根据公司计划投资两条处理量为500T /24h加1条50T /24h的

The two treatment plans to invest an amount of 500T / 24h plus a 50T / 24h line of fishmeal and fish oil, are now processed by an amount of 1050T / 24h of fishmeal and fish oil production line calculation, the amount of processing of raw fish per hour as the 42T. After a series of production process, the finished product obtained from about fishmeal 10.5T / h, refined oil 1.05T / h. Most of the remaining water in the fish during cooking and drying to form water vapor is evaporated, i.e. the amount of exhaust gas is generated: 26T / h, equivalent to 52000m3 / h (calculated as the evaporation temperature of 95 ℃). Will be substantially reduced by the air and condensed water condensed gas after cooling, a high concentration of the exhaust gas amount calculation by 10000m3 / h condensed.

According to the company's plan to invest in two fishmeal oil production lines with a processing volume of 500T /24h plus 1 50T/24h, the fishmeal fish oil production line with a processing volume of 1050T/24h is now calculated, i.e. the processing volume of raw fish and so on per hour is 42T. After a series of production and processing processes, about 10.5T/h of finished fishmeal and 1.05T/h of finished oil. The remaining majority of the fish body moisture in the cooking and drying process in the form of water vapor is evaporated, that is, the emission of: 26T/h, equivalent to 52000m3/h (calculated at the evaporation temperature of 95 degrees C). The amount of air will be greatly reduced after condensation by air condensation and cooling water, and the high concentration of exhaust gas after condensation is calculated at 10000m3/h.

According to the company's plan to invest two fish meal and fish oil production lines with a processing capacity of 500t / 24h plus one 50t / 24h, the current calculation is based on the fish meal and fish oil production line with a processing capacity of 1050t / 24h, that is, the processing capacity of raw fish per hour is 42t. After a series of production and processing processes, about 10.5t/h fish meal and 1.05t/h oil product can be obtained. Most of the remaining water in the fish body is evaporated in the form of water vapor in the process of cooking and drying, i.e. the output of waste gas is 26t / h, equivalent to 52000m3 / h (calculated according to the evaporation temperature of 95 ℃). After air condensation and cooling water condensation, the gas volume will be greatly reduced, and the high concentration waste gas volume after condensation is calculated as 10000m3 / h.