JPS63274614A - Manufacture of alpha-type gypsum hemihydrate - Google Patents

Manufacture of alpha-type gypsum hemihydrate

Info

Publication number
JPS63274614A
JPS63274614A JP10883787A JP10883787A JPS63274614A JP S63274614 A JPS63274614 A JP S63274614A JP 10883787 A JP10883787 A JP 10883787A JP 10883787 A JP10883787 A JP 10883787A JP S63274614 A JPS63274614 A JP S63274614A
Authority
JP
Japan
Prior art keywords
gypsum
sodium citrate
concentration
slurry
alpha
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
JP10883787A
Other languages
Japanese (ja)
Other versions
JPH0686293B2 (en
Inventor
Masakazu Onizuka
鬼塚 雅和
Naoharu Shinoda
篠田 直晴
Atsushi Tatani
多谷 淳
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.)
Chubu Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
Original Assignee
Chubu Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
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 Chubu Electric Power Co Inc, Mitsubishi Heavy Industries Ltd filed Critical Chubu Electric Power Co Inc
Priority to JP10883787A priority Critical patent/JPH0686293B2/en
Publication of JPS63274614A publication Critical patent/JPS63274614A/en
Publication of JPH0686293B2 publication Critical patent/JPH0686293B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B11/00Calcium sulfate cements
    • C04B11/02Methods and apparatus for dehydrating gypsum
    • C04B11/024Ingredients added before, or during, the calcining process, e.g. calcination modifiers
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B11/00Calcium sulfate cements
    • C04B11/02Methods and apparatus for dehydrating gypsum

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

PURPOSE:To continuously obtain the titled gypsum hemihydrate stable in its quality and useful as an architectural material or a board material, etc., by adding a sodium citrate in a gypsum dihydrate slurry and conducting a pressurized water heating treat ment under controlling a temperature and an electric conductivity, etc. CONSTITUTION:The raw material gypsum dihydrate slurry (2CA) is fed from a feeding tank 4 to the pressurized water heating treatment bath 11, agitated by a stirrer 19, and is circulated to a tank 4 through a cyclone 24 under the control by a level sensor 21, a controlling valve 23 etc. On the other side, under the calculation by an arithmetic controller 10 with actuating a electric conductivity sensor 6 and a thermometer 8 according to operation expression, the formula I [wherein A* is the electric conductiv ity mS/cm; (t) is deg.C; C* is a saturated dissolved gypsum concentration g/kg-H2O; alpha, (n) and (m) are factors] and the formula II [wherein Cadd is the sodium citrate (CiNa) concentration wt.%; LAMBDA is the electric conductivity of the 2CA mS/cm; beta is a factor], a <=0.01wt.% CiNa is fed from a storage tank 2 to the treatment bath 11 while being added to the 2CA in the feeding tank 4, and is subjected to the pressurized water heating treatment with stirring at >=140 deg.C for a desired period of time to convert the 2CA to the alpha-type gypsum hemihydrate.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、建築基材やボード材あるいは模型用として用
いられるα型半水石膏の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing α-type hemihydrate gypsum used as a building base material, board material, or model.

〔従来の技術〕[Conventional technology]

α型半水石膏の製法としては、加圧水溶液法、加圧水蒸
気法、音圧水溶液法などが矧られているが、いずれも回
分方式で製造する方法であり、大量のα型半水石膏を製
造するには不適当な方法であつ次。
There are several methods for producing α-type hemihydrate gypsum, such as the pressurized aqueous solution method, pressurized steam method, and sonic pressure aqueous solution method, but all of them are batch production methods and produce large quantities of α-type hemihydrate gypsum. In an inappropriate way.

本発明者らは従来の回分方式を連続生産方式にして工業
的に大容量のα型半水石iIrを連続的に製造する方法
として媒晶剤としてのクエン酸ナトリウム′t−1lL
01重重−以下添加した二水石膏スラリーを140℃以
上で処理しα型半水石膏を連続的に製造する方法を既に
提案し友。(特公昭59〜3406号公報参照) しかしながら、本発明者らは、既提案製造法では連続的
に品質の安定したα型半水石膏を製造することが難かし
く、微細粒径のα型半水石膏が混在したり′■型無水石
膏が生成したりすることをたびたび経験した。
The present inventors developed a method for continuously producing α-type hemihydrate iIr in large quantities industrially by converting the conventional batch method into a continuous production method.
We have already proposed a method for continuously producing α-type hemihydrate gypsum by processing dihydrate gypsum slurry containing 0.01 weight or less at 140°C or higher. (Refer to Japanese Patent Publication No. 59-3406) However, the present inventors discovered that it is difficult to continuously produce α-type hemihydrate gypsum with stable quality using the previously proposed production method, and that I have often experienced the presence of aqueous gypsum or the formation of '■-type anhydrite.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

そこで本発明は、従来方法の欠点を解消しうる微細な粒
のα型半水石膏や■型無水石膏が混在しない品質の安定
したα型半水石膏の連続的な製造法を提供しようとする
ものである。
Therefore, the present invention aims to provide a method for continuously producing α-type hemihydrate gypsum with stable quality and free from the mixture of fine-grained α-type hemihydrate gypsum and ■-type anhydrite, which can eliminate the drawbacks of conventional methods. It is something.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは前記提案方法のα型半水石膏の品質不安定
な原因を検討した結果、原料でろる二水石膏スラリー中
に含有するクエン酸ナトリウム濃度が経時的に変動し、
加圧水熱処理槽内でα型半水石膏の結晶成長速度が安定
していないことが主因であるとの結論に至り、加圧水熱
処理槽でのクエン酸す) IJウム濃度を恒常的に安定
化させることによって連続して安定した品質のα警手水
石1fを製造し得るという知見を得たO 本発明はこの知見に基づいて完成されたものでろって、
二水石膏スラリーを加圧水熱処理してα型半水石膏に転
移させるにあ次り、クエン酸ナトIJウムをα0.01
重量*以下含有した二水石膏スラリーを140℃以上の
温度で適当時間加圧水熱処理槽で処理してα型半水石膏
を連続的に製造する方法において、上記二水石膏スラリ
ーの温度と電気伝導度を測定して、該二水石膏スラリー
に添加するクエン酸ナトリウムの添加tを調節すること
を特徴とするα型半水石膏の製造方法である。
The present inventors investigated the cause of the unstable quality of α-type hemihydrate gypsum produced by the proposed method, and found that the concentration of sodium citrate contained in the dihydrate slurry made from the raw material fluctuates over time.
It was concluded that the main cause was that the crystal growth rate of α-type hemihydrate gypsum was not stable in the pressurized hydrothermal treatment tank. The present invention was completed based on this knowledge, and the present invention was completed based on this knowledge.
After the dihydrate gypsum slurry was subjected to pressure hydrothermal treatment to transform into α-type hemihydrate gypsum, sodium citrate was added to α0.01
In a method for continuously producing α-type hemihydrate gypsum by treating a dihydrate gypsum slurry containing not more than weight * in a pressurized hydrothermal treatment tank at a temperature of 140° C. or higher for an appropriate time, the temperature and electrical conductivity of the dihydrate gypsum slurry are This is a method for producing α-type hemihydrate gypsum, which is characterized in that the addition t of sodium citrate added to the dihydrate gypsum slurry is adjusted by measuring .

水中に溶解する二水石膏の溶解度は温度に依存して変化
し、又この溶解量は液の電気伝導度を測定すれば、測定
された電気伝導度と温度から知ることができる。さらに
これにクエン酸ナトリウムを添加すると電気伝導度は変
化するが二水石膏スラリー中へのクエンばナトリウムの
添加量に応じて変化する電気伝導度の変化とクエン酸ナ
トリウム添加量との関係を各温度との関係として予め検
量しておけば二本石膏スラリー中のクエン酸ナトリウム
量が判る。
The solubility of dihydrate gypsum in water varies depending on the temperature, and the amount dissolved can be determined from the measured electrical conductivity and temperature by measuring the electrical conductivity of the liquid. Furthermore, when sodium citrate is added to this, the electrical conductivity changes, but the relationship between the change in electrical conductivity, which changes depending on the amount of sodium citrate added to the dihydrate gypsum slurry, and the amount of sodium citrate added is If it is calibrated in advance in relation to temperature, the amount of sodium citrate in the two-piece gypsum slurry can be determined.

これらの関係について第2図〜第4図に示した。@2図
は二水石膏の水中への溶解度を温度の関数として示した
図でろり、この溶解度と温度の関係を安達らは(!)式
の3次式として蟲め、次のように示している。(Gyp
日un & Line 。
These relationships are shown in FIGS. 2 to 4. Figure 2 shows the solubility of gypsum dihydrate in water as a function of temperature.Adachi et al. ing. (Gyp
Sun & Line.

No、135.1975.P63−72)8=a + 
tit + at” + dt”          
”” Tl1S:l解反  (f−Ca804/kf/
−HxO)a、 b、 c、 (1:係数 〔−〕t:
@ 匿  (C) 第3図は各温度(40℃、60℃、80℃。
No. 135.1975. P63-72) 8=a +
tit + at” + dt”
"" Tl1S:l solution (f-Ca804/kf/
-HxO) a, b, c, (1: coefficient [-]t:
@ Hidden (C) Figure 3 shows various temperatures (40℃, 60℃, 80℃.

100℃)における溶解石膏濃度と電気伝導度の関係を
示すグラフであり、縦軸は電気伝導度(Δ、単位me/
cm)の対数値、横軸は溶解石膏濃度(Ca804 )
の対数値を示す。第4図はクエン酸す?Vクムa度と電
気伝導度の対数値の関係を示すグラフである。
This is a graph showing the relationship between dissolved gypsum concentration and electrical conductivity at 100°C), where the vertical axis is the electrical conductivity (Δ, unit: me/
cm), the horizontal axis is the dissolved gypsum concentration (Ca804)
Indicates the logarithm value of Figure 4 is citric acid? It is a graph showing the relationship between the V-cum a degree and the logarithm value of electrical conductivity.

先ず2水石膏スラリー中の石1F溶解度は、(11式か
ら計算できるので、温度と電気伝導度の値から第3図、
第4図のグラフの関係を用いて、クエン酸ナトリウムの
濃度を求めることができ、クエン酸ナトリウムの添加t
を適正濃度に管理することができる0 〔実施例〕 第1図は本発明の一実施例として、α型半水石膏製造方
法のフローを示した図でろる〇二水石膏スラリー供給槽
4から配管5t−介して原料二水石膏スラリーを加圧水
熱処理槽11へ供給し、該加圧水熱処理槽11では攪拌
機19で攪拌しながら連続式で二水石膏を半水石膏に転
化させ、該加圧水熱処理槽11内滞留スラリー18の滞
留量が一定となるようにレベル検出器21でレベル検出
器 で制御弁23を作動させ配管20を介して、前記二水石
膏スラリーの供給量相当分を抜き出U液体サイクロン2
4′t−介して粗粒含有スラリー25を微粒スラリー2
6に分級させ、粗粒側25は製品α−半水石貴回収工程
へ送p1微粒側26は前記二水石膏スラリー供給槽4へ
循環させている。該二水石膏スラリー供給槽4にはその
他に二水石膏スラリー1とクエン酸ナトリウム貯槽2か
らクエン酸ナトリウムが供給量れるが、このクエン酸ナ
トリウムの二水石膏スラリー供給槽4への供給量は、前
記加圧水熱処理槽11へ供給している原料二本石膏スラ
リーの電気伝導度と温度を各々電気伝導度検知器6及び
温度計8で検卸し、各々の検知信号を増幅器7.9で処
理し、この信号を演算調節計10で処理して、切出し器
3を作動させて調節している。演算調節計10では下記
の演算を行なわせる。
First, the solubility of stone 1F in dihydrate gypsum slurry can be calculated from Equation 11 (Fig. 3) using the temperature and electrical conductivity values.
Using the relationship shown in the graph in Figure 4, the concentration of sodium citrate can be determined, and the addition t of sodium citrate
[Example] Figure 1 is a diagram showing the flow of a method for producing α-type hemihydrate gypsum as an example of the present invention. The raw material dihydrate gypsum slurry is supplied to the pressurized hydrothermal treatment tank 11 through the pipe 5t, and in the pressurized hydrothermal treatment tank 11, the dihydrate gypsum is continuously converted into hemihydrate gypsum while being stirred by the stirrer 19. A control valve 23 is actuated by a level detector 21 so that the amount of retained slurry 18 retained in the interior becomes constant, and an amount equivalent to the supply amount of the dihydrate gypsum slurry is extracted via piping 20. 2
4'T - Coarse particle-containing slurry 25 is passed through fine particle slurry 2.
The coarse grain side 25 is sent to the product α-hemihydrate precious recovery process, and the fine grain side 26 is circulated to the dihydrate slurry supply tank 4. The dihydrate slurry supply tank 4 is also supplied with sodium citrate from the dihydrate slurry 1 and the sodium citrate storage tank 2, but the amount of sodium citrate supplied to the dihydrate slurry supply tank 4 is , the electrical conductivity and temperature of the two raw material gypsum slurries supplied to the pressurized hydrothermal treatment tank 11 are detected by an electrical conductivity detector 6 and a thermometer 8, and each detection signal is processed by an amplifier 7.9. This signal is processed by the arithmetic controller 10, and the cutter 3 is operated and adjusted. The calculation controller 10 performs the following calculations.

(演算調節計演算項目) (1)  原料二水石膏スラリー中の飽和溶解石膏濃度
c++I  を計算 (イ)(1)式に表−1の二水石膏のa、b、cを代入 (ロ)(1)式のtは測定値を使用 (2)  媒晶剤濃度の計算 ←) 上記からtCにおける飽和溶解石膏濃度が判れば
、第3図の関係が求めた次の(2)式より Ca804
による電気伝導度が判る0A” = ff(t)n(C
’)I+11−+21、X* : WL電気伝導度  
〔ms/lI〕t:温度  〔℃〕 C“:上記(1)項で得た飽和溶解石膏濃度1度(t7
kg−H2o ) α、n、m:係数   〔−〕 (ロ)実測した電気伝導度AとA”の計算値の差からク
エン酸ナトリウム濃度が求まる。
(Arithmetic controller calculation items) (1) Calculate the saturated dissolved gypsum concentration c++I in the raw dihydrate gypsum slurry (a) Substitute a, b, and c of dihydrate gypsum in Table 1 into equation (1) (b) Use the measured value for t in equation (1). (2) Calculate modifier concentration ←) If the saturated dissolved gypsum concentration at tC is known from the above, then from the following equation (2), which calculates the relationship in Figure 3, Ca804
The electric conductivity is determined by 0A” = ff(t)n(C
') I+11-+21, X*: WL electrical conductivity
[ms/lI] t: Temperature [℃] C": Saturated dissolved gypsum concentration 1 degree obtained in the above (1) (t7
kg-H2o) α, n, m: coefficient [-] (b) The sodium citrate concentration is determined from the difference between the calculated values of the actually measured electrical conductivity A and A''.

Cadd=β(A−A”) Cada :クエン酸ナトリウム濃度 (wt%〕A 
:供給される二水石膏スラリーの電気伝導度     
     (m8/an〕β :係数      〔−
〕 (βは上記、α、n、mと同様事前に測定して定める。
Cadd=β(A-A”) Cada: Sodium citrate concentration (wt%) A
: Electrical conductivity of supplied dihydrate gypsum slurry
(m8/an]β: Coefficient [-
] (β is determined by measuring in advance like α, n, and m above.

) 本実施例での操作条件及び装置仕様扛次の通りでろる〇 (操作条件) +11  原料二水石膏スラリー濃度 :  15wt
チ(2)  クエン酸ナトリウム濃度   : α01
wtチ(3)  加圧水熱処理濃度     =140
℃(4)  加圧水熱処理槽ホールド液ii : 20
01(主要装置条件) 0) 二水石膏原料供給槽容積  : 2000t(2
)  加圧水熱処理槽容積     :  250t(
3)  加圧水熱処理槽攪拌機   :タービ4(4)
  同上撹拌機攪拌動力    : 1 kW/m”次
に本発明の効果を示すために、第5図に製品α半水石膏
の100倍拡大写真を示した。
) The operating conditions and equipment specifications in this example are as follows (Operating conditions) +11 Raw material dihydrate slurry concentration: 15wt
H (2) Sodium citrate concentration: α01
wt Chi (3) Pressurized hydrothermal treatment concentration = 140
°C (4) Pressurized hydrothermal treatment tank hold liquid II: 20
01 (Main equipment conditions) 0) Dihydrate gypsum raw material supply tank volume: 2000t (2
) Pressurized hydrothermal treatment tank volume: 250t (
3) Pressurized hydrothermal treatment tank agitator: Turbi 4 (4)
Stirring power of the same stirrer as above: 1 kW/m''Next, in order to show the effect of the present invention, FIG. 5 shows a 100 times enlarged photograph of the product α hemihydrate gypsum.

〔発明の効果〕〔Effect of the invention〕

以上述べたごとく、二水石膏原料スラリー中のクエン酸
ナトリウム濃度を所望濃度に制御維持させることによっ
て、安定した品質のα警手水石貴の連続製造ができるよ
うになった。
As described above, by controlling and maintaining the sodium citrate concentration in the dihydrate gypsum raw material slurry at a desired concentration, it has become possible to continuously produce α-Keite Suiseki with stable quality.

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

第1図は本発明方法の一実施例を示す図、第2図は二水
石膏の水中への醪解反と温度の関係を示すグラフ、第3
図は各温度における溶解石1f@度と電気伝導度の関係
を示すグラフ、第4図はクエン酸ナトリウム濃度と電気
伝導度の関係を示すグラフ、第5図は本発明の実施例で
得られ次α半水石膏の結晶構造の顕微鏡写真(100倍
)である。
Fig. 1 is a diagram showing an embodiment of the method of the present invention, Fig. 2 is a graph showing the relationship between melting of dihydrate gypsum in water and temperature, and Fig. 3
The figure is a graph showing the relationship between molten stone 1f@degree and electrical conductivity at each temperature, Figure 4 is a graph showing the relationship between sodium citrate concentration and electrical conductivity, and Figure 5 is a graph showing the relationship between the concentration of sodium citrate and electrical conductivity. This is a micrograph (100x magnification) of the crystal structure of α-hemihydrate gypsum.

Claims (1)

【特許請求の範囲】[Claims] 二水石膏スラリーを加圧水熱処理してα型半水石膏に転
移させるにあたり、クエン酸ナトリウムを0.01重量
%以下含有した二水石膏スラリーを140℃以上の温度
で適当時間加圧水熱処理槽で処理してα型半水石膏を連
続的に製造する方法において、上記二水石膏スラリーの
温度と電気伝導度を測定して、該二水石膏スラリーに添
加するクエン酸ナトリウムの添加量を調節することを特
徴とするα型半水石膏の製造方法。
In order to transform the dihydrate gypsum slurry into α-type hemihydrate gypsum through pressure hydrothermal treatment, the dihydrate gypsum slurry containing 0.01% by weight or less of sodium citrate is treated in a pressure hydrothermal treatment tank at a temperature of 140°C or higher for an appropriate period of time. In the method for continuously producing α-type hemihydrate gypsum, the temperature and electrical conductivity of the dihydrate gypsum slurry are measured and the amount of sodium citrate added to the dihydrate gypsum slurry is adjusted. Characteristic method for producing α-type hemihydrate gypsum.
JP10883787A 1987-05-06 1987-05-06 Method for producing α-type hemihydrate gypsum Expired - Fee Related JPH0686293B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10883787A JPH0686293B2 (en) 1987-05-06 1987-05-06 Method for producing α-type hemihydrate gypsum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10883787A JPH0686293B2 (en) 1987-05-06 1987-05-06 Method for producing α-type hemihydrate gypsum

Publications (2)

Publication Number Publication Date
JPS63274614A true JPS63274614A (en) 1988-11-11
JPH0686293B2 JPH0686293B2 (en) 1994-11-02

Family

ID=14494818

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10883787A Expired - Fee Related JPH0686293B2 (en) 1987-05-06 1987-05-06 Method for producing α-type hemihydrate gypsum

Country Status (1)

Country Link
JP (1) JPH0686293B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0379266A2 (en) * 1989-01-17 1990-07-25 Mitsubishi Jukogyo Kabushiki Kaisha Production method for anhydrous gypsum
JP2006273599A (en) * 2005-03-28 2006-10-12 Tokuyama Corp Method for treating waste gypsum
CN104355560A (en) * 2014-10-21 2015-02-18 金正大生态工程集团股份有限公司 Production method of alpha-gypsum powder with high strength

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0379266A2 (en) * 1989-01-17 1990-07-25 Mitsubishi Jukogyo Kabushiki Kaisha Production method for anhydrous gypsum
JP2006273599A (en) * 2005-03-28 2006-10-12 Tokuyama Corp Method for treating waste gypsum
CN104355560A (en) * 2014-10-21 2015-02-18 金正大生态工程集团股份有限公司 Production method of alpha-gypsum powder with high strength

Also Published As

Publication number Publication date
JPH0686293B2 (en) 1994-11-02

Similar Documents

Publication Publication Date Title
Abdel‐Aal et al. Crystallization of calcium sulfate dihydrate at different supersaturation ratios and different free sulfate concentrations
US4324772A (en) Process for producing hydroxyapatite
NO117067B (en)
TW200621167A (en) Process for producing food containing plant sterol
US2616789A (en) Method of producing gypsum plaster
ES8205536A1 (en) Process for producing a basic foodstuff instantaneously dispersable in water.
EP0012487B1 (en) Process for the preparation of calcium sulphate anhydrite and calcium sulphate anhydrite obtained by this process
JPS63274614A (en) Manufacture of alpha-type gypsum hemihydrate
CN107382111A (en) A kind of method that normal pressure salt solustion mehtod produces α super strong gypsums
ES329179A1 (en) Procedure for the manufacture of phosphoric acid and calcium sulfate hemihydrate via via humeda. (Machine-translation by Google Translate, not legally binding)
Brahim et al. Effect of temperature on the attack of fluorapatite by a phosphoric acid solution
US3225026A (en) Method of producing azobisformamides
Redman et al. On‐Line control of supersaturation in a continuous cooling KCL crystallizer
US2385188A (en) Process for making alkali metal ferric pyrophosphate
JP4815082B2 (en) Treatment method of iron-containing sulfuric acid solution
JP2563552B2 (en) Continuous production method of alpha-type hemihydrate gypsum
RU1797596C (en) Process for producing phosphoric acid
JP2000053418A (en) Production of gypsum fiber
EP0379266B1 (en) Production method for anhydrous gypsum
SU805943A3 (en) Method of producing calcium sulfate alpha-semihydrate
Rocha et al. Effect of surfactants on calcium sulfate crystallization in phosphoric acid solutions
SU692880A1 (en) Method of control of oxydative leaching of pyrrotine concentrates
SU1177284A1 (en) Method of automatic control for process of nitrogen-sulfate-sulfuric-acid decomposition of apatite in production of nitrate-phosphate solution (versions)
Donnison et al. Retardation of Gypsum Plaster by Calcium Tartrate
GB848617A (en) Improvements in or relating to the preparation of anhydrite

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees