Catalyst for treating waste water, method for preparing the same and process for treating waste water

Inactive Publication Date: 2001-09-20
NIPPON SHOKUBAI CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

0022] The present invention has been accomplished to solve these problems. Accordingly, an object of the present invention is to provide a catalyst for oxidizing and/or d

Problems solved by technology

Biological treatment has a disadvantage in consuming a long time to decompose the oxidizable substances in the waste water.
Further, this treatment is limited to treat waste water of a low concentration.
The method demands a large space for the installation of facilities for diluting waste water.
Further, microorganisms that are used in the biological treatment are susceptible to change of the environment such as temperature.
These factors make it difficult to stably operate the waste water treatment for a long time.
Such a low temperature and low pressure condition contributes to loosening the requirements for reaction.
Therefore, it has been impossible to utilize activated carbon as a catalytic component for wet oxidation.
Specifically, in the case where a catalyst containing activated carbon is employed, it is often the case that the catalyst does not have heat resistance of resisting a high temperature such as 170.degree. C. or more.
Even if the catalyst exhibits a high catalytic activity at an initial stage of reaction, the catalytic activity deteriorates rapidly within 100 hours or less.
Therefore, utilization of the catalyst containing activated carbon has been practically impossible.
On the other hand, in the case where there is not provided sufficient measures for protecting the catalyst during its use even at a low temperature such as 170.degree. C. or less, the activated carbon itself is subjected to combustion due to existence of oxygen containing gas.
Consequently, the catalytic activity also deteriorates within a short period such as within one hundred to several hundreds hours.
Thus, utilization of the activated-carbon-containing catalyst was impossible in the conventional wet oxidation for treating waste water.
This technique is not applicable to treating an organic compound having two or more carbon atoms per molecule or inorganic compound.
Also, this publication does not fully consider durability (heat resistance) of the catalyst in which a precious metal is supported on activated carbon.
The above problems such as a possibility of combustion of activated carbon itself and deterioration of catalytic activity were also observed when treating waste water containing organic and/or inorganic oxidizable substances at the time of temperature rising by starting up the operation of the wet oxidation apparatus

Method used

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  • Catalyst for treating waste water, method for preparing the same and process for treating waste water
  • Catalyst for treating waste water, method for preparing the same and process for treating waste water
  • Catalyst for treating waste water, method for preparing the same and process for treating waste water

Examples

Experimental program
Comparison scheme
Effect test

example 1 to 5

[0160] 500 hours of waste water treatment was performed under the following conditions with using the equipment illustrated in FIG. 1. A reactor 1 having cylindrical shape (a diameter of 26 mm.phi. and a length of 3000 mm) was used in the treatment. Into the reactor, loaded were 1 liter (380 g) of pellet type solid catalysts having a diameter of 4 mm .phi. to give a catalyst bed height of 1880 mmH. The solid catalyst had activated carbon and platinum as main components and included 0.3 mass % of platinum with respect to the total amount of the solid catalyst. In addition, as the waste water to be treated in the present examples, used was waste water exhausted by manufacturing facilities of aliphatic carboxylic acids and aliphatic carboxylate. The waste water contained organic compounds having 2 or more carbon atoms per molecule such as alcohol, aldehyde and carboxylic acid. The COD (Cr) concentration of the waste water was 20000 mg / liter and pH thereof equaled 2.8. In addition, 55% ...

example 6

[0164] The treatment was performed in the same manner including the same catalyst, treatment processes, treatment conditions and equipment as in example 4, except that the treatment temperature was set to 140.degree. C. This result was also shown in table 1. In addition, after 5000-hour treatment, the catalyst was extracted from the reactor to be observed. As a result, it was found that the catalyst in this experiment stayed unchanged after the treatment.

example 7

[0165] The treatment was performed in the same manner including the same catalyst, treatment processes, treatment conditions and equipment as in example 1 except for the following 3 points: 1) the treatment temperature was set to 95.degree. C.; 2) the treatment pressure was set to the atmosphere pressure; and 3) the supply amount of oxygen-containing gas was adjusted to 0.40 in term of O.sub.2 / COD. This result was also shown in table 1. In addition, after 5000-hour treatment, the catalyst was extracted from the reactor to be observed. As a result, it was found that the catalyst in this experiment stayed unchanged after the treatment.

1TABLE 1 COD(Cr) COD(Cr) Treatment Treatment Efficiency Efficiency After Oxygen After 500 Hour Concentration 5000 Hour Treatment In Exhaust Treatment O.sub.2 / COD D Value (%) Gas (vol %) (%) Example 0.75 0.79 77 0 --1 Example 0.85 0.89 86 0 86 2 Example 0.95 1.00 95 0.2 95 3 Example 1.00 1.05 93 1.5 92 4 Example 1.10 1.15 93 3.5 90 5 Example 1.00 1.00 99....

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Abstract

This invention discloses a method for oxidizing and/or decomposing organic and/or inorganic oxidizable substances in waste water by wet oxidation with a use of a catalyst, wherein the oxidizable substances are oxidized and/or decomposed with an oxygen containing gas in the presence of the catalyst under pressure such that said waste water retains the liquid phase thereof at temperature of 50 to less than 170° C.; the catalyst contains activated carbon; and controlling an oxygen concentration in an exhaust gas in the range from 0 to 5 vol %. The present inventive method is capable of treating waste water efficiently for a long period in a stable manner at the reduced temperatures and as compared with the substantially higher temperatures and pressures used in many of the prior art method.

Description

[0001] 1. Field of the Invention[0002] This invention relates to a process for treating waste water containing organic and / or inorganic oxidizable substances by wet oxidation with a use of a catalyst performed in the presence of an oxygen-containing gas, and more particularly pertains to a process for treating waste water efficiently for a long period in a stable manner by using a solid catalyst containing activated carbon and by regulating the oxygen concentration in an exhaust gas.[0003] This invention further relates to a process for suppressing deterioration of the catalytic activity of the solid catalyst at the time of temperature rising when starting up a operation of the wet oxidation and / or at the time of temperature lowering when suspending the operation by protecting the catalyst according to needs, or to a process for efficiently recovering the degraded catalytic activity of the solid catalyst containing activated carbon according to needs.[0004] 2. Description of the Rel...

Claims

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Application Information

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IPC IPC(8): B01J23/64B01J21/18B01J23/40B01J23/54B01J23/56B01J23/62B01J23/63B01J23/644B01J23/656B01J23/89B01J37/02C02F1/72C02F11/08
CPCB01J21/18B01J23/40B01J23/54B01J23/626B01J23/63B01J23/6447B01J23/6562B01J23/89B01J23/8906B01J37/0205C02F1/725C02F11/08B01J23/56B01J23/64
Inventor SHIOTA, YUSUKEMIYAZAKI, KUNINORIHASHIMOTO, TAKAAKIISHII, TOHRU
Owner NIPPON SHOKUBAI CO LTD
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