CN1064330C - Method for leaching phosphate from low-grade powdered rock phosphate - Google Patents

Method for leaching phosphate from low-grade powdered rock phosphate Download PDF

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CN1064330C
CN1064330C CN97121643A CN97121643A CN1064330C CN 1064330 C CN1064330 C CN 1064330C CN 97121643 A CN97121643 A CN 97121643A CN 97121643 A CN97121643 A CN 97121643A CN 1064330 C CN1064330 C CN 1064330C
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phosphate
leaching
grade
low
calcium
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CN1218003A (en
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张晓宇
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Abstract

The invention discloses a method for leaching and synthesizing phosphate by low-grade powdered rock phosphate, which is characterized in that the low-grade powdered rock phosphate is leached by sulfuric acid, and 2 percent of SiO is added2And 4% of KCl for defluorination, calcining marble, digesting, diluting to obtain lime milk containing 15% of calcium, adding into phosphoric acid, stirring, press-filtering, oven-drying and pulverizing to obtain feed-grade calcium hydrogen phosphate, if sectional synthesis is adopted, firstly synthesizing feed-grade calcium hydrogen phosphate, and then synthesizing calcium hydrogen phosphate for toothpaste, medicine and food.

Description

Method for leaching phosphate from low-grade powdered rock phosphate
The invention relates to a method for directly synthesizing calcium hydrophosphate by deep processing and leaching low-grade phosphorite.
At present, the phosphorus and phosphate deficiency in north China is in short supply, especially the feed grade calcium hydrophosphate in recent years. The traditional process for producing calcium hydrogen phosphate is to synthesize calcium hydrogen phosphate by removing impurities from phosphoric acid. In the research of secondary defluorination for producing feed-grade calcium hydrophosphate, which is published in the fourth stage 1-4 of 1991 of inorganic salt industry, the process of the method is to leach phosphate fertilizer and synthesize calcium hydrophosphate by secondary impurity removal. The disadvantages are that: the phosphate fertilizer is firstly bought and synthesized by water immersion and secondary impurity removal, the process is complex and needs two manufacturers to complete the process. The cost is high.
The invention aims to provide a method for directly synthesizing calcium hydrophosphate by leaching low-grade powdered rock phosphate and removing impurities.
The technical solution of the invention comprises the following steps:
leaching: with P2O5Heating 20% of phosphate rock powder at a solid-liquid ratio of 1: 2, stirring at 80-100 ℃, adding industrial sulfuric acid for leaching, and dripping sulfuric acid until the pH value is equal to 2, wherein the main reaction formula is as follows:
and (3) fluorine removal: 2% SiO is added in the later stage of leaching2And 4% KCl to convert fluorine to potassium fluorosilicate, which has the formula:
preparing calcium: the marble is calcined, heated and hydrolyzed, passes through a cement bridge, a drum sieve, a hydrocyclone and a 200-mesh sieve, and is diluted to lime milk containing 15 percent of calcium.
Synthesizing: adding lime milk into 35-40 deg.C phosphoric acid, stirring, adding acid until pH is 6.8, aging for 30 min, press filtering, rapidly oven drying, pulverizing to obtain feed grade calcium hydrogen phosphate, and synthesizing by stages to obtain feed grade calcium hydrogen phosphate, wherein the filtrate contains part of phosphoric acid and calcium, and preparing into toothpaste, medicine and food grade calcium hydrogen phosphate.
And (4) leaching the low-grade phosphate rock powder twice or three times until the concentration of phosphoric acid reaches 20-40%.
The invention has the advantages that:
1. further develops low-grade phosphorite resources, changes the indigestion products into delicateness commodities, and drives raw materials such as marble, coal and the like to be commercialized at the same time.
2. The products are transported in a long distance, are three local commodities which are locally processed and digested from the raw materials in the north, and reduce the product cost.
3. The low-grade ground phosphate rock is leached and then simultaneously subjected to impurity removal, so that the calcium hydrophosphate is directly synthesized, the process is simple, the cost is low, and the effect is quick.

Claims (2)

1. The method for leaching phosphate from low-grade powdered rock phosphate is characterized by comprising the following steps: the method comprises the following steps:
leaching: with P2O5Heating 20% of phosphate rock powder at a solid-to-liquid ratio of 1: 2, stirring at 80-100 ℃, adding industrial sulfuric acid for leaching, and dripping sulfuric acid until the pH value is equal to 2;
and (3) fluorine removal: 2% SiO is added in the later stage of leaching2And 4% KCl to make fluorine become potassium fluosilicate, and precipitate in the filter residue;
preparing calcium: calcining marble, heating, hydrolyzing, sieving with a cement bridge, a drum sieve, a hydrocyclone, a 200-mesh sieve, and diluting to lime milk containing 15% of calcium;
synthesizing: adding lime milk into phosphoric acid at 35-40 deg.C, stirring, stopping adding acid until pH is 6.8, aging for 30 min, press filtering, rapidly oven drying, and pulverizing to obtain feed grade calcium hydrogen phosphate.
2. The method for leaching phosphate from low-grade powdered rock phosphate according to claim 1, characterized in that: and (4) leaching the low-grade phosphate rock powder twice or three times until the concentration of phosphoric acid reaches 20-40%.
CN97121643A 1997-11-20 1997-11-20 Method for leaching phosphate from low-grade powdered rock phosphate Expired - Fee Related CN1064330C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN97121643A CN1064330C (en) 1997-11-20 1997-11-20 Method for leaching phosphate from low-grade powdered rock phosphate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN97121643A CN1064330C (en) 1997-11-20 1997-11-20 Method for leaching phosphate from low-grade powdered rock phosphate

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CN1218003A CN1218003A (en) 1999-06-02
CN1064330C true CN1064330C (en) 2001-04-11

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Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101302129B (en) * 2008-05-22 2011-11-30 东莞市施普旺生物科技有限公司 Calcium hydrophosphate suspending agent
CN103723698B (en) * 2013-11-25 2015-07-15 瓮福(集团)有限责任公司 Method for reducing content of magnesium in feed grade calcium hydrophosphate
CN106882778A (en) * 2015-12-15 2017-06-23 中国科学院大连化学物理研究所 A kind of method that toothpaste grade calcium hydrophosphate is prepared in micro passage reaction
CN114106837B (en) * 2021-11-25 2023-11-21 中化农业(临沂)研发中心有限公司 Saline-alkali soil conditioner containing polyphosphate and preparation method and application thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4485078A (en) * 1982-03-16 1984-11-27 Agrico Chemical Company Process for producing wet process phosphoric acid from phosphate rocks containing fluochlorapatite and related minerals
CN1048015A (en) * 1990-02-17 1990-12-26 云南易门矿务局 Low ratio acid wet method is produced calcium hydrophosphate fodder
CN1113880A (en) * 1994-06-01 1995-12-27 龚家竹 Method for extracting phosphoric acid and solution containing phosphate by sulfuric acid method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4485078A (en) * 1982-03-16 1984-11-27 Agrico Chemical Company Process for producing wet process phosphoric acid from phosphate rocks containing fluochlorapatite and related minerals
CN1048015A (en) * 1990-02-17 1990-12-26 云南易门矿务局 Low ratio acid wet method is produced calcium hydrophosphate fodder
CN1113880A (en) * 1994-06-01 1995-12-27 龚家竹 Method for extracting phosphoric acid and solution containing phosphate by sulfuric acid method

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