CN206428008U - A kind of process units for improving medicinal sodium bicarbonate product granularity - Google Patents
A kind of process units for improving medicinal sodium bicarbonate product granularity Download PDFInfo
- Publication number
- CN206428008U CN206428008U CN201720019246.2U CN201720019246U CN206428008U CN 206428008 U CN206428008 U CN 206428008U CN 201720019246 U CN201720019246 U CN 201720019246U CN 206428008 U CN206428008 U CN 206428008U
- Authority
- CN
- China
- Prior art keywords
- crystallization kettle
- dissolving tank
- sodium bicarbonate
- process units
- chuck
- 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.)
- Active
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model provides a kind of process units for improving medicinal sodium bicarbonate product granularity, the open dissolving tank of heating jacket and upper end is provided with including outside, heating jacket is connected with temperature controller, dissolving tank is connected with the charging aperture of crystallization kettle, and prefilter and transfering material pump are disposed between dissolving tank and crystallization kettle, crystallization kettle bottom discharge mouthful is connected by pipeline with centrifuge, and centrifugal pump is provided with pipeline;Chuck is provided with outside the crystallization kettle, inwall is provided with temperature sensor, is internally provided with above agitator, chuck and is provided with water inlet, lower section is provided with delivery port;Temperature sensor is connected with PLC, and PLC is connected with cooling water supply system.It is simple that the utility model significantly improves product cut size, low cost, technological operation.
Description
Technical field
The utility model belongs to a kind of process units of sodium acid carbonate, and in particular to one kind improves medicinal sodium bicarbonate product
The process units of granularity.
Background technology
Sodium acid carbonate is commonly referred to as sodium bicarbonate, also known as acid sodium carbonate, is also soda, baking soda, method alkali, roasting alkali, English
Title Sodium Bicarbonate, chemical molecular formula is NaHCO3, molecular weight 84.01, proportion 2.16 ~ 2.22, be white or
Opaque monoclinic system crystal, weak base, toxicity is smaller, nonflammable explosive, can be dissolved in water, but insoluble in alcohol.Its product point
For industrial, edible and medicinal three kinds of specifications.Sodium acid carbonate is one of important inorganic chemical product, it be widely used in chemical industry,
The various fields such as light industry, medicine, weaving and fine chemistry industry.
As a kind of important chemical products, many necks that sodium acid carbonate has been had been applied in the life such as medication chemistry
Domain.Expanding economy in the last few years, China has become one of important composition country of production sodium acid carbonate, has formed hundred so far
More than ten thousand tons of scale, the speedup of annual sodium bicarbonate yield occupies first place in the world, for many years always with every year on average 2% ~ 3% speed
Degree increases.
Crystallisation by cooling method is the existing main method for preparing medicinal sodium bicarbonate.Crystallizer is that the core of crystallisation by cooling method is set
It is standby, type, internal structure of crystallizer etc., can be directly connected to obtain satisfactory crystallization.The nucleation of crystallization and growth
It is not separate, but is mutually related, it is dynamic by crystalline material, nucleation kinetics, suspension fluid mechanical state, growth
The influence of the parameters such as mechanics, crystallization area, is a very complicated influence system.In order to obtain, particle size distribution characteristics are good, purity
High crystalline product, in crystallization process, need to control crystallization temperature, input concentration and mold liquid level height, to ensure
The stable operation in Metastable zone of degree of supersaturation in crystallization process, to prevent substantial amounts of two grades and primary nucleation, it is accordingly required in particular to control
Cooling curve in crystallization process processed.The natural cooling process not controlled, occurs degree of supersaturation peak value, no in the early stage of process
Occurs spontaneous nucleation with can avoiding, the deterioration for causing product grain size number to be distributed.
Utility model content
The utility model proposes that the purpose is to provide a kind of raising in order to overcome shortcoming present in prior art
The process units of medicinal sodium bicarbonate product granularity.
The technical solution of the utility model is:
A kind of process units for improving medicinal sodium bicarbonate product granularity, including outside is provided with heating jacket and upper end is spacious
Mouthful dissolving tank, heating jacket is connected with temperature controller, and dissolving tank is connected with the charging aperture of crystallization kettle, and dissolving tank and crystallization kettle it
Between be disposed with prefilter and transfering material pump, crystallization kettle bottom discharge mouthful is connected by pipeline with centrifuge, and is set on pipeline
It is equipped with centrifugal pump;Chuck is provided with outside the crystallization kettle, inwall is provided with temperature sensor, is internally provided with agitator, pressed from both sides
Set top is provided with water inlet, and lower section is provided with delivery port;Temperature sensor is connected with PLC, PLC and cooling
Water supply system is connected.
Angle is 45 ° between the axis of the charging aperture axis and delivery port.
The beneficial effects of the utility model are:
The utility model provide it is a kind of improve medicinal sodium bicarbonate granularity device, realized on the basis of recrystallization method with
Soda ash is that raw material continuously prepares granular-grade medicinal sodium bicarbonate product of the particle diameter in the mesh of 40 mesh ~ 80.With traditional processing technology phase
It is simple that product cut size, low cost, technological operation are significantly improved than, the technology.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the top view of crystallization kettle in the utility model.
Wherein:
The crystallization kettle of 1 dissolving tank 2
The PLC of 3 centrifuge 4
The transfering material pump of 5 temperature controller 6
The prefilter of 7 centrifugal pump 8
The chuck of 11 heating jacket 21
The water inlet of 22 charging aperture 23
The temperature sensor of 24 delivery port 25
The discharging opening of 26 agitator 27.
Embodiment
With reference to Figure of description and embodiment raising medicinal sodium bicarbonate product granularity a kind of to the utility model
Process units is described in detail:
As shown in Figure 1, 2, a kind of process units for improving medicinal sodium bicarbonate product granularity, including outside are provided with heating
The open dissolving tank 1 of chuck 11 and upper end, heating jacket 11 is connected with temperature controller 5, the charging aperture 22 of dissolving tank 1 and crystallization kettle 2
Connection, and prefilter 8 and transfering material pump 6 are disposed between dissolving tank 1 and crystallization kettle 2, the bottom discharge mouthful of crystallization kettle 2 27 leads to
Cross pipeline to connect with centrifuge 3, and centrifugal pump 7 is provided with pipeline;Chuck 21, inwall peace are provided with outside the crystallization kettle 2
Equipped with temperature sensor 25, agitator 26 is internally provided with, the top of chuck 21 is provided with water inlet 23, and lower section is provided with delivery port
24;Temperature sensor 25 is connected with PLC 4, and PLC 4 is connected with cooling water supply system.
Angle is 45 ° between the axis of the axis of charging aperture 22 and delivery port 24.
3000 mesh fine sand polishings have been carried out to crystallization kettle and annex.
Application method of the present utility model is:
Mother liquor is heated to 90 °C or so in dissolving tank 1, is proportionally added into sodium acid carbonate(The amount of reordering sodium carbonate when just starting),
It is prepared into sodium carbonate 12%, the thick alkali lye of sodium acid carbonate 13% or so, temperature control is at 90 °C, by transfering material pump 6 and prefilter 8
It is sent to crystallization kettle 2.Lead in the chuck 21 of crystallization kettle 2 under conditions of cooling water, control is entered with 4 ~ 10 °C of cooling rates per hour
Row sodium acid carbonate is crystallized, and crystallization operation is completed when reaching 30 ~ 40 °C to temperature of charge, and crystal solution is put into centrifuge 3 and carried out
Separation of solid and liquid, sodium acid carbonate is that drying is finished product, and mother liquor is returned for choline.PLC 4 is according on the inwall of crystallization kettle 2
The temperature that temperature sensor 25 feeds back, the control cooling water supply system supply cooling water of chuck 21.
The utility model effectively prevents product during the course of the reaction by the common-ion effect that produces between application raw material
Decompose, improve yield, reduce cost, realize that product granularity increases, bulky grain of the granularity between the mesh of 40 mesh ~ 80 can be reached
Sodium bicarbonate product, simple to operate, indices reach industry relevant criterion, and carbonic acid can be produced without using carbonators
Hydrogen sodium particle.
Claims (2)
1. a kind of process units for improving medicinal sodium bicarbonate product granularity, it is characterised in that:Outside is provided with heating folder
Set(11)And the open dissolving tank in upper end(1), heating jacket(11)With temperature controller(5)Connection, dissolving tank(1)With crystallization kettle(2)
Charging aperture(22)Connection, and dissolving tank(1)With crystallization kettle(2)Between be disposed with prefilter(8)And transfering material pump(6),
Crystallization kettle(2)Bottom discharge mouthful(27)Pass through pipeline and centrifuge(3)Connection, and centrifugal pump is provided with pipeline(7);The knot
Brilliant kettle(2)Outside is provided with chuck(21), inwall is provided with temperature sensor(25), it is internally provided with agitator(26), chuck
(21)Top is provided with water inlet(23), lower section is provided with delivery port(24);Temperature sensor(25)With PLC(4)Even
Connect, PLC(4)It is connected with cooling water supply system.
2. a kind of process units for improving medicinal sodium bicarbonate product granularity according to claim 1, it is characterised in that:Institute
State charging aperture(22)Axis and delivery port(24)Axis between angle be 45 °.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720019246.2U CN206428008U (en) | 2017-01-09 | 2017-01-09 | A kind of process units for improving medicinal sodium bicarbonate product granularity |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720019246.2U CN206428008U (en) | 2017-01-09 | 2017-01-09 | A kind of process units for improving medicinal sodium bicarbonate product granularity |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206428008U true CN206428008U (en) | 2017-08-22 |
Family
ID=59584743
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720019246.2U Active CN206428008U (en) | 2017-01-09 | 2017-01-09 | A kind of process units for improving medicinal sodium bicarbonate product granularity |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206428008U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109264746A (en) * | 2018-10-12 | 2019-01-25 | 河南精康制药有限公司 | A kind of preparation method of pharmaceutical grade sodium bicarbonate |
CN111994923A (en) * | 2020-08-28 | 2020-11-27 | 新兴凌云医药化工有限公司 | Production medicine level large granule sodium bicarbonate crystal system |
-
2017
- 2017-01-09 CN CN201720019246.2U patent/CN206428008U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109264746A (en) * | 2018-10-12 | 2019-01-25 | 河南精康制药有限公司 | A kind of preparation method of pharmaceutical grade sodium bicarbonate |
CN111994923A (en) * | 2020-08-28 | 2020-11-27 | 新兴凌云医药化工有限公司 | Production medicine level large granule sodium bicarbonate crystal system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109608372A (en) | A kind of multistage continuous crystallisation process of corynebacterium methionine crystal | |
CN104003445B (en) | A kind of method of producing high-dissolvability Ammonium Heptamolybdate | |
CN104788345B (en) | A kind of production method of high-purity hydrochloric acid metformin | |
CN102992957B (en) | Solvent-out crystallization method of erythritol | |
CN206428007U (en) | A kind of process units of granular-grade medicinal sodium bicarbonate | |
CN102580347B (en) | Continuous crystallization method of tetraacetylethylenediamine | |
CN206428008U (en) | A kind of process units for improving medicinal sodium bicarbonate product granularity | |
CN105771304A (en) | Double-effect countercurrent evaporation crystallization system for monosodium glutamate and working process thereof | |
CN102329212A (en) | Refining method for long-chain binary acid | |
CN101210256A (en) | Method for preparing maltitol | |
CN102894247B (en) | Technology for producing greasy crystallized honey | |
CN104261432A (en) | Production method of spherical edible refined salt | |
CN111909058A (en) | Production method for producing metformin hydrochloride | |
CN106987608B (en) | Dynamic crystallization method of calcium gluconate | |
WO2024119731A1 (en) | Preparation system and method for xylitol crystal | |
CN210711829U (en) | System for utilize citric acid gypsum production gypsum whisker | |
CN105671215B (en) | A kind of preparation method of monocrystalline fructose | |
CN109503441B (en) | Preparation method of high-content cysteamine hydrochloride | |
CN111518119B (en) | Continuous amoxicillin crystallization process | |
CN109400491B (en) | Crystallization preparation method of L-p-hydroxyphenylglycine methyl ester | |
CN103570783B (en) | Crystal transformation method for disodium guanylate | |
CN102633834A (en) | Continuous crystallizing method for acephate | |
CN116675644B (en) | Method for producing imidazole by step interactive cooling crystallization | |
CN202122849U (en) | Stirring propeller for pravastatin sodium salt crystallization process | |
CN101391967A (en) | Method for producing acrylic amide crystal |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder |
Address after: 300457 No. 5, 7th Street, Binhai New Area Development Zone, Tianjin Patentee after: Tianjin Haiguang Technology Development Co.,Ltd. Address before: 300457 No. 5, 7th Street, Binhai New Area Development Zone, Tianjin Patentee before: TIANJIN HAIGUANG PHARMACEUTICAL CO.,LTD. |
|
CP01 | Change in the name or title of a patent holder |