Solid-liquid separation device and method for producing Hopcalite

A technology of solid-liquid separation and gas-liquid separator, which is applied in the direction of separation methods, filtration separation, chemical instruments and methods, etc. It can solve the problems of non-recyclable, large amount of soda ash used, and low production efficiency, so as to avoid waste and improve production efficiency. The effect of high efficiency and low cost

Active Publication Date: 2015-06-10
邯郸市同俊达矿山设备股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The production technology of traditional hopcalate agent has the following disadvantages: 1, the sulfate ion discharged is the mixture of potassium sulfate and sodium sulfate, which cannot be recycled; 2, the production cost is high, and the usage amount of soda ash is large (generating basic carbonic acid The copper process will use a large amount of soda ash to neutralize dilute sulfuric acid and convert it into sodium sulfate); 3. The production efficiency is low, and it usually takes 8 days to complete

Method used

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  • Solid-liquid separation device and method for producing Hopcalite
  • Solid-liquid separation device and method for producing Hopcalite

Examples

Experimental program
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Effect test

Embodiment 1

[0044] A solid-liquid separation device, see figure 1Shown, comprise airtight tank 2, air compressor 16, vacuum pump 14 and gas-liquid separator 13; The outer side of the airtight tank 2 is provided with a rotating shaft 3, and the rotating shaft 3 is connected with the power turning device of the airtight tank 2; the rotating shaft 3 is a hollow shaft, and the upper part of the filter layer 6 inside the airtight tank 2 is connected with the air compressor 16 through the rotating shaft 3 and the air pressure pipeline 21; The bottom of the airtight tank 2 is provided with a drain valve 9 and a drain pipeline 11, the other end of the drain pipeline 11 is connected to a gas-liquid separator 13, and the top of the gas-liquid separator 13 is connected to a vacuum pump 14 through a vacuum pipeline 15, and the gas-liquid separator 13 The bottom is provided with a discharge port 12; the air pressure pipeline 21 and the discharge pipeline 11 are connected by a pipeline 19, and the pip...

Embodiment 2

[0067] Solid-liquid separation device is with embodiment 1, and the difference of the method for producing hopcalate agent and embodiment 1 is:

[0068] The applied pressure in step 2) and step 4) is: applied positive pressure 2MPa, applied negative pressure -0.1MPa.

[0069] Step 5): The amount of water added to the airtight tank 2 is 10 times the mass of the solid material in the airtight tank 2 in step 6).

[0070] Step 6): After repeating the washing operation of step 5) once, a damp semi-finished product of hopcalate agent is obtained.

[0071] Step 7): In the water removal step, the heating temperature of the airtight tank 2 is 60°C.

Embodiment 3

[0073] Solid-liquid separation device is with embodiment 1, and the difference of the method for producing hopcalate agent and embodiment 1 is:

[0074] The applied pressure in step 2) and step 4) is: applied positive pressure 0.1MPa, applied negative pressure -0.1MPa.

[0075] Step 5): The amount of water added to the airtight tank 2 is 0.5 times the mass of the solid material in the airtight tank 2 in step 6).

[0076] Step 6): After repeating the step 5) washing operation for 3 times, a damp semi-finished product of hopcalate agent is obtained.

[0077] Step 7): In the water removal step, the heating temperature of the airtight tank 2 is 120°C.

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Abstract

The invention discloses a solid-liquid separation device and a method for producing Hopcalite, relating to the field of solid-liquid separation devices of chemical reaction products and catalyst preparation. The device comprises a sealed tank, wherein a feed opening is formed in the top of the sealed tank, a filtering layer is arranged at the lower middle part in the sealed tank, a rotating shaft is arranged on the outer side of the sealed tank, and the rotating shaft is a hollow shaft and is connected with a power overturning device; the upper side of the filtering layer in the sealed tank is connected with an air compressor through the rotating shaft and an air compression pipeline; a drain valve and a drain pipeline are arranged at the bottom of the sealed tank, the other end of the drain pipeline is connected with a gas-liquid separator, the top of the gas-liquid separator is connected with a vacuum pump through a vacuum pipeline, and a liquid outlet is formed in the bottom of the gas-liquid separator; the air compression pipeline is connected with the drain pipeline through a pipeline, and valves, liquid inlet valves and air compression valves are respectively arranged on the pipeline, the drain pipeline and the air compression pipeline. The device is good in solid-liquid separation effect and is high in production efficiency; when the device is used for producing Hopcalite, the cost is low, the production cycle is short, potassium sulfate and sodium sulfate can be respectively recovered, and thus the potassium sulfate and the sodium sulfate can be recycled.

Description

technical field [0001] The invention relates to the technical field of preparation of a chemical reactant solid-liquid separation device and a catalyst. Background technique [0002] Hopcalate agent is a catalyst product for filtering carbon monoxide, its main component is a mixture of manganese oxide and copper oxide. Produced by a chemical reaction, accompanied by sulfate ions such as sodium sulfate and potassium sulfate, it is a substance harmful to hopcalate products, and it is necessary to remove sulfate ions from hopcalate to produce qualified Hopcalla agent. [0003] Hopcalate agent is a kind of solid, insoluble in water, and sulfate ion is easy to dissolve in water, and the production process device of traditional hopcalate agent is as figure 2 Shown, comprise the following steps: 1, water is added reactor, add the vitriol oil, as the medium solution of reaction; 2, add manganese sulfate in reactor, dissolve; Add potassium permanganate reaction, generate manganese ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D36/00B01D29/01B01J23/34
Inventor 王志敏梁振同
Owner 邯郸市同俊达矿山设备股份有限公司
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