Sludge calorific value control method
A control method and sludge technology, applied in the direction of dewatering/drying/concentrating sludge treatment, etc., can solve problems such as the inability to solve the calorific value control, achieve the technical problems of solving the calorific value control, widen the high value, and facilitate the industrialized production. Effect
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Embodiment 1
[0027] In this example, the calorific value of the sludge is controlled by adding an auxiliary fuel that can not only help the sludge to be squeezed and dehydrated but also provide heat value to the initially concentrated and dewatered sludge, and carry out dehydration and drying methods of mechanical pressing and dehydration and drying to remove water. Auxiliary fuel is added when the sludge is dewatered by mechanical pressing and dewatered by drying. During mechanical press dehydration, the auxiliary fuel is added to the sludge by laying on the filter medium of the tension press or counter press of the mechanical press dewatering equipment. The method of adding this auxiliary fuel is the same as that disclosed by the applicant in Chinese Patent Application 200810059917.2 "A Method for Bridging and Dewatering Sludge" by laying an overhead tank composed of one or more solid particle auxiliary materials between the filter medium and the sludge. layer method. By adding auxiliar...
Embodiment 2
[0035] In this embodiment, the drying and dewatering process adopts the natural air-drying drying and dewatering process, and the sludge that has been dehydrated by mechanical pressing and added with auxiliary fuel is then dried and dewatered by natural air drying. The method of controlling the calorific value of the sludge includes mechanical pressing dehydrated and air-dried, figure 2 It is the control process of the combined process control method of mechanical pressing dehydration + natural air drying. The auxiliary fuel is added at the feed inlet of the belt filter press, the feed inlet of the high pressure dehydration zone and before natural air drying. The moisture content of the sludge dewatered by mechanical pressing basically meets the conditions for pressing and forming. Before forming, according to the specific conditions of the cohesiveness of the treated industrial sludge, auxiliary fuel is added to further increase the calorific value of the sludge and improve t...
Embodiment 3
[0038] see image 3 , In this embodiment, the drying and dewatering process adopts the drying and dewatering process of heating and drying, and the sludge dewatered by mechanical pressing and added with auxiliary fuel is then heated and dried for drying and dewatering. Auxiliary fuel is added at the feed inlet of the press and the feed inlet of the high-pressure press dehydration zone. The addition amount of the press feed port is given by the press process, and auxiliary fuel is added to the feed port of the high-pressure press dehydration zone to help the sludge to dehydrate further. According to the requirements of the conditions for the discharge moisture, the required drying time can be known through the process data, and the drying time is set in the control system. When the set time is up, the control system sends out a discharge signal. Whether to add auxiliary fuel before heating and drying, according to the amount of auxiliary fuel added during mechanical pressing a...
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