JPS60222439A - Purification of crude acetic anhydride - Google Patents
Purification of crude acetic anhydrideInfo
- Publication number
- JPS60222439A JPS60222439A JP7963684A JP7963684A JPS60222439A JP S60222439 A JPS60222439 A JP S60222439A JP 7963684 A JP7963684 A JP 7963684A JP 7963684 A JP7963684 A JP 7963684A JP S60222439 A JPS60222439 A JP S60222439A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- acetic anhydride
- containing gas
- test
- acetic acid
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 title claims abstract description 117
- 238000000746 purification Methods 0.000 title description 5
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000000034 method Methods 0.000 claims description 21
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 abstract description 41
- CCGKOQOJPYTBIH-UHFFFAOYSA-N ethenone Chemical compound C=C=O CCGKOQOJPYTBIH-UHFFFAOYSA-N 0.000 abstract description 10
- 239000007789 gas Substances 0.000 abstract description 10
- 238000004821 distillation Methods 0.000 abstract description 6
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 150000001875 compounds Chemical class 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 abstract description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 2
- 239000012295 chemical reaction liquid Substances 0.000 abstract description 2
- 238000001816 cooling Methods 0.000 abstract description 2
- 229910052760 oxygen Inorganic materials 0.000 abstract description 2
- 239000001301 oxygen Substances 0.000 abstract description 2
- 239000012495 reaction gas Substances 0.000 abstract description 2
- 239000011347 resin Substances 0.000 abstract description 2
- 229920005989 resin Polymers 0.000 abstract description 2
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 230000015556 catabolic process Effects 0.000 abstract 1
- 238000006731 degradation reaction Methods 0.000 abstract 1
- 238000012360 testing method Methods 0.000 description 24
- 241000122205 Chamaeleonidae Species 0.000 description 11
- 239000012535 impurity Substances 0.000 description 7
- 241001550224 Apha Species 0.000 description 5
- 238000009835 boiling Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 230000014759 maintenance of location Effects 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- 229920002301 cellulose acetate Polymers 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- WASQWSOJHCZDFK-UHFFFAOYSA-N diketene Chemical compound C=C1CC(=O)O1 WASQWSOJHCZDFK-UHFFFAOYSA-N 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241001292396 Cirrhitidae Species 0.000 description 1
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229920004482 WACKER® Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 description 1
- KXKVLQRXCPHEJC-UHFFFAOYSA-N acetic acid trimethyl ester Natural products COC(C)=O KXKVLQRXCPHEJC-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000012264 purified product Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000005987 sulfurization reaction Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はケテン法によって得られた粗製無水酢酸の精製
法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for purifying crude acetic anhydride obtained by the ketene method.
無水酢酸の工業的な製造方法としては酢酸を熱分解して
ケテンを得、酢酸にそのケテンを吸収反応せしめて無水
酢酸を得る所請ワッヵー法(ケテン法)、酢酸メチルに
一酸化炭素を反応せしめて無水酢酸を得る、所謂ハルコ
ン法等が知られているが、酢酸の熱分解によるワラカー
法が一般的でおる。Industrial methods for producing acetic anhydride include the Wacker method (ketene method), in which acetic acid is thermally decomposed to obtain ketene, and the ketene is absorbed and reacted with acetic acid to obtain acetic anhydride, and methyl acetate is reacted with carbon monoxide. Although the so-called Halcon method and the like are known to obtain at least acetic anhydride, the Varaka method, which involves thermal decomposition of acetic acid, is more common.
酢酸を熱分解して得られたケテンを酢酸に吸収反応せし
めて得られる粗製無水酢酸中には多種多様な不純物が少
なからず混入しておシこれらの不純物は蒸留操作によっ
て分離されている。Crude acetic anhydride obtained by absorbing and reacting ketene obtained by thermally decomposing acetic acid with acetic acid contains a considerable number of various impurities, and these impurities are separated by distillation.
酢酸セルロース製造工程で使用される無水酢酸は、その
原料酢酸として酢酸セルロース製造工程から排出される
酢酸水溶液から濃縮回収された酢酸が使用される場合が
多く、この濃縮酢酸にはセルロース系から来る不純物が
完全に除去されずに含まれるため、製造された無水酢酸
もそれらの影響を受ける欠点を免れない。Acetic anhydride used in the cellulose acetate production process is often made from acetic acid that has been concentrated and recovered from the acetic acid aqueous solution discharged from the cellulose acetate production process, and this concentrated acetic acid contains impurities from the cellulose system. are contained without being completely removed, so the produced acetic anhydride is also subject to the disadvantages of these.
このようにして得られた粗製無水酢酸は酢酸の熱分解反
応及びケテンと酢酸の吸収反応時に生ずる種々の低沸点
及び高沸点化合物を含むため蒸留によって脱低沸及び脱
高沸を行なうが、無水酢酸は高温下に於て平衡的に酢酸
とケテンに分解し、更にケテンは相互に反応してジケテ
ン及びその高沸点化合物を形成していくため収率の低下
と同時に精製のための熱エネルギーの消費を大きくする
(このことは蒸貿鞘製した無色透明の無水酢酸が常圧で
加温する仁とによシ着色し経時的にその度合を増して行
くことから明らかである。)。Since the crude acetic anhydride thus obtained contains various low-boiling and high-boiling compounds generated during the thermal decomposition reaction of acetic acid and the absorption reaction of ketene and acetic acid, it is removed by distillation to remove low and high boiling points. Acetic acid decomposes into acetic acid and ketene in equilibrium at high temperatures, and ketene reacts with each other to form diketene and its high-boiling compounds, resulting in a decrease in yield and an increase in thermal energy used for purification. This increases consumption (this is clear from the fact that the colorless and transparent acetic anhydride made from the steamer becomes more colored when heated under normal pressure, and the degree of coloration increases over time).
又、このとき副生じた高沸点化合物は、更に樹脂状物炭
化物となシ、塔内、熱交換器等の器壁に付着し、稼動率
の低下と、トラブルの原因となっている。In addition, the high-boiling compounds produced by-product at this time are further converted into resin-like chars and adhere to the inside of the tower and the walls of heat exchangers, etc., resulting in a decrease in operating efficiency and troubles.
無水酢酸中に含まれる不純物の正体はまだ充分に解明さ
れていないが、普通、無水酢酸の品質を評価する実用的
尺度として過マンガン酸カリウム試験(以下、カメレオ
ン試験という)、硫酸着色試験(以下、破着試験という
)等が実施されている(カメレオン試験保持時間が長く
、破着試験の着色状態を表わすAPHA値が低いものが
品質の良い無水酢酸とされている)。Although the identity of the impurities contained in acetic anhydride has not yet been fully elucidated, the potassium permanganate test (hereinafter referred to as the Chameleon test) and the sulfuric acid coloring test (hereinafter referred to as the Chameleon test) are commonly used as practical measures to evaluate the quality of acetic anhydride. , and tear adhesion test) (chameleon test) Acetic anhydride with a long retention time and a low APHA value, which indicates the state of coloration in the tear adhesion test, is considered to be of good quality.
カメレオン試験はJ工S K−8886で実施され、硫
着試験社サンプル!+01に硫酸0.5−を加え25℃
で′5分間経過後その着色状態をAPHAで表現するこ
とで実施される0
無水酢酸中の不純物は蒸留のみでは容易に除去されない
ため品質向上対策として薬剤添加法などが採用されてい
る。しかしこれらの添加法ではその後処理(特に廃棄物
の公害問題)が面倒である。The Chameleon test was conducted with J-Ko S K-8886, and the Sulfur Test Company sample! Add 0.5- sulfuric acid to +01 and 25℃
After 5 minutes have elapsed, the colored state is expressed using APHA. Since impurities in acetic anhydride cannot be easily removed by distillation alone, chemical addition methods are used as a quality improvement measure. However, with these addition methods, post-processing (especially waste pollution problems) is troublesome.
本発明者らは、高品質の無水酢酸を得る方法を長期にわ
たシ検討を重ねた結果、従来法とは全く異なる方法でそ
れらの欠点を有しない精製方法、即ち粗製無水酢酸をオ
ゾン含有ガスで処理することによシ蒸留操作を行なわな
くても蒸留精製品と同等又はそれ以上の高品質(カメレ
オン試験:保持時間の長い、破着試験: APHAの淡
い)の無水酢酸を得る方法を見い出し本発明を完成した
。As a result of long-term research into a method for obtaining high-quality acetic anhydride, the inventors of the present invention have developed a purification method that is completely different from conventional methods and does not have these disadvantages. Discovered a method to obtain acetic anhydride of a high quality equivalent to or better than that of distilled purified products (chameleon test: long retention time, breakage test: pale APHA) without performing distillation operations. The invention has been completed.
本発明の精製方法は、蒸留製品よシも良好な破着試験を
必要とし、更に還元性物質を多量に含み二次的に着色度
が問題となるセルロース処理用として本無水酢酸が使用
される場合、特に価値がある。即ち、オゾン含有ガスと
の接触処理という単一の工11によυ1熱エネルギーを
必要とせず、高温にすることによって無水酢酸の歩留シ
を低下させることもなくカメレオン試験、破着試験の改
善された無水酢酸を得ることができる。The purification method of the present invention requires a good puncture test for distilled products, and the acetic anhydride is used for treating cellulose, which contains a large amount of reducing substances and has a secondary problem of coloration. Particularly valuable if. In other words, the single process 11 of contact treatment with ozone-containing gas does not require υ1 thermal energy, and the chameleon test and fracture test can be improved without reducing the yield of acetic anhydride by increasing the temperature. acetic anhydride can be obtained.
本発明に於て用いられる原料粗製無水酢酸はケテン法無
水酢酸製造工程中、どの濃度の粗製無水酢酸並びにカメ
レオン試験0分、硫着試験ムPHA 500以上のもの
に、も適用できる。しかし反応工程より得られる粗製無
水酢酸中の不純物が多くなる程オゾン含有ガスの吹入量
が多くなる。このため粗製無水酢酸中に含有されるジケ
テン等の二重結合成分量を少なくする反応条件を選び粗
製無水酢酸を製造するのが一層効果的である。The raw material crude acetic anhydride used in the present invention can be applied to any concentration of crude acetic anhydride during the ketene method acetic anhydride production process, as well as those with a chameleon test of 0 minutes and a sulfurization test of PHA 500 or higher. However, as the amount of impurities in the crude acetic anhydride obtained from the reaction process increases, the amount of ozone-containing gas injected increases. For this reason, it is more effective to produce crude acetic anhydride by selecting reaction conditions that reduce the amount of double bond components such as diketene contained in the crude acetic anhydride.
又、処理された無水酢酸中に適量のオゾンを残留させる
ことによシ、後工程で本無水酢酸を酢酸セルロース製造
工程で使用する場合、その酸化力を利用できる点に於て
も有利である。Furthermore, by leaving an appropriate amount of ozone in the treated acetic anhydride, it is advantageous in that its oxidizing power can be utilized when the acetic anhydride is used in the cellulose acetate production process in the subsequent process. .
本発明に於て用いるオゾン含有ガスは市販のオゾン発生
機を使用し、空気或いは酸素を供給することによシ、オ
ゾン化されたものでよく、通常、空気原料の場合オゾン
濃度は10〜20f/m5である。オゾン含有ガスの吹
込量は処理すべき無水酢酸中のカメレオン試験、破着試
験等に悪影響を及はすと考えられる不純物の含有量に見
合う量で充分であるが、実用的には気液の接触効率、精
製率等を考慮して実験によシ適宜決めることが必要であ
シ、通常オゾン消費量紘50θ〜1000 t−0,/
Tであり、好ましくは600〜600 t −0,/
Tで処理する。The ozone-containing gas used in the present invention may be ozonized by using a commercially available ozone generator and supplying air or oxygen. Usually, when air is used as a raw material, the ozone concentration is 10 to 20 f. /m5. The amount of ozone-containing gas injected is sufficient to match the content of impurities that are considered to have an adverse effect on the chameleon test, breakage test, etc. in the acetic anhydride to be treated, but in practical terms It is necessary to determine it appropriately by experiment, taking into account contact efficiency, purification rate, etc., and the ozone consumption is usually 50θ~1000 t-0,/
T, preferably 600 to 600 t −0,/
Process with T.
本発明の方法に於ける反応温度は多くの場合常温で充分
目的が達せられる。反応液と反応ガスとの接触は槽式、
略式等いずれの方式を用いてもよく、必要に応じて冷却
装置を設置してもよい。In most cases, the reaction temperature in the method of the present invention is room temperature, which is sufficient to achieve the purpose. Contact between reaction liquid and reaction gas is by tank type.
Any method such as an informal method may be used, and a cooling device may be installed as necessary.
本発明に於ける効果を挙げると次の通シである。 The effects of the present invention are as follows.
イ)常温、常圧下で実施され、蒸留等を伴わないため熱
エネルギーが節約できる。b) It is carried out at room temperature and pressure and does not involve distillation, so thermal energy can be saved.
ロ)高温下にさらさないため無水酢酸の分解を防止し歩
留υの向上と熱変化による樹脂化。b) Since it is not exposed to high temperatures, it prevents the decomposition of acetic anhydride, improves the yield υ, and converts it into a resin due to thermal changes.
炭化物のトラブルを防止できる。It can prevent troubles caused by carbide.
ハ)オゾン自身、残留物がないため、後処理が全く不要
である。従って薬、剤、酸化剤の添加がないため添加物
の後処理を必要とせず、又その際発生する公害等の問題
も全くない。c) Since ozone itself has no residue, no post-treatment is necessary. Therefore, since there is no addition of drugs, agents, or oxidizing agents, there is no need for post-treatment of additives, and there are no problems such as pollution caused at that time.
二)オゾン含有ガスは現業で直接製造され、直ちに使用
されるため、貯蔵を必要とせず、連続的で自動的管理が
容易である。2) Ozone-containing gas is directly produced on-site and used immediately, so it does not require storage and is easy to continuously and automatically manage.
このようにして、本発明によれば、粗製無水酢酸にオゾ
ン含有ガスを吹込むことによってイ)。Thus, according to the invention, b) by bubbling the crude acetic anhydride with an ozone-containing gas.
口)、ハ)及び二)の効果が発揮され、且つカメレオン
試験;保持時間の長い、破着試験; APHAの淡い高
品質の無水酢酸を得ることが出来る。The effects of (1), (3), and (2) are exhibited, and high-quality acetic anhydride with a chameleon test; a long retention time, and a tear test; and a pale color of APHA can be obtained.
以下、実施例により本発明を更に詳細に説明する。 Hereinafter, the present invention will be explained in more detail with reference to Examples.
実施例−1
内径651111.高さ180III+(内容量600
WLt1有効容量500d)のガラス製容器(洗気瓶)
K粗製無水酢酸!(カメレオン試艙;保持時間1分以下
、破着試験;ムPHA 500以上) 400 tを仕
込み常温、常圧下にてオゾン含有空気(オゾン濃度?
271r’t/ NJ )を50 Ml、/11で供給
して気液接触させた。30分間ワンパス通気後の無水酢
酸の品質を分析したところ、カメレオン試験;保持時間
100分、破着試験i APHA 25であった。Example-1 Inner diameter 651111. Height 180III+ (inner capacity 600
WLt1 effective capacity 500d) glass container (air washing bottle)
K crude acetic anhydride! (Chameleon test tank; holding time 1 minute or less; tearing test; mu PHA 500 or more) 400 tons of ozone-containing air (ozone concentration?
271r't/NJ) was supplied at 50 Ml/11 to bring about gas-liquid contact. The quality of acetic anhydride after one-pass aeration for 30 minutes was analyzed and found to be chameleon test; retention time 100 minutes; tear test i APHA 25.
実施例−2〜3、比較例−1
オゾン含有空気通気時間30分の代シに1種種通気時間
を変えて供給量を増減した以外は。Examples 2 and 3, Comparative Example 1 Except that the ozone-containing air ventilation time was changed to 30 minutes, and the supply amount was increased or decreased by changing the ventilation time for one type of ozone.
実施例−1と同様に処理した結果を表−1に示した。又
比較例−1としてオゾンを含有しない空気を使用した以
外は実施例−1と同様に処理した結果を表−1に示した
。処理粗製無水酢酸量は夫々400tである。Table 1 shows the results of the same treatment as in Example-1. Further, as Comparative Example-1, the same treatment as in Example-1 was performed except that air containing no ozone was used, and the results are shown in Table-1. The amount of treated crude acetic anhydride was 400 tons each.
実施例−4〜7
実施例1〜3で使用したガラス製容器(反応器)を3本
直列に連結し、夫々に粗製無水酢酸を40of仕込み、
オゾン含有空気の通気を実施例−1〜3のワンパス方式
から、排ガス利用の3連通気として処理した結果を表−
2に示した。Examples 4 to 7 Three glass containers (reactors) used in Examples 1 to 3 were connected in series, and each was charged with 40 of crude acetic anhydride.
The table below shows the results of ventilation of ozone-containing air from the one-pass method in Examples 1 to 3 to triple ventilation using exhaust gas.
Shown in 2.
Claims (1)
する粗製無水酢酸の精製法。A method for purifying crude acetic anhydride, characterized by treating crude acetic anhydride with an ozone-containing scalpel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7963684A JPS60222439A (en) | 1984-04-20 | 1984-04-20 | Purification of crude acetic anhydride |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7963684A JPS60222439A (en) | 1984-04-20 | 1984-04-20 | Purification of crude acetic anhydride |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60222439A true JPS60222439A (en) | 1985-11-07 |
JPH0434537B2 JPH0434537B2 (en) | 1992-06-08 |
Family
ID=13695574
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7963684A Granted JPS60222439A (en) | 1984-04-20 | 1984-04-20 | Purification of crude acetic anhydride |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60222439A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994008938A1 (en) * | 1992-10-13 | 1994-04-28 | Eastman Chemical Company | Method for refining acetic anhydride |
US5362365A (en) * | 1992-07-07 | 1994-11-08 | Daicel Chemical Industries, Ltd. | Purification of acetic anhydride or acetic anhydride and acetic acid using ozone |
JP2001226319A (en) * | 2000-02-17 | 2001-08-21 | Daicel Chem Ind Ltd | Method for purifying crude acetic anhydride and method of producing polyoxytetramethylene glycol by using acetic anhydride |
JP2002037756A (en) * | 2000-05-18 | 2002-02-06 | Daicel Chem Ind Ltd | Acetic anhydride |
US6987201B2 (en) | 2000-02-17 | 2006-01-17 | Daicel Chemical Industries, Ltd. | Acetic anhydride, method of purifying crude acetic anhydride, and method of producing polyoxytetramethylene glycol using acetic anhydride |
-
1984
- 1984-04-20 JP JP7963684A patent/JPS60222439A/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5362365A (en) * | 1992-07-07 | 1994-11-08 | Daicel Chemical Industries, Ltd. | Purification of acetic anhydride or acetic anhydride and acetic acid using ozone |
WO1994008938A1 (en) * | 1992-10-13 | 1994-04-28 | Eastman Chemical Company | Method for refining acetic anhydride |
JP2001226319A (en) * | 2000-02-17 | 2001-08-21 | Daicel Chem Ind Ltd | Method for purifying crude acetic anhydride and method of producing polyoxytetramethylene glycol by using acetic anhydride |
US6987201B2 (en) | 2000-02-17 | 2006-01-17 | Daicel Chemical Industries, Ltd. | Acetic anhydride, method of purifying crude acetic anhydride, and method of producing polyoxytetramethylene glycol using acetic anhydride |
DE10108811B4 (en) * | 2000-02-17 | 2017-11-23 | Daicel Chemical Industries, Ltd. | Purification process for crude acetic anhydride and preparation process for polyoxytetramethylene glycol using acetic anhydride |
JP2002037756A (en) * | 2000-05-18 | 2002-02-06 | Daicel Chem Ind Ltd | Acetic anhydride |
Also Published As
Publication number | Publication date |
---|---|
JPH0434537B2 (en) | 1992-06-08 |
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