CN211733870U - Hydrocyclone separator for process for extracting chromium from chromium pollutants - Google Patents
Hydrocyclone separator for process for extracting chromium from chromium pollutants Download PDFInfo
- Publication number
- CN211733870U CN211733870U CN201921533959.6U CN201921533959U CN211733870U CN 211733870 U CN211733870 U CN 211733870U CN 201921533959 U CN201921533959 U CN 201921533959U CN 211733870 U CN211733870 U CN 211733870U
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- chromium
- baffle
- liquid outlet
- casing
- thick bamboo
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G37/00—Compounds of chromium
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/30—Obtaining chromium, molybdenum or tungsten
- C22B34/32—Obtaining chromium
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/006—Wet processes
- C22B7/007—Wet processes by acid leaching
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Metallurgy (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Treatment Of Sludge (AREA)
Abstract
The utility model belongs to the technical field of the chromium pollutant, concretely relates to draw hydrocyclone for technology of chromium in chromium pollutant, which comprises a motor, motor output shaft connects into a liquid section of thick bamboo, feed liquor section of thick bamboo upper portion is equipped with first liquid outlet, feed liquor section of thick bamboo overcoat is established and is leaked hopper-shaped casing, the big opening and the motor base fixed connection of casing, the little opening of casing is the slag notch, the lateral wall of casing still is equipped with second liquid outlet and inlet, the second liquid outlet is higher than the inlet, be equipped with in the casing and separate the baffle, it is located first liquid outlet and second liquid outlet below to separate the baffle, it is located the inlet top to separate the baffle, separate the baffle cover and locate into the liquid section of thick bamboo outside, feed liquor section of thick bamboo overcoat establishes the impeller, the impeller is located the inlet below, the utility model.
Description
Technical Field
The utility model belongs to the technical field of the chromium pollutant, concretely relates to draw hydrocyclone separator for technology of chromium in chromium pollutant.
Background
The chromium salt industry is an indispensable important industry in national economy and is mainly used for aspects of electroplating, tanning, printing and dyeing, medicines, catalysts, metal corrosion inhibition and the like. The main waste residue discharged in the production process of chromium salt (i.e. chromium slag) is a dangerous waste with high toxicity, wherein Cr is6+Is the source of toxicity. According to the analysis result of the chemical composition characteristics of partial chromium slag in China, the average content of total chromium in the chromium slag is about 3-5 percent, and the average content of hexavalent chromium is about 1-5 percent (all by Cr)2O3Meter). The chromium slag contains six components including Cr6+Sodium chromate tetrahydrate, calcium chromate aluminate and basic ferric chromate, calcium silicate-calcium chromate solid solution and calcium aluminoferrite-calcium chromate solid solution, respectively. Wherein the tetrahydrate sodium chromateAnd free calcium chromate is a water-soluble phase and is easily dissolved by surface water and rainwater; the other four components are difficult to dissolve in water, but are easy to cause medium and long-term environmental pollution caused by the chromium slag through weathering and hydration in the long-term open-air storage process.
The prior chromium slag detoxification method comprises the steps of separating chromium slag from waste water, reducing hexavalent chromium in the chromium slag into trivalent chromium, solidifying the trivalent chromium in waste slag, and then safely burying the waste slag.
Disclosure of Invention
An object of the utility model is to provide a hydrocyclone separator for technology with low costs, prevent blockking up, extract chromium in the efficient chromium pollutant.
Based on the purpose, the invention adopts the following technical scheme:
the utility model provides a draw hydrocyclone for technology of chromium in chromium pollutant, which comprises a motor, the motor output shaft connects the feed liquor section of thick bamboo, feed liquor section of thick bamboo upper portion is equipped with first liquid outlet, the feed liquor section of thick bamboo overcoat is established and is leaked hopper-shaped casing, the big opening and the motor base fixed connection of casing, the little opening of casing is the slag notch, the lateral wall of casing still is equipped with second liquid outlet and inlet, the second liquid outlet is higher than the inlet, be equipped with in the casing and separate the baffle, it is located first liquid outlet and second liquid outlet below to separate the baffle, it is located the inlet top to separate the baffle, it locates the feed liquor section of thick bamboo outside to separate the baffle cover, the impeller is established to feed liquor section of.
Furthermore, the baffle is annular, and the outer side edge of the baffle is fixedly connected with the inner side wall of the shell.
Furthermore, the impeller comprises a chassis, the chassis is provided with rotating blades, and a reinforcing rib is arranged between the chassis and the outer side wall of the liquid inlet cylinder.
The utility model discloses utilize the gravity of chromium sediment self, can also be fast with chromium sediment and waste water separation when using a small amount of power, the energy saving consumes, the utility model discloses when discharging the chromium sediment by the slag notch, because its waste water is in mobile state all the time, can prevent that the chromium sediment from blockking up at first liquid outlet, convenient to use, work efficiency is high.
Drawings
FIG. 1 is a schematic diagram of a dynamic hydrocyclone;
FIG. 2 is a schematic view of a liquid inlet cylinder
Fig. 3 is a schematic structural view of the impeller.
Detailed Description
As shown in fig. 1-3, the hydrocyclone for the process of extracting chromium from chromium contaminants includes a motor, a motor output shaft 101 is connected to a liquid inlet cylinder 2, a first liquid outlet 201 is disposed on an upper portion of the liquid inlet cylinder 2, a funnel-shaped casing 3 is sleeved outside the liquid inlet cylinder 2, a large opening of the casing 3 is fixedly connected to a base of the motor 1, a small opening of the casing 3 is a slag outlet 301, a second liquid outlet 302 and a liquid inlet 303 are further disposed on a side wall of the casing 3, the second liquid outlet 302 is higher than the liquid inlet 303, a separation baffle 4 is disposed in the casing 3, the separation baffle 4 is disposed below the first liquid outlet 201 and the second liquid outlet 302, the separation baffle 4 is disposed above the liquid inlet 303, the separation baffle 4 is sleeved outside the liquid inlet cylinder 2, an impeller 5 is sleeved on an outer lower portion of the liquid inlet cylinder 2. The baffle 4 is annular, and the outer side edge of the baffle 4 is fixedly connected with the inner side wall of the shell 3. The impeller 5 comprises a base plate 501, rotary blades 502 are arranged on the upper disc surface of the base plate 501, and reinforcing ribs are arranged between the base plate 501 and the outer side wall of the liquid inlet cylinder 2.
During the use, the chromium sediment after adding water gets into from inlet 303, and impeller 5 begins the stirring, and chromium sediment is because its self gravity is downward and discharge from slag notch 301, and liquid rotates along with the impeller and rotates the first liquid outlet 201 of rotatory liquid inlet 2 and discharges, arrives second liquid outlet 302 again and discharges.
Claims (3)
1. The utility model provides a hydrocyclone separator for technology of drawing chromium in chromium pollutant, a serial communication port, which comprises a motor, motor output shaft connects the feed liquor section of thick bamboo, feed liquor section of thick bamboo upper portion is equipped with first liquid outlet, feed liquor section of thick bamboo overcoat is established and is leaked hopper-shaped casing, the big opening and the motor base fixed connection of casing, the little opening of casing is the slag notch, the lateral wall of casing still is equipped with second liquid outlet and inlet, the second liquid outlet is higher than the inlet, be equipped with in the casing and separate the baffle, it is located first liquid outlet and second liquid outlet below to separate the baffle, it is located the inlet top to separate the baffle, it locates the feed liquor section of thick bamboo outside to separate the baffle cover, the impeller is established to feed liquor section of.
2. The hydrocyclone for extracting chromium from chromium pollutants according to claim 1, wherein the baffle is annular, and the outer edge of the baffle is fixedly connected with the inner side wall of the shell.
3. The hydrocyclone for the process of extracting chromium from chromium pollutants according to claim 1, wherein the impeller comprises a base plate, the base plate is provided with rotating blades, and reinforcing ribs are arranged between the base plate and the outer side wall of the liquid inlet cylinder.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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CN201910482407 | 2019-06-04 | ||
CN2019104824075 | 2019-06-04 |
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CN211733870U true CN211733870U (en) | 2020-10-23 |
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CN201910872380.0A Pending CN110526292A (en) | 2019-06-04 | 2019-09-16 | The technique of chromium is extracted in a kind of chromium pollutant |
CN201921533959.6U Active CN211733870U (en) | 2019-06-04 | 2019-09-16 | Hydrocyclone separator for process for extracting chromium from chromium pollutants |
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CN201910872380.0A Pending CN110526292A (en) | 2019-06-04 | 2019-09-16 | The technique of chromium is extracted in a kind of chromium pollutant |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110526292A (en) * | 2019-06-04 | 2019-12-03 | 河南金谷实业发展有限公司 | The technique of chromium is extracted in a kind of chromium pollutant |
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CN113772730B (en) * | 2021-10-08 | 2023-03-10 | 上海良仁化工有限公司 | Method for preparing chromium potassium sulfate from chromium-containing sludge |
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JPS5021992B1 (en) * | 1968-02-17 | 1975-07-26 | ||
CA1123788A (en) * | 1978-08-21 | 1982-05-18 | David L. Martin | Hydrocyclone underflow density control |
CA2042630A1 (en) * | 1990-09-27 | 1992-03-28 | Louis O. Torregrossa | Method and apparatus for beneficiating waste-waters |
CN1064933C (en) * | 1996-07-20 | 2001-04-25 | 南宁正宇高新技术有限责任公司 | Method for treating waste industrial water from light industry by using burning boiler |
CN101380510A (en) * | 2008-10-30 | 2009-03-11 | 杨恩清 | Chromic slag wet method detoxifcation and resource comprehensive utilization new technique |
CN103114036B (en) * | 2012-12-17 | 2014-06-25 | 陈喆 | Hydraulic cyclone anaerobic digestion tower and using method thereof |
CN103934256B (en) * | 2014-04-21 | 2019-06-04 | 江苏维尔利环保科技股份有限公司 | Chromium slag and wet method detoxifcation method containing chromium pollutant |
CN204148015U (en) * | 2014-08-25 | 2015-02-11 | 成浩 | A kind of cyclone hydraulic separators of modified form |
CN204685317U (en) * | 2015-05-18 | 2015-10-07 | 沈智奇 | Vane type cyclone separator |
CN106929679A (en) * | 2015-12-29 | 2017-07-07 | 核工业北京化工冶金研究院 | A kind of method that sulfuric acid neutrality leaching-reducing process processes chromium slag |
CN106622702A (en) * | 2017-03-17 | 2017-05-10 | 苏州海棠环保材料有限公司 | Method for improving separation efficiency of existing cyclone/hydrocyclone centrifugal separation equipment |
CN110526292A (en) * | 2019-06-04 | 2019-12-03 | 河南金谷实业发展有限公司 | The technique of chromium is extracted in a kind of chromium pollutant |
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2019
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110526292A (en) * | 2019-06-04 | 2019-12-03 | 河南金谷实业发展有限公司 | The technique of chromium is extracted in a kind of chromium pollutant |
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