Gas-phase phosgenation reactor and application thereof in synthesis of organic isocyanates

A reactor and phosgenation technology, applied in the field of reactors, can solve the problems of difficult wall thickness detection, inflexible equipment adjustment, equipment fatigue, etc., to improve the flow field shape and reaction conditions, reduce average energy consumption and maintenance Cost, Guarantee Stability and Smooth Outcomes

Pending Publication Date: 2018-02-23
山东彼岸化工产品有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At the current technical level, the mixer integrates the nozzles of phosgene and organic amines in a small space, resulting in complicated equipment processing, narrow installation space, difficulty in heat tracing, heavy equipment, difficult disassembly and assembly, and equipment Adjustment is not flexible
The entire mixer is often discarded due to a small damage or modification; 3. Since the reactor body is a jacketed tube installed vertically, the jacket contains a large flow of heat-conducting molten salt fluid, and the density of liquid heat-conducting molten salt is relatively high. Large, high-density and large-flow scouring caused the equipment to vibrate continuously, resulting in flow field disturbance in the reaction area and equipment fatigue, and also had a negative impact on production stability; 4. Since the reactor body is a jacketed tube installed vertically , the jacket is a large flow of heat-conducting molten salt fluid, and heat-conducting molten salt usually contains a certain amount of free chlorine (which has a certain corrosive effect on stainless steel), coupled with high-temperature fluid scouring, the problem of local thinning of equipment is more obvious , and the difficulty of detecting the wall thickness in the jacket is relatively large, which has formed a large hidden danger in the long-term operation of the production device; High-power armored electric heating has the problems of large investment, high failure rate, high operation and maintenance costs

Method used

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  • Gas-phase phosgenation reactor and application thereof in synthesis of organic isocyanates
  • Gas-phase phosgenation reactor and application thereof in synthesis of organic isocyanates
  • Gas-phase phosgenation reactor and application thereof in synthesis of organic isocyanates

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] The length of the mixer bushing is 1100mm, the angle between the inclined surface of the expansion port and the vertical surface is 11.2°, the wall thickness of the mixer bushing is 31.5mm; the thickness of the ring gap between the outer wall of the mixer bushing and the inner wall of the reactor body is 8mm; organic amine and inert The diameter of the gas mixture channel pipe is φ26.7, and the distance between the outlet and the upper edge of the expansion port of the bushing is 45mm.

[0048] After preheating the reactor with 0.8MPa medium-pressure steam, start the molten salt circulation, and control the temperature of the heat-conducting molten salt to 342°C, and circulate the phosgene that is also preheated to 342°C into the reactor, and the flow rate of phosgene is 1650kg / h , adjust the internal pressure of the reactor to an absolute pressure of 78kPa, and after the pressure and phosgene flow are stable, put into the mixed gas of toluene diamine (TDA) and nitrogen ...

Embodiment 2

[0050] The length of the mixer bushing is 1100mm, the angle between the inclined surface of the expansion port and the vertical surface is 11.2°, and the wall thickness is 31.5mm; the thickness of the ring gap between the outer wall of the mixer bushing and the inner wall of the reactor body is 8mm; the mixed gas of organic amine and inert gas The diameter of the channel pipe is φ26.7, and the distance between the outlet and the upper edge of the expansion port of the bushing is 45mm.

[0051] After preheating the reactor with 0.8MPa medium-pressure steam, start the molten salt circulation, and control the temperature of the heat-conducting molten salt to 340°C, and circulate the phosgene that is also preheated to 340°C into the reactor, and the flow rate of phosgene is 1820kg / h , adjust the pressure in the reactor to be an absolute pressure of 83-85kPa, and after the pressure and phosgene flow are stable, drop into 4,4'-diaminodicyclohexylmethane (H 12 Mixed gas of MDA) and n...

Embodiment 3

[0053] The length of the mixer bushing is 920mm, the angle between the inclined surface of the expansion port and the vertical surface is 10.8°, and the wall thickness is 29mm; the thickness of the ring gap between the outer wall of the mixer bushing and the inner wall of the reactor body is 6mm; the mixed gas channel of organic amine and inert gas The diameter of the pipe is φ33.4, and the distance between the outlet and the upper edge of the expansion port of the bushing is 0mm.

[0054] After preheating the reactor with 0.8MPa medium-pressure steam, start the molten salt cycle, and control the temperature of the heat-conducting molten salt at 330-335°C, and circulate the phosgene that is also preheated to 330-335°C into the reactor. 1820kg / h, adjust the pressure inside the reactor to an absolute pressure of 85-90kPa, after the pressure and phosgene flow are stable, put in the mixed gas of isophoronediamine (IPDA) and nitrogen preheated to 330-335°C, of ​​which IPDA The flow...

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Abstract

The invention provides a gas-phase phosgenation reactor, comprising a reactor body and a mixer body, wherein a cover plate is arranged at the top end of the reactor body, the reactor body is divided by an inner pipe layer, a middle pipe layer and a reactor outer layer into a center chamber, a middle interlayer and an outer jacket, as three passages, from inside to outside, the mixer body comprisesan organic amine and inert gas mixture passage pipe and a mixer lining, the mixer body is passed through the cover plate on the reactor body and positioned in the center chamber of the inner pipe layer of the reactor body, and an annulus is reserved between the outer wall of the mixer body and the inner wall of the inner pipe layer of the reactor body. The mixer herein is divided into multiple independent assembly parts, so that working is safer, simpler and more convenient; the annulus is reserved between the outer wall of the mixer body and the inner wall of the inner pipe layer of the reactor body, so that the gas-phase phosgenation reactor has improved transferring efficiency and higher capacity.

Description

technical field [0001] The invention belongs to the field of reactors, in particular to a gas-phase phosgenation reactor and its application in the synthesis of organic isocyanate. Background technique [0002] In the field of organic isocyanate synthesis, the gas-phase phosgenation reaction process is gradually becoming mature, and has achieved large-scale production in the field of toluene diisocyanate (TDI) and aliphatic isocyanate (ADI). However, as an emerging industrial technology, the gas-phase phosgenation process still has many technical details that need to be improved. The design of the reactor, as the technical core part of the gas phase phosgenation process, still has the following significant problems: [0003] 1. In the gas phase phosgenation reaction process, the core part of the reactor is the mixer installed on its top. In the process of synthesizing organic isocyanates by gas-phase phosgenation reaction process, the reaction is usually forced to stop due...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J12/00C07C263/10C07C265/14
CPCB01J12/00C07C263/10C07C265/14
Inventor 薛永和
Owner 山东彼岸化工产品有限公司
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