CN201990499U - Calcium chloride reactor - Google Patents
Calcium chloride reactor Download PDFInfo
- Publication number
- CN201990499U CN201990499U CN2011201221499U CN201120122149U CN201990499U CN 201990499 U CN201990499 U CN 201990499U CN 2011201221499 U CN2011201221499 U CN 2011201221499U CN 201120122149 U CN201120122149 U CN 201120122149U CN 201990499 U CN201990499 U CN 201990499U
- Authority
- CN
- China
- Prior art keywords
- tube body
- calcium chloride
- shell
- liquid discharge
- hydrochloric acid
- 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
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- Y02P20/121—
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- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
The utility model relates to a calcium chloride reactor which is characterized by comprising an upper tube body, a conical tube body, a lower tube body, a deslagging butterfly valve, a hydrochloric acid feeding tube, a filter cartridge, a liquid discharge tube, a limestone silo, a planetary feeder, a feeding groove and an exhaust pipe; the lower end of the upper tube body is provided with the conical tube body; the lower tube body is arranged below the conical tube body; the bottom of the lower tube body is provided with the deslagging butterfly valve; the lower end of the lower tube body is provided with the hydrochloric acid feeding tube; the middle part of the upper tube body is provided with the liquid discharge tube; the upper end of the upper tube body is provided with the feeding groove; and the upper end of the feeding groove is provided with the limestone silo. The continuous production of calcium chloride is realized, so that the automatic control of equipment is easier, and the large-scale production is easy; and complicated stirring equipment is omitted, carbon dioxide generate in a reaction process is used for stirring, so that extra stirring equipment does not need to be added, a lot of electricity is saved, and energy is saved while the production cost is reduced.
Description
Technical field
The utility model relates to a kind of calcium chloride reactor, belongs to the chemical industry equipment field.
Background technology
In traditional in the past calcium chloride reaction process; all be to use reactor to finish; hydrochloric acid and lime carbonate are added in the reactor; after finishing, reaction again finished fluid is emitted; just limit reaction process so virtually and be interrupted reaction; be consumes energy like this, lavish labor on again that production efficiency is low simultaneously; to realizing very unfavorable of automatically control and streamlined operation; also be difficult to accomplish scale production, and use reactor production, long reaction time; interruptedization production; the carbonic acid gas that produces in the feasible recovery reaction process is difficulty very, and some carbonic acid gas must be discharged in the atmosphere, and this has just caused the pollution to environment; also caused simultaneously the waste of raw material; and use reactor to produce calcium chloride, the electric energy that whipping device consumed of reactor also is very big, because all will prepare agitator motor in most of reactor.
The utility model content
According to the deficiencies in the prior art, technical problem to be solved in the utility model is: a kind of calcium chloride reactor is provided, realizes the serialization production of calcium chloride, utilize atmospheric carbon dioxide to stir, need not to add extra whipping device.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of calcium chloride reactor is provided, it is characterized in that comprising: upper shell, vertebra type tube body, lower shell, the deslagging butterfly valve, the hydrochloric acid feed-pipe, filter cylinder, liquid discharge pipe, the Wingdale feed bin, the planet feeder, intake chute and vapor pipe, vertebra type tube body is installed in the upper shell lower end, under the conical shell lower shell is installed, the lower shell bottom is equipped with the deslagging butterfly valve, the lower shell lower end is provided with the hydrochloric acid feed-pipe, the upper shell middle part is provided with liquid discharge pipe, the upper shell upper end is equipped with intake chute, and the intake chute upper end is equipped with the Wingdale feed bin.
Described liquid discharge pipe is equipped with filter cylinder at the intravital port of top cylinder.
The planet feeder is installed between described intake chute and the Wingdale feed bin.
Described vertebra type tube body upper end diameter and upper shell coupling, lower end diameter and lower shell coupling.
Wherein vertebra type tube volume surrounding is a carbon steel, and inner lining glass fiber reinforced plastic, lower shell then are borosilicate glass tube.
During use, lime carbonate enters upper shell by the Wingdale feed bin through star feeder and intake chute, arrive lower shell through the body drop of vertebra type tube then, constantly pile up, hydrochloric acid is then by the hydrochloric acid feed-pipe of lower end, enter by the lower shell lower end, hydrochloric acid after entering reacts with lime carbonate, obtain calcium chloride solution, above calcium chloride solution is pressed onto by top lime carbonate solid, when liquid level arrives liquid discharge pipe, calcium chloride solution is through the filter cylinder of liquid discharge pipe port, discharged by liquid discharge pipe then, this reaction unit need not additionally to add whipping appts, and the carbonic acid gas that produces in the reaction process stirs, make it rapid reaction, the carbonic acid gas of Chan Shenging is discharged by the vertical vapor pipe of upper shell subsequently, and the residue of Chan Shenging is discharged by the deslagging butterfly valve at last, and the hydrochloric acid feed-pipe is in the bottom, such setting can be so that lime carbonate fully reacts, lime carbonate that be not easy to react or sedimentary, more down the concentration of hydrochloric acid is just big more, can make that lime carbonate fully reacts.
The beneficial effects of the utility model are:
(1) this equipment has overcome most of problem, has realized the serialization production of calcium chloride;
(2) production of calcium chloride has realized serialization, makes the automatization control of equipment be more prone to, and is easy to the production of extensiveization;
(3) deducted complicated whipping device in this equipment, stirred by the carbonic acid gas that generates in the reaction process, need not increases extra whipping device, has saved a large amount of electric energy, when reducing production cost, has also saved the energy.
Description of drawings
Fig. 1 is the utility model structural representation;
1 is upper shell among the figure; 2 is vertebra type tube body; 3 is lower shell; 4 is the deslagging butterfly valve; 5 is the hydrochloric acid feed-pipe; 6 is filter cylinder; 7 is liquid discharge pipe; 8 is the Wingdale feed bin; 9 is the planet feeder; 10 is intake chute; 11 is vapor pipe.
Embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is described further:
As described in Figure 1, the utility model comprises: upper shell 1, vertebra type tube body 2, lower shell 3, deslagging butterfly valve 4, hydrochloric acid feed-pipe 5, filter cylinder 6, liquid discharge pipe 7, Wingdale feed bin 8, planet feeder 9, intake chute 10 and vapor pipe 11, vertebra type tube body 2 is installed in upper shell 1 lower end, conical shell is equipped with lower shell 32 times, lower shell 3 bottoms are equipped with deslagging butterfly valve 4, lower shell 3 lower ends are provided with hydrochloric acid feed-pipe 5, upper shell 1 middle part is provided with liquid discharge pipe 7, upper shell 1 upper end is equipped with intake chute 10, and intake chute 10 upper ends are equipped with Wingdale feed bin 8.
The port of liquid discharge pipe 7 in upper shell 1 is equipped with filter cylinder 6.
Planet feeder 9 is installed between intake chute 10 and the Wingdale feed bin 8.
Vertebra type tube body 2 upper end diameter and upper shell 1 coupling, lower end diameter and lower shell 3 couplings.
Vertebra type tube volume surrounding is a carbon steel in the present embodiment, and inner lining glass fiber reinforced plastic, lower shell then are borosilicate glass tube.
During use, lime carbonate enters upper shell 1 by Wingdale feed bin 8 through star feeder 9 and intake chute 10, fall lower shell 3 through vertebra type tube body 2 then, constantly pile up, hydrochloric acid is then by the hydrochloric acid feed-pipe 5 of lower end, enter by lower shell 3 lower ends, hydrochloric acid after entering reacts with lime carbonate, obtain calcium chloride solution, above calcium chloride solution is pressed onto by top lime carbonate solid, when liquid level arrives liquid discharge pipe 7, calcium chloride solution is through the filter cylinder 6 of liquid discharge pipe port, discharged by liquid discharge pipe 7 then, this reaction unit need not additionally to add whipping appts, and the carbonic acid gas that produces in the reaction process stirs, make it rapid reaction, the carbonic acid gas of Chan Shenging is discharged by upper shell 1 vertical vapor pipe 11 subsequently, and the residue of Chan Shenging is discharged by deslagging butterfly valve 4 at last, and hydrochloric acid feed-pipe 5 is in the bottom, such setting can be so that lime carbonate fully reacts, lime carbonate that be not easy to react or sedimentary, more down the concentration of hydrochloric acid is just big more, can make that lime carbonate fully reacts.
Claims (4)
1. calcium chloride reactor, it is characterized in that comprising: upper shell (1), vertebra type tube body (2), lower shell (3), deslagging butterfly valve (4), hydrochloric acid feed-pipe (5), filter cylinder (6), liquid discharge pipe (7), Wingdale feed bin (8), planet feeder (9), intake chute (10) and vapor pipe (11), vertebra type tube body (2) is installed in upper shell (1) lower end, lower shell (3) is installed under the conical shell (2), lower shell (3) bottom is equipped with deslagging butterfly valve (4), lower shell (3) lower end is provided with hydrochloric acid feed-pipe (5), upper shell (1) middle part is provided with liquid discharge pipe (7), upper shell (1) upper end is equipped with intake chute (10), and intake chute (10) upper end is equipped with Wingdale feed bin (8).
2. according to right ball 1 described calcium chloride reactor, it is characterized in that the port of described liquid discharge pipe (7) in upper shell (1) is equipped with filter cylinder (6).
3. according to right ball 1 described calcium chloride reactor, it is characterized in that installing between described intake chute (10) and the Wingdale feed bin (8) planet feeder (9).
4. according to right ball 1 described calcium chloride reactor, it is characterized in that described vertebra type tube body (2) upper end diameter and upper shell (1) coupling, lower end diameter and lower shell (3) coupling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201221499U CN201990499U (en) | 2011-04-22 | 2011-04-22 | Calcium chloride reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201221499U CN201990499U (en) | 2011-04-22 | 2011-04-22 | Calcium chloride reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201990499U true CN201990499U (en) | 2011-09-28 |
Family
ID=44666993
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201221499U Expired - Fee Related CN201990499U (en) | 2011-04-22 | 2011-04-22 | Calcium chloride reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201990499U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102745731A (en) * | 2011-04-22 | 2012-10-24 | 山东众诚钡盐股份有限公司 | Calcium chloride reactor |
-
2011
- 2011-04-22 CN CN2011201221499U patent/CN201990499U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102745731A (en) * | 2011-04-22 | 2012-10-24 | 山东众诚钡盐股份有限公司 | Calcium chloride reactor |
| CN102745731B (en) * | 2011-04-22 | 2015-07-15 | 山东众诚钡盐股份有限公司 | Calcium chloride reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20130702 Granted publication date: 20110928 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20140102 Granted publication date: 20110928 |
|
| PP01 | Preservation of patent right |
Effective date of registration: 20140102 Granted publication date: 20110928 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20150102 Granted publication date: 20110928 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110928 Termination date: 20140422 |
|
| EXPY | Termination of patent right or utility model |