CN206731084U - Relieving haperacidity tank - Google Patents
Relieving haperacidity tank Download PDFInfo
- Publication number
- CN206731084U CN206731084U CN201720532618.1U CN201720532618U CN206731084U CN 206731084 U CN206731084 U CN 206731084U CN 201720532618 U CN201720532618 U CN 201720532618U CN 206731084 U CN206731084 U CN 206731084U
- Authority
- CN
- China
- Prior art keywords
- tank
- agitator disk
- relieving haperacidity
- electric machine
- tank body
- 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
Links
Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model provides a kind of relieving haperacidity tank,Including upper tank body and lower tank,The top and side of the upper tank body are respectively equipped with lead channel and breather pipe,The lead channel upper end is provided with and tightens lid,The lower end of the lead channel is provided with tank diameter,The outer wall of the tank diameter is provided with stirring motor,Agitating shaft is provided with the tank diameter,The agitating shaft is provided with multigroup agitating paddle,The middle part of the tank diameter is provided with agitator disk,The agitator disk is provided with stirring sheet,The lower end of the agitator disk is provided with rotary electric machine and guiding gutter,The rotary electric machine side is provided with fix bar,Mozzle is provided with the agitator disk,The mozzle is provided with magnetic valve,The bottom interior wall of the guiding gutter is provided with Filter column,The Filter column is provided with filter bores using sealing-top structure and upper end,The utility model passes through the stirring motor,The agitating paddle,The agitator disk,The rotary electric machine and stirring sheet design,Improve solution efficiency of the sulfur dioxide gas in ammoniacal liquor.
Description
Technical field
Relieving haperacidity technical field is the utility model is related to, more particularly to a kind of relieving haperacidity tank.
Background technology
Ammonium bisulfite (NH4HSO3) solution is a kind of important raw material of industry, it is to produce liquid sulfur dioxide, sodium hydrosulfite
With the raw material of sodium formaldehyde sulfoxylate, reducing agent is used as in pharmaceuticals industry, conventional preparation method is that sulfur dioxide gas is passed through in ammoniacal liquor
Body obtains, and ammonium bisulfite can be used for the synthesis of dyestuff intermediate, surfactant, pesticide herbicide, the reduction of pharmaceuticals industry
Agent, it may also be used for the protection of photosensitive industrial developing process.
Existing relieving haperacidity tank includes tank body, the feed tube on tank body and air inlet pipe, passes through feed tube and air inlet pipe point
Shu Song not be after ammoniacal liquor and sulfur dioxide gas, sulfur dioxide gas obtains bisulfite ammonium salt solution after being dissolved in ammoniacal liquor.
When existing relieving haperacidity tank makes bisulfite ammonium salt solution, dissolved efficiency of the sulfur dioxide gas in ammoniacal liquor is relatively low,
So that more sulfur dioxide gas is not dissolved the liquid level for just having discharged ammoniacal liquor in ammoniacal liquor, and then it result in titanium dioxide
The waste of sulphur gas increases production cost, and existing relieving haperacidity tank production efficiency is relatively low, and the dissolving of sulfur dioxide gas passes through
Cause the rate of dissolution of sulfur dioxide gas slower by the way of dissolving is stood so that the manufacturing process of bisulfite ammonium salt solution
Slowly.
Utility model content
Based on this, mesh of the present utility model is to provide a kind of dissolved efficiency high relieving haperacidity tank.
A kind of relieving haperacidity tank, for making bisulfite ammonium salt solution, including upper tank body and the lower tank that is connected with the upper tank body
Body, the top and side of the upper tank body are respectively equipped with lead channel and breather pipe, and the lead channel upper end is provided with and tightens lid, described
The lower end of lead channel is provided with tank diameter, and the gas outlet of the breather pipe is in the tank diameter；
The outer wall of the tank diameter is provided with stirring motor, is provided with the tank diameter and is stirred with what the stirring motor was connected
Axle is mixed, the agitating shaft is provided with multigroup agitating paddle, is provided with agitator disk in the middle part of the inwall of the tank diameter, is set on the agitator disk
There is stirring sheet, the lower end of the agitator disk is provided with rotary electric machine and guiding gutter, the rotary shaft of the rotary electric machine and the stirring
The bottom connection of disk, the rotary electric machine side are provided with fix bar, one end of the fix bar and the shell of the rotary electric machine
Connection, the other end are connected with the bottom surface of the agitator disk, are provided with mozzle in the agitator disk, the mozzle is provided with electromagnetism
Valve, the bottom interior wall of the guiding gutter are provided with Filter column, and the Filter column was provided with using sealing-top structure and upper end side
Filter opening, the filter bores are used to the bisulfite ammonium salt solution in the guiding gutter being guided in the lower tank.
Above-mentioned relieving haperacidity tank can be passed ammoniacal liquor and sulfur dioxide gas by the design of the lead channel and the breather pipe
Transport in the tank diameter, so that sulfur dioxide gas, which is dissolved into ammoniacal liquor, obtains bisulfite ammonium salt solution, tightened by described
The design of lid prevents dust to enter in the tank diameter, passes through the stirring motor, the agitating shaft and the agitating paddle
Design, dissolved efficiency of the sulfur dioxide gas in ammoniacal liquor is improved by the way of stirring and prevents sulfur dioxide gas
Waste, by the design of the agitator disk, the stirring sheet and the rotary electric machine, further improved by the way of stirring
Dissolved efficiency and speed of the sulfur dioxide gas in ammoniacal liquor so that improve the production efficiency of the relieving haperacidity tank, pass through institute
Stating the design of mozzle and the magnetic valve effectively can be delivered to the bisulfite ammonium salt solution being stirred in the tank diameter
, can be effectively to the sulfurous acid in the guiding gutter by the design of the Filter column and the filter bores in the guiding gutter
Hydrogen ammonium salt solution plays a role in filtering.
Further, the agitator disk is provided with temperature sensor, and the side wall of the upper tank body is provided with and the temperature
The display screen that sensor is electrically connected with.
Further, the bottom of the upper tank body is provided with fixed station, and the inwall of the fixed station is provided with thread groove, described
The top of lower tank is provided with the screw thread matched with the thread groove.
Further, the lead channel uses inverted cone-shaped structure with the guiding gutter.
Further, the radius of the agitator disk is less than the radius of the upper tank body.
Further, the inwall of the tank diameter is provided with zone of heating, and the zone of heating uses electric-heating-wire-heating structure.
Further, fixed column and observation window are respectively equipped with the top of the upper tank body and side outer wall.
Further, the agitating paddle uses arcuate structure.
Further, the top of the tank diameter is provided with filter layer.
Brief description of the drawings
Fig. 1 is the structural representation for the relieving haperacidity tank that the utility model first embodiment provides；
Fig. 2 is the structural representation of agitator disk in Fig. 1；
Fig. 3 is the structural representation of Filter column in Fig. 1；
Fig. 4 is the structural representation for the relieving haperacidity tank that the utility model second embodiment provides；
Essential element symbol description
| Relieving haperacidity tank | 100,100a | Upper tank body | 10 |
| Lead channel | 11 | Tighten lid | 111 |
| Zone of heating | 112 | Filter layer | 113 |
| Display screen | 114 | Fixed column | 115 |
| Observation window | 116 | Breather pipe | 12 |
| Tank diameter | 13 | Stirring motor | 131 |
| Agitating shaft | 132 | Agitating paddle | 133 |
| Agitator disk | 14 | Stirring sheet | 141 |
| Mozzle | 142 | Temperature sensor | 143 |
| Rotary electric machine | 15 | Rotary shaft | 151 |
| Fix bar | 152 | Guiding gutter | 16 |
| Filter column | 17 | Filter bores | 171 |
| Fixed station | 18 | Thread groove | 181 |
| Lower tank | 20 | Drain pipe | 22 |
Following embodiment will further illustrate the utility model with reference to above-mentioned accompanying drawing.
Embodiment
For the ease of more fully understanding the utility model, the utility model is carried out below in conjunction with related embodiment accompanying drawing
It is further explained.Give embodiment of the present utility model in accompanying drawing, but the utility model be not limited in it is above-mentioned preferred
Embodiment.Conversely, there is provided the purpose of these embodiments be in order that open face of the present utility model more fully.
Referring to Fig. 1, the utility model first embodiment provides a kind of relieving haperacidity tank 100, it is molten for making ammonium bisulfite
Liquid, including upper tank body 10 and the lower tank 20 that is connected with the upper tank body 10, the upper tank body 10 and the lower tank 20 are adopted
With cylindrical structural and radius it is equal, the top and side of the upper tank body 10 are respectively equipped with lead channel 11 and breather pipe 12, institute
The upper end of lead channel 11 is stated provided with lid 111 is tightened, described tighten uses screw connection structure between lid 111 and the lead channel 11,
The lid 111 of tightening is used to prevent dust from entering in the lead channel 11, and the lower end of the lead channel 11 is provided with tank diameter 13,
In the tank diameter 13, lead channel 11 described in the present embodiment is used to ammoniacal liquor being guided to for the gas outlet of the breather pipe 12
In the tank diameter 13, the breather pipe 12 is used to transmit sulfur dioxide gas to the tank diameter 13, so that titanium dioxide
Sulphur gas, which is dissolved in ammoniacal liquor, obtains bisulfite ammonium salt solution, and the outer wall of the tank diameter 13 is provided with stirring motor 131, described
Stirring motor 131 uses direct current generator, and the agitating shaft 132 being connected with the stirring motor 131, institute are provided with the tank diameter 13
State agitating shaft 132 and be provided with multigroup agitating paddle 133, the agitating shaft 132 passes through described in the rotation drive of the stirring motor 131
Agitating paddle 133 is stirred, can be right by the design of the stirring motor 131, the agitating shaft 132 and the agitating paddle 133
Ammoniacal liquor in the tank diameter 13 plays stirring action, and then improves dissolution rate of the sulfur dioxide gas in ammoniacal liquor, and prevents
Production cost has been saved in the waste of sulfur dioxide gas, and agitator disk 14 is provided with the middle part of the inwall of the tank diameter 13, described to stir
Mix disk 14 and use cylindrical structural, the solution that the agitator disk 14 is used for the bottom of tank diameter 13 is stirred, so as to enter one
Step improves the dissolved efficiency of sulfur dioxide gas.
Referring to Fig. 2, being the structural representation of agitator disk in Fig. 1 14, the agitator disk 14 is provided with multiple stirring sheets
141, using square structure and vertical with the agitator disk 14, the lower end of the agitator disk 14 is provided with rotation for the stirring sheet 141
Motor 15 and guiding gutter 16, the rotary electric machine 15 use direct current generator, and the rotary shaft 151 of the rotary electric machine 15 is stirred with described
The bottom connection of disk 14 is mixed, the rotary shaft 151 is used to drive the agitator disk 14 to enter by the rotation of the rotary electric machine 15
Row rotation, so that the stirring sheet 141 is stirred, and then improve dissolved efficiency of the sulfur dioxide gas in ammoniacal liquor and anti-
Stopped the waste of sulfur dioxide gas, the side of rotary electric machine 15 is provided with fix bar 152, one end of the fix bar 152 with
The cage connection of the rotary electric machine 15, the other end are connected with the bottom surface of the agitator disk 14, pass through setting for the fix bar 152
Meter, the stability of structure between the rotary electric machine 15 and the agitator disk 14 is improved, water conservancy diversion is provided with the agitator disk 14
Pipe 142, the mozzle 142 are provided with magnetic valve, and the bottom interior wall of the guiding gutter 16 is provided with Filter column 17, the electromagnetism
Valve is used for the on off state for controlling the mozzle 142, and the mozzle 142 is used for the bisulfite in the tank diameter 13
Ammonium salt solution is guided in the guiding gutter 16.
Referring to Fig. 3, being the structural representation of Filter column in Fig. 1 17, the Filter column 17 uses sealing-top structure and upper end
Side is provided with filter bores 171, and the filter bores 171 use ellipsoidal structure, passes through the sealing-top structure of the Filter column 17
Design so that contamination precipitation rises in the lower end of the Filter column 17, and then to the bisulfite ammonium salt solution in the guiding gutter 16
Arrived filtration, the bisulfite ammonium salt solution of free from admixture by the water conservancy diversion of filter bores 171 into the lower tank 20, institute
The bottom for stating lower tank 20 is provided with drain pipe 22, and the drain pipe 22 is used for the bisulfite ammonium salt solution in the lower tank 20
Export, so that operating personnel obtain bisulfite ammonium salt solution.
Temperature sensor 143 is additionally provided with agitator disk 14 described in the present embodiment, the side wall of the upper tank body 10 is provided with
The display screen 114 being electrically connected with the temperature sensor 143, the display screen 114 are used to feel the temperature sensor 143
The temperature that should be arrived is shown, so as to which the temperature information of the bisulfite ammonium salt solution in the tank diameter 13 is shown into operator
Member sees that the bottom of the upper tank body 10 is additionally provided with fixed station 18, and the fixed station 18 uses ladder structure of right angle, the fixed station
18 inwall is provided with thread groove 181, and the top of the lower tank 20 is provided with the screw thread matched with the thread groove 181, so that
Connected between the upper tank body 10 and the lower tank 20 by the way of being screwed, the lead channel 11 and the guiding gutter
16 use inverted cone-shaped structure, and then facilitate the transmission of ammoniacal liquor and bisulfite ammonium salt solution, improve the relieving haperacidity tank 100
Production efficiency.
The radius of the agitator disk 14 is less than the radius of the upper tank body 10, it is therefore prevented that the agitator disk 14 and the upper tank
Collided between the inwall of body 10, and then improve the stability of structure between the agitator disk 14 and the upper tank body 10, institute
State and fixed column 115 and observation window 116 are respectively equipped with the top and side outer wall of upper tank body 10, the fixed column 115 is used for outer
Portion's support fixes the upper tank body 10, so that the upper tank body 10 when the rotary electric machine 15 and the stirring motor 131 work
Balance is kept, and then improves the stability of the structure of relieving haperacidity tank 100, the observation window 116 is used to facilitate operating personnel couple
The condition of production of bisulfite ammonium salt solution in the tank diameter 13 is understood, to facilitate operating personnel to sulfur dioxide gas
Importing control, the agitating paddle 133 uses arcuate structure, and the top of the tank diameter 13 is provided with filter layer 113, passes through institute
The design for stating filter layer 113 serves filtration to importing the ammoniacal liquor in the tank diameter 13.
The utility model, can be by ammoniacal liquor and sulfur dioxide gas by the design of the lead channel 11 and the breather pipe 12
Body is transmitted to the tank diameter 13, so that sulfur dioxide gas, which is dissolved into ammoniacal liquor, obtains bisulfite ammonium salt solution, passes through institute
State and tighten the design of lid 111 and prevent dust to enter in the tank diameter 13, pass through the stirring motor 131, the stirring
The design of axle 132 and the agitating paddle 133, dissolved efficiency of the sulfur dioxide gas in ammoniacal liquor is improved by the way of stirring
And the waste of sulfur dioxide gas is prevented, pass through setting for the agitator disk 14, the stirring sheet 141 and the rotary electric machine 15
Meter, further increases dissolved efficiency of the sulfur dioxide gas in ammoniacal liquor so that improve the system by the way of stirring
The production efficiency of sour tank 100, can be effectively by the tank diameter 13 by the design of the mozzle 142 and the magnetic valve
The bisulfite ammonium salt solution being stirred is delivered in the guiding gutter 16, passes through the Filter column 17 and the filter bores 171
Design, effectively can play a role in filtering to the bisulfite ammonium salt solution in the guiding gutter 16.
Referring to Fig. 4, the relieving haperacidity tank 100a provided for the utility model second embodiment structural representation, second reality
It is more or less the same to apply the structure of example and first embodiment, its difference is that the inwall of tank diameter 13 described in the present embodiment is provided with
Zone of heating 112, the zone of heating 112 use electric-heating-wire-heating structure.
The present embodiment can play heat effect by the design of the zone of heating 112 to the ammoniacal liquor in the tank diameter 13,
To accelerate the solution speeds of sulfur dioxide gas, and then improve the production efficiency of the relieving haperacidity tank 100a.
Above embodiment described technical principle of the present utility model, these descriptions are intended merely to explain of the present utility model
Principle, and the limitation of scope of protection of the utility model can not be construed in any way.Based on explanation herein, the skill of this area
Art personnel, which would not require any inventive effort, can associate other embodiments of the present utility model, and these modes are all
It will fall into the scope of protection of the utility model.
Claims (9)
- A kind of 1. relieving haperacidity tank, for making bisulfite ammonium salt solution, it is characterised in that：Connect including upper tank body and with the upper tank body The lower tank connect, the top and side of the upper tank body are respectively equipped with lead channel and breather pipe, and the lead channel upper end, which is provided with, twists Tight lid, the lower end of the lead channel are provided with tank diameter, and the gas outlet of the breather pipe is in the tank diameter；The outer wall of the tank diameter is provided with stirring motor, and the stirring being connected with the stirring motor is provided with the tank diameter Axle, the agitating shaft are provided with multigroup agitating paddle, are provided with agitator disk in the middle part of the inwall of the tank diameter, the agitator disk is provided with Stirring sheet, the lower end of the agitator disk are provided with rotary electric machine and guiding gutter, the rotary shaft of the rotary electric machine and the agitator disk Bottom connection, the rotary electric machine side is provided with fix bar, one end of the fix bar and the shell company of the rotary electric machine Connect, the other end is connected with the bottom surface of the agitator disk, is provided with mozzle in the agitator disk, the mozzle is provided with electromagnetism Valve, the bottom interior wall of the guiding gutter are provided with Filter column, and the Filter column was provided with using sealing-top structure and upper end side Filter opening, the filter bores are used to the bisulfite ammonium salt solution in the guiding gutter being guided in the lower tank.
- 2. relieving haperacidity tank according to claim 1, it is characterised in that：The agitator disk is provided with temperature sensor, it is described on The side wall of tank body is provided with the display screen being electrically connected with the temperature sensor.
- 3. relieving haperacidity tank according to claim 1, it is characterised in that：The bottom of the upper tank body is provided with fixed station, described solid The inwall for determining platform is provided with thread groove, and the top of the lower tank is provided with the screw thread matched with the thread groove.
- 4. relieving haperacidity tank according to claim 1, it is characterised in that：The lead channel uses back taper with the guiding gutter Structure.
- 5. relieving haperacidity tank according to claim 1, it is characterised in that：The radius of the agitator disk is less than the half of the upper tank body Footpath.
- 6. relieving haperacidity tank according to claim 1, it is characterised in that：The inwall of the tank diameter is provided with zone of heating, described Zone of heating uses electric-heating-wire-heating structure.
- 7. relieving haperacidity tank according to claim 1, it is characterised in that：Set respectively on the top of the upper tank body and side outer wall There are fixed column and observation window.
- 8. relieving haperacidity tank according to claim 1, it is characterised in that：The agitating paddle uses arcuate structure.
- 9. relieving haperacidity tank according to claim 1, it is characterised in that：The top of the tank diameter is provided with filter layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720532618.1U CN206731084U (en) | 2017-05-15 | 2017-05-15 | Relieving haperacidity tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720532618.1U CN206731084U (en) | 2017-05-15 | 2017-05-15 | Relieving haperacidity tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206731084U true CN206731084U (en) | 2017-12-12 |
Family
ID=60565444
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720532618.1U Expired - Fee Related CN206731084U (en) | 2017-05-15 | 2017-05-15 | Relieving haperacidity tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206731084U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113620437A (en) * | 2020-05-09 | 2021-11-09 | 无锡博泛特工程设备有限公司 | Carbon dioxide waste water reduces hardness processing system |
-
2017
- 2017-05-15 CN CN201720532618.1U patent/CN206731084U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113620437A (en) * | 2020-05-09 | 2021-11-09 | 无锡博泛特工程设备有限公司 | Carbon dioxide waste water reduces hardness processing system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206731084U (en) | Relieving haperacidity tank | |
| CN209530490U (en) | A kind of flue gas desulfurizer | |
| CN207929401U (en) | A kind of zinc tail stirring means for feeding acid | |
| CN206793616U (en) | A kind of solid-liquid reaction kettle | |
| CN206951049U (en) | Chemicals dosing plant | |
| CN107739325A (en) | A kind of equipment and technique of continuous production vulcanization of rubber accelerant disulfide tetra methylthiuram | |
| CN205392308U (en) | Efflux mixing system | |
| CN210656319U (en) | Spiral fenton oxidation tower | |
| CN106984216A (en) | A kind of new preliming tank agitating device | |
| CN110743476B (en) | Multifunctional calcium hydroxide preparation tank and preparation method | |
| CN216024773U (en) | Automatic mixing system based on micro-interface mixing tank | |
| CN206666209U (en) | PH value adjustment equipment is used in ammonia nitrogen waste water processing | |
| CN209155170U (en) | A kind of rapid crystallization equipment of potassium fluotitanate | |
| CN108530291A (en) | A kind of continuous acidolysis method of calcium hydrogen citrate | |
| CN107673311A (en) | A kind of continuous device and method for preparing the high-concentrated sodium hypochlorite aqueous solution | |
| CN209451823U (en) | A kind of agitating device of electroplated heavy metals chelating agent | |
| CN207734989U (en) | Neutralization device for anhydrous sodium sulfite production | |
| CN206965904U (en) | One kind uses flue gas during smelting innoxious governance cyanogen-containing tailing system | |
| CN106396187A (en) | Cyanide wastewater treating and recycling method | |
| CN205500914U (en) | Improvement type inner loop anaerobic reactor | |
| CN206157210U (en) | Whole zero release metallurgical process's of tungstenic mineral intermediate product preparation system | |
| CN110386686A (en) | Hydrogen fluoride wastewater treatment production line | |
| CN209464884U (en) | A kind of dilution kettle that flow rate of liquid is controllable | |
| CN205340818U (en) | Production intermediate's reaction kettle device | |
| CN215855304U (en) | Industrial wastewater pH adjusting system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171212 Termination date: 20210515 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |