Liquid-liquid reaction-based oxyalkylation continuous production process and process device thereof
An alkoxylation and reaction technology, which is applied in the field of continuous alkoxylation production process and its process equipment, can solve the problems of complex production process equipment, low production efficiency and large floor space for intermittent alkoxylation reaction
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2016-08-10
Smart Images
Figure 1 Figure 2
Abstract
Description
technical field
[0001] The invention belongs to the field of petrochemical industry, and more specifically relates to a liquid-liquid reaction-based alkoxylation continuous production process and a process device thereof. Background technique
[0002] Since the industrialization of alkoxylation (ethyl / propoxylation) in the 1930s, the batch alkoxylation reaction production process has always played an important role and is still in use today. The Italian Press company successfully developed a batch spray-type alkylation reaction production process. Switzerland Buss company has successfully developed a batch loop alkylation reaction production process. At present, the reaction production process applied in the field of alkoxylation production at home and abroad is mainly the batch stirred tank alkoxylation reaction production process, the Italian Press company's intermittent spray alkoxylation reaction production process and the Swiss Buss company's intermittent loop alkoxyla...
Examples
Embodiment Construction
[0043] The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
[0044] see Figure 1-Figure 2 , a continuous production process for alkoxylation based on a liquid-liquid reaction in this embodiment, comprising the following steps:
[0045] 1) Set control parameters
[0046] Prepare a control program for the DCS program controller 9, set the temperature of the reaction cooling water at 80-180°C, the temperature of the reaction material at 120-260°C, the pressure of the main pipe 21 of the gap reactor 1 at 8MPa, and the temperature at 280°C. The heating temperature of the starter heater 3 is 95-190°C, the heating temperature of the alkoxylation agent heater 6 is 20-80°C, the pressure of the pressure regulating valve 20 is 3-5.5MPa, and the DCS program controller 9 is opened; The reaction material is a chain initiator and an alkoxylating agent;
[0047] 2) Inject cooling water
[0048] The cooling water inlet regul...