JPS596932A - Granulation of powdery fertilizer and feed - Google Patents
Granulation of powdery fertilizer and feedInfo
- Publication number
- JPS596932A JPS596932A JP11470682A JP11470682A JPS596932A JP S596932 A JPS596932 A JP S596932A JP 11470682 A JP11470682 A JP 11470682A JP 11470682 A JP11470682 A JP 11470682A JP S596932 A JPS596932 A JP S596932A
- Authority
- JP
- Japan
- Prior art keywords
- feed
- fertilizer
- starch
- granulation
- kneading
- 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
Links
- 239000003337 fertilizer Substances 0.000 title abstract description 31
- 238000005469 granulation Methods 0.000 title abstract description 10
- 230000003179 granulation Effects 0.000 title abstract description 10
- 229920002472 Starch Polymers 0.000 claims abstract description 18
- 239000008107 starch Substances 0.000 claims abstract description 18
- 235000019698 starch Nutrition 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 14
- 239000012141 concentrate Substances 0.000 claims abstract description 10
- 239000002351 wastewater Substances 0.000 claims abstract description 10
- 239000000843 powder Substances 0.000 claims description 9
- 238000004898 kneading Methods 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- 239000000203 mixture Substances 0.000 abstract description 7
- 239000006227 byproduct Substances 0.000 abstract description 5
- 238000003860 storage Methods 0.000 abstract description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 abstract description 4
- 235000011941 Tilia x europaea Nutrition 0.000 abstract description 4
- 239000004571 lime Substances 0.000 abstract description 4
- 238000001035 drying Methods 0.000 abstract description 3
- 239000008187 granular material Substances 0.000 abstract description 3
- 235000008935 nutritious Nutrition 0.000 abstract 1
- 239000002245 particle Substances 0.000 description 13
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 8
- 238000012360 testing method Methods 0.000 description 8
- 235000008504 concentrate Nutrition 0.000 description 7
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 6
- 239000000920 calcium hydroxide Substances 0.000 description 6
- 235000011116 calcium hydroxide Nutrition 0.000 description 6
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- 229910000019 calcium carbonate Inorganic materials 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 238000009826 distribution Methods 0.000 description 3
- 235000014666 liquid concentrate Nutrition 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 235000002595 Solanum tuberosum Nutrition 0.000 description 2
- 244000061456 Solanum tuberosum Species 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 159000000000 sodium salts Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 235000016068 Berberis vulgaris Nutrition 0.000 description 1
- 241000335053 Beta vulgaris Species 0.000 description 1
- 241001474374 Blennius Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 241000209504 Poaceae Species 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000002547 anomalous effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000002921 fermentation waste Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012047 saturated solution Substances 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 229910001948 sodium oxide Inorganic materials 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Landscapes
- Glanulating (AREA)
- Fertilizers (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は粉体圧飼料、例えば石灰質肥料や粉体飼料を
澱粉廃水濃縮液を用いて造粒する方法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for granulating powder compacted feed, such as calcareous fertilizer or powder feed, using starch wastewater concentrate.
従来、粉体肥料の多くは、取扱性の向上および飛散防止
の点から粒状化の傾向にあり、複合肥料、化成肥料はい
ずれも粒状化され取扱いに便利で。Conventionally, most powdered fertilizers have tended to be granulated to improve handling and prevent scattering, and compound fertilizers and chemical fertilizers are both granulated and convenient to handle.
機械散布に適した製品となっている。しかし、石灰質肥
料は付加価値が小さく造粒することにより、コスト高と
なるため多くは粉体のまま使用されている。省力化が求
められる近代農業は、機械化への道を歩み合理的、能率
的な機械装置の開発、改良、発達を見ている。肥料もそ
れに適したものへと改良されているが、その中で特に飛
散性の高い石灰質肥料は0、一連の機械化作業形態完成
のために、大きな常客と麿っていた。This product is suitable for mechanical spraying. However, since calcareous fertilizers have little added value and are granulated, which increases costs, they are often used in powder form. Modern agriculture, which requires labor saving, has taken the path towards mechanization and has seen the development, improvement, and development of rational and efficient mechanical devices. Fertilizers have also been improved to make them more suitable for this purpose, but limestone fertilizers, which have particularly high scattering properties, have been eliminated.The company has gained a large number of regular customers due to the completion of a series of mechanized work formats.
一方、家畜のえさとしての牧草および開数植物繊維(ビ
ートパルプ、澱粉粕等)は、長期保存、配合のために脱
水を要し天日、機械により乾燥されている。しかし、乾
燥することにより粉化し配合時の偏析、取扱いの不便さ
などの常客が生じその対策が必要であった。On the other hand, grasses and anomalous plant fibers (beet pulp, starch meal, etc.) used as feed for livestock require dehydration for long-term storage and formulation, and are dried in the sun or mechanically. However, due to drying, it becomes powder, causing segregation during blending, inconvenience in handling, etc., and countermeasures were needed.
これらの幣訂全除去する方法として、造粒又は固結が適
していると考えられる。造粒の方法としては、従来
パルプ工業副産物リグニンスルホン酸によるもの、高分
子系統合剤によるもの、
ナトリウム塩類によるもの(特公昭56−27086)
、炭酸ガス吹込法によるもの(特公昭47−13084
)、PH調整O8Fによるもの(特公昭56−8889
3)、アルコール発酵廃液によるもの、
等の添加造粒法が試みられているが、原料の多用化によ
る価格高、地域差による供給量の制限、運賃の負担等の
問題があり低コスト全要求される初体肥飼料に使用する
には経済的に困難でめり、またリグニンスルホン酸、高
分子系統合剤、ナトリウム塩類のように飼料に使用でき
ないものもある。Granulation or caking is considered to be suitable as a method for completely removing these particles. Conventional granulation methods include one using lignin sulfonic acid, a by-product of the pulp industry, one using a polymeric unifying agent, and one using sodium salts (Japanese Patent Publication No. 56-27086).
, by carbon dioxide gas injection method (Special Publication No. 47-13084)
), by PH adjustment O8F (Special Publication No. 56-8889
3) Additive granulation methods, such as those using alcoholic fermentation waste liquid, have been attempted, but there are problems such as high prices due to the multiple use of raw materials, limited supply due to regional differences, and burden of freight charges, and low cost is not required at all. However, it is economically difficult to use them in feedstuffs, and some of them cannot be used in feeds, such as lignin sulfonic acid, polymeric integrators, and sodium salts.
本発明は上述の事情に鑑み開発式1したもので。The present invention was developed in Formula 1 in view of the above-mentioned circumstances.
肥料は勿論のこと飼料に用いても何ら支障のないと共に
むしろ養分ともなる澱粉廃水濃縮液奢粉体肥飼料1例え
ば石灰質肥料や粉体飼料に添加し、取扱い容易で保存期
間中吸湿性なく、シかも水中においては速かに崩壊分散
する性質全確保しつつ、上記肥飼料全造粒する方法を提
供することを目的とするものである。Concentrated starch wastewater liquid rich powder fertilizer feed that can be used not only as fertilizer but also as feed without any problems, and even as a nutrient.It can be added to, for example, calcareous fertilizer or powder feed, and is easy to handle and does not absorb moisture during storage. The object of the present invention is to provide a method for completely granulating the above-mentioned fertilizer feed while ensuring the property of disintegrating and dispersing quickly in water.
本発明は、微細な粉体の肥料あるいは飼料、例えば石灰
質肥料、副産石灰そして副産飼料に澱粉廃液濃縮液を添
加し混練したVt、、これを造粒して成るものである・
上記混線は、肥飼料の種類・状態そして澱粉廃液濃縮液
が含む水分の量によっても異なるが、連続的に混練機に
供給される肥飼料に、該肥飼料よりも少量の上記澱粉廃
液濃縮液を添加して行う。The present invention is made by granulating fine powder fertilizer or feed, such as calcareous fertilizer, by-product lime, and Vt, which is obtained by adding and kneading starch waste liquid concentrate to by-product feed. Although it varies depending on the type and condition of the fertilizer feed and the amount of water contained in the starch waste liquid concentrate, it is possible to add a smaller amount of the above starch waste liquid concentrate to the fertilizer feed that is continuously fed to the kneading machine. and do it.
混線条件は特に限定されることはなく通常の混練機によ
り常温において混練すれば十分である。The mixing conditions are not particularly limited, and it is sufficient to knead at room temperature using an ordinary kneader.
混練後造粒を行うが、該造粒も通常の造粒機、例えば転
勤型造粒機でよい。After kneading, granulation is performed, and the granulation may also be performed using a normal granulator, such as a transfer type granulator.
上記造粒で一応本来の工程を終るが、後工程として造粒
された肥飼料を乾燥させる。乾燥時間は含有する水分量
に応じて適宜決定される。The above-mentioned granulation ends the original process, but the granulated fertilizer feed is dried as a post-process. The drying time is appropriately determined depending on the amount of moisture contained.
以上のように本発明は、粉体側飼料に澱粉廃水濃縮液を
添力[1することによっても該肥飼料の造粒全行うこと
ができるようKなりしかも澱粉という養分全同時に添加
できることになる。そして上記造粒物は、保存期間中の
吸湿性が低く、シかも水中においては速かに崩壊分散す
るという成果を示した。As described above, in the present invention, by adding a starch wastewater concentrate to the powdered feed, it is possible to completely granulate the fertilizer feed, and furthermore, the nutrients of starch can be added at the same time. . The above-mentioned granules had low hygroscopicity during storage and quickly disintegrated and dispersed in water.
以下実施例を示すと共に各物性試験についてその試験結
果を第3表及び第1〜6図に示す。Examples are shown below, and the test results for each physical property test are shown in Table 3 and Figures 1 to 6.
なお不発明に使用埒れる濃縮液とは、澱粉製造工程にお
いて磨砕した馬鈴しよから澱粉と生粕を取除いたあとの
廃水を濃縮化したものである。上記廃水は澱粉製造工程
において、大tK排出されるものでるる。その処理方法
としては、貯水池での曝気、地下浸透および河川への排
出等があるが、公害防止上問題点かめり、その対策と廃
水中に含まれる租タンパクの活用のためにこれを水分6
0〜70チ程度に濃縮し家畜用飼料に当てている。The concentrated liquid used in the invention is concentrated wastewater after removing starch and raw lees from ground potato lees during the starch manufacturing process. The waste water mentioned above is one that is discharged in a large amount during the starch manufacturing process. Treatment methods include aeration in reservoirs, underground infiltration, and discharge into rivers, but there are problems in terms of pollution prevention.
It is concentrated to about 0 to 70 g and used as feed for livestock.
不発明ではかかる濃縮廃液を粉体側飼料の造粒に採用し
几ものであり、その成分分析は第1表のごとくである。In the present invention, such concentrated waste liquid is used for granulation of powdered feed, and its component analysis is as shown in Table 1.
第1表 澱粉廃水濃縮敢分析成績
水 分 (H宜0) 67
、36チ窒素全量(N) 1.41#
りん酸全t (PzOs) 1 、25 #
加里全噴(K2O) 3.221石灰全量(Oa
O) o、o2y苦土全t (MgO)
o 、 25 #酸化ナトリウム (Na20)
o 、 i s #有 機 物 (強熱減
量法) 22.18#比 重
1.14pH5・5
また以下の実施例にて使用妊れた石灰質肥料は第2表の
どとくの粒度である。Table 1 Starch wastewater concentration analysis results Moisture content (H0) 67
, 36 t Total amount of nitrogen (N) 1.41 # Total phosphoric acid (PzOs) 1, 25 #
Total amount of potassium (K2O) 3.221 Total amount of lime (Oa
O) o, o2y magnesia total t (MgO)
o, 25 #sodium oxide (Na20)
o, is #organic substance (ignition loss method) 22.18# specific gravity
1.14 pH 5.5 In addition, the calcareous fertilizer used in the following examples has the particle size of Table 2.
第2表 実施例に使用した石灰質肥料粒度実施例1
炭酸カルシウム肥料の粉砕工程で微粉砕された肥料を、
連続的に混練機に送り、その入口(′こ1′m粉廃水濃
縮液全肥料流t#J破の7重量%〜9M縫チにあたる量
を添加し、混練機により約120秒混練し、転勤型造粒
機へ送り約300秒転動造粒した。Table 2 Particle size of calcareous fertilizer used in Examples Example 1 Fertilizer finely pulverized in the pulverization process of calcium carbonate fertilizer,
Continuously send it to a kneading machine, add an amount equivalent to 7% by weight to 9M stitches of the total fertilizer flow t#J, and knead it for about 120 seconds using a kneading machine. The mixture was sent to a rolling granulator and granulated by rolling for about 300 seconds.
さらに並流型乾燥機へ投入し約600秒で水分0.7チ
以下まで乾燥したものを物性試験に供した。Furthermore, the material was placed in a co-current dryer and dried to a moisture content of 0.7 g or less in about 600 seconds, and then subjected to a physical property test.
実施例2
肥料用消石灰全実施例1同様連続的に混線機へ送り、そ
の入口に澱粉廃水濃縮液を肥料流動量の25重量俤〜4
0重量%にあたる情を添加して、混練機により約300
秒混練し転勤型造粒機により約300抄造粒したのち、
対向型乾燥機で約600秒乾燥し水分約1.5チ以下の
ものを物性試験に供した。Example 2 All slaked lime for fertilizers Same as in Example 1, the starch wastewater concentrate is continuously fed to the mixer at the inlet of the mixer at a rate of 25 to 4 ml of the fertilizer flow rate.
With the addition of 0% by weight, approximately 300%
After kneading for seconds and granulating approximately 300 pieces using a transfer type granulator,
The material was dried for about 600 seconds in a counter-type dryer, and the material having a moisture content of less than about 1.5 inches was subjected to a physical property test.
実施例3
馬鈴しよ全磨砕し遠心分離機により脱水した後、遠心ふ
るいにより澱粉と分離さり、た生釉を、直火式乾燥機で
乾燥し混合機へ送る。混合機入口で飼料流動量の30重
量係の濃縮液を添加し混合造粒をする。その後熱風によ
シ乾燥して破砕機で粉砕し整粒する。Example 3 Potato seaweed was ground whole and dehydrated using a centrifugal separator, then separated from starch using a centrifugal sieve, and the raw glaze was dried using an open flame dryer and sent to a mixer. At the inlet of the mixer, 30% of the feed flow rate by weight of concentrate is added and mixed and granulated. After that, it is dried with hot air, crushed with a crusher, and sized.
試験結果
吸湿性試験
第3表 吸湿性試験結果
20度C相対湿度70% 食塩飽和溶液恒湿デシケータ
−により、水分の増加率を測定した。Test Results Hygroscopic Test Table 3 Hygroscopic Test Results 20° C. Relative Humidity 70% The rate of increase in moisture was measured using a saline saturated solution in a constant humidity desiccator.
(%)
上記成績から粒状炭酸カルシウム肥料については吸湿性
は見られなかったが、消石灰については空気中のOoz
&反応しU a Oo 3が増加したものと考えられる
。(%) From the above results, granular calcium carbonate fertilizer did not show any hygroscopicity, but slaked lime did not have hygroscopicity in the air.
It is considered that U a Oo 3 increased due to & reaction.
図面は試験結果を示すもので、第1図は実施例1におい
て粒状炭酸カルシウム粒径分布図、第2図は実施例2に
おいて粒状消石灰粒径分布図、第3園は実施例1におい
て粒状炭酸カルシウム粒子強度、第4図は実施例2にお
いて粒状消石灰粒子強度、第5図は実施例1において粒
状炭酸カルシウム(粒径2.0謔)の水中(水温20℃
)における崩壊速度、そして第6図は実施例2において
粒状消石灰(粒径2.Owm)の水中(水温20℃)に
おける崩壊速度を示す。
特許出願人 訓子府石灰工業株式会社
美幌地方農産加工農業協同組合連合会
代理人 弁理士 藤 岡 徹
第j図
−0,5+0.5 +1.O+2.0 +3.5粒
径 mm
第2図
濃縮液混合率
一〇、5+0.5 刊、0 +2.0 +3.5粒
径 mm
濃縮液混合率
粒径 mm
濃m液混合率
粒径 mm
濃縮液混合浴
時間 m1n
a縮液混合率
時間 min
192The drawings show the test results. Figure 1 is a particle size distribution diagram of granular calcium carbonate in Example 1, Figure 2 is a distribution diagram of granular slaked lime particle size in Example 2, and the third diagram is a diagram of granular slaked lime particle size distribution in Example 1. Figure 4 shows the strength of granular slaked lime particles in Example 2. Figure 5 shows the strength of granular calcium carbonate (particle size 2.0 cm) in Example 1 in water (water temperature 20°C).
), and FIG. 6 shows the disintegration rate in water (water temperature 20° C.) of granular slaked lime (particle size 2.Owm) in Example 2. Patent Applicant: Kunikofu Lime Industry Co., Ltd. Bihoro Regional Agricultural Processing Agricultural Cooperative Federation Agent Patent Attorney: Toru Fujioka Figure J - 0.5 + 0.5 +1. O+2.0 +3.5 Particle size mm Fig. 2 Concentrate mixture ratio 10, 5 + 0.5 edition, 0 +2.0 +3.5 Particle size mm Concentrate mixture ratio Particle size mm Concentrate mixture ratio Particle size mm Concentration Liquid mixing bath time m1n a Condensed liquid mixing rate time min 192
Claims (1)
すること全特徴とする粉体圧飼料の造粒法。A method for granulating powder compacted feed, which is characterized in that the entire starch wastewater concentrate is added to powder compacted feed, kneaded, and then granulated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11470682A JPS596932A (en) | 1982-07-01 | 1982-07-01 | Granulation of powdery fertilizer and feed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11470682A JPS596932A (en) | 1982-07-01 | 1982-07-01 | Granulation of powdery fertilizer and feed |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS596932A true JPS596932A (en) | 1984-01-14 |
| JPH0127039B2 JPH0127039B2 (en) | 1989-05-26 |
Family
ID=14644579
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11470682A Granted JPS596932A (en) | 1982-07-01 | 1982-07-01 | Granulation of powdery fertilizer and feed |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS596932A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4855874A (en) * | 1971-11-16 | 1973-08-06 | ||
| JPS51118669A (en) * | 1975-04-07 | 1976-10-18 | Hokkaido Sugar Co | Process for producing granular bark compost |
| JPS5688893A (en) * | 1979-12-17 | 1981-07-18 | Hokkaido Sugar Co | Method of granulating furtilizer with stephen waste water concentrated liquid |
-
1982
- 1982-07-01 JP JP11470682A patent/JPS596932A/en active Granted
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4855874A (en) * | 1971-11-16 | 1973-08-06 | ||
| JPS51118669A (en) * | 1975-04-07 | 1976-10-18 | Hokkaido Sugar Co | Process for producing granular bark compost |
| JPS5688893A (en) * | 1979-12-17 | 1981-07-18 | Hokkaido Sugar Co | Method of granulating furtilizer with stephen waste water concentrated liquid |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0127039B2 (en) | 1989-05-26 |
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