High performance continuous reaction/separation process using a continuous liquid-solid contactor

a liquid-solid contactor, high-performance technology, applied in separation processes, ion-exchangers, organic chemistry, etc., can solve the problems of high cost, high temperature sensitivity and azeotrope formation, and prevent the system from handling many reaction/separation applications, etc., to improve product quality, reduce cost, and increase productivity

Inactive Publication Date: 2004-05-27
CALGON CARBON
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0018] Particularly, when used with the present process, this device allows for a wide variety of processing possibilities that have not been taught in the prior art of combined reaction / separation technologies. The ability to incorporate parallel liquid flow, reverse liquid flow, and combination unit configuration, as single or multiple zones and in any combination within a single unit, is a capability that is unique to the present invention. This can prove especially advantageous in the present invention because this process is not limited to a series bed arrangement and unidirectional fluid flow as is the prior art. This flexibility advantageously increases productivity, reduces costs and improves product quality over traditional processes. Other features, aspects and advantages of the present invention will become better understood or apparent from a perusal of the following detailed description and examples of the invention and appended claims.

Problems solved by technology

Despite these advantages, however, this technique has drawbacks, which include temperature sensitivity and azeotrope formation.
Despite these advantages, the traditional SMB techniques have certain drawbacks.
This limited configuration inherently prevents the system from handling many reaction / separation applications, such as those that require high mass flow, toxin removal, and individual optimization of reaction and separation conditions.
With these applications, the traditional SMB reactor system becomes very complicated, very expensive, and sometimes impractical.
Furthermore, none of the present technologies allow for a continuous reaction and separation process using contacting beds arranged in parallel, rather than series, having reverse flow capabilities, or combination unit capabilities.

Method used

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  • High performance continuous reaction/separation process using a continuous liquid-solid contactor
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  • High performance continuous reaction/separation process using a continuous liquid-solid contactor

Examples

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example 2

Parallel Flow Configuration

[0032] In another embodiment of the present invention, multiple columns are connected together in parallel flow mode. As shown for example in FIG. 3, the feed 11 column is connected in parallel. The components of the process system can, either alone or alternatively in combination, employ parallel flow, including the feed, eluent, raffinate, or extract streams. This offers the ability to obtain high flow rates while maintaining an acceptable pressure drop and reaction performance for the process. These capabilities prove especially useful for reactions that require long hold-up time and high mass flow. Such reactions can encounter high pressure drops when performed using the prior art configuration where the columns are connected in a series configuration. The pressure drop requirement for a given process is a very important design parameter. As the pressure drop requirement increases, the cost of the equipment increases and at some point the process becom...

example 3

2-in-1 Configuration (Type A)

[0033] In another embodiment of the present invention, one or multiple columns are connected together separately inside of a separation train, as shown for example in FIG. 4. This combination unit configuration is also referred to herein as a "2-in-1 flow configuration." The 2-in-1 flow configuration optimizes the reaction and separation operations by allowing each to be carried out under different conditions. In addition to reaction / separation, another reaction may be conducted, i.e., reaction / separation / reaction or 3-in-1. This configuration is not limited to 2-in-1 or 3-in-1, but may be used to perform multiple reactions and separations in N-in-1 configuration, where N is an integer greater than 1. The feed 11 column is not connected directly in series with the column that precedes it, but rather is connected independently into the liquid flow of the system. Thus, the user can vary the hold-up time, the composition, and the temperature for the reactio...

example 4

2-in-1 Configuration (Type B)

[0038] In another embodiment of the present invention, one or multiple columns are connected together in a zone that is still within the same unit but outside the separation process zone. The 2-in-1 flow configuration (type A) shown in Example 3 incorporates a reaction zone into the middle of a traditional SMB process. The composition of the material in the reaction zone is influenced by the composition of the adjacent column which will move into the reaction zone position. With the 2-in-1 flow configuration (type B), the reaction zone V receives the next column from elution in zone I. Because of this process feature, the reaction zone is a clean column rather than a column that already contains a certain composition of material. This allows for additional process optimization that goes beyond the 2-in-1 (type A) configuration. This type of process is also outside the traditional SMB process which relies on columns that are endlessly connected in series....

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Abstract

A process for reaction and separation which comprises inputting a process material into at least one column of a plurality of columns wherein each column has at least one inlet for accepting flow from another column or group of columns, an external feed stream, an external eluent stream or a combination thereof, and each column has at least one outlet for connecting to another column, a group of columns, an external product stream or a combination thereof. Each column is independently operable in an up-flow or down-flow mode and connected independently to one of the group comprising another column, an external feed stream, an external eluent stream, an external product stream and combinations thereof.

Description

[0001] This invention relates to a process for chemical reaction and separation using a liquid-solid contacting system and, more particularly, to a chemical reaction and separation process using a plurality of columns wherein each column can be independently connected and independently operated for flow inlet and outlet, such as parallel fluid flow, reverse fluid flow or combination of flows.[0002] Combining a process for conducting a continuous reaction with concurrent separation into a single process technique has received renewed attention in recent years. Various reaction / separation technologies are being investigated and have reached differing degrees of development or commercial viability. Fairly developed techniques include, for example, reactive distillation techniques and reactive chromatography. Other techniques, such as reactive membranes and reactive crystallization techniques, are also being developed. Some of these techniques have provided certain benefits such as redu...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B01D15/18C07C37/20C07C39/16
CPCB01D15/1857B01D15/1864B01D2215/023B01D2215/028C07C37/20C07C39/16
Inventor CHIANG, CHEN-CHOUFAIR, DAVID L.
Owner CALGON CARBON
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