CN111575486B - Pta氧化母液回收利用方法 - Google Patents

Pta氧化母液回收利用方法 Download PDF

Info

Publication number
CN111575486B
CN111575486B CN202010428957.1A CN202010428957A CN111575486B CN 111575486 B CN111575486 B CN 111575486B CN 202010428957 A CN202010428957 A CN 202010428957A CN 111575486 B CN111575486 B CN 111575486B
Authority
CN
China
Prior art keywords
filtrate
mother liquor
distilled water
carrying
methanol
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202010428957.1A
Other languages
English (en)
Other versions
CN111575486A (zh
Inventor
杨文辉
唐多金
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN202010428957.1A priority Critical patent/CN111575486B/zh
Publication of CN111575486A publication Critical patent/CN111575486A/zh
Application granted granted Critical
Publication of CN111575486B publication Critical patent/CN111575486B/zh
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/006Wet processes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B7/00Halogens; Halogen acids
    • C01B7/09Bromine; Hydrogen bromide
    • C01B7/096Bromine
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74Separation; Purification; Use of additives, e.g. for stabilisation
    • C07C29/76Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
    • C07C29/80Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/48Separation; Purification; Stabilisation; Use of additives
    • C07C67/52Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
    • C07C67/54Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0453Treatment or purification of solutions, e.g. obtained by leaching
    • C22B23/0461Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B47/00Obtaining manganese
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Metallurgy (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

本发明公开一种PTA氧化母液回收利用方法,是将除铁、回收钴及锰的后的碱性废液蒸发得饱和液;向饱和液中加入酸得到弱酸液;将弱酸液离心过滤,得滤出物A及滤液A;将滤液A反复经过过滤及蒸发,得到滤出物B及滤液B;将滤出物A与滤出物B混合得滤出混合物并干燥,得干料;向干料中加入甲醇得甲醇溶解物后精密过滤,得混合盐A和滤液C;将混合盐A与滤液B混合后提取溴素并产生提溴废液,将提溴废液经过蒸发结晶过滤分别得到蒸馏水、混合盐B及酸性母液;将滤液C反应精馏得到蒸馏水、甲醇及有机酯,将有机脂反复经过精馏分离、提纯蒸馏及结晶塔分离,得到苯甲酸甲酯及对苯二甲酸二甲酯或间苯二甲酸二甲酯或邻苯二甲酸二甲酯。

Description

PTA氧化母液回收利用方法
技术领域
本发明涉及一种废液回收方法,尤其是一种可充分回收资源及避免对污水处理系统造成危害的PTA氧化母液回收利用方法。
背景技术
现有聚合级PTA(精对苯二甲酸)生产方法是以对二甲苯(PX)为原料、醋酸为溶剂,在钴锰溴催化剂和一定温度、压力下,利用空气连续氧化制得对苯二甲酸浆料(PTA氧化母液),然后经结晶、分离、干燥得粗对苯二甲酸(TA),再经加氢反应,结晶、分离、干燥,得到精对苯二甲酸。为防止对二甲苯氧化阶段的副产物在系统中的积聚而影响PTA的产量和质量,生产过程中需抽出一部分PTA氧化母液。PTA氧化母液中含有钴、锰、溴、大量有机副产物和因设备腐蚀等产生的少量铁,具有较高的利用价值。
目前,对于PTA氧化母液的回收利用方法有多种,其中之一是向PTA氧化母液中加碱沉淀除铁,然后再加碱沉淀过滤回收钴离子、锰离子,之后形成碱性废水进入污水处理系统,按照污水进行处理后排放。PTA氧化母液中所含的溴离子及有机物等并没有回收,不仅造成资源浪费,而且会对污水处理系统造成危害(设备腐蚀及活性污泥中毒等)。
发明内容
本发明是为了解决现有技术所存在的上述技术问题,提供一种可充分回收资源及避免对污水处理系统造成危害的PTA氧化母液回收利用方法。
本发明的技术解决方案是:一种PTA氧化母液回收利用方法,依次按照如下步骤进行:
a. 取PTA氧化母液,向PTA氧化母液中加入碱,沉淀过滤除铁及回收钴及锰后得碱性废液;
b. 将碱性废液经过MVR蒸发得饱和液及蒸馏水;
c. 向饱和液中加入酸调节,得到弱酸液;
d. 将弱酸液离心过滤,得滤出物A及滤液A;将滤液A反复经过陶瓷膜过滤及MVR蒸发,得到滤出物B、滤液B及蒸馏水;将滤出物A与滤出物B混合得滤出混合物;
e. 将滤出混合物干燥,得干料及蒸馏水;
f. 向干料中加入甲醇,得甲醇溶解物;
g. 将甲醇溶解物精密过滤,得混合盐A和滤液C;将混合盐A与滤液B混合后经过氯化蒸馏得到溴素及提溴废液,将提溴废液经过蒸发结晶过滤分别得到蒸馏水、混合盐B及酸性母液;
h. 将滤液C反应精馏得到蒸馏水、甲醇及有机酯,将有机脂经过精馏分离、提纯蒸馏及结晶塔分离,得到苯甲酸甲酯、固体废物及对苯二甲酸二甲酯或间苯二甲酸二甲酯或邻苯二甲酸二甲酯。
本发明不仅可以将PTA氧化母液的钴及锰提取出来,而且还可以提取溴,并得到蒸馏水、混合盐、酸性母液、甲醇、苯甲酸甲酯及对苯甲酸二甲酯或间苯二甲酸二甲酯或邻苯二甲酸二甲酯等副产品,可避免资源浪费及对污水处理系统造成危害。
附图说明
图1是本发明实施例的工艺流程图。
具体实施方式
本发明的PTA氧化母液回收利用方法如图1所示,依次按照如下步骤进行:
a. 按照现有技术的方法取PTA氧化母液,并向PTA氧化母液中加入碱,沉淀过滤除铁及过滤回收钴及锰后得碱性废液;经检测,所得碱性废液中溴离子含量在2500ppm左右,PH在8~9左右;
b. 将碱性废液经过MVR蒸发得饱和液及蒸馏水;
c. 将饱和液冷却至常温并向饱和液中加入硫酸调节pH值,得到弱酸液;
d. 将弱酸液离心过滤,得滤出物A及滤液A;将滤液A反复经过陶瓷膜过滤及MVR蒸发,得到滤出物B、滤液B(近饱和液盐)及蒸馏水;将滤出物A与滤出物B混合得滤出混合物;
e. 将滤出混合物喷雾干燥,尾气冷凝,得干料及蒸馏水;
f. 向干料中加入甲醇,得甲醇溶解物;
g. 将甲醇溶解物精密过滤,得混合盐A和滤液C;将混合盐A与滤液B混合后经过通入氯气的氯化蒸馏得到溴素及提溴废液,将提溴废液经过蒸发结晶过滤分别得到蒸馏水、混合盐B及酸性母液;
h. 将滤液C加热到140℃以上喷入精馏塔反应精馏,得到蒸馏水、甲醇(可用于g步骤)及有机酯,将有机脂反复经过精馏分离、提纯蒸馏及结晶塔分离,得到含量99.9%的苯甲酸甲酯、固体废物及含量99.9%的对苯二甲酸二甲酯或间苯二甲酸二甲酯或邻苯二甲酸二甲酯,具体得到何种副产物以PTA原料对二甲苯杂质,比如对二甲苯杂质是间二甲苯或邻二甲苯等为准。

Claims (1)

1.一种PTA氧化母液回收利用方法,依次按照如下步骤进行:
a. 取PTA氧化母液,向PTA氧化母液中加入碱,沉淀过滤除铁及回收钴及锰后得碱性废液;
b. 将碱性废液经过MVR蒸发得饱和液及蒸馏水;
c. 向饱和液中加入酸调节,得到弱酸液;
d. 将弱酸液离心过滤,得滤出物A及滤液A;将滤液A反复经过陶瓷膜过滤及MVR蒸发,得到滤出物B、滤液B及蒸馏水;将滤出物A与滤出物B混合得滤出混合物;
e. 将滤出混合物干燥,得干料及蒸馏水;
f. 向干料中加入甲醇,得甲醇溶解物;
g. 将甲醇溶解物精密过滤,得混合盐A和滤液C;将混合盐A与滤液B混合后经过氯化蒸馏得到溴素及提溴废液,将提溴废液经过蒸发结晶过滤分别得到蒸馏水、混合盐B及酸性母液;
h. 将滤液C反应精馏得到蒸馏水、甲醇及有机酯,将有机酯反复经过精馏分离、提纯蒸馏及结晶塔分离,得到苯甲酸甲酯、固体废物及对苯二甲酸二甲酯或间苯二甲酸二甲酯或邻苯二甲酸二甲酯。
CN202010428957.1A 2020-05-20 2020-05-20 Pta氧化母液回收利用方法 Active CN111575486B (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010428957.1A CN111575486B (zh) 2020-05-20 2020-05-20 Pta氧化母液回收利用方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010428957.1A CN111575486B (zh) 2020-05-20 2020-05-20 Pta氧化母液回收利用方法

Publications (2)

Publication Number Publication Date
CN111575486A CN111575486A (zh) 2020-08-25
CN111575486B true CN111575486B (zh) 2023-03-21

Family

ID=72109489

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010428957.1A Active CN111575486B (zh) 2020-05-20 2020-05-20 Pta氧化母液回收利用方法

Country Status (1)

Country Link
CN (1) CN111575486B (zh)

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6811763B2 (en) * 2002-10-07 2004-11-02 The Procter & Gamble Company Conversion of sodium bromide to anhydrous hydrobromic acid and sodium bisulfate
CN101693525B (zh) * 2009-10-14 2011-04-13 祁洪波 水蒸汽蒸馏制溴法
CN102923663A (zh) * 2012-11-06 2013-02-13 绍兴汉青环保科技有限公司 一种从pta废水中回收溴的方法
CN104058514A (zh) * 2013-08-28 2014-09-24 无锡市兴盛环保设备有限公司 一种pta废水分段分离回收钴锰方法
CN103613073A (zh) * 2013-11-07 2014-03-05 浙江双益环保科技发展有限公司 一种从含溴废水中提取溴素的方法
CN104229738B (zh) * 2014-10-08 2016-06-15 潍坊北海绿洲太阳能科技股份有限公司 一种真空蒸馏法从海水中提取溴的方法
CN109371416B (zh) * 2018-12-12 2020-12-04 浙江大学 一种由含溴废水回收溴素的方法
CN109776307A (zh) * 2019-03-27 2019-05-21 佰仕邦水处理环保科技(大连)有限公司 一种针对精对苯二甲酸氧化单元的母液抽出液的处理工艺

Also Published As

Publication number Publication date
CN111575486A (zh) 2020-08-25

Similar Documents

Publication Publication Date Title
CN107176739B (zh) 一种异丁酸盐废水的资源化处理方法
CN114906964B (zh) 一种pta废水处理系统及应用方法
CN111138347A (zh) 一种乙烯基吡啶类化合物分水工业化方法和装置
CN101941901B (zh) 一种pta精制废水母固回收方法
CN111575486B (zh) Pta氧化母液回收利用方法
CN113121333A (zh) 用于回收芳香族单羧酸的方法
KR101943115B1 (ko) 필터 공급 슬러리중 물의 백분율을 제어함으로써 테레프탈산 퍼지 여과 속도를 개선하는 방법
CN102137707B (zh) 用于从对苯二甲酸生产中回收有价值的物质的方法和设备
KR101946657B1 (ko) 필터 공급 슬러리중 물의 백분율을 제어함으로써 테레프탈산 퍼지 여과 속도를 개선하는 방법
EA022449B1 (ru) Способ и система для выделения карбоновых кислот из суспензии
KR101943116B1 (ko) 필터 공급 슬러리중 물의 백분율을 제어함으로써 테레프탈산 퍼지 여과 속도를 개선하는 방법
CN101845038B (zh) 丙交酯精制残液处理方法及装置
CN214299725U (zh) 一种pta精制母液的净化装置
WO2009064037A1 (en) Recovery of catalysts, benzoic acid and aromatic acid
CN112520931A (zh) 一种pta精制母液的净化方法及装置
CN112694409A (zh) 一种回收废水中三乙胺的方法和装置
CN111196788A (zh) 一种2-巯基苯并噻唑精制提纯方法
CN104744238A (zh) 在苯氧乙酸类农药废水中回收羟基乙酸的方法
CN111454449B (zh) 一种合成ppta用溶剂体系回收循环利用的方法
KR101013489B1 (ko) 방향족산 제조공장의 폐기물로부터 촉매와 방향족산의 회수방법
CN114684947A (zh) 一种pta废水中有机物回收利用方法
JP4657674B2 (ja) テレフタル酸の製造方法
KR100431688B1 (ko) 트리멜리트산 및 촉매의 회수방법 및 장치
CN113105630A (zh) 一种聚苯硫醚生产工艺流程中的溶剂回收工艺
KR100650536B1 (ko) 테레프탈산의 제조 방법

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant