制鹽工藝流程(1)

1、鹽田飽和鹵水直接進(jìn)蒸發(fā)罐真空制鹽工藝介紹靳志玲（中鹽制鹽工程技術(shù)研究院，天津300450）內(nèi)容摘要：利用灘田飽和鹵水直接進(jìn)蒸發(fā)罐蒸發(fā)結(jié)晶制取氯化鈉，在制鹽過(guò)程中采取三次洗滌方法，除去鈣鎂離子，以獲得純度超過(guò)99.1%的氯化鈉和濃度較高的制鹽母液。關(guān)鍵詞：灘田飽和鹵水真空精制鹽1簡(jiǎn)介目前，國(guó)內(nèi)大部分井礦鹽企業(yè)采用以井礦鹽鹵為原料，北方部分生產(chǎn)企業(yè)采用原鹽化成飽和鹽水再精制真空鹽的生產(chǎn)方法。隨著國(guó)內(nèi)兩堿”的迅速發(fā)展和人民生活水平的提高，原鹽供需矛盾已越來(lái)越突出。特別是在海鹽區(qū)，以原鹽溶解成飽和鹵水再生產(chǎn)精制鹽，不僅增加了原鹽的消耗，而且降低了鹽田面積的使用效率，增加投資，生產(chǎn)成本高，不同程度上影響

2、了食用鹽生產(chǎn)企業(yè)的經(jīng)濟(jì)效益，造成許多食用鹽定點(diǎn)生產(chǎn)企業(yè)減產(chǎn)、虧損，直接影響了百姓的生活。而采用灘田飽和鹵水直接進(jìn)蒸發(fā)罐制鹽，即可以節(jié)約結(jié)晶面積，其母液還可以為生產(chǎn)氯化鉀、氯化鎂等鹽化工產(chǎn)品提供高質(zhì)量原料苦鹵，達(dá)到充分利用鹵水中的各種有效成分，實(shí)現(xiàn)零排放、無(wú)污染、循環(huán)經(jīng)濟(jì)的目的。2 .工藝流程簡(jiǎn)述鹵水經(jīng)灘田日曬蒸發(fā)，至飽和后引入一個(gè)鹵水庫(kù)中儲(chǔ)存。鹵水庫(kù)的作用，一是儲(chǔ)存一定量的飽和鹵水，以備真空制鹽生產(chǎn)的需要；二是鹵水在此有一定的停留時(shí)間，可以使其中的一些雜質(zhì)顆粒沉淀下來(lái)，達(dá)到凈化鹵水的目的。凈化后的飽和鹵水從鹵水庫(kù)引出后，進(jìn)入蒸發(fā)制鹽車(chē)間的精鹵桶。采用預(yù)熱后的鹵水進(jìn)罐，順流轉(zhuǎn)料、末效排鹽漿，集中

3、排母液的方式進(jìn)行生產(chǎn)。I效蒸發(fā)罐鹽箱中的鹽排到II效下循環(huán)管中，II效鹽箱中的鹽排到III效下循環(huán)管中，III效鹽箱中的鹽排到IV效下循環(huán)管中，最后集中在IV效鹽箱；IV效排出鹽漿，同時(shí)由IV效分離罐排出母液。工藝流程簡(jiǎn)圖見(jiàn)圖1。生烝汽原料鹵水效二次蒸汽U效二次蒸汽A鹽漿閃皿效二次蒸汽不凝汽去真空泵IV效二次蒸汽冷卻水海合冷凝器回鍋爐冷凝水I效閃發(fā)桶O冷凝水冷凝I效蒸發(fā)罐'閃IV平橫桶皿效閃發(fā)桶II效平衡桶冷凝水冷凝水冷凝水預(yù)生活用水熱器發(fā)汽i'.鹽漿閃II效蒸發(fā)罐III效蒸發(fā)罐一效閃發(fā)桶皿效平衡桶冷卻水母液原料鹵水原料鹵水鹽漿3 .工藝的優(yōu)缺點(diǎn)運(yùn)用該工藝已在中國(guó)北方建設(shè)了一個(gè)

4、年產(chǎn)15萬(wàn)噸的真空制鹽生產(chǎn)線，相比再制鹽生產(chǎn)工藝，其實(shí)施效果如下：本工藝采用飽和鹵水制鹽，不需要淡水化原鹽，淡水消耗低，可節(jié)約淡水資源，根據(jù)生產(chǎn)情況，1t鹽消耗淡水1.4-0.2m3,而再制鹽生產(chǎn)工藝需要淡水3.5-4.53.73m3,噸鹽節(jié)約了2.1-4.3m3淡水。2）節(jié)約日曬鹽場(chǎng)土地，減少原鹽消耗，提高了鹽田利用率對(duì)再制鹽生產(chǎn)線來(lái)說(shuō)，一般生產(chǎn)1t精制鹽需要消耗1.2t日曬原鹽，年產(chǎn)15萬(wàn)t的精制鹽需要18萬(wàn)t原鹽，需要結(jié)晶面積136.36公頃（按目前中國(guó)北方鹽場(chǎng)有效結(jié)晶單產(chǎn)1650t公頃，有效面積占80%）,采用飽和鹵水直接進(jìn)蒸發(fā)罐工藝，不需要飽和鹵水進(jìn)結(jié)晶池繼續(xù)蒸發(fā)制鹽，只需要建設(shè)一個(gè)

5、約2公頃的飽和鹵庫(kù)，因此，節(jié)約了土地面積134.36公頃，節(jié)省的結(jié)晶面積可用于增加日曬鹽產(chǎn)量8547t，按日曬鹽銷(xiāo)售價(jià)160元/t計(jì)算，日曬鹽增加產(chǎn)值136.8萬(wàn)元。如果土地按3萬(wàn)元/W計(jì)算,節(jié)約土地價(jià)值為6000多萬(wàn)元。3）采用三次洗滌方法洗滌鹽漿以去除鈣鎂離子，使氯化鈉含量超過(guò)99.4%,精制鹽達(dá)到優(yōu)級(jí)鹽質(zhì)量。蒸發(fā)結(jié)晶過(guò)程中鹽漿會(huì)夾帶大量的母液，母液中含有大量的鈣、鎂雜質(zhì)，因此，采用三次不同的洗滌方式洗滌鹽漿，提高精制鹽質(zhì)量。4）用飽和鹵水直接生產(chǎn)精制鹽母液損失小，提高了母液的利用率，實(shí)現(xiàn)鹽化聯(lián)采用鹽田飽和鹵水直接生產(chǎn)優(yōu)級(jí)真空精制鹽工藝，每產(chǎn)1t精制鹽副產(chǎn)母液約1.7m3,以年產(chǎn)15萬(wàn)t精

6、制鹽計(jì)算，全年可產(chǎn)生25.5萬(wàn)m3蒸發(fā)母液，且排出的苦鹵氯化鉀含量達(dá)到了2430§/1,濃度為2934°Be',鈉鎂比值為1.40.6,排出的苦鹵中氯化鉀總含量為6589t,氯化鎂總量為36540t,硫酸鎂總量為18900t,氯化鈉總量為37600t,澳總量510t。而年產(chǎn)18萬(wàn)t原鹽，排出的苦鹵量一般只有18萬(wàn)m3,經(jīng)過(guò)復(fù)曬、滲透損失、溝道輸送進(jìn)入化工廠后只有原來(lái)的45%左右，也就是說(shuō)還有8.1萬(wàn)m3,這時(shí)氯化鉀總含量為2036t,氯化鎂總量為15280t,硫酸鎂總量為7727.4t,氯化鈉總量為11128t,澳總量162t。因此，該工藝可為鹽化工生產(chǎn)提供更多的原

7、料，提高了生產(chǎn)效率，降低了各種消耗，節(jié)約能源。該工藝排出的制鹽蒸發(fā)母液溫度在55.04C以上，可通過(guò)管道直接進(jìn)入下步生產(chǎn)氯化鉀的工序，生產(chǎn)氯化鉀產(chǎn)品，節(jié)約氯化鉀生產(chǎn)過(guò)程中所需熱量，折標(biāo)煤1157噸/年5）由于灘田飽和鹵水較化鹽鹵水氯化鈉含量低，因此單位產(chǎn)品的蒸發(fā)水量較高，噸鹽產(chǎn)品電、蒸汽消耗量較大，能耗較高。6）蒸發(fā)設(shè)備換熱面積較化鹽溶解工藝稍高，因此設(shè)備投資相對(duì)較高，但由于節(jié)省大量鹽田結(jié)晶面積，總體投資低。4 .與原鹽溶解再制鹽工藝技術(shù)經(jīng)濟(jì)指標(biāo)比較國(guó)內(nèi)海鹽區(qū)生產(chǎn)真空鹽的工藝主要有灘田飽和鹵水進(jìn)罐蒸發(fā)制鹽和原鹽溶解制成飽和鹵水蒸發(fā)制鹽兩種方法。原鹽溶解制成飽和鹵水蒸發(fā)制鹽工藝優(yōu)缺點(diǎn)有：（1）需

8、建結(jié)晶池，工程總體投資較高；（2）單位產(chǎn)品蒸發(fā)水量小，設(shè)備投資稍低，（3）噸鹽消耗電、蒸汽量較??；（4）水消耗較大，噸鹽產(chǎn)品耗水2.4m3,（5）蒸發(fā)母液損失大。比較兩種制鹽方法技術(shù)經(jīng)濟(jì)指標(biāo)如表。表主要經(jīng)濟(jì)技術(shù)指標(biāo)比較項(xiàng)目再制鹽生產(chǎn)飽和鹵水直接進(jìn)罐生產(chǎn)投資：結(jié)晶池投資550萬(wàn)元0蒸發(fā)設(shè)備投資9701080單位產(chǎn)品投資335元/噸306元/噸消耗指標(biāo)：原煤0.23噸0.21噸原鹽1.25噸一1.15噸0.00噸鹵水0.007.5m3白水3.5-4.5m331.4-0.2m3電50-70度50-70度兩種工藝在投資和單位產(chǎn)品生產(chǎn)成本中有較大的差別，飽和鹵水法單位產(chǎn)品總投資低于原鹽溶解法，單位產(chǎn)品成

9、本低于原鹽溶解法30%。5 .結(jié)論對(duì)于北方海鹽區(qū)生產(chǎn)精制鹽企業(yè)來(lái)說(shuō)，利用灘田飽和鹵水直接進(jìn)蒸發(fā)罐制取精制鹽是一個(gè)較好的生產(chǎn)工藝，節(jié)約投資，節(jié)約土地，特別是將寶貴的原鹽溶解成飽和鹵水再進(jìn)行制鹽是對(duì)土地資源的浪費(fèi)，再有其生產(chǎn)成本低，企業(yè)有較高的利潤(rùn)空間；排出的制鹽母液綜合利用生產(chǎn)鉀、澳、鎂等產(chǎn)品，使鹵水全部吃干榨凈，沒(méi)有廢物排放，減少了環(huán)境污染，有利于可持續(xù)發(fā)展。NewtechnologyofproducingrefinedsaltbyaddingsaltfieldsaturatedbrineintoevaporatordirectlyJinzhilingGeJinyang(SaltResearc

10、hInstituteChinaNaturalSaltIndustryCorporation,TianJin300450)Abstract:AfterMakingsalinesaturatedbrineflowinevaporatingpot,thesodiumchlorideisobtainedbyevaporativecrystallization.Calciumandmagnesiumionscanberemovedbywashingsaltthreetimesinordertogetthesodiumchloridethatthepurityisover99.1percentandthe

11、motherliquorthathavehighconcentration.Keywords:salinesaturatedbrine,vacuum,refinesaltmagnesiumchlorideetc.inorderto1. BRIEFINTRODUCTIONmakeuseofallkindsofeffectiveAtpresent,thematerialsofmakingvacuumsaltareusingthewellandrocksaltinmostofthewellandrocksaltcorporationsandthesaturatedbrinegotbydissolvi

12、ngcrudesalt.Alongwiththerapiddevelopmentofcausticalkaliandsodiumcarbonateandthegrowthinthepeople'slivingstandard,thecontradictionofcrudesaltinsupplyandrequireismoreandmorestoodout.Particularlyintheseasaltareas,productingrefinesaltwithsaturatedbrinethatisgotbydissolvingcrudesaltcanincreasethecons

13、umptionofrawsalt,reducetheavailabilityfactorofsaltfield,addinvestmentandproductioncost.Thiswillinfluencetheeconomicefficiencyofediblesaltmanufacturingenterprises,makethemreduceoutputandaffectpeopleslive.However,usingthemethodofmakingsalinesaturatedbrineflowinevaporatingpotandthenobtainingsodiumchlor

14、idebyevaporativecrystallizationcansavingcrystalarea.Furthermore,themotherliquorcanbeusedasmaterialtoproducechemicallyproductssuchaspotassiumchloride,constituentsinthebrineandachievetheobjectsofnodischarge,nopollutionandcirculatingeconomy.2. INDICATIONOFTHEPROCESSFLOWAfterbeingsolarizedtosaturationin

15、beachfieldbrinewasinductedtobrinetankandstored.Ontheonehandbrinetankcanstoresomesaturatedbrinethatisusedtoproducevacuumsalt.Ontheotherhand,brinehavesomeresidencetimeheresosomeimpuritiescanbedepositedinordertomakethebrinebepurified.Afterbeingdrawoutedfrombrinetankthecleanedsaturatedbrinewaspumpedtofi

16、nebrinetankinthemanufacturesaltplant.Andproductioncanbegoneonbyusingthemethodsofpreheatingbrine,transferringstuffinparallelflow,dischargingsaltslurryinthelasteffectandexportingmotherliquorconcentratedly.Thesaltinthefirsteffecttankisdischargedtothecirculationpipeofthesecondeffect,Thesaltinthesecondef

17、fecttankisdischargedtothecirculationpipeofthethirdeffect,Thesaltinthethirdeffecttankisdischargedtothecirculationpipeofthefourtheffect.Atlastthesaltiscollectedinthefourtheffecttankwherethesaltslurryandthemotherliquoraredischarged.Fig.1isthediagramoftheprocessflow.生烝汽原料鹵水閃發(fā)汽回鍋爐冷凝水冷凝水i效二次蒸汽效二次蒸汽皿效二次蒸汽I

18、效蒸發(fā)罐閃發(fā)汽不凝汽去真空泵W效二次蒸汽n效蒸發(fā)罐冷凝水I效平衡桶I效閃發(fā)桶II效平衡桶冷凝水冷凝水原料鹵水川效蒸發(fā)罐閃發(fā)汽水凝.冷，In效平衡桶n效閃發(fā)桶漿閃發(fā)汽鹽In效閃發(fā)桶W平橫桶混合冷凝器冷卻水冷卻水原料鹵水生活用水冷凝水冷凝水+鹽漿Figure.1Diagramoftheprocessflow3. RELATIVEMERITSOFTHEPROCESSInthenorthofChinaaproductionlinehasbeenbuiltwiththisprocess,whichcanproduce1.5milliontonssaltperyear.Comparingwithrewor

19、ksaltproductionprocess,theeffectofthisprocessisasfollows:1) Thesaturatedbrineisusedinthisprocesstaketheplaceofdissolvingcrudesaltwithfreshwater.Suchcanreducetheconsumptionoffreshwaterandsavetheresource.Accordingtotheproduceconditions,producing1tonsaltwillconsume1.4-0.2m3freshwater.Andthatifusetherew

20、orkingsaltprocess3.5-4.53m3freshwaterwillbeused.Thatistosay2.1-4.3m3freshwatercanbesavedcorrespondingto1tonsalt.2) Savingthesolarsaltfield,reducetheconsumptionofcrudesalt,increasetheavailabilityofthesaltfield.Forthereworkingsaltproductionline,asageneralruleproducing1tonrefinesaltwillconsume1.2tonsso

21、larsalt.Producing1.5milliontonrefinesaltneeds1.8milliontonscrudesaltand136.36hectarecrystalarea(Accordingtotheexperiencethatonehectarecanproduce1650toncrystalandtheeffectiveareais80percent).Usingtheprocessthatthesaturatedbrineispumpedtoevaporatingtankdirectlythebrineneednotevaporateincrystalpondbutf

22、orasaturatedbrinestoreroomofabout2hectare.Suchcansavesurfaceareaof134.36hectareandthisareacanbeusedtoincrease8547tonoutputofsolarsalt.Hencetheproductivevalueofsolarsaltwillincrease136.8tenthousandyuanaccordingtothemarketpriceofsolarsaltwhichis160yuan/t.Andlandvalueof60millionyuancanbesavedifthelandi

23、s30,000yuanpermou.3) Adoptingthemethodofwashingsaltthreetimesinordertogetridofcalciumandmagnesiumions,makethepurityofsodiumchlorideexceed99.4%andmaketherefinesaltreachfirstquality.Intheprocessofevaporativecrystallizationmuchmotherliquorwillexistinsaltslurry.Themotherliquorcontainsalotofimpurityofcal

24、ciumandmagnesium.Sosaltslurryiswashedinthreedifferentwaysinordertoimprovethequalityofrefinesalt.4) Usingthesaturatedbrinetoproducerefinesaltcanreducetheconsumeofmotherliquors,enhanceit'asailabilityandrealizetheproductionofsaltandchemicalstogether.Theprocessthatproducingexcellentvacuumsaltwithsal

25、inasaturatedbrinedirectlycanget1.7m3motherliquorinrelationto1trefinesalt.Onthebaseof150,000tonrefinesalt,wecanget255,000m3evaporationmotherliquor.Inbitterbrinewhoseconcentrationis29340Be'thecontentofpotassiumchlorideis2430g/landtheratioofsodiumandmagnesiumis140.6.And6589tpotassiumchloride,36540t

26、magnesiumchloride,18900tmagnesiumsulfate,37600tsodiumchlorideand510tbrominearecontainedinthebitterbrine.Thebitterbrineisabout180,000m3inrelationto180,000tcrudesalt.Afterbeingsolarizedrepeatedlyandconsumingforfilterthebrineisleft45%whenitispumpedtochemicalplant.Thatistosaythereare81,000m3brine.Bynowt

27、hereare2036tpotassiumchloride,15280tmagnesiumchloride,7727.4tmagnesiumsulfate,11128tsodiumchlorideand162tbromine.Sotheprocesscanprovidemorematerialforsaltandchemicalsplants,heightenproductionefficiency,reduceallkindsofconsumptionandsaveenergy.Thetemperatureofthemotherliquorgotfromthisprocessisover55

28、.04C.Soitcanbepumpedtothepotassiumchlorideprocesswithpipetoproducepotassiumchloride.Suchwillsavetheheatquantityintheprocessofproducingpotassiumchloride.Andtheheatquantityisequalto11578t/ystandardcoal.5) Becausethecontentofsodiumchlorideinthebeachsaturatedbrineislowerthanthecontentinthebrinethatisgot

29、bydissolvingsalt,theevaporatedwaterofunitproduceishigher,theelectricityandsteamconsumptionaremore.Thatistosaytheenergyconsumptionishigher.6) Theheatexchangeareaisalittlerbiggerthantheprocessofdissolvingsalt,sotheequipmentinvestmentishigher.Butbecauseofsavingalotofsalinacrystalareathetotalinvestmenti

30、slower.4.COMPARETHEECONOMICINDICATORSWITHTHEPROCESSOFDISSOLVINGCRUDESALTANDTHENREMAKINGSALTInChinaTherearetwomainmethodstoproducingvacuumsaltinseasaltarea.Oneispumpingthebeachsaturatedbrineintoevaporatingpot.Theotherisusingthesaturatedbrinegotbydissolvingcrudesalt.Comparingthesecondmethodwiththefirs

31、tmethodtherelativemeritsofthesecondmethodisasfollows:(1)needtobuildcrystalpondandthetotalinvestmentishigher.(2)Theevaporatedwaterofunitproductissmallerandtheequipmentinvestmentislower.(3)Theconsumingofelectricityandsteamislower.(4)Theconsumingofwaterismoreand2.4m3waterwillbeconsumedinrelationto1tonsalt.(5)Thelossofmotherliquorisbigger.Theeconomicindicatorsofthetwomethodsareasfollows:ComparisonofthemaineconomicandtechnicalnormsItemTheprocessbydissolvingsaltThepro