ᱜᱨᱚᱵᱽ ᱟᱨ ᱜᱨᱚᱵᱽ ᱨᱮ ᱠᱟᱹᱢᱤ ᱠᱟᱛᱮ ᱟᱹᱰᱤ ᱜᱟᱱ ᱚᱠᱛᱚ ᱾

ᱵᱚᱦᱚᱜ ᱟᱨ ᱵᱚᱦᱚᱜ ᱫᱚ ᱴᱤᱭᱩᱵᱽ ᱟᱨ ᱴᱤᱭᱩᱵᱽ ᱨᱮ ᱢᱤᱫ ᱴᱤᱭᱩᱵᱽ, ᱴᱤᱭᱩᱵᱤᱝ, ᱟᱨ ᱴᱤᱭᱩᱵᱽ ᱨᱮ ᱢᱤᱫ ᱴᱤᱭᱩᱵᱽ ᱛᱮ ᱦᱮᱲᱮᱢ ᱜᱮᱭᱟ ᱾ ᱚᱱᱟ ᱠᱚ ᱢᱩᱫᱽ ᱨᱮ, ᱞᱚᱞᱚ ᱫᱚ ᱢᱤᱫ ᱞᱚᱞᱚ, ᱟᱨ ᱢᱤᱫ (ᱟᱨᱟᱜ) (ᱟᱨᱟᱜ) ᱨᱮᱭᱟᱜ ᱞᱚᱞᱚ ᱛᱮ ᱯᱮᱨᱮᱡ ᱟᱠᱟᱱᱟ ᱟᱨ ᱮᱴᱟᱜ ᱠᱚ ᱫᱚ ᱯᱞᱟᱴᱤᱱᱟᱢ ᱠᱚ ᱨᱮ ᱞᱚᱞᱚ ᱛᱮ ᱠᱚ ᱛᱟᱦᱮᱱᱟ ᱾ 2.2 μm, μg . . . . . . . . . . . . . , extime lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕ lạgit̕, ᱱᱚᱶᱟ ᱫᱚ ᱞᱟᱛᱟᱨ ᱨᱮ ᱢᱮᱱᱟᱜ-ᱟ᱾

ᱡᱟᱦᱟᱸ ᱛᱤᱱ ᱨᱮ, ᱞᱚᱞᱚ ᱫᱚ ᱞᱚᱞᱚ ᱛᱮ ᱞᱚᱞᱚᱜ-ᱟ, ᱚᱱᱟ ᱛᱟᱭᱚᱢ ᱫᱚ ᱜᱞᱩᱠᱚᱡᱽ ᱨᱮ ᱢᱤᱫ ᱴᱟᱲᱟᱝ ᱵᱷᱤᱛᱨᱤ ᱨᱮ ᱢᱮᱱᱟᱜ-ᱟ ᱾ ᱱᱚᱣᱟ ᱦᱚᱨᱟ ᱫᱚ ᱞᱚᱞᱚ ᱨᱮᱭᱟᱜ ᱮᱥᱮᱨ ᱵᱟᱝ ᱠᱟᱱᱟ, ᱢᱮᱱᱠᱷᱟᱱ ᱚᱱᱟ ᱫᱚ ᱵᱟᱝ ᱵᱮᱥ ᱞᱮᱠᱟ ᱛᱮ ᱞᱚᱞᱚ ᱨᱮᱭᱟᱜ ᱮᱥᱮᱨ ᱦᱩᱭ ᱫᱟᱲᱮᱭᱟᱜᱼᱟ᱾ In addition, the shell and tube heat exchanger can also be designed as a single-pass or multi-pass structure according to actual needs to meet different heat exchange requirements.