CN-224226882-U - Combined structure of float glass kiln and natural gas hydrogen production conversion pipe
Abstract
The utility model discloses a combined structure of a float glass kiln and a natural gas hydrogen production conversion pipe, which comprises a melting part and a cooling part of the melting part, wherein heat storage chambers are arranged on two sides of the melting part, and a heat exchange structure is arranged on one side of the melting part.
Inventors
- DONG QINGSHI
- ZHANG MINRUI
- CHEN XIONG
- LI SONGBO
- DENG YIFAN
Assignees
- 信义节能玻璃(芜湖)有限公司
Dates
- Publication Date
- 20260512
- Application Date
- 20250421
Claims (7)
- 1. The combined structure of the float glass kiln and the natural gas hydrogen production conversion pipe is characterized by comprising a melting part (1) of the kiln and a cooling part (2) of the kiln, wherein heat storage chambers (3) are arranged on two sides of the melting part (1) of the kiln, and a heat exchange structure is arranged on one side of the melting part (1) of the kiln.
- 2. The combination structure of a float glass furnace and a natural gas hydrogen production conversion pipe according to claim 1, wherein the heat exchange structure comprises a mixed gas main pipeline (6) and a cooling coil pipe (5), and two ends of the cooling coil pipe (5) are connected with the mixed gas main pipeline (6).
- 3. The combination structure of a float glass furnace and a natural gas hydrogen production conversion pipe according to claim 2, wherein the furnace cooling part (2) comprises a cooling part breast wall (8), the cooling coil (5) is arranged in the furnace cooling part (2), two ends of the cooling coil (5) penetrate through the cooling part breast wall (8), and the mixed gas main pipeline (6) is arranged at two sides of the furnace cooling part (2).
- 4. The float glass furnace and natural gas hydrogen production conversion tube combined structure according to claim 2 is characterized in that two transverse furnace passages (4) are connected between the furnace melting part (1) and the furnace cooling part (2), the two furnace cooling parts (2) are arranged in parallel and are respectively connected with two ends of the transverse furnace passages (4), the transverse furnace passages (4) comprise transverse passage breast walls (9), the cooling coils (5) are arranged in the transverse furnace passages (4), two ends of the cooling coils (5) penetrate through the transverse passage breast walls (9), and the mixed gas main pipelines (6) are arranged at two sides of the transverse furnace passages (4).
- 5. The combined structure of a float glass furnace and a natural gas hydrogen production conversion pipe according to claim 3 or 4, wherein one end of the melting part (1) of the melting furnace is provided with a feed port (10), and oxygen guns (11) are arranged on two sides of the feed port (10).
- 6. The combined structure of a float glass furnace and a natural gas hydrogen production conversion pipe according to claim 5, wherein control valves (7) are arranged at two ends of the mixed gas main pipeline (6).
- 7. The combination structure of a float glass furnace and a natural gas hydrogen production conversion pipe according to claim 6, wherein the cooling coils (5) are arranged at equal intervals.
Description
Combined structure of float glass kiln and natural gas hydrogen production conversion pipe Technical Field The utility model belongs to the field of glass kilns, and particularly relates to a combined structure of a float glass kiln and a natural gas hydrogen production conversion tube. Background In the float glass production process, the batch is melted, clarified and cooled at high temperature (relatively high temperature) and then enters a tin bath for forming, and is cooled by an annealing kiln (relatively low temperature). In the actual production process, the batch materials after being fully absorbed and melted in the melting part of the melting furnace form glass liquid, and the glass liquid is circulated in the melting furnace for a plurality of times. Wherein part of the glass liquid passes through the neck and reaches the cooling part to be cooled and lowered. The cooling part in the glass kiln is usually cooled by using a cooling fan to blow lower air through a cooling air pipe to blow the molten glass directly to take away the heat of the molten glass body, so as to achieve the purpose of cooling. In the production of different types of glass, there are often different requirements on the temperature of the glass liquid entering the cooling section for cooling. The upper layer glass liquid, the middle layer glass liquid and the lower layer glass liquid of the cooling part of the melting furnace can be cooled unevenly by the cooling fan, so that the cooling rate is too high when cooling air contacts the uppermost layer glass liquid, the temperature of the upper layer glass liquid is reduced, the density is increased and sunk, and the temperature of the middle layer glass liquid is higher than that of the upper layer glass liquid, thereby forming a heat shower and affecting the normal production process. Conventionally, fossil fuels such as natural gas, heavy oil, coal tar and the like are mainly used in glass melting furnaces, wherein hydrogen produced by a natural gas hydrogen production device can be mixed with natural gas to form a mixed fuel, so that dependence on the traditional fossil fuels is reduced, carbon emission can be remarkably reduced, and meanwhile, the combustion efficiency of the natural gas is improved. In the existing natural gas hydrogen production equipment, the natural gas and steam reforming pyrolysis hydrogen production needs to be subjected to heat acceleration reaction, the heat provided by external natural gas combustion in actual production firstly provides catalytic kinetic energy for mixed gas of natural gas and steam, then after main reaction, the burnt natural gas flue gas gradually enters a preheating section to supplement water and preheat a boiler for producing steam, the combustion gas is preheated, the mixed gas of the natural gas and the steam is preheated, the flue gas is finally discharged to an atmosphere through a chimney after passing through the preheating section, the temperature is always kept at about 180-280 ℃, and the conditions of energy waste and large natural gas quantity required by combustion heat supply exist. The utility model patent with publication number CN207944012U discloses a cooling air pipe system of a glass melting furnace melting part in 2018, 10 and 9, which comprises a cooling air main pipe, a first cooling air branch pipe for guiding cooling air to a front face wall, and a second cooling air branch pipe for guiding cooling air to a slag beam, wherein the first cooling air branch pipe and the second cooling air branch pipe are communicated with the cooling air main pipe. The cooling air duct system of the melting section of the glass melting furnace cannot solve the above-described technical problems. Disclosure of utility model The utility model aims at overcoming the defects of the prior art, and provides a combined structure of a float glass kiln and a natural gas hydrogen production conversion pipe, which replaces a cooling fan, reduces production electricity consumption, ensures stable production process and improves the hydrogen production efficiency of natural gas. In order to achieve the above purpose, the technical scheme adopted by the utility model is as follows: the combined structure of the float glass kiln and the natural gas hydrogen production conversion pipe comprises a melting part of the melting kiln and a cooling part of the melting kiln, wherein heat storage chambers are arranged on two sides of the melting part of the melting kiln, and a heat exchange structure is arranged on one side of the melting part of the melting kiln. The heat exchange structure comprises a mixed gas main pipeline and a cooling coil, and two ends of the cooling coil are connected with the mixed gas main pipeline. The cooling part of the melting furnace comprises a cooling part breast wall, the cooling coil is arranged in the cooling part of the melting furnace, two ends of the cooling coil penetrate through the cooling part breast