3-氯萘-2,6-二磺酸 | 89222-87-7

• 分子结构分类: 有机化合物 - 苯类化合物 - 萘
• 中文名称: 3-氯萘-2,6-二磺酸
• 英文名称: 3-chloro-naphthalene-2,6-disulfonic acid
• 英文别名: 3-Chlor-naphthalin-2,6-disulfonsaeure；3-Chloronaphthalene-2,6-disulfonic acid
• CAS: 89222-87-7
• 化学式: C₁₀H₇ClO₆S₂
• 分子量: 322.747
• InChiKey: DKXOUVHRDJCGRG-UHFFFAOYSA-N

物化性质

• 密度：
  1.782±0.06 g/cm3(Predicted)

计算性质

• 辛醇/水分配系数(LogP)：
  1.3
• 重原子数：
  19
• 可旋转键数：
  2
• 环数：
  2.0
• sp3杂化的碳原子比例：
  0.0
• 拓扑面积：
  126
• 氢给体数：
  2
• 氢受体数：
  6

反应信息

• 作为产物：
  描述：

  3-Aminonaphthalene-2,6-disulfonic acid 生成 3-氯萘-2,6-二磺酸
  参考文献：
  名称：

  Armstrong; Wynne, Chemical news and journal of industrial science, 1890, vol. 62, p. 163

  摘要：

  DOI：

文献信息

• [EN] PROCESS FOR MAKING BUTENYL ESTERS FROM BUTADIENE<br/>[FR] PROCEDE DE FABRICATION D'ESTERS A PARTIR DE BUTADIENE
  申请人：BP CHEM INT LTD

  公开号：WO2003082796A1

  公开（公告）日：2003-10-09

  A process for making a butenyl ester from butadiene by reacting butadiene or a hydrocarbon fraction containing butadiene with a saturated aliphatic monocarboxylic acid, wherein the catalyst is rhenium (VII) oxide or an organic sulphonic acid containing at least (2) sulphonic acid groups per molecule wherein the ratio of the number of carbon atoms to the number of sulphonic acid groups in the organic sulphonic acid is in the range 1 : 1 to 1 : 0.15. Preferred catalysts are organic disulphonic acids for example ethane-1,2-disulphonic acid. The process can be used for making unsaturated esters, or, by hydrogenation of the product, for making saturated esters such as for example butyl acetate. Catalyst can be purified and recycled to the reactor.

  一种从丁二烯中制备丁烯酸酯的方法，包括将丁二烯或含有丁二烯的碳氢化合物与饱和脂肪族一元羧酸反应，其中催化剂为铼（VII）氧化物或含有每个分子至少（2）磺酸基团的有机磺酸，有机磺酸中碳原子数与磺酸基团数的比值在1：1至1：0.15范围内。优选的催化剂是有机二磺酸，例如乙烷-1,2-二磺酸。该方法可用于制备不饱和酯，或通过产物的加氢，用于制备饱和酯，例如醋酸丁酯。催化剂可以被净化并回收到反应器中。
• Process for making esters from butadiene
  申请人：Cook John Darren

  公开号：US20050065365A1

  公开（公告）日：2005-03-24

  A process for making a butyl ester from butadiene by reacting butadiene or a hydrocarbon fraction containing butadiene with a saturated aliphatic monocarboxylic acid, wherein the catalyst is rhenium(VII) oxide or an organic sulphonic acid containing at least 2 sulphonic acid groups per molecule wherein the ratio of the number of carbon atoms to the number of sulphonic acid groups in the organic sulphonic acid is in the range 1:1 to 1:0.15. Preferred catalysts are organic disulphonic acids for example ethane-1,2-disulphonic acid. The process can be used for making unsaturated esters, or, by hydrogenation of the product, for making saturated esters such as for example butyl acetate. Catalyst can be purified and recycled to the reactor.

  一种通过丁二烯或含有丁二烯的烃馏分与饱和脂肪族一元羧酸反应从丁二烯制取丁酯的工艺，其中催化剂为氧化铼（VII）或每分子至少含有 2 个磺酸基团的有机磺酸，其中有机磺酸中碳原子数与磺酸基团数之比范围为 1:1 至 1:0.15。首选催化剂是有机二磺酸，例如乙烷-1,2-二磺酸。该工艺可用于制造不饱和酯，或通过氢化产品制造饱和酯，例如乙酸丁酯。催化剂可以净化并循环到反应器中。
• PROCESS FOR MAKING BUTENYL ESTERS FROM BUTADIENE
  申请人：THE UNIVERSITY OF SOUTHERN MISSISSIPPI

  公开号：EP1490321A1

  公开（公告）日：2004-12-29
• INTEGRATED PROCESS TO PRODUCE DERIVATIVES OF BUTADIENE ADDITION PRODUCTS
  申请人：University of Southern Mississippi Research Foundation

  公开号：EP1641737A2

  公开（公告）日：2006-04-05
• Integrated process to produce derivatives of butadiene addition products
  申请人：Gracey Patrick Benjamin

  公开号：US20070060769A1

  公开（公告）日：2007-03-15

  An integrated chemical process to form derivatives of butadiene addition products comprises forming an addition product of butadiene and a selected carboxylic acid, alcohol, or glycol, to form a reaction mixture containing at least a crotyl addition product and a sec-butenyl addition product; separating the reaction product mixture into streams comprising a crotyl product stream, a sec-butenyl product stream, and at least one stream containing other reacted and unreacted products; controlling the proportion of the product streams, preferably by recycling a portion or all of a separated crotyl product stream and/or a sec-butenyl product stream and other product streams to the addition reactor; subjecting one or more separated product streams to one or more process selected from hydrolysis, hydrogenation, and isomerization to form product derivatives in preselected proportions; and recovering one or more resulting product derivatives.