CN102115441A - Method for producing industrial calcium oxalate and phosphoric acid by utilizing phosphogypsum - Google Patents

Method for producing industrial calcium oxalate and phosphoric acid by utilizing phosphogypsum Download PDF

Info

Publication number
CN102115441A
CN102115441A CN2010106155440A CN201010615544A CN102115441A CN 102115441 A CN102115441 A CN 102115441A CN 2010106155440 A CN2010106155440 A CN 2010106155440A CN 201010615544 A CN201010615544 A CN 201010615544A CN 102115441 A CN102115441 A CN 102115441A
Authority
CN
China
Prior art keywords
filtrate
filter residue
phosphogypsum
phosphoric acid
acid
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.)
Pending
Application number
CN2010106155440A
Other languages
Chinese (zh)
Inventor
马艳荣
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN2010106155440A priority Critical patent/CN102115441A/en
Publication of CN102115441A publication Critical patent/CN102115441A/en
Pending legal-status Critical Current

Links

Landscapes

  • Fertilizers (AREA)

Abstract

The invention provides a method for producing industrial calcium oxalate and phosphoric acid by utilizing phosphogypsum, which comprises the following steps of: crushing the phosphogypsum into coarse powder with the granularity of 80 to 100 meshes, fully mixing with water, and filtering to obtain filter residue one and filtrate one; reacting the filter residue one with excessive sulfuric acid, and filtering to obtain filter residue two and filtrate two; reacting the filtrate residue two with excessive hydrochloric acid, and filtering a reaction product to obtain filtrate three and filter residue mainly containing calcium sulfate; washing, drying and crushing the filter residue three to obtain the calcium sulfate; mixing the obtained calcium sulfate with water, reacting with oxalic acid to obtain a calcium oxalate precipitate and sulfuric acid, and filtering and separating to obtain calcium oxalate filter cakes and sulfuric acid filtrate; washing, crushing and drying the obtained calcium oxalate filter cakes to obtain a calcium oxalate product; and combining the filtrate one, the filtrate two and the filtrate three, distilling under reduced pressure, condensing to collect phosphoric acid to obtain the phosphoric acid, and burying residual.

Description

A kind of method of utilizing phosphogypsum manufacture caoxalate and phosphoric acid
Technical field
The present invention relates to phosphogypsum, particularly, relate to a kind of method of utilizing phosphogypsum manufacture caoxalate and phosphoric acid.
Background technology
Phosphogypsum is meant in phosphoric acid production, the solid slag that produces during with sulfuric acid treating phosphorite, and its main component is a calcium sulfate.Contain multiple other impurity in addition, as insoluble impurities: as the phosphoric acid salt and the vitriol of quartz, undecomposed phosphatic rock, fluorochemical and fluorine, aluminium, magnesium; Soluble impurity: as water-soluble P 2O 5, fluorochemical that solubleness is lower and vitriol.In addition, also contain arsenic, copper, zinc, iron, manganese, lead, cadmium, mercury and radioelement in the phosphogypsum, equal trace extremely, and great majority are insoluble solid, its hazardness can be ignored.Institute's fluoride, free phosphoric acid, P in the phosphogypsum 2O 5, impurity such as phosphoric acid salt is to cause phosphogypsum to cause the principal element of environmental pollution in the process of storing up.The improvement of phosphogypsum and to utilize problem be a global difficult problem.
China is as first production of phosphate fertilizer state in the world, also is simultaneously first phosphogypsum by-product state.According to incompletely statistics, the domestic phosphogypsum slag of storing up reaches more than 100,000,000 ton at present, also will newly produce tens million of tons every year.Because the phosphogypsum generation is huge, the market capacity of phosphogypsum comprehensive utilization product is limited, also can't accomplish in a short time phosphogypsum is all utilized, and can only adopt air storage to handle.Storing up in a large number of phosphogypsum, injustice has been occupied land resources, has caused the pollution of atmosphere, water system and soil owing to wind erosion, weathering.The Long contact time phosphogypsum may cause people's death or pathology certainly.
For this reason, be necessary to explore the industry application method thereof of phosphogypsum, give full play to its potential economic worth.
Summary of the invention
For this reason, the application provides a kind of method of utilizing phosphogypsum manufacture caoxalate and phosphoric acid, and this method is effectively extracted the calcium sulfate in the phosphogypsum, for the industrial application of phosphogypsum provides new approach.
The main component of phosphogypsum is a calcium sulfate, contains multiple other impurity in addition, as insoluble impurities: the phosphoric acid salt and the vitriol of quartzy, undecomposed phosphatic rock, fluorochemical and fluorine, aluminium, magnesium; Soluble impurity: as P 2O 5, fluorochemical that solubleness is lower and vitriol.
The application's technical scheme is as follows: a kind of method of utilizing phosphogypsum manufacture caoxalate and phosphoric acid, this method comprises following concrete steps: it is 80-100 purpose meal that phosphogypsum is pulverized, place reactor and water thorough mixing, make the water-soluble after-filtration of soluble impurity in the phosphogypsum, obtain filter residue one and filtrate one; Be water-fast impurity in the filter residue one, it mainly contains calcium sulfate, calcium phosphate, and the phosphoric acid salt of a spot of other insoluble impuritiess such as fluorochemical and fluorine, aluminium, magnesium and vitriol etc.; With filter residue one and excess sulfuric acid reaction, at this moment, calcium phosphate in the filter residue one and sulfuric acid reaction generate insoluble calcium sulfate and soluble phosphoric acid, after the filtration, obtain filter residue two and filtrate two; Filter residue two mainly contains the phosphoric acid salt and the vitriol of calcium sulfate and a spot of other insoluble impuritiess such as fluorochemical and fluorine, aluminium, magnesium, filter residue two reacts with excessive hydrochloric acid again, at this moment, insoluble calcium phosphate is converted to the phosphoric acid and the calcium chloride of solubility, and the phosphoric acid salt of insoluble fluorine, aluminium, magnesium also is converted to the phosphoric acid and the muriate of solubility; Reactant refilters, and obtains the filter residue three of filtrate three and main sulfur acid calcium and a small amount of vitriol; Gained filter residue three promptly obtains highly purified calcium sulfate through washing, crushed after being dried; The calcium sulfate that gained is high-purity mixes back and oxalic acid reaction with water, obtain calcium oxalate precipitation and sulfuric acid, separates after filtration, obtains caoxalate filter cake and sulfuric acid filtrate; Sulphuric acid soln returns with filter residue one reaction and reuses; Gained caoxalate filter cake obtains the caoxalate product through washing, pulverizing and dry.
Gained filtrate one, after filtrate two and filtrate three merged, through underpressure distillation, phosphoric acid was collected in condensation, obtains highly purified phosphoric acid, and residuum is buried.
The method of utilizing phosphogypsum production manufacture caoxalate and phosphoric acid of the present invention, this method is effectively extracted the calcium sulfate in the phosphogypsum, for the industrial application of phosphogypsum provides new approach.
Embodiment
Embodiment 1:
A kind of method of utilizing phosphogypsum manufacture caoxalate and phosphoric acid, it is 80 purpose meal that the 500kg phosphogypsum is pulverized, and places reactor and water thorough mixing, makes the water-soluble after-filtration of soluble impurity in the phosphogypsum, obtains filter residue one and filtrate one; With filter residue one and excess sulfuric acid reaction, after the filtration, obtain filter residue two and filtrate two; Filter residue two reacts with excessive hydrochloric acid again, and reactant refilters, and obtains the filter residue three of filtrate three and main sulfur acid calcium; Gained filter residue three promptly obtains calcium sulfate through washing, crushed after being dried; Gained calcium sulfate is mixed back and oxalic acid reaction with water, obtain calcium oxalate precipitation and sulfuric acid, separate after filtration, obtain caoxalate filter cake and sulfuric acid filtrate; Sulphuric acid soln returns with filter residue one reaction and reuses; Gained caoxalate filter cake obtains the caoxalate product through washing, pulverizing and dry; Gained filtrate one, after filtrate two and filtrate three merged, through underpressure distillation, phosphoric acid was collected in condensation, obtains phosphoric acid, and residuum is buried.
Embodiment 2:
A kind of method of utilizing phosphogypsum manufacture caoxalate and phosphoric acid, it is 100 purpose meal that the 500kg phosphogypsum is pulverized, and places reactor and water thorough mixing, makes the water-soluble after-filtration of soluble impurity in the phosphogypsum, obtains filter residue one and filtrate one; With filter residue one and excess sulfuric acid reaction, after the filtration, obtain filter residue two and filtrate two; Filter residue two reacts with excessive hydrochloric acid again, and reactant refilters, and obtains the filter residue three of filtrate three and main sulfur acid calcium; Gained filter residue three promptly obtains calcium sulfate through washing, crushed after being dried; Gained calcium sulfate is mixed back and oxalic acid reaction with water, obtain calcium oxalate precipitation and sulfuric acid, separate after filtration, obtain caoxalate filter cake and sulfuric acid filtrate; Sulphuric acid soln returns with filter residue one reaction and reuses; Gained caoxalate filter cake obtains the caoxalate product through washing, pulverizing and dry; Gained filtrate one, after filtrate two and filtrate three merged, through underpressure distillation, phosphoric acid was collected in condensation, obtains phosphoric acid, and residuum is buried.
Above content be in conjunction with concrete preferred implementation to further describing that the present invention did, can not assert that concrete enforcement of the present invention is confined to these explanations.For the general technical staff of the technical field of the invention, without departing from the inventive concept of the premise, its framework form can be flexible and changeable, can the subseries product.Just make some simple deduction or replace, all should be considered as belonging to the scope of patent protection that the present invention is determined by claims of being submitted to.

Claims (1)

1. method of utilizing phosphogypsum manufacture caoxalate and phosphoric acid, it is characterized in that, comprise following concrete steps: it is 80-100 purpose meal that phosphogypsum is pulverized, place reactor and water thorough mixing, make the water-soluble after-filtration of soluble impurity in the phosphogypsum, obtain filter residue one and filtrate one; With filter residue one and excess sulfuric acid reaction, after the filtration, obtain filter residue two and filtrate two; Filter residue two reacts with excessive hydrochloric acid again, and reactant refilters, and obtains the filter residue three of filtrate three and main sulfur acid calcium; Gained filter residue three promptly obtains calcium sulfate through washing, crushed after being dried; Gained calcium sulfate is mixed back and oxalic acid reaction with water, obtain calcium oxalate precipitation and sulfuric acid, separate after filtration, obtain caoxalate filter cake and sulfuric acid filtrate; Sulphuric acid soln returns with filter residue one reaction and reuses; Gained caoxalate filter cake obtains the caoxalate product through washing, pulverizing and dry; Gained filtrate one, after filtrate two and filtrate three merged, through underpressure distillation, phosphoric acid was collected in condensation, obtains phosphoric acid, and residuum is buried.
CN2010106155440A 2010-12-31 2010-12-31 Method for producing industrial calcium oxalate and phosphoric acid by utilizing phosphogypsum Pending CN102115441A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010106155440A CN102115441A (en) 2010-12-31 2010-12-31 Method for producing industrial calcium oxalate and phosphoric acid by utilizing phosphogypsum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010106155440A CN102115441A (en) 2010-12-31 2010-12-31 Method for producing industrial calcium oxalate and phosphoric acid by utilizing phosphogypsum

Publications (1)

Publication Number Publication Date
CN102115441A true CN102115441A (en) 2011-07-06

Family

ID=44214382

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010106155440A Pending CN102115441A (en) 2010-12-31 2010-12-31 Method for producing industrial calcium oxalate and phosphoric acid by utilizing phosphogypsum

Country Status (1)

Country Link
CN (1) CN102115441A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103642852A (en) * 2013-11-29 2014-03-19 大连创达技术交易市场有限公司 Preparation method of oxalate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103642852A (en) * 2013-11-29 2014-03-19 大连创达技术交易市场有限公司 Preparation method of oxalate

Similar Documents

Publication Publication Date Title
CN103922372A (en) Method for recovering phosphorus in phosphate tailings with high magnesium content and preparing magnesium sulfate by adopting indirect sulfuric acid method
CN104477992A (en) Method for preparing vanadium pentoxide
CN110117720B (en) Method for comprehensively extracting valuable metals from sulfate slag through phosphorylation roasting, leaching and extraction
CN113120875B (en) Production method of low-impurity wet-process phosphoric acid and high-quality alpha-hemihydrate gypsum
CN110002421B (en) Method for preparing battery-grade iron phosphate by using sulfuric acid residues
CN113697790A (en) Method for preparing phosphoric acid by hydrochloric acid wet process combining organic solvent extraction and water back extraction
CN104291539A (en) Method for dealkalizing Bayer process red mud by using CO2 and waste acid in combined way
CN103553722A (en) Method for preparing super phosphate by use of ardealite slag site sewage
CN107827113B (en) Method for recovering fluorine in industrial monoammonium phosphate neutralized slag slurry
CN103466579A (en) Method for producing full-water-soluble monoammonium phosphate by phosphoric acid by wet process
CN102838097A (en) Method for removing magnesium oxide in phosphate concentrate through phosphatic fertilizer and phosphorus chemical industry acid wastewater
CN107473775B (en) Method for recovering phosphorus and fluorine in phosphoric acid concentrated slag acid and co-producing low-fluorine water-soluble fertilizer
CN102167671A (en) Method for preparing dicyandiamide, industrial calcium sulfate and charcoal by using dicyandiamide waste residue
CN102115142A (en) Method for producing industrial calcium sulfate by producing ardealite
CN102115141A (en) Method for producing industrial calcium sulfate and phosphoric acid by using phosphogypsum
CN102115120A (en) Method for producing calcium carbonate by using carbide slag
CN102115441A (en) Method for producing industrial calcium oxalate and phosphoric acid by utilizing phosphogypsum
CN116656952A (en) Method for treating and recovering manganese, magnesium and ammonium in leachate of electrolytic manganese slag warehouse
CN103408050A (en) Method of efficient extraction of aluminum, iron, and titanium in coal gangue
CN102115143A (en) Method for producing calcium sulfate from carbide slag
CN106829900A (en) The method that carbide slag is used for phosphoric acid by wet process desulfurization
CN102115133A (en) Method for producing calcium nitrate by carbide slag
CN102167672A (en) Method for preparing dicyandiamide and industrial calcium phosphate and carbon from dicyandiamide waste slag
CN103539487B (en) Produce the method for phosphorus ammonium
CN105732154A (en) Method for preparing potassium fertilizer from potassium feldspar

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20110706