Preparation of sodium carbonate peroxide and its dry granular products

A technology of sodium peroxycarbonate, sodium carbonate, applied in directions such as peroxide/peroxyhydrate/peroxyacid/superoxide/ozone, chemical instruments and methods, organic peroxy/inorganic per compound compositions, etc., It can solve the problems of substandard products, low recovery rate, low reagent conversion rate, etc.

Inactive Publication Date: 2004-04-21
比利时索尔维因特罗斯公司
View PDF2 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] Although theoretically wet processing can be operated without a salting-out agent, the absence of a salting-out agent results in lower conversion of reagents to PCS, and lower recovery of PCS from solution, so that the returned mother liquor contains higher concentrations of supernatants. Hydrogen peroxide, thus increasing the possibility of premature crystallization on return, and the degree of loss of hydrogen peroxide during return
[0009] Perhaps the most acute problem faced by persalt manufacturers wishing to wet process PCS is the fact that wet processing often employs salting-out agents to operate the process effectively, yet the resulting product may have undesired the nature of

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Preparation of sodium carbonate peroxide and its dry granular products
  • Preparation of sodium carbonate peroxide and its dry granular products
  • Preparation of sodium carbonate peroxide and its dry granular products

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0099] In this example, a set of equipment in Fig. 1 is used to continuously produce PCS without adding any salting-out agent. 60% of the soda ash was added per cycle via the dissolution tank at 25°C, resulting in a solution of 87% saturated solution concentration, and 40% of the soda ash was added by direct addition of solids to the reactor. Leaving the dissolving tank mother liquor peroxide content is 30g / L. The molar ratio of sodium carbonate to hydrogen peroxide in the crystallizer is kept at 1-1.1:1. After drying of sodium percarbonate, the 7-day aging thermal radiation is 1 μW / g for 16 hours, and the average particle size is 680 microns (when using the laser particle size analyzer according to the formula (D 90 -D 10 ) / D 50 When measuring, the span (span) is 1.0, where D is the diameter expressed in microns). The product had a moisture absorption of 14 g / kg, a bulk density of 990 g / kg and an oxygen content of 14.7%.

example 2

[0101] In this example, a set of equipment in Fig. 2 is used to continuously produce PCS without adding any salting-out agent. The dissolution tank is operated at 45°C, and the soda ash is dissolved in the circulating mother liquor to reach a concentration of 76% saturated solution. The mother liquor leaving the dissolving tank contains 8g / L hydrogen peroxide. The molar ratio of sodium carbonate to hydrogen peroxide in the crystallizer is kept at 1-1.1:1.

[0102] The resulting product had an average particle size of 650 microns (span 0.9), a 7-day aging heat radiation of 2 µW / g, a moisture absorption of 1.5 g / kg and an available oxygen of 14.9%. Compared with Example 1, it can be seen that the method loses more hydrogen peroxide in the process of Example 2 return, while the product retains the good heat radiation and hygroscopic properties of Example 1.

example 3-5

[0104] These examples, according to Fig. 1 a set of equipment is operated, and 100% soda ash that will add directly joins reactor. The hydrogen peroxide to sodium carbonate mol ratio in the reactor, the dissolution tank temperature and product characteristics are summarized in Table 1 below.

[0105] instance number

[0106] As can be seen from Table 1, products with both low thermal radiation (LKB) and high available oxygen can be obtained, and it is observed that the average particle size increases with H 2 o 2 The correlation tends to increase with increasing molar ratios of soda ash, demonstrating that, for at least some applications, the optimum molar ratio is from about 0.8 to about 0.85:1.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
particle sizeaaaaaaaaaa
water absorptionaaaaaaaaaa
particle sizeaaaaaaaaaa
Login to view more

Abstract

Sodium percarbonate is traditionally made in a crystallisation process from aqueous hydrogen peroxide and sodium carbonate with recycle of mother liquor in the presence of a substantial concentration of a salting-out agent, conventionally sodium chloride. The invention provides a process intended to be conducted without addition of chloride salting-out agent in which the dissolution step (1) is controlled to restrict the sodium carbonate concentration to below 95 %; preferably 60 to 90 % of its saturated concentration at a temperature preferably controlled to at most 35 DEG C and the mole ratio of hydrogen peroxide: sodium carbonate in the reaction vessel is controlled to between 0.7 to 1.2:1, and preferably about 1:1. In some embodiments at least a fraction of the mother liquor introduced into the dissolution tank (1) is obtained by extraction from the reaction vessel (6) and in other embodiments a fraction of the sodium percarbonate (2) is introduced in solution in the mother liquor (4) and a fraction is introduced in particulate form (8) directly into the reaction vessel (6). Large particle sodium percarbonate is provided which has a 7 day aged heat emission at 40 DEG C of not more than 3 mu W/g measured in a microcalorimeter over 16 hours that is lower than the heat emission from conventionally produced sodium percarbonate employing a chloride salting-out agent.

Description

technical field [0001] The present invention relates to a process for the preparation of persalts, and more particularly to the preparation of sodium percarbonate and sodium percarbonate so prepared. It also relates to sodium percarbonate itself and compositions comprising sodium percarbonate. Background technique [0002] Sodium percarbonate term as used herein, is that the molecular formula is Na 2 CO 3 1.5H 2 o 2 Sodium carbonate peroxyhydrate is the name commonly used in the industry, and is often called PCS. Despite its wide range of uses due to its oxidizing and disinfectant properties, PCS is currently most widely used as a bleaching agent in detergent compositions, especially concentrated and super concentrated compositions that have been advocated by the detergent industry since the 1980s agent, or as a bleaching agent in dishwashing compositions or as a bleach additive, or as a bleaching agent in hard surface cleaning compositions. [0003] Sodium percarbonat...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Patents(China)
IPC IPC(8): C01B15/10C11D3/06C11D3/12C11D3/39C11D7/18
CPCC11D3/3942C11D3/128C01B15/103C11D3/39
Inventor A·P·杰梅斯G·R·霍尔内R·勒斯勒S·帕瓦内R·帕迪尼P·L·德里R·欧文L·斯诺里尼S·比吉尼U·德罗斯特M·马特斯
Owner 比利时索尔维因特罗斯公司
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products