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1. 发明申请

US20160175735A1 PROCESS SYSTEM FOR SEPARATING CHEMICALS, DISTILLATION COLUMN ARRANGEMENT, AND METHOD OF SEPARATING CHEMICALS 审中-公开
标题翻译：分离化学品的处理系统，蒸馏塔装置和分离化学品的方法
公开(公告)号：US20160175735A1
公开(公告)日：2016-06-23
申请号：US14973266
申请日：2015-12-17
申请人： Chempolis Oy
发明人： Juha Tanskanen , Werner Marcelo Goldmann Valdes
IPC分类号： B01D3/40 , B01D3/14 , B01D3/36 , B01D3/00
CPC分类号： B01D3/40 , B01D3/009 , B01D3/143 , B01D3/36 , C07C51/46 , C07C67/327 , Y02P20/127 , C07C53/02 , C07C53/08
摘要： An arrangement for separating chemicals comprises a first distillation column (100) and the first distillation column (100) receives a mixture that comprises water and at least two organic acids and extractant that comprises at least one of the following: hexanol, an ester of hexanol with said at least one organic acid and 2-methylpentanol. The first distillation column (100) forms a heterogeneous azeotrope of water and extractant at its top (104) on the basis of reactive heteroazeotropic extractive distillation not controlling chemical reactions between the extractant and said at least two organic acids, said first distillation column (100) removing the azeotrope through its top (104) for separating water from the organic acid.
摘要翻译：用于分离化学品的装置包括第一蒸馏塔（100）和第一蒸馏塔（100）接收包含水和至少两种有机酸的混合物，以及包含以下至少一种的萃取剂：己醇，己醇酯与所述至少一种有机酸和2-甲基戊醇。所述第一蒸馏塔（100）在其顶部（104）的基础上形成水和萃取剂的非均相共沸物，基于不控制萃取剂与所述至少两种有机酸之间的化学反应的反应性杂化萃取蒸馏，所述第一蒸馏塔（100 ）通过其顶部（104）除去共沸物以从有机酸分离水。

2. 发明申请

US20020069983A1 Process for producing cellulose, and by-product 失效
标题翻译：生产纤维素和副产物的方法
公开(公告)号：US20020069983A1
公开(公告)日：2002-06-13
申请号：US09969616
申请日：2001-10-03
申请人： Chempolis Oy
发明人： Pasi P. Rousu , Paivi P. Rousu , Esa J. Rousu
IPC分类号： D21C011/00 , D21C011/12 , D21C003/02
CPC分类号： D21C11/0028 , C05D1/00 , D21C9/1063 , D21C11/0007
摘要： The invention relates to a process for producing cellulose and a fertilizer by-product by using a closed cycle of cooking chemicals and process waters. In the process of the invention, the pulp is bleached by at least partly using potassium hydroxide as a bleaching chemical. Thus, a bleach concentrate rich in potassium is obtained from the bleach filtrate, which bleach concentrate is combined with ashes obtained from the burning of lignin and other organic matter recovered from pulp production as a by-product, in order to be used as a potash fertilizer. The bleach concentrate can also be used as a potash fertilizer as such. The invention also relates to a potash fertilizer obtained this way.
摘要翻译：本发明涉及通过使用烹饪化学品和处理水的封闭循环来生产纤维素和副产物的方法。在本发明的方法中，纸浆通过至少部分地使用氢氧化钾作为漂白化学品漂白。因此，从漂白滤液中获得富含钾的漂白浓缩物，漂白浓缩物与作为副产物从纸浆生产回收的木质素和其它有机物质的燃烧中获得的灰分相结合，以便用作钾盐肥料。漂白浓缩物也可以作为钾肥使用。本发明还涉及以这种方式获得的钾肥。

3. 发明授权

US10441897B2 Process system for separating chemicals, distillation column arrangement, and method of separating chemicals 有权
公开(公告)号：US10441897B2
公开(公告)日：2019-10-15
申请号：US14973266
申请日：2015-12-17
申请人： Chempolis Oy
发明人： Juha Tanskanen , Werner Marcelo Goldmann Valdes
IPC分类号： B01D3/40 , B01D3/00 , B01D3/36 , C07C51/46 , B01D3/14 , C07C67/327
摘要： An arrangement for separating chemicals comprises a first distillation column (100) and the first distillation column (100) receives a mixture that comprises water and at least two organic acids and extractant that comprises at least one of the following: hexanol, an ester of hexanol with said at least one organic acid and 2-methylpentanol. The first distillation column (100) forms a heterogeneous azeotrope of water and extractant at its top (104) on the basis of reactive heteroazeotropic extractive distillation not controlling chemical reactions between the extractant and said at least two organic acids, said first distillation column (100) removing the azeotrope through its top (104) for separating water from the organic acid.

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