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METHOD FOR SEPARATING TRIOXANE FROM A TRIOXANE/ FORMALDEHYDE/ WATER MIXTURE BY MEANS OF PRESSURE CHANGE RECTIFICATION

机译:压力变化整流法从三恶烷/甲醛/水混合物中分离三恶烷的方法

摘要

A PROCESS FOR SEPARATING TRIOXANE FROM A FEED STREAM I (8) COMPRISING FORMALDEHYDE, TRIOXANE AND WATER, IN WHICH A) A FEED STREAM I (8) COMPRISING FORMALDEHYDE AS MAIN COMPONENT AND TRIOXANE AND WATER AS SECONDARY COMPONENTS IS PROVIDED, B) THE FEED STREAM I (8), A RECYCLE STREAM V (12) AND A RECYCLE STREAM VII (15) COMPRISING FORMALDEHYDE AS MAIN COMPONENT AND WATER AND TRIOXANE AS SECONDARY COMPONENTS ARE FED INTO A FIRST DISTILLATION STAGE AND DISTILLED AT A PRESSURE OF FROM 0.01 TO 0.25 MPA (0.1 TO 2.5 BAR) TO GIVE A STREAM II (6) COMPRISING FORMALDEHYDE AS MAIN COMPONENT AND WATER AS SECONDARY COMPONENT AND A STREAM III (9) COMPRISING TRIOXANE AS MAIN COMPONENT AND WATER AND FORMALDEHYDE AS SECONDARY COMPONENTS AND A STREAM X COMPRISING WATER, TRIOXANE AND FORMALDEHYDE, C) THE STREAM III (9) IS, IF APPROPRIATE AFTER REMOVAL OF LOW BOILERS FROM THE STREAM III (9) IN A LOW BOILER REMOVAL STAGE, DISTILLED IN A SECOND DISTILLATION STAGE AT A PRESSURE OF FROM 0.02 TO 1.75 MPA (0.2 TO 17.5 BAR), WITH THE PRESSURE IN THE SECOND DISTILLATION STAGE BEING FROM 0.01 TO 1.5 MPA (0.1 TO 15 BAR) HIGHER THAN THE PRESSURE IN THE FIRST DISTILLATION STAGE, TO GIVE A STREAM IV (11) CONSISTING ESSENTIALLY OF TRIOXANE AND THE RECYCLE STREAM V (12) COMPRISING TRIOXANE AS MAIN COMPONENT AND WATER AND FORMALDEHYDE AS SECONDARY COMPONENTS, C1) THE STREAM IV (11) IS PURIFIED IN AT LEAST ONE FURTHER TRIOXANE DISTILLATION STAGE AT A PRESSURE AT THE TOP OF FROM 0.05 TO 0.2 MPA (0.5 TO 2 BAR) TO GIVE PURIFIED TRIOXANE AS SIDE OFFTAKE STREAM XII IN THE ENRICHMENT SECTION OF THE COLUMN (10), D) THE STREAM X AND, IF APPROPRIATE, A STREAM IX (3) COMPRISING WATER AS MAIN COMPONENT ARE FED INTO A THIRD DISTILLATION STAGE AND DISTILLED AT A PRESSURE OF FROM 0.1 TO 1 MPA (1 TO 10 BAR) TO GIVE A STREAM VI (14) CONSISTING ESSENTIALLY OF WATER AND A RECYCLE STREAM VII (15) COMPRISING FORMALDEHYDE AS MAIN COMPONENT AND WATER AND TRIOXANE AS SECONDARY COMPONENTS, IS DESCRIBED. (FIGURE 1)
机译:从进料流I(8)包含甲醛,三恶烷和水中分离三恶烷的方法,其中A)进料流I(8)含甲醛作为主要成分,三恶烷和水为次级组分,B)第I阶段(8),第V阶段的循环(12)和第VII阶段的循环(15),其中以甲醛为主要成分,以水和三恶烷为主要成分,被送入第一个蒸馏阶段,并在0.01至0.25的压力下蒸馏MPA(0.1至2.5 BAR)给出流态II(6),其中甲醛为主要成分,水为第二成分,并且流态III(9),其中三恶烷为主要成分,水和甲醛为第二成分,并且X成分为水,三恶烷和甲醛,C)如果在低沸物去除阶段以适当的方式从流III(9)中去除低沸物之后,在第二蒸馏阶段以0.02至1.75的压力蒸馏除去了流III(9) MPA(0.2比1 7.5巴),第二蒸馏阶段的压力比第一蒸馏阶段的压力高0.01至1.5 MPA(0.1至15巴),从而获得IV(11)级,基本上由三恶烷和循环流组成V(12)以三恶烷为主要成分,水和甲醛为次要成分,C1)流IV(11)在至少一个更高的三恶烷蒸馏阶段进行净化,压力最高为0.05 MPA至0.2 MPA(0.5至在蒸馏塔X12的富集部分中,将纯化的三恶烷作为进水口XII排出(10),D)进料X和合适的话,将进水IX(3)作为主要成分加入到第三蒸馏塔中在0.1到1 MPA(1到10巴)的压力下进行蒸馏和蒸馏,以提供流VI(14)基本由水和循环流VII(15)组成的流态,其中甲醛为主要成分,水和三恶烷为第二成分,已描述。 (图1)

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