CN100347084C - Process of extracting borax decahydrate from salt lake sediment - Google Patents

Process of extracting borax decahydrate from salt lake sediment Download PDF

Info

Publication number
CN100347084C
CN100347084C CNB2006100203266A CN200610020326A CN100347084C CN 100347084 C CN100347084 C CN 100347084C CN B2006100203266 A CNB2006100203266 A CN B2006100203266A CN 200610020326 A CN200610020326 A CN 200610020326A CN 100347084 C CN100347084 C CN 100347084C
Authority
CN
China
Prior art keywords
raw material
constant temperature
container
salt lake
temperature
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.)
Expired - Fee Related
Application number
CNB2006100203266A
Other languages
Chinese (zh)
Other versions
CN1810643A (en
Inventor
严家华
陈明福
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.)
Tibet Shigatse tribute boron Processing Co., Ltd.
Original Assignee
TIBET QIFA MINING 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 TIBET QIFA MINING CO Ltd filed Critical TIBET QIFA MINING CO Ltd
Priority to CNB2006100203266A priority Critical patent/CN100347084C/en
Publication of CN1810643A publication Critical patent/CN1810643A/en
Application granted granted Critical
Publication of CN100347084C publication Critical patent/CN100347084C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The present invention discloses a method for extracting borax decahydrate from salt lake sediment. The processing steps comprise that A. grains of which the grain diameter are in a scope ranging from 0.8cm to 1.2cm is formed by crushing green ore of the salt lake sediment; B. raw materials which are crushed are poured in a container, and water of which the weight is two to three times as great as that of the raw materials is poured in the container and is uniformly blended; the mixed liquid is heated to 70 DEG C to 80 DEG C, and after the raw materials are completely dissolved, the mixed liquid is kept for 15 to 25 minutes at constant temperature; C. the water of which the weight is three to four times as great as that of the raw materials is poured in the mixed liquid of the constant temperature, the temperature of mixtures is reduced to 40 DEG C to 50 DEG C, and the temperature of mixtures is kept for 3.5 to 4.5 hours at constant temperature; D. saturated solution positioned at the upper part of the interior of a dissolver is poured in the other container, the product of borax decahydrate can be crystallized and separated out by evaporating and reducing the temperature to 10 DEG C to 37 DEG C. The present invention has the advantages of simple technical skill, low production cost, no pollution for environment, low energy consumption and high output value, and the present invention needs not add in chemical raw materials.

Description

From salt lake sediment, extract the method for borax decahydrate
Technical field
The present invention relates to a kind of preparation method of inorganic salt, particularly, the present invention relates to from salt lake sediment, extract the method for borax.
Background technology
Borax is a clear crystal, is the most important compound of boron.It is of many uses, can be used as the filler of washing powder and soap, also is the raw material of making opticglass, enamel and enamel, also can make artificial gems, welding agent etc., can cook heat-clearing and detoxicating drug after refining exquisiteness, cool in nature, sweet-salty can be controlled diseases such as swelling and pain in the throat, noma, aphtha, the living ocular of order.Borax also is commonly used for the metal-derusting agent, and on agricultural, borax also can serve as boron fertilizer.
Boron often is listed in rare elements abroad.Yet in China abundant native borax is arranged but, as be located in the salt lake sediment on ground such as Tibet, Xinjiang, Qinghai and just contain competent native borax.Main component is urao [Na 2CO 3NaHCO 32H 2O], saltcake [Na 2SO 410H 2O], native borax [Na 2O2B 2O 310H 2O] etc., main physical parameters sees the following form:
The composition title Density Solvent temperature Concentration Tc
Urao [Na 2CO 3·NaHCO 3·2H 2O] 2~2.14 35℃ 30~33°Bé -2~35℃
Saltcake [Na 2SO 4·10H 2O] 1.46 32.4℃ 30~32°Bé -5~10℃
Native borax [Na 2O·2B 2O 3·10H 2O] 1.7~1.72 70~80℃ 6~20°Bé 10~37℃
From the above: the crystallization concentration height of nitre, alkali, temperature is low, and borax needs could to be crystallized out under lower concentration and high-temperature.
The method of domestic production borax is mainly sulfuric acid process, carbonatation process, the interpretation of the law of pressurization alkali etc. at present, and all adopting with boron magnesium ore deposit is raw material, need add other industrial chemicals simultaneously to make auxiliary material, its technical sophistication, various being not easy of technical process grasped, and causes production cost to increase thus, and energy consumption is also big.In addition, far away because generally all remote mountain area, mining area, also there is the transportation cost height in ground factory process in raw materials for production are transported to from the mining area, the big and problems such as environmental pollution brought of expense.
Summary of the invention
The present invention is intended to overcome the defective of prior art, and a kind of method of extracting borax from salt lake sediment is provided.This method Technology is simple, does not need to add industrial chemicals, and production cost is low, environmentally safe, and energy consumption is low, output value height.
The technical solution used in the present invention is as follows:
A kind of method of extracting borax from salt lake sediment is characterized in that processing step is as follows:
A, raw material crushing: it is the particle of 0.8~1.2cm that the salt lake sediment crushing raw ore is become particle diameter;
B, dissolving: the raw material after the fragmentation is poured in the container, be incorporated as the water of 2~3 times of weight of raw material, mixing is heated to mixed solution 70~80 ℃ again, and raw material dissolves the back fully and continued constant temperature 15~25 minutes;
C, dilution cooling: in the mixed solution behind constant temperature, be incorporated as the water of 3~4 times of raw material weights again, and the temperature of mixture dropped to 40~50 ℃, constant temperature 3.5~4.5 hours;
D, crystallization: the saturated solution of container internal upper part is put in another container, and when evaporating and cooling to 10~37 ℃, i.e. the product borax decahydrate is separated out in crystallization.
The products obtained therefrom borax decahydrate can obtain anhydrous sodium tetraborate after thermal dehydration is handled.
The invention has the advantages that:
1, the present invention only need not add any industrial chemicals with water as auxiliary material, and production cost is low, environmentally safe.
2, Technology of the present invention is simple, can found the factory on the spot, has reduced transportation cost, and energy consumption is low, output value height.
3, the raw material of the present invention's employing is not for transporting the B that contains of value added 2O 3Be about 10% discarded ore deposit, saved limited resources effectively, turn waste into wealth.
4, the present invention has filled up a big blank of domestic system boron, has great economic benefit and social benefit.
Embodiment
Embodiment 1 salt lake is selected from the Bange lake in Tibet
A kind of method of extracting borax decahydrate from salt lake sediment is characterized in that processing step is as follows:
A, raw material crushing: it is the particle of 1cm that the salt lake sediment crushing raw ore is become particle diameter;
B, dissolving: the raw material after the fragmentation is poured in the container, be incorporated as the water of 2.5 times of weight of raw material, mixing is heated to mixed solution 70~80 ℃ again, and raw material dissolves the back fully and continued constant temperature 20 minutes;
C, dilution cooling: in the mixed solution behind constant temperature, be incorporated as the water of 3.5 times of raw material weights again, and the temperature of mixture dropped to 45 ℃, constant temperature 4 hours;
D, crystallization: the saturated solution of container internal upper part is put in another container, and when evaporating and cooling to 10~37 ℃, i.e. product borax decahydrate, wherein B are separated out in crystallization 2O 3Content be 36.51%
The products obtained therefrom borax decahydrate promptly obtains anhydrous sodium tetraborate after being heated to 400~500 ℃.
The cloth that embodiment 2 salt lakes are selected from the Zhongba County, Tibet is pricked coconut palm tea card lakeside (arrange in the autumn lake)
A kind of method of extracting borax decahydrate from salt lake sediment is characterized in that processing step is as follows:
A, raw material crushing: it is the particle of 0.8cm that the salt lake sediment crushing raw ore is become particle diameter;
B, dissolving: the raw material after the fragmentation is poured in the container, be incorporated as the water of 2 times of weight of raw material, mixing is heated to mixed solution 80 ℃ again, and raw material dissolves the back fully and continued constant temperature 15 minutes;
C, dilution cooling: in the mixed solution behind constant temperature, be incorporated as the water of 4 times of raw material weights again, and the temperature of mixture dropped to 40 ℃, constant temperature 4.5 hours;
D, crystallization: the saturated solution of container internal upper part is put in the crystallisation vessel, and when evaporating and cooling to 10~37 ℃, i.e. product borax decahydrate, wherein B are separated out in crystallization 2O 3Content be 41.3%.
The products obtained therefrom borax decahydrate can obtain anhydrous sodium tetraborate after thermal dehydration is handled.
Embodiment 3 salt lakes are selected from Tibet Mei Gahu
A kind of method of extracting borax decahydrate from salt lake sediment is characterized in that processing step is as follows:
A, raw material crushing: it is the particle of 1.2cm that the salt lake sediment crushing raw ore is become particle diameter;
B, dissolving: the raw material after the fragmentation is poured in the container, be incorporated as the water of 3 times of weight of raw material, mixing is heated to mixed solution 70 ℃ again, and raw material dissolves the back fully and continued constant temperature 25 minutes;
C, dilution cooling: in the mixed solution behind constant temperature, be incorporated as the water of 3 times of raw material weights again, and the temperature of mixture dropped to 50 ℃, constant temperature 3.5 hours;
D, crystallization: the saturated solution of container internal upper part is put in another container, and when evaporating and cooling to 10~37 ℃, i.e. product borax decahydrate, wherein B are separated out in crystallization 2O 3Content be 44.3%.
The products obtained therefrom borax decahydrate can obtain anhydrous sodium tetraborate after thermal dehydration is handled.

Claims (2)

1, a kind of method of extracting borax decahydrate from salt lake sediment is characterized in that processing step is as follows:
A, raw material crushing: it is the particle of 0.8~1.2cm that the salt lake sediment crushing raw ore is become particle diameter;
Described salt lake sediment is meant and is located in Tibet, Xinjiang, Qinghai that main component is urao [NaCO 3NaHCO 32H 2O], saltcake [Na 2SO 410H 2O], native borax [Na 2O2B 2O 310H 2O] mineral substance;
B, dissolving: the raw material after the fragmentation is poured in the container, be incorporated as the water of 2~3 times of weight of raw material, mixing is heated to mixed solution 70~80 ℃ again, and raw material dissolves the back fully and continued constant temperature 15~25 minutes:
C, dilution cooling: in the mixed solution behind constant temperature, be incorporated as the water of 3~4 times of raw material weights again, and the temperature of mixture dropped to 40~50 ℃, constant temperature 3.5~4.5 hours:
D, crystallization: the saturated solution of container internal upper part is put in another container, and when evaporating and cooling to 10~37 ℃, i.e. the product borax decahydrate is separated out in crystallization.
2, the method for extraction borax decahydrate according to claim 1 is characterized in that processing step is as follows:
A, raw material crushing: it is the particle of 1cm that the salt lake sediment crushing raw ore is become particle diameter;
B, dissolving: the raw material after the fragmentation is poured in the container, be incorporated as the water of 2.5 times of weight of raw material, mixing is heated to mixed solution 70~80 ℃ again, and raw material dissolves the back fully and continued constant temperature 20 minutes;
C, dilution cooling: in the mixed solution behind constant temperature, be incorporated as the water of 3.5 times of raw material weights again, and the temperature of mixture dropped to 45 ℃, constant temperature 4 hours;
D, crystallization: the saturated solution of container internal upper part is put in another container, and when evaporating and cooling to 10~37 ℃, i.e. the product borax decahydrate is separated out in crystallization.
CNB2006100203266A 2006-02-21 2006-02-21 Process of extracting borax decahydrate from salt lake sediment Expired - Fee Related CN100347084C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2006100203266A CN100347084C (en) 2006-02-21 2006-02-21 Process of extracting borax decahydrate from salt lake sediment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2006100203266A CN100347084C (en) 2006-02-21 2006-02-21 Process of extracting borax decahydrate from salt lake sediment

Publications (2)

Publication Number Publication Date
CN1810643A CN1810643A (en) 2006-08-02
CN100347084C true CN100347084C (en) 2007-11-07

Family

ID=36843793

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2006100203266A Expired - Fee Related CN100347084C (en) 2006-02-21 2006-02-21 Process of extracting borax decahydrate from salt lake sediment

Country Status (1)

Country Link
CN (1) CN100347084C (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101519212A (en) * 2009-04-09 2009-09-02 严笳化 Method for enriching borax pentahydrate from low-grade deposits of salt lake
CN101565188B (en) * 2009-06-03 2011-07-27 邛崃市鸿丰钾矿肥有限责任公司 Technique for preparing borax from brine
CN103641129A (en) * 2013-12-06 2014-03-19 忻世和 Method for desliming of raw borax ore in lake
CN103991878B (en) * 2014-05-19 2016-02-10 中国科学院青海盐湖研究所 The enriching method of low-grade native borax and system

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU420561A1 (en) * 1971-11-11 1974-03-25 A METHOD FOR GETTING A DECESSIVE BURAH
US3910773A (en) * 1970-04-06 1975-10-07 Occidental Petroleum Corp Beneficiation of salts crystallized from searles lake brine
SU1608116A1 (en) * 1988-06-21 1990-11-23 Предприятие П/Я А-7125 Method of producing borax decahydrate
US5676916A (en) * 1995-05-12 1997-10-14 Sociedad Minera Salar De Atacama S.A. Process for extracting the boron content in the brine of natural or industrial salt mines
RU2104949C1 (en) * 1996-09-26 1998-02-20 Закрытое акционерное общество "Кыштымский медеэлектролитный завод" Method for production of pure nickel sulfate

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3910773A (en) * 1970-04-06 1975-10-07 Occidental Petroleum Corp Beneficiation of salts crystallized from searles lake brine
SU420561A1 (en) * 1971-11-11 1974-03-25 A METHOD FOR GETTING A DECESSIVE BURAH
SU1608116A1 (en) * 1988-06-21 1990-11-23 Предприятие П/Я А-7125 Method of producing borax decahydrate
US5676916A (en) * 1995-05-12 1997-10-14 Sociedad Minera Salar De Atacama S.A. Process for extracting the boron content in the brine of natural or industrial salt mines
RU2104949C1 (en) * 1996-09-26 1998-02-20 Закрытое акционерное общество "Кыштымский медеэлектролитный завод" Method for production of pure nickel sulfate

Also Published As

Publication number Publication date
CN1810643A (en) 2006-08-02

Similar Documents

Publication Publication Date Title
CN100347084C (en) Process of extracting borax decahydrate from salt lake sediment
CN101255504B (en) Production technique for extracting gallium from coal ash and coal gangue
WO2011003266A1 (en) A preparation method for battery level lithium carbonate using lithium chloride solution
CN104310444B (en) The method of saltpetre is extracted in the waste nitric acid potassium raw material of chemically rigidifying glass production
CN104003445B (en) A kind of method of producing high-dissolvability Ammonium Heptamolybdate
CN102557085B (en) Method for extracting sodium salt in cesium salt and rubidium salt production process
CN101168799A (en) Extraction separation method for circularly preparing saponification organic phase rear earth from chloride solvent
CN106517196A (en) Production method of wooden activated carbon
CN101891530A (en) Activated calcium magnesium phosphate fertilizer and preparation method thereof
CN102633886A (en) Method for preparing plant-based polyether polyol by straw liquefaction
CN101585675A (en) Sulphonation method for naphthalene series water reducing agent without naphthalene discharging
CN1298904A (en) Process for preparing crystal lycopene and/or lycopene oil resin from tomato paste
CN103936034B (en) Preparation method of high-purity sodium iodide powder
CN1899963A (en) Method for preparing boric acid from borax
CN101880329A (en) Method for preparing plant hemicellulose hydrolysis liquid and method for extracting xylose and gum sugar
CN101559967B (en) Method for preparing barium nitrate, calcium nitrate, calcium sulfate and sodium nitrate by utilizing middle and low grade barium carbonate ore
CN105819442B (en) The method that penicillin waste mycelia denitrogenation prepares activated carbon
CN102617323A (en) Method for recovering pentaerythritol and sodium formate
CN108640130A (en) By the rough method for preparing lithium sulfate of salt lake sulfuric acid lithium salts
CN104445281A (en) Waste residue comprehensive utilization method for trichlorosilane leaching system
CN1696130A (en) Method for continuous extracting chlorophyll from silkworm dropping
CN206428008U (en) A kind of process units for improving medicinal sodium bicarbonate product granularity
CN102326803A (en) Method for dissolving peanut cake dregs by using imidazole ion liquid
CN109704384B (en) Preparation method of anhydrous calcium chloride
CN1673150A (en) Process of producing gypsum with mirabilite slag

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: XIZANG XIGAZE GONGJIA BORON PROCESSING LIMITED

Free format text: FORMER NAME: TIBET QIFA MINING CO., LTD.

CP03 Change of name, title or address

Address after: 850000, Tibet Prefecture, Shigatse Prefecture, Zhongba County, PA Jiang Township

Patentee after: Tibet Shigatse tribute boron Processing Co., Ltd.

Address before: Cai Cun 850000 Tibet autonomous region Lhasa city Niangre road eqin Rexiang

Patentee before: Tibet Qifa Mining Co., Ltd.

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20071107

Termination date: 20180221

CF01 Termination of patent right due to non-payment of annual fee