CN205627606U - Nitrate water dealkalize jar - Google Patents
Nitrate water dealkalize jar Download PDFInfo
- Publication number
- CN205627606U CN205627606U CN201620272697.2U CN201620272697U CN205627606U CN 205627606 U CN205627606 U CN 205627606U CN 201620272697 U CN201620272697 U CN 201620272697U CN 205627606 U CN205627606 U CN 205627606U
- Authority
- CN
- China
- Prior art keywords
- pipe
- tank body
- dealkalize
- baffle
- flue gas
- 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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Abstract
The utility model discloses a nitrate water dealkalize jar, including a jar body, input tube, output tube, jar body top intercommunication has the pipe of discharging fume, the input tube communicates in the upper portion of the jar body, the intercommunication is gone up to the jar body has into tobacco pipe, advances to be equipped with the baffle between tobacco pipe and the input tube, evenly is provided with a plurality of through -holes on this baffle, the output tube communicates in the bottom of the jar body, is equipped with rear pump and filter on this output tube, the utility model discloses simple structure, convenient to use utilizes original out of use flue gas for save manufacturing cost during the bicarbonate radical of enterprise in getting rid of nitrate water, advancing to be equipped with the baffle between tobacco pipe and the input tube, evenly being provided with a plurality of through -holes on the baffle, nitrate water in getting into jar and the flue gas through -hole on by the baffle disperses for nitrate water and flue gas intensive mixing guarantee reaction.
Description
Technical field
This utility model relates to chemical machinery field, is specifically related to a kind of former glass gall dealkalize tank.
Background technology
Sodium sulfate, inorganic compound, it is bright that the anhydride that Disodium sulfate decahydrate has another name called Natrii Sulfas, high-purity, granule are thin is referred to as unit
Powder.Matrii Sulfas Exsiccatus, white, odorless, the crystallization having bitterness or powder, there is hygroscopicity.Profile be colourless, transparent, big crystallization or
The little crystallization of graininess.Dilute mainly for the manufacture of waterglass, glass, enamel, paper pulp, refrigeration intermixture, detergent, desiccant, dyestuff
Release agent, analytical chemistry reagent, pharmaceuticals, feedstuff etc..The mirabilite (mirabilite ore) of China is broadly divided into two kinds: a kind of for calcium awns
Nitre ore deposit；Another kind is NaCl type associated minerals, wherein, from the NaCl type associated minerals molten former glass gall adopted outside sulfuric acid sodium, also
Containing higher sodium chloride and a certain amount of sodium bicarbonate, these sodium bicarbonate may eventually form particulate matter, affect Matrii Sulfas Exsiccatus
Product quality so that by former glass gall sodium bicarbonate remove (mainly bicarbonate radical therein being removed), at present
The way of enterprise is that addition sulphuric acid, sulphuric acid and reaction of sodium bicarbonate generate sodium sulfate in former glass gall, needs every day to expend in a large number
Sulphuric acid, enterprise's manufacturing cost is bigger.It addition, Zhi Xiao enterprise uses evaporation according to salt made from earth containing a comparatively high percentage of sodium chloride saturation solubility with temperature relation feature
Separating out sodium sulfate and sodium chloride, need boiler to heat, the flue gas of burning contains sulfur dioxide, and flue gas needs to take off before discharging
Sulphuring treatment, and when flue gas is discharged, temperature is higher, can produce a certain degree of thermal pollution, cause energy waste.
Summary of the invention
The technical problems to be solved in the utility model is to provide a kind of former glass gall dealkalize tank, solves prior art at former nitre
In water, addition sulphuric acid dealkalize causes enterprise's manufacturing cost relatively big and flue gas needs to carry out temperature when desulfurization process and flue gas discharge
Spend the higher problem causing a certain degree of thermal pollution and cause energy waste.
This utility model is achieved through the following technical solutions:
A kind of former glass gall dealkalize tank, including tank body, input pipe, outlet tube, described tank body top is communicated with smoke exhaust pipe, described
Input pipe is communicated in the top of tank body, and described tank body is communicated with smoke-intake pipe, is provided with dividing plate between smoke-intake pipe and input pipe, should be every
Being evenly arranged with multiple through hole on plate, described outlet tube is communicated in the bottom of tank body, and this outlet tube is provided with rear pump and filtration
Device.
The further improvement project of this utility model is that described smoke-intake pipe is positioned at the lower section of input pipe.
This utility model further improvement project is, is communicated with many circulations between bottom and the top of described tank body
Pipe.
This utility model further improvement project is that described circulation pipe is provided with circulating pump.
This utility model compared with prior art, has the advantage that
1, this utility model simple in construction, easy to use, the former glass gall containing sodium bicarbonate is entered in tank body by input pipe,
Flue gas containing sulfur dioxide is entered in tank body by smoke-intake pipe, and sodium bicarbonate and sulfur dioxide react the bicarbonate in former glass gall
Root is removed, and the former glass gall after dealkalize is discharged by outlet tube by rear pump, and by the filter being located on outlet tube by flue gas
The particulate matter being dissolved in former glass gall is removed, and then the former glass gall of dealkalize carries out next process, by the most useless in entering evaporator
Flue gas utilizes so that enterprise saves production cost when removing the bicarbonate radical in former glass gall；
2, it is provided with dividing plate between smoke-intake pipe and input pipe, dividing plate is evenly arranged with multiple through hole, enter the former nitre in tank
Water is disperseed by the through hole on dividing plate with flue gas so that former glass gall is sufficiently mixed with flue gas, it is ensured that reaction is fully；
3, being communicated with many circulation pipes between bottom and the top of tank body, circulation pipe is provided with circulating pump, by tank base
Former glass gall be extracted into tank body top so that former glass gall is sufficiently mixed with flue gas, it is ensured that reaction abundant；
The temperature of the former glass gall 4, entering tank body is 30-40 DEG C, and the temperature of the flue gas entering tank body is about 120 DEG C, two
After person's hybrid reaction, the temperature of the former glass gall of dealkalize has risen, and a certain degree of subtract next procedure and adds the heat needed for pyrogen glass gall
Measure, and the temperature of the flue gas discharged has declined, and decreases thermal pollution, energy-saving and emission-reduction；
5, the calcium ions and magnesium ions in former glass gall is solidified by the carbon dioxide in flue gas, and is filtered by the filter on outlet tube,
Reduce the impurity in the sodium sulfate produced further, it is ensured that product quality.
With embodiment, this utility model is described further below in conjunction with the accompanying drawings.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the sectional view of Fig. 1.
Detailed description of the invention
As shown in Figures 1 and 2, this utility model includes tank body 01, input pipe 03, outlet tube 09, described tank body 01 top
Being communicated with smoke exhaust pipe 04, described input pipe 03 is communicated in the top of tank body 01, described tank body 01 is communicated with smoke-intake pipe 02, enters cigarette
Being provided with dividing plate 10 between pipe 02 and input pipe 03, this dividing plate 10 is evenly arranged with multiple through hole, described outlet tube 09 is communicated in
The bottom of tank body 01, this outlet tube 09 is provided with rear pump 07 and filter 08, and described smoke-intake pipe 02 is positioned at input pipe 03 time
Side, is communicated with many circulation pipes 05 between bottom and the top of described tank body 01, described circulation pipe 05 is provided with circulating pump 06.
It should be pointed out that, for those skilled in the art, without departing from this utility model principle
On the premise of, it is also possible to making some improvements and modifications, these improvements and modifications also should be regarded as protection domain of the present utility model.
Claims (4)
1. a former glass gall dealkalize tank, it is characterised in that: include tank body (01), input pipe (03), outlet tube (09), described tank body
(01) top is communicated with smoke exhaust pipe (04), and described input pipe (03) is communicated in the top of tank body (01), and described tank body connects on (01)
Being connected with smoke-intake pipe (02), be provided with dividing plate (10) between smoke-intake pipe (02) and input pipe (03), this dividing plate is evenly arranged with on (10)
Multiple through holes, described outlet tube (09) is communicated in the bottom of tank body (01), and this outlet tube (09) is provided with rear pump (07) and mistake
Filter (08).
One the most according to claim 1 former glass gall dealkalize tank, it is characterised in that: described smoke-intake pipe (02) is positioned at input pipe
(03) lower section.
One the most according to claim 1 former glass gall dealkalize tank, it is characterised in that: the bottom of described tank body (01) and top
Between be communicated with many circulation pipes (05).
One the most according to claim 3 former glass gall dealkalize tank, it is characterised in that: described circulation pipe (05) is provided with circulation
Pump (06).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620272697.2U CN205627606U (en) | 2016-04-05 | 2016-04-05 | Nitrate water dealkalize jar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620272697.2U CN205627606U (en) | 2016-04-05 | 2016-04-05 | Nitrate water dealkalize jar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205627606U true CN205627606U (en) | 2016-10-12 |
Family
ID=57067041
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620272697.2U Expired - Fee Related CN205627606U (en) | 2016-04-05 | 2016-04-05 | Nitrate water dealkalize jar |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205627606U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111646507A (en) * | 2020-06-11 | 2020-09-11 | 大冶市都鑫摩擦粉体有限公司 | Preparation device and method for antimony sulfide |
-
2016
- 2016-04-05 CN CN201620272697.2U patent/CN205627606U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111646507A (en) * | 2020-06-11 | 2020-09-11 | 大冶市都鑫摩擦粉体有限公司 | Preparation device and method for antimony sulfide |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161012 Termination date: 20170405 |