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Glass batch presintering treatment technology

A technology of glass batch materials and processing technology, applied in glass production, glass manufacturing equipment, manufacturing tools, etc., can solve the problems of discontinuous production process and increased difficulty of breaking, so as to increase single-line production, reduce energy consumption, and increase heat the effect of transmission

Inactive Publication Date: 2018-12-18
钱圣奎
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This patent reduces the dust flying in the glass melting furnace, prolongs the life of refractory materials, prevents the clogging of the regenerator, and reduces the flying loss of batch materials, etc. The sintered block has a certain strength in the hot state of 1000 ℃, so the difficulty of crushing is increased; at the same time, after the crushing process is added, it also causes discontinuity in the production process

Method used

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  • Glass batch presintering treatment technology

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Such as figure 1 As shown, a device for decomposing glass batch materials outside a carbonate melting furnace - a rotary heating furnace, which includes a feeding device 2, a rotary heating cylinder 3 with an inclination angle of 3 to 12° from the horizontal, and a kiln head sealing device 8 , kiln tail sealing device 11 and burner 4;

[0026] The upper end of the feeding device 2 is provided with a storage bin 1, and the lower end is connected with the kiln tail sealing device 11;

[0027] The high end and the low end of the rotary heating cylinder 3 are respectively sealed and connected with the kiln tail sealing device 11 and the kiln head sealing device 8, and one end of the kiln tail sealing device 11 is connected with the inlet of the high-temperature induced draft fan 12, and the kiln head The sealing device 8 is provided with a flue gas inlet 7 and a spherical pellet outlet 9;

[0028] The burner 4 extends into the rotary heating cylinder 3 through the kiln he...

Embodiment 2

[0037] The difference with embodiment 1 is:

[0038] (1) Dissolve the water glass accounting for 1.5wt% of the glass batch in water accounting for 8wt.% of the glass batch, then mix the above-mentioned water glass solution into the glass batch, mix well, and use a semicircular concave surface on the surface It is pressed into spherical pellets of 5-18 mm by pair of rollers.

[0039] (2) Put the spherical pellets into the rotary heating furnace, pre-fire at 1180-1250° C., and feed the sintered and compacted spherical pellets into the glass melting furnace from the outlet of the rotary heating furnace.

[0040] Since the pellets compressed into a spherical shape are 5-18mm in size, the pre-calcination decomposition time in the rotary heating cylinder is about 1 hour.

[0041] Water glass described in the present embodiment can also be replaced with methyl cellulose.

Embodiment 3

[0043] The difference with embodiment 1 is:

[0044] (1) Dissolve water glass accounting for 3wt% of the glass batch in hot water (80-100°C) accounting for 7wt.% of the glass batch, then add the above-mentioned water glass solution into the glass batch, mix well, It is pressed into spherical pellets of 8-25 mm by means of a pair of rollers with a semicircular concave surface on the surface.

[0045] (2) Put the spherical pellets into the rotary heating furnace, pre-fire at 1020-1150° C., and feed the sintered and compacted spherical pellets into the glass melting furnace from the outlet of the rotary heating furnace.

[0046] Since the pellets compressed into a spherical shape are 8-25mm in size, the pre-calcination decomposition time in the rotary heating drum is about 1.5 hours. In this embodiment, three sets of devices described in Embodiment 1 are used to simultaneously pre-fire the glass batch.

[0047] Water glass described in the present embodiment can also be replaced ...

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Abstract

The invention discloses a glass batch presintering treatment technology including steps of: (1) blending 1-3 wt% of a binder and 6.5-8 wt% of water to the glass batch with uniform mixing and pressingthe mixture into spherical granules being 5-25 mm; (2) adding the spherical granules into a revolving heating furnace and preheating the material at 1050-1250 DEG C for 1-2 h, then sending the sintered and compacted spherical granules into a glass smelting kiln from the outlet of the revolving heating furnace. In the technology, carbonate decomposition is carried out outside the glass smelting kiln, so that gas content of the glass batch is greatly reduced, heat transfer is effectively enhanced and glass clarifying and homogenizing time is shortened; it is equivalent to increase single-line production yield and reduce energy consumption without enlargement on the area of the glass smelting kiln. The technology can increase smelting capacity by 20-30% without the enlargement on the size ofthe present glass smelting kiln.

Description

technical field [0001] The invention relates to a flat glass melting technology, in particular to a glass batch material pre-burning treatment process. Background technique [0002] Powdery batch materials are used in flat glass. This method is to crush and sieve various raw materials to a certain particle size, and then weigh and mix them to make loose powder materials. This kind of loose material is prone to stratification and powder flying in the process of transportation and storage, and the batch material just entered the kiln is easily blown up by the flame and taken out of the furnace, which not only changes the composition of the glass, but also affects the The large wall of the kiln and the regenerator cause erosion and pollute the environment. [0003] The loose form of the batch material is put into the furnace, and because of its low bulk density, the heating efficiency of the flame on the batch material is low. In addition, the batch material is put into the m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C03B3/02C03B1/02
CPCC03B1/02C03B3/023Y02P40/57
Inventor 钱圣奎
Owner 钱圣奎
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