CN101659429A - Process for producing potassium chloride with purity above 99 percent - Google Patents

Process for producing potassium chloride with purity above 99 percent Download PDF

Info

Publication number
CN101659429A
CN101659429A CN200810054288A CN200810054288A CN101659429A CN 101659429 A CN101659429 A CN 101659429A CN 200810054288 A CN200810054288 A CN 200810054288A CN 200810054288 A CN200810054288 A CN 200810054288A CN 101659429 A CN101659429 A CN 101659429A
Authority
CN
China
Prior art keywords
potassium chloride
purity
repone
percent
mother liquor
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
CN200810054288A
Other languages
Chinese (zh)
Inventor
冯立云
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.)
TIANJIN LIHONG CHEMICAL TECHNICAL CO Ltd
Original Assignee
TIANJIN LIHONG CHEMICAL TECHNICAL 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 TIANJIN LIHONG CHEMICAL TECHNICAL CO Ltd filed Critical TIANJIN LIHONG CHEMICAL TECHNICAL CO Ltd
Priority to CN200810054288A priority Critical patent/CN101659429A/en
Publication of CN101659429A publication Critical patent/CN101659429A/en
Pending legal-status Critical Current

Links

Abstract

The invention discloses a process for producing potassium chloride with a purity above 99 percent. The process comprises the following steps: taking 50 grams of potassium chloride with a purity below98 percent; mixing the potassium chloride with water to obtain saturated potassium chloride solution; arranging a filter tank of a filter sieve on the outlet of a pump; removing insoluble substance ofwater to obtain potassium chloride mother liquor; cooling and crystallizing the mother liquor in a cooling tank; drying the mother liquor by a drying machine to obtain potassium chloride crystal; anddrying the potassium chloride crystal to obtain potassium chloride with a purity above 99 percent.

Description

A kind of purity is the production technique of 99% above Repone K
Technical field
The present invention designs the production technique that a kind of purity is 99% above Repone K
Background technology
High purity chlorination potassium is the important source material of medicine and foodstuff additive, the content requirement of its Repone K reaches more than 99%, the most of manufacturing enterprise of China continues to use traditional thermosol cold crystallization technology always at present, the heat energy consumption of this explained hereafter Repone K is big, equipment corrosion is serious, need import equipment, so the cost height of product.
Summary of the invention
The objective of the invention is to overcome above-mentioned defective, it is 99% above Repone K production technique that a kind of purity is provided.
Technical scheme of the present invention is: a kind of purity is the production technique of 99% above Repone K, get purity and be Repone K 50 grams below 98%, add water mix obtain saturated potassium chloride solution after, through add the hay tank of filter sieve at pump outlet, remove the insolubles that anhydrates and obtain the Repone K mother liquor, after mother liquor carried out crystallisation by cooling by cooling tank, dry by drier and obtain potassium chloride, obtaining purity through oven dry at last is 99% above Repone K.
The present invention has the following advantages: pollution-free, rate of recovery height has reduced product cost.
Specific embodiment
Embodiment: a kind of purity is the production technique of 99% above Repone K, get purity and be Repone K 50 grams below 98%, add water mix obtain saturated potassium chloride solution after, through add the hay tank of filter sieve at pump outlet, remove the insolubles that anhydrates and obtain the Repone K mother liquor, after mother liquor carried out crystallisation by cooling by cooling tank, dry by drier and obtain potassium chloride, obtaining purity through oven dry at last is 99% above Repone K.

Claims (1)

1, a kind of purity is the production technique of 99% above Repone K, it is characterized in that: get purity and be Repone K 50 grams below 98%, add water mix obtain saturated potassium chloride solution after, through add the hay tank of filter sieve at pump outlet, remove the insolubles that anhydrates and obtain the Repone K mother liquor, after mother liquor carried out crystallisation by cooling by cooling tank, dry by drier and obtain potassium chloride, obtaining purity through oven dry at last is 99% above Repone K.
CN200810054288A 2008-08-26 2008-08-26 Process for producing potassium chloride with purity above 99 percent Pending CN101659429A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200810054288A CN101659429A (en) 2008-08-26 2008-08-26 Process for producing potassium chloride with purity above 99 percent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200810054288A CN101659429A (en) 2008-08-26 2008-08-26 Process for producing potassium chloride with purity above 99 percent

Publications (1)

Publication Number Publication Date
CN101659429A true CN101659429A (en) 2010-03-03

Family

ID=41787714

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200810054288A Pending CN101659429A (en) 2008-08-26 2008-08-26 Process for producing potassium chloride with purity above 99 percent

Country Status (1)

Country Link
CN (1) CN101659429A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103588225A (en) * 2013-11-21 2014-02-19 浙江大洋生物科技集团股份有限公司 Method for producing food-grade potassium chloride through multistage flash evaporation, cooling and continuous crystallization
CN104192867A (en) * 2014-08-25 2014-12-10 连云港树人科创食品添加剂有限公司 Method for removing floating agent out of potassium chloride

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103588225A (en) * 2013-11-21 2014-02-19 浙江大洋生物科技集团股份有限公司 Method for producing food-grade potassium chloride through multistage flash evaporation, cooling and continuous crystallization
CN104192867A (en) * 2014-08-25 2014-12-10 连云港树人科创食品添加剂有限公司 Method for removing floating agent out of potassium chloride

Similar Documents

Publication Publication Date Title
CN104473120B (en) A kind of production technology of monosodium glutamate
CN103725731B (en) Special crystalline dextrose of Sunmorl N 60S and preparation method thereof
CN104118891B (en) Double decomposition air cooling crystallization method produces potassium nitrate technique
CN103709006B (en) Method for crystallizing erythritol fermentation liquid by evaporation-elution coupled process
CN106045879B (en) Method for preparing cyanoacetic acid
CN101070168B (en) Method for producing sodium nitrate
CN101156675A (en) Glutamic acid abstraction technics combining rotation crystal
CN105016373A (en) Method for producing copper chloride through waste etching liquid containing copper
CN101182011B (en) Medicinal natrium chloratum double-effect forced circulation evaporation technique
CN101659428A (en) Process for producing high-purity potassium chloride
CN102070475B (en) Sodium glutamate double-action crystallization production process
CN101659429A (en) Process for producing potassium chloride with purity above 99 percent
CN103588223B (en) Method for producing high-purity ammonium chloride through multistage flash evaporation, cooling and continuous crystallization
CN102690191A (en) Method for producing calcium lactate by taking duck egg shell as raw material
CN104355990B (en) Method for recycling and mechanically using L- (+) -tartaric acid in D-ethyl ester production
CN101659430A (en) Process for producing purified potassium chloride
CN103012509B (en) Method of separating and purifying sucrose-6-acetate mother liquor by salt fractionation
CN104911235A (en) Medical dextrose monohydrate production technology
CN104557685A (en) Method for producing nicotinic acid by using nicotinamide mother solution
CN1309698C (en) Purifying process of 3,4,5-trimethoxyl benzoic acid
CN104118958A (en) Fumaric acid wastewater recovery treatment technique
CN102530902B (en) Industrialized continuous potassium dihydrogen phosphate production method
CN102336685B (en) Method for preparing cyanoacetic acid through continuous dehydration
CN101659427A (en) Process for producing food-grade potassium chloride
CN101659434A (en) Process for producing high-purity magnesium chloride

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Open date: 20100303