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Continuous production process for polyaluminium chloride and production equipment

A technology of polyaluminum chloride and production equipment, which is applied in the directions of aluminum chloride, aluminum halide, flocculation/sedimentation water/sewage treatment, etc. High operational safety, low energy and material losses, improved mixing reaction conditions

Inactive Publication Date: 2010-11-03
广东慧信环保有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

No matter whether the PAC is produced in an open reaction tank or a kettle reactor, it is inconvenient to add solid raw materials. When the solid raw materials are added, the reaction with the acid is very violent, which may easily cause material spraying and cause safety accidents; In the follow-up process, the reaction product is extracted or placed from the reaction pool or reactor to make aluminum chloride better polymerized (cured), so it occupies a large area, takes a long time, and has low production efficiency; the production process of polyaluminum chloride is liquid , solid two-phase reaction, since the open reaction pool or tank reactor is used, the mixing effect of the reaction system is poor when the industrial scale-up is carried out. With the increase of the reactor volume, the energy consumption of mechanical stirring and the investment cost increase sharply
Moreover, the reaction temperature should be around 90-120°C, so it must be heated by boilers and other equipment during the production process, which not only increases infrastructure facilities, but also consumes a lot of energy. High production cost and low product market competitiveness affect the large-scale industrial production and application of the water purifier
[0005] Numerous documents have also carried out a large amount of reports to polyaluminum chloride production method and technique, but mainly propose new production method for raw material as CN1032150, CN1046512, CN1051541, CN1090555, CN1251824, CN1290656, CN1180661, CN1334241, CN1483675, CN1544348, CN1686813 etc.; To improve the performance of product polyaluminum chloride or improve the stripping rate of aluminum such as CN1205306, CN1381401, CN1718543, CN1865149, CN1948156, CN200978239 etc. for production process, and then lack report for the continuous production process of polyaluminum chloride

Method used

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  • Continuous production process for polyaluminium chloride and production equipment
  • Continuous production process for polyaluminium chloride and production equipment

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] According to the concentration of industrial concentrated hydrochloric acid, a certain amount of water (or waste acid) is added in proportion to the hydrochloric acid pool and mixed so that the concentration of HCl% in the hydrochloric acid is 14%, and it is used after stirring evenly.

[0033] Put calcium aluminate powder and water into the slurry mixer at a ratio of 7:3 (mass ratio) each time, stir until the slurry becomes paste, open the discharge door and put the slurry into the slurry funnel. After the slurry in the slurry mixer is completely put into the slurry funnel, add calcium aluminate powder and water in proportion in time to ensure that there is enough slurry in the slurry funnel to be continuously pumped into the reaction kettle.

[0034] Use the hydrochloric acid metering pump to pump hydrochloric acid at 800L / h and the slurry metering pump to pump the slurry at a speed of 148L / h into the reaction kettle at the same time, control the stirring speed at 63rp...

Embodiment 2

[0036]According to the concentration of industrial concentrated hydrochloric acid, a certain amount of water (or waste acid) is added in proportion to the hydrochloric acid pool and mixed so that the concentration of HCl% in the hydrochloric acid is 16%, and it is used after stirring evenly.

[0037] Put calcium aluminate powder and water into the slurry mixer at a ratio of 7:3 (mass ratio) each time, stir until the slurry becomes paste, open the discharge door and put the slurry into the slurry funnel. After the slurry in the slurry mixer is completely put into the slurry funnel, add calcium aluminate powder and water in proportion in time to ensure that there is enough slurry in the slurry funnel to be continuously pumped into the reaction kettle.

[0038] Use the hydrochloric acid metering pump to pump hydrochloric acid at 1000L / h and the slurry metering pump to pump the slurry at a speed of 195L / h into the reaction kettle at the same time, control the stirring speed at 63rp...

Embodiment 3

[0040] According to the concentration of industrial concentrated hydrochloric acid, a certain amount of water (or waste acid) is added in proportion to the hydrochloric acid pool and mixed so that the concentration of HCl% in the hydrochloric acid is 16%, and it is used after stirring evenly.

[0041] Put calcium aluminate powder and water into the slurry mixer at a ratio of 7:3 (mass ratio) each time, stir until the slurry becomes paste, open the discharge door and put the slurry into the slurry funnel. After the slurry in the slurry mixer is completely put into the slurry funnel, add calcium aluminate powder and water in proportion in time to ensure that there is enough slurry in the slurry funnel to be continuously pumped into the reaction kettle.

[0042] Use a hydrochloric acid metering pump to pump hydrochloric acid at 600L / h and a slurry metering pump to pump the slurry at a speed of 120L / h into the reaction kettle at the same time, control the stirring speed at 63rpm, a...

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Abstract

The invention discloses a method for continuously producing poly-aluminum chloride and the production equipment thereof. The method comprises the steps of preparing uniform mushy slurry with a solid material and water; inputting the slurry and hydrochloric acid into a reactor for hybrid reaction; maintaining the reaction and a proper reaction temperature during the maturing process by controllingthe heat produced by the reaction itself; maintaining the torrential mixed state of the slurry during the reaction and the maturing processes; and filtering the slurry after the reaction and the maturing processes to obtain liquid poly-aluminum chloride. The equipment comprise a slurry inputting device, a hydrochloric acid inputting device, a reactor, a maturing reactor and a filter; the slurry inputting device and the hydrochloric acid inputting device are respectively connected to the reactor through a metering pump; the output end of the reactor is connected with the maturing reactor; and the output end of the maturing reactor is connected with the filter. All raw materials enter the reactor in liquid form, so that adding materials is safe and convenient, the effect of mixing materialsin the reactor is good, the material and the energy losses during the whole process are small, the temperature is easy to control, the continuous production can be realized, and the production efficiency is high.

Description

technical field [0001] The invention relates to the technical field of production and application of polyaluminum chloride, in particular to a continuous production method of polyaluminum chloride and production equipment thereof. Background technique [0002] Polyaluminum chloride (PAC) is a high-performance inorganic polymer flocculant, which can remove suspended solids, organic matter, heavy metals and radioactive pollutants in water. Due to the characteristics of large molecular structure, strong adsorption force, strong cohesion force, large flocs formed, fast sedimentation, and small dosage, it is widely used in the water treatment industry. [0003] There are many methods for domestic production of PAC, currently mainly acid-soluble method, alkali method, gel method, thermal decomposition method and so on. Commonly used raw materials are: (1) elemental aluminum (aluminum ingot, aluminum ash, aluminum chips and other aluminum processing waste); (2) aluminum-containing...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F7/56C02F1/52
Inventor 潘江浚谭铭卓蒋志飞
Owner 广东慧信环保有限公司
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