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Device for recycling organic entrained spent acid extracted through wet process and recycling method by using recycling device

A recovery device and organic technology, applied in the field of wet extraction organic entrained residual acid recovery device, can solve problems such as waste, increased input costs, and impact on product quality, so as to reduce production costs, improve product quality, and reduce acid ammonia consumption Effect

Active Publication Date: 2013-07-24
江西金世纪新材料股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] In wet smelting, due to environmental conditions, process conditions, flow ratio, clarification time during stripping, and insufficient tank capacity, etc., the final blank organics are seriously entrained with stripped residual acid, and these residual acids are not easy to be recycled uniformly. Direct discharge and waste, if not handled properly, it will lead to increased acid ammonia consumption and affect product quality
It has always been an intractable problem in the production of extraction process
Some technicians solve this problem by infinitely expanding the ratio of the clarification chamber to the mixing chamber of the tank body, but this will lead to an increase in the initial investment cost, and there are disadvantages such as excessively large valuable raw materials in the tank volume.

Method used

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  • Device for recycling organic entrained spent acid extracted through wet process and recycling method by using recycling device

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0011] Example 1 as figure 1 Shown: A recovery device for organic entrained residual acid by wet extraction, the main tank 5 in the extraction, separation and smelting includes a multi-stage clarification chamber 2 and a mixing chamber 3; Bucket 4 and main tank 5, the clarification chamber 2 of the last stage, mixing chamber 3, blank organic turnover tank 4 and main tank 5 communicate with each other through siphon 1; The siphon pipe 1 is introduced into the clarification chamber 2, and then enters the main tank 5 through the water phase overflow port of the clarification chamber 2 itself, and the liquid level height of each part is the same; the water phase overflow port 10 of the final stage main tank clarification chamber 2 is connected to The screw screw 9 is connected, and the rotation of the screw screw 9 can adjust the height of the water phase overflow of the last stage clarification chamber 2 of the main body tank, thereby controlling the height of residual acid allow...

Embodiment 2

[0013] Example 2 as figure 1 As shown: the method for recovering residual acid entrained by wet extraction using the recovery device described in Example 1, including: the clarification chamber 2, the mixing chamber 3, and the blank organic turnover barrel 4 of the last stage in the extraction, separation and smelting are connected to each other through a siphon 1 ; The residual acid of the blank organic turnover barrel 4 and the mixing chamber 3 is introduced into the clarification chamber 2 through the siphon 1, and then enters the main tank 5 through the water phase overflow port of the clarification chamber 2 self, and the liquid level height of each position is the same; finally The water phase overflow port 10 of the clarification chamber 2 of the primary main tank is connected to the screw screw 9, and the rotation of the screw screw 9 can adjust the height of the water phase overflow port 10 of the clarification chamber 2 of the main tank, thereby controlling the allowa...

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Abstract

The invention relates to a device for recycling organic entrained spent acid extracted through a wet process and a recycling method by using the device. A clarifying chamber, a mixing chamber, a blank organic transfer barrel and a main body tank which are at the last level are communicated with each other through siphons. Spent acid in the blank organic transfer barrel and the mixing chamber is guided into the clarifying chamber through the siphons and enters into the main body tank through a water-phase overflowing port of the clarifying chamber, and the height of liquid level at every position is the same. A water-phase overflowing port of the main body tank at the last level is connected with a spiral lead screw, and the height of the water-phase overflowing port of the main body tank can be adjusted by rotating the spiral lead screw so as to control the height of the spent acid allowed to be reserved at every position. A regeneration total valve is connected with a tap water inletpipe and is closed after the tap water inlet pipe is opened to enable water to be filled in all the siphons, and then three regeneration branch valves are opened so that siphon can be activated and started. By means of the device for recycling the organic entrained spent acid extracted through the wet process and the recycling method by using the device, the entrained spent acid can be recycled immediately, cleanly, safely, stably and timely in an unpowered mode, acid ammonia consumption in a wet smelting process is reduced, product quality is improved, and production cost is reduced.

Description

technical field [0001] The invention relates to the recovery and utilization of a wet extraction separation smelting process, in particular to a wet extraction organic entrainment residual acid recovery device and a recovery method thereof. Background technique [0002] In wet smelting, due to environmental conditions, process conditions, flow ratio, clarification time during stripping, and insufficient tank capacity, etc., the final blank organics are seriously entrained with stripped residual acid, and these residual acids are not easy to be recycled uniformly. Direct discharge is wasteful. If it is not properly handled, it will lead to increased acid ammonia consumption and affect product quality. It has always been an intractable problem in the production of extraction process. Some technicians solve this problem by infinitely expanding the ratio of the clarification chamber to the mixing chamber of the tank body, but this will lead to an increase in the initial investm...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/26B01D11/04
CPCY02P10/20
Inventor 李常清姜亚龙张五国詹海波周武风钟杨根
Owner 江西金世纪新材料股份有限公司
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