Continuous noncatalytic esterification of lower formates by Ih-Cheo Yang A THESIS Submitted to the Graduate Faculty in partial fulfillment of the requirements for the degree of Master of Science in Chemical Engineering Montana State University © Copyright by Ih-Cheo Yang (1951) Abstract: It was found that the rate of esterification of lower alcohols (n-propyl, n-butyl, iso-butyl, n-amyl, iso-amyl alcohol) with formic acid is increased by the raising of temperature. The use of increased temperature obtained by rectifying at 60 psig pressure was investigated as a means of carrying out the continuous non-eatalytic esterification of n-propyl, n-butyl, iso-butyl, n-amyl, and iso-amyl alcohol with formic acid. The non-catalytic esterification rates at the atmospheric pressure and at 60 psig pressure were determined for n-propyl, n-butyl, iso-butyl, n-amyl and iso-amyl alcohol with formic acid. The ternary azeotropic composition at 60 psig pressure was determined for each formate system and a continuous non-catalytic esterification carried out for each ester.  COHTiMJOUS HONCATALYTIG ESTERIFICATION OF LOWER FORMATES by H-CHEO YANG A THESIS S u bm itte d t o t h e G rad u a te F a c u l ty I n p a r t i a l f u l f i l lm e n t o f th e r e q u i r em e n ts \ f o r th e d e g re e o f M a s te r o f S c ie n c e i n C hem ica l E n g in e e r in g a t . M ontana S t a t e C o lle g e A pproved : H ead , M ajo r D.ep&ptmspit C hairm an , E xam in ing C d ^ n i t te eB zPe U ehn , '"'Graduate D iv i s io n ( Bozeman', M btitana August,11951 - 2 -y o cT * TABLE OF CONTENTS Bags A b s t r a c t 3 I . I n t r o d u c t i o n .................................. ......................................................... .... . 4 I I . P r o c e s s e s .................... .... ................................................................................. 6 A. D e te rm in a t io n o f th e e s t e r i f i c a t i o n r a t e a t a tm o sp h e r ic p r e s s u r e . . . . . . . . . . . . 6 ( I ) Equipm ent (2) M a te r ia l s (3 ) P ro ­ c e d u re . B. P r e p a r a t i o n o f 60 p s ig p r e s s u r e t e r n a r y and a n a ly s i s o f i t s c o m p o s i t i o n .................... .... 6 ( I ) Equ ipm ent (2 ) P ro c e d u re . C. E s t im a t io n o f th e e s t e r i f i c a t i o n r a t e u n d e r 60 p s ig p r e s s u r e ..............................................................9 I I I . R e s u l t s .................. . . . . . . . . . . ......................... . . . 1 1 IV . Summary o f R e s u l t s . ............................................................... .... . . . 11 V. D is c u s s io n ................................................................................ 12 V I . L i t e r a t u r e C i t e d ................................... . 1 2 V I I . A ppend ix ................................ 13 103009 ABSTRACT I t was found t h a t th e r a t e o f e s t e r i f i c a t i o n o f low e r a lc o h o l s ( n - p r o p y l , n - b u t y l , i s o - b u t y l , n -am y l, i s o -am y l a lc o h o l ) w i t h fo rm ic a c id i s in c r e a s e d b y th e r a i d i n g o f tem p e ra tu re * - ■ ' . ' - T h e .u se o f in c r e a s e d tem p e ra tu re o b ta in e d b y r e c t i f y i n g a t 60 p s ig p r e s s u r e was i n v e s t i g a t e d a s a means o f c a r r y in g o u t th e c o n tin u o u s n o n - c a t a l y t i c e s t e r i f i c a t i o n o f n -p ro p y l: , n - b u t y l , i s o - b u t y l , n -am y l, and is o -am y l a lc o h o l w i th fo rm ic a c id . The n o n - c a t a l y t i c e s t e r i f i c a t i o n r a t e s a t t h e ; a tm o sp h e r ic p r e s s u r e and a t 60 p s i g p r e s s u r e w ere d e te rm in e d f o r n - p r o p y l , n - b u t y l , i s o - b u t y l n -am y l and is o -am y l a lc o h o l w i th fo rm ic a c id . The t e r n a r y a z e o t r o p ic c om p o s i t io n a t 60 p s ig p r e s s u r e was d e te rm in e d f o r e a c h fo rm a te sy s tem and a c o n tin u o u s n o n - c a t a l y t i c e s t e r i f i c a t i o n c a r r i e d o u t f o r e a ch e s t e r L , INTRODUCTION ' The m ost im p o r ta n t f a c t o r s c a u s in g an in c r e a s e d r a t e o f e s t o r i f i - ( ' c a t i o n a r e c a t a l y s t and r i s e i n t e m p e ra tu r e e C a t a l y s t s , su ch a s h y d r o c h lo r ic and s u l f u r i c a c id s a r e u sed in comm erc ia l p r e p a r a t i o n s o f e s t e r s b e c a u s e o f t h e i r r e l a t i v e low c o s t . The raw m a t e r i a l s a r e o rg a n ic a c i d , low e r a l c o h o l i n e x c e s s , and a l i t t l e s u l f u r i c a c i d . They a r e m ix ed , c o n d u c ted th ro u g h h e a t e x c h an g e rs and p a s s e d th ro u g h an e s t e r i f i c a t i o n column a t a tm o sp h e r ic p r e s s u r e . The o v e rh ead from t h i s column i s t h e t e r n a r y a z e o tro p e and c o n s i s t s o f a lc o h o l e s t e r and w a te r . The r a t e o f c h em ic a l r e a c t i o n i n c r e a s e s r a p i d l y w i th in c r e a s e d t e m p e r a tu r e . The e m p i r i c a l A r rh e n iu s E q u a t io n : a l a k 5 A dT RTzr i s t h e r e l a t i o n b e tw een th e s p e c i f i c r e a c t i o n v e l o c i t y c o n s ta n t K and t e m p e r a tu r e . T i s th e a b s o lu te t e m p e r a tu r e , R i s th e g a s law c o n s ta n t , and A i s t h e e n e rg y o f a c t i v a t i o n . I f t h e r e a c t i o n can be e f f e c t e d a t a s u f f i c i e n t l y h ig h t e m p e r a tu r e , a s a t i s f a c t o r y r a t e c a n be o b ta in e d i n th e a b sen ce o f any c a t a l y s t . A s u i t a b l e tem p e ra tu re may be o b ta in e d by c a r r y in g o u t t h e e s t e r i f i c a t i o n i n a r e c t i f i c a t i o n column o p e ra te d u n d e r s u f f i c i e n t p r e s s u r e t o g iv e t h e d e s i r e d b o i l i n g tem p e ra tu r e . I n o r d e r t o c a r r y o u t t h e r e a c t i o n c o n t in u o u s ly , th e e s t e r m ust be removed from th e r e a c t i o n m ix tu re i n th e fo rm o f a t e r n a r y c o n s ta n t b o i l i n g m ix tu r e . The t e r n a r y c o n s i s t s o f a l c o h o l , e s t e r and w a te r , and th e f e e d c h a rg e i s c a l c u l a t e d from th e c om p o s i t io n o f t h i s t e r n a r y . The f e e d c h a rg e m ust b e o f su ch a c om p o s i t io n t h a t no component w i l l b u i ld up a s e x c e s s in th e s t i l l p b t e B e fo re th e c o n tin u o u s e s t e r i f i c a t i o n i s c a r r i e d o u t , i t i s n e c e s s a r y t o d e te rm in e a tem p e ra tu re and p r e s s u r e a t w h ich th e e s t e r i f i c a t i o n r a t e i s s u f f i c i e n t l y h ig h , a s w e l l a s th e compo­ s i t i o n o f t h e lo w e s t b o i l i n g t e r n a r y a z e o t ro p e a t t h a t p r e s s u r e , • I t w as th e p u rp o se o f t h i s w ork t o d e te rm in e : (1 ) th e non-r’c a t a l y t i c e s t e r i f i c a t i o n r a t e (e x p re s s e d a s p e r c e n t . . c o n v e rs io n p e r h o u r ) a t th e b o i l i n g p o in t u n d e r a tm o sp h e r ic p r e s s u r e o f n - p r o p y l , n - b u t y l , i s o - b u t y l , n -am y l, and iso -am y l a lc o h o l w i th fo rm ic a c id , (2 ) th e n o n - e a t a l y t i e e s t e r i f i c a t i o n r a t e a t th e b o i l i n g tem p e ra tu re c o r r e s p o n d in g t o 60 p s i g p r e s s u r e o f e a c h o f th e a l c o h o l s named ab o v e , (3 ) t h e c om p o s i tio n o f th e t e r n a r y a z e o t ro p e form ed i n e a c h c a se a t th e tem p e ra tu re c o r r e s p o n d in g t o 60 p s ig p r e s s u r e , (4 ) th e p r o p e r c h a rg e f o r e a c h o f th e sy s tem s named ab o v e , c o r r e c t f o r 60 p s i g p r e s s u r e , and t o o p e r a te th e e s t e r i f i c a t i o n . p r o c e s s c o n t in u o u s ly a t t h i s 60 p s i g p r e s s u r e . “ 6 ~ Ho. PROCESSES A0 D e te rm in a t io n o f t h e e s t e r i f i c a t i o n r a t e a t a tm o sp h e r ic p ressu re® I 0 E qu ipm en t: The equ ipm en t c o n s i s t e d o f 250 m l. E r lenm ey e r f l a s k , a P y re z g l a s s L ie b ig c o n d e n se r , a 1 1 0 - v o l t , 500 W att h e a t e r c o n t r o l l e d by an a u t© tra n s fo rm e r , a n i c e b a th , and a 50 ml* buret® . 2o M a t e r i a l s ; The fo rm ic a c id u sed was 98^-100% p u r e , o b ta in e d from G en e ra l ■ ................. . C hem ica l ..D iv is io n ,.. A l l i e d ..C hem ica l.& .Dye C o rp o r a t io n , (The c a l c u l a t i o n i n t h i s . i n v e s t i g a t i o n . i s ..based on 99$.; p u re ) . The n - p r o p y l , n - b u t y l , n -am y l, i s o - b u t y l , and is o -am y l a lc o h o ls used , w ere -C„p, g r a d e , . o b ta in e d .f r o m S h a r p ie s , E im er and Aofend, ........................and E astm an Kodak Co* ........ So P ro c e d u r e : E q u a l m ol p o r t i o n s o f a lc o h o l and fo rm ic a c id w ere p la c e d in an E rle nm ey e r f l a s k and b o i l e d u n d e r a tm o sp h e r ic p r e s s u r e a t t o t a l ' ..re f l u x ..by u s in g a P y rex g l a s s - L i e b i g condenser® A f t e r one h o u r b o i l i n g , th e f l a s k was p la c e d i n a n i c e b a th and th e u n re a c te d a c id was t i t r a t e d w i th a s ta n d a r d s o lu t i o n o f sod ium h y d ro x id e u s in g p h e n o lp h th a le i n a s th e in d ic a to r® The p e r c e n t o f e s t e r i f i ­ c a t i o n c o u ld t h e n be c a lc u la te d® B® P r e p a r a t i o n o f 60 p s lg p r e s s u r e t e r n a r y and a n a ly s i s o f i t s composition® (a ) The 60 p s ig p r e s s u r e e s t e r i f i c a t i o n u n i t i s shown in Pig® 1® The u n i t c o n s is te d , o f a c o p p e r p r e c i s i o n column l | r in c h e s i n - d iam e te r by 52 in c h e s Io n g e The column was p acked w i th ^ in c h , g l a s s h e l i c e s . The s t i l l p o t w h ich was s i l v e r s o ld e r e d t o th e ■ co p p e r co lum n, was c o n s t r u c te d from a s t a i n l e s s s t e e l oxygen t a n k w i th a c a p a c i ty o f ab o u t 1800 m le The co p p e r column was j a c k e te d by 48 mm, g l a s s tu b in g in s i d e 64 mm, g l a s s t u b in g , w i th a h e a t in g c o i l s p i r a l i n g th e l e n g th o f th e i n s id e t u b e . Power was s u p p l ie d t o th e h e a t i n g e lem en t th ro u g h an a u to t r a n s f o rm e r . The co n d en se r s e c t i o n c o n s i s t e d o f a w a te r j a c k e t c o n s t r u c te d o f an I l= I n c h s e c t i o n o f tw o - in c h s ta n d a r d i r o n p ip e and a c o ld f i n g e r 12 in c h e s lo n g c o n s t r u c te d .o f ^ i n c h - co pp e r tu b in g ( I ) , The f low o f w a te r th ro u g h th e c o ld f i n g e r was c o n t r o l l e d by u s in g a l a b o r a to r y -b e l lo w s pump. The c o n d e n se r m o to r was s u p p l ie d from a c o n s ta n t h e a d .s o u r c e . The r e f l u x r a t i o o b ta in e d i n th e c o ld f i n g e r was e s t im a te d t o be i n t h e ra n g e o f 5 -1 t o 10=1, C onnec ted to t h e s t i l l p o t was a co p p e r f e e d t a n k w i th a- . c a p a c i ty o f a b o u t f i v e l i t e r s , and a r e c e i v e r c o n s t r u c te d o f l | - in c h s ta n d a rd i r o n p ip e . B o th t h e fe e d b a c k and r e c e i v e r were k e p t u n d e r th e same o p e r a t in g p r e s s u r e a s t h e co lum n. The d e s i r e d p r e s s u r e was o b ta in e d by means o f an a i r com p resso r a n d .a B eV ilb is s P r e s s u r e .R e g u la t o r , Two 1 1 0 -v o l t 550 w a t t h e a t e r s c o n t r o l l e d by a u to - t r a n s f o rm e r s s u p p l ie d th e h e a t t o ‘th e s t i l l p o t and th e co lum n , ' . - (b ) F o r . th e p u r p o s e . o f . a n a l y s i s : A g l a s s p r e c i s i o n co lum n, one in c h in d iam e te r , w i th a 3 6 - in c h s e c t i o n , p ack ed w i th ^ = in £ h g l a s s - h e l i c e s and e q u ip p ed w i th a Cqfad , tyfce c o n d e n s in g h ead was u sed t o make a tm o sp h e r ic s e p a r a t i o n s . S 0 P r o c e d u r e : «a0ca I t was f i r s t assum ed t h a t th e t e r n a r y a z e o tro p e c om p o s itio n u n d e r 60 p s i g p r e s s u r e w ould be th e same a s a t a tm o sp h e r ic p re s s u re * From th e a tm o sp h e r ic t e r n a r y c om p o s itio n d a t a , T ab le I , t h e p ro p o r ­ t i o n s o f a l c o h o l , a c id and w a te r ( i f n e c e s s a ry ) r e q u i r e d t o fo rm th e t e r n a r y a z e o t ro p e w e re . c a lc u la te d * F o r ex am p le : A tm osphe ric t e r n a r y o f i s o - b u t y l fo rm a te c o n s i s t s o f th e f o l lo w ­ in g : ■ I s o b u ty l , fo rm a te I s o b u ty l a lc o h o l .W ater Wto - GLASS ^ JACKETS 1/4' COPPER TUBING DRAI N F ig u re I S ch em a tic D iagram o f Equipm ent TABLE I - ATMOSPHERIC AZEOTROPE COMPOSITIONS ( 3 ) Ethyl Formate n-Propyl Formate Isopropyl Formate n-Butyl Formate Isobu ty l Formate n-Amyl Formate Isoamyl Formate E - A E Binary Binary E-W A-W B.P. B.P. B.P. w t. % B.P. ■wt. % °C 0C OC W OQ W 78.3 54.1 78.15 4 .4 79.2 81 71.6 2 .3 87.7 28.3 82.5 Tl No data 80 .4 12 .1 117.7 106.9 83 .8 15 92 .4 38 107.9 98.5 80 .4 7 .8 89 .9 33 137.8 132 91.6 23 .4 95.9 54 131.6 123.3 90 .2 21. 95 .2 49.6 Ester A - Alcohol Binary E-A B.P. w t. % B.P. wt.% wt. % w t. % OC A OC E A W No Azeo. No data 80.6 9 .8 70.8 82 5 13 No data No data 105 .8 23 .7 83.6 68 .7 10 „ 21.3 97.8 20.6 80 .2 76 6 .7 17.3 130.4 43 91 .4 41 .2 21 .2 37.6 123.6 26 89 .8 48 19.6 32 .4 W - Water tL Ul I -16' TABLE I I - ESTERIFICATION RATES E s t e r A tm osphe ric R a te Temp. °C R a te 60 p s ig R a te Temp. °C R a te n -P ro p y l Form ate 90 1 1 .0 134 2 6 .3 n -B u ty l Form ate 1 0 4 .5 2 8 .9 144 3 1 .6 I s o b u ty l Form ate 98 2 4 .6 138 5 1 .6 n-Amyl Form ate 108 1 3 .9 144 .5 1 8 .6 Iso am y l Form ate 106 2 1 .0 143 2 3 .3 (From l i t e r a t u r e th e e s t e r i f i c a t i o n r a t e a t 155°C . i s 61.69%) (2) o f I s o b u ty l Fo rm ate TABLE I I I - 60 PSIG TERNARY AZEOTROPES E s t e r B .P .°C w t . % A lco h o l w t. % E s t e r wt . % W ater n -P ro p y l Form ate 134 3 0 .7 3 2 .4 3 6 .9 n -B u ty l Form ate 144 2 7 .3 3 9 .0 33 .7 I s o b u ty l Form ate 138 1 8 .9 4 8 .1 33 .0 n-Amyl Form ate 1 44 .5 2 0 .2 24 .5 5 5 .3 Iso am y l Form ate 143 2 7 .6 1 8 .3 5 4 .1 ■17 TABLE IV . - FEED COMPOSITION FOR CONTINUOUS OPERATION E s t e r w t. % Acid n -P ro p y l Form ate 1 7 .0 n -B u ty l Form ate 1 7 .5 I s o b u ty l Form ate 2 1 .6 n-Amyl Form ate 9 .6 Iso am y l Form ate 7 .3 w t. % A lco h o l w t. % W ater 5 2 .9 3 0 .1 5 5 .7 2 6 .8 5 3 .9 2 4 .5 3 9 .5 5 0 .9 4 0 .7 5 2 .0 103009 10022724 6 «5*‘ 105009 author J-c : Ih-Cheo TITLE u 0 n ^ l i i U U U d 1 ) 0 !'}C 'T l ___e8torificatinn of I d a t e d u e ower om a BORROWER 'S NAME 103009