Unlock instant, AI-driven research and patent intelligence for your innovation.

High-flux micro-channel reactor

A microchannel reactor and high-throughput technology, applied in the field of high-throughput microchannel reactors, can solve problems such as increased industrial application costs, inconsistent residence time, and blockage of microchannel reactors, achieving batch industrial production, Meet the needs of industrial production, the effect of controllable state

Pending Publication Date: 2020-05-12
品孚罗特过滤设备(北京)有限公司
View PDF0 Cites 2 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At present, there are mainly two types of gas-liquid-solid reactors, one is the traditional tank reactor, and the other is a small microchannel (10-1000 μm) reactor, but these two reactors have their own advantages and disadvantages. Advantages and disadvantages: the tank reactor has a wide range of applications, less investment, and is easy to put into production. However, the heat exchange area of ​​this type of reactor is small, the reaction temperature is not suitable for control, and the residence time is inconsistent. The product reaction cycle is long and the yield is not ideal; Microchannel reactors can fully solve the problems of small heat transfer area, long reaction cycle and yield, but the channel size of microchannel reactors is very small, and the particles in the raw materials have a certain agglomeration phenomenon in the production process, which makes microchannel reactors It is often blocked, and the biggest disadvantage of microchannel reactors is that its processing capacity is very limited, staying at the laboratory level, and it is difficult to apply to mass production
If there are too many microchannel reactors, the structure of the integrated reactor device will be very complicated, and it will be difficult to detect and control the state of a single microchannel reactor, which will virtually increase the cost of industrial application.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • High-flux micro-channel reactor
  • High-flux micro-channel reactor
  • High-flux micro-channel reactor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment Construction

[0033] The present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments, so that those skilled in the art can implement it with reference to the description.

[0034] It should be understood that terms such as "having", "comprising" and "including" as used herein do not entail the presence or addition of one or more other elements or combinations thereof. In the description of the present invention, the terms "transverse", "longitudinal", "axial", "radial", "upper", "lower", "front", "rear", "left", "right", The orientations or positional relationships indicated by "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. are based on the orientation or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and simplified descriptions, do not indicate or imply that the device or element referred to must have a specific orientation, be constructed a...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a high-flux micro-channel reactor. The reactor comprises a plurality of reaction units which are overlapped, wherein each reaction unit comprises a substrate which is horizontally arranged; an air guide groove is formed in the substrate; a first locating slot is formed by horizontally extending outwards in the circumferential direction of the air guide groove; a second locating slot is formed by horizontally extending outwards in the circumferential direction of the first locating slot; a cooling liquid inlet hole, a cooling liquid outlet hole and an air inlet hole areformed in the substrate; a gas injection plate is clamped in the first locating slot; a heat exchange plate is clamped in the second locating slot; the two opposite sides of the heat exchange plate and the side wall of the second locating slot form two drainage grooves with the bottom of the second locating slot as the bottom face; a flow guide groove is formed in the surface of the heat exchangeplate; a plurality of through heat exchange holes are formed at intervals in the end face of the heat exchange plate; and the two ends of the multiple heat exchange holes are communicated with the twodrainage grooves correspondingly. According to the invention, the gas-liquid-solid three-phase contact is sufficient, the yield is high, the channel is large in size but not easy to block, the batchindustrial production can be realized, and the industrial production requirements are met.

Description

technical field [0001] The invention relates to the technical field of microreactors, in particular to a high-throughput microchannel reactor. Background technique [0002] At present, there are mainly two types of gas-liquid-solid reactors, one is the traditional tank reactor, and the other is a small microchannel (10-1000 μm) reactor, but these two reactors have their own advantages and disadvantages. Advantages and disadvantages: the tank reactor has a wide range of applications, less investment, and is easy to put into production. However, the heat exchange area of ​​this type of reactor is small, the reaction temperature is not suitable for control, and the residence time is inconsistent. The product reaction cycle is long and the yield is not ideal; Microchannel reactors can fully solve the problems of small heat transfer area, long reaction cycle and yield, but the channel size of microchannel reactors is very small, and the particles in the raw materials have a certa...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): B01J19/00
CPCB01J19/0093
Inventor 周旭陈新刚郑超杨志彬杨春清张珍浩
Owner 品孚罗特过滤设备(北京)有限公司