1. Thin film drying system process flow
Sludge medium process: wet sludge receiving bin + sludge delivery pump + thin film dryer + semi-dry sludge output equipment + linear dryer + product cooler.
Exhaust gas medium process: evaporation steam (mixed steam)+ waste gas box + condenser + mist eliminator + induced draft fan + deodorization device.
The sludge in the sludge receiving bin is directly sent to the thin film dryer by the sludge screw pump for drying treatment. The sludge inlet of the thin film dryer is equipped with a pneumatic knife gate valve, which is interlocked with the logic control parameters of the feeding pump, feeding screw, safety protection of the thin film dryer and other equipment and detection instruments.
The thin film dryer body model, the net weight of a single machine is 33 000 kg, the net size of the equipment is Φ1 800×15 180, horizontal layout and installation, the sludge entering the thin film dryer is evenly distributed on the hot wall surface of the dryer by the rotor during the rotation process, while the paddle on the rotor repeatedly re-mixing the sludge on the hot wall surface, And forward to the outlet of the sludge, the water in the sludge is evaporated in the process. The semi-dry sludge particles after drying from the thin layer are transported to the linear dryer through the sludge conveyor (activated according to the demand of the moisture content of the sludge product), and then enter the sludge cooler. The sludge product is cooled by the air flowing in the cooler and the cooling water flowing in the shell and rotating shaft. The moisture content is reduced from 80% to 35%(the sludge moisture content of 35% is the process control upper limit of the single equipment of the thin film dryer).
The carrier gas discharged from the thin film dryer contains a lot of water vapor, dust and a certain amount of volatile gas (mainly H2S and NH3). If directly discharged, it will cause a certain degree of pollution to the environment. Therefore, this project considers the carrier gas collection system and condenser and mist remover to remove the dust and water vapor in the exhaust gas, which is opposite to the direction of sludge movement in the rotating cylinder. The exhaust gas pipe outlet above the sludge enters the condenser, and the water is cooled down from the evaporation exhaust gas. By means of indirect heat exchange, the spray water is removed by plate heat exchanger and cooling tower, so as to save water and reduce sewage discharge. Non-condensible gas (a small amount of steam, N2, air and sludge volatiles) passes through the demister. Finally, the exhaust induced draft fan is discharged from the drying system to the deodorization device.
The heat source demand is determined to be steam, which is taken from the thermal coverage pipe network built nearby the project implementation site. The steam supply conditions are steam pressure of 1.0MPa, steam temperature of 180 ℃ and steam supply of 2.5t /h.
2. Technical parameters of main equipment for thin film drying process
According to the demand of this project, the sludge treatment capacity of a single set of sludge drying system is determined to be 2.5t /h(according to the moisture content of 80%), and the sludge moisture content is 35%. The daily sludge treatment capacity of a single thin film dryer is 60 t/d(according to the moisture content of 80%), the rated evaporation capacity of a single thin film dryer is 1.731 t/h, the heat exchange area of a single thin film dryer is 50 m2, and the moisture content of sludge inlet is 80%, and the moisture content of sludge outlet is 35%. The heat source of the thin film dryer is saturated steam, and the quality of steam supply is imported parameters: steam temperature is 180 ℃, steam pressure is 1.0 MPa, steam consumption of a single thin film dryer is 2.33t /h, and the number of thin film dryer is 2, one for one use.
The saturated steam of 180 ℃ is transported to the linear dryer through the pressure pipeline, and it is used as a heat source to indirectly heat the semi-dry sludge. The water in the semi-dry sludge is further evaporated in the linear dryer. According to the actual demand of the sludge product (start and stop), the final sludge can reach 10% moisture content and go to the product cooler.
The processing capacity of linear dryer is 0.769t /h(moisture content 35%), the rated evaporation is 0.214t /h, the heat exchange area is 50 m2, the moisture content of sludge inlet of linear dryer is 35%, the moisture content of sludge outlet is 10%, the steam quality inlet parameters of linear dryer: The steam temperature is 180 ℃, the steam pressure is 1.0 MPa, the steam consumption of a single linear dryer is 0.253 t/h, and the quantity is equipped with 1 set.
The equipment type of carrier gas condenser is direct injection hybrid condenser, with an air intake of 3 500 Nm3/h, an inlet gas temperature of 95~110 ℃, an outlet gas temperature of 90~180 Nm3/h, and an outlet gas temperature of 55 ℃.
The equipment type of carrier gas induced draft fan is high pressure centrifugal fan, the maximum air suction volume is 400 Nm3/h, the air pressure is 4.8 kPa, the physical parameters of the carrier gas medium: the temperature is 45 ℃, the humidity is 80%~100% wet air odor gas mixture, a single set of drying system is equipped with 1 set.
The processing capacity of the product cooler is 1.8t /h, the sludge inlet temperature is 110 ° C, the sludge outlet temperature is ≤45 ° C, the heat exchange area is 20 m2, and the quantity is 1 unit.
3. Analysis of economic energy consumption during commissioning of thin film dryer
After nearly half a month of single commissioning and mud load commissioning of the thin film drying process system, the results are as follows.
The design configuration processing capacity of a single thin film dryer in this project is 60 t/d. At present, the average wet sludge treatment during the commissioning period is 50 t/d(moisture content is 79%), which has reached 83% of the designed sludge wet base treatment scale and 87.5% of the designed sludge dry base treatment scale.
The average moisture content of the semi-dry sludge produced by the thin film dryer is 36%, and the moisture content of the semi-dry sludge exported by the linear dryer is 36%, which is basically in line with the target value of the design product (35%).
Measured by the external saturated steam meter in the sludge drying workshop, the saturated steam consumption is 25 t/d, and the theoretical total daily heat consumption of latent heat of steam vaporization is 25 t×1 000×2 014.8 kJ/kg÷4.184 kJ =1.203 871 9×107 kcal/d. The average daily total evaporation water of the drying system is (50 t ×0.79)-[50 t ×(1-0.79)]÷(1-0.36)×1 000=23 875 kg/d, Then the unit heat consumption of sludge drying system is 1.203 871 9×107÷23 875=504 kcal/kg evaporated water; Because the sludge drying system is subject to the change of wet sludge moisture content, the quality of external steam, and the characteristics of semi-dry sludge product transportation equipment for granularity requirements and other factors, it is necessary to optimize the value of various variables in the future long-term trial operation, so as to summarize the best operating conditions and economic energy consumption index of the system.