JPH0134960B2 - - Google Patents
Info
- Publication number
- JPH0134960B2 JPH0134960B2 JP59202527A JP20252784A JPH0134960B2 JP H0134960 B2 JPH0134960 B2 JP H0134960B2 JP 59202527 A JP59202527 A JP 59202527A JP 20252784 A JP20252784 A JP 20252784A JP H0134960 B2 JPH0134960 B2 JP H0134960B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- parts
- fertilizer
- phosphoric acid
- decomposition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000007788 liquid Substances 0.000 claims description 62
- 239000003337 fertilizer Substances 0.000 claims description 53
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 34
- 150000003839 salts Chemical class 0.000 claims description 18
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 17
- 238000000354 decomposition reaction Methods 0.000 claims description 17
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 16
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 239000003513 alkali Substances 0.000 claims description 5
- 229920002261 Corn starch Polymers 0.000 claims description 4
- 240000008042 Zea mays Species 0.000 claims description 4
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 claims description 4
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims description 4
- 235000005822 corn Nutrition 0.000 claims description 4
- 239000008120 corn starch Substances 0.000 claims description 4
- 229940099112 cornstarch Drugs 0.000 claims description 4
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 15
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical class [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 8
- 239000006228 supernatant Substances 0.000 description 8
- 238000003756 stirring Methods 0.000 description 7
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical class OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical class NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 6
- 235000019270 ammonium chloride Nutrition 0.000 description 6
- 239000004202 carbamide Chemical class 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000002244 precipitate Substances 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 5
- 239000013049 sediment Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 4
- 239000001103 potassium chloride Substances 0.000 description 4
- 235000011164 potassium chloride Nutrition 0.000 description 4
- 235000011118 potassium hydroxide Nutrition 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 238000005191 phase separation Methods 0.000 description 3
- 239000002689 soil Substances 0.000 description 3
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical class [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000002738 chelating agent Substances 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 239000002921 fermentation waste Substances 0.000 description 2
- 230000035558 fertility Effects 0.000 description 2
- 230000012010 growth Effects 0.000 description 2
- 239000004310 lactic acid Substances 0.000 description 2
- 235000014655 lactic acid Nutrition 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000003895 organic fertilizer Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 239000011736 potassium bicarbonate Substances 0.000 description 2
- 235000015497 potassium bicarbonate Nutrition 0.000 description 2
- 229910000028 potassium bicarbonate Inorganic materials 0.000 description 2
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 1
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical class [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 description 1
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 1
- ONIBWKKTOPOVIA-BYPYZUCNSA-N L-Proline Chemical compound OC(=O)[C@@H]1CCCN1 ONIBWKKTOPOVIA-BYPYZUCNSA-N 0.000 description 1
- QNAYBMKLOCPYGJ-REOHCLBHSA-N L-alanine Chemical compound C[C@H](N)C(O)=O QNAYBMKLOCPYGJ-REOHCLBHSA-N 0.000 description 1
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 description 1
- ROHFNLRQFUQHCH-YFKPBYRVSA-N L-leucine Chemical compound CC(C)C[C@H](N)C(O)=O ROHFNLRQFUQHCH-YFKPBYRVSA-N 0.000 description 1
- ROHFNLRQFUQHCH-UHFFFAOYSA-N Leucine Natural products CC(C)CC(N)C(O)=O ROHFNLRQFUQHCH-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ONIBWKKTOPOVIA-UHFFFAOYSA-N Proline Natural products OC(=O)C1CCCN1 ONIBWKKTOPOVIA-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 235000004279 alanine Nutrition 0.000 description 1
- 235000001014 amino acid Nutrition 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- 239000001110 calcium chloride Chemical class 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 235000011148 calcium chloride Nutrition 0.000 description 1
- 235000013877 carbamide Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical class [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- 235000013922 glutamic acid Nutrition 0.000 description 1
- 239000004220 glutamic acid Substances 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000003898 horticulture Methods 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 235000005772 leucine Nutrition 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 1
- 235000019796 monopotassium phosphate Nutrition 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 1
- GNSKLFRGEWLPPA-UHFFFAOYSA-M potassium dihydrogen phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 235000013930 proline Nutrition 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 210000005253 yeast cell Anatomy 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- Fertilizers (AREA)
Description
本発明は、液体肥料の製造方法、殊に、コーン
ステイープリカー(以下「C・S・L」という)
を使用した液体肥料の製造方法に関する。
近年、液体肥料は、施設園芸や園芸作物の栽培
が普及するに伴い、その需要は著しく伸長してい
る。
液体肥料を製造する方法は、従来、数多く提案
されてきたが、その多くは無機液体肥料の安定化
方法、即ち、結晶析出を見ない液安定性に優れた
液体肥料の製造方法であつて、例えば、ヒドロキ
シポリカルボン酸を利用する方法、界面活性剤を
利用する方法、キレート剤を利用する方法、肥料
塩類の添加順序を工夫した方法、湿式りん酸を精
製し、これを利用する方法等である。
また、アルコール醗酵廃液等の有機質と無機塩
類とを混合した液体肥料も開発されている。然し
ながら、無機肥料塩類のみを用いた液体肥料は、
土壌の荒廃を来たし、地力を低下せしめ、作物の
生育にとつても必ずしも好結果をもたらすもので
はない。
一方、有機質と無機肥料塩類を使用したもの
は、地力の向上、作物の生育に対して好結果をも
たらすけれども、二層分離現象が生起し易く、肥
料塩類、不純物による結晶が析出し、液安定性が
充分でない。
そこで、本発明者らは、有機質と無機質の肥料
塩類を含有し、安定性の優れた液体肥料の製造方
法について研究を重ねた結果、とうもろこし澱粉
製造時の副産物たるコーンステイープリカー(以
下「C・S・L」という)を特殊処理すれば、有
機物を含有せる安定な液体肥料を製造し得ること
を発見し、かかる知見に基いて、以下に詳記する
本発明を完成するに至つた次第である。
即ち、本第1の発明は、C・S・Lをアルカリ
分解した後、該分解液をりん酸液によつてPH7以
下に調整し、次いで肥料塩類を添加溶解すること
からなる液体肥料の製造方法に関し、本第2の発
明は、本第1の発明に更に酵母を加えることによ
つて液の安定性をより高める方法に関する。
本発明に利用するC・S・Lは、とうもろこし
澱粉を製造する際の副産物であつて、とうもろこ
し粒内の弱酸性で溶解する各成分を抽出し、これ
を乳酸醗酵させてから濃縮したものであり、グル
タミン酸、ロイシン、アラニン、プロリン等のア
ミノ酸の他、各種のビタミン及びリン、カリウ
ム、マグネシウム等の無機成分を含み、植物生育
上好適な養分を多含している。現在、市販されて
いるC・S・Lの成分は、凡そ、全窒素2.8%以
上、アミノ態窒素0.9%以上、乳酸9〜11%、水
分45〜50%であつて、微生物工業用試験用培地と
して、或いは乾燥して飼料として使われている。
本第1の発明の第1工程は、このC・S・Lを
アルカリ性物質で分解することである。アルカリ
性物質としては、苛性ソーダ、苛性カリ、アンモ
ニア水、炭酸ソーダ、重炭酸カリ等を全て使用し
得るが、肥料という観点よりすれば窒素や加里を
含有せるアンモニア水、苛性カリ、重炭酸カリ等
の他、トリエタノールアミン、ジエタノールアミ
ン、モノエタノールアミン等のアルカノールアミ
ン類が特に望ましい。
C・S・Lに対するアルカリ性物質の使用割合
は、その種類によつても異なるが、概ね、溶液PH
が8以上になるように添加する。用いる装置とし
ては通常の撹拌機付反応装置の他、コロイドミ
ル、ボールミル等各種粉砕機能を兼備する装置が
効果的である。
分解時間は分解装置の種類、分解PHによつて異
なるが、概ね10〜60分間であり、この際、加温す
ると更に分解時間を短縮することができる。分解
後の液はりん酸液でPHを7以下に調整する。りん
酸液は、特に、乾式りん酸または精製りん酸が好
ましく、PHは液安定性の点からみて6〜3が殊に
望ましい。とりわけ、二層分離現象防止に関して
はPH5〜3が、また、結晶析出防止に関してはPH
6前後乃至は2以下が良い。
第2の工程は、このようにしてアルカリ分解
後、りん酸液によつてPH調整したC・S・Lに肥
料塩類を添加溶解することであるが、該塩類とし
ては、硝酸カルシウム、硝酸カリウム、りん酸ア
ンモニウム、りん酸カリウム、尿素、塩化カルシ
ウム、塩化アンモニウム、硝酸アンモニウムその
他の肥料塩及び微量要素を使用する。
肥料塩の添加量に関して云えば、使用する肥料
塩の種類、成分含量、アルカリ分解に要したアル
カリ物質量、中和に要したりん酸量等によつても
異なるが、先に使用したC・S・L100重量部
(以下、「重量部」を「部」という)に対して、概
ね10〜80部を添加し、充分に撹拌し、溶解させ
る。
尚、本第1の発明の肥料塩の添加は、前述の如
くC・S・Lをアルカリ分解し、りん酸で中和後
に肥料塩を添加するが、別の方法としてC・S・
Lをアルカリ分解したものに肥料塩を先に添加し
りん酸で中和を行なつたものは、不安定であつて
沈澱物の生成が速く、液安定性が悪くなる。
この事から肥料塩の添加時期は本発明に於て、
極めて重要である。
このようにして得られた本第1の発明の液体肥
料は、長期間に亘つて、液の二層分離及び沈澱を
生ずることなく、液安定性に優れている。
次に、本第2の発明の製造方法に関して云え
ば、C・S・Lとともに酵母をアルカリ分解する
ものであり、これによつて、本第1発明における
液安定性を一層高めた製造方法である。本第2の
発明に使用する酵母としては、一般に知られる酵
母、例えば、パルプ酵母、パン酵母、ビール酵
母、飼料用酵母、及びこれらの酵母を原料とし核
酸製造に用いた脱核酵母等である。
使用する酵母は、C・S・L100部に対して、
凡そ3〜20部が良い。
3部未満では、液安定効果の向上を大きく期待
することが出来ず、20部を超えると液の粘度が増
大し、液体肥料としての特質が失われるから、却
つて好ましくない。
C・S・Lと酵母をアルカリ分解後、りん酸液
によつてPH調整したものには、とうもろこしの繊
維状物質や穀粒皮、酵母の細胞壁が残存している
ことがあるから、肥料塩類添加後に、コロイドミ
ル等によつて、再度、湿式粉砕を行い、要すれば
過工程を併用すると、更に要質な液体肥料を得
ることができる。尚、本第2の発明に於けるアル
カリ分解時間は、酵母量によつて異なるが、概
ね、20〜120分くらいである。
本第2の発明の前記以外の工程は、本第1の発
明を踏襲すればよい。
このようにして得られた本発明の液体肥料は極
めて安定であつて、有機質及び無機質成分を含有
し、甚だ肥効性の高いものである。
尚、本発明の液体肥料の界面活性剤、キレート
剤、醗酵廃液その他の可溶性有機質等を加えて、
更に液安定性を高めたり、肥料成分を調整したり
することは何ら差支えない。
以下に本発明の実施例を挙げ更に説明するが、
本発明はこれら実施例に限定されるものではな
い。
尚、実施例中%は特にことわらない限り重量%
を示す。
実施例 1
C・S・L(T−N2.9%、T−P2O53.2%、T
−K2O3.0%)100部に苛性カリ(T−K2O80.6%)
9部を加え、80℃で撹拌しながら、1時間、アル
カリ分解を行つた。この分解液のPHは9.5であつ
た。該液を乾式りん酸(T−P2O554%)6.64部で
中和した。この時の液PHは6.5であつた。続いて、
塩化カリウム(T−K2O60%)1.64部、硝酸アン
モニウム(AN17%、N−N17%)12.4部、塩化
アンモニウム(A−N26%)3.8部、尿素(T−
N46%)18.4部、水48.12部を加え、充分、撹拌溶
解させ、液体肥料とした。該液肥の肥料成分は、
T−N8.0%、A−N1.5%、N−N1.0%、T−
P2O53.0%、T−K2O5.0%であつた。
該液肥の液安定性を試験するため、上澄み液生
成量及び沈澱物発生量を測定した。
その結果を第1表に示す。(本第1の発明例)
また、比較のために前記C・S・L100部に、
塩加カリウム9.4部、硝酸アンモニウム12.4部、
りん酸1カリウム(T−K2O34%、T−P2O552
%)6.88部、塩化アンモニウム3.8部、尿素18.4
部、水49.12部を加え、充分、撹拌溶解させて、
液体肥料とした。
該液肥は上澄み液が速く、かつ大量に生成し、
かつ沈澱物発生量が多く、液安定性が悪い結果と
なつた。(比較例1)
更に、別途、前記C・S・L100部に、乾式り
ん酸6.64部、塩化カリウム13.34部、硝酸アンモ
ニウム12.4部、塩化アンモニウム3.8部、尿素18.4
部、水45.42部を加え、充分、撹拌溶解させて、
液体肥料とした。
該液肥も液層分離が遠く、かつ沈澱物発生量が
多く、液安定性は良くなかつた。(比較例2)
次いで、別途、前記C・S・L100部に苛性カ
リ9部を加え、80℃で撹拌しながら、1時間アル
カリ分解を行つた。この分解液のPHは9.5であつ
た。該液に塩化カリウム1.64部、硝酸アンモニウ
ム12.4部、塩化アンモニウム3.8部、尿素18.4部を
加え、撹拌分散させた後、乾式りん酸6.64部で中
和し水48.12部を加え、充分撹拌溶解させ、液体
肥料とした。該液肥も前二者に比べ、二層分離現
象が速く、かつ沈澱物発生量が多く、液安定性が
悪かつた。
比較例 3
The present invention relates to a method for producing liquid fertilizer, particularly corn staple liquor (hereinafter referred to as "C・S・L").
This invention relates to a method for producing liquid fertilizer using. In recent years, demand for liquid fertilizers has increased significantly as greenhouse horticulture and cultivation of horticultural crops have become widespread. Many methods for producing liquid fertilizers have been proposed in the past, but most of them are methods for stabilizing inorganic liquid fertilizers, that is, methods for producing liquid fertilizers with excellent liquid stability without crystal precipitation. For example, methods using hydroxypolycarboxylic acids, methods using surfactants, methods using chelating agents, methods using a devised addition order of fertilizer salts, methods using purified wet phosphoric acid, etc. be. In addition, liquid fertilizers made by mixing organic matter such as alcohol fermentation waste liquid with inorganic salts have also been developed. However, liquid fertilizer using only inorganic fertilizer salts is
It causes deterioration of the soil, reduces soil fertility, and does not necessarily bring good results for crop growth. On the other hand, those using organic and inorganic fertilizer salts have good results for improving soil fertility and crop growth, but they tend to cause two-layer separation, and crystals due to fertilizer salts and impurities precipitate, resulting in liquid stability. Not sexual enough. As a result of repeated research into a method for producing a highly stable liquid fertilizer containing organic and inorganic fertilizer salts, the present inventors discovered that cornstarch liquor (hereinafter referred to as "C"), a by-product during the production of corn starch, The inventors discovered that it is possible to produce a stable liquid fertilizer containing organic matter by special treatment of ``S・L''), and based on this knowledge, they completed the present invention as detailed below. It is. That is, the first invention is a process for producing a liquid fertilizer, which comprises decomposing C, S, and L with an alkali, adjusting the decomposed solution to pH 7 or less with a phosphoric acid solution, and then adding and dissolving fertilizer salts. Regarding the method, the second invention relates to a method of further increasing the stability of the liquid by further adding yeast to the first invention. C・S・L used in the present invention is a byproduct of producing corn starch, and is obtained by extracting components that dissolve in weak acidity in corn grains, fermenting them with lactic acid, and then concentrating them. It contains amino acids such as glutamic acid, leucine, alanine, and proline, as well as various vitamins and inorganic components such as phosphorus, potassium, and magnesium, and is rich in nutrients suitable for plant growth. Currently, the components of commercially available C・S・L are approximately 2.8% or more of total nitrogen, 0.9% or more of amino nitrogen, 9 to 11% of lactic acid, and 45 to 50% of water, and are suitable for microbial industrial testing. It is used as a culture medium or dried as feed. The first step of the first invention is to decompose this C.S.L with an alkaline substance. As alkaline substances, caustic soda, caustic potash, aqueous ammonia, soda carbonate, potassium bicarbonate, etc. can all be used, but from the viewpoint of fertilizers, in addition to aqueous ammonia, caustic potash, potassium bicarbonate, etc., which contain nitrogen and potassium, Particularly preferred are alkanolamines such as triethanolamine, diethanolamine, and monoethanolamine. The ratio of alkaline substances used for C・S・L varies depending on the type, but in general, the solution PH
Add so that the value is 8 or more. As the apparatus used, in addition to the usual reaction apparatus with a stirrer, apparatuses having various pulverizing functions such as a colloid mill and a ball mill are effective. The decomposition time varies depending on the type of decomposition device and the decomposition pH, but is approximately 10 to 60 minutes, and the decomposition time can be further shortened by heating. After decomposition, adjust the pH of the solution to 7 or less using phosphoric acid solution. The phosphoric acid liquid is preferably dry phosphoric acid or purified phosphoric acid, and the pH is particularly preferably 6 to 3 from the viewpoint of liquid stability. In particular, PH5 to 3 is effective for preventing two-layer separation phenomenon, and PH5 is especially effective for preventing crystal precipitation.
Around 6 or 2 or less is good. The second step is to add and dissolve fertilizer salts into C・S・L whose pH has been adjusted with phosphoric acid solution after alkaline decomposition in this way. Use ammonium phosphate, potassium phosphate, urea, calcium chloride, ammonium chloride, ammonium nitrate and other fertilizer salts and trace elements. Regarding the amount of fertilizer salt added, it varies depending on the type of fertilizer salt used, its component content, the amount of alkaline material required for alkaline decomposition, the amount of phosphoric acid required for neutralization, etc. Approximately 10 to 80 parts are added to 100 parts by weight of S.L (hereinafter, "parts by weight" will be referred to as "parts"), and the mixture is thoroughly stirred and dissolved. The addition of the fertilizer salt according to the first invention involves decomposing C.S.L with an alkali and adding the fertilizer salt after neutralizing it with phosphoric acid as described above.
When L is decomposed with an alkali and fertilizer salts are added first and neutralized with phosphoric acid, the solution is unstable and forms precipitates quickly, resulting in poor liquid stability. From this, in the present invention, the timing of adding fertilizer salt is
extremely important. The liquid fertilizer of the first invention thus obtained has excellent liquid stability over a long period of time without causing two-layer separation or precipitation. Next, regarding the manufacturing method of the second invention, the yeast is alkali-decomposed together with C.S.L, and thereby, the manufacturing method of the first invention further improves the liquid stability. be. The yeast used in the second invention includes commonly known yeasts, such as pulp yeast, baker's yeast, beer yeast, feed yeast, and denucleated yeast using these yeasts as raw materials for nucleic acid production. . The yeast used is 100 parts of C.S.L.
Approximately 3 to 20 copies is good. If the amount is less than 3 parts, no significant improvement in the liquid stabilizing effect can be expected, and if it exceeds 20 parts, the viscosity of the liquid will increase and the characteristics as a liquid fertilizer will be lost, which is rather undesirable. After alkali decomposition of C・S・L and yeast, the pH is adjusted with a phosphoric acid solution. Since corn fibrous substances, grain husks, and yeast cell walls may remain, fertilizer salts are not recommended. After the addition, wet pulverization is performed again using a colloid mill or the like, and if necessary, a passing step is also used to obtain a liquid fertilizer of even higher quality. Incidentally, the alkaline decomposition time in the second invention varies depending on the amount of yeast, but is approximately 20 to 120 minutes. The steps of the second invention other than those described above may follow those of the first invention. The liquid fertilizer of the present invention thus obtained is extremely stable, contains organic and inorganic components, and has extremely high fertilizer efficacy. In addition, in addition to the surfactant, chelating agent, fermentation waste liquid and other soluble organic substances of the liquid fertilizer of the present invention,
Furthermore, there is no problem in increasing the liquid stability or adjusting the fertilizer components. Examples of the present invention will be given below and further explained.
The present invention is not limited to these examples. In addition, % in the examples is weight % unless otherwise specified.
shows. Example 1 C・S・L (T-N2.9%, T-P 2 O 5 3.2%, T
- K 2 O 3.0%) 100 parts caustic potash (T-K 2 O 80.6%)
9 parts were added, and alkaline decomposition was carried out for 1 hour while stirring at 80°C. The pH of this decomposition solution was 9.5. The liquid was neutralized with 6.64 parts of dry phosphoric acid (T- P2O5 54 %). The pH of the liquid at this time was 6.5. continue,
Potassium chloride (T- K2O60 %) 1.64 parts, ammonium nitrate (AN17%, N-N17%) 12.4 parts, ammonium chloride (A-N26%) 3.8 parts, urea (T-
18.4 parts of nitrogen (46%) and 48.12 parts of water were added and thoroughly stirred and dissolved to form a liquid fertilizer. The fertilizer components of the liquid fertilizer are:
T-N8.0%, A-N1.5%, N-N1.0%, T-
The P 2 O 5 content was 3.0%, and the TK 2 O content was 5.0%. In order to test the liquid stability of the liquid fertilizer, the amount of supernatant liquid produced and the amount of sediment produced were measured. The results are shown in Table 1. (First Invention Example) Also, for comparison, in the 100 copies of C.S.L.
Potassium salt 9.4 parts, ammonium nitrate 12.4 parts,
Monopotassium phosphate (T-K 2 O 34%, T-P 2 O 5 52
%) 6.88 parts, ammonium chloride 3.8 parts, urea 18.4 parts
Add 49.12 parts of water and stir well to dissolve.
It was made into liquid fertilizer. The liquid fertilizer produces supernatant liquid quickly and in large quantities,
In addition, a large amount of precipitate was generated, resulting in poor liquid stability. (Comparative Example 1) Additionally, to 100 parts of the above C・S・L, 6.64 parts of dry phosphoric acid, 13.34 parts of potassium chloride, 12.4 parts of ammonium nitrate, 3.8 parts of ammonium chloride, and 18.4 parts of urea were added.
Add 45.42 parts of water and stir well to dissolve.
It was made into liquid fertilizer. This liquid fertilizer also had a long liquid phase separation, produced a large amount of sediment, and had poor liquid stability. (Comparative Example 2) Next, 9 parts of caustic potash was separately added to 100 parts of the above C.S.L, and alkaline decomposition was carried out for 1 hour while stirring at 80°C. The pH of this decomposition solution was 9.5. Add 1.64 parts of potassium chloride, 12.4 parts of ammonium nitrate, 3.8 parts of ammonium chloride, and 18.4 parts of urea to the liquid, stir and disperse, neutralize with 6.64 parts of dry phosphoric acid, add 48.12 parts of water, stir thoroughly and dissolve. Used as fertilizer. Compared to the former two, this liquid fertilizer also had a faster two-layer separation phenomenon, produced a larger amount of precipitate, and had poorer liquid stability. Comparative example 3
【表】
(液安定性の試験方法)
(1) 上澄み液生成量
液体肥料を1の共栓付メスシリンダーに標
線まで入れ、30℃の恒温器中で一定期間静置
後、上澄み液の容積を測定した。
(2) 沈澱物発生量
液体肥料1を共栓付メスシリンダーに標線
まで入れ、30℃の恒温器中で一定期間静置後シ
リンダーの底部に沈降した流動性を示さない沈
澱の容積を沈澱物の発生量とした。
実施例 2
前記C・S・L100部と酵母6部に苛性ソーダ
(T−Na2O76.7%)7部を加え、80%で撹拌しな
がら1時間、アルカリ分解を行つた。この分解液
のPHは9.3であつた。該液を乾式りん酸6.64部で
中和した。この時の液PHは6.0であつた。続いて、
塩化カリウム13.34部、硝酸アンモニウム12.4部、
塩化アンモニウム3.8部、尿素18.4部、水32.42部
を加え、充分、撹拌溶解させ、液体肥料とした。
該液肥の上澄み液生成量及び沈澱物発生量を測
定したところ、長期間に亘つて、上澄みは殆ど生
じず、即ち全くと云つて良い程、液層分離を起さ
ず、かつ沈澱は発生しなかつた。かように結果
は、格別良好であつた。(本第2の発明例)
上記本第2の発明例に於ける酵母の使用の他
は、本第1の発明例と全く同一の操作によつて液
体肥料を製造し、該液肥の上澄み液生成量及び沈
澱物発生量を測定したところ、長期間に亘つて、
殆ど上澄みを生じず、即ち、殆ど液層分離を起さ
ずかつ沈澱は極く僅しか発生しなかつた。かよう
に、結果は良好であつた。(本第1の発明例)
これら結果を、第2表に示す。[Table] (Test method for liquid stability) (1) Amount of supernatant liquid produced Pour liquid fertilizer into a measuring cylinder with a stopper (No. 1) up to the marked line, let it stand for a certain period of time in a thermostat at 30°C, and then calculate the amount of supernatant liquid produced. The volume was measured. (2) Amount of sediment generated Fill a measuring cylinder with a stopper with liquid fertilizer 1 up to the marked line, leave it for a certain period of time in a thermostat at 30℃, and then settle the volume of sediment that does not show fluidity and settles to the bottom of the cylinder. It was defined as the amount of material generated. Example 2 7 parts of caustic soda (T-Na 2 O 76.7%) was added to 100 parts of the above C.S.L and 6 parts of yeast, and alkaline decomposition was carried out for 1 hour while stirring at 80%. The pH of this decomposition solution was 9.3. The liquid was neutralized with 6.64 parts of dry phosphoric acid. The pH of the liquid at this time was 6.0. continue,
Potassium chloride 13.34 parts, ammonium nitrate 12.4 parts,
3.8 parts of ammonium chloride, 18.4 parts of urea, and 32.42 parts of water were added and thoroughly stirred and dissolved to obtain a liquid fertilizer. When the amount of supernatant liquid produced and the amount of sediment generated from the liquid fertilizer were measured, it was found that over a long period of time, almost no supernatant was formed, that is, almost no liquid phase separation occurred, and no precipitation occurred. Nakatsuta. The results were thus particularly good. (Second Invention Example) A liquid fertilizer is manufactured by the same operation as in the first invention example except for the use of yeast in the above-mentioned second invention example, and the supernatant liquid of the liquid fertilizer is When we measured the amount of production and the amount of precipitate generated, we found that over a long period of time,
Almost no supernatant was formed, that is, almost no liquid phase separation occurred, and very little precipitation occurred. Thus, the results were good. (First Invention Example) These results are shown in Table 2.
Claims (1)
後、該分解液をりん酸液によつてPH7以下に調整
し、次いで、肥料塩類を添加溶解することからな
る液体肥料の製造方法。 2 コーンステイープリカーとともに酵母をアル
カリ分解した後、該分解液をりん酸液によつてPH
7以下に調整し、次いで、肥料塩類を添加溶解す
ることからなる液体肥料の製造方法。[Scope of Claims] 1. A method for producing a liquid fertilizer, which comprises decomposing corn staple liquor with an alkali, adjusting the pH of the decomposed liquid to 7 or less with a phosphoric acid solution, and then adding and dissolving fertilizer salts. 2 After alkaline decomposition of yeast together with cornstarch liquor, the pH of the decomposition liquid is adjusted using phosphoric acid solution.
7 or less, and then adding and dissolving fertilizer salts.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59202527A JPS6183696A (en) | 1984-09-26 | 1984-09-26 | Manufacture of liquid fertilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59202527A JPS6183696A (en) | 1984-09-26 | 1984-09-26 | Manufacture of liquid fertilizer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6183696A JPS6183696A (en) | 1986-04-28 |
| JPH0134960B2 true JPH0134960B2 (en) | 1989-07-21 |
Family
ID=16458967
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59202527A Granted JPS6183696A (en) | 1984-09-26 | 1984-09-26 | Manufacture of liquid fertilizer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6183696A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006206341A (en) * | 2005-01-25 | 2006-08-10 | San-Ei Sucrochemical Co Ltd | Organic fertilizer and its manufacturing method |
| JP5438341B2 (en) * | 2009-02-27 | 2014-03-12 | 三井造船株式会社 | Irrigation method, irrigation apparatus, irrigation water reforming method, and irrigation water reforming apparatus |
| EP3336071A1 (en) | 2016-12-19 | 2018-06-20 | Danstar Ferment AG | Method and composition for improving plant growth |
| JP2019099409A (en) * | 2017-11-30 | 2019-06-24 | 片倉コープアグリ株式会社 | Liquid fertilizer containing urea and ammonium salt |
-
1984
- 1984-09-26 JP JP59202527A patent/JPS6183696A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6183696A (en) | 1986-04-28 |
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