CN103965098A - 一种吡啶及3-甲基吡啶制备过程的节能技术 - Google Patents

一种吡啶及3-甲基吡啶制备过程的节能技术 Download PDF

Info

Publication number
CN103965098A
CN103965098A CN201410217754.2A CN201410217754A CN103965098A CN 103965098 A CN103965098 A CN 103965098A CN 201410217754 A CN201410217754 A CN 201410217754A CN 103965098 A CN103965098 A CN 103965098A
Authority
CN
China
Prior art keywords
tank
communicated
saving technology
water
pyridine
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.)
Pending
Application number
CN201410217754.2A
Other languages
English (en)
Inventor
徐学峰
赵立立
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.)
Gunther Bio Tech Ltd Shandong
Original Assignee
Gunther Bio Tech Ltd Shandong
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 Gunther Bio Tech Ltd Shandong filed Critical Gunther Bio Tech Ltd Shandong
Priority to CN201410217754.2A priority Critical patent/CN103965098A/zh
Publication of CN103965098A publication Critical patent/CN103965098A/zh
Pending legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D213/00—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
    • C07D213/02—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
    • C07D213/04—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
    • C07D213/06—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom
    • C07D213/16—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom containing only one pyridine ring
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • F22B1/1838—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines the hot gas being under a high pressure, e.g. in chemical installations
    • F22B1/1846—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines the hot gas being under a high pressure, e.g. in chemical installations the hot gas being loaded with particles, e.g. waste heat boilers after a coal gasification plant
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Pyridine Compounds (AREA)

Abstract

一种吡啶及3-甲基吡啶制备过程的节能技术，其特征在于：包括再生器，所述再生器与外旋风联通，所述外旋风下部联通催化剂罐，上部与废热炉联通，所述废热炉与软水罐联通，所述软水罐上部设有软化水进口和出口，软水罐出口与闪蒸罐联通，所述闪蒸罐设有疏水进口和蒸汽出口。本发明有益效果：本方法在再生器内的排气口增加一个废热炉和一个软水罐，将热空气和软水换热，将会产生0.5Mpa的蒸汽，从而这些蒸汽可以给物料的伴热、储罐的盘管加热等使用，对热能回收利用，从而减低了热能消耗，大大降低产品成本。

Description

一种吡啶及3-甲基吡啶制备过程的节能技术
技术领域
本发明属于精细化工生产技术领域，尤其涉及一种吡啶及3-甲基吡啶制备过程的节能技术。
背景技术
吡啶类化合物是指吡啶及其衍生物，主要包括吡啶、3-甲基吡、2-甲基吡啶等，是生产精细化工产品的重要的有机原料，主要用途有：主要广泛应用在农药、医药、染料、日用化工、香料、饲料添加剂、橡胶助剂等领域，目前国内生产吡啶及其衍生物时采用生产工艺和生产方法，只注重生产产品转化率而忽略了生产工艺的节能技术，生产过程中能耗过高，尾气中含有大量有机物质未能经过有效处理排放到空气中严重污染了环境；在实际生产中，如何充分利用生产过程中的吡啶合成中产生大量尾气、并其进行效处理，达到节能、降耗、环保，成为生产企业急需解决的问题。
发明内容
本发明的目的是针对现有技术存在的问题，提供一种吡啶及3-甲基吡啶制备过程的节能技术。
本发明采用的技术方案是：一种吡啶及3-甲基吡啶制备过程的节能技术，其特征在于：包括再生器，所述再生器与外旋风联通，所述外旋风下部联通催化剂罐，上部与废热炉联通，所述废热炉与软水罐联通，所述软水罐上部设有软化水进口和出口，软水罐出口与闪蒸罐联通，所述闪蒸罐设有疏水进口和蒸汽出口。
本发明有益效果：本方法在再生器内的排气口增加一个废热炉和一个软水罐，将热空气和软水换热，将会产生0.5Mpa的蒸汽，从而这些蒸汽可以给物料的伴热、储罐的盘管加热等使用，对热能回收利用，从而减低了热能消耗，大大降低产品成本。
附图说明
下面结合附图和具体实施方式对本发明做进一步说明。
附图为本发明工作原理示意框图。
具体实施方式
如图所示的一种吡啶及3-甲基吡啶制备过程的节能技术，其特征在于：由再生器产生600℃的空气，空气量为8000Kg/h经管道进入外旋风将空气中夹杂的催化剂粉末分离后进入催化剂罐，其余空气由外旋风上部排出进入废热炉，废热炉与软水罐联通给软水换热，进入废热炉的空气经换热后进行排空，软化水经软水罐换热后产生0.5Mpa的蒸汽，进入闪蒸罐，与来自各设备疏水在闪蒸罐内进行闪蒸，闪蒸出0.5Mpa，温度为150℃的蒸汽，一部分作为伴热用，另一部分给其他车间供汽。

Claims (1)

1.一种吡啶及3-甲基吡啶制备过程的节能技术，其特征在于：包括再生器，所述再生器与外旋风联通，所述外旋风下部联通催化剂罐，上部与废热炉联通，所述废热炉与软水罐联通，所述软水罐上部设有软化水进口和出口，软水罐出口与闪蒸罐联通，所述闪蒸罐设有疏水进口和蒸汽出口。
CN201410217754.2A 2014-05-22 2014-05-22 一种吡啶及3-甲基吡啶制备过程的节能技术 Pending CN103965098A (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410217754.2A CN103965098A (zh) 2014-05-22 2014-05-22 一种吡啶及3-甲基吡啶制备过程的节能技术

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410217754.2A CN103965098A (zh) 2014-05-22 2014-05-22 一种吡啶及3-甲基吡啶制备过程的节能技术

Publications (1)

Publication Number Publication Date
CN103965098A true CN103965098A (zh) 2014-08-06

Family

ID=51235158

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410217754.2A Pending CN103965098A (zh) 2014-05-22 2014-05-22 一种吡啶及3-甲基吡啶制备过程的节能技术

Country Status (1)

Country Link
CN (1) CN103965098A (zh)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54164052A (en) * 1978-06-16 1979-12-27 Teijin Ltd Full heat exchanging membrane and full heat exchanger
CN1252388A (zh) * 1998-08-19 2000-05-10 三浦工业株式会社 除去锅炉积垢的方法
CN1330068A (zh) * 2000-06-26 2002-01-09 广荣化学工业株式会社 制备吡啶碱类的方法
US20050113515A1 (en) * 2003-11-26 2005-05-26 Sutton Robert A. Method of making copolymers containing olefinic type monomers
CN101560151A (zh) * 2009-05-22 2009-10-21 南京大学 一种以离子液体为催化剂的反应精馏生产醋酸甲酯的工艺
CN102219730A (zh) * 2010-04-15 2011-10-19 中国石油化工股份有限公司 吡啶碱的制备方法
CN102219731A (zh) * 2010-04-15 2011-10-19 中国石油化工股份有限公司 吡啶碱的生产方法
CN102464521A (zh) * 2010-11-04 2012-05-23 中国科学院大连化学物理研究所 一种微反应器系统内合成环状碳酸酯的方法
CN202953967U (zh) * 2012-12-18 2013-05-29 山东昆达生物科技有限公司 一种一乙胺精制塔节能技术

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54164052A (en) * 1978-06-16 1979-12-27 Teijin Ltd Full heat exchanging membrane and full heat exchanger
CN1252388A (zh) * 1998-08-19 2000-05-10 三浦工业株式会社 除去锅炉积垢的方法
CN1330068A (zh) * 2000-06-26 2002-01-09 广荣化学工业株式会社 制备吡啶碱类的方法
US20050113515A1 (en) * 2003-11-26 2005-05-26 Sutton Robert A. Method of making copolymers containing olefinic type monomers
CN101560151A (zh) * 2009-05-22 2009-10-21 南京大学 一种以离子液体为催化剂的反应精馏生产醋酸甲酯的工艺
CN102219730A (zh) * 2010-04-15 2011-10-19 中国石油化工股份有限公司 吡啶碱的制备方法
CN102219731A (zh) * 2010-04-15 2011-10-19 中国石油化工股份有限公司 吡啶碱的生产方法
CN102464521A (zh) * 2010-11-04 2012-05-23 中国科学院大连化学物理研究所 一种微反应器系统内合成环状碳酸酯的方法
CN202953967U (zh) * 2012-12-18 2013-05-29 山东昆达生物科技有限公司 一种一乙胺精制塔节能技术

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
余穗颖: "生产烟酰胺新工艺技术", 《化工设计》, vol. 10, no. 05, 31 October 2000 (2000-10-31), pages 12 - 13 *
王光国: "制备芳腈的一种新方法", 《辽宁化工》, no. 04, 31 August 1979 (1979-08-31), pages 69 - 74 *

Similar Documents

Publication Publication Date Title
CN204690006U (zh) 发酵车间余热利用装置
CN201713470U (zh) 一种炭黑制备工艺的余热回收装置
CN204079838U (zh) 一种酯交换反应装置
CN103965098A (zh) 一种吡啶及3-甲基吡啶制备过程的节能技术
CN203469506U (zh) 真空闪蒸罐蒸汽冷凝水余热回收装置
CN203862214U (zh) 一种防止出料结晶的高压反应釜
CN104086413A (zh) 一种工业化醋酸乙酯生产装置
CN202346788U (zh) 设有高温乏气回收装置的氧化铁料浆生产系统
CN201873631U (zh) 乙醇氧化制备乙醛工艺中原料乙醇预热装置
CN202277812U (zh) 一种过氧化二异丙苯母液洗涤装置
CN205709913U (zh) 废旧覆铜板反应回收系统
CN204058315U (zh) 用于硝化棉煮洗锅的废气回收装置
CN204193909U (zh) 一种用于生产邻苯基苯酚的催化剂再生设备
CN204369777U (zh) 一种甲醇回收处理系统
CN204337804U (zh) 高沸点有机物脱水设备
CN203834052U (zh) 用于结晶的节能环保酸洗装置
CN205288131U (zh) 一种乳化机
CN205079454U (zh) 一种生产设备热源回收利用系统
CN202876785U (zh) 环保加热型反应槽
CN203090931U (zh) 一种节能型反应釜
CN205170709U (zh) 一种用于提高1,4-丁二醇收率的装置
CN203408702U (zh) 成品酸过滤器
CN204185416U (zh) 一种用于生产聚酯二醇的分馏装置
CN203373293U (zh) 蒸汽分级循环利用系统
CN204644241U (zh) 废汽、废水循环再利用系统

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20140806