Analysis of current efficiency by metal manganese electrolysis

Electrolytic manganese metal is a high-energy process, to increase the current efficiency (η c) is a practical problem in the production of most concern. The current efficiency is directly related to the production and economic benefits of metal manganese and the quality of the product.
Through the simultaneous electrolysis of Mn and H 2 , the staff clarified the quantitative relationship between the ammonia adjustment and the (NH 4 ) 2 SO 4 content in the catholyte to the cathode current efficiency η c , and discussed the important technical conditions affecting the current efficiency η c . .
I. Simultaneous Electrolysis of Manganese Electrolytic Cathode Mn and H 2
It has been mentioned that two phase-to-competitive reactions are carried out on the electrolytic manganese cathode, and the reaction of precipitation of manganese metal belongs to diffusion control reaction, and the reaction of hydrogen evolution (H 2 ) belongs to electrochemical control reaction. Then according to the principle of equilibrium reaction, the necessary condition for simultaneous discharge of Mn 2+ and H + should be the precipitation of Mn, and the precipitation potentials of the two reactions of H 2 are equal, ie

(1) where i d and i d∞ are the manganese precipitation diffusion current density and the ultimate diffusion current density (A/m 2 ).
Cathode current efficiency That is, reducing the current density i H2 of the precipitated H 2 is the main way to increase η c .
It can be seen from the formula (1) that i H2 increases as the value of φ increases, but decreases as the pH value and a H2 increase, and vice versa.
Regarding the i d ∞ value in (1), we take the diffusion coefficient of Mn 2+ D=10 -5 cm/S, [Mn 2+ ]=1mol/L10 -3 mol/cm 3 , and take the thickness of the diffusion layer=0.025 Cm, then i° d∞ =0.0772A/cm 2 =772A/m 2 .
i d∞ =i° d∞ , [Mn 2 + ] takes electrolytic catholyte [MnSO 4 ]=[Mn 2+ ]=0.5mol/L, then i d∞ =772×0.5=386A/m 2 .
(1) where a H2 is the Tafel coefficient, and the hydrogen exchange current density on the metal Mn in the 0.05 mol/L H 2 SO 4 solution is i 0 = 10 -7 A/cm 2 .
The overvoltage of H 2 on the metal is related to pH. At 25 ° C, η H2 = a H2 + 0.0591 pH + 0.1182lgi
η H2 =-0.1182lgi° 0 +0.0591pH+0.1182lgi
I° 0 is the standard exchange current density at pH=0.
In 0.05 mol/L H 2 SO 4 , i 0 = 10 -7 A/cm 2 , which is calculated by data. The pH of the 0.05 mol/L H 2 SO 4 solution is 1.231, then i 0 =i° 0 •[H + ] 0.5 , ie 10 -7 =i° 0 •10 -1.231×0.5 ,i° 0 =10 -6.325
Then a H2 =-0.1182lg10 -6.325 =0.755V
Therefore, the overvoltage of H 2 on Mn is η H2 =0.755+0.0591pH+0.1182lgi H2[next]
Using the values ​​of i d∞ and a H2 derived above, and using the φ value calculated by the electrochemical balance, substituting into equation (1), the data of Table 1 and Table 2 can be calculated, and the amount of ammonia added can be quantitatively determined. The effect of NH 3 ] addition and [NH 4 ] 2 SO 4 (B) concentration on cathode current efficiency η c is shown in Figures 1 and 2 .

[next]

As seen from Table 1 and Figure 2, the addition of ammonia thermodynamically increases the value of φ, kinetically increasing the pH of the solution to increase the overvoltage of hydrogen. The combined results of thermodynamic and kinetic effects are all improved by the current efficiency η c .

Table 1 [MnSO 4 ] = 0.5 mol·L -1 , [(NH 4 ) 2 SO 4 ] = 1 mol·L -1
Effect of ammonia addition ([NH 3 ] addition) on Ph, φ and η c

[NH 3 ] added (mol·L -1 )
0.3488
0.1258
0.0822
0.0257
pH
7.9225
7.668
7.267
6.969
[NH 3 ]/(mol·L -1 )
9.05×10 -2
5×10 -2
2×10 -2
1×10 -2
φ/V
-0.727
-0.7392
-0.7605
-0.7775
i d /(A·m -2 )
386
386
386
386
i H2 /(A·m -2 )
102
174
215
241
D c /(A·m -2 )
488
560
601
627
η c /%
79.1
64.2
64.2
61.6
Table 2 Effect of solution composition on equilibrium pH A , [NH 3 ], φ value, ammonia addition amount and current efficiency

The concentration of each component in the solution / (mol · L -1 )
A=0.5
B=0.75
A=0.5
B=1
A=0.5
B=1.2
[NH 3 ]/(mol·L -1 )
6.2×10 -2
9.05×10 -2
1.17×10 -2
Ph
7.885
7.9225
7.9548
φ/V
-0.7274
-0.7272
-0.7272
[NH 3 ] added / (mol·L -1 )
0.2468
0.3488
0.4359
pH A
7.885
7.9225
7.9548
i d /(A·m -2 )
386
386
386
i H2 /(A·m -2 )
106
102
98
D c /(A·m -2 )
492
488
48.4
η c /%
78.46
79.1
79.75

It can be seen from Table 2 and Fig. 2 that increasing (NH 4 ) 2 SO 4 also increases the potential difference (Δφ) and pH, which is advantageous for the improvement of the current efficiency η c , but the effect is not as significant as the ammonia adjustment.
Second, the main factors affecting the efficiency of metal manganese deposition current
The main factors affecting the current efficiency of metal manganese are:
1. Electrolyte composition The manganese electrolyte includes a new liquid (purification liquid), a catholyte, and an anolyte.
(1) New liquid, the new liquid sent to manganese electrolysis is pure solution after purification, Mn 2+ 34~38g/L, (NH 4 ) 2 SO 4 100~120g/L, pH 6.5~7. In order to maintain The high cathode current efficiency, the impurity content of the foreign electrolytic manganese new liquid is shown in Table 3.

Table 3 Contents of impurity components of foreign electrolytic manganese new liquid (mg/L)

Country names
Fe
Zn
Ni
Co
As
Cu
Si
P
Japan
20
20
1
0.5
8
8
South Africa
15
10
1
0.3
/
5
10
Former Soviet Union
twenty four
15~20
1
0.5
8
5
0.2

[next]
As a result of the domestic iron effective measures, in addition to iron 1mg / L or less, using the SDD (ziram sodium) in addition to heavy metals, nickel and cobalt can be purified to 0.5mg / L or less.
(2) Catholyte 1Mn 2+ content, industrial manganese content of catholyte fluctuates between 15~18g/L. Too high will lead to the precipitation of manganese ammonium double salt and destroy the electrolysis process.
2 (NH4) 2 SO 4 content, increasing the concentration of (NH 4 ) 2 SO 4 can increase the stability of Mn 2+ in solution, preventing its hydrolysis at high pH, ​​and it can also increase the conductivity of the solution.
In the foreign manganese industry, the (NH 4 ) 2 SO 4 content fluctuates between 120 and 140 g/L (without selenium ), and the domestic is 100 to 120 g/L (with selenium).
3 pH adjustment, the test confirmed that with the increase of the pH of the catholyte, the current efficiency increased significantly, but decreased after pH>9. The relationship between catholyte pH and current efficiency is shown in Table 4.

Table 4 Relationship between pH and current efficiency of catholyte

pH
2
3
4
5
6
7
8
9
10
10.5
11
η c /%
0
0
twenty two
30
35
48
55
62
50
40
33

In order to increase the pH of the catholyte, 1:1 ammonia water is added in practice. The amount of ammonia in the production of manganese is generally 0.08t, and the ammonia concentration in the catholyte is generally 3.2g/L.
It should be noted that the amount of ammonia adjustment should be appropriate. Excess ammonia leads to the hydrolysis of Mn 2+ on the one hand, and the increase in free NH 3 due to an increase in pH, which leads to loss of ammonia. See Table 5 for the relationship between the pH of the catholyte for ammonia loss.

Table 5 Relationship between ammonia loss and cathode pH

pH value
6
7
8
9
Tons of Mn liquid ammonia loss / (kg·t -1)
8
10
12
28

Generally, the pH of the catholyte is preferably controlled at 7-8.
(3) Anolyte The anolyte contains about Mn 2+ (14~15) g/L, and contains H 2 SO 4 40g/L.
When SeO 2 is added as an antioxidant, the pH is preferably controlled at 6.8 to 7.2, and when SO 2 is used as an antioxidant, the pH is preferably controlled at 7.8 to 8.2. [next]

(4) Additives, Mn 2+ can be easily oxidized to high-valence manganese compounds MnOOH (Mn 2 O 3 •3H 2 O) and MnO 2 under high pH conditions. In order to prevent oxidation of Mn 2+ , it is necessary to add antioxidants. The solution remains reducible. Even if Mn 2 O 3 and MnO 2 particles are formed occasionally, they will be immediately reduced by reduction. Antioxidants such as hydroxylammonium, glycerol, ammonium acetate, ammonium oxalate, alcohol, citric acid, formaldehyde and thiocyanate have been tested. H 2 TeO 6 (0.1~0.3g/L) and ants have also been reported. acid.
In the 1940s and 1950s, metal manganese electrolysis successfully used SO 2 as an antioxidant, adding 0.1 g/L of SO 2 to the solution and raising the pH of the solution to 8, which can maintain high cathode current efficiency and dense metal. Manganese deposition.
The role of SO 2 is to maintain the reducibility of the solution, and the resulting MnO 2 and Mn 2 O 3 are reduced to Mn 2+ , ie MnO 2 +HSO - 3 +H + ===Mn 2+ +SO 4 2- +H 2 O
E=1.229-0.0591=1.1689V
Mn 2 O 3 +HSO - 3 +3H + ===2Mn 2+ +SO 4 2- +2H 2 O
E=1.4434-0.0591=1.3843V
In the 1960s, a more effective antioxidant, SeO 2 , was started in metal manganese electrolysis with an added concentration of 0.03 to 0.06 g/LSe.
The morphology of SeO 2 in solution depends on the pH.

Under the production conditions of pH>6.58, the electromotive force of SeO 2 to reduce manganese oxide is MnO 2 +SeO 3 2- +2H + ===Mn 2+ +SeO 4 2- +H 2 O
E=1.229-0.875=0.354V
Mn 2 O 3 +SeO 3 2- +4H + ===2Mn 2+ +SeO 4 2- +2H 2 O
E=1.4434-0.875=0.5684V
Production practice has confirmed that the addition of SO 2 and SeO 2 to the electrolyte can significantly improve the current efficiency, and it is recognized that they exhibit a good antioxidant effect.
In addition, studies have confirmed that SeO 2 and SO 2 reducing agents also play the following roles:
1SeO 2 and SO 2 are reduced to elemental selenium and elemental sulfur at the cathode, and adsorption on the cathode can increase the precipitation overvoltage of hydrogen;
2SO 2 is reduced to H 2 S at the cathode, and reacts with Co 2+ and Ni 2+ to form a sulfide precipitate, thereby alleviating the harmful effects of Co and Ni.
3 There are SO 2 , SO 3 2- , SeO 3 2- , colloidal sulfur and thiourea in the electrolytic solution, which is favorable for depositing a-type manganese, which has stronger corrosion resistance than γ-type manganese.
A disadvantage of using SO 2 as a reducing agent is an increase in the sulfur content of the manganese metal product.
SeO 2 currently widely used as an additive, was added in an amount of control of manganese t 2 ~ 4kg. [Next]
2. Electrolyte temperature The use of a low electrolysis temperature is the main condition for ensuring a high Tafel value a. Since the activation energy of the hydrogen evolution reaction is high (14 to 16 kJ/mol), the elevated temperature significantly decreases the value of a. Production practice has confirmed that when the temperature exceeds 45 ° C, the current efficiency is greatly reduced, and when the temperature is above 50 ° C, electrolysis cannot be performed. However, the electrolyte temperature should not be too low, and a temperature lower than 20 °C results in excessive fine particle size Mn deposition and a significant decrease in electrolyte conductivity.
The temperature of the electrolyte used in the industry is 38~44 °C.
In order to eliminate the influence of Joule heat released during the electrolysis process, for the 3000A current electrolyzer, Ø33mm, 3mm thick, 4m long serpentine lead pipe or stainless steel pipe, plastic pipe and other corrosion-resistant pipes are used on both sides, with circulating cooling water. Indirect cooling.
3. Current Density (1) Cathode current density, in order to increase the overvoltage of hydrogen, a higher cathode current density is used in electrolytic manganese production to improve cathode current efficiency. See Table 6 for the relationship between cathode current density and current efficiency.

Table 6 Relationship between current density and current efficiency of electrolytic manganese cathode

D c (A·m -2 )
200
400
500
700
η c /%
60
64
65
62.8

The cathode current density is too low, not only is the current efficiency low, but also causes matte metal deposition. The current density is too high, the electric efficiency is also lowered, and dendritic products are easily produced.
The cathode current density employed in the industry is usually controlled in the range of 300 to 400 A/m 2 . The current density of domestic electrolytic manganese plants is generally 350~400A/m 2 . Practice has confirmed that the product quality is good when using lower current density.
(2) The anode current density generally uses a high current density of 680 to 800 A/m 2 to reduce the amount of MnO 2 precipitated on the anode.
4. Cathodic deposition time As the electrolysis time continues, the surface of the precipitated manganese becomes rough, and even granular or dendritic crystals are produced, and the current efficiency is lowered, so the electrolysis time should not be too long. However, the deposition time is too short, which will increase the number of troughs, increase the workload, and increase the consumption of ammonia and SeO 2 . Therefore, the domestic precipitation period is generally 24h.


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4. The body is small, short wheelbase, compact structure;
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6. The power output double speed 540/720, can form a complete set of various agricultural machinery;

7.Flat floor, hanging pedal, flexible and easy to operate;

8.Hydraulic steering, steering is more flexible.

1. Matching the 485 diesel engine, Large torque reserve, Strong power;
2. Using 8 + 2 meshing swap file, reasonable matching speed, high efficiency;
3. Power emissions upgrades, performance, low fuel consumption, high reliability;
4. The body is small, short wheelbase, compact structure;
5. Using underneath type exhaust pipe bending, rear accumulator, overall appearance is narrow;
6. The power output double speed 540/720, can form a complete set of various agricultural machinery;

7.Flat floor, hanging pedal, flexible and easy to operate;

8.Hydraulic steering, steering is more flexible.


801

80.

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