TWI558816B - Calcium fluoride powder or sludge granulation method - Google Patents

Calcium fluoride powder or sludge granulation method Download PDF

Info

Publication number
TWI558816B
TWI558816B TW104139326A TW104139326A TWI558816B TW I558816 B TWI558816 B TW I558816B TW 104139326 A TW104139326 A TW 104139326A TW 104139326 A TW104139326 A TW 104139326A TW I558816 B TWI558816 B TW I558816B
Authority
TW
Taiwan
Prior art keywords
calcium fluoride
powder
sludge
premix
fluoride powder
Prior art date
Application number
TW104139326A
Other languages
Chinese (zh)
Other versions
TW201718881A (en
Inventor
Zheng-Xian Cai
Ping-Si Cai
Yu-Min Su
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 filed Critical
Priority to TW104139326A priority Critical patent/TWI558816B/en
Priority to CN201610009721.8A priority patent/CN106799192A/en
Application granted granted Critical
Publication of TWI558816B publication Critical patent/TWI558816B/en
Publication of TW201718881A publication Critical patent/TW201718881A/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/28Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic using special binding agents

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treatment Of Sludge (AREA)
  • Processing Of Solid Wastes (AREA)

Description

氟化鈣粉體或污泥的造粒方法Granulation method of calcium fluoride powder or sludge

本發明是有關於一種造粒方法,特別是指一種氟化鈣粉體或污泥的造粒方法。The present invention relates to a granulation method, and more particularly to a granulation method of a calcium fluoride powder or sludge.

晶圓工廠於製程中經常會使用到大量的氫氟酸,使用後的氫氟酸廢液會先以氫氧化納調整適當的pH值,再與氯化鈣或氫氧化鈣等鈣化物反應產生氟化鈣沉澱物,最後再經由壓濾或其他方法脫水後即得氟化鈣污泥(Calcium Fluoride Sludge),含水率常介於60%~80%。為了進一步降低含水量,可再進行乾燥步驟以製得氟化鈣粉體。The wafer factory often uses a large amount of hydrofluoric acid in the process. After use, the hydrofluoric acid waste liquid will first adjust the appropriate pH value with sodium hydroxide, and then react with calcium chloride or calcium hydroxide. The calcium fluoride precipitate is finally dehydrated by pressure filtration or other methods to obtain calcium fluoride sludge (Calcium Fluoride Sludge), and the water content is often between 60% and 80%. In order to further reduce the water content, a drying step may be further performed to obtain a calcium fluoride powder.

由於氟化鈣為螢石(fluorspar)的主要成分,而螢石的工業用途又相當廣泛,可應用於玻璃、陶瓷、水泥,以及鋼鐵等工業中。例如:於煉鋼時提升熔液的流動性,並可去除有害雜質,因此將氟化鈣粉體或污泥製成煉鋼用螢石將可重新回收使用並產生商業價值。然而,將氟化鈣粉體或污泥製成煉鋼用螢石須經過特定處理以確保成分符合煉鋼需求,例如:氟化鈣的重量百分比不小於75%、含水量不大於2%,及二氧化矽不大於18%。另外,煉鋼用螢石的結構強度亦有一定的要求,須再經過轉桶試驗後未通過6.3釐米的重量百分比須達88%以上。參閱圖1,台灣第496796專利核准公告號揭示的一種氟化鈣污泥資源回收處理方法,主要是將氟化鈣污泥與親氧材料、助熔劑、還原劑、發熱劑,及硬化劑輾壓混合,再冷結造粒成煉鋼用螢石。然而,此種處理方法加入相當繁複的化學材料,而提高處理成本。Since calcium fluoride is the main component of fluorspar, fluorite is widely used in industrial applications such as glass, ceramics, cement, and steel. For example, when the steel is used to improve the fluidity of the melt and remove harmful impurities, the use of calcium fluoride powder or sludge as a fluorite for steelmaking can be recycled and commercialized. However, calcium fluoride powder or sludge is made into fluorite for steelmaking, which must be specially treated to ensure that the composition meets the steelmaking requirements. For example, the weight percentage of calcium fluoride is not less than 75%, and the water content is not more than 2%. And cerium oxide is not more than 18%. In addition, the structural strength of fluorite for steelmaking also has certain requirements, and it must be more than 88% by weight of 6.3 cm after passing the drum test. Referring to Figure 1, a calcium fluoride sludge resource recovery treatment method disclosed in Taiwan No. 496796 Patent Approved Announcement No., mainly uses calcium fluoride sludge and an oxygen-friendly material, a flux, a reducing agent, a heat generating agent, and a hardener. Press mixing, then cold granulation into fluorite for steelmaking. However, such a treatment method adds a relatively complicated chemical material and increases the processing cost.

經上述說明可知,簡易地將氟化鈣粉體或污泥製成煉鋼用螢石是此技術領域的相關技術人員所待突破的難題。As can be seen from the above description, the simple use of calcium fluoride powder or sludge as fluorite for steelmaking is a problem to be solved by those skilled in the art.

因此,本發明之目的,即在提供一種氟化鈣粉體或污泥的造粒方法。Accordingly, it is an object of the present invention to provide a method of granulating a calcium fluoride powder or sludge.

於是,本發明氟化鈣粉體或污泥的造粒方法,包含一混拌步驟與一造粒步驟。Thus, the granulation method of the calcium fluoride powder or sludge of the present invention comprises a mixing step and a granulation step.

該混拌步驟將一氟化鈣粉體或污泥、一瀝青(Asphalt),及水充分混拌成一預混物。The mixing step thoroughly mixes the calcium fluoride powder or sludge, an asphalt (Asphalt), and water into a premix.

該造粒步驟將該預混物進行造粒處理,得到多數氟化鈣塊體。The granulation step granulates the premix to obtain a plurality of calcium fluoride blocks.

本發明之功效在於:僅用該瀝青作為黏著劑(binder),便能將氟化鈣粉體或污泥進行造粒,製成符合煉鋼用之螢石,因而降低處理成本。The effect of the present invention is that the calcium fluoride powder or the sludge can be granulated by using only the asphalt as a binder, thereby making fluorite suitable for steelmaking, thereby reducing the processing cost.

如圖2所示,本發明氟化鈣粉體或污泥的造粒方法的一實施例,依序包含一粉碎步驟11、一混拌步驟12、一造粒步驟13,及一除濕步驟14。As shown in FIG. 2, an embodiment of the granulation method of the calcium fluoride powder or sludge of the present invention comprises a pulverization step 11, a mixing step 12, a granulation step 13, and a dehumidification step 14 in sequence. .

該粉碎步驟11是取自一半導體工廠產出的氟化鈣污泥,並且經過脫水、高溫鍛燒成結塊體,其粒度尺寸大於0.5 mm,並經由粉碎機進行機械性粉碎後而得的氟化鈣粉體,使其粉體粒徑小於0.5 mm。The pulverizing step 11 is obtained by taking calcium fluoride sludge produced by a semiconductor factory, and dehydrating and high-temperature calcining into an agglomerate having a particle size larger than 0.5 mm and mechanically pulverized by a pulverizer. Calcium fluoride powder, the powder particle size is less than 0.5 mm.

該混拌步驟12將一氟化鈣粉體或污泥、一乳化瀝青,及水於室溫下以五段式碗型拌合器充分混拌,並持續30分鐘成一預混物。The mixing step 12 thoroughly mixes the calcium fluoride powder or sludge, an emulsified asphalt, and water at room temperature in a five-stage bowl mixer for 30 minutes to form a premix.

須說明的是,前述該粉碎步驟11的目的在於提高該氟化鈣粉體的總表面積,使粉體顆粒間與該乳化瀝青的接觸面積增加,進一步提升該預混物的結構強度。It should be noted that the purpose of the pulverization step 11 is to increase the total surface area of the calcium fluoride powder, increase the contact area between the powder particles and the emulsified asphalt, and further improve the structural strength of the premix.

瀝青是一種性能優良的黏結材料,具有施工快捷、工藝簡單、節約資源和污染小等優點。然而,一般瀝青須在高溫條件下才能熔融,操作使用並不方便,因此,本案利用將乳化瀝青(Emulsified Asphalt, EA)做黏結劑,由於,乳化後的瀝青於常溫下即呈液狀,因此,不僅可同時利用瀝青優良的黏結性,還可在常溫下進行混拌而更易於操作。詳細的說,乳化瀝青由以下三種主要物質組成:瀝青、水和乳化劑。其中,乳化劑是用於降低瀝青與水之間的界面張力,含量約0.3-5%,並根據不同乳化瀝青的用途選擇不同的乳化劑進行調配。在本實施例中,該乳化瀝青是購自竣盛科技股份有限公司。較佳地,該乳化瀝青佔該預混物的重量百分比介於1%至20%,而該預混物中的水則佔該預混物的重量百分比介於10%至80%。為了進一步讓該預混物可易於進行造粒,及由該預混物製得的氟化鈣顆粒的氟化鈣含量可符合煉鋼標準,該混拌步驟12中的水佔該預混物的重量百分比介於20%至60%,該乳化瀝青則佔該預混物的重量百分比介於3%至13%。Asphalt is a kind of bonding material with excellent performance, which has the advantages of quick construction, simple process, resource saving and low pollution. However, the general asphalt must be melted under high temperature conditions, and it is not convenient to use. Therefore, in this case, Emulsified Asphalt (EA) is used as a binder, because the emulsified asphalt is liquid at normal temperature, so Not only can the asphalt be excellent in adhesion at the same time, but it can also be mixed at room temperature for easier operation. In detail, emulsified asphalt consists of three main substances: asphalt, water and emulsifiers. Among them, the emulsifier is used to reduce the interfacial tension between asphalt and water, the content is about 0.3-5%, and different emulsifiers are selected according to the use of different emulsified asphalt. In this embodiment, the emulsified asphalt is purchased from Yusheng Technology Co., Ltd. Preferably, the emulsified asphalt comprises from 1% to 20% by weight of the premix, and the water in the premix comprises from 10% to 80% by weight of the premix. In order to further facilitate the granulation of the premix, and the calcium fluoride content of the calcium fluoride particles prepared from the premix can meet the steelmaking standard, the water in the mixing step 12 accounts for the premix. The weight percentage ranges from 20% to 60%, and the emulsified asphalt accounts for 3% to 13% by weight of the premix.

此外,要說明的是,前述該粉碎步驟11也可以視製程而不執行,尤其是氟化鈣粉體粒徑已經小於0.5 mm,或者使用氟化鈣污泥時可直接進行該混拌步驟12。In addition, it should be noted that the pulverizing step 11 described above may also be performed according to the process, in particular, the calcium fluoride powder has a particle diameter of less than 0.5 mm, or the mixing step 12 may be directly performed when the calcium fluoride sludge is used. .

值得一提的是,本發明也能單獨使用瀝青直接作為黏結劑,而無須與乳化劑混合成乳化瀝青,當單獨使用瀝青直接作為黏結劑時,則該混拌步驟12是在溫度130℃將氟化鈣粉體或污泥、水,及瀝青攪拌混合即可。It is worth mentioning that the present invention can also directly use asphalt as a binder without mixing with an emulsifier to form an emulsified asphalt. When the asphalt is directly used as a binder, the mixing step 12 is at a temperature of 130 ° C. Calcium fluoride powder or sludge, water, and asphalt can be mixed and mixed.

接著,進行該造粒步驟13,將該預混物以攪拌混合成型造粒法進行造粒處理,得到多數氟化鈣塊體。較佳地,為求應用於煉鋼工業,該等氟化鈣塊體粒度尺寸應該介於10 mm~70 mm之間。Next, the granulation step 13 is carried out, and the premix is subjected to granulation treatment by a stirring mixing granulation method to obtain a plurality of calcium fluoride bulks. Preferably, in order to be applied to the steelmaking industry, the calcium fluoride block size should be between 10 mm and 70 mm.

最後,進行該除濕步驟14,將對該等氟化鈣塊體進行乾燥處理,在溫度不大於100℃下乾燥,將該等氟化鈣塊體的含水比例調整至3%以下。經乾燥後的該等氟化鈣塊體的氟化鈣含量,經由熱重與X射線繞射分析確認後可知為84.2%,可滿足煉鋼需求標準(氟化鈣的重量百分比不小於75%)。要說明的是,乾燥溫度須控制在不大於100℃以避免水分沸騰而破壞塊體的結構強度。Finally, the dehumidifying step 14 is carried out, and the calcium fluoride blocks are dried, dried at a temperature of not more than 100 ° C, and the water content of the calcium fluoride blocks is adjusted to 3% or less. The calcium fluoride content of the dried calcium fluoride blocks after drying is confirmed by thermogravimetry and X-ray diffraction analysis to be 84.2%, which can meet the steelmaking demand standard (the weight percentage of calcium fluoride is not less than 75%). ). It should be noted that the drying temperature must be controlled to not more than 100 ° C to avoid boiling of water and destroy the structural strength of the block.

為了進一步測試該實施例的製品的結構強度,將該造粒步驟13得到的氟化鈣塊體製作成一直徑為5公分且高度為1.9公分的柱狀試體,並在室溫下靜置48小時後脫模,再以 95℃烘乾 5 hr後,室溫下進行養護,等待七天的試驗齡期到達時再依據Japanese Industrial Standard JIS M 8712-1971  規範進行轉桶強度試驗。簡單地說,該轉桶強度試驗是在轉桶轉13圈下量測造粒試體粒度未通過 6.3 mm篩網之重量比。參閱圖3,當該乳化瀝青到達7%時,未通過6.3 mm篩網之重量比可達88.2%,顯示利用本發明製得的氟化鈣塊體強度符合可煉鋼需求標準(未通過6.3mm篩網之重量比須達88%以上)。In order to further test the structural strength of the article of this example, the calcium fluoride block obtained in the granulation step 13 was formed into a columnar sample having a diameter of 5 cm and a height of 1.9 cm, and allowed to stand at room temperature. After the hour, the mold was released, and then dried at 95 ° C for 5 hr, and then cured at room temperature. When the test age of seven days was reached, the barrel strength test was carried out according to the Japanese Industrial Standard JIS M 8712-1971 specification. Briefly, the drum strength test measures the weight ratio of the granulated test piece to the 6.3 mm screen after 13 turns of the drum. Referring to Figure 3, when the emulsified asphalt reaches 7%, the weight ratio of the un-passed 6.3 mm screen can reach 88.2%, indicating that the strength of the calcium fluoride block produced by the present invention meets the demand standard of the refinable steel (failed 6.3) The weight ratio of the mm screen must be over 88%).

綜上所述,本發明透過利用瀝青或乳化瀝青作為黏著劑,便能將氟化鈣粉體或污泥製成煉鋼用螢石,使降低處理成本。因此,確實可達到本發明之目的。In summary, the present invention can make calcium fluoride powder or sludge into fluorite for steel making by using asphalt or emulsified asphalt as an adhesive, thereby reducing the processing cost. Therefore, the object of the present invention can be achieved.

惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍,凡是依本發明申請專利範圍及專利說明書內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。The above is only the preferred embodiment of the present invention, and the scope of the present invention is not limited thereto, and the simple equivalent changes and modifications made by the scope of the patent application and the patent specification of the present invention are It is still within the scope of the invention patent.

11‧‧‧粉碎步驟
13‧‧‧造粒步驟
12‧‧‧混拌步驟
14‧‧‧除濕步驟
11‧‧‧Smashing steps
13‧‧‧granulation step
12‧‧‧mixing step
14‧‧‧Dehumidification step

本發明之其他的特徵及功效,將於參照圖式的實施方式中清楚地呈現,其中: 圖1是一步驟流程圖,說明由台灣第496796專利核准公告號所揭示的一種氟化鈣污泥資源回收處理方法; 圖2是一步驟流程圖,說明本發明氟化鈣粉體或污泥的造粒方法的一實施例;及 圖3是一轉桶試驗數據圖,說明該實施例所製得的製品的結構強度。Other features and effects of the present invention will be apparent from the following description of the drawings, wherein: Figure 1 is a flow diagram illustrating a calcium fluoride sludge disclosed by Taiwan Patent No. 496796 Approved Publication No. FIG. 2 is a flow chart showing a method of granulating a calcium fluoride powder or sludge according to the present invention; and FIG. 3 is a data chart of a rotary drum test, illustrating the system of the embodiment. The structural strength of the resulting product.

11‧‧‧粉碎步驟 11‧‧‧Smashing steps

12‧‧‧混拌步驟 12‧‧‧mixing step

13‧‧‧造粒步驟 13‧‧‧granulation step

14‧‧‧除濕步驟 14‧‧‧Dehumidification step

Claims (6)

一種氟化鈣粉體或污泥的造粒方法,包含:一混拌步驟:將瀝青先與一乳化劑及水混合成乳化瀝青,再與氟化鈣粉體或污泥、水充分混拌成一預混物,其中,該乳化瀝青佔該預混物的重量百分比介於1%至20%,水則佔該預混物的重量百分比介於10%至80%;及一造粒步驟:將該預混物進行造粒處理,得到多數氟化鈣塊體。 The invention relates to a granulation method of calcium fluoride powder or sludge, comprising: a mixing step: mixing asphalt with an emulsifier and water to form an emulsified asphalt, and then fully mixing with calcium fluoride powder or sludge and water. Forming a premix, wherein the emulsified asphalt comprises from 1% to 20% by weight of the premix, and water comprises from 10% to 80% by weight of the premix; and a granulation step: The premix was subjected to granulation treatment to obtain a plurality of calcium fluoride blocks. 如請求項第1項所述的氟化鈣粉體或污泥的造粒方法,其中,該混拌步驟中的乳化瀝青佔該預混物的重量百分比介於3%至13%,水則佔該預混物的重量百分比介於20%至60%。 The method for granulating calcium fluoride powder or sludge according to claim 1, wherein the emulsified asphalt in the mixing step accounts for 3% to 13% by weight of the premix, and the water is The weight percentage of the premix is between 20% and 60%. 如請求項第1項所述的氟化鈣粉體或污泥的造粒方法,還包含一實施於該混拌步驟之前的粉碎步驟,該粉碎步驟是將一氟化鈣結塊體粉碎成複數粉體粒徑小於0.5mm的氟化鈣粉體。 The method for granulating calcium fluoride powder or sludge according to claim 1, further comprising a pulverizing step performed before the mixing step, the pulverizing step is pulverizing the calcium fluoride agglomerate into A powder of calcium fluoride having a powder particle size of less than 0.5 mm. 如請求項第1項所述的氟化鈣粉體或污泥的造粒方法,還包含一實施於該造粒步驟之後的除濕步驟,該除濕步驟是對該等氟化鈣塊體進行乾燥處理。 The method for granulating calcium fluoride powder or sludge according to claim 1, further comprising a dehumidifying step performed after the granulating step, wherein the dehumidifying step is to dry the calcium fluoride blocks. deal with. 如請求項第4項所述的氟化鈣粉體或污泥的造粒方法,其中,該除濕步驟乾燥後的該等氟化鈣塊體的氟化鈣含量不小於75%。 The method for granulating calcium fluoride powder or sludge according to claim 4, wherein the calcium fluoride content of the calcium fluoride bulk after drying in the dehumidifying step is not less than 75%. 如請求項第4項所述的氟化鈣粉體或污泥的造粒方法,其中,該除濕步驟是在溫度不大於100℃下乾燥,將該等氟化鈣塊體的含水比例調整至3%以下。The method for granulating calcium fluoride powder or sludge according to claim 4, wherein the dehumidifying step is drying at a temperature not higher than 100 ° C, and adjusting the water content of the calcium fluoride block to Less than 3%.
TW104139326A 2015-11-26 2015-11-26 Calcium fluoride powder or sludge granulation method TWI558816B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
TW104139326A TWI558816B (en) 2015-11-26 2015-11-26 Calcium fluoride powder or sludge granulation method
CN201610009721.8A CN106799192A (en) 2015-11-26 2016-01-07 Granulation method of calcium fluoride powder or sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW104139326A TWI558816B (en) 2015-11-26 2015-11-26 Calcium fluoride powder or sludge granulation method

Publications (2)

Publication Number Publication Date
TWI558816B true TWI558816B (en) 2016-11-21
TW201718881A TW201718881A (en) 2017-06-01

Family

ID=57851672

Family Applications (1)

Application Number Title Priority Date Filing Date
TW104139326A TWI558816B (en) 2015-11-26 2015-11-26 Calcium fluoride powder or sludge granulation method

Country Status (2)

Country Link
CN (1) CN106799192A (en)
TW (1) TWI558816B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111994937B (en) * 2020-08-31 2023-11-03 苏州中材非金属矿工业设计研究院有限公司 Method for recycling calcium fluoride from fluorine-containing sludge

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101041725A (en) * 2006-03-24 2007-09-26 陈书怡 Reproduction new method for waste elastomer and plastic
CN101289310A (en) * 2008-03-24 2008-10-22 昆明理工大学 Low-temperature ceramic permeable bricks and production method thereof

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100422086C (en) * 2006-12-25 2008-10-01 张远 Synthotic fluospar
CN101837435B (en) * 2009-03-20 2011-09-21 宝山钢铁股份有限公司 Method for preparing casting covering slag by utilizing stainless steel cold-rolling pickling wastewater
CN102107127B (en) * 2011-01-11 2015-04-22 西安蓝晓科技新材料股份有限公司 Technology for granulating powder
CN102776325A (en) * 2012-08-16 2012-11-14 大余县萤通工贸有限公司 Fluorite pellet and method for producing same
CN104804443A (en) * 2015-04-28 2015-07-29 上海路惠环保科技有限公司 Emulsified asphalt and preparation method and application thereof

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101041725A (en) * 2006-03-24 2007-09-26 陈书怡 Reproduction new method for waste elastomer and plastic
CN101289310A (en) * 2008-03-24 2008-10-22 昆明理工大学 Low-temperature ceramic permeable bricks and production method thereof

Also Published As

Publication number Publication date
TW201718881A (en) 2017-06-01
CN106799192A (en) 2017-06-06

Similar Documents

Publication Publication Date Title
Eloneva et al. Steel converter slag as a raw material for precipitation of pure calcium carbonate
CN104193202B (en) A kind of high-moisture-retention cement
CN102126838B (en) Method for preparing light building material ceramsites by using lithium extraction slag of lithium mica
WO2019210729A1 (en) Caulking gypsum powder and preparation method therefor, and harmless treatment method for phosphogypsum
CN104261363B (en) A kind of ground phosphate rock granulating and forming roasting method
TWI716910B (en) Ceramic membrane and method for manufacturing ceramic membrane by recycling incinerator fly ash
TWI558816B (en) Calcium fluoride powder or sludge granulation method
JP2013088237A (en) Cesium contaminated soil surface solidification method, cesium solidification/insolubilization method, soil solidification agent used therefor, cesium removal method and magnesium-oxide based adsorbent used therefor
CN105693125B (en) A kind of sulphate aluminium cement heat stabilizer and its application method
TWM467518U (en) Equipment for fabricating fluorite balls using calcium fluoride sludge
TWI682916B (en) Method of manufacturing binder material, cured mortar and cured mortar forming by thereof
TW201524934A (en) A artificial fluorite and its manufacturing method
JP2013014492A (en) Silicic acid phosphate fertilizer, and method for producing the same
JP2007254188A (en) Method for producing acid-expandable mica
CN106892579A (en) Make raw material production white portland cement clinker using industrial residue lithium slag
TWI634082B (en) Method for treating and mixing inorganic sludge for cold-solidified artificial aggregate
CN103143316A (en) Method for preparing fluorine removal agent by taking perhafnate cement as raw material
CN103193516A (en) Method for preparing potassium sulphate fertilizer and co-producing special cement from potassium rock
CN107619253A (en) A kind of inorganic mining anchoring agent and preparation method thereof
CN104261362B (en) A kind of ground phosphate rock pressure ball molding method of roasting
CN104261368A (en) Powdered rock phosphate pellet pressing, molding and drying method
JPS5830380A (en) Treatment for incineration ash of sewage sludge
CN100344553C (en) Production method of medication for removing water sulfate radical ion
CN109836061A (en) The manufacturing method and mortar constituent of mortar fine granules
TWI675813B (en) Method of resourceful disposal for stabilizing materials with the property of expansion

Legal Events

Date Code Title Description
MM4A Annulment or lapse of patent due to non-payment of fees