JPS58104048A - Manufacture of granular slaked lime - Google Patents

Manufacture of granular slaked lime

Info

Publication number
JPS58104048A
JPS58104048A JP20022081A JP20022081A JPS58104048A JP S58104048 A JPS58104048 A JP S58104048A JP 20022081 A JP20022081 A JP 20022081A JP 20022081 A JP20022081 A JP 20022081A JP S58104048 A JPS58104048 A JP S58104048A
Authority
JP
Japan
Prior art keywords
slaked lime
powder
particle size
granular
granular slaked
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
JP20022081A
Other languages
Japanese (ja)
Other versions
JPS618025B2 (en
Inventor
竹中 伸一
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP20022081A priority Critical patent/JPS58104048A/en
Publication of JPS58104048A publication Critical patent/JPS58104048A/en
Publication of JPS618025B2 publication Critical patent/JPS618025B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 開示技術は消石灰の造粒効率を向上させる技術分野に属
する0 而して、この発明は、生石灰等より工業的に生産される
消石灰粉末から肥料用消石灰の散布等に好適な粒状消石
灰を製造す′る方法に関する発明であり、特に、上記消
石灰粉末を予かしめ加湿し、これに生石灰粉末を添加混
合した後、加圧成形し、該成形物を反応養生することに
よって、上記生石灰粉末の水利反応を起こさせ、その膨
張力を利用して崩壊させるようにした粒状消石灰の製造
方法に係る発明である。
DETAILED DESCRIPTION OF THE INVENTION The disclosed technology belongs to the technical field of improving the granulation efficiency of slaked lime. Therefore, the present invention is applicable to the application of slaked lime for fertilizer, etc. from slaked lime powder industrially produced from quicklime etc. This invention relates to a method for producing suitable granular slaked lime, and in particular, the above-mentioned slaked lime powder is pre-caulked and humidified, quicklime powder is added and mixed therein, and then pressure molded and the molded product is subjected to reaction curing. This invention relates to a method for producing granular slaked lime in which the quicklime powder undergoes a water utilization reaction and its expansion force is used to disintegrate it.

周知の如く、散布肥料等に用いられる粒状消石灰の製造
方法としては、これまで消石灰粉末に水を添加して練り
込み、これを所定ダイスより押出して乾燥する所謂湿式
方法や、上記消石灰粉末をそのま\加圧成形して、これ
を所定解砕機によって破砕した後、分級する所謂乾式方
法が採用されている。
As is well known, the methods for producing granular slaked lime used for spraying fertilizers, etc. have been the so-called wet method in which water is added to slaked lime powder, kneaded, extruded through a designated die and dried, and the slaked lime powder is A so-called dry method is employed in which the material is pressure-molded, crushed by a designated crusher, and then classified.

しかしながら、上記在米の湿式方法では、粒径を特に1
關以下とした場合に生・産能率を向上させ難い難点があ
り、又、乾燥工程を必要とするので工程が多(作業が煩
雑となる欠点があり、更に。
However, in the above-mentioned wet method in the United States, the particle size is particularly limited to 1
There is a drawback that it is difficult to improve the production efficiency when the drying process is lower than that, and there is also the disadvantage that the process is complicated because it requires a drying process.

乾燥のため多量の熱エネルギーを必要とし、コスト高に
なる不利点があった。
This has the disadvantage of requiring a large amount of thermal energy for drying, resulting in high costs.

又、前記乾式方法では1例えば、粒径2〜511m程度
の製品を得ようとする場合、その回収率が50−以下と
なり、回収歩留りが悪い不具合があり。
Furthermore, in the dry method, for example, when trying to obtain a product with a particle size of about 2 to 511 m, the recovery rate is less than 50 mm, resulting in a poor recovery yield.

又、回収率が悪いことから製品量の2倍以上の容積を有
する解砕、分級設備等が必要とされ、この点からもコス
トがか\る不利点があり、更に、得られた製品は先のと
がった角ばった尖角突状態様のものが多く、手ざわりや
流動性が悪いという欠点があった。
In addition, due to the poor recovery rate, crushing and classification equipment with a volume more than twice the volume of the product is required, which also has the disadvantage of increasing costs. Many of them had a sharp, angular shape, and had the disadvantage of poor texture and fluidity.

この発明の目的は、上述従来技術に基づく粒状消石灰の
製造方法の問題を解決すべき技術的課題とし、消石灰粉
末を予かしめ加湿し、これに生石灰粉末を添加混合して
加圧成形し、養生中の該生石灰粉末の水利反応による膨
張力を利用して崩壊させる技術的手段を講することによ
り、上述問題点を解決し、簡単な工程で良質な製品を効
率良く製造出来るようにしたことを要旨とする生石灰産
業に於ける粒状消石灰利用分野に益し得る優れた粒状消
石灰の製造方法を提供せんとするあのである0 次にこの発明の1実施例を第1図乃至第5図に1 従って説明すれば以下の通りである。
The purpose of this invention is to solve the technical problem of the method for producing granular slaked lime based on the above-mentioned conventional technology, and to solve the problem by pre-caulking and humidifying slaked lime powder, adding and mixing quicklime powder to it, press-molding it, and curing it. We have solved the above-mentioned problems by taking technical measures to disintegrate the quicklime powder by utilizing its expansion force due to the water use reaction, and we have made it possible to efficiently manufacture high-quality products in a simple process. The purpose of this invention is to provide an excellent method for producing granular slaked lime that can be useful in the field of utilizing granular slaked lime in the quicklime industry.Next, one embodiment of the present invention is shown in Figs. Therefore, the explanation is as follows.

第1図に示す様に原料の消石灰粉末1は粒径5〜15μ
のものが80重量%以上含まれている。
As shown in Figure 1, the raw material slaked lime powder 1 has a particle size of 5 to 15 μm.
Contains over 80% by weight.

而して、上記消石灰粉末lに重量比で2〜15チ程度の
水を添加して混合し、第2図に示す様に水によって凝集
した軟らかい集合体2とする。
Then, approximately 2 to 15 inches of water is added by weight to the slaked lime powder 1 and mixed to form a soft aggregate 2 coagulated by water as shown in FIG.

次いで、第3図に示す様に粒径l〜3m程度以下の生石
灰粉末3を上記消石灰粉末IK対する重量比で5〜20
%程度加えてよく混合する。
Next, as shown in FIG. 3, quicklime powder 3 having a particle size of about 1 to 3 m or less is added at a weight ratio of 5 to 20 to the slaked lime powder IK.
% and mix well.

上記混合物を周知のブリケットマシンや加圧プレス等を
利用して、例えば、200 K9/cd以上の圧力で速
やかに加圧成形すると、第4図に示す様に素材集合体空
隙が少な(なり、従って、前記集合体2は硬い粒状消石
灰4となる。
When the above-mentioned mixture is quickly pressure-molded using a well-known briquette machine, pressure press, etc. at a pressure of, for example, 200 K9/cd or more, the material aggregate has fewer voids (as shown in Fig. 4). Therefore, the aggregate 2 becomes hard granular slaked lime 4.

そこで、この様にして得られた上記成形物を保存養生す
ると、第5図に示す機に前記生石灰粉末3は周囲の水分
を吸収して粒状消石灰4′と生長し、その反応過程で約
2倍の体積膨張を起こす為に上記成形物は細かく崩壊す
る。
Therefore, when the molded product obtained in this way is stored and cured, the quicklime powder 3 absorbs surrounding moisture and grows into granular slaked lime 4', and in the reaction process, about 2 Because the volume expansion is doubled, the molded product collapses into small pieces.

而して、前記粒状消石灰4と上記粒状消石灰4′とから
成る好ましい粒径の粒状物が得られ、その中に上記生石
灰粉末3が残留していることはな(、しかも、水分はほ
とんどが水利反応で消費されるので乾燥状態となってい
る。
As a result, a granular material of a preferable particle size consisting of the granular slaked lime 4 and the granular slaked lime 4' is obtained, in which the quicklime powder 3 does not remain (and most of the water is contained). It is in a dry state because it is consumed in water use reactions.

尚、この発明の実施態様は上従実施例に限るものでない
ことは勿論であり1例えば、水の添加量。
It should be noted that the embodiments of the present invention are of course not limited to the above embodiments; for example, the amount of water added may vary.

生石灰粉末の粒径及び添加量、加圧成形の際の圧力等t
it特に駆足されず、これらの条件を変えることによっ
て粒状物の粒径や回収率を種々に変化させることが出来
る。
Particle size and amount of quicklime powder added, pressure during pressure molding, etc.
However, by changing these conditions, the particle size and recovery rate of the granules can be varied.

次に上述実施例に従って行なった実験データについて第
6図及び第7図を参照して説明すれば以下の通りである
Next, the experimental data conducted according to the above embodiment will be explained with reference to FIGS. 6 and 7.

第6図には0.149〜Q、5m/m粒径の生石灰粉末
を使用し、その添加量を変えた場合に於いて、得られた
粒状消石灰の粒径分布が示されており、縦軸に累積透過
率T%を、横軸に消石灰粒径”/−I RkとるO 尚1図中、・・・0・・・0・・・の曲線は3重量%、
−x−xの曲線1d5重量係、−・−・の曲線は8重量
%、−△−−−△−の曲線は9重量%添加した場合をそ
れぞれ表わしている。
Figure 6 shows the particle size distribution of granular slaked lime obtained when quicklime powder with a particle size of 0.149~Q, 5m/m was used and the amount added was changed. The cumulative transmittance T% is plotted on the axis, and the slaked lime particle size is plotted on the horizontal axis.
-x-x curve 1d5 weight ratio, --- curve represents 8% by weight, and -Δ--Δ- curve represents 9% by weight.

第7図に叫生石灰粉末を10重量%添加し、その粒径を
変えた場合に於いて、得られた粒状消石灰の粒径分布が
示されており、縦軸には累積透過率T%を、横軸には消
石灰粒径−/−R1に示し、図中、−・−・−の曲線は
−0,149Ill/II、−−x−−x−−の曲線は
0.149〜Q、5 m/y*1−Δ−Δ−の曲#は0
.5〜1.0 m/m、−o −o−の曲線はto〜3
.07+1/、の粒径のものを使用した場合の分布をそ
れぞれ表わしている。
Figure 7 shows the particle size distribution of the obtained granular slaked lime when 10% by weight of slaked lime powder was added and the particle size was changed, and the vertical axis shows the cumulative transmittance T%. , the horizontal axis shows the slaked lime particle size -/-R1, in the figure, the curve of -...- is -0,149Ill/II, the curve of -x--x- is 0.149~Q, 5 m/y*1-Δ-Δ- song # is 0
.. 5~1.0 m/m, -o -o- curve is to~3
.. 07+1/, respectively.

而して、上記@6図及び第7図の分布状態を参照すると
、得られた粒状消石灰は粒径311JI以下のものがほ
とんどであり、しかも、消石灰粉末の本質的な粒径であ
る100μ以下のものはわずか1゜チ以下であり、優れ
た回収率であることが明らかである。
Therefore, referring to the distribution state shown in Figure 6 and Figure 7 above, most of the obtained granular slaked lime has a particle size of 311JI or less, and moreover, it has a particle size of 100μ or less, which is the essential particle size of slaked lime powder. It is clear that the recovery rate is only 1° or less, which is an excellent recovery rate.

前述の如く、この発明によれば、消石灰粉末を予かしめ
加湿し、これに生石灰粉末を添加混合した後、加圧成形
し、該成形物を反応養生することによって上記生石灰粉
末の水利膨張力を利用して崩壊させるので、破砕工程を
省略出来るという優れた効果がある。
As described above, according to the present invention, slaked lime powder is pre-caulked and humidified, quicklime powder is added and mixed therein, and then pressure molded, and the molded product is reacted and cured, thereby increasing the water expansion power of the quicklime powder. Since it is used to disintegrate it, it has the excellent effect of omitting the crushing process.

又、上記生石灰粉末の水利反応によって水分が消費され
るので、得られた粒状消石灰は乾燥状態となっており、
乾燥工程を省略出来るという効果もある。
In addition, since water is consumed by the water utilization reaction of the quicklime powder, the obtained granular slaked lime is in a dry state.
Another advantage is that the drying process can be omitted.

更に、上記粒状消石灰の粒径分布は3 mar以下のも
のがほとんどであり、消石灰粉末のま\である100μ
以下のものは10’1以下であるので、回収率が極めて
高(なるという優れた効果がある。
Furthermore, the particle size distribution of the above-mentioned granular slaked lime is mostly 3 mar or less, and the particle size distribution of the slaked lime powder is 100 μm.
Since the following substances have a molecular weight of 10'1 or less, they have an excellent effect of having an extremely high recovery rate.

加えて、上記粒状消石灰は崩壊によって得られるものな
ので、破砕によって得られるものと比べて非常に丸みを
帯びており、手ざわりや流動性に関して優れた性質ti
するという効果もある。
In addition, since the granular slaked lime is obtained by disintegration, it is much more rounded than that obtained by crushing, and has superior properties in terms of texture and fluidity.
There is also the effect of

【図面の簡単な説明】[Brief explanation of the drawing]

図面はこの発明の実施例を示すものであり、第1図は消
石灰粉末の状態説明図、第2図は水を添加混合した状態
説明図、第3図は生石灰粉末を添〃口混合した状態説明
図、第4.:、、図は加圧成形した状態説明図、第5図
は成形物4′iM壊した状態説明図、第6図は生石灰粉
末の添加量を変えた場合における得られた粒状消石灰の
粒径分布図、第7図は生石灰粉末の粒径を変えた場合に
おける得られた粒状消石灰の粒径分布図である。 4.4′・・・粒状消石灰、 1・・・消石灰粉末、3
・・・生石灰粉末 1′ 第1図  第2図  第3図 第4図   第5 F2+ @6  図 丁 (’A) 第7図 儀T
The drawings show examples of the present invention; Fig. 1 is an explanatory diagram of the state of slaked lime powder, Fig. 2 is an explanatory diagram of the state in which water is added and mixed, and Fig. 3 is an explanatory diagram of the state in which quicklime powder is added and mixed. Explanatory diagram, 4th. :,,The figure is an explanatory diagram of the state after pressure molding, Figure 5 is an explanatory diagram of the state of broken molded product 4'iM, and Figure 6 is the particle size of the obtained granular slaked lime when the amount of quicklime powder added is changed. Distribution diagram, FIG. 7 is a particle size distribution diagram of granular slaked lime obtained when the particle size of quicklime powder was changed. 4.4'... Granular slaked lime, 1... Slaked lime powder, 3
...Quicklime powder 1' Fig. 1 Fig. 2 Fig. 3 Fig. 4 Fig. 5 F2+ @6 Illustration ('A) Fig. 7 T

Claims (1)

【特許請求の範囲】[Claims] 消石灰粉末より粒状消石灰を製造する方法において、該
消石灰粉末をあらかじめ加湿し、これに生石灰粉末を添
加混合した後、加圧成形し、該成形物を反応養生するこ
とによって上記生石灰粉末の水利膨張力を利用して崩壊
させることを特徴とする粒状消石灰の製造方法。
In a method for producing granular slaked lime from slaked lime powder, the slaked lime powder is humidified in advance, quicklime powder is added and mixed therein, and then pressure molded, and the molded product is reacted and cured to improve the water expansion capacity of the quicklime powder. A method for producing granular slaked lime characterized by disintegrating it using.
JP20022081A 1981-12-14 1981-12-14 Manufacture of granular slaked lime Granted JPS58104048A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20022081A JPS58104048A (en) 1981-12-14 1981-12-14 Manufacture of granular slaked lime

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20022081A JPS58104048A (en) 1981-12-14 1981-12-14 Manufacture of granular slaked lime

Publications (2)

Publication Number Publication Date
JPS58104048A true JPS58104048A (en) 1983-06-21
JPS618025B2 JPS618025B2 (en) 1986-03-11

Family

ID=16420800

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20022081A Granted JPS58104048A (en) 1981-12-14 1981-12-14 Manufacture of granular slaked lime

Country Status (1)

Country Link
JP (1) JPS58104048A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6081021A (en) * 1983-10-12 1985-05-09 Tokio Kanou Granulating method of slaked lime
JPS6085860A (en) * 1983-10-12 1985-05-15 Sumitomo Metal Ind Ltd Displacement transmitting device and three- dimentioninal operating mechanism
JPS6136142A (en) * 1984-07-27 1986-02-20 新東工業株式会社 Dry granulation for slaked lime powder or slaked lime mixed powder
JPS6142327A (en) * 1984-08-02 1986-02-28 Nippon Mining Co Ltd Method for discharging caked waste catalyst

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6081021A (en) * 1983-10-12 1985-05-09 Tokio Kanou Granulating method of slaked lime
JPS6085860A (en) * 1983-10-12 1985-05-15 Sumitomo Metal Ind Ltd Displacement transmitting device and three- dimentioninal operating mechanism
JPS6316332B2 (en) * 1983-10-12 1988-04-08 Tokio Kano
JPS6136142A (en) * 1984-07-27 1986-02-20 新東工業株式会社 Dry granulation for slaked lime powder or slaked lime mixed powder
JPS6142327A (en) * 1984-08-02 1986-02-28 Nippon Mining Co Ltd Method for discharging caked waste catalyst
JPH0212140B2 (en) * 1984-08-02 1990-03-19 Nippon Mining Co

Also Published As

Publication number Publication date
JPS618025B2 (en) 1986-03-11

Similar Documents

Publication Publication Date Title
US4780144A (en) Method for producing a building element from a fly ash comprising material and building element formed
JPH0657605B2 (en) Method for producing calcium sulfate-α-hemihydrate from fine powder of calcium sulfate dihydrate
US4919722A (en) Method of manufacturing a granular building material from refuse
JPS62197343A (en) Manufacture of low water-absorptive artificial lightweight aggregate
CN102776047B (en) Method for molding calcium-base industrial powder
JPS58104048A (en) Manufacture of granular slaked lime
CN104451135A (en) Method for agglomerating pellets containing ultrafine coal powder and ultrafine quicklime powder
CN103539987B (en) A kind of plastic waste, waste rubber make modified plastic rubber working method
JPH0234513A (en) Production of slaked lime granule
JPH0416533A (en) Production of nonswellable slag with steel making slag
CN111675200A (en) Method for producing powdered rock phosphate pellets by using powdered rock phosphate
SU990756A1 (en) Process for producing granulated potassium fertilizer
JPS63170215A (en) Granulating method for aluminium dross
US3053819A (en) Compacting water-soluble polymers of acrylamides
JP5362234B2 (en) Slaked lime granular material and method for producing the same
CN115893401B (en) Secondary particle artificial graphite negative electrode material and preparation method thereof
CN103408235A (en) Powder forming adhesive
US4139587A (en) Process for forming fluorspar compacts
JPH061855A (en) Production of granular polyphenylene sulfide
JPS60228622A (en) Production of charcoal powder briquette
JP2000198983A (en) Production of porous carbonized material by using liquor waste, and porous carbonized material prepared thereby
TWI686280B (en) Manufacturing method for pelletizing iron sand
US2328573A (en) Slakable lime in pebble form and method of producing the same
US1967222A (en) Granulation of finely divided materials
SU1096265A1 (en) Method for producing potassium fertilizers