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Tama calc - suponjiakaru calcium carbonate

Tama calc - suponjiakaru

Voice 1 from a user
"I thought that only the removal of the SO2 was impossible by the dry process processing.
At last I found the treatment agent which could be equivalent to the emission control that became severe generally year by year."
-Tokyo A garbage and sewage plant -
 
⇒The reason?
Voice 2 from a user
"Drug consumption became 1/2, and large reduction of the hihaitokori cost was enabled."
-Tokyo B garbage and sewage plant -
 
⇒The reason?
Voice 3 from a user
As "I gave it up when clogging and an alcohol smell of the plumbing, the evil to facilities are peculiar to an effluent gas treatment agent, original direct is surprised at improvement, the thing that was able to dissolve so."
-Tokyo C garbage and sewage plant -
 
⇒The reason?
The reason is the pore capacity 3 times as large as JIS *go*ishihai.
 
 
SEM photograph

JIS *go*ishihai
 


Tama calc ®- suponjiakaru
CaO
(%)
The pore capacity
(cm3/g)
BET ratio surface area
(m2/g)
Dynamic appearance specific gravity
(-)
Average particle size
(μm)
JIS *go*ishihai
72.8
0.07
15
0.55
9.4
Tama calc ®- suponjiakaru
73.1
0.22
43
0.43
6.0
  1. The pore capacity : The measurements of the capacity of the pore (pore) which the calcium hydroxide particle by the nitrogen gas adsorption method (the BJH method) has.
  2. BET ratio surface area : The measurements of the area of the calcium hydroxide particle surface by the nitrogen gas adsorption method (the BJH method).
  3. Dynamic appearance specific gravity : With the value that I calculated than measurements of slack appearance specific gravity and the harder appearance specific gravity, it is approximately equal to the specific gravity in the calcium hydroxide retention tank.
  4. Average particle size : Measurements with laser diffraction / dispersion-type particle size distribution measuring equipment (dry process compulsion dispersion mode).
Solution 1 HCI, removal efficiency improvement of the SO2.
HCI removal performance curve (20% of A factory BF temperature 180 degrees Celsius water)
 
HCI removal rate (%)   
SO2 removal performance curve (20% of B factory BF temperature 150 degrees Celsius water)
 
SO2 removal rate (%)   
Equivalent
Equivalent
The reason has drug consumption and a decrease of hihaihatsuseiryo to becoming it.
 
Drug consumption and hihaihatsuseiryohikaku
Reduction of the solution 2 processing cost
Cost comparison in the model factory
Drug consumption reduction example in the true factory
Dust collection
Method
Dust collection
Temperature
(℃)
Water
(%)
Unit consumption
(kg/ton)
HCI exit density
(ppm)
SOx exit density
(ppm)
*go
TK-SP
*go
TK-SP
*go
TK-SP
A factory
BF
160
18
20.9
9.0
30
25
25
12
B factory
BF
170
40
15.6
7.5
25
10
20
3
The reason is powders fluidity superior to JIS *go*ishihai.
 
Powders fluidity comparison
JIS *go*ishihai
Tama calc ®-
suponjiakaru
Appearance specific gravity
(g/cm3)
The slack
0.38
0.31
Hardening
0.74
0.60
Dynamic 1)
0.55
0.45
Compression degree (%)2)
48.80
49.00
Fluidity index 3)
19.00
28.00
Jet-related index 4)
52.50
59.75
It depends on "paudatesuta PT-N model" made in Hosokawa Micron
 
 
 
 
1) Dynamic appearance specific gravity (g/cm3)
=(hardening appearance specific gravity - slack appearance specific gravity) X compression degree /100 slack appearance specific gravity
 
 
2) Compression degree (%)
=100* (hardening appearance specific gravity - slack appearance specific gravity) / hardening appearance specific gravity
 
 
3) Fluid index
The number that expressed easiness of outflow when the powders which stood still began to flow. Generally, cross-linked preventive measures are necessary so that this number is small.
 
 
4) Jet-related index
The number that expressed easy flushing (the difficulty that is up of working powders). Generally, a tendency of the flushing becomes strong so that this number is big.
 
 
In the operation inclination by the solution 3 "poor supply" solution
 
Even such a plumbing state is improved and can dissolve.

Calcium carbonate

I crush limestone and make it
■Calcium carbonate (san, 800 kg of furekon) for the desulfurization
I use it as a neutralizer.
75μm (200mesh)  The 100% passage
45μm (350mesh)  The 95% passage
●pH: 11 or less
 
■Granular calcium carbonate (disperse)
I use it as floor materials.
●Size (mm): 0.25-1.2
●pH: 11 or less
 
■Calcium carbonate (disperse) for the road
I raise the durability of the asphalt pavement.
600μm (28mesh)  The 100% passage
150μm (100mesh)  The 90% passage
75μm (200mesh)  The 70% passage
 
■White calcium carbonate (disperse)
I use it as a neutralizer.
 
250μm (60mesh)  The 100% passage
150μm (100mesh)  The 90% passage
 
■Calcium carbonate (san, 30 kg) for the feed
75μm (200mesh)  The 100% passage
45μm (350mesh)  The 95% passage
 
◎As there is the particle size except the above, please talk.
Yakusen lime
〒759-2222
3362, Isachoisa, Mine-shi, Yamaguchi
TEL. 0837-52-1148
FAX. 0837-52-1125
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