until the detected value of the temperature sensor 17 reaches the maximum heating limit value of about 800 ° C., as shown in FIG. The inside is heated (ST23 ').

ここで、竹材Bを白炭化させるのに必要な加熱温度値は約1,000℃であることから、ST23′の加熱が行われるだけでは、竹白炭を得ることができない。そこで、炭化炉C内に詰め込まれた竹材Bが全て完全に黒炭化したらその時点で、バルブ21を一時的に緩めて空気導入管19内に空気を一時的に導入することにより、各噴射細管22の噴射口22a,22b,22c,・・・から空気を均等に噴射させて炭化炉C内を追い加熱する(ST23″)。このようにすることで、炭化炉C内にて黒炭化した竹材Bが空気に曝されて発火するなどして、竹材Bが白炭化する温度値約1,000℃まで炭化炉C内が一様に昇温されて、温度ムラが発生することなく同炉C内の隅々まで、竹白炭生成に必要な熱が充分に行き渡るために均されることから(ST24)、それら全ての黒炭化済み竹材Bがその繊維物質まで充分且つ確実に白炭化されることとなり、ST23′の加熱を終了する。   Here, since the heating temperature value necessary for white carbonization of the bamboo material B is about 1,000 ° C., bamboo white charcoal cannot be obtained only by heating of ST23 ′. Therefore, when all of the bamboo material B packed in the carbonization furnace C is completely black carbonized, the valve 21 is temporarily loosened and air is temporarily introduced into the air introduction pipe 19 at each point, whereby each injection tubule The air is uniformly injected from the 22 injection ports 22a, 22b, 22c,... To heat the inside of the carbonizing furnace C (ST23 ″). By doing so, black carbonization is performed in the carbonizing furnace C. When the bamboo material B is exposed to air and ignites, the temperature in the carbonization furnace C is uniformly raised to a temperature value of about 1,000 ° C. at which the bamboo material B is white carbonized, and the furnace does not cause temperature unevenness. Since the heat necessary for producing bamboo white charcoal is evenly distributed to every corner in C (ST24), all these black carbonized bamboo materials B are white carbonized sufficiently and reliably up to the fiber material. This completes the heating of ST23 '.

さらに炭化炉C内が充分に均されて、そこに詰め込まれた竹材Bが全て完全に白炭化したら、バルブ21を締めて空気導入管19内への空気の導入を止めた後、適当な時点でバルブ20を緩めて窒素ガス導入管18内に窒素ガスを導入することにより、各噴射細管22の噴射口22a,22b,22c,・・・から窒素ガスを均等に噴射させて同炉C内を冷却する(ST25)。このとき、炭化炉C内で既に生成された竹白炭が窒素ガスに曝されることで賦活(活性化)されて、活性竹炭となる。   Further, when the inside of the carbonizing furnace C is sufficiently leveled and all the bamboo material B packed therein is completely white carbonized, after the valve 21 is closed and the introduction of air into the air introduction pipe 19 is stopped, an appropriate time point is reached. Then, the valve 20 is loosened and nitrogen gas is introduced into the nitrogen gas introduction pipe 18, whereby nitrogen gas is evenly injected from the injection ports 22a, 22b, 22c,. Is cooled (ST25). At this time, bamboo white charcoal already generated in the carbonization furnace C is activated (activated) by being exposed to nitrogen gas, and becomes activated bamboo charcoal.

以上説明したように、竹黒炭生成工程の場合には、図4に図示の各処理手順を順次実施する一方、竹白炭生成工程の場合には、図5に図示の各処理手順を順次実施することとすれば、繊維質まで充分且つ確実に黒炭化又は白炭化された高品質な竹黒炭及び竹白炭の生成を単一の装置(炭化炉C)のみで行うことが初めて可能となる。   As described above, in the case of the bamboo black charcoal generating step, the processing procedures illustrated in FIG. 4 are sequentially performed, whereas in the case of the bamboo white charcoal generating step, the processing procedures illustrated in FIG. 5 are sequentially performed. If this is the case, it becomes possible for the first time to produce high-quality bamboo black charcoal and bamboo white charcoal that have been carbonized or white carbonized sufficiently and reliably up to the fiber using only a single device (carbonization furnace C).

そして、竹黒炭生成工程及び竹白炭生成工程の何れの場合でも、炭化炉C内が充分に冷却されたら、生成された複数の竹黒炭又は竹白炭を引出作業車4ごと同炉C内から取り出す。これにて竹黒炭生成工程や竹白炭生成工程を終了する場合には、製品検査や安全保管等を行うこととしても良い。一方、新たな竹黒炭生成工程や竹白炭生成工程に移行する場合には、図4又は図5に図示の各処理手順を再度順次実施することとなる。このようにすることで、繊維質まで充分且つ確実に黒炭化又は白炭化された高品質な竹黒炭及び竹白炭を均質にて量産することが始めて可能となる。   And in any case of a bamboo black charcoal production | generation process and a bamboo white charcoal production | generation process, if the inside of the carbonization furnace C is fully cooled, several produced | generated bamboo black charcoal or bamboo white charcoal will be taken out from the same furnace C together with the drawing work vehicle 4. . Thus, when the bamboo black charcoal generation process or the bamboo white charcoal generation process is completed, product inspection, safe storage, or the like may be performed. On the other hand, when shifting to a new bamboo black charcoal production process or bamboo white charcoal production process, each processing procedure illustrated in FIG. 4 or 5 is sequentially performed again. By doing in this way, it becomes possible for the first time to mass-produce high quality bamboo black charcoal and bamboo white charcoal that have been sufficiently and surely black carbonized or white carbonized up to fiber quality.

なお、上述のような構成である炭化炉Cは、既存の炭焼き窯と異なり、その内部に充満した煤煙の殆どが外部に漏れずに竹の黒炭化や白炭化に利用されるため、竹酸液の採集には向かないものの、大気汚染の防止対策を考慮する必要がない。   In addition, the carbonization furnace C having the above-described configuration is different from existing charcoal baking kilns, and most of the smoke filled inside is used for black carbonization and white carbonization of bamboo without leaking to the outside. Although not suitable for liquid collection, it is not necessary to consider measures to prevent air pollution.

図2に図示するように、竹黒炭生成工程(ST2a)及び竹白炭生成工程(ST2b)の次には、生成された竹黒炭及び竹白炭を微粉末化することを目的とする竹炭微粉末化工程(ST3)が行われる。なお、この竹炭微粉末化工程により得られた竹黒炭粉末や竹白炭粉末だけでなく、竹黒炭生成工程(ST2a)又は竹白炭生成工程(ST2b)において炭化炉C内に発生した残渣の竹黒炭粉末や竹白炭粉末をも利用することとすれば、経済的である。   As shown in FIG. 2, after the bamboo black charcoal production step (ST2a) and the bamboo white charcoal production step (ST2b), bamboo charcoal pulverization for the purpose of pulverizing the produced bamboo black charcoal and bamboo white charcoal. Step (ST3) is performed. Not only bamboo black charcoal powder and bamboo white charcoal powder obtained by this bamboo charcoal fine powdering process, but also residual bamboo black charcoal generated in carbonization furnace C in bamboo black charcoal production process (ST2a) or bamboo white charcoal production process (ST2b) If powder and bamboo white charcoal powder are also used, it is economical.

竹炭微粉末化工程(ST3)の次には、この工程にて得られた竹黒炭粉末及び竹白炭粉末の混合物にゼオライト粉末をさらに混入することを目的とするゼオライト粉末混入工程(ST4)が行われる。ここで、竹黒炭粉末、竹白炭粉末、及びゼオライト粉末の割合は、順次、混合重量比、30%〜25%、30%〜25%、及び40%〜50%にそれぞれ設定される。   Next to the bamboo charcoal fine powdering step (ST3), there is a zeolite powder mixing step (ST4) for the purpose of further mixing the zeolite powder into the mixture of bamboo black charcoal powder and bamboo white charcoal powder obtained in this step. Is called. Here, the ratio of bamboo black charcoal powder, bamboo white charcoal powder, and zeolite powder is set to the mixing weight ratio, 30% to 25%, 30% to 25%, and 40% to 50%, respectively.

ゼオライト粉末混入工程(ST4)と同時又は事後的に、水を適宜加えつつ(ST5)、竹黒炭及び竹白炭の各粉末とゼオライト粉末との均等混練を目的とする混練工程(ST6)が行われる。この混練工程では、例えば、既存の混合機ニーダ等が用いられる。   Simultaneously with or after the zeolite powder mixing step (ST4), a kneading step (ST6) is performed for the purpose of uniform kneading of each powder of bamboo black and bamboo white and zeolite powder while adding water as appropriate (ST5). . In this kneading step, for example, an existing mixer kneader or the like is used.

混練工程(ST6)の次には、この工程にて得られた混練物に水を適宜加えることで、それに含まれるゼオライト粉末のバインダ作用を現出させるとともに必要に応じ成形展性を良好とすることを目的とする加水工程(ST7)が行われる。   Next to the kneading step (ST6), water is appropriately added to the kneaded product obtained in this step, so that the binder action of the zeolite powder contained in the kneaded product appears and the moldability is improved as necessary. The water addition process (ST7) aiming at this is performed.

加水工程(ST7)の次には、この工程にて得られた、ゼオライト粉末によるバインダ作用及び必要に応じた成形展性作用現出済みの混練物を押型に入れ、既存の造粒機を用いるなどして、φ3ミリの丸粒状に押出成形することを目的とする成形工程(ST8)が行われる。この段階において得られる造粒物によっても、環境改善に有効な効能を相乗的に発揮且つ半永久的に持続可能であるものの、硬度が低いため、一定の形状を維持するには至らず長持ちしない。なお、ST8にて得られる造粒物の形状は、適当な押型を用いることで、丸粒状以外の形状(例えば、四角粒形状や碁石形状その他の玉粒状)とすることも可能である。   Next to the hydration step (ST7), the kneaded material obtained in this step, the binder action by the zeolite powder and the moldability action as necessary, which has already been revealed, is put into a mold, and an existing granulator is used. Thus, a molding step (ST8) for the purpose of extruding into a round particle of φ3 mm is performed. Even the granulated product obtained at this stage synergistically exhibits an effect effective for improving the environment and can be sustained semipermanently, but since the hardness is low, it does not maintain a certain shape and does not last long. In addition, the shape of the granulated product obtained in ST8 can be changed to a shape other than a round shape (for example, a quadrangular shape, a meteorite shape, or another globular shape) by using an appropriate stamping die.

成形工程(ST8)の次には、この工程にて得られた成形物のセラミック化を目的とする焼結工程(ST9)が、既存の乾留炉を用いるなどして行われ、これにより、所望の形状を維持し得る硬度を有するセラミック(環境浄化成形体α)が初めて得られることとなる。   Next to the forming step (ST8), a sintering step (ST9) for the purpose of converting the molded product obtained in this step into a ceramic is performed using an existing dry distillation furnace, etc. Thus, a ceramic (environmental purification molded body α) having a hardness capable of maintaining the shape is obtained for the first time.

以上、本発明の実施の形態について説明してきたが、本発明は、必ずしも上述した手段、手法、及び使用例にのみ限定されるものではなく、前述した効果を達成する範囲内において、適宜、変更実施することが可能なものである。例えば、竹黒炭粉末1、竹白炭粉末2、及びゼオライト粉末3からなる混練物を所要量用いて人形や仏像、皿、花瓶等の置物を製造すれば、居住・生活空間に花を添えるインテリアとしても利用可能である。   Although the embodiments of the present invention have been described above, the present invention is not necessarily limited only to the above-described means, methods, and usage examples, and can be appropriately changed within the scope of achieving the above-described effects. It is possible to implement. For example, if figurines such as dolls, Buddha statues, dishes, vases, etc. are produced using the required amount of kneaded material consisting of bamboo black charcoal powder 1, bamboo white charcoal powder 2 and zeolite powder 3, it can be used as an interior that adds flowers to living and living spaces. Is also available.

また、所要数の環境浄化成形体αを水中(例えば、水槽,海,河川,湖沼,溜池)に沈めることとすれば、上述の諸作用発揮により、その浄水化や富栄養抑制化、滅菌化等に大きく貢献することが可能である。さらに、土壌改良を目的とする場合には、環境浄化成形体αを土中に埋めれば良い。   Also, if the required number of environmental purification molded bodies α are submerged in water (for example, aquariums, seas, rivers, lakes, and ponds), the water purification, eutrophication suppression, and sterilization can be achieved through the above-mentioned various functions. It is possible to contribute greatly to Furthermore, when aiming at soil improvement, the environmental purification molded body α may be buried in the soil.

また、環境浄化成形体αに含まれる竹黒炭粉末1が、感熱すると遠赤外線を発生させる特徴を有することから、この環境浄化成形体αを身に付けることで遠赤外線による様々な効果が期待される。即ち、例えば、環境浄化成形体αを洋服の裏ポケットに入れたり、湿布等で肌に貼り付けたりするなどすれば、この環境浄化成形体αが体温を感熱して遠赤外線を発生させることとなり、環境浄化成形体αから放射された遠赤外線が保温効果や温湿布に準じた効果等を齎すと期待される。   In addition, since the bamboo black charcoal powder 1 contained in the environmental purification molded body α has a feature of generating far infrared rays when heat-sensitive, various effects of the far infrared rays are expected by wearing the environmental purification molded body α. The That is, for example, if the environmental purification molded body α is put in the back pocket of the clothes or attached to the skin with a compress or the like, the environmental purification molded body α heats the body temperature and generates far infrared rays. The far-infrared rays emitted from the environmental purification molded body α are expected to have a heat retaining effect, an effect similar to a warm compress, and the like.

(a)は、本発明の実施形態の一例たる環境浄化成形体の概略外観図であり、(b)は、この一使用例を示す図である。(A) is a general | schematic external view of the environmental purification molded object which is an example of embodiment of this invention, (b) is a figure which shows this one example of use. 図1に図示の環境浄化成形体の製造工程の一処理手順例を示す工程図である。It is process drawing which shows the example of 1 process sequence of the manufacturing process of the environmental purification molded object shown in FIG. 図2に図示の製造工程を構成する前工程の一処理手順例を示す工程図である。It is process drawing which shows the example of 1 process sequence of the pre-process which comprises the manufacturing process shown in FIG. 図2に図示の製造工程を構成する竹黒炭生成工程の一処理手順例を示す工程図である。It is process drawing which shows the example of 1 process sequence of the bamboo black charcoal production | generation process which comprises the manufacturing process shown in FIG. 図2に図示の製造工程を構成する竹白炭生成工程の一処理手順例を示す工程図である。It is process drawing which shows one processing procedure example of the bamboo white charcoal production | generation process which comprises the manufacturing process shown in FIG. (a)は、図4又は図5それぞれに詳細に図示の竹黒炭生成工程及び竹白炭生成工程で用いる竹炭化炉の概略構成図、(b)は、同竹炭化炉のクラッチ炉蓋付近拡大図、(c)は、同竹炭化炉のI−I線視簡略断面図、及び(d)は、同竹炭化炉の噴射細管一部拡大図である。(A) is a schematic block diagram of a bamboo carbonization furnace used in the bamboo black charcoal production process and the bamboo white charcoal production process shown in detail in FIG. 4 or FIG. 5, respectively, and (b) is an enlargement near the clutch furnace lid of the bamboo carbonization furnace. FIG. 4C is a simplified cross-sectional view taken along line II of the bamboo carbonization furnace, and FIG. 4D is a partial enlarged view of the injection thin tube of the bamboo carbonization furnace.

符号の説明Explanation of symbols

α・・・環境浄化成形体
A・・・篭
B・・・竹材
C・・・竹炭化炉
D・・・台車
E・・・真空ポンプ
1・・・竹黒炭粉末
2・・・竹白炭粉末
3・・・ゼオライト粉末
4・・・引出作業車
4a・・・車輪
5・・・炉壁
5a・・・ステンレス層
5b・・・ファインセラミックス層
5c・・・ステンレス層又は鋼鉄層
6・・・排気管
7,8・・・真空ゲージ
9・・・クラッチ炉蓋
10・・・炉蓋開閉支持機構
11・・・油圧モータ
12・・・油圧シリンダ
13・・・油圧式回転クラッチ環
14・・・ステンレス・パイプ
14a,14b,18a,19a・・・外口端
14c・・・円弧状部
15・・・オイルバーナ
16・・・煙突
17・・・温度センサ
18・・・窒素ガス導入管
19・・・空気導入管
18b,19b・・・閉塞端
20,21・・・バルブ
22・・・噴射細管
22a,22b,22c・・・噴射口
23・・・引出作業車収納床面
24・・・フィルタ部材
α ... Environmentally purified compact A ... 篭 B ... Bamboo material C ... Bamboo carbonization furnace D ... Carriage E ... Vacuum pump 1 ... Bamboo black charcoal powder 2 ... Bamboo white charcoal powder DESCRIPTION OF SYMBOLS 3 ... Zeolite powder 4 ... Pull-out work vehicle 4a ... Wheel 5 ... Furnace wall 5a ... Stainless steel layer 5b ... Fine ceramics layer 5c ... Stainless steel layer or steel layer 6 ... Exhaust pipes 7, 8 ... Vacuum gauge 9 ... Clutch furnace lid 10 ... Furnace lid opening / closing support mechanism 11 ... Hydraulic motor 12 ... Hydraulic cylinder 13 ... Hydraulic rotary clutch ring 14 ... Stainless steel pipes 14a, 14b, 18a, 19a ... Outer end 14c ... Arc-shaped part 15 ... Oil burner 16 ... Chimney 17 ... Temperature sensor 18 ... Nitrogen gas introduction pipe 19 ... Air introduction pipes 18b, 19b ... Clogging 20, 21 valve 22 ... injection capillary 22a, 22b, 22c ... injection opening 23 ... pull-out work vehicle housing floor 24 ... filter member

Claims (12)

所定割合の竹黒炭粉末、竹白炭粉末、及びゼオライト粉末を加水混練し、所望の形状に成形後、焼結することで構成される、
ことを特徴とする環境浄化成形体。
A mixture of bamboo black charcoal powder, bamboo white charcoal powder, and zeolite powder in a predetermined proportion is kneaded and formed into a desired shape and then sintered.
An environmental purification molded body characterized by that.
前記竹黒炭粉末、前記竹白炭粉末、及び前記ゼオライト粉末の割合は、順次、
組成重量比、30%〜25%、30%〜25%、及び40%〜50%にそれぞれ設定されている、
ことを特徴とする請求項1に記載の環境浄化成形体。
The proportions of the bamboo black charcoal powder, the bamboo white charcoal powder, and the zeolite powder are sequentially
The composition weight ratio is set to 30% to 25%, 30% to 25%, and 40% to 50%,
The environmental purification molded body according to claim 1, wherein:
前記竹黒炭粉末及び前記竹白炭粉末は、
その加工原料を孟宗竹、真竹、苦竹、淡竹を含む竹材とする、
ことを特徴とする請求項1又は2に記載の環境浄化成形体。
The bamboo black charcoal powder and the bamboo white charcoal powder are:
The processing raw materials are bamboo materials, including Miso bamboo, true bamboo, maitake, and light bamboo.
The environmental purification molded article according to claim 1 or 2, characterized in that.
前記竹材は、
黒炭化又は白炭化される前に、過マンガン酸カリウム溶液又はニッケルが溶け込んだ硝酸溶液に漬け込まれる、
ことを特徴とする請求項1、2又は3に記載の環境浄化成形体。
The bamboo is
Before being black carbonized or white carbonized, soaked in potassium permanganate solution or nitric acid solution in which nickel is dissolved,
The environmental purification molded body according to claim 1, 2, or 3.
前記ゼオライト粉末は、
珪酸アルミナ含水塩鉱物(沸石)に焼成処理を施すことで生成される、
ことを特徴とする請求項1、2、3又は4に記載の環境浄化成形体。
The zeolite powder is
Produced by subjecting silicate alumina hydrate salt mineral (zeolite) to firing treatment,
The environmental purification molded article according to claim 1, 2, 3 or 4.
前記形状は、
玉粒状を含む、
ことを特徴とする請求項1、2、3、4又は5に記載の環境浄化成形体。
The shape is
Including jade grain,
The environmental purification molded body according to claim 1, 2, 3, 4 or 5.
黒炭化又は白炭化される竹材を加工処理する前工程と、
真空引きされた竹炭化炉内で当該竹材をこれが黒炭化する目標温度まで加熱・温調することにより、竹黒炭を生成する竹黒炭生成工程と、
真空引きされた前記竹炭化炉内で前記竹材をこれが白炭化する目標温度まで加熱・温調することにより、竹白炭を生成する竹白炭生成工程と、
前記竹黒炭及び当該竹白炭を微粉末化する竹炭微粉末化工程と、
所定割合の前記竹黒炭及び前記竹白炭それぞれの粉末からなる混合物に所定割合のゼオライト粉末をさらに混入するゼオライト粉末混入工程と、
当該ゼオライト粉末混入工程の円滑化のために水を加える第1加水工程と、
前記竹黒炭粉末と前記竹白炭粉末と前記ゼオライト粉末とを均等に混練する混練工程と、
当該混練工程で得られた混練物に水を加えることで、これに含まれる前記ゼオライト粉末のバインダ作用とともに必要に応じ成形展性作用を現出させる第2加水工程と、
当該混練物を所望の形状に成形する成形工程と、
当該成形工程で得られた成形物を焼結する焼結工程と、を順次実施する、
ことを特徴とする環境浄化成形体の製造方法。
A pre-process for processing black carbonized or white carbonized bamboo material;
Bamboo black charcoal production process for producing bamboo black charcoal by heating and temperature-controlling the bamboo material to a target temperature at which it is black carbonized in a vacuumed bamboo carbonization furnace;
Bamboo white charcoal producing step for producing bamboo white charcoal by heating and adjusting the temperature to a target temperature at which the bamboo material is white carbonized in the evacuated bamboo carbonization furnace;
Bamboo charcoal pulverization step for pulverizing the bamboo black charcoal and bamboo white charcoal,
A zeolite powder mixing step of further mixing a predetermined ratio of zeolite powder into a mixture of the bamboo black charcoal and the bamboo white charcoal of a predetermined ratio;
A first hydration step of adding water to facilitate the zeolite powder mixing step;
A kneading step of uniformly kneading the bamboo black charcoal powder, the bamboo white charcoal powder and the zeolite powder;
By adding water to the kneaded product obtained in the kneading step, a second hydration step that manifests a moldability action as necessary together with the binder action of the zeolite powder contained therein,
A molding step of molding the kneaded product into a desired shape;
Sequentially carrying out a sintering step of sintering the molded product obtained in the molding step,
The manufacturing method of the environmental purification molded object characterized by the above-mentioned.
前記竹黒炭生成工程及び前記竹白炭生成工程は、
前記加工処理された前記竹材を前者は約700℃、後者は約1,000℃の炉内温度管理の厳密な峻別の下にそれぞれ焼成される、
ことを特徴とする請求項7に記載の環境浄化成形体の製造方法。
The bamboo black charcoal producing step and the bamboo white charcoal producing step are
The processed bamboo material is fired under strict distinction of furnace temperature control of about 700 ° C. for the former and about 1,000 ° C. for the latter,
The manufacturing method of the environmental purification molded object of Claim 7 characterized by the above-mentioned.
前記竹黒炭生成工程及び前記竹白炭生成工程は、
前記加工処理された前記竹材を複数収容する前記炉内の真空引き用の排気管と、
当該炉内の真空度を検出する真空度検出手段と、
当該炉内の温度を検出する温度検出手段と、
当該炉内を一様に制御加熱する加熱手段と、を具備した前記竹炭化炉を用いて、
前記排気管から前記真空度検出手段の検出値に基づいて、前記加工処理された前記竹材を収容した前記炉内を密封真空雰囲気にするため真空引きする処理手順と、
前記温度検出手段の検出値に基づき前記加熱手段を制御することにより、前記炉内に収容された前記加工処理済みの前記竹材が黒炭化又は白炭化する目標温度までそれぞれ前記密封真空雰囲気とした当該炉内を一様に加熱する処理手順と、を含む、
ことを特徴とする請求項7又は8に記載の環境浄化成形体の製造方法。
The bamboo black charcoal producing step and the bamboo white charcoal producing step are
An exhaust pipe for evacuation in the furnace containing a plurality of the processed bamboo materials;
A degree of vacuum detecting means for detecting the degree of vacuum in the furnace;
Temperature detecting means for detecting the temperature in the furnace;
Using the bamboo carbonization furnace provided with heating means for uniformly controlling and heating the inside of the furnace,
Based on the detection value of the vacuum degree detection means from the exhaust pipe, a processing procedure for evacuating the furnace containing the processed bamboo material to create a sealed vacuum atmosphere;
By controlling the heating means based on the detection value of the temperature detection means, the sealed vacuum atmosphere is set up to a target temperature at which the processed bamboo material accommodated in the furnace is black carbonized or white carbonized, respectively. A treatment procedure for uniformly heating the inside of the furnace,
The manufacturing method of the environmental purification molded object of Claim 7 or 8 characterized by the above-mentioned.
前記竹黒炭生成工程及び前記竹白炭生成工程は、
供給された冷却済み窒素ガスを前記炉内にて均等に噴射する窒素ガス噴射手段を、さらに具備した前記竹炭化炉を用いて、
前記竹黒炭又は前記竹白炭の生成から間もない前記炉内にて前記窒素ガス噴射手段により前記窒素ガスを均等に噴射する処理手順を、さらに含む、
ことを特徴とする請求項7、8又は9に記載の環境浄化成形体の製造方法。
The bamboo black charcoal producing step and the bamboo white charcoal producing step are
Using the bamboo carbonization furnace further equipped with nitrogen gas injection means for uniformly injecting the supplied cooled nitrogen gas in the furnace,
A treatment procedure for evenly injecting the nitrogen gas by the nitrogen gas injection means in the furnace shortly after the production of the bamboo black charcoal or the bamboo white charcoal;
The method for producing an environmental purification molded article according to claim 7, 8 or 9.
前記竹白炭生成工程は、
外気から取入れた空気を前記炉内にて均等に噴射する空気噴射手段を、さらに具備した前記竹炭化炉を用いて、
前記窒素ガス噴射前の前記炉内にて前記空気噴射手段により前記空気を均等に噴射する処理手順を、さらに含む、
ことを特徴とする請求項10に記載の環境浄化成形体の製造方法。
The bamboo white charcoal production process,
Using the bamboo carbonization furnace further comprising air injection means for uniformly injecting air taken from outside air in the furnace,
A treatment procedure for evenly injecting the air by the air injection means in the furnace before the nitrogen gas injection,
The manufacturing method of the environmental purification molded object of Claim 10 characterized by the above-mentioned.
前記前工程は、
伐採・切断した前記竹材を一旦乾燥してから所定寸法に割竹し、板状化したものを複数結束する一連の処理手順の実施の後、当該結束した板状竹群を過マンガン酸カリウム溶液又はニッケルが溶け込んだ硝酸溶液に漬け込む処理手順を実施した上で乾燥仕上げする処理手順に至る、
ことを特徴とする請求項7、8、9、10又は11に記載の環境浄化成形体の製造方法。
The pre-process includes
After the bamboo material that has been cut and cut is dried once, split into a predetermined size, and after a series of treatment procedures for binding a plurality of plate-like materials, the bound plate-like bamboo group is treated with a potassium permanganate solution. Or, after carrying out the treatment procedure of dipping in a nitric acid solution in which nickel is dissolved, it leads to a treatment procedure to dry finish,
The method for producing an environmental purification molded body according to claim 7, 8, 9, 10 or 11.
JP2005079187A 2005-03-18 2005-03-18 Environment cleaning formed article and its producing method Pending JP2006256930A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6041415B1 (en) * 2016-07-04 2016-12-07 田山 ▲吉▼基 A method of reducing the tar component during suction to 1 mg or less in a filter of cigarette with filter.
JP2017029030A (en) * 2015-07-30 2017-02-09 田山 ▲吉▼基 Method for adjusting tar component to be 1 milligram or less in filter of filter-attached cigarette
CN114410361A (en) * 2022-02-11 2022-04-29 福建竹家女工贸有限公司 Bamboo charcoal rod hardness modification process

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017029030A (en) * 2015-07-30 2017-02-09 田山 ▲吉▼基 Method for adjusting tar component to be 1 milligram or less in filter of filter-attached cigarette
JP6041415B1 (en) * 2016-07-04 2016-12-07 田山 ▲吉▼基 A method of reducing the tar component during suction to 1 mg or less in a filter of cigarette with filter.
WO2018008465A1 (en) * 2016-07-04 2018-01-11 吉基 田山 Method for reducing amount of tar components to be 1 mg or less in filter of filter cigarette being smoking
CN114410361A (en) * 2022-02-11 2022-04-29 福建竹家女工贸有限公司 Bamboo charcoal rod hardness modification process

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