JP3581018B2 - Method for producing clay-containing fatty acid composition and the like - Google Patents

Method for producing clay-containing fatty acid composition and the like Download PDF

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Publication number
JP3581018B2
JP3581018B2 JP14435298A JP14435298A JP3581018B2 JP 3581018 B2 JP3581018 B2 JP 3581018B2 JP 14435298 A JP14435298 A JP 14435298A JP 14435298 A JP14435298 A JP 14435298A JP 3581018 B2 JP3581018 B2 JP 3581018B2
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Prior art keywords
clay
fatty acid
composition
oils
fats
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JP14435298A
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JPH11335692A (en
Inventor
洋一 白川
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Adeka Corp
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Asahi Denka Kogyo KK
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/74Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Detergent Compositions (AREA)
  • Fats And Perfumes (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、白土含有脂肪酸組成物等の製造方法に関し、詳しくは、廃白土を有効利用し、これから脂肪酸組成物や石鹸(金属石鹸を含む)を製造しようとするものである。
【0002】
【従来の技術及び発明が解決しようとする課題】
油脂産業などにおいては、例えば油脂を精製する工程で漂白を行なうために油脂を白土で処理することが行なわれている。
油脂を処理した白土には、濾過後にも約25〜40重量%の油脂が吸着されているが、該油脂を工業的に適正なコストで分離することは難しいものであった。
しかし、資源節約、廃棄物減量の観点から、白土に吸着されている油脂の有効活用が要望されている。
このような観点から、油脂を含有する廃白土を原料としてクレンザーを製造する試みが特開昭60−84399号公報に記載されている。しかし、この方法は苛性ソーダを高温で使用するため、白土が苛性ソーダと反応して珪酸ソーダが副生し、用途が制限されてしまう等の欠点を有していた。
【0003】
従って、本発明の目的は、上記のような欠点がなく、油脂を含有する廃白土を有効活用できる白土含有脂肪酸組成物及び白土含有石鹸の製造方法を提供することにある。
【0004】
【課題を解決するための手段】
本発明は、油脂の処理に使用した廃白土100重量部に、リパーゼ水溶液10〜60重量部を均一に混合して粘土状組成物とし、該粘土状組成物を酵素処理することを特徴とする白土含有脂肪酸組成物の製造方法、及び該製造方法により製造された白土含有脂肪酸組成物を中和することを特徴とする白土含有石鹸(金属石鹸を含む)の製造方法を提供することにより、上記目的を達成したものである。
【0005】
【発明の実施の形態】
以下、先ず第一発明である白土含有脂肪酸組成物の製造方法について詳述する。
本発明に使用する廃白土は、油脂の処理に使用した廃白土であり、例えば、動植物油脂の精製工程中の脱色工程等では活性白土を油脂に加えて加熱し、油脂中に存在する色素類を吸着させて除去することが行なわれており、色素類を吸着させた白土はフィルター等によって濾過され油脂と分離されるが、この濾過残さ( 圧搾濾過白土)を一般に廃白土と称しており、このような廃白土を使用することができる。
廃白土中に含まれる油脂は、特に限定されるものではなく、牛脂、豚脂、魚油、鯨油などの動物油脂、パーム油、パーム核油、大豆油、菜種油、コーン油等の植物油脂、これらの動植物油脂の混合油脂、及びこれらの油脂の水素添加油脂(硬化油)、さらにこれらの油脂のエステル交換油脂など、どのような油脂でも良い。
【0006】
本発明においては、上記廃白土100重量部に対して、リパーゼ水溶液を10〜60重量部、好ましくは15〜50重量部使用する。
リパーゼ水溶液に使用するリパーゼは、油脂分解活性を有するものであればどのようなものでも良く、微生物由来のリパーゼでも、植物由来のリパーゼでも、膵臓由来のリパーゼ(パンクレアチンリパーゼ)でも良い。
リパーゼ水溶液の廃白土に対する使用量は上記の通りであり、少なすぎると廃白土に対して均一に水分が行き渡らず酵素処理が不十分となりやすい。逆に多すぎると組成物が粘土状とならず水分が分離しやすく、結果的に廃白土中の油脂分に均一にリパーゼが作用せず酵素処理が不十分となりやすい。
ここで、「粘土状」なる語句は厳密に定義されるものではなく、水分の分離が起こらない程度であれば良いので、所謂ペースト状であっても支障無い。
【0007】
リパーゼの使用量は、廃白土に含有されている油脂の量などによって適宜従来の油脂の酵素処理において使用されている通常の量を使用すれば良いが、概ね廃白土中の油脂分に対して0.01〜0.5重量%程度であれば支障ない。
【0008】
本発明は上記廃白土とリパーゼ水溶液を均一に混合して粘土状組成物とした後、リパーゼ水溶液中のリパーゼによって油脂を酵素処理し、分解する。
酵素処理はリパーゼの活性な温度域で行なえば良く、例えば概ね20℃〜50℃であれば良い。酵素処理の時間は特に限定されず、所望とする油脂分解率に応じて時間を調節すれば良いが、例えば概ね1時間〜5日程度行なえば実用的な結果を得ることができる。
また、上記酵素処理は、このような条件の下で、組成物をそのまま放置しておくことにより行っても良いし、組成物をニーダーなどで混練しながら酵素処理しても良く、一時的な混練(単数回でも複数回でも良い)を行っても良い。
【0009】
このようにして得られる本発明の白土含有脂肪酸組成物は、粘土状組成物のままでもクレンザー等として使用することができるが、乾燥させれば肥料、堆肥発酵促進剤、土壌改良剤等として良好に使用することができる。
【0010】
次に、第二発明である白土含有石鹸(金属石鹸を含む)の製造方法について詳述する。
本第二発明においては、上記の第一発明で製造された白土含有脂肪酸組成物を中和する。中和は公知の方法によれば良く、例えば、上記白土含有脂肪酸組成物に、水酸化ナトリウム、水酸化カリウム等の苛性アルカリ、炭酸ナトリウム、炭酸カリウム等の炭酸アルカリなどの公知の中和剤を添加すれば石鹸とすることができる。又、水酸化カルシウムなどを使用して中和すれば金属石鹸とすることができる。
【0011】
中和剤の量は、組成物の酸価を測定して、ほぼ当量となるように使用すれば良く、特に限定されない。
中和剤は、水溶液であっても、固体(粉末)状であっても良い。水溶液として使用すると組成物はスラリー状となるので均一な混合が容易であるが、最終生成物の形態として低水分量の形態を所望する場合は脱水の工程が必要となるので、このような場合は固体(粉末)状のまま添加し、ニーダーで混練すれば粘土状組成物の形態のまま中和することができる。
【0012】
このようにして得られる本発明の白土含有石鹸は、粘土状組成物のままでも洗浄剤、特にクレンザーとして良好に使用できるものであるが、さらに水分を除去することにより粉末状としても、逆に若干水分を増加させてペースト状としても良好なものとなる。
水酸化カルシウムなどで中和して金属石鹸とする場合などでは、粉末状あるいはスラリー状とすればセメント添加剤として良好に使用できる。
【0013】
【実施例】
以下に実施例を挙げて本発明を具体的に説明する。
【0014】
(実施例−1)
牛脂系廃白土(含油分38.5重量%、酸価1.9)1kgを小型ニーダーに入れ、室温下、攪拌しながらリパーゼ(リパーゼOF:名糖産業(株)製)0.5gを400gの水に溶解した水溶液をニーダー内の廃白土に滴下しながら、30分間かけて混合した。
リパーゼ水溶液が廃白土にすべて吸収され柔らかい粘土状の混合物(粘土状組成物)になったことを確認後、内容物をチャック付きポリ袋に入れて密封し、40℃の恒温槽内に8時間放置した。
8時間後の廃白土中の油分の酸価は152で、油脂の分解率(酸価×1/2で計算)は76%と半固体状態でも油脂の分解は進んでいることが確認された。
この粘土状の混合物(白土含有牛脂脂肪酸組成物)をニーダーに入れ、室温下、苛性ソーダ70gを水700gに溶解した水溶液を攪拌しながらニーダー内に滴下すると、直ちに発熱を伴いながら中和反応が進み、増粘して内容物が淡黄色変化した。
ニーダーのジャケットに温水を流して、内部温度を50℃に保ち、未中和部分を完全に中和する為に10分間攪拌を続けると、ペースト状の白土を含有したままの牛脂脂肪酸のナトリウム石鹸が得られた。
この中和物をアルミ製のトレイに広げ、40℃で通風乾燥後、粉砕して黄白色の白土含有牛脂脂肪酸石鹸1050gを得た。
上記で得られた粉末状の石鹸を、フタ付のガラスビンに1g秤り、水50gを加えて、50回振盪すると非常に良く起泡し、30分後の泡持ちも良好であった。又、この石鹸を、水を含ませたスポンジに付け、油性マジックインキを塗ったガラス製のビーカー及び機械油を塗布したステンレス板の表面を磨くと、市販のクレンザーと同等の研磨、洗浄効果が認められた。
【0015】
(実施例−2)
実施例−1でリパーゼの量を1.0gとすると他は、同様に操作を行ない、得られた粘土状の混合物を40℃で8時間保った。
8時間後の廃白土中の油分の酸価は188であった。この含水油脂分解物をアルミ製トレイ上に拡げて、40℃で通風乾燥し、粉砕して灰白色の白土含有牛脂脂肪酸組成物の粉末1035gを得た。
ここで得られた粉末は40重量%近くの脂肪酸を含有するが、常温下の外観は油を含むようには見えない乾燥した、流動性のある粉体であった。
この粉末を用いて鋼板を研磨すると、このままでも充分研磨効果が認められ、研磨後の表面は光沢、撥水性にすぐれていた。
【0016】
(実施例−3)
パーム油廃白土(含油分39.0重量%、酸価1.5)1kgを小型ニーダーに入れ、水200gにリパーゼOFを1.0g溶解したリパーゼ水溶液を、室温下、攪拌しながら、ニーダー内に滴下、混合した。
リパーゼ水溶液はすべて廃白土に吸収され、外観はやや湿った粉体となった。この混合物(粘土状組成物)をチャック付ポリ袋に入れ室温(約20℃)に24時間放置した。24時間放置後の廃白土中の油分の酸価は175であり、常温下でも充分油脂の分解は進んでいた。
この含水廃白土(白土含有パーム油脂肪酸組成物)をニーダーに入れ、苛性ソーダ70gを水500gに溶解した水溶液を攪拌下、ニーダー内に滴下、中和を行ない、50℃に昇温して更に10分間攪拌して、黄色粘性のあるペースト状の白土含有パーム油脂肪酸ナトリウム石鹸を得た。
このペースト状の石鹸を乾燥、粉砕して黄白色の粉末1050gを得た。
得られた粉末の1gを用いて、実施例−1と同様に起泡試験を行った所、牛脂系廃白土より同様な操作で得られる石鹸より、更に起泡性、泡持ちが良いことが認められた。
【0017】
(実施例−4)
実施例−3でリパーゼを0.2g、水を300gとする以外は同様に操作を行い、室温下に48時間放置後の廃白土中の油分の酸価を測定すると120であった。
実施例−3と同様に中和、乾燥、粉砕して白土含有パーム油脂肪酸ナトリウム石鹸の粉末1033gを得た。この粉末1gの起泡性、泡の持ちを同様な方法で比較したところ、実施例−3で得られた石鹸より劣る結果ではあったが、クレンザーとして充分に使用可能であった。
【0018】
(実施例−5)
大豆硬化油(mp.36℃)の廃白土(含油分37.2重量%)1kgを用いる他は、実施例−2と同様に操作を行ない、白土含有大豆硬化油脂肪酸組成物を得た。次に得られた白土含有大豆硬化油脂肪酸組成物の全量をニーダーに入れ、無水炭酸ナトリウム180g及び水800gを攪拌下、混合した。若干の発熱を伴いながら中和反応が進み、やや粘性のあるペースト状の白土含有大豆硬化油脂肪酸石鹸が得られた。
乾燥、粉砕して白土含有大豆硬化油脂肪酸石鹸の粉末1120gを得た。この組成物1gの起泡性、泡の持ちは、牛脂系廃白土からの石鹸と同様であった。
【0019】
(比較例−1)
パーム油廃白土(含油分39.0重量%、酸価1.5)1kgを小型ニーダーに入れ、苛性ソーダ70gを含む1kgの水をニーダーに投入して、内部を85〜90℃に保って2時間、攪拌を継続した。2時間後、黄褐色のスラリーを2gとり、水50gと混合して、起泡試験を行ったが、ほとんど起泡力がなく、スラリーの一部を硫酸酸性にした後の抽出油分酸価も16と分解も極めて低いことが認められた。
【0020】
(実施例−6)
実施例−2で得られた白土含有牛脂脂肪酸組成物の粉末500gに消石灰粉末25gをニーダー内で混合し、これに水250gを加え、70℃に加熱しながら攪拌し、再度粉末になるまで水を蒸発させた。
ここで得られた粉末は、撥水性と固体潤滑性に優れ、脂肪酸を吸着している白土粒子表面で、カルシウム石鹸が生成していることが認められた。
【0021】
【発明の効果】
本発明の効果は、油脂を含有する廃白土を有効活用できる白土含有脂肪酸組成物及び白土含有石鹸の製造方法を提供したことにある。
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method for producing a clay-containing fatty acid composition and the like, and more particularly, to effectively use waste clay to produce a fatty acid composition and a soap (including metal soap) therefrom.
[0002]
Problems to be solved by the prior art and the invention
In the fats and oils industry, for example, fats and oils are treated with clay to perform bleaching in the step of refining fats and oils.
Approximately 25 to 40% by weight of the fats and oils is adsorbed on the clay treated with the fats and oils even after filtration, but it has been difficult to separate the fats and oils at an industrially appropriate cost.
However, effective utilization of fats and oils adsorbed on clay is demanded from the viewpoint of resource saving and waste reduction.
From such a viewpoint, Japanese Patent Application Laid-Open No. 60-84399 describes an attempt to produce a cleanser using waste clay containing oils and fats as a raw material. However, in this method, since caustic soda is used at a high temperature, the clay has a drawback that it reacts with caustic soda to produce sodium silicate as a by-product, thereby restricting the use.
[0003]
Accordingly, an object of the present invention is to provide a clay-containing fatty acid composition and a method for producing a clay-containing soap, which do not have the above-mentioned drawbacks and can effectively utilize waste clay containing oils and fats.
[0004]
[Means for Solving the Problems]
The present invention is characterized in that 10 to 60 parts by weight of an aqueous lipase solution is uniformly mixed with 100 parts by weight of waste clay used for treating fats and oils to obtain a clay-like composition, and the clay-like composition is subjected to enzyme treatment. By providing a method for producing a clay-containing fatty acid composition, and a method for producing a clay-containing soap (including a metal soap), the method comprising neutralizing the clay-containing fatty acid composition produced by the production method. The purpose has been achieved.
[0005]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, first, the method for producing the clay-containing fatty acid composition of the first invention will be described in detail.
The waste clay used in the present invention is waste clay used for the treatment of fats and oils. It is performed by adsorbing and removing the clay, and the clay adsorbing the pigments is filtered by a filter or the like and separated from fats and oils. The filtration residue (press-filtered clay) is generally referred to as waste clay. Such waste clay can be used.
The fats and oils contained in the waste clay are not particularly limited, and vegetable fats and oils such as tallow, lard, fish oil, whale oil, etc., palm oil, palm kernel oil, soybean oil, rapeseed oil, corn oil, etc. Any fats and oils such as mixed fats and oils of animal and vegetable fats and oils, hydrogenated fats and oils (hardened oils) of these fats and oils, and transesterified fats and oils of these fats and oils may be used.
[0006]
In the present invention, the lipase aqueous solution is used in an amount of 10 to 60 parts by weight, preferably 15 to 50 parts by weight, based on 100 parts by weight of the waste clay.
The lipase used in the aqueous lipase solution may be any lipase having an activity of decomposing fat and oil, and may be a lipase derived from a microorganism, a lipase derived from a plant, or a lipase derived from pancreas (pancreatin lipase).
The amount of the lipase aqueous solution used for the waste clay is as described above. If the amount is too small, moisture is not uniformly distributed to the waste clay and the enzyme treatment tends to be insufficient. Conversely, if the amount is too large, the composition does not become clay-like and water is easily separated. As a result, the lipase does not act uniformly on the fats and oils in the waste clay, and the enzyme treatment tends to be insufficient.
Here, the term "clay-like" is not strictly defined, and it is sufficient that the separation of water does not occur.
[0007]
The amount of lipase used may be a normal amount used in conventional enzymatic treatment of fats and oils depending on the amount of fats and oils contained in the waste clay, etc. There is no problem if it is about 0.01 to 0.5% by weight.
[0008]
In the present invention, the waste clay and the lipase aqueous solution are uniformly mixed to form a clay-like composition, and then the fats and oils are enzymatically treated with the lipase in the lipase aqueous solution and decomposed.
The enzymatic treatment may be carried out in a lipase active temperature range, for example, approximately 20 ° C to 50 ° C. The time for the enzyme treatment is not particularly limited, and the time may be adjusted according to the desired fat / oil decomposition rate. However, a practical result can be obtained by performing the treatment for about 1 hour to about 5 days, for example.
In addition, the enzyme treatment may be performed under such conditions by leaving the composition as it is, or may be subjected to enzyme treatment while kneading the composition with a kneader or the like, Kneading (single or multiple times) may be performed.
[0009]
The thus-obtained clay-containing fatty acid composition of the present invention can be used as a cleanser or the like even as a clay-like composition, but if dried, it can be used as a fertilizer, a compost fermentation promoter, a soil conditioner, etc. Can be used for
[0010]
Next, the method for producing clay-containing soap (including metal soap) according to the second invention will be described in detail.
In the second invention, the clay-containing fatty acid composition produced in the first invention is neutralized. Neutralization may be performed according to a known method.For example, a sodium hydroxide, a caustic alkali such as potassium hydroxide, sodium carbonate, a known neutralizing agent such as an alkali carbonate such as potassium carbonate may be added to the clay-containing fatty acid composition. If added, it can be made into a soap. In addition, metal soap can be obtained by neutralizing using calcium hydroxide or the like.
[0011]
The amount of the neutralizing agent is not particularly limited, as long as the acid value of the composition is measured and used so as to be approximately equivalent.
The neutralizing agent may be an aqueous solution or a solid (powder) form. When used as an aqueous solution, the composition is in the form of a slurry, so that uniform mixing is easy.However, if a low moisture content form is desired as the final product form, a dehydration step is required. Can be added in a solid (powder) form and kneaded with a kneader to neutralize in the form of a clay-like composition.
[0012]
The clay-containing soap of the present invention thus obtained can be used as a detergent, particularly as a cleanser, even as a clay-like composition. Even if it becomes paste-like by slightly increasing the water content, it becomes good.
In the case where the metal soap is neutralized with calcium hydroxide or the like, it can be favorably used as a cement additive in the form of a powder or slurry.
[0013]
【Example】
Hereinafter, the present invention will be described specifically with reference to examples.
[0014]
(Example-1)
400 g of lipase (Lipase OF: manufactured by Meito Sangyo Co., Ltd.) is placed in a small kneader with 1 kg of beef tallow waste clay (oil content 38.5% by weight, acid value 1.9) while stirring at room temperature. The aqueous solution dissolved in water was added dropwise to the waste clay in the kneader and mixed for 30 minutes.
After confirming that the lipase aqueous solution was completely absorbed into the waste clay and turned into a soft clay-like mixture (clay-like composition), the contents were sealed in a plastic bag with a zipper, and sealed in a 40 ° C constant temperature bath for 8 hours. I left it.
Eight hours later, the acid value of the oil in the waste clay was 152, and the decomposition rate of the fat (calculated by the acid value x 1/2) was 76%, confirming that the decomposition of the fat was progressing even in the semi-solid state. .
This clay-like mixture (clay-containing tallow fatty acid composition) is placed in a kneader, and at room temperature, an aqueous solution in which 70 g of caustic soda is dissolved in 700 g of water is dropped into the kneader with stirring. The content increased and the content changed to pale yellow.
Pour hot water into the jacket of the kneader, keep the internal temperature at 50 ° C, and continue stirring for 10 minutes to completely neutralize the unneutralized part. Soap of tallow fatty acid containing paste-like clay was gotten.
The neutralized product was spread on an aluminum tray, air-dried at 40 ° C., and pulverized to obtain 1,050 g of a yellow-white clay-containing tallow fatty acid soap.
1 g of the powdery soap obtained above was weighed into a glass bottle with a lid, 50 g of water was added, and the mixture was shaken 50 times to foam very well, and the foam retention after 30 minutes was also good. When this soap is applied to a sponge soaked in water and the surface of a glass beaker coated with oil-based magic ink and a stainless steel plate coated with machine oil are polished, the same polishing and cleaning effect as a commercially available cleanser is obtained. Admitted.
[0015]
(Example-2)
The operation was performed in the same manner as in Example 1, except that the amount of lipase was set to 1.0 g, and the obtained clay-like mixture was kept at 40 ° C. for 8 hours.
The acid value of the oil in the waste clay after 8 hours was 188. The hydrolyzed oil-and-fat decomposed product was spread on an aluminum tray, dried by ventilation at 40 ° C., and pulverized to obtain 1,035 g of an off-white clay-containing tallow fatty acid composition powder of gray clay.
The powder obtained here contained nearly 40% by weight of fatty acids, but was a dry, free-flowing powder that did not appear to contain oil at normal temperature.
When a steel plate was polished using this powder, a sufficient polishing effect was recognized as it was, and the surface after polishing was excellent in gloss and water repellency.
[0016]
(Example-3)
1 kg of palm oil waste clay (oil content: 39.0% by weight, acid value: 1.5) is placed in a small kneader, and an aqueous lipase solution obtained by dissolving 1.0 g of lipase OF in 200 g of water is stirred at room temperature in the kneader. And mixed.
All the lipase aqueous solution was absorbed by the waste clay, and the appearance became a slightly wet powder. This mixture (clay-like composition) was placed in a plastic bag with a zipper and left at room temperature (about 20 ° C.) for 24 hours. The acid value of the oil in the waste clay after standing for 24 hours was 175, and the decomposition of the oil and fat proceeded sufficiently even at room temperature.
This water-containing waste clay (white clay-containing palm oil fatty acid composition) is placed in a kneader, and an aqueous solution obtained by dissolving 70 g of caustic soda in 500 g of water is dropped into the kneader with stirring, neutralized, heated to 50 ° C., and further heated to 10 ° C. After stirring for minutes, a paste of white clay-containing palm oil fatty acid sodium soap having a yellow viscous paste was obtained.
The paste-like soap was dried and pulverized to obtain 1,050 g of yellowish white powder.
Using 1 g of the obtained powder, when a foaming test was performed in the same manner as in Example 1, it was found that the foaming property and the foam retention were better than the soap obtained from the beef tallow waste clay by the same operation. Admitted.
[0017]
(Example-4)
The same operation as in Example 3 was carried out except that the amount of lipase was 0.2 g and the amount of water was 300 g, and the acid value of the oil in the waste clay after standing at room temperature for 48 hours was 120.
Neutralization, drying and pulverization were carried out in the same manner as in Example 3 to obtain 1033 g of clay-containing palm oil fatty acid sodium soap powder. When the foaming property and foam retention of 1 g of this powder were compared in the same manner, the results were inferior to those of the soap obtained in Example 3, but were sufficiently usable as a cleanser.
[0018]
(Example-5)
The same operation as in Example 2 was carried out except that 1 kg of waste clay (oil content: 37.2% by weight) of hardened soybean oil (mp. 36 ° C) was used, to obtain a hardened soybean-containing hardened soybean oil fatty acid composition. Next, the whole amount of the obtained soy-cured oil-containing fatty acid composition containing clay was placed in a kneader, and 180 g of anhydrous sodium carbonate and 800 g of water were mixed with stirring. The neutralization reaction proceeded with some heat generation, and a slightly viscous paste-like soybean hardened oil fatty acid soap containing clay was obtained.
The powder was dried and pulverized to obtain 1120 g of powder of a clay-containing soybean hardened oil fatty acid soap. The foaming properties and foam retention of 1 g of this composition were the same as those of soap from waste tallow based clay.
[0019]
(Comparative Example-1)
1 kg of palm oil waste clay (oil content: 39.0% by weight, acid value: 1.5) is put in a small kneader, 1 kg of water containing 70 g of caustic soda is put into the kneader, and the inside is kept at 85-90 ° C. Stirring was continued for hours. Two hours later, 2 g of the yellow-brown slurry was taken and mixed with 50 g of water to conduct a foaming test. The foaming test had almost no foaming power, and the acid value of the extracted oil after acidifying a part of the slurry with sulfuric acid was also high. 16 and also very low decomposition.
[0020]
(Example-6)
500 g of the clay-containing tallow fatty acid composition powder obtained in Example-2 was mixed with 25 g of slaked lime powder in a kneader, 250 g of water was added thereto, and the mixture was stirred while being heated to 70 ° C., and the water was again obtained until the powder was obtained. Was evaporated.
The powder obtained here was excellent in water repellency and solid lubricity, and it was confirmed that calcium soap was generated on the surface of the clay particles adsorbing the fatty acid.
[0021]
【The invention's effect】
An effect of the present invention is to provide a clay-containing fatty acid composition and a method for producing a clay-containing soap that can effectively utilize waste clay containing oils and fats.

Claims (3)

油脂の処理に使用した廃白土100重量部に、リパーゼ水溶液10〜60重量部を均一に混合して粘土状組成物とし、該粘土状組成物を酵素処理することを特徴とする白土含有脂肪酸組成物の製造方法。100 to 100 parts by weight of waste clay used for the treatment of fats and oils, 10 to 60 parts by weight of an aqueous lipase solution are uniformly mixed to obtain a clay-like composition, and the clay-like composition is subjected to an enzyme treatment. Method of manufacturing a product. 粘土状組成物の酵素処理を、該粘土状組成物を間欠若しくは連続して混練しながら行う請求項1記載の白土含有脂肪酸組成物の製造方法。The method for producing a clay-containing fatty acid composition according to claim 1, wherein the enzymatic treatment of the clay-like composition is performed while intermittently or continuously kneading the clay-like composition. 請求項1又は2記載の製造方法により製造された白土含有脂肪酸組成物を中和することを特徴とする白土含有石鹸の製造方法。A method for producing a clay-containing soap, comprising neutralizing the clay-containing fatty acid composition produced by the production method according to claim 1.
JP14435298A 1998-05-26 1998-05-26 Method for producing clay-containing fatty acid composition and the like Expired - Lifetime JP3581018B2 (en)

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