CN106629784A - Process for producing rice-shaped crystalline potassium nitrate by brine mixing method - Google Patents

Process for producing rice-shaped crystalline potassium nitrate by brine mixing method Download PDF

Info

Publication number
CN106629784A
CN106629784A CN201611058700.1A CN201611058700A CN106629784A CN 106629784 A CN106629784 A CN 106629784A CN 201611058700 A CN201611058700 A CN 201611058700A CN 106629784 A CN106629784 A CN 106629784A
Authority
CN
China
Prior art keywords
potassium nitrate
rice
cooling
shaped
crystallization
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
CN201611058700.1A
Other languages
Chinese (zh)
Other versions
CN106629784B (en
Inventor
余茅
余一茅
余荣华
李炳生
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.)
Zhejiang Lianda Chemical Co Ltd
Original Assignee
Zhejiang Lianda Chemical Co Ltd
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 Zhejiang Lianda Chemical Co Ltd filed Critical Zhejiang Lianda Chemical Co Ltd
Priority to CN201611058700.1A priority Critical patent/CN106629784B/en
Publication of CN106629784A publication Critical patent/CN106629784A/en
Application granted granted Critical
Publication of CN106629784B publication Critical patent/CN106629784B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D9/00Nitrates of sodium, potassium or alkali metals in general
    • C01D9/04Preparation with liquid nitric acid
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D9/00Nitrates of sodium, potassium or alkali metals in general
    • C01D9/16Purification
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D9/00Nitrates of sodium, potassium or alkali metals in general
    • C01D9/18Preparation in the form of shaped products, e.g. granules

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Agronomy & Crop Science (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a process for producing rice-shaped crystalline potassium nitrate by a brine mixing method. The process comprises the following steps: reacting nitric acid, magnesium oxide and potassium chloride serving as raw materials; cooling for crystallization to obtain crude potassium nitrate; mixing a high-temperature solution and a low-temperature solution of the potassium nitrate according to a certain proportion by the brine mixing method; adding a potassium nitrate seed crystal at the same time; controlling the temperature and stirring speed of a mixed solution; crystalizing to obtain the rice-shaped crystalline potassium nitrate. In the production process, a reaction solution is heated by heat produced in a reaction of the nitric acid and the magnesium oxide, so that the reaction speed is high, and energy is saved; cooling crystallization is performed in a way of mixing brine and adding the seed crystal, so that the crystallization speed is high, the efficiency is high, and the obtained potassium nitrate product is an elliptical rice-shaped crystal, and has the advantages of high purity, low impurity content, large crystal particle size, uniform granularity, high fluidity, no tendency to agglomeration, convenience in use and wide application.

Description

The technique that a kind of adding halogen method production rice-shaped crystallizes potassium nitrate
Technical field
Present invention relates particularly to chemical products production technical field, and in particular to a kind of adding halogen method production rice-shaped crystallization nitre The technique of sour potassium.
Background technology
In existing process for producing potassium nitrate, more using direct water-cooling or it is air-cooled by the way of crystallisation by cooling, gained potassium nitrate Crystal is thinner, mostly powder, easily caking, in-convenience in use.Convention resolution method is addition anticaking agent, but have impact on product Product purity, limits the purposes of product.
The content of the invention
In order to solve the deficiencies in the prior art, the present invention's produces rice-shaped crystallization potassium nitrate there is provided a kind of adding halogen method Technique.
The present invention adopt technical solution be:A kind of adding halogen method production rice-shaped crystallizes the technique of potassium nitrate, including Following steps:
(1)Nitric acid, magnesia and potassium chloride are pressed into mass fraction 5:1:3 ratio, input retort is reacted, after having reacted It is filtered to remove insoluble matter impurity;
(2)By the filtrate crystallisation by cooling for obtaining, centrifugation, potassium nitrate crude product is obtained;
(3)Gained potassium nitrate crude product is added water, heating for dissolving is filtered, and obtains the pyrosol of potassium nitrate;(4)Potassium nitrate is high Warm solution is proportionally added in crystallizer with the potassium nitrate cryogenic fluid after cooling, while potassium nitrate crystal seed is added, by control The solution temperature freezed in but water rate control crystallizer is at 30~50 DEG C, and stirring, the potassium nitrate that crystallisation by cooling obtains rice-shaped is brilliant Body;
(5)Centrifugation, drying obtains rice-shaped crystallization potassium nitrate product, and centrifugation gained filtrate returns to step(4)Followed Ring.
Described step(4)The mass ratio of the middle potassium nitrate cryogenic fluid by after potassium nitrate pyrosol and cooling is 1: 1~3.
Described step(4)Middle mixing speed is 30~60 turns per minute.
The invention has the beneficial effects as follows:The invention provides a kind of adding halogen method production rice-shaped crystallizes the technique of potassium nitrate, By being reacted as raw material with nitric acid, magnesia, potassium chloride, crystallisation by cooling obtains potassium nitrate crude product, then by adding halogen method, i.e., The pyrosol and cryogenic fluid of potassium nitrate are mixed by a certain percentage, while adding potassium nitrate crystal seed, mixeding liquid temperature is controlled And mixing speed, crystallize the production technology of the potassium nitrate crystals for obtaining rice-shaped.The production technology is anti-using nitric acid and magnesia The heat that should be produced is heated to reaction solution, and reaction speed is fast, and energy saving;Carry out by the way of halogen plus crystal seed using being converted Crystallisation by cooling, crystallization rate is fast, efficiency high, and gained potassium nitrate product is a kind of oval rice-shaped crystal, and purity is high, impurity Few, crystal particle diameter is larger and epigranular, and good fluidity is prevented from caking, easy to use, of many uses.
Description of the drawings
Fig. 1 is present invention production rice-shaped crystallization potassium nitrate process chart.
Specific embodiment
The present invention is further described in conjunction with Fig. 1,
High purity magnesium hydroxide preparation technology
Comprise the following steps:
(1)Nitric acid, magnesia and potassium chloride are pressed into mass fraction 5:1:3 ratio, input retort is reacted, after having reacted It is filtered to remove insoluble matter impurity;
(2)By the filtrate crystallisation by cooling for obtaining, centrifugation, potassium nitrate crude product is obtained;
(3)Gained potassium nitrate crude product is added water, heating for dissolving is filtered, and obtains the pyrosol of potassium nitrate;(4)Potassium nitrate is high Warm solution is 1 with the potassium nitrate cryogenic fluid example in mass ratio after cooling:1~3 is added in crystallizer, while adding potassium nitrate Crystal seed, by the solution temperature in control cooling water inflow control crystallizer at 30~50 DEG C, stirring, mixing speed is per minute 30 ~60 turns, crystallisation by cooling obtains the potassium nitrate crystals of rice-shaped;
(5)Centrifugation, drying obtains rice-shaped crystallization potassium nitrate product, and centrifugation gained filtrate returns to step(4)Followed Ring.
By being reacted as raw material with nitric acid, magnesia, potassium chloride, crystallisation by cooling obtains potassium nitrate crude product to the present invention, Again by adding halogen method, will potassium nitrate pyrosol and cryogenic fluid mix by a certain percentage, while add potassium nitrate crystal seed, Control mixeding liquid temperature and mixing speed, crystallization obtains the production technology of the potassium nitrate crystals of rice-shaped.The production technology is utilized The heat that nitric acid and oxidation reactive magnesium are produced is heated to reaction solution, and reaction speed is fast, and energy saving;Added using halogen is converted The mode of crystal seed carries out crystallisation by cooling, and crystallization rate is fast, efficiency high, and gained potassium nitrate product is that a kind of oval rice-shaped is brilliant Body, purity is high, and impurity is few, and crystal particle diameter is larger and epigranular, and good fluidity is prevented from caking, easy to use, of many uses.
The above is only the preferred embodiment of the present invention, and protection scope of the present invention is not limited merely to above-mentioned enforcement Example, all technical schemes belonged under thinking of the present invention belong to protection scope of the present invention.It should be pointed out that for the art Those of ordinary skill for, some improvements and modifications without departing from the principles of the present invention, these improvements and modifications Should be regarded as protection scope of the present invention.

Claims (3)

1. the technique that a kind of adding halogen method production rice-shaped crystallizes potassium nitrate, it is characterised in that comprise the following steps:
(1)Nitric acid, magnesia and potassium chloride are pressed into mass fraction 5:1:3 ratio, input retort is reacted, after having reacted It is filtered to remove insoluble matter impurity;
(2)By the filtrate crystallisation by cooling for obtaining, centrifugation, potassium nitrate crude product is obtained;
(3)Gained potassium nitrate crude product is added water, heating for dissolving is filtered, and obtains the pyrosol of potassium nitrate;(4)Potassium nitrate is high Warm solution presses 1 with the potassium nitrate cryogenic fluid after cooling:1~3 mass ratio is added in crystallizer, while adding potassium nitrate brilliant Kind, by control cooling water inflow control crystallizer in solution temperature at 30~50 DEG C, stirring, mixing speed be per minute 30~ 60 turns, crystallisation by cooling obtains the potassium nitrate crystals of rice-shaped;
(5)Centrifugation, drying obtains rice-shaped crystallization potassium nitrate product, and centrifugation gained filtrate returns to step(4)Followed Ring.
2. the technique that a kind of adding halogen method production rice-shaped according to claim 1 crystallizes potassium nitrate, it is characterised in that described The step of(4)The mass ratio of the middle potassium nitrate cryogenic fluid by after potassium nitrate pyrosol and cooling is 1:1~3.
3. the technique that a kind of adding halogen method production rice-shaped according to claim 1 crystallizes potassium nitrate, it is characterised in that described The step of(4)Middle mixing speed is 30~60 turns per minute.
CN201611058700.1A 2016-11-28 2016-11-28 A kind of technique of adding halogen method production rice-shaped crystallization potassium nitrate Active CN106629784B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611058700.1A CN106629784B (en) 2016-11-28 2016-11-28 A kind of technique of adding halogen method production rice-shaped crystallization potassium nitrate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611058700.1A CN106629784B (en) 2016-11-28 2016-11-28 A kind of technique of adding halogen method production rice-shaped crystallization potassium nitrate

Publications (2)

Publication Number Publication Date
CN106629784A true CN106629784A (en) 2017-05-10
CN106629784B CN106629784B (en) 2018-05-29

Family

ID=58812138

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611058700.1A Active CN106629784B (en) 2016-11-28 2016-11-28 A kind of technique of adding halogen method production rice-shaped crystallization potassium nitrate

Country Status (1)

Country Link
CN (1) CN106629784B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107117634A (en) * 2017-05-28 2017-09-01 赵家春 A kind of Production of Potassium Nitrate method
CN110862101A (en) * 2019-12-25 2020-03-06 安徽胜达化工科技有限公司 Preparation method of potassium nitrate
CN112645360A (en) * 2020-11-05 2021-04-13 浙江联大化工股份有限公司 Potassium nitrate tablet and production equipment and production process thereof
CN112875728A (en) * 2021-02-07 2021-06-01 武汉世吉药业有限公司 Preparation method of high-purity potassium nitrate and high-purity potassium nitrate

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1461439A (en) * 2000-03-01 2003-12-10 索尼计算机娱乐公司 Variable-mode PC card and input/output control device of PC card

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1461439A (en) * 2000-03-01 2003-12-10 索尼计算机娱乐公司 Variable-mode PC card and input/output control device of PC card

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107117634A (en) * 2017-05-28 2017-09-01 赵家春 A kind of Production of Potassium Nitrate method
CN110862101A (en) * 2019-12-25 2020-03-06 安徽胜达化工科技有限公司 Preparation method of potassium nitrate
CN112645360A (en) * 2020-11-05 2021-04-13 浙江联大化工股份有限公司 Potassium nitrate tablet and production equipment and production process thereof
CN112875728A (en) * 2021-02-07 2021-06-01 武汉世吉药业有限公司 Preparation method of high-purity potassium nitrate and high-purity potassium nitrate

Also Published As

Publication number Publication date
CN106629784B (en) 2018-05-29

Similar Documents

Publication Publication Date Title
CN106629784A (en) Process for producing rice-shaped crystalline potassium nitrate by brine mixing method
CN102174040B (en) Preparation method of electronic grade triglycidyl isocyanurate
CN106496159B (en) A kind of production technology of the big granularity crystal of acesulfame potassium
CN103420401B (en) Method for preparing large-particle picromerite
CN104003445B (en) A kind of method of producing high-dissolvability Ammonium Heptamolybdate
CN104118891B (en) Double decomposition air cooling crystallization method produces potassium nitrate technique
CN106045879B (en) Method for preparing cyanoacetic acid
CN104891549B (en) A kind of be raw material production barium chloride with witherite technique
CN108329205A (en) It is double(Aspirin)The preparation method of calcium carbamide compound
CN105384735A (en) Preparation method for bulk crystal product of thiamine nitrate
CN104003428A (en) Method for producing lithium hydroxide by dissolving spodumene out of pipeline reactor
CN102993237A (en) Aqueous-phase synthesis method of chlorpyrifos by using trichloro-acetic chloride as initial material
CN102674405B (en) Method for preparing potassium sulfate by using picromerite
CN107935842A (en) A kind of preparation method of 2 chlorine, 4 bromine, 6 methyl benzoic acid
CN107673946A (en) The method that continuity method isomerization produces durol
CN104355983B (en) A kind of method for crystallising of coarse granule shape nickel acetate
CN109721082A (en) A kind of production method of high purity magnesium hydroxide and potassium nitrate coproduction
CN102910638A (en) Preparation method of anhydrous lithium metaborate
CN103467272B (en) Rapid energy-saving and emission-reduction production method for high purity large particle nickel acetate
CN111056573A (en) Continuous production method of crystalline ferric chloride
CN104860812B (en) A kind of preparation method of ammonium lactate solid
CN107649171A (en) Continuity method isomerization produces the catalyst of durol
CN103754915A (en) Preparation method of strontium carbonate
CN101302028B (en) Method for producing barium chloride by heterogeneous co-heating method
CN105293579A (en) Preparation method of lithium molybdate

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