JPH10265584A - Production of molded product using algae as raw material and its molded product - Google Patents

Production of molded product using algae as raw material and its molded product

Info

Publication number
JPH10265584A
JPH10265584A JP7246697A JP7246697A JPH10265584A JP H10265584 A JPH10265584 A JP H10265584A JP 7246697 A JP7246697 A JP 7246697A JP 7246697 A JP7246697 A JP 7246697A JP H10265584 A JPH10265584 A JP H10265584A
Authority
JP
Japan
Prior art keywords
algae
polyethylene resin
molded article
raw material
carbon dioxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP7246697A
Other languages
Japanese (ja)
Other versions
JP3749921B2 (en
Inventor
Masatada Yamashita
正忠 山下
Toshi Otsuki
利 大月
Takahiro Hirotsu
孝弘 廣津
Hiroshi Kabetani
洋 壁谷
Ryoichi Kitagawa
良一 北川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHIKYU KANKYO SANGYO GIJUTSU
CHIKYU KANKYO SANGYO GIJUTSU KENKYU KIKO
IHI Corp
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
CHIKYU KANKYO SANGYO GIJUTSU
CHIKYU KANKYO SANGYO GIJUTSU KENKYU KIKO
Agency of Industrial Science and Technology
IHI Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by CHIKYU KANKYO SANGYO GIJUTSU, CHIKYU KANKYO SANGYO GIJUTSU KENKYU KIKO, Agency of Industrial Science and Technology, IHI Corp filed Critical CHIKYU KANKYO SANGYO GIJUTSU
Priority to JP7246697A priority Critical patent/JP3749921B2/en
Publication of JPH10265584A publication Critical patent/JPH10265584A/en
Application granted granted Critical
Publication of JP3749921B2 publication Critical patent/JP3749921B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Cultivation Of Plants (AREA)

Abstract

PROBLEM TO BE SOLVED: To completely nullify the occurrence of a hazardous substance as chlorine and residue of hazardous substance as heavy metals even when calcination is forced to be done and reduce the production cost for molding. SOLUTION: A polyethylene is selected as a thermoplastic resin and an alga (preferably chlorella) fixed carbon dioxide is selected as a raw material for molding product. The polyethylene resin is crushed to fine particle powder of <=1 mm particle sizes in a low temperature atmosphere, while the alga is used in the form of fine particle powder and they are homogeneously mixed and molded.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、特に、工業的な大
量培養が容易な微細藻類の有効利用に関し、大気中の二
酸化炭素の低減,再資源化に用いて有効なものである。
The present invention particularly relates to the effective use of microalgae, which can be easily industrially mass-cultured, and is effective in reducing and recycling carbon dioxide in the atmosphere.

【0002】[0002]

【従来の技術】近年、都市化,産業化の発展により化石
燃料が大量消費され、二酸化炭素の排出量が年々増え続
ける傾向にあり、これにともなう大気中の二酸化炭素濃
度の増大が地球温暖化をもたらす一因として考えられて
いる。地球温暖化は、生物の生存環境に直接影響を与え
るため、大気中の二酸化炭素濃度の低減を図ることが急
務とされている。
2. Description of the Related Art In recent years, fossil fuels have been consumed in large quantities due to the development of urbanization and industrialization, and the emission of carbon dioxide has been increasing year by year. As a result, the concentration of carbon dioxide in the atmosphere has been increasing due to global warming. Is thought to be one of the causes of Since global warming directly affects the living environment of living organisms, it is urgently necessary to reduce the concentration of carbon dioxide in the atmosphere.

【0003】大気中の二酸化炭素濃度の低減を図る方法
として、植物体に、光合成反応を行わせて二酸化炭素を
固定し、これを熱可塑性樹脂に混合して成形体を形成し
て再資源化を図る方法がある。この場合、植物体として
農業廃棄物,林業廃棄物または余剰培養体等の非木質植
物廃棄物が採用され、具体的には、サトウキビかす,麦
わら,イネわらなどのわら類,ジュートなどのじん皮繊
維,アサなどの葉繊維、あるいはクロレラ等の余剰培養
体が採用される。
As a method for reducing the concentration of carbon dioxide in the atmosphere, a plant is subjected to a photosynthetic reaction to fix carbon dioxide, and this is mixed with a thermoplastic resin to form a molded body and to recycle it. There is a way to plan. In this case, non-woody plant wastes such as agricultural wastes, forestry wastes or surplus cultures are used as plants, and specifically, straws such as sugarcane meal, straw, rice straw, and jute or other skins. Fibers, leaf fibers such as hemp, or surplus cultures such as chlorella are employed.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、これら
の再資源化に際して、以下のような課題が残されてい
る。 1) 植物体は、熱可塑性樹脂に対して5〜70重量%
程度混合することが好ましいものの、混合率をあげると
成形品の引張り強さが低下して製品の用途を限定してし
まう。 2) 熱可塑性樹脂としてポリ塩化ビニール(PVC)
の使用が考えられているが、劣化防止剤(安定剤)とし
て、例えば、三塩基性硫酸鉛(TC),二塩基性ステア
リン酸鉛(DBL),カドミウム,バリウム,鉛脂肪酸
塩,バリウム,亜鉛脂肪酸などが使用され、さらに、製
品の褐色防止剤としてパラフィンを添加するなど、必要
に応じて強化充填材,滑材,可塑材等の添加剤を使用す
ることになるため、製品やその切断材(端材)等の焼却
処分を行ったときに、塩素ガスを発生しかつ燃えかす中
に、添加剤、劣化防止剤(安定剤)、重金属類等の有害
物質が残留してその処理を新たに考慮する必要がある。
However, the following problems remain when recycling these resources. 1) The plant is 5 to 70% by weight based on the thermoplastic resin.
Although it is preferable to mix to a certain extent, if the mixing ratio is increased, the tensile strength of the molded article is reduced, and the use of the product is limited. 2) Polyvinyl chloride (PVC) as thermoplastic resin
However, as a deterioration inhibitor (stabilizer), for example, tribasic lead sulfate (TC), dibasic lead stearate (DBL), cadmium, barium, lead fatty acid salt, barium, zinc Fatty acids are used, and additives such as reinforcing fillers, lubricants, plasticizers, etc. are used as necessary, such as the addition of paraffin as a browning inhibitor for products. During the incineration of (cut off materials) etc., harmful substances such as additives, deterioration inhibitors (stabilizers), heavy metals, etc. remain during the generation and burning of chlorine gas, and the treatment is newly performed. Need to be considered.

【0005】本発明は、このような課題に鑑みてなされ
たものであり、以下の目的を達成するものである。 焼却を余儀なくされる場合にあっても、塩素等の有
害物質の発生を防止すること。 重金属類等の有害物質の残留を皆無とすること。 成形品を形成する際の生産コストを低減すること。
[0005] The present invention has been made in view of such problems, and achieves the following objects. Prevent the generation of harmful substances such as chlorine even when incineration is required. Eliminate harmful substances such as heavy metals. To reduce production costs when forming molded articles.

【0006】[0006]

【課題を解決するための手段】熱可塑性樹脂に藻類を混
合して成形体を作製するとともに、熱可塑性樹脂として
ポリエチレン樹脂を選択し、成形体原材料として炭酸ガ
スを固定した藻類を選択する技術が採用される。ポリエ
チレン樹脂として、低温雰囲気で粉砕することによっ
て、粒径を1mm以下の微粉体に調整したポリエチレン
樹脂粉体が使用される。藻類は、光合成反応によって炭
酸ガスを固定したものを乾燥させるとともに、この乾燥
した藻類を粉砕して粒径を数μmの微粉末状に調製した
微粉末状藻体が使用され、藻体は、クロレラ等の微細藻
が選択される。具体的には、ポリエチレン樹脂粉体と微
粉末状藻体とを均質混合させる。均質混合された混合体
を金型に充填し、加熱圧縮することによって加熱圧縮成
形体を製造する。他の手段として、溶融状態のポリエチ
レン樹脂と、藻類とを混合する工程と、ポリエチレン樹
脂と藻類との混合物をペレット化する工程と、前記ペレ
ットを金型に充填して加熱圧縮して成形体を成形する工
程とを有する技術が採用され、これらの手段に、一度、
金型から成形体を取り出し、該成形体が可塑状態にある
うちに再度加圧して冷却することにより製品を安定させ
る技術が付加される。
Means for Solving the Problems A technique of mixing a thermoplastic resin with algae to produce a molded article, selecting a polyethylene resin as the thermoplastic resin, and selecting algae having carbon dioxide fixed as a raw material of the molded article. Adopted. As the polyethylene resin, a polyethylene resin powder whose particle diameter is adjusted to a fine powder of 1 mm or less by pulverization in a low-temperature atmosphere is used. Algae, while drying the carbon dioxide fixed by a photosynthesis reaction, pulverized this dried algae to prepare a fine powdered algal body with a particle size of several μm is used, algal body, Microalgae such as chlorella are selected. Specifically, the polyethylene resin powder and the finely powdered algal body are homogeneously mixed. A homogeneously mixed mixture is filled in a mold and heated and compressed to produce a heat-compressed molded body. As other means, a step of mixing the polyethylene resin in a molten state and algae, a step of pelletizing a mixture of the polyethylene resin and the algae, and a step of filling the pellets in a mold, heating and compressing the molded body, A technique having a molding step is adopted.
A technique is added to take out the molded product from the mold and stabilize the product by applying pressure again and cooling while the molded product is in a plastic state.

【0007】[0007]

【発明の実施の形態】BEST MODE FOR CARRYING OUT THE INVENTION

【0008】本発明に係わる藻類を原材料とする成形体
の製造方法およびその成形体の第1実施形態について、
図1を参照して説明する。図1は、藻類としてクロレラ
を選択した場合の成形体の製造工程を示している。
The first embodiment of the method for producing a molded article using algae as a raw material and the molded article according to the present invention are described below.
This will be described with reference to FIG. FIG. 1 shows a manufacturing process of a molded body when chlorella is selected as algae.

【0009】〔S1:ポリエチレン樹脂〕成形体とし
て、高密度ポリエチレン樹脂(HDPE)が採用され
る。このポリエチレン樹脂は、通常、ペレット状に加工
されたものが提供される。
[S1: Polyethylene resin] A high-density polyethylene resin (HDPE) is used as the molded article. This polyethylene resin is usually provided in the form of a pellet.

【0010】〔S2:樹脂の低温化〕ポリエチレン樹脂
は、およそ−20℃の温度まで冷却した状態として、以
下の工程に供給される。低温化を行うのが微粉体化を効
率的に行うためにも望ましいことであるが、この工程を
省略しても微粉体化を行うことができる。しかし、低温
化しない場合は、周囲に付着する等して取扱いが若干困
難となる。
[S2: Lowering the temperature of the resin] The polyethylene resin is supplied to the following steps in a state of being cooled to a temperature of about -20 ° C. Although it is desirable to lower the temperature for efficient pulverization, the pulverization can be performed even if this step is omitted. However, if the temperature is not lowered, it becomes slightly difficult to handle due to adhesion to the surroundings.

【0011】〔S3:ポリエチレン樹脂の微粉体化〕常
温下のポリエチレン樹脂もしくはそれ以下に低温化され
たポリエチレン樹脂は、適宜粉砕機等により粉砕された
後、篩い等にかけられて、粒径が1mm以下の微粉体の
みが選別される。低温で粉砕する理由は、樹脂の粘性を
低下させて粉砕し易い状態とするとともに、破砕時に生
じる粉砕粒の造粒化現象を防止するためである。かかる
ポリエチレン樹脂の微粉体化技術としては、特開平7−
261458号公報「トナー用微粒子の製造方法及びそ
の装置」等が提案されている。つまり、この技術例のよ
うに、原料粉体をドライアイス粒子の介在下で粉砕する
とともに、ドライアイス粒子の気化を利用して粉砕時の
発生熱を除去するようにしてもよい。
[S3: Pulverization of polyethylene resin] The polyethylene resin at room temperature or the polyethylene resin cooled to a lower temperature is appropriately pulverized by a pulverizer or the like and then sieved to have a particle diameter of 1 mm. Only the following fine powders are sorted out. The reason for pulverizing at a low temperature is to reduce the viscosity of the resin to make it easier to pulverize and to prevent the granulation phenomenon of the pulverized particles generated at the time of pulverization. As a technique for pulverizing polyethylene resin, Japanese Patent Application Laid-Open No.
No. 261458, "Method and Apparatus for Producing Fine Particles for Toner" and the like have been proposed. That is, as in this technical example, the raw material powder may be pulverized in the presence of dry ice particles, and the heat generated during the pulverization may be removed by utilizing the vaporization of the dry ice particles.

【0012】〔S4:二酸化炭素固定化〕成形体原材料
として、光合成反応により炭酸ガスを固定した状態の微
細藻類のクロレラが適用される。
[S4: Fixation of carbon dioxide] Chlorella of microalgae in a state in which carbon dioxide is fixed by a photosynthesis reaction is applied as a raw material of a molded article.

【0013】〔S5:藻体の乾燥〕クロレラは、増殖容
器等の中で大量培養された後、乾燥されるとともに、一
定量に秤量されてブロック状あるいはペレット状の固形
体として提供される。
[S5: Drying of Algae] Chlorella is cultivated in large quantities in a growth vessel or the like, and then dried and weighed to a certain amount to be provided as a block-shaped or pellet-shaped solid.

【0014】〔S6:藻体の微粉化〕ブロック状あるい
はペレット状のクロレラは、粉砕機等により粉砕され
る。
[S6: Pulverization of Algae] Chlorella in the form of blocks or pellets is pulverized by a pulverizer or the like.

【0015】〔S7:微粉末状藻体〕微粉末状藻体は、
粒径が数μmの微粉末状藻体に調製されて、微粉末状藻
体供給容器等に収納されるとともに、以下の工程に供給
される。
[S7: Finely powdered algal body]
It is prepared into a fine powdery algal body having a particle size of several μm, is stored in a fine powdery algal body supply container or the like, and is supplied to the following steps.

【0016】〔S8:混合(粉/粉)〕S3のポリエチ
レン樹脂の微粉体と、S7の微粉末状藻体とは所望の比
率で均質に混合される。つまり、粉末状態の混合体が作
製される。この混合時においては、ポリエチレン樹脂と
クロレラとが1mm以下の微粉末相互の混合となること
により、均質混合性が高められる。
[S8: Mixing (powder / powder)] The fine powder of the polyethylene resin of S3 and the fine algal bodies of S7 are homogeneously mixed at a desired ratio. That is, a powdery mixture is produced. During this mixing, the polyethylene resin and the chlorella are mixed with each other in a fine powder of 1 mm or less, so that the homogenous mixing property is enhanced.

【0017】〔S9:加熱圧縮成形〕所望比の混合体を
秤量し、これを金型内に充填して加熱する。この時の成
形温度はポリエチレン樹脂の成形適温に準じ、およそ1
60℃に設定される。
[S9: Heat compression molding] A mixture having a desired ratio is weighed, filled in a mold and heated. The molding temperature at this time is approximately 1 according to the appropriate molding temperature of polyethylene resin.
Set to 60 ° C.

【0018】〔S10:取出し〕成形時において、成形
体が半固化状態にあるうちに、金型より成形途中の成形
体(半成形体)が取り出される。
[S10: Removal] During molding, while the molded body is in a semi-solid state, the molded body (semi-molded body) in the middle of molding is removed from the mold.

【0019】〔S11:再加圧(冷却)〕金型より取り
出された半成形体は、再度金型に装填して再加圧を行
い、そのまま冷却して製品の品質をより安定させる。
[S11: Repressurization (Cooling)] The semi-molded product taken out of the mold is loaded into the mold again, repressurized, and cooled as it is to further stabilize the quality of the product.

【0020】〔S12:取出し〕形成された成形体は金
型より取り出され、必要に応じて仕上げ加工を施し完成
品となる。
[S12: Removal] The formed body is removed from the mold and subjected to finishing if necessary to obtain a finished product.

【0021】以下に、本発明に係わる藻類を原材料とす
る成形体の製造方法およびその成形体の第2実施形態に
ついて、図2を参照して説明する。図2も、藻類として
クロレラを原材料とする成形体を製造するものである
が、以下に説明するように、途中にポリエチレン樹脂と
クロレラのとの混合体をペレット化する工程が付加され
ている。
Hereinafter, a second embodiment of a method for producing a molded article using algae as a raw material and a molded article according to the present invention will be described with reference to FIG. FIG. 2 also shows the production of a molded article using chlorella as a raw material as an algae, but as described below, a step of pelletizing a mixture of a polyethylene resin and chlorella is added in the middle.

【0022】〔S21:ポリエチレン樹脂の溶融〕成形
材として、ポリエチレン樹脂が採用される。このポリエ
チレン樹脂は、ペレット状のものが提供されるが、ここ
では、加熱溶解してポリエチレン樹脂を溶融状態とす
る。
[S21: Melting of polyethylene resin] A polyethylene resin is used as the molding material. The polyethylene resin is provided in the form of pellets. Here, the polyethylene resin is heated and melted to bring the polyethylene resin into a molten state.

【0023】〔S22:微細藻〕クロレラは、ペレット
状,あるいは粉末状等に乾燥,加工されたものが採用さ
れる。
[S22: Microalgae] Chlorella dried and processed into pellets or powders is used.

【0024】〔S23:混合〕溶融状態のポリエチレン
樹脂と乾燥クロレラとを混合して、高温状態で混練し、
均質状態の混合体を作製する。
[S23: Mixing] The polyethylene resin in a molten state and dry chlorella are mixed and kneaded at a high temperature.
Make a homogeneous mixture.

【0025】〔S24:冷却〕S23で作製された混合
体を冷却するとともに、可塑性を有するものを次工程に
供給する。
[S24: Cooling] The mixture prepared in S23 is cooled, and a mixture having plasticity is supplied to the next step.

【0026】〔S25:ペレット化〕ポリエチレン樹脂
とクロレラとの混合体をペレット化する。このペレット
化により取扱い性が高められるとともに、ポリエチレン
樹脂とクロレラとの均質混合化が図られる。
[S25: Pelletizing] A mixture of polyethylene resin and chlorella is pelletized. This pelletization enhances the handleability and homogenous mixing of the polyethylene resin and chlorella.

【0027】〔S26:秤量〕成形体形成に必要なペレ
ット量が秤量される。
[S26: Weighing] The amount of pellets necessary for forming the molded body is weighed.

【0028】〔S27:加熱圧縮成形〕ペレットを成形
金型内部に充填して溶解し、およそ160℃の温度で成
形する。
[S27: Heat Compression Molding] The pellets are filled in a molding die, dissolved and molded at a temperature of about 160 ° C.

【0029】〔S28:取出し〕S10に準じて、半成
形体が金型より取り出される。
[S28: Take-out] According to S10, the half-molded body is taken out of the mold.

【0030】〔S29:再加圧(冷却)〕S11に準じ
て、半成形体を再度金型に装填して再加圧および冷却
し、製品の品質を安定させる。
[S29: Re-pressurization (cooling)] According to S11, the semi-molded body is again loaded in the mold, re-pressurized and cooled, and the quality of the product is stabilized.

【0031】〔S30:取出し〕成形された成形品は金
型より取り出され、必要に応じて仕上げ加工を施し完成
品となる。
[S30: Take-out] The formed product is taken out of the mold and subjected to finishing if necessary to obtain a finished product.

【0032】[0032]

【実施例】以下、藻類を原材料とする成形体の製造実施
例について図3ないし図5を参照して説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the production of a molded article using algae as a raw material will be described below with reference to FIGS.

【0033】図3は、ポリエチレン樹脂からなる成形体
の成形圧力と引張強度との関係を計測した結果を示すも
のである。成形体の仕様は以下の通りである。 材料: 高密度ポリエチレン樹脂(HDPE) 成形温度: 160℃ 成形時間: 2分
FIG. 3 shows the result of measuring the relationship between the molding pressure and the tensile strength of a molded article made of polyethylene resin. The specifications of the molded body are as follows. Material: High density polyethylene resin (HDPE) Molding temperature: 160 ° C Molding time: 2 minutes

【0034】図3から明らかなように、成形圧力を1〜
7MPaの範囲で変化させた場合に、引張強度は24〜
25MPaを示し、顕著な値差が認められない。これ
は、成形圧力が1〜7MPaの範囲においては、成形圧
力が成形体の引張強度に及ぼす影響は極めて小さいこと
を意味する。
As is apparent from FIG.
When changed in the range of 7 MPa, the tensile strength is 24 to
25 MPa, and no remarkable value difference is observed. This means that when the molding pressure is in the range of 1 to 7 MPa, the influence of the molding pressure on the tensile strength of the molded body is extremely small.

【0035】図4は、高密度ポリエチレン成形体におけ
る成形温度と引張強度との関係を計測した結果を示すも
のである。使用した成形体(サンプル1,サンプル2)
の仕様は以下の通りである。 〔サンプル1(○印)〕 ポリエチレン樹脂の形状: ペレット 成形圧力: 2.2MPa 成形時間: 2分 〔サンプル2(△印)〕 ポリエチレン樹脂の形状: 細片 成形圧力: 2.2MPa 成形時間: 2分
FIG. 4 shows the result of measuring the relationship between the molding temperature and the tensile strength of the high-density polyethylene molded body. Moldings used (Sample 1, Sample 2)
Is as follows. [Sample 1 (marked with ○)] Shape of polyethylene resin: pellets Molding pressure: 2.2 MPa Molding time: 2 minutes [Sample 2 (marked with △)] Shape of polyethylene resin: strip Molding pressure: 2.2 MPa Molding time: 2 Minute

【0036】図4から明らかなように、成形温度を15
0〜190℃の範囲で変化させた場合に、引張強度は2
5〜26MPaを示し、顕著な値差が認められない。こ
れは、成形温度が150〜190℃の範囲においては、
成形温度が成形体の引張強度に及ぼす影響は極めて小さ
いことを意味する。
As is clear from FIG.
When changed in the range of 0 to 190 ° C., the tensile strength is 2
5 to 26 MPa, and no remarkable value difference is observed. This means that when the molding temperature is in the range of 150 to 190 ° C,
This means that the influence of the molding temperature on the tensile strength of the compact is extremely small.

【0037】図5は、高密度ポリエチレン樹脂とクロレ
ラとの成形体におけるクロレラの含有量と引張強度との
関係を計測した結果を示すものである。成形体の仕様は
以下の通りである。 原材料: クロレラ(粒径:数μm) 熱可塑性樹脂: 高密度ポリエチレン樹脂(粒径:1m
m以下) 成形温度: 160℃ 成形時間: 2分 成形圧力: 2.2MPa
FIG. 5 shows the result of measurement of the relationship between the content of chlorella and the tensile strength in a molded article of a high-density polyethylene resin and chlorella. The specifications of the molded body are as follows. Raw material: Chlorella (particle size: several μm) Thermoplastic resin: High-density polyethylene resin (particle size: 1 m)
m) Molding temperature: 160 ° C Molding time: 2 minutes Molding pressure: 2.2 MPa

【0038】図5から明らかなように、クロレラ混合比
を0〜60%の範囲で変化させた場合に、引張強度が2
5MPaから10MPaに徐々に減少しているのが認め
られる。また、この時、加熱圧縮成形によるクロレラの
褐色変化は認められなかった。
As apparent from FIG. 5, when the chlorella mixture ratio was changed in the range of 0 to 60%, the tensile strength was 2%.
A gradual decrease from 5 MPa to 10 MPa is observed. At this time, no brown change of chlorella due to the heat compression molding was observed.

【0039】以上より、高密度ポリエチレン樹脂は、成
形圧力1〜7MPaの範囲,成形温度150〜190℃
の範囲において、引張強度に及ぼす影響がほとんど認め
られないため、成形体の引っ張り強度(所望強度)に応
じてクロレラの混合比を設定すればよい。つまり、比較
的広い範囲の樹脂成形条件を設定することができるた
め、製品を様々な用途に十分に適用させることができ
る。
As described above, the high-density polyethylene resin has a molding pressure of 1 to 7 MPa and a molding temperature of 150 to 190 ° C.
In the range described above, there is almost no effect on the tensile strength. Therefore, the mixing ratio of chlorella may be set according to the tensile strength (desired strength) of the molded article. That is, since a relatively wide range of resin molding conditions can be set, the product can be sufficiently applied to various uses.

【0040】[0040]

【発明の効果】本発明に係わる藻類を原材料とする成形
体の製造方法およびその成形体によれば、以下の効果を
奏する。 (1) 塩化ビニールを使用する場合と比較して塩素を
含有しないポリエチレン樹脂を使用することにより、製
品または端材を焼却処分する必要が生じた場合にあって
も塩素ガス等の有害物質の発生を防止することができ
る。 (2) 成形温度を低くしてクロレラの褐色(劣化)を
防止することにより、褐色変防止剤(パラフィン等)を
使用せずに成形品を形成することができる。 (3) 成形温度を低くしてクロレラの劣化を防止する
とともに、成形体を再加圧してり製品を安定させること
により、塩化ビニールと比較して褐変防止剤や安定剤等
の添加剤の使用を省略することができる。 (4) 炭水化物の組成に近いポリエチレン樹脂と植物
体(炭水化物)とを混合して成形体を形成することによ
り、燃えかす中に重金属等の有害物質を残留させずに焼
却することができる。 (5) 粉末状の混合体を直接金型に充填して加熱圧縮
することにより、熱エネルギーを多く必要とする熱混和
や再ペレット化を省略することができる。 (6) 熱可塑性樹脂および原材料の微粉化して粉末状
の混合体を作製することにより、混合体の均等混合を加
熱せずに行うことができる。 (7) ポリエチレン樹脂粉体と微粉末状藻体とを混合
することにより、均質混合時の作業時間を大幅に短縮す
ることができる。
According to the method for producing a molded article using algae as a raw material and the molded article according to the present invention, the following effects can be obtained. (1) By using polyethylene resin that does not contain chlorine as compared with the case of using vinyl chloride, even if it becomes necessary to incinerate products or scrap materials, generation of harmful substances such as chlorine gas Can be prevented. (2) By lowering the molding temperature to prevent brown (deterioration) of chlorella, a molded article can be formed without using a browning inhibitor (paraffin or the like). (3) Use of additives such as anti-browning agents and stabilizers compared to vinyl chloride by lowering the molding temperature to prevent chlorella degradation and by re-pressing the molded body to stabilize the product. Can be omitted. (4) By mixing a polyethylene resin having a carbohydrate composition and a plant body (carbohydrate) to form a molded body, it is possible to incinerate without leaving harmful substances such as heavy metals in the burning. (5) By directly filling the powdery mixture into a mold and compressing it by heating, it is possible to omit heat mixing and repelletization that require a large amount of thermal energy. (6) By finely pulverizing the thermoplastic resin and the raw material to produce a powdery mixture, the mixture can be uniformly mixed without heating. (7) By mixing the polyethylene resin powder and the fine powdery algal body, the working time at the time of homogeneous mixing can be greatly reduced.

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

【図1】 本発明に係わる藻類を原材料とする成形体の
製造方法およびその成形体の第1実施形態における実施
工程のフローチャートである。
FIG. 1 is a flowchart of a method for producing a molded article using algae as a raw material according to the present invention, and the steps of an embodiment of the molded article in the first embodiment.

【図2】 本発明に係わる藻類を原材料とする成形体の
製造方法およびその成形体の第2実施形態における実施
工程のフローチャートである。
FIG. 2 is a flowchart of a method for producing a molded article using algae as a raw material according to the present invention and a process of implementing the molded article in a second embodiment.

【図3】 ポリエチレン樹脂成形体の成形圧力と引張強
度との関係曲線図である。
FIG. 3 is a relationship curve diagram between a molding pressure and a tensile strength of a polyethylene resin molded article.

【図4】 ポリエチレン樹脂成形体の成形温度と引張強
度との関係曲線図である。
FIG. 4 is a graph showing the relationship between the molding temperature and the tensile strength of a polyethylene resin molded article.

【図5】 クロレラを混合したときの混合比と引張強度
との関係曲線図である。
FIG. 5 is a graph showing the relationship between the mixing ratio and the tensile strength when chlorella is mixed.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C08L 23/06 C08L 23/06 C12N 1/12 ZAB C12N 1/12 ZABC // B29K 23:00 105:16 (72)発明者 山下 正忠 東京都港区西新橋2丁目8番11号 財団法 人 地球環境産業技術研究機構内 (72)発明者 大月 利 東京都港区西新橋2丁目8番11号 財団法 人 地球環境産業技術研究機構内 (72)発明者 廣津 孝弘 香川県高松市林町2217番14 工業技術院 四国工業技術研究所内 (72)発明者 壁谷 洋 香川県高松市林町2217番14 工業技術院 四国工業技術研究所内 (72)発明者 北川 良一 香川県高松市林町2217番14 工業技術院 四国工業技術研究所内──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification symbol FI C08L 23/06 C08L 23/06 C12N 1/12 ZAB C12N 1/12 ZABC // B29K 23:00 105: 16 (72) Inventor Masatada Yamashita 2-8-11 Nishi-Shimbashi, Minato-ku, Tokyo Foundation of the Institute for Global Environmental Technology (72) Inventor Toshi Otsuki 2-8-11 Nishi-Shimbashi, Minato-ku, Tokyo Global Environmental Industry Within the Research Institute of Technology (72) Inventor Takahiro Hirotsu 2217-14 Hayashi-cho, Takamatsu-shi, Kagawa Prefecture Within the Institute of Industrial Technology, Shikoku Institute of Industrial Technology (72) Inventor Hiroshi Kamiya, 2217-14 Hayashi-cho, Takamatsu-shi, Kagawa Prefecture Institute of Industrial Science Shikoku Industrial Technology In-house (72) Inventor Ryoichi Kitagawa 2217-14 Hayashi-cho, Takamatsu-shi, Kagawa Pref.

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 熱可塑性樹脂に藻類を混合してなる成形
体の成形方法であって、熱可塑性樹脂としてポリエチレ
ン樹脂を選択し、成形体原材料として炭酸ガスを固定し
た藻類が選択されることを特徴とする藻類を原材料とす
る成形体の製造方法。
1. A method for molding a molded article obtained by mixing algae with a thermoplastic resin, wherein a polyethylene resin is selected as the thermoplastic resin, and carbon dioxide-fixed algae is selected as a raw material of the molded article. A method for producing a molded product using algae as a raw material.
【請求項2】 ポリエチレン樹脂を常温もしくはそれ以
下の低温雰囲気で粉砕して微粉体化することを特徴とす
る請求項1記載の藻類を原材料とする成形体の製造方
法。
2. The method according to claim 1, wherein the polyethylene resin is pulverized in a low-temperature atmosphere at room temperature or lower to form a fine powder.
【請求項3】 ポリエチレン樹脂を粒径が1mm以下の
微粉体に加工することを特徴とする請求項2記載の藻類
を原材料とする成形体の製造方法。
3. The method according to claim 2, wherein the polyethylene resin is processed into a fine powder having a particle size of 1 mm or less.
【請求項4】 炭酸ガスを固定した藻類を粉砕して微粉
末状藻体に加工することを特徴とする請求項1、2また
は3記載の藻類を原材料とする成形体の製造方法。
4. The method for producing a molded product using algae as a raw material according to claim 1, wherein the algae to which carbon dioxide is fixed are crushed and processed into fine powdery algal bodies.
【請求項5】 藻体として炭酸ガスを固定したクロレラ
が選択されることを特徴とする請求項1、2、3または
4記載の藻類を原材料とする成形体の製造方法。
5. The method for producing a molded article using algae as a raw material according to claim 1, wherein a chlorella in which carbon dioxide is fixed is selected as the algal body.
【請求項6】 ポリエチレン樹脂粉体と微粉末状藻体と
を混合する工程と、混合体を金型に充填して加熱圧縮し
成形体を製造する工程と、可塑状態の成形体を金型から
取り出して再度加圧して冷却する工程とを有することを
特徴とする請求項1、2、3、4または5記載の藻類を
原材料とする成形体の製造方法。
6. A step of mixing a polyethylene resin powder and a fine powdery algal body, a step of filling the mixture into a mold, and heating and compressing to produce a molded article; 6. The method for producing a molded product using algae as a raw material according to claim 1, further comprising a step of taking out of the algae and cooling again by pressurizing.
【請求項7】 熱可塑性樹脂に藻類を混合してなる成形
体の成形方法であって、溶融状態のポリエチレン樹脂と
藻類とを混合する工程と、ポリエチレン樹脂と藻類との
混合物をペレット化する工程と、前記ペレットを金型に
充填して加熱圧縮して成形体を成形する工程とを有する
請求項1、4、5または6記載の成形体の製造方法。
7. A method for molding a molded article obtained by mixing algae with a thermoplastic resin, comprising the steps of: mixing a polyethylene resin and an algae in a molten state; and pelletizing a mixture of the polyethylene resin and the algae. 7. The method for producing a molded article according to claim 1, further comprising the steps of: filling the pellet into a mold, heating and compressing the molded article to form a molded article.
【請求項8】 ポリエチレン樹脂粉体と、光合成反応に
より炭酸ガスを固定し微粉末処理を行った微粉末状藻体
とを均等混合することによって成形されることを特徴と
する藻類を原材料とする成形体。
8. An algae characterized by being formed by uniformly mixing a polyethylene resin powder and a finely powdered algal body that has been subjected to a fine powder treatment by fixing carbon dioxide gas by a photosynthetic reaction. Molded body.
【請求項9】 ポリエチレン樹脂粉体と、光合成反応に
より炭酸ガスを固定し微粉末処理を行った微粉末状のク
ロレラ等の微細藻とを均等混合することによって成形さ
れることを特徴とする藻類を原材料とする請求項7記載
の成形体。
9. An algae formed by uniformly mixing a polyethylene resin powder and a microalga such as chlorella in the form of a fine powder, which has been subjected to a fine powder treatment by fixing carbon dioxide by a photosynthetic reaction. The molded article according to claim 7, wherein the molded article is a raw material.
JP7246697A 1997-03-25 1997-03-25 Method for producing molded body using algae as raw material Expired - Lifetime JP3749921B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7246697A JP3749921B2 (en) 1997-03-25 1997-03-25 Method for producing molded body using algae as raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7246697A JP3749921B2 (en) 1997-03-25 1997-03-25 Method for producing molded body using algae as raw material

Publications (2)

Publication Number Publication Date
JPH10265584A true JPH10265584A (en) 1998-10-06
JP3749921B2 JP3749921B2 (en) 2006-03-01

Family

ID=13490124

Family Applications (1)

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

Country Link
JP (1) JP3749921B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010125490A2 (en) 2009-04-28 2010-11-04 Kimberly-Clark Worldwide, Inc. Algae-blended compositions for thermoplastic articles
ES2903291A1 (en) * 2020-09-30 2022-03-31 Garcia Marcos Carrero Recycling and recyclable product based on vegetable fibers from debris (Machine-translation by Google Translate, not legally binding)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010125490A2 (en) 2009-04-28 2010-11-04 Kimberly-Clark Worldwide, Inc. Algae-blended compositions for thermoplastic articles
EP2424937A2 (en) * 2009-04-28 2012-03-07 Kimberly-Clark Worldwide, Inc. Algae-blended compositions for thermoplastic articles
EP2424937A4 (en) * 2009-04-28 2012-10-31 Kimberly Clark Co Algae-blended compositions for thermoplastic articles
US8524811B2 (en) 2009-04-28 2013-09-03 Kimberly-Clark Worldwide, Inc. Algae-blended compositions for thermoplastic articles
ES2903291A1 (en) * 2020-09-30 2022-03-31 Garcia Marcos Carrero Recycling and recyclable product based on vegetable fibers from debris (Machine-translation by Google Translate, not legally binding)

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