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CN100436647C - Scale eliminating method for casing pre-heater - Google Patents

Scale eliminating method for casing pre-heater Download PDF

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Publication number
CN100436647C
CN100436647C CNB2005102002089A CN200510200208A CN100436647C CN 100436647 C CN100436647 C CN 100436647C CN B2005102002089 A CNB2005102002089 A CN B2005102002089A CN 200510200208 A CN200510200208 A CN 200510200208A CN 100436647 C CN100436647 C CN 100436647C
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China
Prior art keywords
sleeve pipe
cleaning
scabs
preheater
stage
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Expired - Fee Related
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CNB2005102002089A
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Chinese (zh)
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CN1847460A (en
Inventor
高振文
铝胜利
杨小平
白英伟
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Guiyang Aluminum Magnesium Design and Research Institute Co Ltd
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Guiyang Aluminum Magnesium Design and Research Institute Co Ltd
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Abstract

The present invention discloses a method for cleaning scabs of a sleeve pipe preheater, which uses diluted sulfuric acid for cleaning scabs of a sleeve pipe preheater. The method for cleaning scabs of a sleeve pipe preheater comprises: diluted sulfuric acid for cleaning scabs of a sleeve pipe preheater is firstly filled from a last-stage sleeve pipe and discharged from a first-stage sleeve pipe so as to clean the sleeve pipe preheaters; the cleaning is carried out repeatedly, until the scab in the last-stage sleeve pipe is clean; thus, the scabs in the sleeve pipe preheater are cleaned. The present invention has the advantages that the quantity of the sleeve pipe preheaters can be increased so as to replace autoclaves; the first-stage sleeve pipe is used instead of a first-stage autoclave for preheating so as to save the construction investment by about 3 million yuan; when a five-stage sleeve pipe preheater is changed into a six-stage sleeve pipe preheater, the live steam can be saved by about 0.12t per ton of aluminium oxide, and the live steam can be saved by 96 kt every year for an alumina plant with the annual output of 800 kt, namely that the production cost can be saved by about 7 million yuan every year; the method for cleaning scabs of a sleeve pipe preheater has the advantages of favorable cleaning effect, and has favorable effect on scab treatment for hot sections; acid is filled from the front end and the rear end for cleaning so as to reduce the corrosion of diluted sulfuric acid to seamless steel pipes.

Description

套管预热器结疤的清洗方法 Cleaning method of casing preheater scab

技术领域: Technical field:

本发明涉及一种氧化铝生产中,用于原矿浆预热的套管预热器结疤的清洗方法,属于套管预热器技术领域。The invention relates to a method for cleaning scabs on a casing preheater used for raw ore pulp preheating in alumina production, and belongs to the technical field of casing preheaters.

背景技术: Background technique:

在氧化铝生产中,采用高温、高压溶出时,溶出矿浆经多级闪蒸发后产生大量的二次蒸汽,该项二次汽不外排,而用于原矿浆的预热,以达到节能、降耗有效的保护环境及劳动生产的安全与卫生。现有技术中,用于间接预热的方法有以下两种:In alumina production, when high-temperature and high-pressure dissolution is used, a large amount of secondary steam is generated after the stripped pulp undergoes multi-stage flash evaporation. This secondary steam is not discharged outside, but is used for preheating the original pulp to achieve energy saving Reduce consumption and effectively protect the environment and the safety and health of labor production. In the prior art, there are two methods for indirect preheating:

间接加热压煮器预热:该设备虽是实现高压溶出间接加热的一种先进和十分有效的设备;但它具有自重大和带有传动搅拌装置,加热管束及润滑系统等,即系统较为复杂;由此而带来投资大,操作难度和维护检修、结疤清理工作量大,此外传热系数较低。Indirect heating autoclave preheating: Although this equipment is an advanced and very effective equipment for indirect heating of high-pressure dissolution; but it has its own weight and has a transmission stirring device, heating tube bundle and lubrication system, etc., that is, the system is relatively complicated. ; As a result, the investment is large, the operation is difficult, the maintenance and repair, and the workload of scab cleaning are large, and the heat transfer coefficient is low in addition.

套管预热:管道预热器的内、外管均采用无缝钢管,内管为溶液流道,外管为加热蒸汽流道,同压煮器相比,具有传热系数高,建设投资省、维护检修、清洗工作量小和结构紧凑等优点;但是随着管道预热级数的增加(即管道长度增大),随着运行时间的推进,高温端的结疤会不断增厚,即使采用现有技术中的处理方法进行处理,其高温段的结疤仍然无法处理干净,由此而带来传热系统数明显的降低,管道阻力损失增大,甚至造成管道堵塞,迫使生产无法连续稳定的运行。故在现有技术中,机械搅拌间接加热溶出系统的套管预热器管道最多只有五级。Casing preheating: The inner and outer pipes of the pipe preheater are made of seamless steel pipes, the inner pipe is the solution flow channel, and the outer pipe is the heating steam flow channel. Compared with the pressure cooker, it has a higher heat transfer coefficient and less construction investment. It has the advantages of low maintenance and overhaul, small cleaning workload and compact structure; however, as the number of pipeline preheating stages increases (that is, the length of the pipeline increases), as the running time advances, the scarring at the high-temperature end will continue to thicken, even if Using the treatment method in the prior art, the scabs in the high-temperature section still cannot be cleaned, resulting in a significant reduction in the number of heat transfer systems, an increase in pipeline resistance loss, and even pipeline blockage, forcing production to be uncontinuous stable operation. Therefore, in the prior art, there are at most five stages of casing preheater pipelines in the mechanically stirred indirect heating dissolution system.

发明内容: Invention content:

本发明的目的在于:提供一种较好清洗套管内结疤的套管预热器结疤的清洗方法,以克服现有技术的不足。The object of the present invention is to provide a method for cleaning the scabs of the casing preheater to better clean the scabs in the casing, so as to overcome the shortcomings of the prior art.

本发明是这样构成的:一种套管预热器结疤的清洗方法,它采用稀硫酸清洗套管预热器结疤,将用于清洗套管预热器结疤的稀硫酸,首先由最后一级套管注入、从第一级套管排出进行清洗,如此反复循环清洗,直到将最后一级套管内的结疤清洗干净,这样即可完成对套管预热器结疤的清洗;当第一级套管内还残留有结疤时,将用于清洗套管预热器结疤的稀硫酸,从第一级套管注入、从最后一级套管排出,如此反复循环清洗,直到将第一级套管内残留的结疤清洗干净,即可结束对套管预热器结疤的清洗;清洗套管预热器结疤的稀硫酸的PH值为:3~6。The present invention is constituted like this: a kind of cleaning method of casing preheater scab, it adopts dilute sulfuric acid to clean casing preheater scab, will be used to clean the dilute sulfuric acid of casing preheater scab, first by Inject the last-stage casing, discharge from the first-stage casing for cleaning, and repeat the cycle of cleaning until the scars in the last-stage casing are cleaned, so that the cleaning of the casing preheater scars can be completed; When there are scars remaining in the first-stage casing, the dilute sulfuric acid used to clean the casing preheater is injected from the first-stage casing and discharged from the last-stage casing, and the cleaning cycle is repeated until Clean the residual scabs in the first-stage casing to complete the cleaning of the casing preheater scabs; the pH value of dilute sulfuric acid for cleaning the casing preheater scabs: 3-6.

本发明具有以下优点:1、清洗效果更好,特别是对高温段的结疤处理效果更好;The present invention has the following advantages: 1. The cleaning effect is better, especially the scarring treatment effect on the high temperature section is better;

2、可增加现有高压溶出系统中的套管预热器数量,代替压煮器使用,以一级套管取代一级压煮器预热可节省建设投资约300万元;2. The number of casing preheaters in the existing high-pressure dissolution system can be increased to replace the pressure cooker, and the construction investment can be saved by about 3 million yuan by using the first-level casing instead of the first-level pressure cooker for preheating;

3、将五级套管预热器增至六级以上,每生产1吨氧化铝可节约新蒸汽0.12t左右,一个年产800kt的氧化铝厂每年可节约新蒸汽96kt,即每年可节约生产成本约700万元;3. Increase the five-stage casing preheater to more than six stages, and save about 0.12 tons of new steam for every ton of alumina produced. An alumina plant with an annual output of 800kt can save 96kt of new steam every year, that is, it can save production every year The cost is about 7 million yuan;

4、采用首末两端进酸清洗,减轻了稀硫酸对无缝钢管的腐蚀。4. The first and last ends are cleaned with acid, which reduces the corrosion of dilute sulfuric acid on seamless steel pipes.

附图说明: Description of drawings:

附图1为本发明的结构示意图。Accompanying drawing 1 is the structural representation of the present invention.

具体实施方式: Detailed ways:

本发明的实施例:本发明可在现有的技术上改进,当套管预热器的结疤需要处理时,采用PH值为3~6的稀硫酸进行清洗,将用于清洗套管预热器结疤的稀硫酸,首先由最后一级套管注入、从第一级套管排出进行清洗,清洗1小时,直到将最后一级套管内的结疤清洗干净;当上述清洗工作完成后,如果第一级套管内还残留有结疤,将用于清洗套管预热器结疤的稀硫酸,从第一级套管注入、从最后一级套管排出,如此反复循环清洗,直到将第一级套管内残留的结疤清洗干净,这样即可完成对套管预热器结疤的清洗。Embodiments of the present invention: the present invention can be improved on the existing technology. When the scarring of the casing preheater needs to be treated, it is cleaned with dilute sulfuric acid with a pH value of 3 to 6, which will be used for cleaning the casing preheater. The dilute sulfuric acid scabbed on the heater is firstly injected from the last-stage casing and discharged from the first-stage casing for cleaning for 1 hour until the scars in the last-stage casing are cleaned; when the above cleaning work is completed , if there are still scars in the first-stage casing, the dilute sulfuric acid used to clean the casing preheater is injected from the first-stage casing and discharged from the last-stage casing, and the cleaning cycle is repeated until Clean the remaining scabs in the first-stage casing, so that the cleaning of the casing preheater scabs can be completed.

Claims (3)

1. purging method that cannula primary heater scabs, it is characterized in that: it adopts dilute sulphuric acid cannula cleaning preheater to scab, to be used for the dilute sulphuric acid that the cannula cleaning preheater scabs, at first inject, discharge from first step sleeve pipe and clean by the last step sleeve pipe, wash cycles so repeatedly, up to scabbing in the last step sleeve pipe cleaned up, can finish the cleaning that cannula primary heater is scabbed like this.
2. the purging method that cannula primary heater according to claim 1 scabs, it is characterized in that: when in the first step sleeve pipe during also residual scabbing, to be used for the dilute sulphuric acid that the cannula cleaning preheater scabs, inject, discharge from first step sleeve pipe from the last step sleeve pipe, wash cycles so repeatedly, residual scabbing cleans up in first step sleeve pipe, can finish the cleaning that cannula primary heater is scabbed.
3. the purging method that cannula primary heater according to claim 1 and 2 scabs is characterized in that: the pH value of the dilute sulphuric acid that the cannula cleaning preheater scabs is: 3~6.
CNB2005102002089A 2005-04-05 2005-04-05 Scale eliminating method for casing pre-heater Expired - Fee Related CN100436647C (en)

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Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101608312B (en) * 2008-06-19 2011-04-20 中国铝业股份有限公司 Method for descaling evaporator set used in alumina production by pickling
CN102553864A (en) * 2010-12-29 2012-07-11 中国铝业股份有限公司 Method for cleaning scab of high pressure dissolution system through water dissolution method
CN102755974A (en) * 2011-04-27 2012-10-31 贵阳铝镁设计研究院有限公司 Chemical cleaning and heating device and heating method thereof
CN102350422A (en) * 2011-06-21 2012-02-15 中国铝业股份有限公司 Method for clearing scabs dissolved out of autoclave
CN104438243B (en) * 2014-11-12 2016-08-31 贵州大学 A kind of method for cleaning of single-sleeve preheating device inner tube scab
CN108160625A (en) * 2018-01-04 2018-06-15 山东潍焦集团薛城能源有限公司 A kind of method of cork dry quenching disposable dust remover water cold sleeve on-line cleaning
CN112574828A (en) * 2020-12-11 2021-03-30 河南丰达智能装备有限公司 Formula and preparation method of cleaning agent for material scale dissolved out of pipeline in alumina plant
CN114210663A (en) * 2021-11-19 2022-03-22 中铝中州铝业有限公司 Method for cleaning bauxite leaching sleeve

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU700774A1 (en) * 1978-02-20 1979-11-30 Предприятие П/Я А-1297 Method of removing carbonate crust from surface of heat exchange apparatus

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU700774A1 (en) * 1978-02-20 1979-11-30 Предприятие П/Я А-1297 Method of removing carbonate crust from surface of heat exchange apparatus

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
锅炉和热交换器安全酸洗技术. 周定中.造船技术,第06期. 1984 *

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