{"title":"修改现有预热系统以提高生产率和效率(水泥工业)","authors":"T. Lang","doi":"10.1109/CITCON.1990.111063","DOIUrl":null,"url":null,"abstract":"Three cases of preheater/precalciner modifications covering a production capacity ranging from 1500 to 4500 mt/d for plants in France, Canada and the USA are described. The first example deals with the addition of an RSP type furnace to an existing PREPOL-AT precalciner for capacity enhancement and improvement of circulating elements behavior within the kiln. The second covers the replacement of an ACL grate preheater by a one-stage PREPOL-AS calciner enabling low alkali clinker production from high alkali, high sulfur, high kerogen raw materials in an environmentally sound manner. The third example shows the replacement of two underdimensioned Fuller-SF-calciners of a two-string preheater kiln by one large FLS type SLC-S precalciner in connection with the installation of a 10-50% capacity range bypass system. All three kiln conversions have been basically successful and able to meet the expectations almost entirely. However, since they came onstream a comparatively short while ago, some optimization and fine tuning work still has to be completed.<<ETX>>","PeriodicalId":339195,"journal":{"name":"IEEE Technical Conference on cement Industry","volume":"129 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"1990-05-22","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Modifying existing preheater systems for improved productivity and efficiency (cement industry)\",\"authors\":\"T. Lang\",\"doi\":\"10.1109/CITCON.1990.111063\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"Three cases of preheater/precalciner modifications covering a production capacity ranging from 1500 to 4500 mt/d for plants in France, Canada and the USA are described. The first example deals with the addition of an RSP type furnace to an existing PREPOL-AT precalciner for capacity enhancement and improvement of circulating elements behavior within the kiln. The second covers the replacement of an ACL grate preheater by a one-stage PREPOL-AS calciner enabling low alkali clinker production from high alkali, high sulfur, high kerogen raw materials in an environmentally sound manner. The third example shows the replacement of two underdimensioned Fuller-SF-calciners of a two-string preheater kiln by one large FLS type SLC-S precalciner in connection with the installation of a 10-50% capacity range bypass system. All three kiln conversions have been basically successful and able to meet the expectations almost entirely. However, since they came onstream a comparatively short while ago, some optimization and fine tuning work still has to be completed.<<ETX>>\",\"PeriodicalId\":339195,\"journal\":{\"name\":\"IEEE Technical Conference on cement Industry\",\"volume\":\"129 1\",\"pages\":\"0\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1990-05-22\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"IEEE Technical Conference on cement Industry\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.1109/CITCON.1990.111063\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"IEEE Technical Conference on cement Industry","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1109/CITCON.1990.111063","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Modifying existing preheater systems for improved productivity and efficiency (cement industry)
Three cases of preheater/precalciner modifications covering a production capacity ranging from 1500 to 4500 mt/d for plants in France, Canada and the USA are described. The first example deals with the addition of an RSP type furnace to an existing PREPOL-AT precalciner for capacity enhancement and improvement of circulating elements behavior within the kiln. The second covers the replacement of an ACL grate preheater by a one-stage PREPOL-AS calciner enabling low alkali clinker production from high alkali, high sulfur, high kerogen raw materials in an environmentally sound manner. The third example shows the replacement of two underdimensioned Fuller-SF-calciners of a two-string preheater kiln by one large FLS type SLC-S precalciner in connection with the installation of a 10-50% capacity range bypass system. All three kiln conversions have been basically successful and able to meet the expectations almost entirely. However, since they came onstream a comparatively short while ago, some optimization and fine tuning work still has to be completed.<>