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Physics, 26.12.2021 14:00 franklinkaylieg1145

Thực phẩm lỏng đang được chuyển qua một đường ống không cách nhiệt ở 90 ° C. Tốc độ dòng chảy của sản phẩm là 0,25 kg / s và có khối lượng riêng là 1000 kg / m³, nhiệt dung riêng 4 kJ / (kg K), độ nhớt 8 x 106 Pa s, và độ dẫn nhiệt 0,55 W / (m K). Giả sử hiệu chỉnh độ nhớt là không đáng kể. Đường kính ống bên trong là 20 mm với độ dày 3 mm được làm bằng thép không gỉ (k = 15 W / [m ° C]). Nhiệt độ bên ngoài là 15 ° C. Nếu hệ số truyền nhiệt đối lưu bên ngoài là 18 W / (m2 ° C), hãy tính tổn thất nhiệt ở trạng thái ổn định từ sản phẩm trên một đơn vị chiều dài ống.

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