CN110040991A - A method of quickly preparing short cylinder sulfate hemihydrate calcium material using calcium sulphate dihydrate - Google Patents

A method of quickly preparing short cylinder sulfate hemihydrate calcium material using calcium sulphate dihydrate Download PDF

Info

Publication number
CN110040991A
CN110040991A CN201910373883.3A CN201910373883A CN110040991A CN 110040991 A CN110040991 A CN 110040991A CN 201910373883 A CN201910373883 A CN 201910373883A CN 110040991 A CN110040991 A CN 110040991A
Authority
CN
China
Prior art keywords
calcium
sulphate dihydrate
calcium sulphate
water
short cylinder
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
CN201910373883.3A
Other languages
Chinese (zh)
Other versions
CN110040991B (en
Inventor
史培阳
杨文�
胡吕
彭朋
姜茂发
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.)
Northeastern University China
Original Assignee
Northeastern University China
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 Northeastern University China filed Critical Northeastern University China
Priority to CN201910373883.3A priority Critical patent/CN110040991B/en
Publication of CN110040991A publication Critical patent/CN110040991A/en
Application granted granted Critical
Publication of CN110040991B publication Critical patent/CN110040991B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • C04B11/028Devices therefor characterised by the type of calcining devices used therefor or by the type of hemihydrate obtained
    • C04B11/032Devices therefor characterised by the type of calcining devices used therefor or by the type of hemihydrate obtained for the wet process, e.g. dehydrating in solution or under saturated vapour conditions, i.e. to obtain alpha-hemihydrate

Abstract

The invention belongs to field of inorganic nonmetallic material, disclose a kind of method that short cylinder sulfate hemihydrate calcium material is quickly prepared using calcium sulphate dihydrate, recrystallization process occurs for common calcium sulphate dihydrate original structure after processing, crystal growth is complete, without Shrinkage Problem, the short cylinder sulfate hemihydrate calcium material use value with higher prepared.Calcium sulphate dihydrate controls the dissolution and recrystallization speed of crystal face according to the difference of each crystal face energy by the difference of energy possessed by crystal difference crystal face under different solutions system, and then completes the growth behavior control of short cylinder material.This method be calcium sulphate dihydrate is ground, the reaction of ingredient, hydrothermal solution, separation and the processes composition such as dry.The problems such as present invention can not only effectively solve the easy dusting of calcium sulphate dihydrate, intensity difference and stability are low, can also extend the application field of calcium sulfate, have important practical significance to efficient utilize of China's flue gas desulfurization product and gypsum resource.

Description

A method of quickly preparing short cylinder sulfate hemihydrate calcium material using calcium sulphate dihydrate
Technical field
The invention belongs to field of inorganic nonmetallic material, it is related to a kind of quickly preparing short cylinder half using calcium sulphate dihydrate The method of H 2 O calcium sulphate material.
Background technique
Inorganic material oriented growth control technology is most important in inorganic non-metallic material technology of preparing, not only influences To crystal structure performance, and also relate to its application field.Short cylinder sulfate hemihydrate calcium material is as a kind of high-intensity inorganic Crystalline material, because its performance is stablized, intensity is high, can significantly improve the comprehensive mechanical property of cement preparation, to concrete and builds The application market of the raising and gypsum of building material property all has important function.
With the rapid development of our country's economy, environment and land occupation are not only polluted in the increase year by year of solid waste, And huge waste is caused to resource.2018, China only industrial waste gypsum resource discharge amount just more than 100,000,000 tons or more.I The annual gypsum materials demand amount of state is huge, and the exploitation of one side natural gypsum mineral is not only caused by land reclamation vegetation Destruction be easy to cause the safe gypsum of class that caves in and due to gypsoide springy texture;Another aspect China waste gypsum Stock number is huge.Therefore, in view of China's waste gypsum current resources situation, if calcium sulphate dihydrate can be prepared into short cylinder material half Water gypsum material will have great importance to the higher value application of the large waste gypsum resource in China.
Calcium sulphate dihydrate usually exists under field conditions (factors) with lamellar form, and the particle of flake superposition composition Calcium sulphate dihydrate is often accompanied by a large amount of defects in additive process and exists in shape object, especially Industrial Solid Waste, so short cylinder material The preparation of material half-H 2 O calcium sulphate crystal is particularly important, and it is steady that the result of study of this patent not only can solve calcium sulphate dihydrate Qualitative difference and easy pulverizing problem, can also significantly improve the comprehensive mechanical property of calcium sulfate.
Chinese patent (Publication No. CN107721220A) describes for gypsum to be added to the water, and is configured to slurry, The aqueous solution of medium crystallization agent is added into slurry, is stirred evenly under room temperature, obtains reaction system;Wherein, medium crystallization agent be band phenyl ring or The polybasic carboxylic acid of hexatomic ring, the polycarboxylate with phenyl ring or hexatomic ring or be the multi-anhydride with phenyl ring or hexatomic ring; Reaction system is moved into hydrothermal reaction kettle, hydro-thermal reaction is carried out;It is cooling after hydro-thermal reaction, to obtained suspension mistake Filter, drying, obtain short cylinder αsemiwatergypsum.The difference of this patent and the patent (CN107721220A) is the reaction time It significantly reduces, 20~40min is foreshortened to by minimum 3h~6h;Additive is by the polybasic carboxylic acid with phenyl ring or hexatomic ring, band phenyl ring Or hexatomic ring polycarboxylate or be that the multi-anhydride type organic with phenyl ring or hexatomic ring is changed to magnesium chloride and lemon Sour calcium compound, calcium chloride and magnesium citrate mixture, magnesium chloride and gluconic acid calcium compound and calcium chloride and glucose Sour magnesium compound class nontoxicity environment-friendly type substance, this cleans and innoxious peace short cylinder half-H 2 O calcium sulphate crystalline material Full production has important practical significance.
Summary of the invention
The present invention provides a kind of method that short cylinder sulfate hemihydrate calcium material is quickly prepared using calcium sulphate dihydrate, places Recrystallization process occurs for common calcium sulphate dihydrate original structure after reason, and crystal growth is complete, no Shrinkage Problem, and for preparing is short Column sulfate hemihydrate calcium material use value with higher.Calcium sulphate dihydrate is under different solutions system by crystal difference Energy possessed by crystal face is different, according to the difference of each crystal face energy, controls the dissolution and recrystallization speed of crystal face, in turn Complete the growth behavior control of short cylinder material.
The technical solution adopted by the invention is as follows:
A method of quickly preparing short cylinder sulfate hemihydrate calcium material using calcium sulphate dihydrate, including the following steps:
(1) calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, planetary ball mill revolution be 50~ Under conditions of 200r/min, 30~60min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, with additive and Water mixing, is placed in high-pressure bottle, and 20~40min is kept the temperature at 120~160 DEG C, and pressure is 0.1~2MPa.Wherein add Agent is one of following: magnesium chloride and calcium citrate mixture, calcium chloride and magnesium citrate mixture, magnesium chloride and grape Saccharic acid calcium compound and calcium chloride and gluconic acid magnesium compound;
(2) to separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier and is dried 10~30min is handled, the liquid phase circulation after separation uses.
The solid-to-liquid ratio of the calcium sulphate dihydrate and water is 1:6~1:14, and the mass ratio of additive and water is 1:40~1: 100。
The consersion unit used for titanium system is rapidly heated autoclave or enamel is rapidly heated autoclave, is increased to from 20 DEG C 160 DEG C of time is 1~3h.
The present invention can prepare short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) Crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, and longitudinal length and lateral length ratio are 1~3.It is preparing Three-waste free discharge in the process, solution use closed cycle, non-environmental-pollution problem, meet China develop a circular economy and energy conservation The target of emission reduction.The problems such as present invention can not only effectively solve the easy dusting of calcium sulphate dihydrate, intensity difference and stability are low, also The application field that calcium sulfate can be extended shows China's flue gas desulfurization product and the efficient of gypsum resource using with important Sincere justice.
Specific embodiment
Specific embodiments of the present invention are described in detail below in conjunction with technical solution.
Embodiment 1:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 200r/min's in planetary ball mill revolution Under the conditions of, grind 30min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, with additive (calcium chloride and magnesium citrate Ratio 1:1) and water mixing, wherein the mass ratio of additive and water is 1:40, and the solid-to-liquid ratio of calcium sulphate dihydrate and water is 1:6, is put It is placed in high-pressure bottle, the time that 120 DEG C are increased to from 20 DEG C is 1h, pressure 1MPa, and keeps the temperature 40min at 120 DEG C; To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier and 30min is dried, point Liquid phase circulation from after uses.Prepared short cylinder sulfate hemihydrate calcium material belongs to by (002), (200), (110) and (1- 10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, and longitudinal length and lateral length ratio are 3 or so.
Embodiment 2:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 50r/min Under part, 60min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive It is 1:100 with the mass ratio of water, wherein additive is calcium chloride and magnesium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio is 1:14, is placed in high-pressure bottle, and the time that 160 DEG C are increased to from 20 DEG C is 3h, pressure 2MPa, and 160 20min is kept the temperature at DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier and is done Dry processing 10min, the liquid phase circulation after separation use.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length and laterally length Spending ratio is 1 or so.
Embodiment 3:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 180r/min's in planetary ball mill revolution Under the conditions of, grind 30min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:90, and wherein additive is calcium chloride and magnesium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:12, be placed in high-pressure bottle, be increased to from 20 DEG C 150 DEG C time be 2.5h, pressure 1.5MPa, And 25min is kept the temperature at 150 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier In 15min is dried, liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2 or so.
Embodiment 4:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 160r/min's in planetary ball mill revolution Under the conditions of, grind 35min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:80, and wherein additive is calcium chloride and magnesium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:11, be placed in high-pressure bottle, be increased to from 20 DEG C 160 DEG C time be 2h, pressure 1.2MPa, and 30min is kept the temperature at 160 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 20min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1.5 or so.
Embodiment 5:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 140r/min's in planetary ball mill revolution Under the conditions of, grind 40min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:70, and wherein additive is calcium chloride and magnesium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:10, be placed in high-pressure bottle, be increased to from 20 DEG C 140 DEG C time be 1.5h, pressure 1MPa, and 35min is kept the temperature at 140 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 25min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1 or so.
Embodiment 6:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 120r/min's in planetary ball mill revolution Under the conditions of, grind 45min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:60, and wherein additive is calcium chloride and magnesium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:9, be placed in high-pressure bottle, be increased to from 20 DEG C 130 DEG C time be 1h, pressure 0.8MPa, and 40min is kept the temperature at 130 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 30min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 3 or so.
Embodiment 7:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 100r/min's in planetary ball mill revolution Under the conditions of, grind 50min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:50, and wherein additive is calcium chloride and magnesium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:8, be placed in high-pressure bottle, be increased to from 20 DEG C 150 DEG C time be 2h, pressure 16MPa, and 20min is kept the temperature at 150 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 15min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2 or so.
Embodiment 8:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 80r/min Under part, 55min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive It is 1:45 with the mass ratio of water, wherein additive is calcium chloride and magnesium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio is 1:7, is placed in high-pressure bottle, is increased to 130 DEG C of time from 20 DEG C as 2.5h, pressure 1.8MPa, and 30min is kept the temperature at 130 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 20min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 3 or so.
Embodiment 9:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 60r/min Under part, 60min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive It is 1:90 with the mass ratio of water, wherein additive is calcium chloride and magnesium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio is 1:13, is placed in high-pressure bottle, is increased to 120 DEG C of time from 20 DEG C as 2h, pressure 0.1MPa, and 40min is kept the temperature at 120 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 30min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1.5 or so.
Embodiment 10:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 200r/min's in planetary ball mill revolution Under the conditions of, grind 30min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:75, and wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:8, be placed in high-pressure bottle, be increased to from 20 DEG C 140 DEG C time be 2.5h, pressure 1.6MPa, and 10min is kept the temperature at 140 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 25min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1 or so.
Embodiment 11:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 50r/min Under part, 60min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive It is 1:65 with the mass ratio of water, wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio is 1:12, is placed in high-pressure bottle, is increased to 130 DEG C of time from 20 DEG C as 1.5h, pressure 0.4MPa, and 30min is kept the temperature at 130 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 30min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2.5 or so.
Embodiment 12:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 130r/min's in planetary ball mill revolution Under the conditions of, grind 30min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:45, and wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:9, be placed in high-pressure bottle, be increased to from 20 DEG C 160 DEG C time be 2h, pressure 1.5MPa, and 20min is kept the temperature at 160 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 10min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 3 or so.
Embodiment 13:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 150r/min's in planetary ball mill revolution Under the conditions of, grind 35min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:80, and wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:10, be placed in high-pressure bottle, be increased to from 20 DEG C 140 DEG C time be 2.5h, pressure 2MPa, and 10min is kept the temperature at 140 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 10min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1 or so.
Embodiment 14:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 170r/min's in planetary ball mill revolution Under the conditions of, grind 45min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:60, and wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:11, be placed in high-pressure bottle, be increased to from 20 DEG C 150 DEG C time be 2h, pressure 1MPa, and 30min is kept the temperature at 150 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 30min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2.5 or so.
Embodiment 15:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 90r/min Under part, 45min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive It is 1:95 with the mass ratio of water, wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio is 1:12, is placed in high-pressure bottle, and the time that 120 DEG C are increased to from 20 DEG C is 3h, pressure 2MPa, and 120 20min is kept the temperature at DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier and is done Dry processing 10min, the liquid phase circulation after separation use.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length and laterally length Spending ratio is 2 or so.
Embodiment 16:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 70r/min Under part, 30min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive It is 1:60 with the mass ratio of water, wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio is 1:10, is placed in high-pressure bottle, is increased to 150 DEG C of time from 20 DEG C as 1.5h, pressure 1MPa, and 30min is kept the temperature at 150 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 30min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 3 or so.
Embodiment 17:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 110r/min's in planetary ball mill revolution Under the conditions of, grind 40min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:50, and wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:7, be placed in high-pressure bottle, be increased to from 20 DEG C 160 DEG C time be 1h, pressure 0.8MPa, and 30min is kept the temperature at 160 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 20min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2 or so.
Embodiment 18:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 190r/min's in planetary ball mill revolution Under the conditions of, grind 60min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:60, and wherein additive is magnesium chloride and calcium citrate mixture (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:8, be placed in high-pressure bottle, be increased to from 20 DEG C 140 DEG C time be 1.5h, pressure 0.5MPa, and 20min is kept the temperature at 140 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 30min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1.5 or so.
Embodiment 19:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 200r/min's in planetary ball mill revolution Under the conditions of, grind 30min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, with additive (calcium chloride and gluconic acid Magnesium ratio 1:1) and water mixing, wherein the mass ratio of additive and water is 1:40, and the solid-to-liquid ratio of calcium sulphate dihydrate and water is 1:6, It is placed in high-pressure bottle, the time that 120 DEG C are increased to from 20 DEG C is 3h, pressure 0.1MPa, and is kept the temperature at 120 DEG C 40min;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier and is dried 30min, the liquid phase circulation after separation use.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) it encloses with (1-10) crystal face and its symmetrical crystal face and forms short cylinder crystalline material, longitudinal length and lateral length ratio It is 3 or so.
Embodiment 20:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 50r/min Under part, 60min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive Mass ratio with water is 1:100, and wherein additive is calcium chloride and gluconic acid magnesium compound (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:14, be placed in high-pressure bottle, be increased to from 20 DEG C 160 DEG C time be 3h, pressure 1.2MPa, and 20min is kept the temperature at 160 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 10min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1 or so.
Embodiment 21:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 180r/min's in planetary ball mill revolution Under the conditions of, grind 30min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:90, and wherein additive is calcium chloride and gluconic acid magnesium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water is 1:12, is placed in high-pressure bottle, and the time that 150 DEG C are increased to from 20 DEG C is 2.5h, and pressure is 1.5MPa, and 25min is kept the temperature at 150 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of air blast 15min is dried in drier, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, Belong to and is enclosed by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face into short cylinder crystalline material, longitudinal direction Length and lateral length ratio are 3 or so.
Embodiment 22:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 160r/min's in planetary ball mill revolution Under the conditions of, grind 35min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:80, and wherein additive is calcium chloride and gluconic acid magnesium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water be 1:11, be placed in high-pressure bottle, be increased to from 20 DEG C 160 DEG C time be 2h, pressure 1.2MPa, And 30min is kept the temperature at 160 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier In 20min is dried, liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2 or so.
Embodiment 23:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 140r/min's in planetary ball mill revolution Under the conditions of, grind 40min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:70, and wherein additive is calcium chloride and gluconic acid magnesium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water be 1:10, be placed in high-pressure bottle, be increased to from 20 DEG C 140 DEG C time be 1.5h, pressure 1MPa, And 35min is kept the temperature at 140 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier In 25min is dried, liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1 or so.
Embodiment 24:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 120r/min's in planetary ball mill revolution Under the conditions of, grind 45min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:60, and wherein additive is calcium chloride and gluconic acid magnesium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water is 1:9, is placed in high-pressure bottle, is increased to 130 DEG C of time from 20 DEG C as 1h, pressure 0.8MPa, and 40min is kept the temperature at 130 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 30min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1.5 or so.
Embodiment 25:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 100r/min's in planetary ball mill revolution Under the conditions of, grind 50min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:50, and wherein additive is calcium chloride and gluconic acid magnesium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water is 1:8, is placed in high-pressure bottle, is increased to 150 DEG C of time from 20 DEG C as 2h, pressure 1.6MPa, and 20min is kept the temperature at 150 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 15min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2 or so.
Embodiment 26:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 80r/min Under part, 55min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive Mass ratio with water is 1:45, and wherein additive is calcium chloride and gluconic acid magnesium compound (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:7, be placed in high-pressure bottle, be increased to from 20 DEG C 130 DEG C time be 2.5h, pressure 1.8MPa, and 30min is kept the temperature at 130 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 20min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 3 or so.
Embodiment 27:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 60r/min Under part, 60min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive Mass ratio with water is 1:90, and wherein additive is calcium chloride and gluconic acid magnesium compound (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:13, be placed in high-pressure bottle, be increased to from 20 DEG C 120 DEG C time be 2h, pressure 1.5MPa, and 20min is kept the temperature at 120 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 30min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2.5 or so.
Embodiment 28:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 200r/min's in planetary ball mill revolution Under the conditions of, grind 30min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, with additive (magnesium chloride and gluconic acid Ca proportion 1:1) and water mixing, wherein the mass ratio of additive and water is 1:40, and the solid-to-liquid ratio of calcium sulphate dihydrate and water is 1:6, It is placed in high-pressure bottle, the time that 120 DEG C are increased to from 20 DEG C is 1h, pressure 0.1MPa, and is kept the temperature at 120 DEG C 40min;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier and is dried 30min, the liquid phase circulation after separation use.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) it encloses with (1-10) crystal face and its symmetrical crystal face and forms short cylinder crystalline material, longitudinal length and lateral length ratio It is 3 or so.
Embodiment 29:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 50r/min Under part, 60min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive Mass ratio with water is 1:100, and wherein additive is magnesium chloride and gluconic acid calcium compound (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:14, be placed in high-pressure bottle, be increased to from 20 DEG C 160 DEG C time be 3h, pressure 2MPa, and 20min is kept the temperature at 160 DEG C;To separate after reaction, the solid product isolated be placed in 120 DEG C of blast drier into Row is dried 10min, and the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1 or so.
Embodiment 30:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 180r/min's in planetary ball mill revolution Under the conditions of, grind 30min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:90, and wherein additive is magnesium chloride and gluconic acid calcium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water is 1:12, is placed in high-pressure bottle, and the time that 150 DEG C are increased to from 20 DEG C is 2.5h, and pressure is 1.5MPa, and 25min is kept the temperature at 150 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of air blast 15min is dried in drier, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, Belong to and is enclosed by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face into short cylinder crystalline material, longitudinal direction Length and lateral length ratio are 2 or so.
Embodiment 31:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 160r/min's in planetary ball mill revolution Under the conditions of, grind 35min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:80, and wherein additive is magnesium chloride and gluconic acid calcium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water be 1:11, be placed in high-pressure bottle, be increased to from 20 DEG C 160 DEG C time be 2h, pressure 1.2MPa, And 30min is kept the temperature at 160 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier In 20min is dried, liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 3 or so.
Embodiment 32:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 140r/min's in planetary ball mill revolution Under the conditions of, grind 40min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:70, and wherein additive is magnesium chloride and gluconic acid calcium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water be 1:10, be placed in high-pressure bottle, be increased to from 20 DEG C 140 DEG C time be 1.5h, pressure 1MPa, And 35min is kept the temperature at 140 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier In 25min is dried, liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1 or so.
Embodiment 33:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 120r/min's in planetary ball mill revolution Under the conditions of, grind 45min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:60, and wherein additive is magnesium chloride and gluconic acid calcium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water is 1:9, is placed in high-pressure bottle, is increased to 130 DEG C of time from 20 DEG C as 3h, pressure 0.8MPa, and 40min is kept the temperature at 130 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 30min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 3 or so.
Embodiment 34:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, is 100r/min's in planetary ball mill revolution Under the conditions of, grind 50min;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein adding The mass ratio of agent and water is 1:50, and wherein additive is magnesium chloride and gluconic acid calcium compound (1:1), calcium sulphate dihydrate with The solid-to-liquid ratio of water is 1:8, is placed in high-pressure bottle, is increased to 150 DEG C of time from 20 DEG C as 2h, pressure 1.6MPa, and 20min is kept the temperature at 150 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 15min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 15 or so.
Embodiment 35:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 80r/min Under part, 55min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive Mass ratio with water is 1:45, and wherein additive is magnesium chloride and gluconic acid calcium compound (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:7, be placed in high-pressure bottle, be increased to from 20 DEG C 130 DEG C time be 2.5h, pressure 1.8MPa, and 30min is kept the temperature at 130 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 20min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 2 or so.
Embodiment 36:
Calcium sulphate dihydrate is placed in the ball grinder of planetary ball mill, in the item that planetary ball mill revolution is 60r/min Under part, 60min is ground;Calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, is mixed with additive and water, wherein additive Mass ratio with water is 1:90, and wherein additive is magnesium chloride and gluconic acid calcium compound (1:1), calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:13, be placed in high-pressure bottle, be increased to from 20 DEG C 120 DEG C time be 2h, pressure 1.5MPa, and 20min is kept the temperature at 120 DEG C;To separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier 30min is dried, the liquid phase circulation after separation uses.Prepared short cylinder sulfate hemihydrate calcium material, belong to by (002), (200), (110) and (1-10) crystal face and its symmetrical crystal face, which enclose, forms short cylinder crystalline material, longitudinal length with Lateral length ratio is 1.5 or so.

Claims (2)

1. a kind of method for quickly preparing short cylinder sulfate hemihydrate calcium material using calcium sulphate dihydrate, which is characterized in that including with Lower step:
(1) calcium sulphate dihydrate being placed in planetary ball mill and is ground, the calcium sulphate dihydrate granularity after grinding is controlled at≤5 μm, Mix, be placed in high-pressure bottle with additive and water, at 120~160 DEG C keep the temperature 20~40min, pressure be 0.1~ 2MPa;Wherein, the additive is one of following: magnesium chloride and calcium citrate mixture, calcium chloride and magnesium citrate Mixture, magnesium chloride and gluconic acid calcium compound, calcium chloride and gluconic acid magnesium compound;The calcium sulphate dihydrate and water Solid-to-liquid ratio be 1:6~1:14;The mass ratio of the additive and water is 1:40~1:100;
(2) to separate after reaction, the solid product isolated is placed in 120 DEG C of blast drier and is dried 10 ~30min, the liquid phase circulation after separation use.
2. a kind of side for quickly preparing short cylinder sulfate hemihydrate calcium material using calcium sulphate dihydrate according to claim 1 Method, it is characterized in that being: titanium system is rapidly heated autoclave or enamel is rapidly heated autoclave, from 20 DEG C be increased to 160 DEG C when Between be 1~3h.
CN201910373883.3A 2019-05-07 2019-05-07 Method for rapidly preparing short column-shaped calcium sulfate hemihydrate material by using calcium sulfate dihydrate Active CN110040991B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910373883.3A CN110040991B (en) 2019-05-07 2019-05-07 Method for rapidly preparing short column-shaped calcium sulfate hemihydrate material by using calcium sulfate dihydrate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910373883.3A CN110040991B (en) 2019-05-07 2019-05-07 Method for rapidly preparing short column-shaped calcium sulfate hemihydrate material by using calcium sulfate dihydrate

Publications (2)

Publication Number Publication Date
CN110040991A true CN110040991A (en) 2019-07-23
CN110040991B CN110040991B (en) 2020-04-07

Family

ID=67280953

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910373883.3A Active CN110040991B (en) 2019-05-07 2019-05-07 Method for rapidly preparing short column-shaped calcium sulfate hemihydrate material by using calcium sulfate dihydrate

Country Status (1)

Country Link
CN (1) CN110040991B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112299468A (en) * 2020-10-30 2021-02-02 山东聚鑫新材料有限公司 Flaky calcium sulfate crystal and preparation method thereof

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5261198A (en) * 1975-11-14 1977-05-20 Mitsubishi Chem Ind Ltd Process for production of prismatic alpha-type gypsum hemihydrate
JPS5299992A (en) * 1976-02-17 1977-08-22 Mitsubishi Chem Ind Ltd Production of alpha-type hemihydrate gypsum of prismatic crystal from phosphoric acid by-product dihydrate gypsum
CN1569642A (en) * 2004-04-20 2005-01-26 浙江大学 Process for preparing alpha-semi-hydrated gypsum from modified gypsum at normal pressure
CN102992375A (en) * 2011-09-15 2013-03-27 北京朗新明环保科技有限公司 Alpha type ultra-high strength gypsum preparation method
CN105174760A (en) * 2015-09-18 2015-12-23 金正大生态工程集团股份有限公司 Method for preparing alpha semi-hydrated gypsum from dihydrate gypsum
CN107399755A (en) * 2017-08-23 2017-11-28 河北工业大学 A kind of method that desulfurated plaster prepares high whiteness short cylinder αsemiwatergypsum
CN107721220A (en) * 2017-09-30 2018-02-23 中国科学院青海盐湖研究所 The preparation method of short cylinder αsemiwatergypsum
CN107973329A (en) * 2016-10-25 2018-05-01 北京化工大学 A kind of short prism-shaped α-half-H 2 O calcium sulphate raw powder's production technology

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5261198A (en) * 1975-11-14 1977-05-20 Mitsubishi Chem Ind Ltd Process for production of prismatic alpha-type gypsum hemihydrate
JPS5299992A (en) * 1976-02-17 1977-08-22 Mitsubishi Chem Ind Ltd Production of alpha-type hemihydrate gypsum of prismatic crystal from phosphoric acid by-product dihydrate gypsum
CN1569642A (en) * 2004-04-20 2005-01-26 浙江大学 Process for preparing alpha-semi-hydrated gypsum from modified gypsum at normal pressure
CN102992375A (en) * 2011-09-15 2013-03-27 北京朗新明环保科技有限公司 Alpha type ultra-high strength gypsum preparation method
CN105174760A (en) * 2015-09-18 2015-12-23 金正大生态工程集团股份有限公司 Method for preparing alpha semi-hydrated gypsum from dihydrate gypsum
CN107973329A (en) * 2016-10-25 2018-05-01 北京化工大学 A kind of short prism-shaped α-half-H 2 O calcium sulphate raw powder's production technology
CN107399755A (en) * 2017-08-23 2017-11-28 河北工业大学 A kind of method that desulfurated plaster prepares high whiteness short cylinder αsemiwatergypsum
CN107721220A (en) * 2017-09-30 2018-02-23 中国科学院青海盐湖研究所 The preparation method of short cylinder αsemiwatergypsum

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112299468A (en) * 2020-10-30 2021-02-02 山东聚鑫新材料有限公司 Flaky calcium sulfate crystal and preparation method thereof
CN112299468B (en) * 2020-10-30 2022-12-30 山东聚鑫新材料有限公司 Flaky calcium sulfate crystal and preparation method thereof

Also Published As

Publication number Publication date
CN110040991B (en) 2020-04-07

Similar Documents

Publication Publication Date Title
EP3351506B1 (en) Method for producing phosphoric acid and by-producing alpha-hemihydrate gypsum by wet-process
CN105174760B (en) A kind of method that dihydrate gypsum prepares αsemiwatergypsum
CN102617107B (en) Building silt soil non-sintered ceramic aggregate and preparation method thereof
CN102603219B (en) Process for preparing high-activity semi-hydrated gypsum cementing material and gypsum product by aid of phosphorous gypsum
CN103553492B (en) It is a kind of that with polyaluminium waste slag of aluminum and red mud, to be major ingredient non-burning brick and preparation method thereof
CN102424412B (en) Method of producing alumina from fly ash
CN103755322B (en) Low-silica iron ore tailings expanded ceramsite and preparation method thereof
CN105036691A (en) Method for preparing non-sintered ceramsite by adding dredged sludge
CN103964716B (en) The method of high-strength α-half water titanium gypsum is prepared with trade waste two water titanium gypsum
CN105130235A (en) Casing method of dredging sediment non-sintered ceramsites
CN103274616B (en) The method of phosphorus plaster of Paris produced by a kind of phosphogypsum
CN105985038B (en) A kind of water-fast and sulfate attack inorganic coagulation material and preparation method thereof
CN102219228A (en) Comprehensive modification method for attapulgite
CN107311588A (en) A kind of environmentally friendly brushing gypsum and preparation method thereof
CN106810094B (en) The system and method for cement joint production sulphur is prepared using municipal waste and Industrial Solid Waste
CN104671682A (en) Method for preparing hemihydrate gypsum gel material and gypsum products on line by using phosphogypsum at hot stage
CN101113083A (en) Method for modifying pre-processing titanium gypsum
CN104628412B (en) Utilize the method that hot vexed slag produces insulation blocks haydite
CN102603218A (en) Method for preparing high belite and sulphoaluminate cement clinker by aid of high-alumina fly ash
CN110040991A (en) A method of quickly preparing short cylinder sulfate hemihydrate calcium material using calcium sulphate dihydrate
CN103880318A (en) Cement grinding aid activation synergist by using marble powder, granite powder, limestone, desulfurization slag powder and papermaking white clay as composite materials
CN101492262A (en) Low-calcium silicate cement produced by using waste slag of aluminum and method of producing the same
CN108264318A (en) A kind of waterproof brushing gypsum and preparation method thereof
CN107445592A (en) A kind of multi-functional haydite and its production method that fluxing agent is made using pickling sludge
CN108585699A (en) A kind of building energy conservation brick and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant