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Process and equipment for continuous production of diphenylguanidine

A biphenylguanidine and process technology, applied in the field of continuous production of diphenylguanidine production technology and equipment, can solve the problems that the operating conditions of each kettle cannot be completely unified, the quality of finished products is unstable, and increase equipment, etc., so as to improve the utilization rate of equipment and production efficiency, product quality improvement and stability, and the effect of reducing operators

Active Publication Date: 2020-08-21
SHANDONG SUNSINE CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of this process are as follows: DPG oxidation is a single-pot batch reaction, and the single-pot operation is not only cumbersome, but also has disadvantages such as high cost and unstable quality.
The traditional method needs to use steam to heat up first, and then use water to cool down, and the steam consumes a lot of energy; the equipment is frequently opened, and the power consumption is high; If the production capacity needs to be increased, the only way to increase the equipment is to increase the investment; because the operating conditions of each kettle cannot be completely unified, resulting in unstable quality of the finished product; most of the single-table oxidation kettles used in the traditional process are mechanically sealed, which are easy to leak and cause high temperature and explosion due to friction , poor safety performance

Method used

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  • Process and equipment for continuous production of diphenylguanidine

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Comparison scheme
Effect test

Embodiment 1

[0039] Embodiment 1. This embodiment provides equipment for continuous production of diphenylguanidine, including oxygen buffer tank 7, oxygen pipeline, diphenyl thiourea slurry metering pump 1, diphenyl thiourea slurry pipeline, catalyst feeding device 9, oxidation Heater 4, oxidation circulation pump 2, primary oxidation reactor 5, secondary oxidation reactor 6, water washing tank 8, discharge pump 3; the primary oxidation reactor 5 is provided with a Venturi mixer 14, so The upper part of the first-stage oxidation reactor 5 communicates with the upper part of the second-stage oxidation reactor 6 through an oxygen pipeline, communicates with the diphenylthiourea slurry metering pump 1 through a diphenylthiourea slurry pipeline, and communicates with a catalyst feeding device 9 through a catalyst feeding pipeline. Connected; the inlet end of the oxidation circulation pump 2 is connected to the bottom of the primary oxidation reactor 5 through a pipeline, the outlet end is conne...

Embodiment 2

[0040] Embodiment 2. This embodiment provides a process for the continuous production of diphenylguanidine, including the following steps: (1) Pump 3000L of 25% (W / W) ammonia water into the first-stage oxidation reactor through a metering pump, and stop the pump. Turn on the oxidation circulation pump;

[0041] (2) Add 0.5 kg of copper acetate from the catalyst feeding device;

[0042] (3) Adjust the valve group from the oxygen buffer tank to the secondary oxidation reactor to increase the pressure of the system to 0.45-0.5Mpa;

[0043] (4) Turn on the heater steam and heat up the ammonia to 60°C;

[0044] (5) The 50000L diphenylthiourea slurry prepared in advance is added to the first-stage oxidation reactor at 5000L / h through a metering pump, and the first-stage oxidation reactor is used to control the level of the first-stage oxidation reactor. At 2 meters, when the liquid level of the secondary oxidation reactor reaches 0.5 meters, start the stirring of the secondary oxidation re...

Embodiment 3

[0049] Embodiment 3, this embodiment provides a process for the continuous production of diphenylguanidine, including the following steps: (1) 3000L of 25% (W / W) ammonia water is pumped into the primary oxidation reactor through a metering pump, and the pump is stopped. Turn on the oxidation circulation pump;

[0050] (2) Add 2 kg of copper acetate from the catalyst feeding device;

[0051] (3) Adjust the valve group from the oxygen buffer tank to the secondary oxidation reactor to increase the pressure of the system to 0.45Mpa;

[0052] (4) Turn on the heater steam and heat up the ammonia to 65°C;

[0053] (5) The 50000L diphenylthiourea slurry prepared in advance is added to the first-stage oxidation reactor at 5000L / h through a metering pump, and the first-stage oxidation reactor is used to control the level of the first-stage oxidation reactor. At 2 meters, when the liquid level of the secondary oxidation reactor reaches 0.5 meters, start the stirring of the secondary oxidation r...

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Abstract

The invention belongs to the technical field of production of rubber accelerators and relates to a production process and equipment for continuously producing diphenylguanidine. The equipment comprises an oxygen buffer tank, an oxygen pipeline, a diphenylthiourea slurry metering pump, a diphenylthiourea slurry pipeline, a catalyst adding device, a heater, an oxidation circulating pump, a primary oxidation reactor, a secondary oxidation reactor, a water washing tank, a discharging pump and the like. The production process is a process for continuously producing diphenylguanidine. Through two-stage oxidation reactions and continuous feeding and discharging, the production process is better than existing processes in the aspects of both technology and economy, continuous production is reallyrealized, and the process realizes energy conservation and consumption reduction and is safe and environmentally friendly.

Description

Technical field [0001] The invention belongs to the technical field of production of rubber accelerators, and relates to a production process and equipment for the continuous production of diphenylguanidine. Background technique [0002] Rubber accelerator DPG, chemical name diphenylguanidine, white powder, non-toxic, but irritating when in contact with the skin. This product is used in natural rubber and synthetic rubber. It is often used as an active agent for thiazole, thiuram and sulfenamide accelerators. It can be used for continuous vulcanization when used together with accelerators DM and TMTD. In neoprene rubber, this product It has the function of plasticizer and peptizer. The use of this product has discoloration, so it is not suitable for white and light-colored rubber products, and rubber products in contact with food. It is mainly used to make tires, rubber sheets, shoe soles, industrial products, hard rubber and thick products. [0003] The traditional production pr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C277/08C07C279/18B01J8/00B01J8/10B01J8/26B01J19/00
CPCB01J8/0015B01J8/10B01J8/26B01J19/0013C07C277/08C07C279/18
Inventor 刘坤单鑫静海旺谢道庆张顺郭焕宇沙德昌
Owner SHANDONG SUNSINE CHEM
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