SU146734A1 - Method for separating ethylene chlorohydrin from its azeotrope with water - Google Patents

Method for separating ethylene chlorohydrin from its azeotrope with water

Info

Publication number
SU146734A1
SU146734A1 SU696146A SU696146A SU146734A1 SU 146734 A1 SU146734 A1 SU 146734A1 SU 696146 A SU696146 A SU 696146A SU 696146 A SU696146 A SU 696146A SU 146734 A1 SU146734 A1 SU 146734A1
Authority
SU
USSR - Soviet Union
Prior art keywords
water
ethylene chlorohydrin
azeotrope
separating ethylene
nitromethane
Prior art date
Application number
SU696146A
Other languages
Russian (ru)
Inventor
В.Б. Коган
Б.В. Мамонтов
А.И. Морозова
М.С. Немцов
С.К. Огородников
Р.А. Шляхтер
хтер Р.А. Шл
Original Assignee
В.Б. Коган
Б.В. Мамонтов
А.И. Морозова
М.С. Немцов
С.К. Огородников
хтер Р.А. Шл
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 В.Б. Коган, Б.В. Мамонтов, А.И. Морозова, М.С. Немцов, С.К. Огородников, хтер Р.А. Шл filed Critical В.Б. Коган
Priority to SU696146A priority Critical patent/SU146734A1/en
Application granted granted Critical
Publication of SU146734A1 publication Critical patent/SU146734A1/en

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Известен способ выделени  этиленхлоргидрина из его водного азеотропа обезвоживанием последнего азеотропной перегонкой с органическим экстрагентом, например с дихлорэтаном. Однако с дихлорэтаном тер етс  и некоторое количество этиленхлоргидрина. Дл  предотвращени  потерь основного продукта приходитс  усложн ть технологическую схему обезвоживани  введением дополнительной дистилл ционной колонны.There is a method for isolating ethylene chlorohydrin from its aqueous azeotrope by dehydrating the latter by azeotropic distillation with an organic extractant, for example dichloroethane. However, some ethylene chlorohydrin is lost with dichloroethane. To prevent the loss of the main product, it is difficult to dehydrate the flow chart by introducing an additional distillation column.

Предлагаемый способ выделени  этиленхлоргидрина из его азеотропа с водой лишен указанного недостатка и тем самым упрощает процесс. Он заключаетс  в обезвоживании азеотропа этиленхлоргидрин - вода азеотропной перегонкой с органическим экстрагентом, не образующим тройной нераздельнокип щей смеси с водой и этиленхлоргидрином . В кнчестве таких экстрагентов могут быть использованы, например , нитрометан, диизопропиловый эфир.The proposed method for isolating ethylene chlorohydrin from its azeotrope with water is devoid of this disadvantage and thus simplifies the process. It consists in dehydrating the azeotrope of ethylene chlorohydrin — water by azeotropic distillation with an organic extractant that does not form a triple non-separable mixture with water and ethylene chlorohydrin. In particular, such extractants can be used, for example, nitromethane, diisopropyl ether.

Пример 1. В куб ректификационной колонны периодического действи  загружают .1000 кг водного раствора этиленхлоргидрина, содержащего 57,5% вес. последнего, и 400 кг нитрометана- После доведени  колонны до равновеси  начинают отбор верхнего вод ного сло , получающегос  при расслаивании гетероазеотропа нитрометан-вода, имеющего температуру кипени  83,6° и содержащего 54,8% мол. воды. После отбора около 470 кг указанного верхнего сло , состо щего приблизительно из 90% вес. воды и 10% вес. нитрометана, отбирают фракцию, представл ющую собой практически чистый нитрометан. Затем отбирают небольшую промежуточную фракцию смеси нитрометана и этиленхлоргидрина . В кубе колонны остаетс  практически чистый этиленхлоргидрин .Example 1. A 1,000 kg of an ethylene chlorohydrin aqueous solution containing 57.5% by weight is loaded into a cube of a batch distillation column. the latter, and 400 kg of nitromethane. After the column is brought to equilibrium, the removal of the upper water layer, which is obtained by stratifying the nitromethane-water heteroazeotrope, having a boiling point of 83.6 ° and containing 54.8 mol%, begins. water. After collection, about 470 kg of said upper layer consisting of approximately 90% by weight is taken water and 10% weight. nitromethane, a fraction is taken which is practically pure nitromethane. Then a small intermediate fraction of a mixture of nitromethane and ethylene chlorohydrin is collected. Almost pure ethylene chlorohydrin remains in the bottom of the column.

SU696146A 1961-02-04 1961-02-04 Method for separating ethylene chlorohydrin from its azeotrope with water SU146734A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU696146A SU146734A1 (en) 1961-02-04 1961-02-04 Method for separating ethylene chlorohydrin from its azeotrope with water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU696146A SU146734A1 (en) 1961-02-04 1961-02-04 Method for separating ethylene chlorohydrin from its azeotrope with water

Publications (1)

Publication Number Publication Date
SU146734A1 true SU146734A1 (en) 1961-11-30

Family

ID=48302165

Family Applications (1)

Application Number Title Priority Date Filing Date
SU696146A SU146734A1 (en) 1961-02-04 1961-02-04 Method for separating ethylene chlorohydrin from its azeotrope with water

Country Status (1)

Country Link
SU (1) SU146734A1 (en)

Similar Documents

Publication Publication Date Title
NO152371C (en) PROCEDURE FOR THE PREPARATION OF ANCIENT OR APPROXIMATED Aqueous ACID
SU146734A1 (en) Method for separating ethylene chlorohydrin from its azeotrope with water
US2865955A (en) Method for separating water-soluble alcohols and esters
ES8101064A1 (en) Process for the purification of olefin oxides.
US4705902A (en) DDTR-free 1,1-bis(chlorophenyl)-2,2,2-trichloroethanol
GB722390A (en) Separating methyl acetate from other organic compounds by extractive distillation
SU518121A3 (en) Method for separating a mixture of 3,3-dimethyl-acrolein and 3-methyl-3-butenol-1 or 3,3-dimethylacrolein, 3-methyl-3-butenol-1 and 3-methyl-2 butenol-1
SU107275A1 (en) The method of separation of mixtures of hydrocarbons and monohydric alcohols
SU119525A1 (en) Method for separating 2-niropropane from mixtures thereof with primary nitroparaffins
GB851342A (en) Improvements in the purification of acrylic esters
GB803552A (en) Dehydration process
ES263287A1 (en) Procedure for separating uranium impurities (Machine-translation by Google Translate, not legally binding)
GB1094523A (en) Process for the purification of dimethyl sulphoxide
US3133957A (en) Purification of acrylonitrile
GB1199120A (en) Process for Separating Methanol from a Mixture Thereof With Methyl Acetate
SU387968A1 (en) Method of dehydrating acetic acid
SU545662A1 (en) The method of separation of a mixture of hydrocarbons and oxygen-containing products
GB870012A (en) Improvements in the purification of crude dimethyl terephthalate by distillation
GB762974A (en) Dehydrating alcohols by extractive distillation
SU31939A1 (en) Methyl ethyl ketone dehydration method
US2885408A (en) Production of anhydroenneaheptitol
SU121443A1 (en) The method of obtaining formals
SU413136A1 (en)
SU119655A1 (en) Method for preparing nicotinic acid esters
SU105130A1 (en) The method of selection of higher fatty alcohols