A kind of anti-caking artesian coke oven raw gas waste heat recovery heat exchange unit
A technology of heat exchange unit and waste heat recovery, applied in the direction of heat exchanger types, indirect heat exchangers, lighting and heating equipment, etc., can solve the problems of easy adhesion, coking, and easy adhesion of tar to heat exchange devices. , to achieve the effect of saving resources, preventing sticking and coking
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Embodiment 1
[0034] Such as figure 1 , figure 2 , image 3 , Figure 4 with Figure 5As shown, an anti-bonding self-flowing self-flowing coke oven raw gas waste heat recovery heat exchange unit in this embodiment includes a heat exchange vertical pipe 1, a heat exchange horizontal pipe and a heat exchange working medium delivery pipe, wherein: the two ports of the heat exchange horizontal pipe Sealed, the heat exchange horizontal tube includes an upper heat exchange horizontal tube 201 and a lower heat exchange horizontal tube 202 , and the heat exchange working medium delivery tube includes an upper heat exchange working medium delivery tube 301 and a lower heat exchange working medium delivery tube 302 . The heat exchange unit body includes a plurality of single-row components arranged at the same interval and fixed together to form a rectangular parallelepiped heat exchange unit body. The single-row assembly includes a heat exchange vertical pipe 1, an upper heat exchange horizonta...
Embodiment 2
[0053] The structure of the heat exchange unit for recovering waste heat from raw coke oven waste gas that resists sticking in this embodiment is basically the same as that in Embodiment 1, the difference being that the body of the heat exchange unit is inclined 45 degrees upward along the horizontal plane during assembly; The total length of the heat exchange unit body is 3000mm, the total height is 1800mm, and the total width is 1800mm; the diameter of the heat exchange vertical tube 1 is 50mm, and the length of the heat exchange vertical tube 1 is 1800mm; The length of the heat horizontal pipe is 3000mm; the diameter of the heat exchange working medium delivery pipe is 50mm, and the length of the heat exchange working medium delivery pipe is 300mm; the distance between adjacent heat exchange vertical pipes 1 on the single row assembly outside the heat exchange unit body is 10mm.
[0054] The construction method of an anti-bonding self-flowing coke oven raw gas waste heat re...
Embodiment 3
[0056] The structure of the anti-bonding self-flowing coke oven raw gas waste heat recovery heat exchange unit of this embodiment is basically the same as that of embodiment 1, the difference is that the heat exchange unit body is inclined 30 degrees upward along the horizontal plane during assembly; The total length of the heat exchange unit body is 2000mm, the total height is 1100mm, and the total width is 1050mm; the diameter of the heat exchange vertical tube 1 is 40mm, and the length of the heat exchange vertical tube 1 is 1100mm; The length of the heat horizontal pipe is 2000mm; the diameter of the heat exchange working medium delivery pipe is 40mm, and the length of the heat exchange working medium delivery pipe is 225mm; the distance between adjacent heat exchange vertical pipes 1 on the single row assembly outside the heat exchange unit body is 6mm.
[0057] The construction method of an anti-bonding self-flowing coke oven raw gas waste heat recovery heat exchange uni...
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