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A cleaning method of primary cooler and purification system of primary cooler

A primary cooler and cleaning technology, applied in the primary cooler cleaning method and primary cooler purification system, can solve the problems of poor condensate quality, affecting the normal operation of the primary cooler, and reduced naphthalene dissolution and absorption capacity

Active Publication Date: 2022-06-21
SGIS SONGSHAN CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] When the temperature of the gas entering the upper section of the primary cooler is high, more heavy tar will be brought into the light tar. Using this part of tar to wash naphthalene in a cycle will easily cause the gap of the cooling water pipe inside the primary cooler to be blocked, and the temperature of the gas will drop. If it does not come down, the ability of light tar to dissolve and absorb naphthalene will decrease, and the naphthalene content after the primary cooler will increase, resulting in a vicious cycle of high gas temperature and high naphthalene content in the gas, which is not conducive to the purification of subsequent sections
[0004] Therefore, after the horizontal tube primary cooler is put into use for a period of time, a large amount of impurities will accumulate in the gaps of the internal cooling water pipes, which will increase the resistance of the primary cooler and need to be reversed and cleaned
[0005] However, when using emulsion and condensate to clean the upper section of the primary cooler and the lower section of the primary cooler, a large amount of impurities will enter the emulsion and condensate, especially the condensate containing a large amount of impurities after cleaning in the lower section of the primary cooler. It will irritate the condensate entering the lower condensate tank and pollute the condensate in the lower condensate tank, resulting in poor quality of condensate and reduced cleaning ability. In severe cases, it will also affect the normal operation of the primary cooler

Method used

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  • A cleaning method of primary cooler and purification system of primary cooler
  • A cleaning method of primary cooler and purification system of primary cooler

Examples

Experimental program
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Effect test

Embodiment 1

[0080] The application provides a cleaning method of a primary cooler, which comprises the following steps:

[0081] 1. Preparation

[0082] Before cleaning, the emulsion in the upper section 100 of the primary cooler and the condensate in the lower section 200 of the primary cooler are discharged, the emulsion pipe connected with the emulsion spraying device 110 is replaced with an ammonia water pipe, and the condensate spraying device 210 is replaced with an ammonia water pipe. The connected condensate pipe 220 is replaced with an ammonia water pipe, a displacement pump 430 is installed at the second liquid outlet 402 , the condensate pump 410 of the first liquid outlet 401 is closed, and the displacement pump 430 of the second liquid outlet 402 is opened.

[0083] 2. Steam purge

[0084] The upper section 100 of the primary cooler and the lower section 200 of the primary cooler are respectively purged for 6h with steam with a pressure of 0.4MPa and a flow rate of 0.3t / h. ...

Embodiment 2

[0088] The application provides a cleaning method of a primary cooler, which comprises the following steps:

[0089] 1. Preparation

[0090] Before cleaning, the emulsion in the upper section 100 of the primary cooler and the condensate in the lower section 200 of the primary cooler are discharged, the emulsion pipe connected with the emulsion spraying device 110 is replaced with an ammonia water pipe, and the condensate spraying device 210 is replaced with an ammonia water pipe. The connected condensate pipe 220 is replaced with an ammonia water pipe, a displacement pump 430 is installed at the second liquid outlet 402 , the condensate pump 410 of the first liquid outlet 401 is closed, and the displacement pump 430 of the second liquid outlet 402 is opened.

[0091] 2. Steam purge

[0092] The upper section 100 of the primary cooler and the lower section 200 of the primary cooler were respectively purged for 4h with steam with a pressure of 0.3MPa and a flow rate of 0.4t / h. ...

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Abstract

The application provides a method for cleaning a primary cooler and a purification system for the primary cooler, which belong to the technical field of cleaning the primary cooler. The cleaning method of the primary cooler includes purging the upper section of the primary cooler and the lower section of the primary cooler with steam respectively. After the steam is purged, use ammonia water to clean the upper section of the primary cooler and the lower section of the primary cooler respectively. First use steam to purge and heat the upper section of the primary cooler and the lower section of the primary cooler, and some impurities will be taken away by the steam, so that the gap between the cooling water pipes in the upper section of the primary cooler and the lower section of the primary cooler will be widened. The cleaning of the upper section of the cooler and the lower section of the primary cooler is conducive to the unimpeded flow of ammonia water in the upper section of the primary cooler and the lower section of the primary cooler and the removal of impurities. At the same time, the impurities that are heated and humidified will gradually soften and be more easily washed and taken away by ammonia water. The two methods of steam purging and ammonia water cleaning cooperate with each other to reduce the resistance of the upper section of the primary cooler and the lower section of the primary cooler, and improve the cleaning effect of the primary cooler.

Description

technical field [0001] The present application relates to the technical field of primary cooler cleaning, and in particular, to a primary cooler cleaning method and a primary cooler purification system. Background technique [0002] Primary cooler is a kind of cooling equipment used to cool hot gas in chemical production. For example, the condensing blasting process uses a high-efficiency horizontal tube cooler, which can be used to cool the gas from 80 to 90 °C to 21 to 23 °C, so that most of the naphthalene in the gas is removed by initial cooling. Make sure that the subsequent equipment is not blocked. [0003] When the temperature of the gas entering the upper section of the primary cooler is high, more heavy tar will be brought into the light tar. Using this part of the tar to circulate naphthalene to wash naphthalene is very likely to cause blockage of the cooling water pipe gap inside the primary cooler, and the gas temperature will drop. If not, the dissolving and ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F28G9/00C10K1/00C10K1/04
CPCF28G9/00C10K1/002C10K1/04
Inventor 邱誉杨涛杨志军郭震宇廖志均谢紫峰吴冠雄欧阳书山蒋耀煌余勇辉
Owner SGIS SONGSHAN CO LTD