CN209155560U - It is a kind of industry zinc oxide preparation in sulfuric acid thinning tank - Google Patents

It is a kind of industry zinc oxide preparation in sulfuric acid thinning tank Download PDF

Info

Publication number
CN209155560U
CN209155560U CN201821941435.6U CN201821941435U CN209155560U CN 209155560 U CN209155560 U CN 209155560U CN 201821941435 U CN201821941435 U CN 201821941435U CN 209155560 U CN209155560 U CN 209155560U
Authority
CN
China
Prior art keywords
sulfuric acid
tank
zinc oxide
dilution
water
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
Application number
CN201821941435.6U
Other languages
Chinese (zh)
Inventor
齐磊
王东
苗祯
白金聪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Jiyuan City Turner Rice Materials Co Ltd
Original Assignee
Shandong Jiyuan City Turner Rice Materials Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shandong Jiyuan City Turner Rice Materials Co Ltd filed Critical Shandong Jiyuan City Turner Rice Materials Co Ltd
Priority to CN201821941435.6U priority Critical patent/CN209155560U/en
Application granted granted Critical
Publication of CN209155560U publication Critical patent/CN209155560U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The application belongs to nano zine oxide preparation technical field, and in particular to it is a kind of industry zinc oxide preparation in sulfuric acid thinning tank.The dilution tank is integrally conical, and is two layer composite structure;Specifically: the formed cavity of tank body endothecium structure for dilute sulphuric acid use, bottom be equipped be used to discharge dilution after sulfuric acid delivery pipe;Tank body layer structure bottom is equipped with water inlet, and it is cavity structure among layer structure and endothecium structure that top, which is equipped with water outlet,.In the application, by being two-layer composite by tank design, on the one hand discharged heat in sulfuric acid dilution can be absorbed in favor of the industrial water that outer layer cavity is passed through, and fast cooling, on the other hand, other subsequent technological reaction water demand for heat can be reduced, to reduce demand for heat, and then reach energy-saving and emission-reduction purpose.The sulfuric acid thinning tank of the application, structure design is relatively reasonable, can establish certain basis for zinc oxide preparation process process optimization, reduction energy consumption.

Description

It is a kind of industry zinc oxide preparation in sulfuric acid thinning tank
Technical field
The application belongs to nano zine oxide preparation technical field, and in particular to it is a kind of industry zinc oxide preparation in sulfuric acid it is dilute Release tank.
Background technique
Zinc oxide, especially high-activity nano zinc oxide be widely used in chemical industry, electronics, biology, coating, ink, papermaking, The fields such as chemical fibre, rubber are a kind of important raw materials for production.In existing industrialized nano zinc oxide preparation process, with Whote-wet method Preparation process is more mature and application is more universal.Its technical process are as follows: with tutty or metallurgical works flue dust (zinc oxide content is 60% ~ 70%) does raw material, obtains by sulfuric acid to leach containing Fe2+、Mn2+Etc. foreign metal ions it is non-pure Net solution of zinc sulfate, then by once oxidation and displacement reaction (zinc powder reduction) being purified, with remove the copper in solution, The impurity elements such as iron, lead, manganese prepare basic zinc carbonate by reacting with soda ash after secondary oxidation, into one It can be obtained zinc oxide product after walking washed, drying and calcining.
In existing scale industrial production preparation process, the whole preparation process of zinc oxide can be generally divided into: leaching work Section, purification section neutralize several workshop sections such as workshop section, washing calcining workshop section, consequently facilitating production management, but due to different factories Production equipment type model involved by family and different workshop sections is more, and mostly big scale production equipment, therefore sets to existing production Standby and technique further improvement work more lacks, and it is larger to improve difficulty.And on the other hand, further to adapt to improve life The technical requirements for producing efficiency, reducing energy consumption and optimized production process and production environment still have existing equipment further Research and the necessity for improving promotion.
For the prior art, large-scale production needs are limited by, according to function difference, although in zinc oxide preparation process It is related to a variety of tank body equipments such as dissolving tank, reactor tank, but since its volume is larger (generally between several cubes to tens of cubes), Therefore this kind of equipment is generally mostly is directly welded using iron and steel material quality, and special construction design is had no, therefore subsequent is both needed to Certain structure of modification is carried out according to production is practical to meet production needs.And for specific dilute sulphuric acid thinning tank, generally And conventional can body is prepared, and has no special designing, but the amount of heat as involved in sulfuric acid dilution discharges, and dilute It releases rear sulfuric acid and is only cooled to after room temperature and just can enter subsequent leaching material technique, so that heat is a large amount of in sulfuric acid dilution Waste, while the time required to also extending preparing craft, thus pole it is necessary to targetedly for existing tank structure into The certain Curve guide impeller of row.
Summary of the invention
The application is designed to provide sulfuric acid thinning tank used in a kind of industrial zinc oxide preparation process, to be subsequent Certain Equipment Foundations are established in the optimization of associated production technique.
Details are as follows for the technical solution that the application is taken.
Sulfuric acid thinning tank in a kind of industry zinc oxide preparation, the dilution tank is integrally conical, compound for two layers Structure;Specifically:
Tank body endothecium structure formed cavity is still used to dilute sulphuric acid use, bottom is equipped be used to discharge dilution after sulfuric acid Delivery pipe;
Tank body layer structure bottom is equipped with water inlet, and it is empty among layer structure and endothecium structure that top, which is equipped with water outlet, Cavity configuration, for circulating and holding industrial water.
Specific design in use, water inlet front end should design inlet valve, and inlet valve front end be connected with into Water pump, to provide water inlet power, and design has flowing water Valve in water outlet rear end.It is to be understood that the design of intake is in tank Below body, so that water flow from bottom up flow process, is released so as to more adequately absorb in sulfuric acid dilution Thermal discharge.
The dilution tank material is irony or for the iron-based ferroalloy material for principal component.
In preferred design, the dilution tank body top edge, which offers, adjusts water pipe placement mouth, for placing adjusting water pipe, It places mouth openings of sizes and adjusts water pipe diameter and be adapted;Further, it is easy to place and be fixed on dilution to make to adjust water pipe Vessel edge is configured with fixed ring (that is, being configured with card at adjusting water pipe placement mouth sets adjusting water pipe adjusting water pipe port Fixed ring);
The fixed ring is two openable and closable semicircle annulus, and semicircle annulus, which can be arranged in, to be placed at mouth, while two Inner cavity after a semicircle annulus merges directly is slightly less than and adjusts water pipe outer diameter, sets and fixed function to play card;Specifically set In meter, two semicircle annulus can be attached in connecting pin by spring or pin shaft inserting mode, consequently facilitating fixed ring Folding.
In the prior art, in zinc oxide entirety preparation process, generality operation be first by after diluting concentrated sulfuric acid, then plus The raw materials for production (secondary zinc powder) for entering butt are leached, therefore sulfuric acid dilution early period can be related to amount of heat release.In and It is often necessary to ensure that certain reaction temperature could preferably ensure reaction process again with workshop section, therefore faces again and centainly use heat demand.
In the application, by being two-layer composite by tank design, on the one hand it can be passed through in favor of outer layer cavity Industrial water absorbs discharged heat in sulfuric acid dilution, and on the other hand fast cooling it is anti-can to reduce other subsequent techniques Using water demand for heat, to reduce demand for heat, and then reach energy-saving and emission-reduction purpose.In general, provided herein Sulfuric acid thinning tank, structure design is relatively reasonable, can lay the foundation for zinc oxide preparation process process optimization, reduction energy consumption, because And there is certain practical value and promote and apply meaning.
Detailed description of the invention
Fig. 1 is sulfuric acid thinning tank structural schematic diagram provided herein;
Fig. 2 is thinning tank marginal texture schematic diagram;
Fig. 3 is fixed ring structural schematic diagram.
Specific embodiment
Explanation is further explained to the application below with reference to embodiment.
Embodiment
As shown in Figure 1, sulfuric acid thinning tank in industrial zinc oxide preparation provided herein, structure are integrally in cone Shape is two layer composite structure;It is described as follows.
The formed cavity 3 of tank body endothecium structure still be used to dilute sulphuric acid with (when dilution, first clear water is put into tank body, Be then pumped into the concentrated sulfuric acid, generally use horizontal sulfuric acid pump), bottom be equipped be used to discharge dilution after sulfuric acid delivery pipe 5.
Tank body layer structure bottom is equipped with water inlet 1, and top is equipped with water outlet 2, is among layer structure and endothecium structure Cavity structure 4, for flowing and holding industrial water.On the one hand the industrial water (clear water) being passed through is used to absorb sulfuric acid dilute Discharged heat during releasing makes it be quickly cooled down and then save the waiting time, on the other hand, can provide for subsequent reactions process Warm water with a certain amount of heat, to reduce demand for heat.
When specifically used design, water inlet front end should design inlet valve, and inlet valve front end be connected with into Water pump to provide water inlet power, and has flowing water Valve (inlet valve, flowing water Valve, intake pump, figure in the design of water outlet rear end In be not shown, conventional design).It is to be understood that water inlet 1 designs below tank body, so that water flow is past from bottom During upper flowing, so as to more adequately absorb discharged heat in sulfuric acid dilution.
The dilution tank material is irony or for the iron-based ferroalloy material for principal component.
In actual use and design process, (for example, accelerates dilution due to various reasons or need further to adjust sulphur The reasons such as acid concentration), it generally requires additionally to be put into clear water into tank body by adjusting water pipe in dilution top of the tank.And existing skill In art, when to thinning tank additional input clear water, often lacks certain fixed device, need worker is hand-held to adjust water pipe, and then give Production brings inconvenience.Therefore in preferred design, dilution tank body top edge, which offers, adjusts water pipe placement mouth (as shown in Figure 2), For placing adjusting water pipe, places mouth openings of sizes and adjusting water pipe diameter is adapted.
Further, it is easy to place and be fixed on dilution vessel edge to make to adjust water pipe, water pipe port is mating adjusting There is fixed ring;The fixed ring is two openable and closable semicircle annulus (as shown in figure 3, including semicircle annulus 6 and 8), partly Round annulus, which can be arranged in, to be placed at mouth (shown in Fig. 2), while the inner cavity after two semicircle annulus merging is directly slightly less than tune Water-saving pipe outside diameter is set and fixed function to play card;In specific design, two semicircle annulus can pass through at connecting pin 7 Spring or pin shaft inserting mode are attached, consequently facilitating the folding of fixed ring.
In general, it by above-mentioned optimization and adjustment for tank structure, for optimization zinc oxide production technology, reduces Reaction time and reduction energy consumption have certain productive value.

Claims (6)

1. sulfuric acid thinning tank in a kind of industry zinc oxide preparation, which is characterized in that the dilution tank is integrally conical, and is Two layer composite structure;Specifically:
The formed cavity of tank body endothecium structure for dilute sulphuric acid use, bottom be equipped be used to discharge dilution after sulfuric acid delivery pipe;
Tank body layer structure bottom is equipped with water inlet, and it is cavity knot among layer structure and endothecium structure that top, which is equipped with water outlet, Structure.
2. sulfuric acid thinning tank in the preparation of industry zinc oxide as described in claim 1, which is characterized in that water inlet Front-end Design has Inlet valve, and it is connected with intake pump in inlet valve front end, the design of water outlet rear end has flowing water Valve.
3. sulfuric acid thinning tank in the preparation of industry zinc oxide as described in claim 1, which is characterized in that the dilution tank material Matter is irony or for the iron-based ferroalloy material for principal component.
4. sulfuric acid thinning tank in the preparation of industry zinc oxide as described in claim 1, which is characterized in that the dilution tank top Portion's edge, which has, adjusts water pipe placement mouth.
5. sulfuric acid thinning tank in the preparation of industry zinc oxide as claimed in claim 4, which is characterized in that place mouth with water pipe is adjusted It is configured with card and sets the fixed ring for adjusting water pipe;The fixed ring is two openable and closable semicircle annulus, and semicircle annulus card is set At placement mouth.
6. sulfuric acid thinning tank in the preparation of industry zinc oxide as claimed in claim 5, which is characterized in that two semicircle annulus exist Connecting pin is attached by spring or pin shaft inserting mode.
CN201821941435.6U 2018-11-23 2018-11-23 It is a kind of industry zinc oxide preparation in sulfuric acid thinning tank Active CN209155560U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821941435.6U CN209155560U (en) 2018-11-23 2018-11-23 It is a kind of industry zinc oxide preparation in sulfuric acid thinning tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821941435.6U CN209155560U (en) 2018-11-23 2018-11-23 It is a kind of industry zinc oxide preparation in sulfuric acid thinning tank

Publications (1)

Publication Number Publication Date
CN209155560U true CN209155560U (en) 2019-07-26

Family

ID=67339721

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821941435.6U Active CN209155560U (en) 2018-11-23 2018-11-23 It is a kind of industry zinc oxide preparation in sulfuric acid thinning tank

Country Status (1)

Country Link
CN (1) CN209155560U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112604541A (en) * 2020-11-25 2021-04-06 河北超威电源有限公司 Preparation method of colloid acid for storage battery and special preparation device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112604541A (en) * 2020-11-25 2021-04-06 河北超威电源有限公司 Preparation method of colloid acid for storage battery and special preparation device
CN112604541B (en) * 2020-11-25 2023-02-07 河北超威电源有限公司 Preparation method of colloid acid for storage battery and special preparation device

Similar Documents

Publication Publication Date Title
CN103194768B (en) High ferro high-phosphorus manganese is utilized to prepare the method for electrolytic metal Mn
CN209155560U (en) It is a kind of industry zinc oxide preparation in sulfuric acid thinning tank
CN103374658A (en) Ultrafine lead oxide prepared from desulfurated lead plaster by means of three-stage process and method thereof
CN103000968B (en) A kind of waste lead acid battery lead cream desulfurization and transformation method
CN112723330A (en) Preparation method and application of iso-phospho-ferromanganese iron phosphate
CN106673064A (en) Method for producing ammonium paratungstate
CN108546826A (en) A kind of closed method stacked from thermal maturation pretreatment extraction vanadium from vanadium slag
CN208018345U (en) Lithium battery tertiary presoma dried dust recovery system
CN106566926A (en) Deironing device, and low-temperature continuous deironing method
CN110526284B (en) Preparation method of tetrabasic lead sulfate
CN210656319U (en) Spiral fenton oxidation tower
CN207619488U (en) Two-part calcining circulated in countercurrent leacher
CN209396901U (en) It is a kind of industry zinc oxide preparation in liquefied soak material system
CN209397246U (en) A kind of system of wet type enrichment titanium material
CN201990481U (en) Concentration device for dilute hydrochloric acid
CN212640582U (en) Alloy mineral air-compressing continuous feeding and equilibrium reaction device
CN209396900U (en) A kind of oxidation agent feeding device in industry zinc oxide preparation process
CN203728903U (en) Leaching system for preparing vanadium solution by quenching roasting clinker of vanadium slag
CN207749162U (en) A kind of zinc metal sheet displacement prepares the device of Spongy Cadmium
CN203613244U (en) Device for leaching black copper slag
CN209828753U (en) Liquid ammonia dilution system suitable for non ferrous metal hydrometallurgy
CN209464880U (en) A kind of raw material slurry system in industry zinc oxide preparation process
CN206970720U (en) A kind of electrolytic manganese production energy-saving device
CN206391958U (en) One kind is used for diluting concentrated sulfuric acid device
CN218345521U (en) Reduce extraction tank structure of phosphorite extraction hydrogen fluoride gas volume of spilling out

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Sulfuric acid dilution tank in industrial zinc oxide preparation

Effective date of registration: 20200330

Granted publication date: 20190726

Pledgee: Bank of China Limited by Share Ltd. Jiyuan branch

Pledgor: JIYUAN LUTAI NANO MATERIAL Co.,Ltd.

Registration number: Y2020980001138

PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20210304

Granted publication date: 20190726

Pledgee: Bank of China Limited by Share Ltd. Jiyuan branch

Pledgor: JIYUAN LUTAI NANO MATERIAL Co.,Ltd.

Registration number: Y2020980001138

PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: A kind of sulfuric acid dilution tank for industrial zinc oxide preparation

Effective date of registration: 20210305

Granted publication date: 20190726

Pledgee: Bank of China Limited by Share Ltd. Jiyuan branch

Pledgor: JIYUAN LUTAI NANO MATERIAL Co.,Ltd.

Registration number: Y2021980001473

PE01 Entry into force of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20220301

Granted publication date: 20190726

Pledgee: Bank of China Limited by Share Ltd. Jiyuan branch

Pledgor: JIYUAN LUTAI NANO MATERIAL CO.,LTD.

Registration number: Y2021980001473

PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Sulfuric acid dilution tank in industrialized zinc oxide preparation

Effective date of registration: 20220303

Granted publication date: 20190726

Pledgee: Bank of China Limited by Share Ltd. Jiyuan branch

Pledgor: JIYUAN LUTAI NANO MATERIAL CO.,LTD.

Registration number: Y2022980002093

PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20230112

Granted publication date: 20190726

Pledgee: Bank of China Limited by Share Ltd. Jiyuan branch

Pledgor: JIYUAN LUTAI NANO MATERIAL CO.,LTD.

Registration number: Y2022980002093