JPS58115021A - Preparation of aluminum chloride - Google Patents

Preparation of aluminum chloride

Info

Publication number
JPS58115021A
JPS58115021A JP56209171A JP20917181A JPS58115021A JP S58115021 A JPS58115021 A JP S58115021A JP 56209171 A JP56209171 A JP 56209171A JP 20917181 A JP20917181 A JP 20917181A JP S58115021 A JPS58115021 A JP S58115021A
Authority
JP
Japan
Prior art keywords
chloride
aluminum
chlorinated paraffin
aluminum chloride
reaction
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
Application number
JP56209171A
Other languages
Japanese (ja)
Other versions
JPS6354650B2 (en
Inventor
Kogaku Komamiya
駒宮 功額
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.)
ROUDOUSHIYOU SANGYO ANZEN KENKYUSHO
Original Assignee
ROUDOUSHIYOU SANGYO ANZEN KENKYUSHO
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 ROUDOUSHIYOU SANGYO ANZEN KENKYUSHO filed Critical ROUDOUSHIYOU SANGYO ANZEN KENKYUSHO
Priority to JP56209171A priority Critical patent/JPS58115021A/en
Publication of JPS58115021A publication Critical patent/JPS58115021A/en
Publication of JPS6354650B2 publication Critical patent/JPS6354650B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F7/00Compounds of aluminium
    • C01F7/48Halides, with or without other cations besides aluminium
    • C01F7/56Chlorides
    • C01F7/58Preparation of anhydrous aluminium chloride

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

PURPOSE:To prepare aluminum chloride safely at a low cost, by utilizing a waste material of vinyl chloride or chlorinated paraffin as a chlorine source in preparing the aluminum chloride. CONSTITUTION:A waste PVC or chlorinated paraffin disused in a factory and aluminum are charged into a reactor and heated in an atmosphere containing no oxygen. The polyvinyl chloride and chlorinated paraffin are thermally decomposed into hydrogen chloride and carbon, and the hydrogen chloride is reacted with the aluminum to form aluminum chloride. There is no fear of danger for the leakage of chlorine gas leakage since chlorine gas is not used, and the preparation cost is low due to the use of the waste materials, e.g. polyvinyl chloride, as the chlorine source. The carbon generated at the same time as a by-product is utilizable as a raw material for active carbon.

Description

【発明の詳細な説明】 併律の填(Vアル1ニウムの製法0.有毒な塩素カスを
用いるの・で安全性を欠き、従ってカスもね時に不安が
生ずる斡の欠点があるロ本発@セ以上の欠点の1去を計
ると共に、廃*mとしで回収されたり、工場で不用とな
った塩化ビニルを塩素の代甲とし、炭素状残漬の油中を
劃り、且つ生型コストの大幅IJt下けの可能性を高め
る艷のことを1的とする口 Illち本発明は無11事零囲気内で境fヒビニル又汀
壊隼化パラフィンtアル電と反応さぜることに#るつ 従来の塩゛化アルミエクムの製造方法け、空気の存在で
アル1=ウムを入れfC反応itカロ熱し次いで塩素を
吹込み生赦した塙fl′アルンニウムを加熱し、次いで
塩素を吹込み#!ltした増化アル1=ウムを1反応器
に接続しで設けた冷却器[1mさせで得るものであろう こわに対し本発明で汀、塩素の代りに屍衆さhた塩化ビ
ニルまた上地化パラフィンとアルミニウムとを反応器に
入れ、内Wく空気を音素などで#換し、無酸素琴゛囲気
としたのち加熱することにより塩化アルミニウムを冷却
l!に生成II!縮させ、るもので1反応式げ塩化ビニ
ルの場合は次の通りである。
[Detailed Description of the Invention] A method for manufacturing Al 1 (V) that lacks safety due to the use of toxic chlorine scum, and therefore has the disadvantage of causing anxiety when removing the scum. In addition to eliminating the above drawbacks, we used vinyl chloride, which was recovered as waste or was no longer used in factories, as a substitute for chlorine, and removed it from the carbonaceous residual oil. The present invention is aimed at increasing the possibility of significantly lowering the IJt cost, and the present invention does not involve reacting with the boundary f-binyl or sulfurized paraffin and alkaline metal in a zero atmosphere. According to the conventional method for producing aluminum chloride, aluminum is added in the presence of air, the fC reaction is heated, and then chlorine is blown into the aluminium, which is then heated. In contrast to the stiffness that would have been obtained by using a cooler connected to one reactor with enriched aluminum containing #!lt, the present invention uses chloride instead of sludge and chlorine. Put the vinyl or overlying paraffin and aluminum into a reactor, exchange the internal air with a phonogen, etc. to create an oxygen-free atmosphere, and then heat it to form aluminum chloride into a cooling liquid.II! In the case of vinyl chloride, the reaction formula is as follows.

5 C2HJCl + A  足 −÷ 、4文と、2
3イ ベこ t 安も)/シトO1lこれ1遮ず塩。化
ビニルが300°0付近の無除素酔気中で熱分解し、塩
化水素と#!、素を兎生成したのち、アル1=ウムと塩
化水素とが1反応するものであり2発熱反応であるei
たこの反応で化成する嶽素は活性縦の製造原料として利
用することができる。なお塩素化パラフィンの反応も塩
化ビニルと−1じであるため欽fjAは省略する口この
ように本反応を利用した塩化アルミニウムの製造法の%
ttハ反応器内を無酸素零I気とするもので・もしも空
気が存在すねば30 d’o付近で発生する塩化水素に
アルミニウムと反応せず、さらVrsoO°0以上に加
熱を紗けねば、生成した屍素がsod’o前後で晩火燃
焼する。したがって反応し内を窒素−で9気を置換しな
め限り、塩化アルミニウムを製造することはできないり
なお塩化水素の生成除料である塩化ビニルや塩素化パラ
フィンセ暁却杷理するような廃集物であつイも、塩化ア
ル(=ラムの生成に支障汀ない。
5 C2HJCl + A foot -÷, 4 sentences, 2
3 I Bekot Yasumo) / Shito O 1 l This 1 Salt without interruption. Vinyl chloride thermally decomposes in unextracted inebriated air at around 300°0, producing hydrogen chloride! , after the formation of an element, there is one reaction between Al 1=um and hydrogen chloride, which is an exothermic reaction.
The sulfur which is chemically formed in the octopus reaction can be used as a raw material for the production of active fibers. Note that the reaction of chlorinated paraffin is also -1 the same as that of vinyl chloride, so the term fjA is omitted.
The inside of the reactor is oxygen-free and has zero atmosphere. If air exists, the hydrogen chloride generated near 30 d'o will not react with aluminum, and it must be heated to over VrsoO°0. , the generated carbon combusts late around sod'o. Therefore, it is not possible to produce aluminum chloride unless the atmosphere is replaced with nitrogen during the reaction.In addition, hydrogen chloride is generated.Vinyl chloride and chlorinated paraffin, which are used as waste materials, are used for disposal. Even if it is hot, it will not interfere with the production of aluminum chloride (= rum).

次に本製造法の実施例を説明する口 貢施f11 :1) 適轟な大きさに′切断したI11板状のアル1=ウムと
、適轟な大きさに破砕された廃業塩化ビニルとを反応し
に入れ、内部空気を窒素で置換し7tのち加熱する。約
aoO°OK達すると塩化ビニルから発生した塩化水素
はアル々エウふと反応し、塩化アル1=ウム1生成する
口これを反応@に凝縮させる亀のである。反応は発熱反
応であるため、加熱セ約SOO“0を保持すればよ(、
また反応器底部に生成した嶽素状残渣は活性炭の原料と
しても賽施9n℃塾 適轟な大きさに切1した薄板状アルミニウムと廃桑*素
化パラフィンとを反応器に入#1.内部空気を窒素で蒙
模したのち加熱する・約300’OK達すると、塩素パ
ラフィンから発生した塩化水素セアルンニウふと反応し
、塩化アルζ;りムを生成する口こhを反応器に1#続
しfi&けた冷却トに導負凝縮寧せるものである。
Next, an example of this production method will be explained. was put into the reaction, the internal air was replaced with nitrogen, and the reactor was heated after 7 tons. When the temperature reaches about aoO°OK, the hydrogen chloride generated from vinyl chloride reacts with aluminum and condenses it into a reaction @, producing 1 = 1 aluminum chloride. Since the reaction is exothermic, the heating temperature should be kept at SOO "0" (,
In addition, the slag-like residue generated at the bottom of the reactor is used as a raw material for activated carbon.Thin plate aluminum cut into a size suitable for 9nC and waste mulberry *chlorinated paraffin are put into the reactor. The internal air is heated with nitrogen and then heated. When it reaches about 300°C, the hydrogen chloride generated from the chlorine paraffin reacts with the hydrogen chloride to form aluminum chloride. The negative condensation is applied to the cooling system.

反応は全熱反応であるため、加熱は約so、00cを保
持できる1皺で十分である・ 特許比−人  労働省童業安全研究所長手続補正書 昭和51生S月19日 製許庁長富  島田春樹 殿 JL@正をする者 偽代蓉人 All+正の対象 jllaltf)発明者の欄 (2F)明細書全文 ム神正の8客 目asa11六aJと訂正した補正−書を提出しました
口 (2)  明細書全文を次の通り訂正する、 添付書類
の目録 ill  fl正動書   正副 j1通(2)  住
民票        1通(s)  不在証明書   
  1通 (41II液証        1通 (6)  明細書(全文)   1通 明細書 発明の名称  塩化アルミニウムの製法特許−家の範、
8 窒素篠の無*tXS気円でアルミニウムと塩化ビニル又
σ塩素化パラフィンとを反応させることを特徴とする塩
化アル1=ウムの製法口発明の詳細な説明 従来の塩化アルミニウムの製法灯、有毒な塩素ガスを酬
いているので、ガスもれ時に不安が生ずる恐わがある。
Since the reaction is a total heat reaction, one wrinkle that can maintain approximately so, 00c is sufficient for heating.Patent Ratio - Person Ministry of Labor Child Work Safety Research Institute Director Procedural Amendment Letter 1978 Birth Sep 19 National License Agency Nagatomi Shimada Mr. Haruki JL @ Those who make corrections false substitutes All + correct objects jllaltf) Inventor's column (2F) I submitted an amendment that corrected the entire specification as the 8th item asa116aJ of the correction ( 2) Correct the entire statement as follows: List of attached documents ill fl Original copy J1 copy (2) Certificate of residence 1 copy (s) Certificate of absence
1 copy (41II liquid certificate 1 copy (6) Specification (full text) 1 copy Title of invention Process patent for aluminum chloride - family law,
8. Detailed description of the invention: Process for producing aluminum chloride, characterized by reacting aluminum with vinyl chloride or σ-chlorinated paraffin in a nitrogen-free *tXS atmosphere. Conventional process for producing aluminum chloride. Lamp, toxic. Since the gas is exchanging chlorine gas, there is a risk of anxiety in the event of a gas leak.

本発Wi4tff以上の欠点の除去を計ると共!IC1
廃棄物として回収されたり、工場で不用となった塩化ビ
ニル中塩素化パラフィンを塩素源として利用するととも
に、さらに反応時に発生する炭素状残の油中を計り、生
産コストの引下けf1的とする口 即ち本発明は無酸素 囲気内で塩化ビニル又は塩素化パ
ラフィンをアルミニウムと反応させることにある。
Along with eliminating the drawbacks of the original Wi4tff! IC1
In addition to using chlorinated paraffin in vinyl chloride, which is collected as waste or unused in factories, as a chlorine source, we also measure the carbonaceous residue generated during the reaction in oil, which reduces production costs. Thus, the present invention consists in reacting vinyl chloride or chlorinated paraffin with aluminum in an oxygen-free atmosphere.

従来の塩化アルミニウムの製造方法は、空気の存在下で
アルミニウムを入れた反応器管加熱し。
The traditional method for producing aluminum chloride involves heating a reactor tube containing aluminum in the presence of air.

次いで塩素を吹込み生成した塩化アルミニウムを重複反
応器I/r接枡しで設けた冷却器に畏縮させて得るもの
である口 これに対し本賢明では、塩素の代りVr廃棄された塩化
ビニルfたけ塩素化パラフィンとアルミニウムとを反応
器に入れ、内部空気を窒素などで置換し、無酸素f−気
としたのち加熱することKより塩化アルミニウムを冷却
器に生成疑iさせるもので1反応式は塩化ビニルの場合
は次の通りである。30zByOL+AL−+A LO
Li+60 +偽5Hiこ#1けまず塩化ビニルが3o
fa付近の無酸−囲気中で熱分解し、塩化水素と炭素を
生成する口この塩化水素はアルミニウムとただちに反応
して塩化アルミニウムを生成するものであり1発熱反応
である口重たこの反応で生成する炭素は活性炭の製造原
料としで利甲することができる。なお塩素化パラフィン
の反応も゛塩゛化ビニルと同じでめるためWiwAは省
略する。
Next, the aluminum chloride produced by blowing in chlorine is cooled in a cooler installed in a double reactor I/R tank. Bamboo chlorinated paraffin and aluminum are placed in a reactor, the internal air is replaced with nitrogen, etc. to make oxygen-free gas, and then heated.This is a reaction method that causes aluminum chloride to be produced in a cooler from K. is as follows in the case of vinyl chloride. 30zByOL+AL-+A LO
Li + 60 + False 5Hi #1 PVC is 3o
It thermally decomposes in an acid-free atmosphere near fa to produce hydrogen chloride and carbon. Hydrogen chloride immediately reacts with aluminum to produce aluminum chloride, which is an exothermic reaction. The carbon produced can be used as a raw material for producing activated carbon. Note that WiwA is omitted because the reaction of chlorinated paraffin is the same as that of vinyl chloride.

このように本反応を利甲した塩化アルミニウムの製造方
法の特徴は1反応器内を無酸素を囲気とするもので、も
しも空気が存在すわばsoo@o付近で発生する塩化水
素はアルミニウムと反応せ文さらに300’O*ilで
発火燃焼する。したがって反応器内を窒素岬で空気を置
換しない限り、塩化アルミニウムを製造することはでき
ない。なお塩化水素の生成原料である塩化ビニルや塩素
化パラフィンは焼却処−を必要とするような廃棄物であ
っても、塩化アルミニウムの生鵞成に支l11[けない
口重(本製造法の賽施例を説明する口 笑施fil  tl) 適当な大きさに切断した薄板状のアルミニウムと、適当
な大きさに破砕された廃棄塩化ビニルとを反応器に入れ
、内部空気を窒素で置換したのち加熱する・約300’
OK達すると塩化ビニルから発生した塩化水素はアルミ
ニウムと反応し、塩化アルミニウムを生成する・これを
反応器に畏縮させるものである。反応は発熱反応である
ため、加熱は約3OO°0を保持すればよく、tた反応
器底部に生成した炭素状残tJIkは活性炭の原料とし
ても利用できるものである。
The feature of the method for producing aluminum chloride that takes advantage of this reaction is that one reactor is surrounded by an oxygen-free atmosphere, and if air is present, the hydrogen chloride generated near soo@o will react with aluminum. It then ignites and burns at 300'O*il. Therefore, aluminum chloride cannot be produced unless the air in the reactor is replaced with nitrogen. Even if vinyl chloride and chlorinated paraffin, which are the raw materials for producing hydrogen chloride, are wastes that require incineration, they cannot be used in the raw production of aluminum chloride. A thin plate of aluminum cut to an appropriate size and waste vinyl chloride crushed to an appropriate size were placed in a reactor, and the internal air was replaced with nitrogen. Heat later for about 300'
When OK is reached, hydrogen chloride generated from vinyl chloride reacts with aluminum to produce aluminum chloride, which is sent to the reactor. Since the reaction is an exothermic reaction, the heating need only be maintained at about 300°0, and the carbonaceous residue tJIk produced at the bottom of the reactor can also be used as a raw material for activated carbon.

実施ipHj21 適当な大きさ°に切断した薄板状アルミニウムと廃棄塩
素化パラフィンとを反応器に入り、内部空気を窒素でf
俟したのち加熱する)約30DDK達すると、塩素化パ
ラフィンから発生した塩化水素灯アルミニウムと反応し
、塩化アルミニウムを生成する。、こ幻を反応器に接抄
しで設けた冷却器に導真畏縮させるものであろう 反応は発熱反応であるため、加熱セ約3009Cを保持
できる程1で十分である。
Implementation ipHj21 Thin plate aluminum cut to an appropriate size and waste chlorinated paraffin are placed in a reactor, and the internal air is flushed with nitrogen.
When the temperature reaches about 30 DDK, it reacts with the hydrogen chloride lamp aluminum generated from the chlorinated paraffin to produce aluminum chloride. Since the reaction that would cause the condenser to flow into the condenser attached to the reactor is an exothermic reaction, 1 is sufficient to maintain the heating temperature at about 3009C.

特許出願人  男番省産業安全研究所長手続補正書 昭和5yiif:s月22日 特許庁長音  島田春11# JLIIIi正をする看 偽代酵人 住所 東家都葛飾区細切雫下目SO番1o号:1)、昭
和8v61:!S″Axe日付提mのWAa書中t>特
許請求幹囲の― (Il、 ’11と同日付提出の補正寮中の発W14の
許細な説明の― :11.特許軸求の岬註  別紙V通り(21発明の詳
細な説明中li2頁枦2行中の「1−4反応b」を「反
応b」と訂正するうill  II3]thlI2行中
「アルきニラふと反応せず1」とする部分の末端のro
 JをQl」除し[アルミニウムと反応せず]と訂正す
るう 以1 特許請求の範囲 会素勢の無酸素雫囲気円でアルミニウムと塩化ビニル又
は塩素化パラフィンとを反応させることを特徴とする塩
化アルミニウムの製法・特許出−人  労働省を檗安全
研究所長用  口  邦  供
Patent Applicant: Procedural Amendment to the Director of the Industrial Safety Research Institute, Ministry of Industry, Government of Japan, 1937, 22nd, January 2009, Japan Patent Office, Nagaon, Haru Shimada, 11#, JLIIIi Corrected, Kansai Daikojin Address: SO number 1o, Hosogiri Shizukuge, Katsushika-ku, Higashiike-ku Issue: 1), Showa 8v61:! S″Axe date submitted in WAa > Patent claim outline - (Il, detailed explanation of issue W14 in the amendment filed on the same date as '11) -: 11. Notes on the patent claim As shown in Attachment V (21 Detailed Description of the Invention, page 2, line 2, "1-4 reaction b" should be corrected as "reaction b". ill II 3) thl I, line 2, "Alkiniba suddenly did not react 1." ro at the end of the part
Dividing "J" by "Ql" and correcting it as [does not react with aluminum]. 1. It is characterized by reacting aluminum with vinyl chloride or chlorinated paraffin in an oxygen-free drop surrounding circle as defined in the claims. Manufacture method and patent for aluminum chloride - Ministry of Labor appointed to Director of Boku Safety Research Institute Kuni Kuchi

Claims (1)

【特許請求の範囲】[Claims] 窺素郷の無酸−零囲気円でアルミニウムと塩化ビニル又
U**化パラフィンとを反ルさせることf特徴とする塩
化アルミニウムの製法@
A manufacturing method for aluminum chloride featuring the process of boiling aluminum and vinyl chloride or U** paraffin in an acid-free zero-air environment in Kisugo.
JP56209171A 1981-12-25 1981-12-25 Preparation of aluminum chloride Granted JPS58115021A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56209171A JPS58115021A (en) 1981-12-25 1981-12-25 Preparation of aluminum chloride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56209171A JPS58115021A (en) 1981-12-25 1981-12-25 Preparation of aluminum chloride

Publications (2)

Publication Number Publication Date
JPS58115021A true JPS58115021A (en) 1983-07-08
JPS6354650B2 JPS6354650B2 (en) 1988-10-28

Family

ID=16568502

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56209171A Granted JPS58115021A (en) 1981-12-25 1981-12-25 Preparation of aluminum chloride

Country Status (1)

Country Link
JP (1) JPS58115021A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53124197A (en) * 1977-03-23 1978-10-30 Aluminum Co Of America Process for producing aluminum chloride

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53124197A (en) * 1977-03-23 1978-10-30 Aluminum Co Of America Process for producing aluminum chloride

Also Published As

Publication number Publication date
JPS6354650B2 (en) 1988-10-28

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