Circulating drier and drying method
A drying method and technology of a drying device, which are applied in the field of circulating drying of drying objects, and can solve the problems of large gas volume, increased device construction costs, and increased costs.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0082] use figure 2 The circulating drying device shown is used to dry the polymer emulsion A and recover the polymer powder.
[0083] figure 2 The circulating drying device is in figure 1 The following equipment is added to the circulating drying device of the company: a heat exchanger for heat exchange between the combustion gas (processing gas) flowing in the supply line 26 and a part of the circulating gas flowing in the heat exchange line described later. 31, a preliminary heater 32 for removing the associated heavy mist contained in the circulating gas discharged from the condenser 15 and preheating the circulating gas, and cooling the cooling medium (water) for cooling the cooling water used for cooling the condenser 15 The cooling tower 33 and the heat exchanger 34 for cooling water exchange heat between the cooling water for the condenser 15 and the cooling medium from the subcooling tower.
[0084] In addition, in figure 2 In the circulating drying device of t...
Embodiment 2
[0104] use figure 2 The circulating drying device shown dries the polymer emulsion B to recover the polymer powder.
[0105] polymer emulsion B
[0106] In a polybutadiene emulsion of 218.75 parts by mass (solid content: 32 mass%), 13.2 parts by mass of methyl methacrylate, 14.4 parts by mass of styrene, and 2.4 parts by mass of ethyl acrylate were graft-polymerized to obtain a polymer Polymer Emulsion B (70% polybutadiene content in grafted polymer). The residual monomers methyl methacrylate and styrene in this emulsion were 1000 ppm and 1000 ppm. The solid content rate (mass %) was 40%. The polymer emulsion B is sent to the dryer 12 for drying at a flow rate of 82.5 kg / hour, and the polymer in the emulsion is recovered. Next, specific operating conditions will be described.
[0107] The circulating gas (dry gas 1563 kg / hour, water vapor 76 kg / hour) is heated to 180° C. by heater 11 and introduced into dryer 12 . The polymer emulsion B was sprayed into the dryer 12 at ...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 