WO2022036923A1 - Technological process for changing physical and chemical properties of new phosphogypsum by using calcium hydroxide - Google Patents

Technological process for changing physical and chemical properties of new phosphogypsum by using calcium hydroxide Download PDF

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WO2022036923A1
WO2022036923A1 PCT/CN2020/133196 CN2020133196W WO2022036923A1 WO 2022036923 A1 WO2022036923 A1 WO 2022036923A1 CN 2020133196 W CN2020133196 W CN 2020133196W WO 2022036923 A1 WO2022036923 A1 WO 2022036923A1
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calcium hydroxide
phosphogypsum
new
technological process
mass
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PCT/CN2020/133196
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French (fr)
Chinese (zh)
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李思言
李文广
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李思言
李文广
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    • 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
    • C04B28/00Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
    • C04B28/14Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing calcium sulfate cements
    • C04B28/142Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing calcium sulfate cements containing synthetic or waste calcium sulfate cements
    • C04B28/143Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing calcium sulfate cements containing synthetic or waste calcium sulfate cements the synthetic calcium sulfate being phosphogypsum
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/28Ammonium phosphates
    • 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
    • C04B40/00Processes, in general, for influencing or modifying the properties of mortars, concrete or artificial stone compositions, e.g. their setting or hardening ability
    • C04B40/04Preventing evaporation of the mixing water
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05BPHOSPHATIC FERTILISERS
    • C05B7/00Fertilisers based essentially on alkali or ammonium orthophosphates
    • 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
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00017Aspects relating to the protection of the environment

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  • the invention belongs to the technical field of new phosphogypsum treatment and utilization, and in particular relates to a technological process for changing the physicochemical properties of new phosphogypsum by using calcium hydroxide or calcium oxide, so as to convert the new phosphogypsum into a building gypsum product.
  • Food security is related to national security
  • phosphate fertilizer production is related to grain output
  • phosphogypsum the waste residue produced by phosphate fertilizer plants
  • Phosphogypsum is different from natural gypsum. Although its purity is as high as 90%, in addition to CaSO 4 ⁇ 2H 2 O, it also contains a small amount of undecomposed phosphate rock, unwashed acid phosphate, soluble fluoride, iron Compounds, aluminum compounds, acidic substances, organic substances and other harmful impurities that endanger human health and biological growth, and improper disposal will cause harm to the environment.
  • the chemical composition/% of phosphogypsum (dry basis) and natural gypsum in a certain place is shown in Table 1-1 and Table 1-2, and the main chemical composition/% of impurities in phosphogypsum samples in different regions is shown in Table 2.
  • the main hazards of phosphogypsum include: 1 water-soluble phosphorus-containing compounds and water-soluble fluorine-containing compounds enter rivers and oceans with precipitation, and some infiltrate into soil and groundwater bodies, causing pollution; 2 in dry climate conditions, the irritation generated by the volatilization of acidic substances Sexual odors and fines form air pollution.
  • the technical solution of the present invention is: a kind of technological process that calcium hydroxide changes the physical and chemical properties of new phosphogypsum, it is characterized in that comprising the following steps:
  • the water-soluble fluorine-containing particles (F - , HF, SiF 6 2- ) were removed with Ca(OH) 2 , and the water-soluble fluorine-containing particles completely existed in the gypsum in the form of CaF 2 as aggregates, thereby eliminating their pollution to the environment.
  • esters ethylene glycol methyl ether acetate (boiling point: 145 °C) , 760mmHg), methyl isothiocyanate (boiling point: 107.8 °C, 760mmHg)] and ethers [3-methoxy-n-pentane boiling point: (63.3 °C, 760mmHg)] and so on.
  • Esters undergo hydrolysis under alkaline conditions to form carboxylates and low-boiling ethers.
  • Ethers are very stable under alkaline conditions, and are easily oxidized to peroxides in the air.
  • the peroxides undergo disproportionation reactions under the catalysis of Fe 3+ to form low-boiling alcohols.
  • the boiling point of these organic substances is below 200°C, and they can be vaporized and removed by heating for recycling.
  • step (3) of the technical solution of the present invention an aspirator is arranged above the double-shaft mixer to recover and process the ammonia gas generated during the mixing and stirring process.
  • the device uses dilute phosphoric acid as an absorbent to convert ammonia gas into ammonium phosphate.
  • step (3) of the technical solution of the present invention the mass of the calcium hydroxide powder is 98-102% B, and the mass of the calcium oxide powder is 98-102% C.
  • the quality of the calcium hydroxide powder is B, and the quality of the calcium oxide powder is C.
  • the heating equipment is a frying pan, a rotary kiln, a boiling furnace or a pit mill.
  • the heating equipment is provided with a waste gas recovery and treatment device.
  • the waste gas recovery and treatment device is a waste gas recovery and treatment device that uses cold water as a trapping agent to cool, enrich and concentrate the organic mixture vapor.
  • the temperature of the material is measured by a temperature measuring device arranged in the material.
  • the invention is mainly used for processing new phosphogypsum into building gypsum products in situ.
  • Fig. 1 is the production process flow chart of phosphorus gypsum of construction of the present invention.
  • the above-mentioned uniformly mixed materials are added to the frying pan, heated so that the temperature of the materials in the frying pan rises to 260 °C, and then cooled to obtain plaster of paris powder; meanwhile, the waste gas generated during the heating process is enriched and recycled by cold water;
  • the modules stacked in the transfer field are covered with plastic film to prevent moisture from evaporating. After being placed at room temperature for 28 days, the plastic film is removed and air-dried in the air to obtain a building gypsum product.
  • the obtained building gypsum product was inspected by the main impurity content of the Experimental Test Center of the Eighth Geological Brigade of the Hubei Provincial Geological Bureau, and obtained the "Inspection Report” (MA 171716040411, report batch number: (2019) A19504), wherein, the main impurity content is shown in Table 5:
  • Hydration mix the prepared plaster of paris with water in a mass ratio of 100:40-50, stir, mold, vibrate, demould for 15-20 minutes, and stack in transfer field;
  • an aspirator is set above the double-shaft mixer to recover and process the ammonia gas generated during the mixing and stirring process.
  • the device uses dilute phosphoric acid as an absorbent to convert ammonia gas into ammonium phosphate.
  • the mass of the calcium hydroxide powder is 98-102% B, and the mass of the calcium oxide powder is 98-102% C.
  • the quality of the calcium hydroxide powder is B, and the quality of the calcium oxide powder is C.
  • the heating equipment is a frying pan, a rotary kiln, a boiling furnace or a pit mill.
  • the heating equipment is provided with an exhaust gas recovery and treatment device.
  • the waste gas recovery and treatment device is a waste gas recovery and treatment device that uses cold water as a trapping agent to cool and enrich the vapor of the organic mixture for centralized treatment.
  • the temperature of the material is measured by a temperature measuring device arranged in the material.
  • the present invention is mainly used for processing new phosphogypsum into building gypsum products in situ.
  • New phosphogypsum is a kind of solid waste that has just left the factory.
  • the principle of calcium hydroxide changing the physical and chemical properties of new phosphogypsum is: the harmful impurities in new phosphogypsum react with calcium hydroxide, and the direction and direction of each reaction are calculated according to the chemical principle.
  • the limit and the residual amount of harmful impurities after the reaction are determined to determine the feasibility of the process; then according to the theory of material structure, the new phosphogypsum is converted into high-quality building gypsum without aging by using an appropriate process.
  • the theoretical calculation results are in good agreement with the experimental measurement data.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)

Abstract

A technological process for changing physical and chemical properties of new phosphogypsum by using calcium hydroxide, relating to the technical field of new phosphogypsum treatment and utilization. In the present invention, an amount of calcium hydroxide is calculated according to a chemical principle and a substance structure theory; and by means of a proper technological process, waste residues produced from a phosphate fertilizer plant, i.e., the new phosphogypsum, are converted into building gypsum in situ without dam building and aging. The present invention is mainly characterized by comprising the following steps: (1) detecting content of water-soluble P2O5, P2O5 in crystals, water-soluble fluorine, Fe2O3, Al2O3, NH4 +, and MgO in the new phosphogypsum; (2) determining mass B of calcium hydroxide or mass C of calcium oxide; (3) uniformly mixing the new phosphogypsum with calcium hydroxide powder accounting for 90-105% of B or calcium oxide powder accounting for 90-105% of C; (4) heating to raise the temperature of the material to 220°C-270°C, and discharging to obtain calcined gypsum powder; (5) mixing the calcined gypsum powder and water according to a mass ratio of 100:(40-50), stirring, putting the mixture into a mold, vibrating, demolding, and transferring and stacking; and (6) curing: placing the obtained product at normal temperature for 28 days, and air-drying to obtain a building gypsum product.

Description

氢氧化钙改变新磷石膏理化性能的工艺流程Process flow of calcium hydroxide changing physical and chemical properties of new phosphogypsum 技术领域technical field
本发明属于新磷石膏处理利用技术领域,具体涉及一种采用氢氧化钙或氧化钙改变新磷石膏理化性能的工艺流程,将新磷石膏转化为建筑石膏产品。The invention belongs to the technical field of new phosphogypsum treatment and utilization, and in particular relates to a technological process for changing the physicochemical properties of new phosphogypsum by using calcium hydroxide or calcium oxide, so as to convert the new phosphogypsum into a building gypsum product.
背景技术Background technique
粮食安全关乎国泰民安,磷肥产量关乎粮食产量,而磷肥厂产生的废渣——磷石膏的合理利用关乎磷肥产业的可持续发展。Food security is related to national security, phosphate fertilizer production is related to grain output, and the rational use of phosphogypsum, the waste residue produced by phosphate fertilizer plants, is related to the sustainable development of the phosphate fertilizer industry.
目前,80%以上的磷酸都采用湿法磷酸二水法流程生产。湿法生产1t磷酸约排放4-5t(干基)磷石膏。At present, more than 80% of phosphoric acid is produced by wet phosphoric acid dihydrate process. Wet production of 1t phosphoric acid emits about 4-5t (dry basis) of phosphogypsum.
磷石膏不同于天然石膏,它的纯度虽高达90%以上,但除含CaSO 4·2H 2O外,还含有少量未分解的磷矿、未洗涤干净的酸式磷酸盐以及可溶性氟化物、铁化合物、铝化合物、酸性物质、有机质等多种危害人体健康及生物生长的有害杂质,处置不当将对环境造成危害。如某地磷石膏(干基)与天然石膏化学成份/%见表1-1、表1-2,不同地区磷石膏样品中杂质主要化学成分/%见表2。 Phosphogypsum is different from natural gypsum. Although its purity is as high as 90%, in addition to CaSO 4 ·2H 2 O, it also contains a small amount of undecomposed phosphate rock, unwashed acid phosphate, soluble fluoride, iron Compounds, aluminum compounds, acidic substances, organic substances and other harmful impurities that endanger human health and biological growth, and improper disposal will cause harm to the environment. For example, the chemical composition/% of phosphogypsum (dry basis) and natural gypsum in a certain place is shown in Table 1-1 and Table 1-2, and the main chemical composition/% of impurities in phosphogypsum samples in different regions is shown in Table 2.
表1-1Table 1-1
原料raw material MgOMgO CaOCaO Fe 2O 3 Fe 2 O 3 Al 2O 3 Al 2 O 3 SiO 2 SiO2 SO 3 SO 3 H 2O H 2 O
磷石膏Phosphogypsum 0.180.18 35.0335.03 1.031.03 1.161.16 10.2510.25 45.6845.68 31.931.9
天然石膏natural gypsum 1.301.30 31.231.2 1.351.35 1.731.73 4.84.8 41.141.1 16.816.8
表1-2Table 1-2
原料raw material 水溶性P 2O 5 Water-soluble P 2 O 5 晶体中P 2O 5 P 2 O 5 in the crystal 水溶性氟water-soluble fluorine 有机物organic matter pHpH
磷石膏Phosphogypsum 1.01.0 0.120.12 0.0440.044 0.120.12 2.62.6
天然石膏natural gypsum __ -- __ __ 6.76.7
表2Table 2
Figure PCTCN2020133196-appb-000001
Figure PCTCN2020133196-appb-000001
Figure PCTCN2020133196-appb-000002
Figure PCTCN2020133196-appb-000002
磷石膏的主要危害包括:①水溶性含磷化合物和水溶性含氟化合物随降水进入河流、海洋,有些渗入土壤和地下水体,造成污染;②在干燥的气候条件下,酸性物质挥发产生的刺激性气味和细粉形成空气污染。The main hazards of phosphogypsum include: ① water-soluble phosphorus-containing compounds and water-soluble fluorine-containing compounds enter rivers and oceans with precipitation, and some infiltrate into soil and groundwater bodies, causing pollution; ② in dry climate conditions, the irritation generated by the volatilization of acidic substances Sexual odors and fines form air pollution.
国务院办公厅关于印发“无废城市”建设试点工作方案的通知(国办[2018]128号),明确指出:严格控制增量,逐步解决工业固体废物历史遗留问题,以磷石膏等为重点,探索实施“以用定产”政策,实现固体废物产消平衡。The Notice of the General Office of the State Council on Printing and Distributing the Pilot Work Plan for the Construction of "Waste-Free Cities" (Guoban [2018] No. 128) clearly pointed out that: strictly control the increment, gradually solve the problems left over from the history of industrial solid waste, and focus on phosphogypsum, etc. Explore and implement the policy of "determining production by use" to achieve a balance between production and consumption of solid waste.
技术问题technical problem
目前,大型磷肥企业采用湿法排渣,在山谷筑坝堆放,建管道收集回水做循环使用。据不完全统计,目前国内堆存的磷石膏渣达到1亿多吨,每年还要新产生3000万吨左右的磷石膏渣,除去综合利用的约10%,其余磷石膏渣要作废弃堆放处理。堆存这些磷石膏渣不仅会占用大量土地,还造成污染,环保压力越来越大,成为磷肥产业生产和发展的制约因素之一。据测算,一个年产重钙(重过磷酸钙)80万吨项目,年排放磷石膏渣达186万吨,堆场投资估算达9000万元,堆场年经营费近1000万元,占地达70万平方米,相当于全厂占地的一半。从环保和技术安全角度看,磷石膏废渣堆存实非上策。新磷石膏需要建坝堆积陈放五年后才能使用;堆积陈化过程中,风吹日晒,尘土飞扬;雨水冲刷,污染水源;使用时,翻挖费工费钱。At present, large-scale phosphate fertilizer enterprises use wet slag discharge, build dams in valleys, and build pipelines to collect backwater for recycling. According to incomplete statistics, more than 100 million tons of phosphogypsum slag are currently stockpiled in China, and about 30 million tons of phosphogypsum slag will be newly generated every year. Except for about 10% of the comprehensive utilization, the rest of the phosphogypsum slag should be discarded and disposed of. . The piling up of these phosphogypsum slag will not only occupy a lot of land, but also cause pollution and increasing pressure on environmental protection, which has become one of the constraints on the production and development of the phosphate fertilizer industry. According to estimates, a project with an annual output of 800,000 tons of heavy calcium (heavy superphosphate) will discharge 1.86 million tons of phosphogypsum slag annually. The investment in the yard is estimated to be 90 million yuan, and the annual operating cost of the yard is nearly 10 million yuan. It reaches 700,000 square meters, which is equivalent to half of the entire factory. From the perspective of environmental protection and technical safety, the storage of phosphogypsum waste residues is not the best strategy. The new phosphogypsum needs to be built and accumulated for five years before it can be used; during the accumulation and aging process, the wind is blowing, the sun is blowing, and the dust is flying;
技术解决方案technical solutions
本发明的技术解决方案是:一种氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于包括以下步骤:The technical solution of the present invention is: a kind of technological process that calcium hydroxide changes the physical and chemical properties of new phosphogypsum, it is characterized in that comprising the following steps:
(1)新磷石膏相关成分含量检测:将质量为M的新磷石膏进行水溶性P 2O 5、晶体中P 2O 5、水溶性氟、Fe 2O 3、Al 2O 3、NH 4 +和MgO含量检测,分别得质量为A 1、A 2、A 3、A 4、A 5、A 6和A 7(1) Content detection of new phosphogypsum related components: The new phosphogypsum with mass of M was subjected to water-soluble P 2 O 5 , P 2 O 5 in crystals, water-soluble fluorine, Fe 2 O 3 , Al 2 O 3 , NH 4 + and MgO content detection, respectively obtain the quality of A 1 , A 2 , A 3 , A 4 , A 5 , A 6 and A 7 ;
(2)根据A 1、A 2、A 3、A 4、A 5、A 6和A 7分别与氢氧化钙或氧化钙的化学反应式计算,确定氢氧化钙质量B或氧化钙质量C: (2) Calculate according to the chemical reaction formulas of A 1 , A 2 , A 3 , A 4 , A 5 , A 6 and A 7 with calcium hydroxide or calcium oxide respectively, and determine the calcium hydroxide mass B or calcium oxide mass C:
B=1.56A 1+0.52A 2+1.95A 3+1.39A 4+2.18A 5+2.06A 6+1.85A 7B=1.56A 1 +0.52A 2 +1.95A 3 +1.39A 4 +2.18A 5 +2.06A 6 +1.85A 7 ;
C=1.18A 1+0.39A 2+1.47A 3+1.05A 4+1.65A 5+1.56A 6+1.40A 7C=1.18A 1 +0.39A 2 +1.47A 3 +1.05A 4 +1.65A 5 +1.56A 6 +1.40A 7 ;
(3)混合均匀:将质量为M的新磷石膏与质量为90~105%B的氢氧化钙粉末或质量为90~105%C的氧化钙粉末加入双轴搅拌机内强制混合均匀;(3) Mix evenly: add the new phosphogypsum with mass M and calcium hydroxide powder with mass of 90-105% B or calcium oxide powder with mass of 90-105% C into the twin-shaft mixer for forced mixing;
(4)加热:将上述混合均匀的物料加入加热设备中,物料温度升至220℃~270℃出炉,得到熟石膏粉;此熟石膏粉力学性能达到中华人民共和国国家标准GB/T9776-2008建筑石膏物理力学性能3.0要求;(4) Heating: add the above-mentioned uniformly mixed material into the heating equipment, and the temperature of the material rises to 220 ℃ ~ 270 ℃ to obtain plaster of paris powder; the mechanical properties of this plaster of paris powder reach the national standard of the People's Republic of China GB/T9776-2008 building Gypsum physical and mechanical properties 3.0 requirements;
(5)水化:将制得的熟石膏粉与水按质量比100:40~50混合,搅拌,装 模,振动,15~20分钟脱模,转场堆放;(5) hydration: the obtained plaster of paris and water are mixed by mass ratio of 100:40~50, stirred, moulded, vibrated, demoulded in 15~20 minutes, and stacked in transition;
(6)养护:将转场堆放的模块用塑料薄膜覆盖,防止水分蒸发,常温放置28天后可撤去塑料薄膜,在空气中风干,得到建筑石膏产品。(6) Maintenance: Cover the modules stacked in the transfer field with plastic film to prevent water evaporation. After 28 days at room temperature, the plastic film can be removed, and air-dried in the air to obtain a building gypsum product.
用Ca(OH) 2除去水溶性含氟粒子(F -、HF、SiF 6 2-),水溶性含氟粒子完全以CaF 2形体作为集料存在于石膏中,从而消除其对环境的污染。 The water-soluble fluorine-containing particles (F - , HF, SiF 6 2- ) were removed with Ca(OH) 2 , and the water-soluble fluorine-containing particles completely existed in the gypsum in the form of CaF 2 as aggregates, thereby eliminating their pollution to the environment.
用Ca(OH) 2除去水溶性P 2O 5(水溶性PO 4 3-、水溶性HPO 4 2-、水溶性H 2PO 4 -、H 3PO 4),水溶性P 2O 5以Ca 3(PO 4) 2形体作为集料存在于石膏中,从而消除其对石膏产品pH及强度的影响。 Use Ca(OH) 2 to remove water-soluble P 2 O 5 (water-soluble PO 4 3- , water-soluble HPO 4 2- , water-soluble H 2 PO 4 - , H 3 PO 4 ), water-soluble P 2 O 5 with Ca The 3 (PO 4 ) 2 form exists in the gypsum as an aggregate, thereby eliminating its influence on the pH and strength of the gypsum product.
用Ca(OH) 2除去Ca SO 4·2H 2O晶体中的P 2O 5(CaHPO 4·2H 2O),在炒制或锻烧过程中有一部分CaHPO 4·2H 2O从晶格中释放出来,在水化过程中又有一部分CaHPO 4·2H 2O从晶格中释放出来,释放出来CaHPO 4·2H 2O与Ca(OH) 2反应生成难溶物Ca 3(PO 4) 2和H 2O。当熟石膏水化时,由于C(H +)很低(10 -7mol·L -1),PO 4 3-不能与H +重新结合生成CaHPO 4·2H 2O进入CaSO 4·2H 2O晶体中,只能以Ca 3(PO 4) 2形体作为集料存在于石膏中,从而消除其对石膏产品pH及强度的影响。 Removal of P 2 O 5 (CaHPO 4 2H 2 O) in CaSO 4 .2H 2 O crystals with Ca(OH) 2 , a portion of CaHPO 4 .2H 2 O from the lattice during frying or calcining During the hydration process, a part of CaHPO 4 ·2H 2 O is released from the lattice, and the released CaHPO 4 ·2H 2 O reacts with Ca(OH) 2 to form insoluble Ca 3 (PO 4 ) 2 and H 2 O. When plaster of paris is hydrated, due to the very low C(H + ) (10 -7 mol·L -1 ), PO 4 3- cannot recombine with H + to form CaHPO 4 ·2H 2 O into CaSO 4 ·2H 2 O Among the crystals, only Ca 3 (PO 4 ) 2 forms exist in gypsum as aggregates, thereby eliminating its influence on pH and strength of gypsum products.
用Ca(OH) 2除去水溶性Fe 3+,充分搅拌,加热,就可使Fe 3+转化为集料(Fe 2O 3),防止它们覆盖在硫酸钙晶体表面,形成包膜。 Use Ca(OH) 2 to remove water-soluble Fe 3+ , stir well, and heat to convert Fe 3+ into aggregates (Fe 2 O 3 ), preventing them from covering the surface of calcium sulfate crystals and forming a coating.
用Ca(OH) 2除去水溶性Al 3+,充分搅拌,加热,就可使Al 3+转化为集料(Al 2O 3),防止它们覆盖在硫酸钙晶体表面,形成包膜,阻碍其溶解或结晶。 Use Ca(OH) 2 to remove water-soluble Al 3+ , stir well, and heat to convert Al 3+ into aggregates (Al 2 O 3 ), preventing them from covering the surface of calcium sulfate crystals, forming a coating and hindering its dissolve or crystallize.
用Ca(OH) 2除去水溶性Mg 2+,产品在空气中露置时,发生如下反应:Mg 2++2OH -+CO 2=MgCO 3↓+H 2O,Mg 2+变为集料(MgCO 3),不影响硫酸钙的性质。 Use Ca(OH) 2 to remove water-soluble Mg 2+ , when the product is exposed in the air, the following reaction occurs: Mg 2+ +2OH - +CO 2 =MgCO 3 ↓+H 2 O, Mg 2+ becomes aggregate (MgCO 3 ), does not affect the properties of calcium sulfate.
用Ca(OH) 2除去NH 4 +,在加热条件下,NH 4 +与Ca(OH) 2生成NH 3,可回收处理。 Use Ca(OH) 2 to remove NH 4 + . Under heating conditions, NH 4 + and Ca(OH) 2 generate NH 3 , which can be recycled.
用Ca(OH) 2与有机物的反应,有机物来源于磷矿石中的有机物和各生产工艺中所加入的有机物添加剂,主要为酯类物质[乙二醇甲醚乙酸酯(沸点:145℃,760mmHg)、异硫氰酸甲酯(沸点:107.8℃,760mmHg)]和醚类[3-甲氧基正戊烷沸点:(63.3℃,760mmHg)]等。酯类物质在碱性条件下发生水解反应生成羧酸盐和低沸点的醚。醚类物质在碱性条件下很稳定,在空气中易被氧化为过氧化物,过氧化物在Fe 3+催化作用下发生歧化反应,生成低沸点的醇。这些有机物的沸点在200℃以下,加热可汽化除去,回收处理。 The reaction between Ca(OH) 2 and organic matter, the organic matter comes from the organic matter in the phosphate rock and the organic matter additives added in each production process, mainly esters [ethylene glycol methyl ether acetate (boiling point: 145 ℃) , 760mmHg), methyl isothiocyanate (boiling point: 107.8 ℃, 760mmHg)] and ethers [3-methoxy-n-pentane boiling point: (63.3 ℃, 760mmHg)] and so on. Esters undergo hydrolysis under alkaline conditions to form carboxylates and low-boiling ethers. Ethers are very stable under alkaline conditions, and are easily oxidized to peroxides in the air. The peroxides undergo disproportionation reactions under the catalysis of Fe 3+ to form low-boiling alcohols. The boiling point of these organic substances is below 200°C, and they can be vaporized and removed by heating for recycling.
本发明的技术解决方案的第(3)步骤中,在所述的双轴搅拌机上方设置吸气机,将混合搅拌过程产生的氨气回收处理。该装置以稀磷酸为吸收剂,将氨气转化为磷酸铵。In step (3) of the technical solution of the present invention, an aspirator is arranged above the double-shaft mixer to recover and process the ammonia gas generated during the mixing and stirring process. The device uses dilute phosphoric acid as an absorbent to convert ammonia gas into ammonium phosphate.
本发明的技术解决方案中第(3)步骤中,所述的氢氧化钙粉末质量为98~102%B,氧化钙粉末的质量为98~102%C。In step (3) of the technical solution of the present invention, the mass of the calcium hydroxide powder is 98-102% B, and the mass of the calcium oxide powder is 98-102% C.
本发明的技术解决方案中第(3)步骤中,所述的氢氧化钙粉末质量为B,氧化钙粉末的质量为C。In the step (3) of the technical solution of the present invention, the quality of the calcium hydroxide powder is B, and the quality of the calcium oxide powder is C.
本发明的技术解决方案中第(3)步骤中,所述的氢氧化钙粉末或氧化钙粉末的加入量以使建筑石膏产品pH=6~7为准。In step (3) of the technical solution of the present invention, the added amount of the calcium hydroxide powder or calcium oxide powder is based on the pH=6-7 of the plaster of Paris product.
本发明的技术解决方案的第(4)步骤中,所述的加热设备为炒锅、回转窑、沸腾炉或彼特磨。In step (4) of the technical solution of the present invention, the heating equipment is a frying pan, a rotary kiln, a boiling furnace or a pit mill.
本发明的技术解决方案的第(4)步骤中,所述的加热设备设置有废气回收处理装置。In the step (4) of the technical solution of the present invention, the heating equipment is provided with a waste gas recovery and treatment device.
本发明的技术解决方案的第(4)步骤中,所述的废气回收处理装置为通过以冷水为捕集剂,将有机混合物蒸汽冷却、富集,集中处理的废气回收处理装置。In step (4) of the technical solution of the present invention, the waste gas recovery and treatment device is a waste gas recovery and treatment device that uses cold water as a trapping agent to cool, enrich and concentrate the organic mixture vapor.
本发明的技术解决方案中第(4)步骤中,所述的物料温度是通过设置在物料内的测温装置测出的。In the step (4) of the technical solution of the present invention, the temperature of the material is measured by a temperature measuring device arranged in the material.
有益效果beneficial effect
1、直接用新磷石膏作原料:将磷肥厂产生的废渣---新磷石膏不经陈化,转化为优质建筑石膏产品,为磷肥厂可持续发展创造条件,增加新的经济增长点;为保护石膏矿产资源,倡导绿色化学,建设无废城市贡献力量;1. Directly use new phosphogypsum as raw material: convert the waste residue produced by the phosphate fertilizer plant---new phosphogypsum into high-quality building gypsum products without aging, creating conditions for the sustainable development of the phosphate fertilizer plant and adding new economic growth points; Contribute to protecting gypsum mineral resources, advocating green chemistry, and building a waste-free city;
2、可与磷肥厂的排渣口接驳,不建堆场;2. It can be connected with the slag discharge port of the phosphate fertilizer plant without building a yard;
3、工艺流程简单:混合——加热——水化——养护,常压操作;3. The technological process is simple: mixing - heating - hydration - maintenance, normal pressure operation;
4、原料配比准确:针对不同产地的新磷石膏,根据新磷石膏化学成分检验报告,计算出新磷石膏质量与氢氧化钙质量比(或新磷石膏质量与氧化钙质量比)。适量的氢氧化钙(氧化钙),可将新磷石膏中有害杂质完全转化为难溶物,该难溶物作为集料留存在产品中,不需要除去。产品对环境友好,pH=6~7,可与天然石膏比美;4. Accurate ratio of raw materials: For new phosphogypsum from different origins, according to the chemical composition inspection report of new phosphogypsum, calculate the mass ratio of new phosphogypsum to calcium hydroxide (or the mass ratio of new phosphogypsum to calcium oxide). An appropriate amount of calcium hydroxide (calcium oxide) can completely convert harmful impurities in new phosphogypsum into insoluble substances, which remain in the product as aggregates and do not need to be removed. The product is environmentally friendly, with pH=6~7, which can be compared with natural gypsum;
5、力学性能达到中华人民共和国国家标准GB/T9776-2008建筑石膏物理力学性能3.0要求。5. The mechanical properties meet the requirements of the National Standard of the People's Republic of China GB/T9776-2008 Building Gypsum Physical and Mechanical Properties 3.0.
本发明主要用于将新磷石膏就地加工成建筑石膏产品。The invention is mainly used for processing new phosphogypsum into building gypsum products in situ.
附图说明Description of drawings
图1为本发明磷建筑石膏生产工艺流程图。Fig. 1 is the production process flow chart of phosphorus gypsum of construction of the present invention.
本发明的最佳实施方式BEST MODE FOR CARRYING OUT THE INVENTION
实施例1:Example 1:
某厂新磷石膏样品化学成分/%见表3-1、表3-2。See Table 3-1 and Table 3-2 for chemical composition/% of new phosphogypsum samples from a factory.
表3-1Table 3-1
Figure PCTCN2020133196-appb-000003
Figure PCTCN2020133196-appb-000003
表3-2Table 3-2
Figure PCTCN2020133196-appb-000004
Figure PCTCN2020133196-appb-000004
1、计量:1. Measurement:
根据表3-1、表3-2,水溶性P 2O 5、晶体中P 2O 5、水溶性氟、Fe 2O 3、Al 2O 3、NH 4 +和MgO的含量分别为A 1=1.56M%、A 2=0.12M%、A 3=0.044M%、A 4=0.70M%、A 5=0.79M%、A 6=0.0004M%和A 7=0.12M%,M为某厂新磷石膏样品质量; According to Table 3-1 and Table 3-2, the contents of water-soluble P 2 O 5 , P 2 O 5 in crystals, water-soluble fluorine, Fe 2 O 3 , Al 2 O 3 , NH 4 + and MgO are respectively A 1 = 1.56M %, A2 = 0.12M%, A3= 0.044M %, A4=0.70M%, A5= 0.79M %, A6= 0.0004M % and A7 =0.12M%, M is a certain The quality of the new phosphogypsum samples from the factory;
根据B=1.56A 1+0.52A 2+1.95A 3+1.39A 4+2.18A 5+2.06A 6+1.85A 7,确定氢氧化钙质量B=4.6M%; According to B=1.56A 1 +0.52A 2 +1.95A 3 +1.39A 4 +2.18A 5 +2.06A 6 +1.85A 7 , determine the calcium hydroxide mass B=4.6M%;
根据C=1.18A 1+0.39A 2+1.47A 3+1.05A 4+1.65A 5+1.56A 6+1.40A 7,确定氧化钙质量C=3.5M%;(氧化钙与水反应生成氢氧化钙); According to C=1.18A 1 +0.39A 2 +1.47A 3 +1.05A 4 +1.65A 5 +1.56A 6 +1.40A 7 , determine the quality of calcium oxide C=3.5M%; (calcium oxide reacts with water to generate hydroxide calcium);
若氢氧化钙或氧化钙过量,增加成本,产品呈强碱性;氢氧化钙或氧化钙不足,达不到完全除去有害杂质之目的;If calcium hydroxide or calcium oxide is excessive, the cost will be increased, and the product will be strongly alkaline; if calcium hydroxide or calcium oxide is insufficient, the purpose of completely removing harmful impurities cannot be achieved;
2、混合搅拌:2. Mix and stir:
分别通过计量装置将新磷石膏(湿基)与氢氧化钙粉末按100:4.6的质量比,或者将新磷石膏(湿基)与氧化钙粉末按100:3.5的质量比加入搅拌机内进行强制混合均匀;同时开启双轴搅拌机上方设置的吸气机,将混合搅拌过程中由NH 4 +转化产生的氨气回收处理; Add new phosphogypsum (wet base) and calcium hydroxide powder in a mass ratio of 100:4.6 through a metering device, or add new phosphogypsum (wet base) and calcium oxide powder in a mass ratio of 100:3.5 into the mixer for forced Mix evenly; at the same time, turn on the aspirator set above the double-shaft mixer to recover and process the ammonia gas produced by the conversion of NH 4 + during the mixing and stirring process;
3、加热:3. Heating:
将上述混合均匀的物料加入炒锅中,加热使炒锅中物料温度升至260℃出炉,冷却,得熟石膏粉;同时将加热过程中产生的废气通过冷水富集回收处理;The above-mentioned uniformly mixed materials are added to the frying pan, heated so that the temperature of the materials in the frying pan rises to 260 ℃, and then cooled to obtain plaster of paris powder; meanwhile, the waste gas generated during the heating process is enriched and recycled by cold water;
4、水化:4. Hydration:
将制得的熟石膏粉与水按质量比100:45混合,搅拌,装模,振动,15分钟脱模,转场堆放;Mix the prepared plaster of paris powder with water in a mass ratio of 100:45, stir, mold, vibrate, demould for 15 minutes, and stack in transfer field;
5、养护:5. Maintenance:
将转场堆放的模块用塑料薄膜覆盖,防止水分蒸发,常温放置28天后撤去塑料薄膜,在空气中风干,得到建筑石膏产品。The modules stacked in the transfer field are covered with plastic film to prevent moisture from evaporating. After being placed at room temperature for 28 days, the plastic film is removed and air-dried in the air to obtain a building gypsum product.
所得建筑石膏产品测试结果:The obtained plaster of Paris product test results:
所得建筑石膏产品经湖北省地质局第八地质大队实验测试中心物理力学试验,得《物理力学试验报告》(MA 171716040411,试验批号:B191015),其中,物理力学性能见表4:The obtained building gypsum product was subjected to physical and mechanical tests by the Experimental Testing Center of the Eighth Geological Brigade of Hubei Provincial Geological Bureau, and obtained the "Physical and Mechanical Test Report" (MA 171716040411, test batch number: B191015), wherein the physical and mechanical properties are shown in Table 4:
表4Table 4
Figure PCTCN2020133196-appb-000005
Figure PCTCN2020133196-appb-000005
所得建筑石膏产品经湖北省地质局第八地质大队实验测试中心主要杂质含量检验,得《检验报告》(MA 171716040411,报告批号:(2019年)A19504号),其中,主要杂质含量见表5:The obtained building gypsum product was inspected by the main impurity content of the Experimental Test Center of the Eighth Geological Brigade of the Hubei Provincial Geological Bureau, and obtained the "Inspection Report" (MA 171716040411, report batch number: (2019) A19504), wherein, the main impurity content is shown in Table 5:
表5table 5
Figure PCTCN2020133196-appb-000006
Figure PCTCN2020133196-appb-000006
以上测试结果表明,所得建筑石膏产品力学性能达到中华人民共和国国家标准GB/T9776-2008建筑石膏物理力学性能3.0要求。The above test results show that the mechanical properties of the obtained building gypsum products meet the requirements of the National Standard of the People's Republic of China GB/T9776-2008 building gypsum physical and mechanical properties 3.0.
本发明的实施方式Embodiments of the present invention
氢氧化钙改变新磷石膏理化性能的工艺流程实施方式,包括以下步骤:The technical process embodiment of calcium hydroxide changing the physical and chemical properties of new phosphogypsum includes the following steps:
(1)新磷石膏相关成分含量检测:将质量为M的新磷石膏进行水溶性P 2O 5、晶体中P 2O 5、水溶性氟、Fe 2O 3、Al 2O 3、NH 4 +和MgO含量检测,分别得质量为A 1、A 2、A 3、A 4、A 5、A 6和A 7(1) Content detection of new phosphogypsum related components: The new phosphogypsum with mass of M was subjected to water-soluble P 2 O 5 , P 2 O 5 in crystals, water-soluble fluorine, Fe 2 O 3 , Al 2 O 3 , NH 4 + and MgO content detection, respectively obtain the quality of A 1 , A 2 , A 3 , A 4 , A 5 , A 6 and A 7 ;
(2)计算:根据A 1、A 2、A 3、A 4、A 5、A 6和A 7分别与氢氧化钙或氧化钙的化学反应式计算,确定氢氧化钙质量B或氧化钙质量C: (2) Calculation: Calculate according to the chemical reaction formula of A 1 , A 2 , A 3 , A 4 , A 5 , A 6 and A 7 with calcium hydroxide or calcium oxide respectively, and determine the calcium hydroxide mass B or calcium oxide mass C:
B=1.56A 1+0.52A 2+1.95A 3+1.39A 4+2.18A 5+2.06A 6+1.85A 7B=1.56A 1 +0.52A 2 +1.95A 3 +1.39A 4 +2.18A 5 +2.06A 6 +1.85A 7 ;
C=1.18A 1+0.39A 2+1.47A 3+1.05A 4+1.65A 5+1.56A 6+1.40A 7C=1.18A 1 +0.39A 2 +1.47A 3 +1.05A 4 +1.65A 5 +1.56A 6 +1.40A 7 ;
(3)混合均匀:将质量为M的新磷石膏与质量为90~105%B的氢氧化钙粉末或质量为90~105%C的氧化钙粉末加入双轴搅拌机内强制混合均匀;(3) Mix evenly: add the new phosphogypsum with mass M and calcium hydroxide powder with mass of 90-105% B or calcium oxide powder with mass of 90-105% C into the twin-shaft mixer for forced mixing;
(4)加热:将上述混合均匀的物料加入加热设备中,物料温度升至220℃~270℃出炉,得到熟石膏粉;此熟石膏粉力学性能达到中华人民共和国国家标准GB/T9776-2008建筑石膏物理力学性能3.0要求;(4) Heating: add the above-mentioned uniformly mixed material into the heating equipment, and the temperature of the material rises to 220 ℃ ~ 270 ℃ to obtain plaster of paris powder; the mechanical properties of this plaster of paris powder reach the national standard of the People's Republic of China GB/T9776-2008 building Gypsum physical and mechanical properties 3.0 requirements;
(5)水化:将制得的熟石膏粉与水按质量比100:40~50混合,搅拌,装模,振动,15~20分钟脱模,转场堆放;(5) Hydration: mix the prepared plaster of paris with water in a mass ratio of 100:40-50, stir, mold, vibrate, demould for 15-20 minutes, and stack in transfer field;
(6)养护:将转场堆放的模块用塑料薄膜覆盖,防止水分蒸发,常温放置 28天后可撤去塑料薄膜,在空气中风干,得到建筑石膏产品。(6) Conservation: Cover the modules stacked in the transfer field with plastic film to prevent moisture from evaporating. After 28 days at room temperature, the plastic film can be removed, and air-dried in the air to obtain a building gypsum product.
实施方式第(3)步骤中,在所述的双轴搅拌机上方设置吸气机,将混合搅拌过程产生的氨气回收处理。该装置以稀磷酸为吸收剂,将氨气转化为磷酸铵。In step (3) of the embodiment, an aspirator is set above the double-shaft mixer to recover and process the ammonia gas generated during the mixing and stirring process. The device uses dilute phosphoric acid as an absorbent to convert ammonia gas into ammonium phosphate.
实施方式第(3)步骤中,所述的氢氧化钙粉末质量为98~102%B,氧化钙粉末的质量为98~102%C。In the step (3) of the embodiment, the mass of the calcium hydroxide powder is 98-102% B, and the mass of the calcium oxide powder is 98-102% C.
实施方式第(3)步骤中,所述的氢氧化钙粉末质量为B,氧化钙粉末的质量为C。In the step (3) of the embodiment, the quality of the calcium hydroxide powder is B, and the quality of the calcium oxide powder is C.
实施方式第(3)步骤中,所述的氢氧化钙粉末或氧化钙粉末的加入量以使建筑石膏产品pH=6~7为准。In the step (3) of the embodiment, the added amount of the calcium hydroxide powder or calcium oxide powder is based on the pH=6-7 of the plaster of Paris product.
实施方式第(4)步骤中,所述的加热设备为炒锅、回转窑、沸腾炉或彼特磨。In the step (4) of the embodiment, the heating equipment is a frying pan, a rotary kiln, a boiling furnace or a pit mill.
实施方式第(4)步骤中,所述的加热设备设置有废气回收处理装置。In the step (4) of the embodiment, the heating equipment is provided with an exhaust gas recovery and treatment device.
实施方式第(4)步骤中,所述的废气回收处理装置为通过以冷水为捕集剂,将有机混合物蒸汽冷却、富集,集中处理的废气回收处理装置。In the step (4) of the embodiment, the waste gas recovery and treatment device is a waste gas recovery and treatment device that uses cold water as a trapping agent to cool and enrich the vapor of the organic mixture for centralized treatment.
实施方式第(4)步骤中,所述的物料温度是通过设置在物料内的测温装置测出的。In the step (4) of the embodiment, the temperature of the material is measured by a temperature measuring device arranged in the material.
工业实用性Industrial Applicability
1、直接用新磷石膏和氢氧化钙(或氧化钙)作原料:将磷肥厂产生的废渣---新磷石膏不经陈化,转化为优质建筑石膏产品,为磷肥厂可持续发展创造条件,增加新的经济增长点;为保护石膏矿产资源,倡导绿色化学,建设无废城市贡献力量;1. Directly use new phosphogypsum and calcium hydroxide (or calcium oxide) as raw materials: convert the waste residue produced by the phosphate fertilizer plant---new phosphogypsum into high-quality building gypsum products without aging, creating a sustainable development for the phosphate fertilizer plant. conditions, and increase new economic growth points; contribute to the protection of gypsum mineral resources, the promotion of green chemistry, and the construction of a waste-free city;
2、可与磷肥厂的排渣口接驳,不建磷石膏堆场;2. It can be connected with the slag discharge port of the phosphate fertilizer plant, and no phosphogypsum storage yard will be built;
3、工艺流程简单:混合——加热——水化——养护,常压操作;3. The process is simple: mixing - heating - hydration - maintenance, normal pressure operation;
4、原料配比准确:针对不同产地的新磷石膏,根据新磷石膏化学成分检验报告,计算出新磷石膏质量与氢氧化钙质量比(或新磷石膏质量与氧化钙质量比)。适量的氢氧化钙(氧化钙),可将新磷石膏中有害杂质完全转化为难溶物,该难溶物作为集料留存在产品中,不需要除去。产品对环境友好,pH=6~7,可与天然石膏比美;4. Accurate ratio of raw materials: For new phosphogypsum from different origins, according to the chemical composition inspection report of new phosphogypsum, calculate the mass ratio of new phosphogypsum to calcium hydroxide (or the mass ratio of new phosphogypsum to calcium oxide). An appropriate amount of calcium hydroxide (calcium oxide) can completely convert harmful impurities in new phosphogypsum into insoluble substances, which remain in the product as aggregates and do not need to be removed. The product is environmentally friendly, with pH=6~7, which can be compared with natural gypsum;
5、力学性能达到中华人民共和国国家标准GB/T9776-2008建筑石膏物理力学性能3.0要求。5. The mechanical properties meet the requirements of the National Standard of the People's Republic of China GB/T9776-2008 Building Gypsum Physical and Mechanical Properties 3.0.
本发明主要用于将新磷石膏就地加工成建筑石膏产品。The present invention is mainly used for processing new phosphogypsum into building gypsum products in situ.
序列表自由内容Sequence Listing Free Content
新磷石膏是磷肥厂刚出厂的一种固体废渣,氢氧化钙改变新磷石膏理化性能的原理是:新磷石膏中的有害杂质与氢氧化钙反应,根据化学原理计算各反应进行的方向和限度及其反应后有害杂的残留量,以此确定工艺流程的可行性;再根据物质结构理论,采用适当的工艺流程将新磷石膏不经陈化,转 化为优质建筑石膏。理论计算结果与实验测量数据符合的很好。New phosphogypsum is a kind of solid waste that has just left the factory. The principle of calcium hydroxide changing the physical and chemical properties of new phosphogypsum is: the harmful impurities in new phosphogypsum react with calcium hydroxide, and the direction and direction of each reaction are calculated according to the chemical principle. The limit and the residual amount of harmful impurities after the reaction are determined to determine the feasibility of the process; then according to the theory of material structure, the new phosphogypsum is converted into high-quality building gypsum without aging by using an appropriate process. The theoretical calculation results are in good agreement with the experimental measurement data.

Claims (9)

  1. 一种氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于包括以下步骤:A kind of technological process that calcium hydroxide changes the physical and chemical properties of new phosphogypsum, it is characterized in that comprising the following steps:
    (1)新磷石膏相关成分含量检测:将质量为M的新磷石膏进行水溶性P 2O 5、晶体中P 2O 5、水溶性氟、Fe 2O 3、Al 2O 3、NH 4 +和MgO含量检测,分别得质量为A 1、A 2、A 3、A 4、A 5、A 6和A 7(1) Content detection of new phosphogypsum related components: The new phosphogypsum with mass of M was subjected to water-soluble P 2 O 5 , P 2 O 5 in crystals, water-soluble fluorine, Fe 2 O 3 , Al 2 O 3 , NH 4 + and MgO content detection, respectively obtain the quality of A 1 , A 2 , A 3 , A 4 , A 5 , A 6 and A 7 ;
    (2)根据A 1、A 2、A 3、A 4、A 5、A 6和A 7分别与氢氧化钙或氧化钙的化学反应式计算,确定氢氧化钙质量B或氧化钙质量C: (2) Calculate according to the chemical reaction formulas of A 1 , A 2 , A 3 , A 4 , A 5 , A 6 and A 7 with calcium hydroxide or calcium oxide respectively, and determine the calcium hydroxide mass B or calcium oxide mass C:
    B=1.56A 1+0.52A 2+1.95A 3+1.39A 4+2.18A 5+2.06A 6+1.85A 7B=1.56A 1 +0.52A 2 +1.95A 3 +1.39A 4 +2.18A 5 +2.06A 6 +1.85A 7 ;
    C=1.18A 1+0.39A 2+1.47A 3+1.05A 4+1.65A 5+1.56A 6+1.40A 7C=1.18A 1 +0.39A 2 +1.47A 3 +1.05A 4 +1.65A 5 +1.56A 6 +1.40A 7 ;
    (3)混合均匀:将质量为M的新磷石膏与质量为90~105%B的氢氧化钙粉末或质量为90~105%C的氧化钙粉末加入双轴搅拌机内强制混合均匀;(3) Mix evenly: add the new phosphogypsum with mass M and calcium hydroxide powder with mass of 90-105% B or calcium oxide powder with mass of 90-105% C into the twin-shaft mixer for forced mixing;
    (4)加热:将上述混合均匀的物料加入加热设备中,物料温度升至220℃~270℃出炉,得到熟石膏粉;(4) Heating: adding the above-mentioned uniformly mixed material into the heating equipment, the temperature of the material rises to 220 ℃~270 ℃ and is released, and obtains plaster of paris;
    (5)水化:将制得的熟石膏粉与水按质量比100:40~50混合,搅拌,装模,振动,15~20分钟脱模,转场堆放;(5) Hydration: mix the prepared plaster of paris with water in a mass ratio of 100:40-50, stir, mold, vibrate, demould for 15-20 minutes, and stack in transfer field;
    (6)养护:将转场堆放的模块用塑料薄膜覆盖,防止水分蒸发,常温放置28天后可撤去塑料薄膜,在空气中风干,得到建筑石膏产品。(6) Conservation: Cover the modules stacked in the transfer field with plastic film to prevent water evaporation. After being placed at room temperature for 28 days, the plastic film can be removed, and air-dried in the air to obtain a building gypsum product.
  2. 根据权利要求1所述的氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于:第(3)步骤中,在所述的双轴搅拌机上方设置吸气机,将混合搅拌过程产生的氨气回收处理。The technological process that calcium hydroxide changes the physicochemical properties of new phosphogypsum according to claim 1, it is characterized in that: in the (3) step, an aspirator is set above the described biaxial mixer, and the Ammonia gas recycling.
  3. 根据权利要求1或2所述的氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于:第(4)步骤中,所述的加热设备为炒锅、回转窑、沸腾炉或彼特磨。The technological process that calcium hydroxide according to claim 1 and 2 changes the physical and chemical properties of new phosphogypsum, it is characterized in that: in the (4) step, the described heating equipment is a frying pan, a rotary kiln, a boiling furnace or a peter mill .
  4. 根据权利要求1或2所述的氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于:第(4)步骤中,所述的加热设备设置有废气回收处理装置。The technological process of changing the physical and chemical properties of new phosphogypsum by calcium hydroxide according to claim 1 or 2 is characterized in that: in step (4), the heating equipment is provided with a waste gas recovery and treatment device.
  5. 根据权利要求4所述的氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于:所述的废气回收处理装置为通过以冷水为捕集剂,将有机混合物蒸汽冷却、富集,集中处理的废气回收处理装置。The technological process of changing the physical and chemical properties of new phosphogypsum by calcium hydroxide according to claim 4, characterized in that: the waste gas recovery and treatment device cools, enriches, and concentrates the organic mixture steam by using cold water as a collector. Treated exhaust gas recovery and treatment device.
  6. 根据权利要求1或2所述的氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于:第(3)步骤中,所述的氢氧化钙粉末质量为98~102%B,氧化钙粉末的质量为98~102%C。The technological process of changing the physical and chemical properties of new phosphogypsum by calcium hydroxide according to claim 1 or 2, is characterized in that: in step (3), the quality of the calcium hydroxide powder is 98-102% B, calcium oxide The mass of the powder is 98-102%C.
  7. 根据权利要求1或2所述的氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于:第(3)步骤中,所述的氢氧化钙粉末质量为B,氧化钙粉末的质量为C。The technological process that calcium hydroxide changes the physicochemical properties of new phosphogypsum according to claim 1 and 2, it is characterized in that: in the (3) step, the quality of the calcium hydroxide powder is B, and the quality of the calcium oxide powder is C.
  8. 根据权利要求1或2所述的氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于:第(4)步骤中,所述的物料温度是通过设置在物料内的测温装置 测出的。The technological process that calcium hydroxide changes the physicochemical properties of new phosphogypsum according to claim 1 and 2, it is characterized in that: in the (4) step, the temperature of the material is measured by a temperature measuring device arranged in the material of.
  9. 根据权利要求1或2所述的氢氧化钙改变新磷石膏理化性能的工艺流程,其特征在于:第(3)步骤中,所述的氢氧化钙粉末或氧化钙粉末的加入量以使建筑石膏产品pH=6~7为准。The technological process that calcium hydroxide changes new phosphogypsum physical and chemical properties according to claim 1 or 2, it is characterized in that: in the (3) step, the addition amount of described calcium hydroxide powder or calcium oxide powder is so as to make the building Gypsum product pH=6~7 shall prevail.
PCT/CN2020/133196 2020-08-20 2020-12-02 Technological process for changing physical and chemical properties of new phosphogypsum by using calcium hydroxide WO2022036923A1 (en)

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