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JPS6039045B2 - How to dry dichlorobutene - Google Patents

How to dry dichlorobutene

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Publication number
JPS6039045B2
JPS6039045B2 JP1063276A JP1063276A JPS6039045B2 JP S6039045 B2 JPS6039045 B2 JP S6039045B2 JP 1063276 A JP1063276 A JP 1063276A JP 1063276 A JP1063276 A JP 1063276A JP S6039045 B2 JPS6039045 B2 JP S6039045B2
Authority
JP
Japan
Prior art keywords
dichlorobutene
mixture
water
mordenite
test
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.)
Expired
Application number
JP1063276A
Other languages
Japanese (ja)
Other versions
JPS5293703A (en
Inventor
孝雄 岩崎
秀樹 松村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP1063276A priority Critical patent/JPS6039045B2/en
Publication of JPS5293703A publication Critical patent/JPS5293703A/en
Publication of JPS6039045B2 publication Critical patent/JPS6039045B2/en
Expired legal-status Critical Current

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

Description

【発明の詳細な説明】 本発明はジクロルブテンの乾燥法に関するものである。[Detailed description of the invention] The present invention relates to a method for drying dichlorobutene.

ジクロルブテンに水が合されるといろいろな支障を生ず
る。例えば、1,4−ジクロルブテン−2をクロロプレ
ンの原料である3,4−ジクロルブテン−1に異性化す
る場合、水が含有されていると異性化反応がいまろくす
すむと、反応速度が遅くなり、反応器内の混合物が固形
化する。又、水を含むジクロルブテンを蒸留すると、蒸
留塔及びコンデンサーを腐触せしめたりする。そして腐
触により生成する塩化鉄の如き化合物はジクロルブテン
の異性化を促進する良好な触媒であるため、折角製造さ
れたジクロルブテン製品に他の異性体が混入する原因に
なる。ジクロルブテンを含む混合物の乾燥方法として、
塩化カルシウムによる脱水がある。
When dichlorobutene is mixed with water, various problems occur. For example, when 1,4-dichlorobutene-2 is isomerized to 3,4-dichlorobutene-1, which is the raw material for chloroprene, if water is contained, the isomerization reaction proceeds slowly and the reaction rate becomes slow. The mixture in the reactor solidifies. Furthermore, when dichlorobutene containing water is distilled, the distillation column and condenser may be corroded. Compounds such as iron chloride produced by corrosion are good catalysts for promoting the isomerization of dichlorobutene, and therefore cause other isomers to be mixed into dichlorobutene products that have been painstakingly produced. As a method for drying a mixture containing dichlorobutene,
There is dehydration due to calcium chloride.

しかし乍ら、塩化カルシウムで脱水した場合、処理温度
にもよるが、200〜70倣pmの水が乾燥ジクロルフ
テンに残留する。200〜700ppmの水分を含むジ
クロルブテンは腐触性が強いため、例えばニッケルの含
有量が高く、モリブデンが添加されているような耐酸性
の高級材料を使用する必要がある。
However, when dehydrating with calcium chloride, 200 to 70 pm of water remains in the dried dichlorophthene, depending on the processing temperature. Since dichlorobutene containing 200 to 700 ppm of water is highly corrosive, it is necessary to use a high-quality acid-resistant material with a high content of nickel and added molybdenum, for example.

この耐酸性の高級材料としては、例えばSUS−316
やハステロィーC(商品名)などが使用される。本発明
の目的はジクロルブテンを含む混合物を残留水分が50
ppm以下まで脱水することが可能な脱水方式を提供す
ることにある。
Examples of this acid-resistant high-grade material include SUS-316
and Hastelloy C (product name) are used. The purpose of the present invention is to prepare a mixture containing dichlorobutene with a residual water content of 50%.
It is an object of the present invention to provide a dehydration method capable of dehydrating down to ppm or less.

本発明に於いては、ジクロルブテン又はジクロルブテン
を含む混合物の乾燥にモルデナィトを脱水剤として使用
する。
In the present invention, mordenite is used as a dehydrating agent for drying dichlorobutene or a mixture containing dichlorobutene.

本発明で使用されるモルデナィトは一対史示性式M20
:N203:XSi02:YH20(但し、Mはアルカ
リ金属、アルカリ士類金属、水素又はそれらの混合物で
あり、nはMの原子価であり、Xは約6〜約45の数で
あり、そしてYは約1沙〆下の数である。)を有する結
晶性のアルミノケィ酸塩である。それの代表的な組成は
Ma20:山203:10 Si02:YH20である
The mordenite used in the present invention has the historical formula M20
:N203:XSi02:YH20 (where M is an alkali metal, alkali metal, hydrogen, or a mixture thereof, n is the valence of M, X is a number from about 6 to about 45, and Y It is a crystalline aluminosilicate having a number of about 1. Its typical composition is Ma20:Ma203:10 Si02:YH20.

モルデナィトは天然にも産するが、合成することも可能
である。モルデナイトのSi02:AI203のモル比
はA型及び×型ゼオラィトが2〜3:1、Y型ゼオライ
トが3〜6:1であるのに対し約6〜45:1であり、
Si02の含有率が高い。モルデナィトの結晶構造は、
a=18.13A、b=20.49A、c=7.52A
の単位格子の大きさをもつ斜方晶系であり、その細孔は
酸素の4,5,6,8及び12員環よりなり、最大細孔
を構成する12員環の最大径は約7.0A、最小蓬は約
5.8Aの楕円である。そしてこれらの細孔が形成する
細孔路はC軸に平行であって、互いが独立したトンネル
構造をとり、こうした紬孔構造は、A型ゼオラィトやX
型及びY型のホージャサィトなどの三次元空洞と異なっ
ている。従ってモルデナィトの結晶構造はX線回析分析
により色別でき、その含有量が分析できる。乾燥を行な
う温度は100℃以下で行なうのが好ましい。1000
0以上の温度で行なうことも可能であるが、脱水剤単位
量当りの水分量が小さくなり、頻繁に再生しなければな
らなくなるので好ましくない。
Mordenite occurs naturally, but it can also be synthesized. The molar ratio of Si02:AI203 in mordenite is about 6 to 45:1, whereas it is 2 to 3:1 in A-type and ×-type zeolites and 3 to 6:1 in Y-type zeolite.
The content of Si02 is high. The crystal structure of mordenite is
a=18.13A, b=20.49A, c=7.52A
It is an orthorhombic system with a unit cell size of , and its pores are composed of 4-, 5-, 6-, 8-, and 12-membered rings of oxygen, and the maximum diameter of the 12-membered ring constituting the largest pore is approximately 7. .0A, the minimum length is an ellipse of about 5.8A. The pore paths formed by these pores are parallel to the C axis and have an independent tunnel structure.
It is different from three-dimensional cavities such as the type and Y-shaped faujasites. Therefore, the crystal structure of mordenite can be color-coded by X-ray diffraction analysis, and its content can be analyzed. The drying temperature is preferably 100°C or lower. 1000
Although it is possible to carry out the process at a temperature of 0 or more, it is not preferable because the amount of water per unit amount of dehydrating agent becomes small and frequent regeneration is required.

実施例 1 温度調節機を備えた電気炉中に挿入した内径25肋のS
US−304製の管を乾燥器として使用し、これにN亀
20・AI203・1庇j02・YH20の組成を有す
るモルデナィトを500cc充填した。
Example 1 S with an inner diameter of 25 ribs inserted into an electric furnace equipped with a temperature controller
A US-304 tube was used as a dryer, and 500 cc of mordenite having the composition of N Kame 20, AI 203, 1 Eiji 02, and YH 20 was filled into it.

水分の含有量を約1000ppmに調製したジクロルブ
テン混合物(3,4ージクロルブテン−1が約36重量
%、1,4−ジクロルブテン−2が約50重量%、低沸
点化合物が約1重量%及び高沸点化合物が約6重量%か
らなる)を7000で毎時1その割合で乾燥器に供給し
た。1報時間連続して供給後、ジクロルフテン混合物の
供給を中断して液を抜取り、窒素ガスで乾燥器内を置換
後毎時100その窒素ガスを供給しながら徐々に昇温し
て再生を行なった。
A dichlorobutene mixture prepared to have a water content of about 1000 ppm (about 36% by weight of 3,4-dichlorobutene-1, about 50% by weight of 1,4-dichlorobutene-2, about 1% by weight of low-boiling compounds, and about 1% by weight of high-boiling compounds) (consisting of approximately 6% by weight) was fed to the dryer at a rate of 7000 ml per hour. After continuously supplying the dichlorophthene mixture for one hour, the supply of the dichlorophthene mixture was interrupted, the liquid was drawn out, the interior of the dryer was replaced with nitrogen gas, and the temperature was gradually raised while supplying the nitrogen gas at a rate of 100% per hour for regeneration.

2時間を要して25000まで昇温し、更に2時間25
000の状態に維持した後約1時間で70o0まで降温
した。
It took 2 hours to raise the temperature to 25,000, and then another 2 hours to 25
After maintaining the temperature at 0.000, the temperature was lowered to 70.00 in about 1 hour.

次に窒素ガスの供給を停止して、再び上記と同じ組成の
ジクロルブテン混合物を7000で毎時1その割合で供
給した。以上のような操作を10回繰返して行ない、乾
燥器出口におけるジクロルブテン混合物中の水分は再生
のため原料の供給を停止する直前に液の一部を採取して
ガスクロマトグラフィ及びカールフィッシャー水分計を
用いて測定した。いずれの場合も出口液中の水分濃度は
5〜loppmの範囲にあった。一方、10回繰返し試
験後のモルデナィトを乾燥器から取り出し性能ならびに
構造をチェックした。その結果、水分吸着量は使用前と
ほとんど変らず、又X線分析による結晶構造も約90%
保持されていた。比較のために3A型ゼオラィトのモレ
キュラィト蛇及び4A型ゼオラィトのモレキュラィトぜ
(いずれも栗田工業株式会社登録商標)を脱水剤として
上記の試験を行なった。
Next, the supply of nitrogen gas was stopped, and a dichlorobutene mixture having the same composition as above was again supplied at a rate of 1/hour at 7000 ml. The above operation was repeated 10 times, and the moisture in the dichlorobutene mixture at the outlet of the dryer was measured using gas chromatography and a Karl Fischer moisture meter by collecting a portion of the liquid just before stopping the supply of raw materials for regeneration. It was measured using In both cases, the water concentration in the outlet liquid was in the range of 5 to loppm. On the other hand, after the test was repeated 10 times, the mordenite was taken out of the dryer and its performance and structure were checked. As a result, the amount of moisture adsorbed was almost the same as before use, and the crystal structure according to X-ray analysis was approximately 90%.
It was retained. For comparison, the above test was conducted using 3A-type zeolite Moleculite Snake and 4A-type zeolite Moleculiteze (both registered trademarks of Kurita Water Industries, Ltd.) as dehydrating agents.

両方共1報時間連続してジクロルプテン混合物を供給後
再生して性能及び構造をチェックした。その結果、水分
吸着量及びX線強度比とも使用前のものの夫々約30%
に低下しており、乾燥器出口液中の水分濃度は50蛇p
m以上であった。更に比較のために、脱水剤として活性
ァルミナを使用してモルデナイトと同じく10回線返し
試験を行なった。
Both were regenerated after feeding the dichloroptene mixture continuously for one hour to check performance and structure. As a result, both the amount of water adsorption and the X-ray intensity ratio were approximately 30% of those before use.
The moisture concentration in the dryer outlet liquid is 50 p
It was more than m. Furthermore, for comparison, a 10-circuit test was conducted using activated alumina as a dehydrating agent in the same manner as mordenite.

10回線返し後の水分吸着量は約50%、又X線強度比
も約50%夫々低下した。乾燥器出口液中の水分濃度は
繰返しとともに徐々に上昇し、10回目の試験では50
加pm以上になった。実施例 2実施例1の方法におい
て、ジクロルブテン混合物中の水分濃度及び再生サイク
ルを変えて長時間試験を実施した。
After 10 cycles, the amount of water adsorption decreased by about 50%, and the X-ray intensity ratio decreased by about 50%. The water concentration in the dryer outlet liquid gradually increases as the test is repeated, and in the 10th test it reaches 50%.
It has become more than pm. Example 2 A long-term test was carried out using the method of Example 1, varying the water concentration in the dichlorobutene mixture and the regeneration cycle.

すなわち、500℃のNa20・山203・1庇i02
・YH20に対して約500ppmの水分を含有してい
るジクロルフテン混合物(成分は実施例1と同じ)を毎
時1その割合で供給した。70℃で4加持間連続的に供
給後、実施例1に記載の方法と全く同じ方法で再生を行
ない、再び上言己組成のジクロルブテン混合物を供給し
た。
In other words, Na20 at 500℃, mountain 203, 1 eave i02
- A dichlorophthene mixture (components are the same as in Example 1) containing about 500 ppm water based on YH20 was fed at a rate of 1 hourly. After continuous feeding at 70° C. for 4 holding periods, regeneration was carried out in exactly the same manner as described in Example 1, and the dichlorobutene mixture having the above-mentioned self-composition was fed again.

このような操作を20回線返して行なった。乾燥後の水
分は毎回測定したが、全試験を通じて5〜30ppmの
範囲にあった。一方、20回繰返し試験後のモルデナィ
トのX線分析による結晶構造は約85%保持されていた
。実施例 3 ジクロルブテン中の水分が縞角虫に及ぼす影響について
試験した。
This operation was repeated 20 times. The moisture content after drying was measured each time and was in the range of 5-30 ppm throughout all tests. On the other hand, about 85% of the crystal structure of mordenite was maintained by X-ray analysis after the test was repeated 20 times. Example 3 The effect of water in dichlorobutene on striped hornworms was tested.

実施例1に用いたと同じ組成を有するジクロルプテン混
合物中の水分濃度を50ppm及び500ppmの2水
準に調製して、夫々の液を試験管に入れ、その中に金属
片を浸潰して密栓後90つCに温度制御されているオイ
ルバスに入れた。2ケ月後に各試験片を取り出し腐触度
を測定して第1表の結果を得た。
The water concentration in the dichloroptene mixture having the same composition as used in Example 1 was adjusted to two levels, 50 ppm and 500 ppm, and each solution was placed in a test tube, a metal piece was immersed in the test tube, and after the tube was sealed, the water concentration was 90 ppm. It was placed in an oil bath whose temperature was controlled at C. After two months, each test piece was taken out and the degree of corrosion was measured, and the results shown in Table 1 were obtained.

表一1Table 1

Claims (1)

【特許請求の範囲】 1 一般示性式M2/nO:Al_2O_3:XSiO
_2:YH_2O(但しMはアルカリ金属、アルカリ土
類金属、水素又はそれらの混合物であり、nはMの原子
価であり、Xは約6〜約45の数であり、そしてYは約
12以下の数である。 )で示されモルデナイトを脱水剤として用いることを特
徴とするジクロルブテンの乾燥方法。
[Claims] 1 General formula M2/nO:Al_2O_3:XSiO
_2: YH_2O (where M is an alkali metal, alkaline earth metal, hydrogen, or a mixture thereof, n is the valence of M, X is a number from about 6 to about 45, and Y is about 12 or less A method for drying dichlorobutene characterized by using mordenite as a dehydrating agent.
JP1063276A 1976-02-03 1976-02-03 How to dry dichlorobutene Expired JPS6039045B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1063276A JPS6039045B2 (en) 1976-02-03 1976-02-03 How to dry dichlorobutene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1063276A JPS6039045B2 (en) 1976-02-03 1976-02-03 How to dry dichlorobutene

Publications (2)

Publication Number Publication Date
JPS5293703A JPS5293703A (en) 1977-08-06
JPS6039045B2 true JPS6039045B2 (en) 1985-09-04

Family

ID=11755584

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1063276A Expired JPS6039045B2 (en) 1976-02-03 1976-02-03 How to dry dichlorobutene

Country Status (1)

Country Link
JP (1) JPS6039045B2 (en)

Also Published As

Publication number Publication date
JPS5293703A (en) 1977-08-06

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