Method for treating 2-mercaptobenzothiazole production waste
A technology for mercaptobenzothiazole and waste production, applied in chemical instruments and methods, amino compound purification/separation, inorganic chemistry, etc., can solve problems such as non-natural degradation, hazardous waste, and environmental pollution, and avoid secondary environmental pollution , solve the problem of environmental pollution, the effect of stable chemical properties
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Embodiment 1
[0014] The treatment method for 2-mercaptobenzothiazole production waste provided in this embodiment, wherein the 2-mercaptobenzothiazole production waste is the remaining waste obtained by refining with acid-base method, comprises the following steps:
[0015] (1) Solid-liquid separation: Take 200kg of 2-mercaptobenzothiazole production waste, heat it to 90°C with steam, and then put it into a centrifuge for solid-liquid separation to obtain 64kg of solids and 126kg of liquid A, and return the solids to Accelerator M workshop is refined and purified to obtain 40kg of product accelerator M;
[0016] (2) Liquid distillation: add liquid A in the distillation pot of the distillation tower to carry out distillation separation, and control the vacuum degree in the distillation tower to be 0.07Mpa; The temperature at the top of the tower is 115-190°C. Collect the obtained fractions to obtain fraction C, a total of 49.6kg, which is a mixture of aniline and benzothiazole. When the tem...
Embodiment 2
[0019] The treatment method of 2-mercaptobenzothiazole production waste provided in this embodiment, wherein the 2-mercaptobenzothiazole production waste is the remaining waste obtained by refining the toluene extraction method, comprises the following steps:
[0020] (1) Solid-liquid separation: Take 200kg of 2-mercaptobenzothiazole production waste, heat it to 95°C with steam, and then put it into a centrifuge for solid-liquid separation to obtain liquid A with 65kg of solids and 125kg of solids, and return the solids to Accelerator M workshop is refined and purified to obtain 42kg of product accelerator M;
[0021] (2) Liquid distillation: add liquid A to the distillation still of the distillation tower for distillation and separation, and control the vacuum degree in the distillation tower to be 0.07Mpa; the top temperature of the distillation tower is 60-115°C, and the obtained fractions are collected to obtain fraction B, A total of 10kg is a mixture of toluene and water...
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